IMPROVED YEAST FOR ETHANOL PRODUCTION

REFERENCE TO A SEQUENCE LISTING

This application contains a Sequence Listing in computer readable form, which is incorporated herein by reference.

REFERENCE TO A DEPOSIT OF BIOLOGICAL MATERIAL

This application contains a reference to a deposit of biological material, which is incorporated herein by reference.

FIELD

Described herein are processes, e.g., including a liquefaction step, for producing ethanol from starch-containing material using yeast for converting fermentable sugars into ethanol. Also described are Saccharomyces yeast strains having improved ability to ferment sugars to ethanol, methods for the production of Saccharomyces yeast strains having improved ability to ferment sugars to ethanol, and the use of Saccharomyces yeast strains having improved ability to ferment sugars to ethanol in the production of ethanol. Finally, also described are compositions comprising the Saccharomyces yeast strains and naturally occurring and/or non-naturally occurring components.

BACKGROUND

Production of ethanol from starch-containing material is well-known in the art. The production of ethanol as a bio-fuel has become a major industry, with in excess of 24 billion gallons of ethanol being produced worldwide in 2014.

The most commonly industrially used commercial process, often referred to as a “conventional process”, includes liquefying gelatinized starch at high temperature (about 85°C) using typically a bacterial alpha-amylase, followed by simultaneous saccharification and fermentation (SSF) carried out anaerobically in the presence of typically a glucoamylase and a Saccharomyces cerevisae yeast.

Yeasts which are used for production of ethanol for use as fuel, such as in the corn ethanol industry, require several characteristics to ensure cost effective production of the ethanol. These characteristics include ethanol tolerance, low by-product yield, rapid fermentation, and the ability to limit the amount of residual sugars remaining in the ferment. Such characteristics have a marked effect on the viability of the industrial process.

Yeast of the genus Saccharomyces exhibits many of the characteristics required for production of ethanol. In particular, strains of Saccharomyces cerevisiae are widely used for the production of ethanol in the fuel ethanol industry. Strains of Saccharomyces cerevisiae that are widely used in the fuel ethanol industry can produce high yields of ethanol under fermentation conditions found in, for example, the fermentation of corn mash. An example of such a strain is the yeast used in commercially available ethanol yeast product called ETHANOL RED®.

Strains of Saccharomyces cerevisiae are used in the fuel ethanol industry to ferment sugars such as glucose, fructose, sucrose and maltose to produce ethanol via the glycolytic pathway. These sugars are obtained from sources such as corn and other grains, sugar juice, molasses, grape juice, fruit juices, and starchy root vegetables and may include the breakdown of cellulosic material into glucose.

Although strains of Saccharomyces cerevisiae currently used in the fuel ethanol industry are well suited to ethanol production, there is an increasing need for improvements in the efficiency of ethanol production owing to the increased demand for ethanol as a fuel, and the increased availability of starch in new strains of corn.

There is therefore a need for new robust yeast strains of Saccharomyces capable of improving the efficiency of ethanol production in industrial scale fermentation.

Further, despite significant improvement of ethanol production processes over the past decade there is still a desire and need for providing processes of producing ethanol from starch-containing material and yeast that can be used in commercial scale ethanol processes.

SUMMARY

Described herein are, inter alia, processes for producing ethanol from starch- containing material and yeast suitable for use in such processes.

A first aspect relates to processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No.

NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces cerevisiae strain MBG5038 having defining characteristics of Saccharomyces cerevisiae strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces cerevisiae strain MBG5012 having defining characteristics of Saccharomyces cerevisiae strain MBG5012.

In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or Saccharomyces cerevisiae strain MBG5012 expresses a glucoamylase and/or an alpha- amylase.

As used herein, the terms“properties” and“defining characteristics” of Saccharomyces cerevisiae strain MBG5038 and/or Saccharomyces cerevisiae strain MBG5012 include at least increased ethanol boost (i.e. , ethanol yield) compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same conditions. Other“properties” and“defining characteristics” include, inter alia, reduced acetaldehyde production, increased temperature tolerance, and decreased glycerol production. A fermenting organism described herein, e.g., used in a process described herein may have one or more the above mentioned“properties” and“defining characteristics”.

The fermenting organism organism described herein, especially Saccharomyces cerevisiae yeast, having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a derivative of Saccharomyces cerevisiae strain MBG5038, or having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a derivative of Saccharomyces cerevisiae strain MBG5012, having one or more, such as all of the following properties and/or defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012;

increased ethanol boost (i.e., ethanol yield) compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions;

reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions; increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions;

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions.

A fermenting organism described herein may have one or more, such as all, of the above mentioned“properties” or“defining characteristics”.

According to the ethanol production process, liquefaction in step i) is carried out by subjecting starch-containing material at a temperature above the initial gelatinization temperature, typically between 80-90°C, using an alpha-amylase. The pH in liquefaction is preferably between 4.5 and 6.0, such as between 4.8 and 5.8. Examples of alpha-amylase can be found below in the “Alpha-Amylase Present and/or Added During Liquefaction”- section. In one embodiment, the alpha-amylase is a thermostable bacterial alpha-amylase. In one embodiment, the alpha-amylase is from the genus Bacillus, such as a strain of Bacillus stearothermophilus, in particular a variant of a Bacillus stearothermophilus alpha-amylase, such as the one shown in SEQ ID NO: 3 in WO 99/019467 or SEQ ID NO: 1 herein. Examples of suitable Bacillus stearothermophilus alpha-amylase variants can be found below in the “Thermostable Alpha-Amylase”-section and include one from the following group of Bacillus stearothermophilus alpha-amylase variants with the following mutations: I 181*+G182*, and optionally N193F, and further one of the following substitutions or combinations of substitutions

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+ Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+ E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 for numbering).

Examples of other suitable Bacillus stearothermophilus alpha-amylases having increased thermostability compared to a reference alpha-amylase ( Bacillus stearothermophilus alpha-amylase with the mutations I 181*+G182*, and optionally substitution N193F, truncated at the C-terminal to be 485-495 amino acids long, such as about 491 amino acids long) at pH 4.5 and 5.5, 0.12 mM CaC can be found in WO 201 1/082425 hereby incorporated by reference. (See also Example 1 below)

Liquefaction in step i) may be carried out using a combination of alpha-amylase and protease. The protease may be a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C. Examples of suitable proteases are described below in the section“Protease Present and/or Added During Liquefaction”.

The protease may be of fungal origin, such as of filamentous fungus origin. Specific examples of suitable fungal proteases are protease variants of metallo protease derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially the strain Thermoascus aurantiacus CGMCC No. 0670 disclosed as the mature part of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein with one of the following substitutions or combinations of substitutions:

D79L+S87P+A112P+D142L;

D79L+S87P+D142L; and

A27K+ D79L+ Y82F+S87G+D104P+A112P+A126V+D142L.

Examples of other suitable protease variants can be found in WO 2011/072191 hereby incorporated by reference (See also Example 2 below).

Suitable proteases also include bacterial proteases. A suitable bacterial protease may be derived from a strain of Pyrococcus, preferably a strain of Pyrococcus furiosus. In one embodiment, the protease is the one shown in SEQ ID NO: 1 in US 6,358,726 or SEQ ID NO: 13 herein.

In one embodiment, 0.5-50 micro gram Pyrococcus furiosus protease per gram DS, such as 1-5 micro gram Pyrococcus furiosus protease per gram DS, such as about 1.5 or 3 micro gram Pyrococcus furiosus protease per gram DS is present and/or added in liquefaction step i).

In one embodiment, the alpha-amylase and/or the protease added in the liquefaction step i) is further combined with a glucoamylase. Thus, a glucoamylase may also be present and/or added during liquefaction step i). The glucoamylase may be thermostable. That means that the glucoamylase has a heat stability at 85°C, pH 5.3, of at least 20%, such as at least 30%, preferably at least 35% determined as described in Example 4 (heat stability). In one embodiment, the glucoamylase present and/or added in liquefaction has a relative activity pH optimum at pH 5.0 of at least 90%, preferably at least 95%, preferably at least 97%. In one embodiment, the glucoamylase has a pH stability at pH 5.0 of at least at least 80%, at least 85%, at least 90% determined as described in Example 4 (pH optimum).

A suitable glucoamylase present and/or added in liquefaction step i) may be derived from a strain of the genus Penicillium, such as a strain of Penicillium oxalicum disclosed as SEQ ID NO: 2 in WO 2011/127802 or SEQ ID NOs: 9 or 14 herein. In one embodiment, the glucoamylase is a variant of the Penicillium oxalicum glucoamylase shown in SEQ ID NO: 2 in WO 201 1/127802 having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 for numbering), such as a variant disclosed in WO 2013/053801. In one embodiment, the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 for numbering) and further one of the following substitutions or combinations of substitutions:

P1 1 F + T65A + Q327F; and

P2N + P4S + P1 1 F + T65A + Q327F (using SEQ ID NO: 14 for numbering).

Examples of other suitable Penicillium oxalicum glucoamylase variants can be found in WO 2013/053801 incorporated by reference (See also Example 15 below).

In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant, used in liquefaction has a thermostability determined as DSC Td at pH 4.0 as described in Example 15 of at least 70°C, preferably at least 75°C, such as at least 80°C, such as at least 81°C, such as at least 82°C, such as at least 83°C, such as at least 84°C, such as at least 85°C, such as at least 86°C, such as at least 87%, such as at least 88°C, such as at least 89°C, such as at least 90°C. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as DSC Td at pH 4.0 as described in Example 15 in the range between 70°C and 95°C, such as between 80°C and 90°C.

In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant, used in liquefaction has a thermostability determined as DSC Td at pH 4.8 as described in Example 15 of at least 70°C, e.g., at least 75°C, at least 80°C, at least 81 °C, at least 82°C, at least 83°C, at least 84°C, at least 85°C, at least 86°C, at least 87%, at least 88°C, at least 89°C, at least 90°C, or at least 91°C. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as DSC Td at pH 4.8 as described in Example 15 in the range between 70°C and 95°C, such as between 80°C and 90°C.

In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant, used in liquefaction has a residual activity determined as described in Example 16 of at least 100%, such as at least 105%, at least 110%, at least 115%, at least 120%, or at least 125%. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as residual activity as described in Example 16 in the range between 100% and 130%.

Further, in one embodiment, a pullulanase may be present during liquefaction in combination with an alpha-amylase, a protease and/or a glucoamylase.

In one embodiment, a glucoamylase may be present and/or added in saccharification and/or fermentation or simultaneous saccharification and fermentation. The glucoamylase may not be the same as the thermostable glucoamylase used in liquefaction.

In one embodiment, the glucoamylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added in saccharification and/or fermentation is of fungal origin, such as of filamentous fungus origin. In one embodiment, the glucoamylase is derived from a strain of Aspergillus, e.g., A. niger, A. awamori, or A. oryzae\ or a strain of Trichoderma, e.g., T. reesei ; or a strain of Talaromyces, e.g., T. emersonii, or a strain of Pycnoporus, or a strain of Gloeophyllum, such as G. serpiarium or G. trabeum, or a strain of Nigrofomes.

In one embodiment, the glucoamylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added in saccharification and/or fermentation is derived from Talaromyces emersonii, such as the one shown in SEQ ID NO: 19 herein. In another embodiment, the glucoamylase is derived from Gloeophyllum serpiarium, such as the one shown in SEQ ID NO: 15 herein. In another embodiment the glucoamylase is derived from Gloeophyllum trabeum such as the one shown in SEQ ID NO: 17 herein.

In one embodiment, the glucoamylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added in saccharification and/or fermentation is a variant of the Gloeophyllum trabeum glucoamylase disclosed in WO 2014/177546 (hereby incorporated by reference), especially a variant having one of the following substitutions or combinations of substitutions: V59A; S95P; A121 P; T119W; S95P+A121 P; V59A+S95P; S95P+T119W; V59A+S95P+A121 P; and S95P+T119W+A121 P, especially S95P+A121 P (using SEQ ID NO: 17 herein for numbering).

In one embodiment, the glucoamylase is in combination with an alpha-amylase and optionally a protease. The alpha-amylase may be of fungal or bacterial origin.

The alpha-amylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added in combination with a glucoamylase may be derived from a strain of the genus Rhizomucor, preferably a strain the Rhizomucor pusillus, such as the one shown in SEQ ID NO: 3 in WO 2013/006756, such as a Rhizomucor pusillus alpha-amylase hybrid having an Aspergillus niger linker and starch-bonding domain, such as the one shown in SEQ ID NO: 16 herein.

In one embodiment, the alpha-amylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added is derived from a strain of Rhizomucor pusillus, e.g., with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), such as the one disclosed as SEQ ID NO: 16 herein, and may have one or more of the following substitutions: G128D, D143N, such as G128D+D143N (using SEQ ID NO: 16 for numering).

In one embodiment, a protease is present and/or added in saccharification and/or fermentation, or SSF, which may result in increased ethanol yield. As described, e.g., in US patent No. 5,231 ,017 (hereby incorporated by reference) the protease may, e.g., be an acid fungal protease. A protease may also be present and/or added in saccharification and/or fermentation or SSF to improve the oil yield.

In one embodiment, a cellulolytic enzyme composition is present and/or added in saccharification, fermentation or simultaneous saccharification and fermentation (SSF). Examples of such compositions can be found in the“Cellulolytic Enzyme Composition present and/or added during Saccharification and/or Fermentation”-section below. In one embodiment, the cellulolytic enzyme composition is present and/or added together with a glucoamylase, such as one disclosed in the “Glucoamylase Present And/Or Added in Saccharification and/or Fermentation”-section below.

A second aspect relates to processes of producing ethanol from starch-containing material, such as granular starch, comprising:

(i) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL

Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of

Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces cerevisiae strain MBG5038 having defining characteristics of Saccharomyces cerevisiae strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL

Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of

Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces cerevisiae strain MBG5012 having defining characteristics of Saccharomyces cerevisiae strain MBG5012.

In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or Saccharomyces cerevisiae strain MBG5012 expresses a glucoamylase and/or an alpha- amylase.

In one embodiment, is a process of producing ethanol from starch-containing material, such as granular starch, comprising:

(i) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism; wherein saccharification and/or fermentation is done in the presence of the following enzymes: glucoamylase and alpha-amylase, and optionally protease; and

wherein the fermenting organism is a Saccharomyces yeast strain providing:

an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions;

reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions;

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions; and/or

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions.

In one embodiment, the fermenting organism is a derivative of Saccharomyces cerevisiae strain MBG5038 having the defining characteristics (e.g., high ethanol yield boost and/or decreased glycerol production of Saccharomyces cerevisiae strain MBG5038). In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, the fermenting organism is a derivative of Saccharomyces cerevisiae strain MBG5012 having the defining characteristics (e.g., high ethanol yield boost and/or decreased glycerol production of Saccharomyces cerevisiae strain MBG5012). In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5012 expresses a glucoamylase and/or an alpha-amylase.

Examples of suitable enzymes used, especially glucoamylases, alpha-amylases, proteases, cellulolytic enzyme compositions etc are described in the“Enzymes And Enzyme Blends Used In A Raw Starch Hydrolysis Process” section below.

A third aspect provides (1) a Saccharomyces cerevisiae yeast strain deposited under the Budapest Treaty and having NRRL accession no. NRRL Y67549, or a derivative of Saccharomyces cerevisiae strain NRRL Y67549. In some embodiments, the derivative of Saccharomyces cerevisiae strain NRRL Y67549 expresses a glucoamylase and/or an alpha- amylase; or (2) a Saccharomyces cerevisiae yeast strain deposited under the Budapest T reaty and having NRRL accession no. NRRL Y67700, or a derivative of Saccharomyces cerevisiae strain NRRL Y67700. In some embodiments, the derivative of Saccharomyces cerevisiae strain NRRL Y67700 expresses a glucoamylase and/or an alpha-amylase. A fourth aspect provides a method of producing a derivative of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) comprising:

(a) culturing a first yeast strain with a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012), under conditions which permit combining of DNA between the first yeast strain and the second yeast strain; and

(b) isolating hybrid strains; and

(c) optionally repeating steps (a) and (b) using a hybrid strain isolated in step (b) as the first yeast strain and/or the second yeast strain. In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

A fifth aspect provides a method of producing a Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA), or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) comprising:

(a) providing: (i) a first yeast strain; and (ii) a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012);

(b) culturing the first yeast strain and the second yeast strain under conditions which permit combining of DNA between the first yeast strain and the second yeast strain;

(c) screening or selecting for a derivative of Saccharomyces cerevisiae strain MBG5038;

(d) optionally repeating steps (b) and (c) with the screened or selected strain from step (c) as the first and/or second strain, until a derivative is obtained which exhibits the defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012. In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase. A sixth aspect provides a method of producing a recombinant derivative of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) comprising:

(a) transforming Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012) with one or more expression vectors encoding a glucoamylase and/or an alpha-amylase; and

(b) isolating the transformed strain.

A seventh aspect provides a Saccharomyces strain produced by the method of the fourth, fifth, or sixth aspect.

An eigth aspect provides a Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or the defining characteristics of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

A nineth aspect provides a method of producing ethanol, comprising incubating a strain of the first, fourth or fifth aspect with a substrate comprising a fermentable sugar under conditions which promote fermentation of the fermentable sugar to produce ethanol.

A tenth aspect provides use of a strain of the third, sixth or seventh aspect in the production of ethanol.

An eleventh aspect provides a method of producing distiller’s grain, comprising:

(a) incubating a Saccharomyces strain of the third, seventh or eigth aspect with a substrate comprising fermentable sugar under conditions which allow fermentation of the fermentable sugar to produce ethanol and distiller’s grains;

(b) isolating the distiller’s grains.

A twelfth aspect provides distiller’s grain produced by the method of the tenth aspect.

A thirteenth aspect provides use of a strain of the third, seventh or eigth aspect in the production of distiller’s grains.

A fourteenth aspect provides use of a strain of the third, seventh or eigth aspect in the production of a Saccharomyces strain which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

A fifteenth aspect provides a composition comprising a Saccharomyces strain of the third, seventh or eigth aspect.

Also described are compositions comprising a Saccharomyces yeast strain described herein, e.g., Saccharomyces cerevisiae strain MBG5038 or MBG5012, or a derivative thereof, and naturally occurring and/or non-naturally occurring components.

BRIEF DESCRIPTION OF THE DRAWINGS

Fig. 1 shows improved ethanol yield from fermentation of Saccharomyces cerevisiae strain MBG5038 under non-stress conditions at varying mash solids (%).

Fig. 2 shows lowered glycerol production from fermentation of Saccharomyces cerevisiae strain MBG5038 under non-stress conditions varying mash solids (%).

Fig. 3 shows improved ethanol yield from fermentation of Saccharomyces cerevisiae strain MBG5038 in the prescence of elevated levels of organic acid.

Fig. 4 shows decreased residual glucose from fermentation of Saccharomyces cerevisiae strain MBG5038 in the prescence of elevated levels of organic acid.

Fig. 5 shows improved ethanol yield from fermentation of Saccharomyces cerevisiae strain MBG5012 under non-stress conditions at high mash solids (%).

Fig. 6 shows decreased residual glucose from fermentation of Saccharomyces cerevisiae strain MBG5012 under non-stress conditions high mash solids (%).

Fig. 7 shows improved ethanol yield from fermentation of Saccharomyces cerevisiae strain MBG5012 in the prescence of elevated levels of organic acid.

Fig. 8 shows decreased residual glucose from fermentation of Saccharomyces cerevisiae strain MBG5012 in the prescence of elevated levels of organic acid.

Definitions

Allelic variant: The term“allelic variant” means any of two or more alternative forms of a gene occupying the same chromosomal locus. Allelic variation arises naturally through mutation, and may result in polymorphism within populations. Gene mutations can be silent (no change in the encoded polypeptide) or may encode polypeptides having altered amino acid sequences. An allelic variant of a polypeptide is a polypeptide encoded by an allelic variant of a gene.

Catalytic domain: The term “catalytic domain” means the region of an enzyme containing the catalytic machinery of the enzyme.

cDNA: The term "cDNA" means a DNA molecule that can be prepared by reverse transcription from a mature, spliced, mRNA molecule obtained from a eukaryotic or prokaryotic cell. cDNA lacks intron sequences that may be present in the corresponding genomic DNA. The initial, primary RNA transcript is a precursor to mRNA that is processed through a series of steps, including splicing, before appearing as mature spliced mRNA.

Coding sequence: The term “coding sequence” means a polynucleotide, which directly specifies the amino acid sequence of a polypeptide. The boundaries of the coding sequence are generally determined by an open reading frame, which begins with a start codon such as ATG, GTG, or TTG and ends with a stop codon such as TAA, TAG, or TGA. The coding sequence may be a genomic DNA, cDNA, synthetic DNA, or a combination thereof.

Control sequences: The term“control sequences” means nucleic acid sequences necessary for expression of a polynucleotide encoding a mature polypeptide of the present invention. Each control sequence may be native (/.e., from the same gene) or foreign (/.e., from a different gene) to the polynucleotide encoding the polypeptide or native or foreign to each other. Such control sequences include, but are not limited to, a leader, polyadenylation sequence, propeptide sequence, promoter, signal peptide sequence, and transcription terminator. At a minimum, the control sequences include a promoter, and transcriptional and translational stop signals. The control sequences may be provided with linkers for the purpose of introducing specific restriction sites facilitating ligation of the control sequences with the coding region of the polynucleotide encoding a polypeptide.

Expression: The term“expression” includes any step involved in the production of a polypeptide including, but not limited to, transcription, post-transcriptional modification, translation, post-translational modification, and secretion.

Expression vector: The term “expression vector” means a linear or circular DNA molecule that comprises a polynucleotide encoding a polypeptide and is operably linked to control sequences that provide for its expression.

Fragment: The term “fragment” means a polypeptide having one or more (e.g., several) amino acids absent from the amino and/or carboxyl terminus of a mature polypeptide or domain; wherein the fragment has pullulanas activity.

Host cell: The term "host cell" means any cell type that is susceptible to transformation, transfection, transduction, or the like with a nucleic acid construct or expression vector comprising a polynucleotide of the present invention. The term“host cell” encompasses any progeny of a parent cell that is not identical to the parent cell due to mutations that occur during replication.

Isolated: The term“isolated” means a substance in a form or environment that does not occur in nature. Non-limiting examples of isolated substances include (1) any non-naturally occurring substance, (2) any substance including, but not limited to, any enzyme, variant, nucleic acid, protein, peptide or cofactor, that is at least partially removed from one or more or all of the naturally occurring constituents with which it is associated in nature; (3) any substance modified by the hand of man relative to that substance found in nature; or (4) any substance modified by increasing the amount of the substance relative to other components with which it is naturally associated (e.g., recombinant production in a host cell; multiple copies of a gene encoding the substance; and use of a stronger promoter than the promoter naturally associated with the gene encoding the substance). An isolated substance may be present in a fermentation broth sample; e.g. a host cell may be genetically modified to express the polypeptide of the invention. The fermentation broth from that host cell will comprise the isolated polypeptide.

Mature polypeptide: The term“mature polypeptide” means a polypeptide in its final form following translation and any post-translational modifications, such as N-terminal processing, C-terminal truncation, glycosylation, phosphorylation, etc. It is known in the art that a host cell may produce a mixture of two of more different mature polypeptides (i.e., with a different C-terminal and/or N-terminal amino acid) expressed by the same polynucleotide. It is also known in the art that different host cells process polypeptides differently, and thus, one host cell expressing a polynucleotide may produce a different mature polypeptide (e.g., having a different C-terminal and/or N-terminal amino acid) as compared to another host cell expressing the same polynucleotide.

Mature polypeptide coding sequence: The term “mature polypeptide coding sequence” means a polynucleotide that encodes a mature polypeptide having protease activity.

Nucleic acid construct: The term "nucleic acid construct" means a nucleic acid molecule, either single- or double-stranded, which is isolated from a naturally occurring gene or is modified to contain segments of nucleic acids in a manner that would not otherwise exist in nature or which is synthetic, which comprises one or more control sequences.

Operably linked: The term“operably linked” means a configuration in which a control sequence is placed at an appropriate position relative to the coding sequence of a polynucleotide such that the control sequence directs expression of the coding sequence.

As used herein, the singular forms“a”,“an” and“the” include plural reference unless the context clearly indicates otherwise. Thus, for example, a reference to“a cell” includes a plurality of such cells. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art. Reference to“about” a value or parameter herein includes aspects that are directed to that value or parameter per se. For example, description referring to“about X” includes the aspect“X”.

As used herein, except where the context requires otherwise due to express language or necessary implication, the word “comprise” or variations such as “comprises” or “comprising” is used in an inclusive sense, i.e. to specify the presence of the stated features but not to preclude the presence or addition of further features in various embodiments.

DETAILED DESCRIPTION

Processes

Described herein are processes for producing ethanol from starch-containing material in a process including liquefaction, saccharification and fermentation. Fermentable sugars generated during saccharification are converted to ethanol during fermentation by yeast. In a first aspect is a process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces cerevisiae strain MBG5038 having defining characteristics of Saccharomyces cerevisiae strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces cerevisiae strain MBG5012 having defining characteristics of Saccharomyces cerevisiae strain MBG5012.

In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase. Steps ii) and iii) are carried out either sequentially or simultaneously (SSF). In one embodiment, steps ii) and iii) are carried out simultaneously (SSF).

Nitroqens-Source added During Fermentation

Generally, fermenting organisms such as yeast, including Saccharomyces cerevisiae yeast, require an adequate source of nitrogen for propagation and fermentation. Many sources of nitrogen can be used and such sources of nitrogen are well known in the art. The nitrogen source may be organic, such as urea, DDGs, wet cake or corn mash, or inorganic, such as ammonia or ammonium hydroxide. In one embodiment, the nitrogen source is urea.

Liquefaction step i)

According to processes described herein, liquefaction in step i) may be carried out by subjecting starch-containing material at a temperature above the initial gelatinization temperature to an alpha-amylase and optionally a protease, and/or a glucoamylase. Other enzymes such as a pullulanase and phytase may also be present and/or added in liquefaction.

Liquefaction step i) may be carried out for 0.5-5 hours, such as 1-3 hours, such as typically about 2 hours.

The term“initial gelatinization temperature” means the lowest temperature at which gelatinization of the starch-containing material commences. In general, starch heated in water begins to gelatinize between about 50°C and 75°C; the exact temperature of gelatinization depends on the specific starch and can readily be determined by the skilled artisan. Thus, the initial gelatinization temperature may vary according to the plant species, to the particular variety of the plant species as well as with the growth conditions. The initial gelatinization temperature of a given starch-containing material may be determined as the temperature at which birefringence is lost in 5% of the starch granules using the method described by Gorinstein and Lii, 1992, Starch/Starke 44(12): 461-466.

Liquefaction is typically carried out at a temperature in the range from 70-100°C. In one embodiment, the temperature in liquefaction is between 75-95°C, such as between 75- 90°C, between 80-90°C, or between 82-88°C, such as about 85°C.

A jet-cooking step may be carried out prior to liquefaction in step i). The jet-cooking may be carried out at a temperature between 110-145°C, 120-140°C, 125-135°C, or about 130°C for about 1-15 minutes, for about 3-10 minutes, or about 5 minutes.

The pH during liquefaction may be between 4 and 7, such as pH 4.5-6.5, pH 5.0-6.5, pH 5.0-6.0, pH 5.2-6.2, or about 5.2, about 5.4, about 5.6, or about 5.8.

In one embodiment, the process further comprises, prior to the step i), the steps of: a) reducing the particle size of the starch-containing material, preferably by dry milling; b) forming a slurry comprising the starch-containing material and water. The starch-containing starting material, such as whole grains, may be reduced in particle size, e.g., by milling, in order to open up the structure, to increase surface area, and allowing for further processing. Generally, there are two types of processes: wet and dry milling. In dry milling whole kernels are milled and used. Wet milling gives a good separation of germ and meal (starch granules and protein). Wet milling is often applied at locations where the starch hydrolysate is used in production of, e.g., syrups. Both dry milling and wet milling are well known in the art of starch processing. In one embodiment the starch-containing material is subjected to dry milling. In one embodiment, the particle size is reduced to between 0.05 to 3.0 mm, e.g., 0.1 -0.5 mm, or so that at least 30%, at least 50%, at least 70%, or at least 90% of the starch-containing material fit through a sieve with a 0.05 to 3.0 mm screen, e.g., 0.1-0.5 mm screen. In another embodiment, at least 50%, e.g., at least 70%, at least 80%, or at least 90% of the starch-containing material fit through a sieve with # 6 screen.

The aqueous slurry may contain from 10-55 w/w-% dry solids (DS), e.g., 25-45 w/w-% dry solids (DS), or 30-40 w/w-% dry solids (DS) of starch-containing material.

The alpha-amylase, optionally a protease, optionally a glucoamylase may initially be added to the aqueous slurry to initiate liquefaction (thinning). In one embodiment, only a portion of the enzymes (e.g., about 1/3) is added to the aqueous slurry, while the rest of the enzymes (e.g., about 2/3) are added during liquefaction step i).

A non-exhaustive list of examples of alpha-amylases can be found below in the“Alpha- Amylase Present and/or Added During Liquefaction”-section. In one embodiment, the alpha- amylase is a bacterial alpha-amylase. Bacterial alpha-amylases are typically thermostable. In one embodiment, the alpha-amylase is from the genus Bacillus, such as a strain of Bacillus stearothermophilus, in particular a variant of a Bacillus stearothermophilus alpha-amylase, such as the one shown in SEQ ID NO: 3 in WO 99/019467 or SEQ ID NO: 1 herein.

In one embodiment, the alpha-amylase has an improved stability compared to a reference alpha-amylase ( Bacillus stearothermophilus alpha-amylase with the mutations I 181*+G182*, optionally with a N193F substitution, truncated to about 491 amino acids, i.e. , from 480-495 amino acids, (using SEQ ID NO: 1 herein for numbering) determined by incubating the reference alpha-amylase and variants at pH 4.5 and 5.5 and temperatures of 75°C and 85°C with 0.12 mM CaC followed by residual activity determination using the EnzChek® substrate (EnzChek® Ultra Amylase assay kit, E33651 , Molecular Probes). This is described in Example 1.

Examples of suitable Bacillus stearothermophilus alpha-amylase variants can be found below in the“Thermostable Alpha-Amylase”-section and include one from the following group of Bacillus stearothermophilus alpha-amylase variants with the following mutations: I 181*+G182*, and optionally substitution N193F, and further one of the following substitutions or combinations of substitutions: E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+ Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+ E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 for numbering).

Examples of other suitable Bacillus stearothermophilus alpha-amylases having increased thermostability compared to a reference alpha-amylase ( Bacillus stearothermophilus alpha-amylase with the mutations I 181*+G182*, and optionally a N193F substitution, C-terminally truncated to be 485-495 amino acids long, such as about 491 amino acids long) at pH 4.5 and 5.5, 0.12 mM CaCI ₂ can be found in WO 201 1/082425 hereby incorporated by reference. (See also Example 1 below)

Liquefaction in step i) may be carried out using a combination of alpha-amylase and protease. The protease may be a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C determined as described in Example 2 (Relative Activty). Examples of suitable proteases are described below in the section“Protease Present and/or Added During Liquefaction”.

The protease may be of fungal origin, such as of filamentous fungus origin. Specific examples of suitable fungal proteases are protease variants of metallo protease derived from a strain of the genus Thermoascus, e.g., a strain of Thermoascus aurantiacus, such as the strain Thermoascus aurantiacus CGMCC No. 0670 disclosed as the mature part of SEQ ID NO. 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein with one of the following substitutions or combinations of substitutions:

D79L+S87P+A1 12P+D142L;

D79L+S87P+D142L; and

A27K+ D79L+ Y82F+S87G+D104P+A1 12P+A126V+D142L.

More examples of suitable variants of the Thermoascus aurantiacus protease can be found in WO 201 1/072191 hereby incorporated by reference (See also Example 2 below).

Suitable proteases also include bacterial proteases. A suitable bacterial protease may be derived from a strain of Pyrococcus, e.g., a strain of Pyrococcus furiosus. In one embodiment, the protease is the one shown in SEQ ID NO: 1 in US 6,358,726 or SEQ ID NO: 13 herein.

In one embodiment, the alpha-amylase and/or protease, added in the liquefaction step i), is/are further combined with a glucoamylase. Thus, a glucoamylase may also be present and/or added during liquefaction step i). The glucoamylase may be thermostable. This means that the glucoamylase has a heat stability at 85°C, pH 5.3, of at least 20%, such as at least 30%, preferably at least 35% determined as described in Example 4 (heat stability). In one embodiment, the glucoamylase present and/or added in liquefaction has a relative activity pH optimum at pH 5.0 of at least 90%, e.g., at least 95%, or at least 97%. In one embodiment, the glucoamylase has a pH stability at pH 5.0 of at least at least 80%, e.g., at least 85%, or at least 90% determined as described in Example 4 (pH stability).

A suitable glucoamylase present and/or added in liquefaction step i) may be derived from a strain of the genus Penicillium, especially a strain of Penicillium oxalicum disclosed as SEQ ID NO: 2 in WO 2011/127802 or SEQ ID NOs: 9 or 14 herein. In one embodiment, the glucoamylase is a variant of the Penicillium oxalicum glucoamylase shown in SEQ ID NO: 2 in WO 201 1/127802 having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 herein for numbering), such as a variant disclosed in WO 2013/053801. In one embodiment, the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 for numbering) and further one of the following substitutions or combinations of substitutions:

P1 1 F + T65A + Q327F; and

P2N + P4S + P1 1 F + T65A + Q327F (using SEQ ID NO: 14 for numbering).

Examples of other suitable Penicillium oxalicum glucoamylase variants can be found in WO 2013/053801 incorporated by reference (see also Examples 10-16 below, such as the Penicillium oxalicum glucoamylase variants in Table 15).

Further, according to the processes described herein, a pullulanase may be present during liquefaction in combination with an alpha-amylase, a protease and/or a glucoamylase.

Saccharification and Fermentation

A glucoamylase is expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, present and/or added in saccharification step ii) and/or fermentation step iii) or simultaneous saccharification and fermentation (SSF). The glucoamylase expressed by the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, added in saccharification step ii) and/or fermentation step iii) or simultaneous saccharification and fermentation (SSF) is typically different from the glucoamylase, optionally added in liquefaction step i). In one embodiment, the glucoamylase is express or added together with a fungal alpha-amylase. Examples of glucoamylases can be found in the“Glucoamylases Present and/or Added In Saccharification and/or Fermentation”-section below.

When doing sequential saccharification and fermentation, saccharification step ii) may be carried out under conditions well-known in the art. For instance, saccharification step ii) may last up to from about 24 to about 72 hours. In one embodiment, pre-saccharification is done. Pre-saccharification is typically done for 40-90 minutes at a temperature between 30- 65°C, typically about 60°C. Pre-saccharification is, in one embodiment, followed by saccharification during fermentation in simultaneous saccharification and fermentation (SSF). Saccharification is typically carried out at temperatures from 20-75°C, preferably from 40- 70°C, typically about 60°C, and typically at a pH between 4 and 5, such as about pH 4.5.

Simultaneous saccharification and fermentation (“SSF”) is widely used in industrial scale fermentation product production processes, especially ethanol production processes. When doing SSF the saccharification step ii) and the fermentation step iii) are carried out simultaneously. There is no holding stage for the saccharification, meaning that a fermenting organism, such as yeast, and enzyme(s), may be added together. However, it is also contemplated to add the fermenting organism and enzyme(s) separately. SSF is typically carried out at a temperature from 25°C to 40°C, such as from 28°C to 35°C, such as from 30°C to 34°C, or about 32°C. In one embodiment, fermentation is ongoing for 6 to 120 hours, in particular 24 to 96 hours. In one embodiment, the pH is between 4-5.

In one embodiment, a cellulolytic enzyme composition is present and/or added in saccharification, fermentation or simultaneous saccharification and fermentation (SSF). Examples of such cellulolytic enzyme compositions can be found in the“Cellulolytic Enzyme Composition present and/or added during Saccharification and/or Fermentation”-section below. The cellulolytic enzyme composition is present and/or added together with a glucoamylase, such as one disclosed in the “Glucoamylase Present And/Or Added in Saccharification and/or Fermentation”-section below.

Starch-Containing Materials

Any suitable starch-containing starting material may be used with the processes described herein. The starting material is generally selected based on the desired fermentation product, here ethanol. Examples of starch-containing starting materials include cereal, tubers or grains. Specifically, the starch-containing material may be corn, wheat, barley, rye, milo, sago, cassava, tapioca, sorghum, oat, rice, peas, beans, or sweet potatoes, or mixtures thereof. Contemplated are also waxy and non-waxy types of corn and barley.

In one embodiment, the starch-containing starting material is corn. In one embodiment, the starch-containing starting material is wheat. In one embodiment, the starch-containing starting material is barley. In one embodiment, the starch-containing starting material is rye. In one embodiment, the starch-containing starting material is milo. In one embodiment, the starch-containing starting material is sago. In one embodiment, the starch-containing starting material is cassava. In one embodiment, the starch-containing starting material is tapioca. In one embodiment, the starch-containing starting material is sorghum. In one embodiment, the starch-containing starting material is rice. In one embodiment, the starch-containing starting material is peas. In one embodiment, the starch-containing starting material is beans. In one embodiment, the starch-containing starting material is sweet potatoes. In one embodiment, the starch-containing starting material is oats.

Fermentation Fermentation is carried out in a fermentation medium. The fermentation medium includes the fermentation substrate, that is, the carbohydrate source that is metabolized by the fermenting organism. With the processes described herein, the fermentation medium may comprise nutrients and growth stimulator(s) for the fermenting organism(s). Nutrient and growth stimulators are widely used in the art of fermentation and include nitrogen sources, such as ammonia; urea, vitamins and minerals, or combinations thereof.

Fermenting Organisms

Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038, or a derivative of Saccharomyces cerevisiae strain MBG5038 having defining characteristics of strain MBG5038, or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012, or a derivative of Saccharomyces cerevisiae strain MBG5012 having defining characteristics of strain MBG5012 may be used in a process described herein. In one embodiment, the fermenting organism has properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 as it provides an increase in ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions.

In one embodiment, the fermenting organism strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 has at least the one or more, such as all of following properties and defining characteristics:

increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

reduces acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

increases temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein; and decreases glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, conditions as described herein.

In one embodiment, the fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 provides an ethanol yield boost over Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) of more than 1.0%, e.g., more than 2.0%, such as more than 2.5%, such as about 2.9% using the same process set-up and conditions, e.g., conditions described herein.

In one embodiment, the fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 reduces acetaldehyde production more than 10%, e.g., more than 20%, more than 30%, more than 40%, more than 45%, such as between 5-60%, such as 30-50%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

In one embodiment, the fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 increases the temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Increased temperature tolerance is an advantage as the fermentation temperature may fluctuate to some degree. In the early part of fermentation plants often do not actively heat the fermentation. The temperature may therefore increase naturally from the yeast’s metabolism. The plant may use heat exchangers to control early fermentation temperatures so it does not go too high. During the majority of the year the plants can easily control the early temperature and the peak temperature is typically about 34°C. However, during the summer months the cooling water used in heat exchangers is not cold enough to control the temperatures. Therefore, in plants that do not have chillers (i.e. , a water refrigeration system), the early fermentation temperatures can reach above 36.5°C which stresses the yeast.

In one embodiment, the fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or MBG5012 decreases glycerol production by more than 3%, e.g., more than 4%, more than 5%, more than 6%, more than 7%, such as between 2-15%, such as 5-10%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein. Recovery

Subsequent to fermentation, e.g., SSF, the ethanol may be separated from the fermentation medium. The slurry may be distilled to recover/extract the desired fermentation product (i.e., ethanol). Alternatively, the desired fermentation product (i.e., ethanol) may be extracted from the fermentation medium by micro or membrane filtration techniques. The fermentation product (i.e., ethanol) may also be recovered by stripping or other method well known in the art.

Alpha-Amylase Present and/or Added In Liquefaction

The alpha-amylase used herein may be present and/or added in liquefaction optionally together with a protease and/or glucoamylase, and/or optional pullulanase, e.g., as disclosed in WO 2012/088303 (Novozymes) or WO 2013/082486 (Novozymes) which references are both incorporated by reference.

The alpha-amylase added in liquefaction step i) may be any alpha-amylase. In one embodiment, the alpha-amylase is a bacterial alpha-amylase, which may be stable at temperature.

Any alpha-amylase described herein, including any bacterial, hybrid and/or thermostable alpha-amylase described below, may be expressed by the Saccharomyces cerevisiae strain MBG5038 or MBG5012.

Bacterial Alpha-Amylase

The term “bacterial alpha-amylase” means any bacterial alpha-amylase classified under EC 3.2.1.1. A bacterial alpha-amylase used herein may, e.g., be derived from a strain of the genus Bacillus, which is sometimes also referred to as the genus Geobacillus. In one embodiment, the Bacillus alpha-amylase is derived from a strain of Bacillus amyloliquefaciens, Bacillus licheniformis, Bacillus stearothermophilus, or Bacillus subtilis, but may also be derived from other Bacillus sp.

Specific examples of bacterial alpha-amylases include the Bacillus stearothermophilus alpha-amylase (BSG) of SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein, the Bacillus amyloliquefaciens alpha-amylase (BAN) of SEQ ID NO: 5 in WO 99/19467, and the Bacillus licheniformis alpha-amylase (BLA) of SEQ ID NO: 4 in WO 99/19467 or SEQ ID NO: 21 herein (all sequences are hereby incorporated by reference). In one embodiment, the alpha-amylase may be an enzyme having a degree of identity of at least 60%, e.g., at least 70%, at least 80%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98% or at least 99% to any of the sequences shown in SEQ ID NOS: 3, 4 or 5, respectively, in WO 99/19467.

In one embodiment, the alpha-amylase may be an enzyme having a degree of identity of at least 60%, e.g., at least 70%, at least 80%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98% or at least 99% to any of the sequences shown in SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein.

In one embodiment, the alpha-amylase is derived from Bacillus stearothermophilus. The Bacillus stearothermophilus alpha-amylase may be a mature wild-type or a mature variant thereof. The mature Bacillus stearothermophilus alpha-amylases may naturally be truncated during recombinant production. For instance, the Bacillus stearothermophilus alpha-amylase may be a truncated at the C-terminal, so that it is from 480-495 amino acids long, such as about 491 amino acids long, e.g., so that it lacks a functional starch binding domain (compared to SEQ ID NO: 3 in WO 99/19467) or SEQ ID NO: 1 herein.

The Bacillus alpha-amylase may also be a variant and/or hybrid. Examples of such a variant can be found in any of WO 96/23873, WO 96/23874, WO 97/41213, WO 99/19467, WO 00/60059, and WO 02/10355 (each hereby incorporated by reference). Specific alpha- amylase variants are disclosed in U.S. Patent Nos. 6,093,562, 6, 187,576, 6,297,038, and 7,713,723 (hereby incorporated by reference) and include Bacillus stearothermophilus alpha- amylase (often referred to as BSG alpha-amylase) variants having a deletion of one or two amino acids at positions R179, G180, 1181 and/or G182, preferably a double deletion disclosed in WO 96/23873 - see, e.g., page 20, lines 1-10 (hereby incorporated by reference), such as corresponding to deletion of positions 1181 and G182 compared to the amino acid sequence of Bacillus stearothermophilus alpha-amylase set forth in SEQ ID NO: 3 disclosed in WO 99/19467 or SEQ ID NO: 1 herein or the deletion of amino acids R179 and G180 using SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein for numbering (which reference is hereby incorporated by reference). In some embodimenst, the Bacillus alpha-amylases, such as Bacillus stearothermophilus alpha-amylases, have a double deletion corresponding to a deletion of positions 181 and 182 and further optionally comprise a N193F substitution (also denoted 1181* + G182* + N193F) compared to the wild-type BSG alpha-amylase amino acid sequence set forth in SEQ ID NO: 3 disclosed in WO 99/19467 or SEQ ID NO: 1 herein. The bacterial alpha-amylase may also have a substitution in a position corresponding to S239 in the Bacillus licheniformis alpha-amylase shown in SEQ ID NO: 4 in WO 99/19467 or SEQ ID NO: 21 herein, or a S242 and/or E188P variant of the Bacillus stearothermophilus alpha- amylase of SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein.

In one embodiment, the variant is a S242A, E or Q variant, e.g., a S242Q variant, of the Bacillus stearothermophilus alpha-amylase (using SEQ ID NO: 1 herein for numbering).

In one embodiment, the variant is a position E188 variant, e.g., E188P variant of the Bacillus stearothermophilus alpha-amylase (using SEQ ID NO: 1 herein for numbering).

The bacterial alpha-amylase may, in one embodiment, be a truncated Bacillus alpha- amylase. In one embodiment, the truncation is so that, e.g., the Bacillus stearothermophilus alpha-amylase shown in SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein, is about 491 amino acids long, such as from 480 to 495 amino acids long, or so it lacks a functional starch bind domain.

Bacterial Hybrid Alpha-Amylases

The bacterial alpha-amylase may also be a hybrid bacterial alpha-amylase, e.g., an alpha-amylase comprising 445 C-terminal amino acid residues of the Bacillus licheniformis alpha-amylase (shown in SEQ ID NO: 4 of WO 99/19467) and the 37 N-terminal amino acid residues of the alpha-amylase derived from Bacillus amyloliquefaciens (shown in SEQ ID NO: 5 of WO 99/19467). In one embodiment, this hybrid has one or more, especially all, of the following substitutions:

G48A+T49I+G107A+H156Y+A181T+N190F+I201 F+A209V+Q264S (using the Bacillus licheniformis numbering in SEQ ID NO: 4 of WO 99/19467) or SEQ ID NO: 21 herein. In some embodiments, the variants have one or more of the following mutations (or corresponding mutations in other Bacillus alpha-amylases): H154Y, A181T, N190F, A209V and Q264S and/or the deletion of two residues between positions 176 and 179, e.g., deletion of E178 and G179 (using SEQ ID NO: 5 of WO 99/19467 for position numbering or SEQ ID NO: 21 herein).

In one embodiment, the bacterial alpha-amylase is the mature part of the chimeric alpha-amylase disclosed in Richardson et al. (2002), The Journal of Biological Chemistry, Vol. 277, No 29, Issue 19 July, pp. 267501-26507, referred to as BD5088 or a variant thereof. This alpha-amylase is the same as the one shown in SEQ ID NO: 2 in WO 2007134207. The mature enzyme sequence starts after the initial“Met” amino acid in position 1.

Thermostable Alpha-Amylase

The alpha-amylase may be a thermostable alpha-amylase, such as a thermostable bacterial alpha-amylase, e.g., from Bacillus stearothermophilus. In one embodiment, the alpha-amylase used in a process described herein has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10 determined as described in Example 1.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of at least 15.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of as at least 20.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of as at least 25.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of as at least 30.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of as at least 40.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of at least 50. In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , of at least 60.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 10-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 15-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 20-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 25-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 30-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 40-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 50-70.

In one embodiment, the thermostable alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ , between 60-70.

In one embodiment, the alpha-amylase is a bacterial alpha-amylase, e.g., derived from the genus Bacillus, such as a strain of Bacillus stearothermophilus, e.g., the Bacillus stearothermophilus as disclosed in WO 99/019467 as SEQ ID NO: 3 (SEQ ID NO: 1 herein) with one or two amino acids deleted at positions R179, G180, 1181 and/or G182, in particular with R179 and G180 deleted, or with 1181 and G182 deleted, with mutations in below list of mutations.

In some embodiment, the Bacillus stearothermophilus alpha-amylases have double deletion 1181 + G182, and optional substitution N193F, further comprising one of the following substitutions or combinations of substitutions:

V59A+Q89R+G1 12D+E129V+K177L+R179E+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+D269E+D281 N;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+I270L;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+H274K;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+Y276F;

V59A+E129V+R157Y+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+H208Y+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+H274K; V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+D281 N;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+G416V;

V59A+E129V+K177L+R179E+K220P+N224L+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

A91 L+M96I+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F+L427M;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+N376*+I377*;

E129V+K177L+R179E+K220P+N224L+Q254S;

E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

E129V+K177L+R179E+S242Q;

E129V+K177L+R179V+K220P+N224L+S242Q+Q254S;

K220P+N224L+S242Q+Q254S;

M284V;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V; and

V59A+E129V+K177L+R179E+Q254S+ M284V;

In one embodiment, the alpha-amylase is selected from the group of Bacillus stearothermophilus alpha-amylase variants with double deletion I 181*+G182*, and optionally substitution N193F, and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+K177L+R179E+Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

It should be understood that when referring to Bacillus stearothermophilus alpha- amylase and variants thereof they are normally produced in truncated form. In particular, the truncation may be so that the Bacillus stearothermophilus alpha-amylase shown in SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein, or variants thereof, are truncated in the C- terminal and are typically from 480-495 amino acids long, such as about 491 amino acids long, e.g., so that it lacks a functional starch binding domain. In one embodiment, the alpha-amylase variant may be an enzyme having a degree of identity of at least 60%, e.g., at least 70%, at least 80%, at least 90%, at least 95%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98% or at least 99%, but less than 100% to the sequence shown in SEQ ID NO: 3 in WO 99/19467 or SEQ ID NO: 1 herein.

In one embodiment, the bacterial alpha-amylase, e.g., Bacillus alpha-amylase, such as especially Bacillus stearothermophilus alpha-amylase, or variant thereof, is dosed to liquefaction in a concentration between 0.01-10 KNU-A/g DS, e.g., between 0.02 and 5 KNU- A/g DS, such as 0.03 and 3 KNU-A, preferably 0.04 and 2 KNU-A/g DS, such as especially 0.01 and 2 KNU-A/g DS. In one embodiment, the bacterial alpha-amylase, e.g., Bacillus alpha- amylase, such as especially Bacillus stearothermophilus alpha-amylases, or variant thereof, is dosed to liquefaction in a concentration of between 0.0001-1 mg EP (Enzyme Protein)/g DS, e.g., 0.0005-0.5 mg EP/g DS, such as 0.001-0.1 mg EP/g DS.

Protease Present and/or Added In Liquefaction

In the processes described ehrein, the protease may optionally be present and/or added in liquefaction together with alpha-amylase, and an optional glucoamylase, and/or pullulanase.

Proteases are classified on the basis of their catalytic mechanism into the following groups: Serine proteases (S), Cysteine proteases (C), Aspartic proteases (A), Metallo proteases (M), and Unknown, or as yet unclassified, proteases (U), see Handbook of Proteolytic Enzymes, A. J. Barrett, N.D. Rawlings, J.F.Woessner (eds), Academic Press (1998), in particular the general introduction part.

In one embodiment, the thermostable protease used according to a process described herein is a “metallo protease” defined as a protease belonging to EC 3.4.24 (metalloendopeptidases); preferably EC 3.4.24.39 (acid metallo proteinases).

To determine whether a given protease is a metallo protease or not, reference is made to the above“Handbook of Proteolytic Enzymes” and the principles indicated therein. Such determination can be carried out for all types of proteases, be it naturally occurring or wild- type proteases; or genetically engineered or synthetic proteases.

Protease activity can be measured using any suitable assay, in which a substrate is employed, that includes peptide bonds relevant for the specificity of the protease in question. Assay-pH and assay-temperature are likewise to be adapted to the protease in question. Examples of assay-pH-values are pH 6, 7, 8, 9, 10, or 11. Examples of assay-temperatures are 30, 35, 37, 40, 45, 50, 55, 60, 65, 70 or 80°C.

Examples of protease substrates are casein, such as Azurine-Crosslinked Casein (AZCL-casein). Two protease assays are described below in the“Materials & Methods”- section, of which the so-called“AZCL-Casein Assay” is the preferred assay. In one embodiment, the thermostable protease has at least 20%, such as at least 30%, such as at least 40%, such as at least 50%, such as at least 60%, such as at least 70%, such as at least 80%, such as at least 90%, such as at least 95%, such as at least 100% of the protease activity of the Protease 196 variant or Protease Pfu determined by the AZCL-casein assay described in the“Materials & Methods” section.

There are no limitations on the origin of the protease used in a process described herein as long as it fulfills the thermostability properties defined below.

In one embodiment the protease is of fungal origin.

The protease may be a variant of, e.g., a wild-type protease as long as the protease has the thermostability properties defined herein. In one embodiment, the thermostable protease is a variant of a metallo protease as defined above. In one embodiment, the thermostable protease used in a process described herein is of fungal origin, such as a fungal metallo protease, such as a fungal metallo protease derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially Thermoascus aurantiacus CGMCC No. 0670 (classified as EC 3.4.24.39).

In one embodiment, the thermostable protease is a variant of the mature part of the metallo protease shown in SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 and shown as SEQ ID NO: 3 herein further with one of the following substitutions or combinations of substitutions:

S5*+ D79L+S87 P+ A 112 P+ D 142 L;

D79L+S87 P+ A 112 P+T 124 V+ D 142 L;

S5*+N26R+D79L+S87P+A1 12P+D142L;

N26R+T46R+D79L+S87P+A1 12P+D142L;

T46R+D79L+S87P+T 1 16V+D142L;

D79L+P81 R+S87P+A1 12P+D142L;

A27 K+ D79L+S87 P+ A 112 P+T 124V+ D 142 L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+S87 P+ A 112 P+T 124 V+ A 126V+ D 142 L;

D79L+S87P+A112P+D142L;

D79L+Y82F+S87P+A1 12P+D142L;

S38T+ D79L+S87P+A1 12P+A126 V+ D 142 L;

D79L+Y82 F+S87P+A1 12P+A126 V+ D 142 L;

A27 K+ D79L+S87 P+ A 112 P+ A 126V+ D 142 L;

D79L+S87P+N98C+A112P+G135C+D142L;

D79L+S87P+A1 12P+D142L+T141 C+M161 C;

S36P+D79L+S87P+A1 12P+D142L; A37P+D79L+S87P+A112P+D142L;

S49P+D79L+S87P+A112P+D142L;

S50P+D79L+S87P+A112P+D142L;

D79L+S87P+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+D142L;

S70V+ D79 L+Y82 F+S87G+ Y97W+A 112 P+ D 142 L;

D79L+Y82F+S87G+Y97W+D104P+A112P+D142L;

S70V+ D79 L+Y82 F+S87G+ A 1 12 P+ D 142 L;

D79L+Y82F+S87G+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+A126V+D142L;

Y82F+S87G+S70V+D79L+D104P+A1 12P+D142L;

Y82F+S87G+D79L+D104P+A112P+A126V+D142L;

A27K+ D79L+Y82 F+S87G+ D 104P+A1 12 P+A126V+ D 142 L;

A27K+Y82F+S87G+D104P+A112P+A126V+D142L;

A27K+D79L+Y82F+ D104P+A112P+A126V+D142L;

A27K+Y82F+ D 104 P+ A 112 P+ A 126V+ D 142 L;

A27K+D79L+S87P+A112P+D142L; and

D79L+S87P+D142L.

In one embodiment, the thermostable protease is a variant of the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein with one of the following substitutions or combinations of substitutions:

D79L+S87P+A112P+D142L;

D79L+S87P+D142L; and

A27K+ D79L+Y82F+S87G+D104P+A1 12P+A126V+D142L

In one embodiment, the protease variant has at least 75% identity preferably at least 80%, more preferably at least 85%, more preferably at least 90%, more preferably at least 91 %, more preferably at least 92%, even more preferably at least 93%, most preferably at least 94%, and even most preferably at least 95%, such as even at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein.

The thermostable protease may also be derived from any bacterium as long as the protease has the thermostability properties.

In one embodiment, the thermostable protease is derived from a strain of the bacterium Pyrococcus, such as a strain of Pyrococcus furiosus (pfu protease). In one embodiment, the protease is one shown as SEQ ID NO: 1 in US patent No. 6,358,726-B1 (Takara Shuzo Company), or SEQ ID NO: 13 herein.

In one embodiment, the thermostable protease is SEQ ID NO: 13 herein or a protease having at least 80% identity, such as at least 85%, such as at least 90%, such as at least 95%, such as at least 96%, such as at least 97%, such as at least 98%, such as at least 99% identity to SEQ ID NO: 1 in US patent no. 6,358,726-B1 or SEQ ID NO: 13 herein. The Pyroccus furiosus protease can be purchased from Takara Bio, Japan.

The Pyrococcus furiosus protease is a thermostable protease. The commercial product Pyrococcus furiosus protease (PfuS) was found to have a thermostability of 110% (80°C/70°C) and 103% (90°C/70°C) at pH 4.5 determined as described in Example 2.

In one embodiment, a thermostable protease used in a process described herein has a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C determined as described in Example 2.

In one embodiment, the protease has a thermostability of more than 30%, more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, such as more than 105%, such as more than 1 10%, such as more than 1 15%, such as more than 120% determined as Relative Activity at 80°C/70°C.

In one embodiment, protease has a thermostability of between 20 and 50%, such as between 20 and 40%, such as 20 and 30% determined as Relative Activity at 80°C/70°C. In one embodiment, the protease has a thermostability between 50 and 115%, such as between 50 and 70%, such as between 50 and 60%, such as between 100 and 120%, such as between 105 and 115% determined as Relative Activity at 80°C/70°C.

In one embodiment, the protease has a thermostability value of more than 10% determined as Relative Activity at 85°C/70°C determined as described in Example 2.

In one embodiment, the protease has a thermostability of more than 10%, such as more than 12%, more than 14%, more than 16%, more than 18%, more than 20%, more than 30%, more than 40%, more that 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, more than 110% determined as Relative Activity at 85°C/70°C.

In one embodiment, the protease has a thermostability of between 10% and 50%, such as between 10% and 30%, such as between 10% and 25% determined as Relative Activity at 85°C/70°C.

In one embodiment, the protease has more than 20%, more than 30%, more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90% determined as Remaining Activity at 80°C; and/or the protease has more than 20%, more than 30%, more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90% determined as Remaining Activity at 84°C. Determination of “Relative Activity” and“Remaining Activity” is done as described in Example 2.

In one embodiment, the protease may have a themostability for above 90, such as above 100 at 85°C as determined using the Zein-BCA assay as disclosed in Example 3.

In one embodiment, the protease has a themostability above 60%, such as above 90%, such as above 100%, such as above 1 10% at 85°C as determined using the Zein-BCA assay.

In one embodiment, protease has a themostability between 60-120, such as between 70-120%, such as between 80-120%, such as between 90-120%, such as between 100-120%, such as 110-120% at 85°C as determined using the Zein-BCA assay.

In one embodiment, the thermostable protease has at least 20%, such as at least 30%, such as at least 40%, such as at least 50%, such as at least 60%, such as at least 70%, such as at least 80%, such as at least 90%, such as at least 95%, such as at least 100% of the activity of the JTP196 protease variant or Protease Pfu determined by the AZCL-casein assay. Glucoamylase Expressed, Present and/or Added In Liquefaction Step i)

A glucoamylase may optionally be expressed, present and/or added in liquefaction step i). In one embodiment, the glucoamylase is added together with or separately from the alpha-amylase and/or the optional protease and/or pullulanase.

In one embodiment, the glucoamylase has a Relative Activity heat stability at 85°C of at least 20%, at least 30%, or at least 35% determined as described in Example 4 (heat stability).

In one embodiment, the glucoamylase has a relative activity pH optimum at pH 5.0 of at least 90%, e.g., at least 95%, at least 97%, or 100% determined as described in Example 4 (pH optimum).

In one embodiment, the glucoamylase has a pH stability at pH 5.0 of at least 80%, at least 85%, at least 90% determined as described in Example 4 (pH stability).

In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant, used in liquefaction has a thermostability determined as DSC Td at pH 4.0 as described in Example 15 of at least 70°C, preferably at least 75°C, such as at least 80°C, such as at least 81°C, such as at least 82°C, such as at least 83°C, such as at least 84°C, such as at least 85°C, such as at least 86°C, such as at least 87%, such as at least 88°C, such as at least 89°C, such as at least 90°C. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as DSC Td at pH 4.0 as described in Example 15 in the range between 70°C and 95°C, such as between 80°C and 90°C.

In one embodiment, the glucoamylase, such as a PeniciHium oxalicum glucoamylase variant, used in liquefaction has a thermostability determined as DSC Td at pH 4.8 as described in Example 15 of at least 70°C, preferably at least 75°C, such as at least 80°C, such as at least 81°C, such as at least 82°C, such as at least 83°C, such as at least 84°C, such as at least 85°C, such as at least 86°C, such as at least 87%, such as at least 88°C, such as at least 89°C, such as at least 90°C, such as at least 91 °C. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as DSC Td at pH 4.8 as described in Example 15 in the range between 70°C and 95°C, such as between 80°C and 90°C.

In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant, used in liquefaction has a residual activity determined as described in Example 16 of at least 100% such as at least 105%, such as at least 1 10%, such as at least 1 15%, such as at least 120%, such as at least 125%. In one embodiment, the glucoamylase, such as a Penicillium oxalicum glucoamylase variant has a thermostability determined as residual activity as described in Example 16 in the range between 100% and 130%.

In one embodiment, the glucoamylase, e.g., of fungal origin such as a filamentous fungi, from a strain of the genus Penicillium, e.g., a strain of Penicillium oxalicum, in particular the Penicillium oxalicum glucoamylase disclosed as SEQ ID NO: 2 in WO 201 1/127802 (which is hereby incorporated by reference) and shown in SEQ ID NO: 9 or 14 herein.

In one embodiment, the glucoamylase has at least 80%, e.g., at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99% or 100% identity to the mature polypeptide shown in SEQ ID NO: 2 in WO 201 1/127802 or SEQ ID NOs: 9 or 14 herein.

In one embodiment, the glucoamylase is a variant of the Penicillium oxalicum glucoamylase disclosed as SEQ ID NO: 2 in WO 2011/127802 and shown in SEQ ID NO: 9 and 14 herein, having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 herein for numbering). The K79V glucoamylase variant has reduced sensitivity to protease degradation relative to the parent as disclosed in WO 2013/036526 (which is hereby incorporated by reference).

In one embodiment, the glucoamylase is derived from Penicillium oxalicum.

In one embodiment, the glucoamylase is a variant of the Penicillium oxalicum glucoamylase disclosed as SEQ ID NO: 2 in WO 2011/127802 and shown in SEQ ID NO: 9 and 14 herein. In one embodiment, the Penicillium oxalicum glucoamylase is the one disclosed as SEQ ID NO: 2 in WO 201 1/127802 and shown in SEQ ID NO: 9 and 14 herein having Val (V) in position 79 (using SEQ ID NO: 14 herein for numbering).

Contemplated Penicillium oxalicum glucoamylase variants are disclosed in WO 2013/053801 which is hereby incorporated by reference.

In one embodiment, these variants have reduced sensitivity to protease degradation.

In one embodiment, these variant have improved thermostability compared to the parent. In one embodiment, the glucoamylase has a K79V substitution (using SEQ ID NO: 14 herein for numbering), corresponding to the PE001 variant, and further comprises one of the following alterations or combinations of alterations:

T65A; Q327F; E501V; Y504T; Y504*; T65A + Q327F; T65A + E501V; T65A + Y504T ; T65A + Y504*; Q327F + E501V; Q327F + Y504T; Q327F + Y504*; E501V + Y504T; E501V + Y504*; T65A + Q327F + E501V; T65A + Q327F + Y504T; T65A + E501V + Y504T ; Q327F + E501V + Y504T; T65A + Q327F + Y504*; T65A + E501V + Y504*; Q327F + E501V + Y504*; T65A + Q327F + E501V + Y504T; T65A + Q327F + E501V + Y504*; E501V + Y504T; T65A + K161S; T65A + Q405T; T65A + Q327W; T65A + Q327F; T65A + Q327Y; P11F + T65A + Q327F; R1K + D3W + K5Q + G7V + N8S + T10K+ P11S + T65A + Q327F; P2N + P4S + P11F + T65A + Q327F; P11F + D26C + K33C + T65A + Q327F; P2N + P4S + P11F + T65A + Q327W + E501V + Y504T ; R1E + D3N + P4G + G6R + G7A + N8A + T10D+ P11D + T65A + Q327F; P11F + T65A + Q327W; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T; P11F + T65A + Q327W+ E501V + Y504T; T65A + Q327F + E501V + Y504T; T65A + S105P + Q327W; T65A + S105P + Q327F; T65A + Q327W+ S364P; T65A + Q327F + S364P; T65A + S103N + Q327F; P2N + P4S + P11F + K34Y + T65A + Q327F; P2N + P4S + P11F + T65A + Q327F + D445N + V447S; P2N + P4S + P11F + T65A + 1172V + Q327F; P2N + P4S + P11F + T65A + Q327F + N502*; P2N + P4S + P11F + T65A + Q327F + N502T + P563S + K571E; P2N + P4S + P11F + R31S + K33V + T65A + Q327F + N564D + K571S; P2N + P4S + P11F + T65A + Q327F + S377T; P2N + P4S + P11F + T65A + V325T+ Q327W; P2N + P4S + P11F + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11F + T65A + 1172V + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + S377T + E501V + Y504T; P2N + P4S + P11F + D26N + K34Y + T65A + Q327F; P2N + P4S + P11F + T65A + Q327F + I375A + E501V + Y504T; P2N + P4S + P11F + T65A + K218A + K221D + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + S103N + Q327F + E501V + Y504T; P2N + P4S + T10D + T65A + Q327F + E501 V + Y504T; P2N + P4S + F12Y + T65A + Q327F + E501V + Y504T; K5A + P11F + T65A + Q327F + E501V + Y504T; P2N + P4S + T10E + E18N + T65A + Q327F + E501V + Y504T; P2N + T10E + E18N + T65A + Q327F + E501 V + Y504T; P2N + P4S + P11F + T65A + Q327F + E501 V + Y504T + T568N; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T + K524T + G526A; P2N + P4S + P11F + K34Y + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11F + R31S + K33V + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11F + D26N + K34Y + T65A + Q327F + E501V + Y504T; P2N + P4S+ P11F + T65A+ F80* + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + K112S + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T + T516P + K524T + G526A; P2N + P4S + P11 F + T65A + Q327F + E501V + N502T + Y504*; P2N + P4S + P11 F + T65A + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + S103N + Q327F + E501V + Y504T; K5A + P1 1 F + T65A + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + Q327F + E501 V + Y504T + T516P + K524T + G526A; P2N + P4S + P1 1 F + T65A + V79A + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + V79G + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + V79I + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + V79L + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + V79S + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + L72V + Q327F + E501 V + Y504T; S255N + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + E74N + V79K + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + G220N + Q327F + E501 V + Y504T; P2N + P4S + P1 1 F + T65A + Y245N + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + Q253N + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + D279N + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + Q327F + S359N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + D370N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + V460S + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + V460T + P468T + E501V + Y504T ; P2N + P4S + P1 1 F + T65A + Q327F + T463N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + S465N + E501V + Y504T; and P2N + P4S + P1 1 F + T65A + Q327F + T477N + E501V + Y504T.

In one embodiment, the Penicillium oxalicum glucoamylase variant has a K79V substitution (using SEQ ID NO: 14 herein for numbering), corresponding to the PE001 variant, and further comprises one of the following substitutions or combinations of substitutions:

P11 F + T65A + Q327F;

P2N + P4S + P11 F + T65A + Q327F;

P11 F + D26C + K33C + T65A + Q327F;

P2N + P4S + P11 F + T65A + Q327W + E501 V + Y504T;

P2N + P4S + P11 F + T65A + Q327F + E501 V + Y504T; and

P11 F + T65A + Q327W + E501 V + Y504T.

The glucoamylase may be added in amounts from 0.1-100 micrograms EP/g, such as 0.5-50 micrograms EP/g, such as 1-25 micrograms EP/g, such as 2-12 micrograms EP/g DS. Pullulanase Present and/or Added In Liquefaction step i)

Optionally a pullulanase may be present and/or added during liquefaction step i) together with an alpha-amylase, and/or optional protease and/or glucoamylase.

The pullulanase may be present and/or added in liquefaction step i) and/or saccharification step ii) or simultaneous saccharification and fermentation (SSF).

Pullulanases (E.C. 3.2.1.41 , pullulan 6-glucano-hydrolase), are debranching enzymes characterized by their ability to hydrolyze the alpha-1 , 6-glycosidic bonds in, for example, amylopectin and pullulan. Contemplated pullulanases include the pullulanases from Bacillus amyloderamificans disclosed in U.S. Patent No. 4,560,651 (hereby incorporated by reference), the pullulanase disclosed as SEQ ID NO: 2 in WO 01/151620 (hereby incorporated by reference), the Bacillus deramificans disclosed as SEQ ID NO: 4 in WO 01/151620 (hereby incorporated by reference), and the pullulanase from Bacillus acidopullulyticus disclosed as SEQ ID NO: 6 in WO 01/151620 (hereby incorporated by reference) and also described in FEMS Mic. Let. (1994) 1 15, 97-106.

Additional pullulanases contemplated include the pullulanases from Pyrococcus woesei, specifically from Pyrococcus woesei DSM No. 3773 disclosed in WO92/02614.

In one embodiment, the pullulanase is a family GH57 pullulanase. In one embodiment, the pullulanase includes an X47 domain as disclosed in US 61/289,040 published as WO 2011/087836 (which are hereby incorporated by reference). More specifically the pullulanase may be derived from a strain of the genus Thermococcus, including Thermococcus litoralis and Thermococcus hydrothermalis, such as the Thermococcus hydrothermalis pullulanase shown in SEQ ID NO: 11 truncated at site X4 right after the X47 domain (i.e. , amino acids 1- 782 in SEQ ID NOS: 11 and 12 herein). The pullulanase may also be a hybrid of the Thermococcus litoralis and Thermococcus hydrothermalis pullulanases or a T hydrothermalis/T. litoralis hybrid enzyme with truncation site X4 disclosed in US 61/289,040 published as WO 2011/087836 (which is hereby incorporated by reference) and disclosed in SEQ ID NO: 12 herein.

In another embodiment the pullulanase is one comprising an X46 domain disclosed in WO 2011/076123 (Novozymes).

The pullulanase may be added in an effective amount which include the preferred amount of about 0.0001-10 mg enzyme protein per gram DS, preferably 0.0001-0.10 mg enzyme protein per gram DS, more preferably 0.0001-0.010 mg enzyme protein per gram DS. Pullulanase activity may be determined as NPUN. An Assay for determination of NPUN is described in the“Materials & Methods”-section below.

Suitable commercially available pullulanase products include PROMOZYME D, PROMOZYME™ D2 (Novozymes A/S, Denmark), OPTIMAX L-300 (DuPont-Danisco, USA), and AMANO 8 (Amano, Japan).

Glucoamylase Expressed. Present And/Or Added in Saccharification and/or Fermentation

Glucoamylase may be expressed, present and/or added in saccharification, fermentation or simultaneous saccharification and fermentation (SSF). The glucoamylse may be derived from any suitable source, e.g., derived from a microorganism or a plant. Preferred glucoamylases are of fungal or bacterial origin, selected from the group consisting of Aspergillus glucoamylases, in particular Aspergillus niger G1 or G2 glucoamylase (Boel et al. (1984), EMBO J. 3 (5), p. 1097-1 102), or variants thereof, such as those disclosed in WO 92/00381 , WO 00/04136 and WO 01/04273 (from Novozymes, Denmark); the A. awamori glucoamylase disclosed in WO 84/02921 , Aspergillus oryzae glucoamylase (Agric. Biol. Chem. (1991), 55 (4), p. 941-949), or variants or fragments thereof. Other Aspergillus glucoamylase variants include variants with enhanced thermal stability: G137A and G139A (Chen et al. (1996), Prot. Eng. 9, 499-505); D257E and D293E/Q (Chen et al. (1995), Prot. Eng. 8, 575-582); N182 (Chen et al. (1994), Biochem. J. 301 , 275-281); disulphide bonds, A246C (Fierobe et al. (1996), Biochemistry, 35, 8698-8704; and introduction of Pro residues in position A435 and S436 (Li et al. (1997), Protein Eng. 10, 1199-1204.

Other glucoamylases include Athelia rolfsii (previously denoted Corticium rolfsii) glucoamylase (see US patent no. 4,727,026 and (Nagasaka et al. (1998)“Purification and properties of the raw-starch-degrading glucoamylases from Corticium rolfsii, Appl Microbiol Biotechnol 50:323-330), Talaromyces glucoamylases, in particular derived from Talaromyces emersonii (WO 99/28448), Talaromyces leycettanus (US patent no. Re. 32,153), Talaromyces duponti, Talaromyces thermophilus (US patent no. 4,587,215). In one embodiment, the glucoamylase used during saccharification and/or fermentation is the Talaromyces emersonii glucoamylase disclosed in WO 99/28448.

Bacterial glucoamylases contemplated include glucoamylases from the genus Clostridium, in particular C. thermoamylolyticum (EP 135, 138), and C. thermohydrosulfuricum (WO 86/01831).

Contemplated fungal glucoamylases include Trametes cingulate (SEQ ID NO: 20), Pachykytospora papyracea\ and Leucopaxillus giganteus all disclosed in WO 2006/069289; or Peniophora rufomarginata disclosed in W02007/124285; or a mixture thereof. Also hybrid glucoamylase are contemplated. Examples include the hybrid glucoamylases disclosed in WO 2005/045018. Specific examples include the hybrid glucoamylase disclosed in Table 1 and 4 of Example 1 (which hybrids are hereby incorporated by reference).

In one embodiment, the glucoamylase is derived from a strain of the genus Pycnoporus, in particular a strain of Pycnoporus as described in WO 2011/066576 (SEQ ID NOs 2, 4 or 6), including the Pycnoporus sanguineus glucoamylase disclosed as SEQ ID NO: 18 herein, or from a strain of the genus Gloeophyllum, such as a strain of Gloeophyllum sepiarium or Gloeophyllum trabeum, in particular a strain of Gloeophyllum as described in WO 2011/068803 (SEQ ID NO: 2, 4, 6, 8, 10, 12, 14 or 16). In one embodiment, the glucoamylase is SEQ ID NO: 2 in WO 2011/068803 or SEQ ID NO: 15 herein (i.e. Gloeophyllum sepiarium glucoamylase).

In one embodiment, the glucoamylase is SEQ ID NO: 17 herein (i.e., Gloeophyllum trabeum glucoamylase disclosed as SEQ ID NO: 3 in WO2014/177546). In another embodiment the glucoamylase is derived from a strain of the genus Nigrofomes, in particular a strain of Nigrofomes sp. disclosed in WO 2012/064351 (SEQ ID NO: 2) (all references hereby incorporated by reference).

Contemplated are also glucoamylases which exhibit a high identity to any of the above mentioned glucoamylases, i.e., at least 60%, such as at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99% or even 100% identity to any one of the mature parts of the enzyme sequences mentioned above, such as any of SEQ ID NOs: 15, 17, 18 or 19 herein, respectively, preferably SEQ ID NO: 15 herein or SEQ ID NO: 17 herein.

Glucoamylases may be added to the saccharification and/or fermentation in an amount of 0.0001-20 AGU/g DS, preferably 0.001-10 AGU/g DS, especially between 0.01-5 AGU/g DS, such as 0.1-2 AGU/g DS.

Glucoamylases may be added to the saccharification and/or fermentation in an amount of 1-1 ,000 pg EP/g DS, preferably 10-500 pg/gDS, especially between 25-250 pg/g DS.

In one embodiment, the glucoamylase is added as a blend further comprising an alpha- amylase. In one embodiment, the alpha-amylase is a fungal alpha-amylase, especially an acid fungal alpha-amylase. The alpha-amylase is typically a side activity.

In one embodiment, the glucoamylase is a blend comprising Talaromyces emersonii glucoamylase disclosed in WO 99/28448 as SEQ ID NO: 34 and SEQ ID NO: 19 herein and Trametes cingulata glucoamylase disclosed as SEQ ID NO: 2 in WO 06/069289 and SEQ ID NO: 20 herein.

In one embodiment, the glucoamylase is a blend comprising Talaromyces emersonii glucoamylase disclosed in WO 99/28448 (SEQ ID NO: 19 herein), Trametes cingulata glucoamylase disclosed as SEQ ID NO: 2 in WO 06/69289 and SEQ ID NO: 20 herein, and an alpha-amylase.

In one embodiment, the glucoamylase is a blend comprising Talaromyces emersonii glucoamylase disclosed in W099/28448 (SEQ ID NO: 19 herein), Trametes cingulata glucoamylase disclosed in WO 06/69289 (SEQ ID NO: 20 herein), and Rhizomucor pusillus alpha-amylase with Aspergillus n/ger glucoamylase linker and SBD disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment, the glucoamylase is a blend comprising Gloeophyllum sepiarium glucoamylase shown as SEQ ID NO: 2 in WO 2011/068803 (SEQ ID NO: 15 herein) and an alpha-amylase, in particular Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), disclosed SEQ ID NO: 3 in WO 2013/006756, in particular with the following substitutions: G128D+D143N.

In one embodiment, the alpha-amylase may be derived from a strain of the genus Rhizomucor, preferably a strain the Rhizomucor pusillus, such as the one shown in SEQ ID NO: 3 in W02013/006756, or the genus Meripilus, preferably a strain of Meripilus giganteus. In one embodiment, the alpha-amylase is derived from a Rhizomucor pusillus with an Aspergillus n/ger glucoamylase linker and starch-binding domain (SBD), disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment, the Rhizomucor pusillus alpha-amylase or the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) has at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; and G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C (using SEQ ID NO: 3 in WO 2013/006756 for numbering or SEQ ID NO: 16 herein).

In one embodiment, the glucoamylase blend comprises Gloeophyllum sepiarium glucoamylase (e.g., SEQ ID NO: 2 in WO 2011/068803 or SEQ ID NO: 15 herein) and Rhizomucor pusillus alpha-amylase.

In one embodiment, the glucoamylase blend comprises Gloeophyllum sepiarium glucoamylase shown as SEQ ID NO: 2 in WO 2011/068803 or SEQ ID NO: 15 herein and Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), disclosed SEQ ID NO: 3 in WO 2013/006756 and SEQ ID NO: 16 herein with the following substitutions: G128D+D143N.

Commercially available compositions comprising glucoamylase include AMG 200L; AMG 300 L; SAN™ SUPER, SAN™ EXTRA L, SPIRIZYME™ PLUS, SPIRIZYME™ FUEL, SPIRIZYME™ B4U, SPIRIZYME™ ULTRA, SPIRIZYME™ EXCEL, SPIRIZYME ACHIEVE™, and AMG™ E (from Novozymes A/S); OPTIDEX™ 300, GC480, GC417 (from DuPont- Danisco); AMIGASE™ and AMIGASE™ PLUS (from DSM); G-ZYME™ G900, G-ZYME™ and G990 ZR (from DuPont-Danisco).

Cellulolytic Enzyme Composition present and/or added during Saccharification and/or Fermentation

A cellulolytic enzyme composition comprising a beta-glucosidase, a cellobiohydrolase and an endoglucanase may be present in saccharification or fermentation or simultaneous saccharification and fermentation (SSF).

Examples of suitable cellulolytic enzyme composition can be found in WO 2008/151079 and WO 2013/028928 which are incorporated by reference.

In preferred embodiments the cellulolytic enzyme composition is derived from a strain of Trichoderma, Humicola, or Chrysosporium. In one embodiment, the cellulolytic enzyme composition is derived from a strain of Trichoderma reesei, Humicola insolens and/or Chrysosporium lucknowense.

In one embodiment, the cellulolytic enzyme composition comprises a beta- glucosidase, e.g., one derived from a strain of the genus Aspergillus, such as Aspergillus oryzae, such as the one disclosed in WO 2002/095014 or the fusion protein having beta- glucosidase activity disclosed in WO 2008/057637, or Aspergillus fumigatus, such as one disclosed in WO 2005/047499 (SEQ ID NO: 29 herein) or an Aspergillus fumigatus beta- glucosidase variant disclosed in WO 2012/044915 (Novozymes), such as one with the following substitutions: F100D, S283G, N456E, F512Y (using SEQ ID NO: 29 herein for numbering); or a strain of the genus a strain Penicillium, such as a strain of the Penicillium brasilianum disclosed in WO 2007/019442, or a strain of the genus Trichoderma, such as a strain of Trichoderma reesei.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity such as one derived from the genus Thermoascus, such as a strain of Thermoascus aurantiacus, such as the one described in WO 2005/074656 as SEQ ID NO: 2 and SEQ ID NO: 30 herein; or one derived from the genus Thielavia, such as a strain of Thielavia terrestris, such as the one described in WO 2005/074647 as SEQ ID NO: 7 and SEQ ID NO: 8; or one derived from a strain of Aspergillus, such as a strain of Aspergillus fumigatus, such as the one described in WO 2010/138754 as

SEQ ID NO: 1 and SEQ ID NO: 2; or one derived from a strain derived from Penicillium, such as a strain of Penicillium emersonii, such as the one disclosed in WO 201 1/041397 as SEQ ID NO: 2 or SEQ ID NO: 31 herein.

In one embodiment, the cellulolytic enzyme composition comprises a cellobiohydrolase I (CBH I), such as one derived from a strain of the genus Aspergillus, such as a strain of Aspergillus fumigatus, such as the Cel7a CBH I disclosed in SEQ ID NO: 2 in WO 2013/028928 or SEQ ID NO: 32 herein, or a strain of the genus Trichoderma, such as a strain of Trichoderma reesei.

In one embodiment, the cellulolytic enzyme composition comprises a cellobiohydrolase II (CBH II, such as one derived from a strain of the genus Aspergillus, such as a strain of Aspergillus fumigatus, such as the one disclosed as SEQ ID NO: 4 in WO 2013/028928 or SEQ ID NO: 33 herein); or a strain of the genus Trichoderma, such as Trichoderma reesei, or a strain of the genus Thielavia, such as a strain of Thielavia terrestris, such as cellobiohydrolase II CEL6A from Thielavia terrestris.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity and a beta-glucosidase.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity, a beta-glucosidase, and a CBH I. In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity, a beta-glucosidase, a CBH I, and a CBH II.

In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic enzyme composition, further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein), and Aspergillus oryzae beta-glucosidase fusion protein (WO 2008/057637).

In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic enzyme composition, further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein) and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 29 herein).

In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic enzyme composition further comprising Penicillium emersonii GH61A polypeptide having cellulolytic enhancing activity disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 29 herein) or a variant thereof with the following substitutions F100D, S283G, N456E, F512Y (using SEQ ID NO; 29 for numbering).

In one embodiment, the cellulolytic enzyme composition comprising one or more of the following components:

(i) an Aspergillus fumigatus cellobiohydrolase I;

(ii) an Aspergillus fumigatus cellobiohydrolase II;

(iii) an Aspergillus fumigatus beta-glucosidase or variant thereof; and

(iv) a Penicillium sp. GH61 polypeptide having cellulolytic enhancing activity; or homologs thereof.

In one embodiment, the cellulolytic enzyme composition is derived from Trichoderma reesei comprising GH61A polypeptide having cellulolytic enhancing activity derived from a strain of Penicillium emersonii (SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein, Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 in WO 2005/047499 or SEQ ID NO: 29 herein) variant with the following substitutions: F100D, S283G, N456E, F512Y) disclosed in WO 2012/044915; Aspergillus fumigatus Cel7A CBH1 disclosed as SEQ ID NO: 6 in WO2011/057140 or SEQ ID NO: 32 herein and Aspergillus fumigatus CBH II disclosed as SEQ ID NO: 18 in WO 2011/057140 or SEQ ID NO: 33 herein.

In one embodiment, the cellulolytic enzyme composition is dosed from 0.0001-3 mg EP/g DS, preferably, 0.0005-2 mg EP/g DS, preferably 0.001-1 mg/g DS, more preferably 0.005-0.5 mg EP/g DS, and even more preferably 0.01-0.1 mg EP/g DS.

Examples of Preferred Processes In one embodiment, is a process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus (e.g., SEQ ID NO: 1 herein);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cere visiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038; or

(2) Saccharomyces cere visiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, a protease is added in saccharification and/or fermentation or

SSF.

In one embodiment, is processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution; (using SEC ID NO: 1 for numbering);

ii) saccharifying using a glucoamylase, e.g., one derived from a strain of Gloephyllum, such as Gloephyllum serpiarium or Gloephyllum trabeum ;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cere visiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(1) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus (e.g., SEQ ID NO:

1);

a protease having a thermostability value of more than 20% determined as

Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or

Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012. In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase, preferably derived from Bacillus stearothermophilus, in particular one comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution (using SEQ ID NO: 1 for numbering) and having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C:

an alpha-amylase, preferably derived from Bacillus stearothermophilus, in particular one having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

a protease, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus, having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C;

optionally a Penicillium oxalicum glucoamylase

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism; wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S:

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

ii) saccharifying using a glucoamylase, such as one from a strain of Gloephyllum, such as a strain of Gloeophyllum serpiarium ;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F, and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S:

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase; iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F, and further optionally one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering),

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F; K79V +P2N + P4S + P1 1 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cere visiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cere visiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F;

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ; and

optionally a pullulanase;

a Penicillium oxalicum glucoamylase having a K79V substilution (using SEC ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is: (1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase, preferably derived from Bacillus stearothermophilus, having a T½

(min) at pH 4.5, 85°C, 0.12 mM CaCL of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus, preferably A. niger, A. awamori, or A. oryzae ; or a strain of Trichoderma, preferably T. reesel·, or a strain of Talaromyces, preferably T. emersonii, or a strain of Pycnoporus, or a strain of Gloeophyllum, such as G. serpiarium or G. trabeum, or a strain of the Nigrofomes;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using; an alpha-amylase, preferably derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F and having a T ½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

optionally a pullulanase;

a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature a temperature between 80-

90°C using; an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS; and optionally a pullulanase;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cere visiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012. In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optional substitution N193F; and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

optionally a pullulanase; and

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus] or a strain of Trichoderma; a strain of Talaromyces, a strain of Pycnoporus] a strain of Gloeophyllum; and a strain of the Nigrofomes; iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or (2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

a protease derived from Pyrococcus furiosus, preferably the one shown in SEQ ID NO: 13 herein;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is: (1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a process comprises the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

a protease derived from Pyrococcus furiosus, preferably the one shown in SEQ ID NO: 13 herein present and/or added in a dosage of 1-5 micro gram protease per gram DS, such as about 1.5 or 3 micro gram protease per gram DS; and

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501 V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501 V + Y504T; and K79V +P1 1 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is:

(1) Saccharomyces cere visiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one embodiment, is a processes for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus ; ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein.

Raw Starch Hydrolysis Process

This aspect concerns improved raw starch hydrolysis processes for producing ethanol using a fermenting organism and yeast strains suitable for use in processes and methods thereof.

More specifically, this aspect relates to processes of producing ethanol from starch- containing material, such as granular starch, comprising: (i) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain Saccharomyces strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase.

In one aspect is a processes of producing ethanol from starch-containing material, such as granular starch, comprising:

(i) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of the following enzymes: glucoamylase and alpha-amylase, and optionally protease; and

the fermenting organism is a Saccharomyces yeast strain providing one or more, such as all, of the following improvements:

an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., conditions as described herein); reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein).

In one embodiment, the fermenting organism used in a process is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA), or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA). In one embodiment, the fermenting organism used in a process is a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 that expresses a glucoamylase and/or an alpha-amylase.

A raw starch chydrolysis process using the yeast described herein results in one or more, such as all, of the following improvements compared to a corresponding process carried out under the same conditions using Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) as the fermenting organism:

an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., conditions as described herein); reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein).

Examples of suitable enzymes used, especially glucoamylases, alpha-amylases, proteases, cellulolytic enzyme compositions etc are described in the“Enzymes And Enzyme Blends Used In A Raw Starch Hydrolysis Process” section below. In one embodiment, the following enzymes are expressed, present and/or added in saccharification and/or fermentation: Trametes cingulata glucoamylase, e.g., the one shown in SEQ ID NO: 20 herein and an alpha-amylase. In one embodiment, the alpha-amylase is a Rhizomucor pusillus alpha-amylase, preferably the Rhizomucor pusillus alpha-amylase with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with Aspergillus niger glucoamylase linker and starch-binding domain shown in SEQ ID NO: 16 herein.

In one embodiment, the following enzymes are expressed, present and/or added in saccharification and/or fermentation: Gloeophyllum trabeum glucoamylase, e.g., the one shown in SEQ ID NO: 17 herein, especially one further having one or more of the following substitutions: S95P, A121 P, especially S95P+A121 P and an alpha-amylase. In one embodiment, the alpha-amylase is derived from Rhizomucor pusillus, e.g., Rhizomucor pusillus alpha-amylase with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch binding domain (SBD) disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment of the process the following enzymes are expressed, present and/or added in saccharification and/or fermentation: Gloeophyllum trabeum glucoamylase, preferably the one shown in SEQ ID NO: 17 herein, preferably one further having one or more of the following substitutions: S95P, A121 P, especially S95P+A121 P and an alpha-amylase. The alpha-amylase may be derived from Rhizomucor pusillus, preferably Rhizomucor pusillus alpha-amylase with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with Aspergillus niger glucoamylase linker and starch-binding domain (SBD) shown in SEQ ID NO: 16 herein, preferably one further having one or more of the following substitutions: G128D, D143N, especially G128D+143N.

In one embodiment, the following enzymes are expressed, present and/or added in saccharification and/or fermentation: Pycnoporus sanguineus glucoamylase, preferably the one shown in SEQ ID NO: 18 herein and an alpha-amylase. In one embodiment, the alpha- amylase is derived from Rhizomucor pusillus, preferably with a linker and starch-binding domain (SBD), e.g., the Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein, such as one further having one or more of the following substitutions: G128D, D143N (e.g., G128D+D143N).

In one embodiment, a protease is present and/or added in saccharification and/or fermentation. In one embodiment, the protease is a metallo protease or a serine protease. In one embodiment, the metallo protease is derived from a strain of the genus Thermoascus, such as a strain of Thermoascus aurantiacus, e.g., Thermoascus aurantiacus CGMCC No. 0670 (e.g., the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature polypeptide of SEQ ID NO: 3 herein).

In one embodiment, a cellulolytic enzyme composition is present and/or added in saccharification and/or fermentation.

In one embodiment, the cellulolytic enzyme composition is derived from Trichoderma reesei, preferably further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (e.g., SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein) and Aspergillus fumigatus beta-glucosidase (e.g., SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 29 herein), or a cellulolytic enzyme composition derived from Trichoderma reesei, preferably further comprising Penicillium emersonii GH61A polypeptide, e.g., the one disclosed as SEQ ID NO: 2 in WO 201 1/041397 or SEQ ID NO: 31 herein, and Aspergillus fumigatus beta-glucosidase, e.g., the one disclosed as SEQ ID NO: 2 in WO 2005/047499 or SEQ I D NO: 29 herein, or a variant thereof, such as a variant having one of, or all of, the following substitutions: F100D, S283G, N456E, F512Y, Aspergillus fumigatus CBH1 , e.g., the one disclosed as SEQ ID NO: 6 in WO2011/057140 and SEQ ID NO: 32 herein, and Aspergillus fumigatus CBH II, e.g., the one disclosed as SEQ ID NO: 18 in WO 201 1/057140 and as SEQ ID NO: 33 herein.

In one embodiment, the glucoamylase to alpha-amylase ratio is between 99: 1 and 1 :2, such as between 98:2 and 1 : 1 , such as between 97:3 and 2: 1 , such as between 96:4 and 3: 1 , such as 97:3, 96:4, 95:5, 94:6, 93:7, 90: 10, 85: 15, 83: 17 or 65:35 (mg EP glucoamylase: mg EP alpha-amylase).

In one embodiment, the glucoamylase to alpha-amylase ratio is between 100: 1 and 1 :2, such as between 90:1 and 1 : 1 , such as between 80: 1 and 2: 1 , such as between 70: 1 and 3: 1 , such as 16: 1 (determined as AGU: FAU-F).

In one embodiment, the total dose of glucoamylase and alpha-amylase is from 10- 1 ,000 pg/g DS, such as from 50-500 pg/g DS, such as 75-250 pg/g DS.

In one embodiment, the total dose of cellulolytic enzyme composition added is from 10-500 pg/g DS, such as from 20-400 pg/g DS, such as 20-300 pg/g DS.

In one embodiment, the dose of protease added is from 1-200 pg/g DS, such as from 2-100 pg/g DS, such as 3-50 pg/g DS.

In one embodiment, saccharification step (a) and fermentation step (b) are carried out simultaneously.

In one embodiment, the fermenting organism is a non-recombinant Saccharomyces strain, e.g., a non-recombinant Saccharomyces cerevisiae strain produced using the method described and concerned in US patent no. 8,257,959-BB.

Enzymes And Enzyme Blends Used In A Raw Starch Hydrolysis Process Glucoamylase and an alpha-amylase may be present and/or added in saccharification step (i) and/or fermentation step (ii) (e.g., simultaneous saccharification and fermentation (SSF)). Optionally a protease and/or a cellulolytic enzyme composition is(are) also present and/or added. Other enzymes such as pullulanases, pectinases, and/or trehalases may also be present and/or added.

A non-exhaustive list of suitable and specifically contemplated enzymes and enzyme combinations (e.g., blends) are described below.

In one embodiment, the following enzymes are present and/or added during saccharification and/or fermentation: Trametes glucoamylase, preferably Trametes cingulata glucoamylase shown in SEQ ID NO: 20 herein and an alpha-amylase.

In one embodiment, the glucoamylase is derived from Trametes cingulata, such as the one shown in SEQ ID NO: 20 herein, or a glucoamylase selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 20 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 20 herein.

In one embodiment, the following enzymes are present and/or added during saccharification and/or fermentation: Gloeophyllum glucoamylase, preferably Gloeophyllum trabeum glucoamylase, especially the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 herein and an alpha-amylase.

In one embodiment, the glucoamylase is derived from Gloeophyllum trabeum, such as the one shown in SEQ ID NO: 17 herein, or a glucoamylase selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 17 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 17 herein.

In one embodiment, the Gloeophyllum glucoamylase, such as the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17, has one of the following substitutions: V59A; S95P; A121 P; T119W; S95P+A121 P; V59A+S95P; S95P+T119W; V59A+S95P+A121 P; or S95P+T 119W+A121 P, especially S95P+A121 P (using SEQ ID NO: 17 for numbering).

The alpha-amylase used in a process described herein is typically a fungal alpha- amylase, such as an acid fungal alpha-amylase. In one embodiment, the alpha-amylase is derived from Rhizomucor, such as a Rhizomucor pusillus alpha-amylase with a linker and starch-binding domain (SBD), e.g., the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment, the alpha-amylase is a Rhizomucor alpha-amylase or the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch binding domain (SBD) shown in SEQ ID NO: 16 herein, e.g., one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N (using SEQ ID NO: 16 for numbering).

In one embodiment, the alpha-amylase is selected from the group consisting of:

(i) an alpha-amylase comprising the mature polypeptide of SEQ ID NO: 16 herein;

(ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 16 herein.

In one embodiment, the following enzymes are present and/or added in saccharification and/or fermentation: the Trametes cingulata glucoamylase shown in SEQ ID NO: 20 herein and an alpha-amylase derived from Rhizomucor pusillus, preferably with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment, the following enzymes are present and/or added in saccharification and/or fermentation: Gloeophyllum glucoamylase, preferably the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 herein and an alpha-amylase derived from Rhizomucor pusillus, preferably with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) disclosed as V039 in Table 5 in WO 2006/069290 or SEQ ID NO: 16 herein.

In one embodiment, the enzymes present and/or added comprises the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 herein having one or more of the following substitutions: S95P, A121 P, especially S95P+A121 P (using SEQ ID NO: 17 herein for numbering) and the alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), preferably one shown in SEQ ID NO: 16 herein, preferably one having one or more of the following substitutions: G128D, D143N, especially especially G128D+D143N (using SEQ ID NO: 16 for numbering).

In one embodiment, the following enzymes are present and/or added in saccharification and/or fermentation: Pycnoporus glucoamylase, in particular the Pycnoporus sanguineus glucoamylase shown in SEQ ID NO: 18 and the Rhizomucor pusillus alpha- amylase with a linker and starch-binding domain (SBD), in particular the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) shown in SEQ ID NO: 16 herein.

In one embodiment, the enzymes present and/or added in saccharification and/or fermentation comprises a Pycnoporus glucoamylase, such as the Pycnoporus sanguineus glucoamylase shown in SEQ ID NO: 18 herein and the alpha-amylase, in particular an alpha- amylase derived from Rhizomucor pusillus with a linker and starch-binding domain (SBD), preferably the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, especially G128D+D143N.

The enzymes present and/or added in saccharification and/or fermentation in a process described herein include i) glucoamylase and ii) alpha-amylase; and may optionally further comprise iii) a cellulolytic enzyme composition and/or iv) a protease.

In one embodiment, the protease is a metallo protease, preferably derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially Thermoascus aurantiacus CGMCC No. 0670, such as the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature polypeptide of SEQ ID NO: 3 herein.

In one embodiment, the protease, in particular a protease derived from Thermoascus aurantiacus, is selected from the group consisting of:

(i) a protease comprising the mature polypeptide of SEQ ID NO: 3 herein;

(ii) a protease comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 3 herein.

In one embodiment, the enzymes present and/or added in saccharification and/or fermentation comprises the Trametes cingulata glucoamylase shown in SEQ ID NO: 20 herein and the alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), such as the one shown in SEQ ID NO: 16 herein, and may have one or more of the following substitutions: G128D, D143N (e.g., G128D+D143N) and optionally further a cellulolytic enzyme composition derived from Trichoderma reesei, e.g., further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein) and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ I D NO: 29 herein); or a cellulolytic enzyme composition derived from Trichoderma reesei, e.g., further comprising Penicillium emersonii GH61A polypeptide disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein and Aspergillus fumigatus beta-glucosidase disclosed as SEQ I D NO: 2 in WO 2005/047499 or SEQ I D NO: 29 herein, or a variant thereof, e.g., a variant having one of, preferably all of, the following substitutions: F100D, S283G, N456E, F512Y, Aspergillus fumigatus Cel7A CBH1 disclosed as SEQ ID NO: 6 in WO201 1/057140 and SEQ ID NO: 32 herein and Aspergillus fumigatus CBH II disclosed as SEQ ID NO: 18 in WO 2011/057140 and as SEQ ID NO: 33 herein.

In one embodiment the enzymes present and/or added in saccharification and/or fermentation comprises the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 herein, preferably having one or more of the following substitutions: S95P, A121 P, especially S95P+A121 P and the alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), preferably the one shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, especially G128D+D143N, and optionally further a cellulolytic enzyme composition derived from Trichoderma reesei, preferably further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein) and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 29 herein); or a cellulolytic enzyme composition derived from Trichoderma reesei, preferably further comprising Penicillium emersonii GH61A polypeptide disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein and Aspergillus fumigatus beta-glucosidase disclosed as SEQ ID NO: 2 in WO 2005/047499 or SEQ ID NO: 29 herein, or a variant thereof, preferably a variant having one of, preferably all of, the following substitutions: F100D, S283G, N456E, F512Y, Aspergillus fumigatus Cel7A CBH1 disclosed as SEQ ID NO: 6 in WO201 1/057140 and SEQ ID NO: 32 herein and Aspergillus fumigatus CBH II disclosed as SEQ ID NO: 18 in WO 201 1/057140 and as SEQ ID NO: 33 herein.

In one embodiment the enzymes present and/or added in saccharification and/or fermentation comprises the Pycnoporus sanguineus glucoamylase shown in SEQ ID NO: 18 herein and the alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), preferably the one shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, especially G128D+D143N, and optionally further a cellulolytic enzyme composition derived from Trichoderma reesei, preferably further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: herein) and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 30 herein); or a cellulolytic enzyme composition derived from Trichoderma reesei, preferably further comprising Penicillium emersonii GH61A polypeptide disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein and Aspergillus fumigatus beta-glucosidase disclosed as SEQ ID NO: 2 in WO 2005/047499 or SEQ ID NO: 29 herein, or a variant thereof, preferably a variant having one of, preferably all of, the following substitutions: F100D, S283G, N456E, F512Y, Aspergillus fumigatus Cel7A CBH I disclosed as SEQ ID NO: 6 in WO201 1/057140 and SEQ ID NO: 29 herein and Aspergillus fumigatus CBH II disclosed as SEQ ID NO: 18 in WO 201 1/057140 and as SEQ ID NO: 33 herein.

In one embodiment, a cellulolytic enzyme composition is one described below in the “Cellulolytic Enzyme Compositions”-section.

The optional cellulolytic enzyme composition, protease or other enzymes, may be added in the process described herein at the same time as the glucoamylase and the alpha- amylase. The enzymes, e.g., in the form of an enzyme composition, may be added to the saccharification and/or fermentation, preferably simultaneous saccharification and fermentation (i.e., one-step process). It should be understood that the enzymes may also be added individually or as two, three, four or more enzyme components/compositions. In one embodiment, the glucoamylase and the alpha-amylase are added as one blend composition and the optional cellulolytic enzyme composition and/and optional protease are added separately. In another embodiment the glucoamylase, the alpha-amylase, and the cellulolytic enzyme composition are added as one enzyme composition and the optional protease is added separately. All enzymes may also in one embodiment be added as one enzyme composition comprising a glucoamylase, an alpha-amylase, a cellulolytic enzyme composition and/or a protease, and optionally other enzymes including pullulanase, trehalase and/or pectinase, such as pectin lyase or polygalacturonase.

Other enzymes may also be present. Specifically contemplated enzymes are described further below.

The glucoamylase used in a process described herein may be of any origin, such as of bacterial or fungal origin. Fungal glucoamylases are preferred.

In one embodiment, the glucoamylase may be one derived from a strain of Trametes, such as a strain of Trametes cingulata (SEQ ID NO: 20 herein); or a strain of Pachykytospora, such as a strain of Pachykytospora papyracea\ or a strain of Leucopaxillus, such as a strain of Leucopaxillus giganteus (all disclosed in WO 2006/069289).

In one embodiment, the glucoamylase, in particular derived from a strain of Trametes cingulata, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 20 herein; (ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 20 herein.

In one embodiment, the glucoamylase is from a strain of Aspergillus, preferably Aspergillus niger, Aspergillus awamori, or Aspergillus oryzae ; or a strain of Trichoderma, preferably Trichoderma reesel·, or a strain of Talaromyces, preferably Talaromyces emersonii (e.g., SEQ ID NO: 19 herein).

In one embodiment, the glucoamylase, such as one derived from a strain of Talaromyces emersonii, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 19 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 19 herein.

In another embodiment the glucoamylase is derived from a strain of Penicillium, such as a strain of Penicillium oxalicum.

In one embodiment, the glucoamylase, such as one derived from a strain of Penicillium oxalicum, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 14 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 14 herein.

In one embodiment, the glucoamylase is derived from a strain of Gloeophyllum, such as a strain of Gloeophyllum sepiarium or Gloeophyllum trabeum, such as one disclosed in WO 2011/068803 as any of SEQ ID NOs: 2, 4, 6, 8, 10, 12, 14 or 16. In one embodiment, the glucoamylase is SEQ ID NO: 2 in WO 2011/068803 or SEQ ID NO: 15 herein. In another embodiment the glucoamylase is SEQ ID NO: 18 in WO 2011/068803 (hereby incorporated by reference).

In one embodiment, the glucoamylase, such as one derived from a strain of Gloeophyllum sepiarium, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 15 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 15 herein. In a further embodiment the glucoamylase is derived from a strain of the genus Pycnoporus, in particular a strain of Pycnoporus sanguineus, such as a strain described in WO 201 1/066576 (SEQ ID NOs 2, 4 or 6). In one embodiment, the glucoamylase is the one shown in SEQ ID NO: 4 in WO 2011/066576 or SEQ ID NO: 18 herein.

In one embodiment, the glucoamylase, such as one derived from a strain of Pycnoporus sanguineus, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ I D NO: 18 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 18 herein.

Contemplated are also glucoamylases which exhibit a high identity to any of the above- mentioned glucoamylases, e.g., at least 60%, at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, such as 100% identity to any one of the mature parts of the enzyme sequences mentioned above.

In one embodiment, the glucoamylase, such as one derived from a strain of Gloeophyllum trabeum, is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 17 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 17 herein.

In one embodiment, the glucoamylase, such as the one derived from Gloeophyllum trabeum, shown in SEQ ID NO: 17 has one of the following substitutions: V59A; S95P; A121 P; T119W; S95P+A121 P; V59A+S95P; S95P+T119W; V59A+S95P+A121 P; or

S95P+T119W+A121 P, especially S95P+A121 P. In one embodiment, the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 18 has one of the following substitutions: V59A; S95P; A121 P; T119W; S95P+A121 P; V59A+S95P; S95P+T1 19W; V59A+S95P+A121 P; or S95P+T119W+A121 P, especially S95P+A121 P (using SEQ ID NO: 17 herein for numbering). All Gloeophyllum trabeum glucoamylase variants, especially variants in SEQ ID NO: 3, disclosed in WO 2014/177546 is hereby incorporated by reference.

A glucoamylase variant may comprise an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99%, but less than 100% sequence identity to the mature polypeptide of SEQ ID NO: 17. Alpha-Amylase The alpha-amylase used in a process described herein may be of any origin, such as of fungal or bacterial origin. In one embodiment, the alpha-amylase is an acid alpha-amylase, such as an acid fungal alpha-amylase, i.e. , having a pH optimum below pH 7.

In one embodiment, the alpha-amylase may be derived from a strain of the genus Rhizomucor, preferably a strain the Rhizomucor pusillus, such as the one shown in SEQ ID NO: 3 in WO 2013/006756 (see e.g., Table 1 in Example 1 - hereby incorporated by reference), or the genus Meripilus, preferably a strain of Meripilus giganteus.

In one embodiment, the alpha-amylase is derived from a Rhizomucor pusillus, such as one with a linker and a starch-binding domain (SBD), preferably Aspergillus niger glucoamylase linker and starch-binding domain (SBD), disclosed as V039 in Table 5 in WO 2006/069290 (incorporated by reference) or SEQ ID NO: 16 herein.

In one embodiment, the alpha-amylase is derived from a Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), disclosed in WO 2013/006756 (incorporated by reference) or SEQ ID NO: 16 herein.

In one embodiment, the Rhizomucor pusillus alpha-amylase or the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) has at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N (using SEQ ID NO: 16 herein for numbering).

In one embodiment, the Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), is selected from the group consisting of:

(i) an alpha-amylase comprising the mature polypeptide of SEQ ID NO: 16 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 16 herein.

In one embodiment, the alpha-amylase is a variant of the Rhizomucor pusillus alpha- amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), wherein the alpha-amylase variant comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity, but less than 100% to the mature polypeptide of SEQ ID NO: 16 herein.

In one embodiment, the alpha-amylase variant has one of the above mentioned substitutions, such as: G128D, Y141W, D143W or K192R (using SEQ ID NO: 16 for numbering).

In one embodiment, the alpha-amylase (using SEQ ID NO: 16 herein for numbering) has the following substitutions: Y141W+D143N.

In one embodiment, the alpha-amylase has the following substitutions:

G128D+Y141W+D143N.

In one embodiment, the alpha-amylase has the following substitutions:

G128D+Y141W+D143N+K192R;

In one embodiment, the alpha-amylase has the following substitutions: G128D+D143N (using SEQ ID NO: 16 for numbering).

A variant may comprise an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99%, but less than 100% sequence identity to the mature polypeptide of SEQ ID NO: 16.

Protease

The enzymes present and/or added to saccharification and/or fermentation may optionally further include a protease. The protease may be of any origin, such as fungal or bacterial origin.

In one embodiment, the protease is of fungal origin.

In one embodiment, the protease is a metallo protease derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially Thermoascus aurantiacus CGMCC No. 0670, such as the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature polypeptide of SEQ ID NO: 3 herein.

In one embodiment, the protease, such as one derived from a strain of Thermoascus aurantiacus, is selected from the group consisting of:

(i) a protease comprising the mature polypeptide of SEQ ID NO: 3 herein;

(ii) a protease comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 3 herein.

In one embodiment, the protease is of bacterial origin. In one embodiment, the protease is derived from a strain of Pyrococcus, such as a strain of Pyrococcus furiosus, such as the protease shown in SEQ ID NO: 1 in US 6,358,726 or SEQ ID NO: 5 herein.

In one embodiment, the protease, such as one derived from Pyrococcus furiosus, is selected from the group consisting of:

(i) a protease comprising the mature polypeptide of SEQ ID NO: 5 herein;

(ii) a protease comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 5 herein.

The enzymes present and/or added to saccharification and/or fermentation may optionally further include a cellulolytic enzyme composition. The cellulolytic enzyme composition may consist of or comprise one or more cellulolytic enzymes. The cellulolytic enzyme composition may be of any origin. In one embodiment, the cellulolytic enzyme composition comprises cellulolytic enzymes of fungal origin.

In one embodiment, the cellulolytic enzyme composition is derived from a strain of Trichoderma, such as Trichoderma reesel·, or a strain of Humicola, such as Humicola insolens; or a strain of Chrysosporium, such as Chrysosporium lucknowense ; or a strain of Penicillium, such as Penicillium decumbens. In one embodiment, the cellulolytic enzyme composition is derived from a strain of Trichoderma reesei.

The cellulolytic enzyme composition may comprise a beta-glucosidase, a cellobiohydrolase, and an endoglucanase.

In one embodiment, the cellulolytic enzyme composition comprising one or more polypeptides selected from the group consisting of:

beta-glucosidase (BG);

cellobiohydrolase I (CBHI);

cellobiohydrolase II (CBHI I);

or a mixture thereof.

In one embodiment, the cellulolytic enzyme composition further comprises a GH61 polypeptide having cellulolytic enhancing activity. Cellulolytic enhancing activity is defined and determined as described in WO 201 1/041397 (incorporated by reference).

The term “GH61 polypeptide having cellulolytic enhancing activity” means a GH61 polypeptide that enhances the hydrolysis of a cellulosic material by enzymes having cellulolytic activity. For purposes of the processes described herein, cellulolytic enhancing activity is determined by measuring the increase in reducing sugars or the increase of the total of cellobiose and glucose from hydrolysis of a cellulosic material by cellulolytic enzyme under the following conditions: 1-50 mg of total protein/g of cellulose in PCS (Pretreated Corn Stover), wherein total protein is comprised of 50-99.5% w/w cellulolytic enzyme protein and 0.5-50% w/w protein of a GH61 polypeptide having cellulolytic enhancing activity for 1-7 days at 50°C compared to a control hydrolysis with equal total protein loading without cellulolytic enhancing activity (1-50 mg of cellulolytic protein/g of cellulose in PCS). In a preferred aspect, a mixture of CELLUCLAST™1.5L (Novozymes A/S, Bagsvasrd, Denmark) in the presence of 2-3% of total protein weight Aspergillus oryzae beta-glucosidase (recombinantly produced in Aspergillus oryzae according to WO 02/095014) or 2-3% of total protein weight Aspergillus fumigatus beta-glucosidase (recombinantly produced in Aspergillus oryzae as described in WO 2002/095014) of cellulase protein loading is used as the source of the cellulolytic activity.

The cellulolytic enzyme composition comprises a beta-glucosidase, preferably one derived from a strain of the genus Aspergillus, such as Aspergillus oryzae, such as the one disclosed in WO 2002/095014 or the fusion protein having beta-glucosidase activity disclosed in WO 2008/057637 (see SEQ ID NOs: 74 or 76), or Aspergillus fumigatus, such as one disclosed in SEQ ID NO: 2 in WO 2005/047499 or SEQ ID NO: 8 herein; or an Aspergillus fumigatus beta-glucosidase variant disclosed in WO 2012/044915; or a strain of the genus a strain Penicillium, such as a strain of the Penicillium brasilianum disclosed in WO 2007/019442, or a strain of the genus Trichoderma, such as a strain of Trichoderma reesei. In one embodiment, the beta-glucosidase is from a strain of Aspergillus, such as a strain of Aspergillus fumigatus, such as Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 29 herein), or a variant thereof, which variant comprises one or more substitutions selected from the group consisting of L89M, G91 L, F100D, 1140V, 1186V, S283G, N456E, and F512Y; such as a variant thereof with the following substitutions:

F100D + S283G + N456E + F512Y;

L89M + G91 L + 1186V + 1140V;

1186V + L89M + G91 L + 1140V + F100D + S283G + N456E + F512Y.

In one embodiment, the parent beta-glucosidase has at least 60% identity, such as at least 70%, such as at least 80%, such as at least 90%, such as at least 95%, such as at least 96%, such as at least 97%, such as at least 98%, such as at least 99% identity to the mature polypeptide of SEQ ID NO: 29 herein.

In case the beta-glucosidase is a beta-glucosidase variant it has at least 60% identity, such as at least 70%, such as at least 80%, such as at least 90%, such as at least 95%, such as at least 96%, such as at least 97%, such as at least 98%, such as at least 99%, but less than 100% identity to the mature polypeptide of SEQ ID NO:29 herein.

In case the cellulolytic enzyme composition comprises a GH61 polypeptide, it may be one derived from the genus Thermoascus, such as a strain of Thermoascus aurantiacus, such as the one described in WO 2005/074656 as SEQ ID NO: 2 or SEQ ID NO: 30 herein; or one derived from the genus Thielavia, such as a strain of Thielavia terrestris, such as the one described in WO 2005/074647 as SEQ ID NO: 7 and SEQ ID NO: 8 (hereby incorporated by reference); or one derived from a strain of Aspergillus, such as a strain of Aspergillus fumigatus, such as the one described in WO 2010/138754 as SEQ ID NO: 1 and SEQ ID NO: 2 (hereby incorporated by reference); or one derived from a strain from Penicillium, such as a strain of Penicillium emersonii, such as the one disclosed in WO 2011/041397 as SEQ ID NO: 2 or SEQ ID NO: 31 herein.

In one embodiment, the GH61 polypeptide, such as one derived from a strain of Thermoascus, is selected from the group consisting of:

(i) a GH61 polypeptide comprising the mature polypeptide of SEQ ID NO: 30 herein;

(ii) a GH61 polypeptide comprising an amino acid sequence having at least 60%, such as at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 30 herein.

In one embodiment, the GH61 polypeptide, such as one derived from a strain of Penicillium sp., is selected from the group consisting of:

(i) a GH61 polypeptide comprising the mature polypeptide of SEQ ID NO: 31 herein;

(ii) a GH61 polypeptide comprising an amino acid sequence having at least 60%, such as at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 31 herein.

In one embodiment, the cellulolytic enzyme composition comprises a cellobiohydrolase I (CBH I), such as one derived from a strain of the genus Aspergillus, such as a strain of Aspergillus fumigatus, such as the Cel7a CBH I disclosed as SEQ ID NO: 6 in WO 2011/057140 or SEQ ID NO: 32 herein, or a strain of the genus Trichoderma, such as a strain of Trichoderma reesei.

In one embodiment, the cellobiohydrolase I, such as one derived from a strain of Aspergillus fumigatus, is selected from the group consisting of:

(i) a cellobiohydrolase I comprising the mature polypeptide of SEQ ID NO: 32 herein;

(ii) a cellobiohydrolase I comprising an amino acid sequence having at least 60%, such as at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 32 herein. In one embodiment, the cellulolytic enzyme composition, comprised in an enzyme composition described herein, comprises a cellobiohydrolase II (CBH II), such as one derived from a strain of the genus Aspergillus, such as a strain of Aspergillus fumigatus ; such as the one disclosed as SEQ ID NO: 33 herein or a strain of the genus Trichoderma, such as Trichoderma reesei, or a strain of the genus Thielavia, such as a strain of Thielavia terrestris, such as cellobiohydrolase II CEL6A from Thielavia terrestris.

In one embodiment, cellobiohydrolase II, such as one derived from a strain of Aspergillus fumigatus, is selected from the group consisting of:

(i) a cellobiohydrolase II comprising the mature polypeptide of SEQ ID NO: 33 herein;

(ii) a cellobiohydrolase II comprising an amino acid sequence having at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 33 herein.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity and a beta-glucosidase.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity derived from a strain of Penicillium, such as a strain of Penicillium emersonii, such as the one disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein, and a beta-glucosidase.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity, a beta-glucosidase, and a CBH I.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity derived from a strain of Penicillium, such as a strain of Penicillium emersonii, such as the one disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein, a beta-glucosidase, and a CBHII.

In one embodiment, the cellulolytic enzyme composition, comprised in an enzyme composition described herein, comprises a GH61 polypeptide having cellulolytic enhancing activity, a beta-glucosidase, a CBH I, and a CBHII.

In one embodiment, the cellulolytic enzyme composition comprises a GH61 polypeptide having cellulolytic enhancing activity derived from a strain of Penicillium, such as a strain of Penicillium emersonii, such as the one disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein, a beta-glucosidase, a CBH I, and a CBH II.

In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic composition further comprising Thermoascus aurantiacus GH61A polypeptide (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein), and Aspergillus oryzae beta- glucosidase fusion protein (WO 2008/057637). In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic enzyme composition further comprising Thermoascus aurantiacus GH61A polypeptide having cellulolytic enhancing activity (SEQ ID NO: 2 in WO 2005/074656 or SEQ ID NO: 30 herein) and Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 2 of WO 2005/047499 or SEQ ID NO: 29 herein).

In one embodiment, the cellulolytic enzyme composition is a Trichoderma reesei cellulolytic composition further comprising Penicillium emerson/V GH61A polypeptide disclosed as SEQ ID NO: 2 in WO 2011/041397 or SEQ ID NO: 31 herein, and Aspergillus fumigatus beta-glucosidase disclosed as SEQ ID NO: 2 in WO 2005/047499 or SEQ ID NO: 29 herein, or a variant thereof, which variant has one of, preferably all of, the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I, e.g., the one disclosed as SEQ ID NO: 6 in WO201 1/057140 and SEQ ID NO: 32 herein and Aspergillus fumigatus CBH II, e.g., the one disclosed as SEQ ID NO: 18 in WO 2011/057140 and as SEQ ID NO: 33 herein.

In one embodiment, the cellulolytic enzyme composition comprises one or more of the following components

(i) an Aspergillus fumigatus cellobiohydrolase I;

(ii) an Aspergillus fumigatus cellobiohydrolase II;

(iii) an Aspergillus fumigatus beta-glucosidase or variant thereof.

In one embodiment, the Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 29 herein), comprises one or more substitutions selected from the group consisting of L89M, G91 L, F100D, 1140V, 1186V, S283G, N456E, and F512Y; such as a variant thereof, with one of the following substitutions or combinations of substitutions:

F100D + S283G + N456E + F512Y;

L89M + G91 L + 1186V + 1140V; and

1186V + L89M + G91 L + 1140V + F100D + S283G + N456E + F512Y (using SEQ ID NO: 29 for numbering).

In one embodiment, the cellulolytic enzyme composition further comprises the Penicillium sp. GH61 polypeptide shown in SEQ ID NO: 31 herein; or a GH61 polypeptide comprising an amino acid sequence having at least 60%, such as at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 31 herein.

Pullulanase

The enzymes present and/or added to saccharification and/or fermentation may optionally further include a pullulanase. The pullulanase may be of any origin, such as fungal or bacterial origin. In one embodiment, the pullulanase is derived from a strain of Bacillus sp. such as a strain of Bacillus deramificans.

Trehalase

The enzymes present and/or added to saccharification and/or fermentation may optionally further include a trehalase.

The trehalase may be of any origin, such as fungal or bacterial origin.

In one embodiment, the trehalase is of fungal origin, such as derived from a strain of Trichoderma, such as Trichoderma reesei.

Pectinase

The enzymes present and/or added to saccharification and/or fermentation may optionally further include a pectinase, such as a pectin lyase (also known as pectolyase) and/or a polygalacturonase, or a combination thereof.

The pectinase may be of any origin, such as fungal or bacterial origin.

In one embodiment, the pectinase is a pectin lyase (EC 4.2.2.10).

In one embodiment, the pectin lyase is derived from a strain of Aspergillus, such as Aspergillus niger.

In one embodiment, the pectinase is a polygalacturonase (EC. 3.2.1.15).

In one embodiment, the polygalacacturonase is derived from a strain of Aspergillus, such as Aspergillus aculeatus.

In one embodiment, the pectinase is a combination of pectin lyase and polygalacturonase. In one embodiment, the pectinase is a combination of pectin lyase derived from Aspergillus niger and polygalacturonase derived from Aspergillus aculeatus.

Examples of Enzymes (e.q.. Blend) Suitable for Use in a Raw Starch Hydrolysis Process

In one embodiment, enzymes (e.g., blend) for use in a process described herein comprise a glucoamylase and an alpha-amylase, and optionally a protease and/or cellulolytic enzyme composition. Other optional enzymes may also be used.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises or consists of a glucoamylase from Trametes cingulata (e.g., SEQ ID NO: 20) and an alpha-amylase from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), e.g., SEQ ID NO: 16.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises the Gloeophyllum trabeum glucoamylase (e.g., SEQ ID NO: 17 herein) having one or more of the following substitutions: S95P, A121 P, preferably S95P+A121 P and an alpha- amylase, preferably an alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, preferably G128D+D143N.

In another embodiment, the enzymes (e.g., blend) used in a process described herein comprises the Pycnoporus sanguineus glucoamylase shown in SEQ ID NO: 18 herein and an alpha-amylase, preferably one derived from Rhizomucor pusillus with a linker and starch binding domain (SBD), preferably Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), in particular the one shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, especially G128D+D143N.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises the Gloeophyllum sepiarium glucoamylase shown in SEQ ID NO: 15 herein and an alpha-amylase, preferably an alpha-amylase derived from Rhizomucor pusillus with a linker and starch-binding domain (SBD), preferably Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD)shown in SEQ ID NO: 16 herein, preferably having one or more of the following substitutions: G128D, D143N, preferably G128D+D143N.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises the Trametes cingulata glucoamylase shown in SEQ ID NO: 20 herein and an alpha-amylase, preferably an alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 16 herein, having one or more of the following substitutions: G128D, D143N, preferably G128D+D143N.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) fungal glucoamylase;

ii) fungal alpha-amylase;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising a GH61 polypeptide, beta-glucosidase, CBH I and CBH II;

iv) optionally a protease.

In one embodiment, the enzymes (blend) used in a process described herein comprises

i) Trametes cingulata glucoamylase;

ii) Rhizomucor pusillus alpha-amylase, or variant thereof;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II; iv) optionally a protease from Thermoascus aurantiacus , or variant thereof.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises a

i) Trametes cingulata glucoamylase;

ii) Rhizomucor pusillus alpha-amylase, or variant thereof;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

iv) optionally a protease from Pyropoccus furiosus.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises i) glucoamylase derived from Trametes cingulata ;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei ;

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof and/or Pyrococcus furiosus.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) fungal glucoamylase;

ii) fungal alpha-amylase;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising a GH61 polypeptide, beta-glucosidase CBH I and CBH II;

iv) pectinase, preferably a pectin lyase or a polygalacturonase, or a combination thereof.

In one embodiment, the pectinase is a combination of pectin lyase derived from Aspergillus niger and polygalacturonase derived from Aspergillus aculeatus.

In one embodiment, the pectinase is a combination of pectin lyase and polygalacturonase. In one embodiment, the pectinase is a combination of pectin lyase derived from Aspergillus niger and polygalacturonase derived from Aspergillus aculeatus.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) fungal glucoamylase;

ii) fungal alpha-amylase;

iii) pectinase, preferably a pectin lyase or a polygalacturonase, or a combination thereof; iv) cellulolytic enzyme composition derived from a strain of Trichoderma reesei , further comprising a GH61 polypeptide, beta-glucosidase CBH I and CBH II;

v) protease.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises a

i) fungal glucoamylase;

ii) fungal alpha-amylase;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising a GH61 polypeptide, beta-glucosidase, CBH I and CBH II;

iv) optionally a protease.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) Trametes cingulata glucoamylase;

ii) Rhizomucor pusillus alpha-amylase, or variant thereof;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

iv) pectin lyase derived from Aspergillus niger or polygalacturonase derived from Aspergillus aculeatus, or a combination thereof;

v) protease from Thermoascus aurantiacus, or a variant thereof and/or Pyrococcus furiosus.

In one embodiment, the enzymes (blend) used in a process described herein comprises

i) Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 18 herein having one or more of the following substitutions: S95P, A121 P, such as S95P+A121 P;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 13 herein, having of the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

optionally iv) protease from Thermoascus aurantiacus, or a variant thereof.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) Pycnoporus sanguineus glucoamylase shown in SEQ ID NO: 18 herein; ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 16 herein, having of the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

optionally iv) protease from Thermoascus aurantiacus, or a variant thereof.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) Gloeophyllum sepiarium glucoamylase shown in SEQ ID NO: 15 herein;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 16 herein, having of the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

optionally iv) protease from Thermoascus aurantiacus, or a variant thereof.

In one embodiment, the enzymes (e.g., blend) used in a process described herein comprises

i) Trametes cingulata glucoamylase shown in SEQ ID NO: 20 herein;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), shown in SEQ ID NO: 16 herein, having of the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from a strain of Trichoderma reesei, further comprising Penicillium emersonii GH61A polypeptide, Aspergillus fumigatus beta-glucosidase with the following substitutions: F100D, S283G, N456E, F512Y, and optionally Aspergillus fumigatus CBH I and Aspergillus fumigatus CBH II;

optionally iv) protease from Thermoascus aurantiacus, or a variant thereof.

Examples of Raw Starch Hydrolysis Processes

In one embodiment, a process of producing ethanol from starch-containing material comprises:

(i) saccharifying starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein saccharification and/or fermentation is done in the presence of the following enzymes: glucoamylase and alpha-amylase, and optionally protease and/or cellulolytic enzyme composition; and

the fermenting organism is a Saccharomyces yeast strain providing an ethanol yield boost compared to ETHANOL RED™ under the same fermentation conditions.

In one embodiment, the process provides one or more, such as all, of the following improvement:

an ethanol yield boost compared to ETHANOL RED™ under the same fermentation conditions (e.g., conditions as described herein);

reduced acetaldehyde production compared to ETHANOL RED™ under the same process conditions (e.g., conditions as described herein);

increased temperature tolerance compared to ETHANOL RED™ under the same process conditions (e.g., conditions as described herein);

decreased glycerol production compared to ETHANOL RED™ under the same process conditions (e.g., conditions as described herein). In one embodiment is a process for producing ethanol from starch-containing material comprising:

(i) saccharifying starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of the following enzymes: glucoamylase and alpha-amylase, and optionally protease and/or cellulolytic enzyme composition; and

the fermenting organism is a Saccharomyces yeast which provides one or more, such as all of the following improvements:

boosts ethanol yield;

reduces acetaldehyde production;

increased temperature tolerance; and

descreases glycose production.

In one embodiment, the process provides one or more, such as all, of the following improvement:

boosts the ethanol yield over ETHANOL RED™ (ER) of more than 0.5%, e.g., more than 1.0%, more than 2.0%, more than 2.5%, such as about 2.9%, such as between 0.5 and 5%, such as between 1-3%, under the same process conditions (e.g., conditions as described herein); reduces acetaldehyde production more than 10%, preferably more than 20%, more preferably more than 30%, even more preferably more than 40%, especially more than 45%, such as between 5-60%, such as 30-50%, compared to ETHANOL RED™ under the same process conditions (e.g., conditions as described herein);

increases temperature tolerance compared to ETHANOL RED™ under the same process conditions (e.g., conditions as described herein); and

decreases glycerol production by more than 3%, preferably more than 4%, more preferably more than 5%, even more preferably more than 6%, especially more than 7%, such as between 2-15%, such as 5-10%, compared to ETHANOL RED™ under the same process conditions, (e.g., conditions as described herein).

In one embodiment is a process of producing ethanol from starch-containing material comprises:

(i) saccharifying starch-containing material at a temperature below the initial gelatinization temperature; and

(ii) fermenting using a fermentation organism;

wherein saccharification and/or fermentation is done in the presence of the following enzymes: glucoamylase and alpha-amylase, and optionally protease; and

wherein the fermenting organism is:

(1) Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces cerevisiae strain MBG5038 having defining characteristics of Saccharomyces cerevisiae strain MBG5038; or

(2) Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces cerevisiae strain MBG5012 having defining characteristics of Saccharomyces cerevisiae strain MBG5012.

In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or Saccharomyces cerevisiae strain MBG5012 expresses a glucoamylase and/or an alpha- amylase.

In one embodiment, the process of producing ethanol from starch-containing material comprises: (a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(b) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of the following enzymes: i) glucoamylase derived from Trametes cingulata, Gloeophyllum trabeum, Gloeophyllum sepiarium, or Pycnoporus sanguineus ;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof;

iii) cellulolytic enzyme composition derived from Trichoderma reesel·,

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof and/or Pyrococcus furiosus; and

wherein

the fermenting organism is a Saccharomyces yeast strain providing one or more, such as all of the following improvements:

an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., conditions as described herein); reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein);

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions (e.g., conditions as described herein).

In one embodiment, the process of producing ethanol from starch-containing material comprises:

(a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(b) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of the following enzymes: i) glucoamylase derived from Gloeophyllum trabeum disclosed in SEQ ID NO: 17, with the following substitutions: S95P+A121 P;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof, shown in SEQ ID NO: 16 herein, with the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from Trichoderma reesel·,

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof; and wherein

the fermenting organism is a Saccharomyces yeast strain providing an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., provides an ethanol yield boost of at least 1.0%, at least 2.0%, at least 2.5%, such as between 0.5-5%, e.g., between 1-3% compared to ETHANOL RED® under the conditions described herein).

In one embodiment, the process of producing ethanol from starch containing material of comprises:

(a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(b) fermenting using a fermentation organism;

wherein saccharification and/or fermentation is done in the presence of the following enzymes: i) glucoamylase derived from Pycnoporus sanguineus shown in SEQ ID NO: 18; ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof, shown in SEQ ID NO: 16 herein, with the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from Trichoderma reesel·,

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof; and wherein the fermenting organism is a Saccharomyces yeast strain providing an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., provides an ethanol yield boost of at least 0.5%, at least 1.0%, at least 2.0%, at least 2.5%, such as between 0.5-5%, e.g., between 1-3% under the same conditions compared to ETHANOL RED®).

In one embodiment, the process of producing ethanol from starch-containing material of comprises:

(a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(b) fermenting using a fermentation organism; wherein saccharification and/or fermentation is done in the presence of the following enzymes: i) glucoamylase derived from Gloeophyllum sepiarium shown in SEQ ID NO: 15; ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof, shown in SEQ ID NO: 16 herein, with the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from Trichoderma reesei ;

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof;

wherein the fermenting organism is a Saccharomyces yeast strain providing an ethanol yield boost compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same fermentation conditions (e.g., provides an ethanol yield boost of at least 0.5%, at least 1.0%, at least 2.0%, at least 2.5%, such as between 0.5-5%, e.g., between 1-3% under the conditions defined in Example 18 compared to ETHANOL RED®).

In one embodiment, the process of producing ethanol from starch-containing material of comprises:

(a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature; and

(b) fermenting using a fermentation organism;

wherein saccharification and/or fermentation is done in the presence of the following enzymes: i) glucoamylase derived from Trametes cingulata shown in SEQ ID NO: 20;

ii) alpha-amylase derived from Rhizomucor pusillus with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD), or a variant thereof, shown in SEQ ID NO: 16 herein, with the following substitutions: G128D+D143N;

iii) cellulolytic enzyme composition derived from Trichoderma reesei ;

iv) optionally a protease from Thermoascus aurantiacus, or a variant thereof; and wherein the fermenting organism is a Saccharomyces yeast strain providing an ethanol yield boost compared to ETHANOL RED™ under the same fermentation conditions (e.g., provides an ethanol yield boost of at least 0.5%, at least 1.0%, at least 2.0%, at least 2.5%, such as between 0.5-5%, e.g., between 1-3% under the conditions defined in Example 18, compared to ETHANOL RED™).

Use of Saccharomyces cerevisiae strain MBG5038, or derivative of Saccharomyces cerevisiae strain MBG5038 expressing a glucoamylase and/or an alpha-amylase.

Use of Saccharomyces cerevisiae strain MBG5012, or derivative of Saccharomyces cerevisiae strain MBG5012 expressing a glucoamylase and/or an alpha-amylase.

Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038, or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5012 may be used for increasing the ethanol yield in fermentation.

In one embodiment, the liquefied mash, to be fermented, has been subjected to alpha- amylase and from 0.5-50 micro gram protease per gram DS, such as 1-5 micro gram protease per gram DS, such as about 1.5 or 3 micro gram protease per gram DS.

The protease may be a bacterial protease. The protease may be derived from a strain of the bacterium Pyrococcus, such as a strain of Pyrococcus furiosus (pfu protease), such as or SEQ ID NO: 13 herein. The protease may be the one disclosed in SEQ ID NO: 13 herein or a protease having at least 80% identity, such as at least 85%, such as at least 90%, such as at least 95%, such as at least 96%, such as at least 97%, such as at least 98%, such as at least 99% identity to SEQ ID NO: 13 herein.

The alpha-amylase used for liquefying may be of bacterial origin, such as from the genus Bacillus, such as a strain of Bacillus stearothermophilus, in particular a variant of a Bacillus stearothermophilus alpha-amylase, such as the one shown in SEQ ID NO: 1 herein. In one embodiment, the Bacillus stearothermophilus alpha-amylase variant is selected from the group with the following mutations: I 181*+G182* and optionally substitution N193F, and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+ Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+ E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 for numbering).

In one embodiment, the liquefied mash to be fermented, has been subjected to alpha- amylase, glucoamylase and from 0.5-50 micro gram protease per gram DS, such as 1-5 micro gram protease per gram DS such as about 1.5 or 3 micro gram protease per gram DS. The glucoamylase may be derived from a strain of the genus Penicillium, especially a strain of Penicillium oxalicum disclosed in SEQ ID NOs: 9 or 14 herein.

The glucoamylase may be a variant of the Penicillium oxalicum glucoamylase having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 for numbering). In one embodiment, the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 for numbering) and further one of the following substitutions or combinations of substitutions:

P11 F + T65A + Q327F; and

P2N + P4S + P1 1 F + T65A + Q327F (using SEQ ID NO: 14 for numbering).

Yeast

In one embodiment is a strain of Saccharomyces cerevisiae deposited under the Budapest Treaty at the Agricultural Research Service Patent Culture Collection (NRRL) having deposit accession no. NRRL Y67549 ( Saccharomyces cerevisiae strain MBG5038), or a derivative thereof expressing a glucoamylase and/or an alpha-amylase.

In one embodiment is a strain of Saccharomyces cerevisiae deposited under the Budapest Treaty at the Agricultural Research Service Patent Culture Collection (NRRL) having deposit accession no. NRRL Y67700 ( Saccharomyces cerevisiae strain MBG5012), or a derivative thereof expressing a glucoamylase and/or an alpha-amylase.

The majority of the world’s fuel ethanol is produced by industrial scale fermentation of starch-based sugars, in substrates such as corn mash. During industrial scale fermentation, the yeast encounter various physiological challenges including variable concentrations of sugars, high concentrations of yeast metabolites such as ethanol, glycerol, organic acids, osmotic stress, as well as potential competition from contaminating microbes such as wild yeasts and bacteria. As a consequence, many Saccharomyces strains, particularly those that are naturally occurring, are not suitable for use in industrial fermentation. A widely used commercially available industrial strain of Saccharomyces (i.e. for industrial scale fermentation) is the Saccharomyces cerevisiae strain used, for example, in the product ETHANOL RED™. This strain is well suited to industrial ethanol production, however improved strains of Saccharomyces cerevisiae are needed.

The Applicants have produced strain NMI V14/004037 (See, WO2015/143324 and WO2015/143317), which is a strain of Saccharomyces cerevisiae which produces higher levels of ethanol from corn mash than naturally occurring strains of Saccharomyces cerevisiae, and strains of Saccharomyces cerevisiae used in the fuel ethanol industry such as ETHANOL RED™. In particular, strain NMI V14/004037 has an ethanol yield from glucose that is higher than other industrial strains such as ETHANOL RED™ during fermentation of corn mash. This means that strain NMI V14/004037 can produce more ethanol per gram of glucose than ETHANOL RED™ during fermentation of corn mash.

The Applicants have further produced strain no. V15/004035, V15/004036, and V15/004037 (See, WO 2016/153924) which are capable of ethanol yields from glucose that are the same or similar to strain V14/004037 under the conditions encountered in industrial scale fermentation, such as those encountered during fermentation of corn mash, and which are higher than commercially available industrial Saccharomyces cerevisiae strains used in the ethanol industry and naturally occurring strains of Saccharomyces cerevisiae.

The Applicants have further produced stain no. NRRL Y67549 and NRRL Y67700 as described herein which demonstate improved properties as describen in the Examples.

The Applicants have further produced derivatives of strain nos. NRRL Y67549 and NRRL Y67700 as described herein which express a glucoamylase and demonstate improved properties as described in the Examples.

Typically, the ethanol produced from fermentation of corn mash is produced from fermentation of sugars that are endogenous to the corn mash. Sugars that are endogenous to the corn mash are sugars that are derived from the corn rather than sugars that are added from an exogenous source.

The ability to produce ethanol rapidly in the first 20 hours of fermentation, the ethanol yield after 50 hours of fermentation, and the ability to utilize much of the glucose present in corn mash substrate within 50 hours of fermentation, are all features which can distinguish the strains herein from naturally occurring strains, and commercially available industrial strains of Saccharomyces cerevisiae.

Additionally, Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) and Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) are capable of growth in media in which cysteine is the sole nitrogen source. As a consequence, the ability of strains Saccharomyces cerevisiae strain MBG5038 and MBG 5012 to utilize cysteine as the sole nitrogen source is a further characteristic which distinguishes this strain from:

(a) contaminating strains of Saccharomyces that do not utilize cysteine as a sole nitrogen source; and

(b) other strains used in the ethanol industry that do not have the ethanol producing capabilities of Saccharomyces cerevisiae strain MBG5038 or MBG5012; and/or do not utilize cysteine as the sole nitrogen source.

As a result of its ability to utilize cysteine as a sole nitrogen source, Saccharomyces cerevisiae strains MBG5038 and MBG5012 are readily differentiated from current strains of Saccharomyces that are used in the ethanol industry such as Ethanol Red®.

The strain may also be a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012. As used herein, a“derivative” of Saccharomyces cerevisiae strain MBG5038 or MBG5012 is a strain derived from said strain, such as through mutagenesis, recombinant DNA technology, mating, cell fusion, or cytoduction between yeast strains. The strain derived from Saccharomyces cerevisiae strain MBG5038 or MBG5012 may be a direct progeny (i.e. the product of a mating between Saccharomyces cerevisiae strain MBG5038 or MBG5012, and another strain or itself), or a distant progeny resulting from an initial mating between Saccharomyces cerevisiae strain MBG5038 or MBG5012 and another strain or itself, followed by a large number of subsequent matings.

In one embodiment, a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 is a hybrid strain produced by culturing a first yeast strain with Saccharomyces cerevisiae strain MBG5038 or MBG5012 under conditions which permit combining of DNA between the first yeast strain and Saccharomyces cerevisiae strain MBG5038 or MBG5012.

In one embodiment, a recombinant derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 has been prepared by genetically modifying Saccharomyces cerevisiae strain MBG5038 or MBG5012 (or another derivative thereof) to express an alpha- amylase and/or glucoamylase described herein.

In one embodiment is a method of producing a recombinant derivative of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA)comprising:

(a) transforming Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012) with one or more expression vectors encoding a glucoamylase and/or an alpha-amylase; and

(b) isolating the transformed strain.

In one embodiment, a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 may be prepared by:

(a) culturing a first yeast strain with a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012), under conditions which permit combining of DNA between the first yeast strain and the second yeast strain; and

(b) isolating hybrid strains; and

(c) optionally repeating steps (a) and (b) using a hybrid strain isolated in step (b) as the first yeast strain and/or the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012. In one embodiment, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012. Derivatives of Saccharomyces which exhibit one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012 are produced using Saccharomyces cerevisiae strain MBG5038 or MBG5012, respectively. In this regard, Saccharomyces cerevisiae strain MBG5038 or MBG5012 forms the basis for preparing other strains having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012, respectively. For example, strains of Saccharomyces which exhibit one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012 can be derived from Saccharomyces cerevisiae strain MBG5038 of MBG5012, respectively using methods such as classical mating, cell fusion, or cytoduction between yeast strains, mutagenesis or recombinant DNA technology.

In one embodiment, a derivative of Saccharomyces cerevisiae strain MBG5038 which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012 may be produced by:

(a) culturing a first yeast strain with a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012), under conditions which permit combining of DNA between the first yeast strain and the second yeast strain;

(b) screening or selecting for a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, such as screening or selecting for a derivative with increased ethanol production in corn mash compared to the first strain;

(c) optionally repeating steps (a) and (b) with the screened or selected strain as the first yeast strain and/or the second yeast strain, until a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 is obtained which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012.

The first yeast strain may be any strain of yeast if the DNA of the strain can be combined with the second yeast strain using methods such as classical mating, cell fusion or cytoduction. Typically, the first yeast strain is a Saccharomyces strain. More typically, the first yeast strain is a Saccharomyces cerevisiae strain. Saccharomyces cerevisiae is as defined by Kurtzman (2003) FEMS Yeast Research vol 4 pp. 233-245. The first yeast strain may have desired properties which are sought to be combined with the defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012. The first yeast strain may be, for example, any Saccharomyces cerevisiae strain, such as for example ETHANOL RED®. It will also be appreciated that the first yeast strain may be Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012).

The first and second yeast strains are cultured under conditions which permit combining of DNA between the yeast strains. As used herein,“combining of DNA” between yeast strains refers to combining of all or a part of the genome of the yeast strains. Combining of DNA between yeast strains may be by any method suitable for combining DNA of at least two yeast cells, and may include, for example, mating methods which comprise sporulation of the yeast strains to produce haploid cells and subsequent hybridising of compatible haploid cells; cytoduction; or cell fusion such as protoplast fusion.

In one embodiment, culturing the first yeast strain with the second yeast, under conditions which permit combining of DNA between the first yeast strain and the second yeast strain, comprises:

(i) sporulating the first yeast strain and the second yeast strain;

(ii) germinating and hybridizing spores produced by the first yeast strain with spores produced by the second yeast strain.

In one embodiment, the method of producing a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012, comprises:

(a) providing: (i) a first yeast strain; and (ii) a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012);

(b) sporulating the first yeast strain and the second yeast strain;

(c) germinating and hybridising the spores of the first yeast strain with germinated spores of the second yeast strain;

(d) screening or selecting for a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012, such as screening or selecting for a derivative with increased ethanol production in 20hrs of fermentation in corn mash compared to the first strain, and/or higher ethanol yield from glucose during fermentation of corn mash than the first strain;

(e) optionally repeating steps (b) to (d) with the screened or selected strain as the first and/or second yeast strain.

Methods for sporulating, germinating and hybridising yeast strains, and in particular, Saccharomyces strains, are known in the art and are described in, for example, Ausubel, F. M. et al., (1997) Current Protocols in Molecular Biology, Volume 2, pages 13.2.1 to 13.2.5 (John Willey & Sons Inc); Chapter 7,“Sporulation and Hybridisation of yeast” by R.R. Fowell, in“The Yeasts” vol 1 , A.H. Rose and J.S. Harrison (Eds), 1969, Academic Press. In one embodiment, the yeast strains may be cultured under conditions which permit cell fusion. Methods for the generation of intraspecific or interspecific hybrids using cell fusion techniques are described in, for example, Spencer et al. (1990) in, Yeast T echnology, Spencer JFT and Spencer DM (Eds), Springer Verlag, New York.

In another embodiment, the yeast strains may be cultured under conditions which permit cytoduction. Methods for cytoduction are described in, for example, Inge-Vechymov et al. (1986) Genetika 22: 2625-2636; Johnston (1990) in, Yeast technology, Spencer JFT and Spencer DM (Eds), Springer Verlag, New York.

In one embodiment, screening or selecting for derivatives of Saccharomyces cerevisiae strain MBG5038 or MBG5012 comprises screening or selecting for a derivative with increased ethanol production in the first 20 hours of fermentation of corn mash compared to the first strain, and/or screening or selecting for a hybrid which has a higher ethanol yield from glucose in corn mash compared to the first strain.

As used herein, “ethanol yield from glucose” is the yield of ethanol that would be achieved from glucose if all of the glucose in a substrate were used in the fermentation. In one embodiment, ethanol yield from glucose is calculated as follows:

(G x 0.51) + E

wherein

G = % weight/volume glucose remaining following fermentation of the glucose- containing substrate; and

E = % weight/volume of ethanol present following fermentation of the glucose- containing substrate.

The derivatives may be screened or selected for ethanol yields by screening for one or more of the following characteristics:

(a) produces a % w/v of acetate that is in the range from an amount higher than that produced by strain Ethanol Red® to the amount produced by Saccharomyces cerevisiae strain MBG5038 or MBG5012, under the same conditions in a corn mash fermentation;

(b) produces a ratio of % w/v glycerol to % w/v acetate that is in the range from less than the ratio of % w/v glycerol to % w/v acetate produced by Ethanol Red® to the ratio of % w/v glycerol to % w/v acetate produced by Saccharomyces cerevisiae strain MBG5038 or MBG5012, under the same conditions in a corn mash fermentation;

(c) produces a ratio of % w/v ethanol to % w/v acetate that is in the range from less than the ratio of % w/v ethanol to % w/v acetate produced by Ethanol Red® to the ratio of % w/v ethanol to % w/v acetate produced by Saccharomyces cerevisiae strain MBG5038 or MBG5012, under the same conditions in a corn mash fermentation.

Methods for determining the amount of ethanol, glycerol and acetate produced by a strain are known in the art. For example, methods for testing for determining the amount of ethanol, glycerol and acetate produced by a strain during fermentation of corn mash are described in, for example, WO 2011/035392. Once the amount of ethanol, glycerol and acetate produced are known, the ratio of ethanol/acetate and glycerol/acetate can be readily determined. Accordingly, strains can be readily screened for production levels of ethanol, acetate and/or glycerol using known methods.

In one embodiment, a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012 may be a mutant of Saccharomyces cerevisiae strain MBG5038 or MBG5012. Methods for producing mutants of Saccharomyces yeast, and specifically mutants of Saccharomyces cerevisiae, are known in the art and described in, for example, Lawrence C.W. (1991) Methods in Enzymology, 194: 273-281.

In another embodiment, a derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012 may be a recombinant derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012. A recombinant derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 is a strain produced by introducing into Saccharomyces cerevisiae strain MBG5038 or MBG5012, respectively, a nucleic acid using recombinant DNA technology. Methods for the introduction of nucleic acid into Saccharomyces yeast cells, and in particular strains of Saccharomyces, are known in the art and are described in, for example, Ausubel, F. M. et al. (1997), Current Protocols in Molecular Biology, Volume 2, pages 13.7.1 to 13.7.7, published by John Wiley & Sons Inc.

Also described are methods for the production of ethanol using the strain described herein. In one form, Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012) is incubated with a substrate comprising fermentable sugars under conditions that allow fermentation of the fermentable sugars. The fermentable sugars may be one or more of glucose, galactose, maltose, fructose and sucrose. Typically, the fermentable sugar is glucose. While strains Saccharomyces cerevisiae strain MBG5038 and MBG5012 are well suited to fermentation in corn mash, it is envisaged the strain may also be suitable for other fermentation processes. Accordingly, the source of the fermentable sugar in the substrate may be, for example, hydrolysed starch, hydrolysed cellulose, molasses, cane juice, grape juice, fruit juice, glucose, maltodextrins, raw sugar juice, galactose, sucrose, or any other forms of fermentable sugars. In one form, the source of fermentable sugar in the substrate is hydrolysed starch. Typically, the starch is obtained from a substrate such as corn mash. In preparing the substrate, the grain is typically ground and mixed with water and hydrolytic enzyme(s) under conditions which result in hydrolysis of the starch and release of fermentable sugars such as glucose. Typical enzymes for hydrolysis of the starch include a-amylase, amyloglucosidase, pullulanase, alpha-amylase, glucoamylase, or mixtures thereof. Enzymes suitable for hydrolysis are available from, for example, Novozymes or Genencor Inc. In one form, substrate is provided in the form of corn mash. Corn mash is typically produced by: (a) grinding corn to form a meal; (b) mixing the meal with water; and (c) hydrolyzing the starch in the corn meal. Methods for preparation of corn mash are known in the art and described in, for example, Thomas, K. C. et al. , (2001) Journal of Applied Microbiology, volume 90, pages 819-828. Methods for the preparation of other starch-based substrates including sorghum, starch streams and combinations thereof are also known in the art and described in, for example, Kwiatkowski J.R. et al. (2003) Industrial Crops and Products 23: 288-296 and Bothast R.J. and Schlicher M. A. (2005) Applied Microbial Biotechnology 67: 19-25

The fermentation is carried out at a temperature which permits fermentation of the fermentable sugars. Typically, the temperature at which the fermentation is carried out is from 25-34°C.

The fermentation results in an alcoholic mash comprising ethanol and residual sugars in solution, and a particulate portion comprising residual solids including yeast. Ethanol is isolated from the mash using methods know in the art such as distillation or filtration.

Methods for fermentation and distillation are known in the art and are described in, for example, Kwiatkowski J.R. et al. (2003) Industrial Crops and Products 23: 288-296 and Bothast R.J. and Schlicher M. A. (2005) Applied Microbial Biotechnology 67: 19-25

Also contemplated are methods of producing distiller’s grain. Distiller’s grains may be produced from the residual solids produced in the fermentation using methods known in the art and described in, for example, United States Patent 7,572,353. Because Saccharomyces cerevisiae strains MBG5038 and MBG5012 reduce the level of residual sugars remaining following fermentation, the distiller’s grain which results from fermentation using Saccharomyces cerevisiae strain MBG5038 or MBG5012 has a lowered glucose content and is therefore more stable and less prone to charring, caramelisation or contamination with unwanted microorganisms.

Furthermore, lower glycerol content in distiller’s grains is a process advantage because less time is required for drying the distiller’s grains. In addition, less glycerol in the distiller’s grains results in improved flowability, and further results in distiller’s grains which has a higher nutrient content (e.g. higher protein).

A further aspect provides dried or compressed yeast comprising Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012), typically having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 or MBG5012. A further aspect provides a composition comprising Saccharomyces cerevisiae strain MBG5038 (or a derivative of Saccharomyces cerevisiae strain MBG5038) or Saccharomyces cerevisiae strain MBG5012 (or a derivative of Saccharomyces cerevisiae strain MBG5012). The composition may be, for example, cream yeast, compressed yeast, wet yeast, dry yeast, semi-dried yeast, crumble yeast, stabilized liquid yeast or frozen yeast. Methods for preparing such yeast compositions are known in the art.

In some embodiments, the derivative of Saccharomyces cerevisiae strain MBG5038 or MBG5012 expresses a glucoamylase and/or an alpha-amylase. The derivatives expressing glucoamylase and/or alpha-amylase have been generated in order to improve ethanol yield and to improve process economy by cutting enzyme costs since part or all of the necessary enzymes needed to hydrolyse starch will be produced by the yeast organism.

One aspect of the present invention therefore relates to yeast strains comprising one or more expression vectors encoding a glucoamylase and/or an alpha-amylase, wherein the yeast is derived from a parent Saccharomyces cerevisiae strain MBG5038 or MBG5012; and wherein the glucoamylase is selected from glucoamylases obtainable from Gloeophyllum, Pycnoporous, Trametes.

Another aspect of the present invention therefore relates to yeast strain comprising one or more expression vectors encoding a glucoamylase and/or an alpha-amylase, wherein the yeast is derived from a parent Saccharomyces cerevisiae strain MBG5038 or MBG5012; and wherein the alpha-amylase is selected from a Rhizomucor pusillus or Aspergillus terreus alpha-amylase.

In one embodiment the the glucoamylase is selected from a Gloeophyllum trabeum, Gloeophyllum sepiarium, or Gloeophyllum abietinum glucoamylase.

In another embodiment the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17.

In one embodiment the the glucoamylase is the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 having one of the following substitutions: V59A; S95P; A121 P; T119W; S95P+A121 P; V59A+S95P; S95P+T119W; V59A+S95P+A121 P; or

S95P+T119W+A121 P, especially S95P+A121 P; and wherein the glucoamylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 17.

In one particular embodiment the glucoamylase is selected from a Trametes cingulata glucoamylase. More particularly the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 20;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 20.

In one particular embodiment the glucoamylase is selected from a Pycnoporus sanguineus glucoamylase. More particularly the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 18;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 18.

In another particular embodiment the alpha-amylase is Rhizomucor pusillus alpha- amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) as shown in SEQ ID NO: 16, preferably one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N (using SEQ ID NO: 16 for numbering), and wherein the alpha-amylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 16.

In another embodiment, the alpha-amylase is an Aspergillus terreus alpha-amylase. More particularly the alpha-amylase is selected from the group consisting of:

(i) an alpha-amylase comprising the polypeptide of SEQ ID NO: 6 of WO2017/087330 (the content of which is incorporated by reference);

(ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 6 of WO2017/087330.

Compositions

This aspect relates to a formulated Saccharomyces yeast composition comprising a yeast strain described herein and a naturally occurring and/or a nonenaturally occurring component. As mentioned above a Saccharomyces yeast strain described herein may be in any viable form, including crumbled, dry, including active dry and instant, compressed, cream (liquid) form etc. In one embodiment, the Saccharomyces cerevisiae yeast strain is dry yeast, such as active dry yeast or instant yeast. In one embodiment, the Saccharomyces cerevisiae yeast strain is crumbled yeast. In one embodiment, the Saccharomyces cerevisiae yeast strain is compressed yeast. In one embodiment, the Saccharomyces cerevisiae yeast strain is cream yeast.

In one embodiment is a composition comprising a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012 and one or more of the component selected from the group consisting of: surfactants, emulsifiers, gums, swelling agent, and antioxidants and other processing aids.

Surfactant

The compositions described herein may comprise a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012 and any suitable surfactants. In one embodiment, the surfactant(s) is/are an anionic surfactant, cationic surfactant, and/or nonionic surfactant.

Emulsifier

The compositions described herein may comprise a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012 and any suitable emulsifier. In one embodiment, the emulsifier is a fatty-acid ester of sorbitan. In one embodiment, the emulsifier is selected from the group of sorbitan monostearate (SMS), citric acid esters of monodiglycerides, polyglycerolester, fatty acid esters of propylene glycol.

In one embodiment, the composition comprises a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012, and Olindronal SMS, Olindronal SK, or Olindronal SPL including composition concerned in European Patent No. 1 ,724,336 (hereby incorporated by reference). These products are commercially available from Bussetti, Austria, for active dry yeast.

Gum

The compositions described herein may comprise a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012 and any suitable gum. In one embodiment, the gum is selected from the group of carob, guar, tragacanth, arabic, xanthan and acacia gum, in particular for cream, compressed and dry yeast.

The compositions described herein may comprise a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012 and any suitable swelling agent. In one embodiment, the swelling agent is methyl cellulose or carboxymethyl cellulose. Antioxidant

The compositions described herein may comprise a Saccharomyces yeast described herein, in particular Saccharomyces cerevisiae strain MBG5038 or MBG5012, and any suitable anti-oxidant. In one embodiment, the antioxidant is butylated hydroxyanisol (BHA) and/or butylated hydroxytoluene (BHT), or ascorbic acid (vitamin C), particular for active dry yeast.

The invention may further be described in the following numbered paragraphs:

Paragraph 1. A process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 2. The process of paragraph 1 , wherein the fermenting organism has at least one or more, such as all, of the following properties and defining characteristics:

increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein; and/or

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein.

Paragraph 3. The process of paragraph 1 or 2, wherein the fermenting organism provides an ethanol yield boost over Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) of more than 0.5%, e.g., more than 1.0%, more than 2.0%, more than 2.5%, such as about 2.9%, such as between 0.5 and 5%, such as between 1-3%, under the same process conditins, e.g., conditions as described herein.

Paragraph 4. The process of any of paragraphs 1-3, wherein the fermenting organism reduces acetaldehyde production more than 10%, e.g., more than 20%, more than 30%, more than 40%, more than 45%, such as 5-60%, such as 30-50%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein.

Paragraph 5. The process of any of paragraphs 1-4, wherein the fermenting organism increases temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein.

Paragraph 6. The process of any of paragraphs 1-5, wherein the fermenting organism decreases glycerol production by more than 3%, e.g., more than 4%, more than 5%, more than 6%, more than 7%, such as 2-15%, such as 5-10%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 7. The process of any of paragraphs 1-6, wherein the fermenting organism:

(a) produces a higher titre of ethanol in the first 20 hours of fermentation than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia), under the same conditions in a corn mash fermentation, e.g., conditions described herein;

(b) leaves less glucose remaining following 50 hours of fermentation than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia), under the same conditions in a corn mash fermentation, e.g., conditions described herein;

(c) has a higher ethanol yield than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) following 50 hours of fermentation under the same conditions in a corn mash fermentation, e.g., conditions described herein. Paragraph 8. The process of any of paragraphs 1-7, wherein a protease is added in saccharification or fermentation or SSF.

Paragraph 9. The process of any of paragraphs 1-8, further comprises, prior to the liquefaction step i), the steps of:

x) reducing the particle size of the starch-containing material, preferably by dry milling; y) forming a slurry comprising the starch-containing material and water.

Paragraph 10. The process of any of paragraphs 1-9, wherein at least 50%, e.g., at least 70%, at least 80%, at least 90% of the starch-containing material fits through a sieve with # 6 screen.

Paragraph 1 1. The process of any of paragraphs 1-10, wherein the pH in liquefaction is between 4-7, such as pH 4.5-6.5, such as pH 5.0-6.5, such as pH 5.0-6.0, such as pH 5.2-6.2, such as about 5.2, such as about 5.4, such as about 5.6, such as about 5.8.

Paragraph 12. The process of any of paragraphs 1-11 , wherein the temperature in liquefaction is in the range of 70-100°C, such as 75-95°C, 75-90°C, 80-90°C, or 82-88°C, such as about 85°C.

Paragraph 13. The process of any of paragraphs 1-12, wherein a jet-cooking step is carried out prior to liquefaction in step i).

Paragraph 14. The process of paragraph 13, wherein the jet-cooking is carried out at a temperature of 1 10-145°C, e.g, 120-140°C, such as 125-135°C, or about 130°C for about 1- 15 minutes, e.g., for about 3-10 minutes, or about 5 minutes.

Paragraph 15. The process of any of paragraphs 1-14, wherein saccharification and fermentation is carried out sequentially or simultaneously (SSF).

Paragraph 16. The process of any of paragraphs 1-15, wherein saccharification is carried out at a temperature from 20-75°C, e.g., from 40-70°C, such as about 60°C, and at a pH between 4 and 5.

Paragraph 17. The process of any of paragraphs 1-16, wherein fermentation or simultaneous saccharification and fermentation (SSF) is carried out carried out at a temperature from 25°C to 40°C, such as from 28°C to 35°C, such as from 30°C to 34°C, or about 32°C. In one embodiment, fermentation is ongoing for 6 to 120 hours, in particular 24 to 96 hours. Paragraph 18. The process of any of paragraphs 1-17, wherein the fermentation product is recovered after fermentation, such as by distillation.

Paragraph 19. The process of any of paragraphs 1-18, wherein the fermentation product is an alcohol, preferably ethanol, especially fuel ethanol, potable ethanol and/or industrial ethanol.

Paragraph 20. The process of any of paragraphs 1-19, wherein the starch-containing starting material is whole grains.

Paragraph 21. The process of any of paragraphs 1-20, wherein the starch-containing material is derived from corn, wheat, barley, rye, milo, sago, cassava, manioc, tapioca, sorghum, oats, rice or potatoes.

Paragraph 22. The process of any of paragraphs 1-21 , wherein the alpha-amylase used or added in liquefaction step i) is of bacterial origin.

Paragraph 23. The process of any of paragraphs 1-22, wherein the alpha-amylase is from the genus Bacillus, such as a strain of Bacillus stearothermophilus, in particular a variant of a Bacillus stearothermophilus alpha-amylase, such as the one shown in SEQ ID NO: 3 in WO 99/019467 or SEQ ID NO: 1 herein.

Paragraph 24. The process of paragraph 23, wherein the Bacillus stearothermophilus alpha- amylase or variant thereof is truncated at the C-terminal, preferably to be from 485-495 amino acids long, such as about 491 amino acids long.

Paragraph 25. The process of any of paragraphs 23 or 24, wherein the Bacillus stearothermophilus alpha-amylase has a double deletion at positions 1181 + G182, and optionally substitution N193F, or deletion of R179 + G180 (using SEQ ID NO: 1 for numbering).

Paragraph 26. The process of any of paragraphs 23-25, wherein the Bacillus stearothermophilus alpha-amylase has a substitution in position S242, e.g., S242Q substitution (using SEQ ID NO: 1 for numbering).

Paragraph 27. The process of any of paragraphs 23-26, wherein the Bacillus stearothermophilus alpha-amylase has a substitution in position E188, e.g., E188P substitution (using SEQ ID NO: 1 for numbering). Paragraph 28. The process of any of paragraphs 1-27, wherein the alpha-amylase has a T ½ (min) at pH 4.5, 85°C, 0.12 mM CaCh) of at least 10, such as at least 15, such as at least 20, such as at least 25, such as at least 30, such as at least 40, such as at least 50, such as at least 60, such as 10-70, such as 15-70, such as 20-70, such as 25-70, such as 30-70, such as 40-70, such as 50-70, such as 60-70.

Paragraph 29. The process of any of paragraphs 1-28, wherein the alpha-amylase present and/or added in liquefaction step i) is selected from the group of Bacillus stearothermophilus alpha-amylase variants with one of the following substitutions or combinations of substitutions in addition to I 181*+G182*, and optionally substitution N193F:

V59A+Q89R+G1 12D+E129V+K177L+R179E+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+D269E+D281 N;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+I270L;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+H274K;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+Y276F;

V59A+E129V+R157Y+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+H208Y+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+H274K;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+D281 N;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+G416V;

V59A+ E129V+ K177L+ R179E+ K220P+ N224L+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

A91 L+M96I+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F+L427M;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+N376*+I377*;

E129V+K177L+R179E+K220P+N224L+Q254S;

E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

E 129V+ K177 L+ R 179E+S242Q ;

E129V+K177L+R179V+K220P+N224L+S242Q+Q254S; K220P+N224L+S242Q+Q254S;

M284V;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V; and

V59A+E129V+K177L+R179E+Q254S+ M284V;

Paragraph 30. The process of any of paragraphs 1-29, wherein the alpha-amylase present and/or added in liquefaction step i) is selected from the following group of Bacillus stearothermophilus alpha-amylase variants comprising the following mutations: I 181*+G182*, and optionally substitution N193F, and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S

V59A+ Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+ E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

Paragraph 31. The process of any of paragraphs 1-30, wherein a glucoamylase is present and/or added in saccharification and/or fermentation.

Paragraph 32. The process of paragraph 31 , wherein the glucoamylase present and/or added in saccharification, fermentation or simultaneous saccharification and fermentation (SSF) is of fungal origin, preferably from a strain of Aspergillus, preferably A. niger, A. awamori, or A. oryzae ; or a strain of Trichoderma, preferably Trichoderma reesel·, or a strain of Talaromyces, preferably Talaroomyces emersonii, or a strain of Pycnoporus, or a strain of Gloeophyllum, such as Gloeophyllum serpiahum or Gloeophyllum trabeum, or a strain of the Nigrofomes.

Paragraph 33. The process of any of paragraphs 1-32, wherein the glucoamylase is derived from Talaromyces emersonii, such as the one shown in SEQ ID NO: 19 herein.

Paragraph 34. The process of any of paragraphs 1-33, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 19 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 19 herein. Paragraph 35. The process of any of paragraphs 1-34, wherein the glucoamylase present and/or added in saccharification is derived from Gloeophyllum serpiarium , such as the one shown in SEQ ID NO: 15 herein.

Paragraph 36. The process of any of paragraphs 1-35, wherein the glucoamylase present and/or added in saccharification is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 15 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 15 herein.

Paragraph 37. The process of any of paragraphs 1-36, wherein the glucoamylase present and/or added in saccharification is derived from Gloeophyllum trabeum such as the one shown in SEQ ID NO: 17 herein.

Paragraph 38. The process of any of paragraphs 1-37, wherein the glucoamylase present and/or added in saccharification is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 17 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 17 herein.

Paragraph 39. The process of any of paragraphs 1-38, wherein the glucoamylase is present and/or added in saccharification and/or fermentation in combination with an alpha-amylase.

Paragraph 40. The process of paragraph 39, wherein the alpha-amylase is present and/or added in saccharification and/or fermentation is of fungal or bacterial origin.

Paragraph 41. The process of paragraph 40 or 41 , wherein the alpha-amylase present and/or added in saccharification and/or fermentation is derived from a strain of the genus Rhizomucor, preferably a strain the Rhizomucor pusillus, such as the one shown in SEQ ID NO: 3 in WO 2013/006756, such as a Rhizomucor pusillus alpha-amylase hybrid having a linker and a starch-binding domain, in particular having an Aspergillus niger linker and starch bonding domain, such as the one shown in SEQ ID NO: 16 herein. Paragraph 42. The process of any of paragraphs 39-41 , wherein the alpha-amylase present and/or added in saccharification and/or fermentation is selected from the group consisting of:

(i) an alpha-amylase comprising the mature polypeptide of SEQ ID NO: 16 herein;

(ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 16 herein.

Paragraph 43. The process of any of paragraphs 39-42, wherein the alpha-amylase is a variant of the alpha-amylase shown in SEQ ID NO: 16 having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H + Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; and G128D + Y141W + D143N + K192R; or G128D + Y141 W+ D143N + K192R + P219C (using SEQ ID NO: 16 for numbering).

Paragraph 44. The process of any of paragraphs 39-43, wherein the alpha-amylase is derived from a Rhizomucor pusillus with an Aspergillus n/ger glucoamylase linker and starch-binding domain (SBD), preferably disclosed as SEQ ID NO: 16 herein, e.g., having one or more of the following substitutions: G128D, D143N, such as G128D+D143N (using SEQ ID NO: 16 for numering).

Paragraph 45. The process of any of paragraphs 39-44, wherein the alpha-amylase variant has at least 75% identity preferably at least 80%, e.g., at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 16 herein.

Paragraph 46. The process of any of paragraphs 1-42, wherein liquefaction step i) is carried out using:

an alpha-amylase;

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C; and

optionally a glucoamylase. Paragraph 47. The process of 46, wherein the protease with a thermostability value of more than 25% determined as Relative Activity at 80°C/70°C.

Paragraph 48. The process of paragraphs 46-47, wherein the protease has a thermostability of more than 30%, e.g., more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, such as more than 105%, such as more than 1 10%, such as more than 115%, such as more than 120% determined as Relative Activity at 80°C/70°C.

Paragraph 49. The process of any of paragraphs 46-48, wherein the protease has a thermostability of between 20 and 50%, such as between 20 and 40%, such as 20 and 30% determined as Relative Activity at 80°C/70°C.

Paragraph 50. The process of any of paragraphs 46-49, wherein the protease has a thermostability of between 50 and 115%, such as between 50 and 70%, such as between 50 and 60%, such as between 100 and 120%, such as between 105 and 1 15% determined as Relative Activity at 80°C/70°C.

Paragraph 51. The process of any of paragraphs 46-50, wherein the protease has a thermostability of more than 10%, e.g., more than 12%, more than 14%, more than 16%, more than 18%, more than 20%, more than 30%, more than 40%, more that 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, more than 110% determined as Relative Activity at 85°C/70°C.

Paragraph 52. The process of any of paragraphs 46-51 , wherein the protease has a thermostability of between 10 and 50%, such as between 10 and 30%, such as between 10 and 25% determined as Relative Activity at 85°C/70°C.

Paragraph 53. The process of any of paragraphs 46-52, wherein the protease has a themostability above 60%, such as above 90%, such as above 100%, such as above 1 10% at 85°C as determined using the Zein-BCA assay.

Paragraph 54. The process of any of paragraphs 46-53, wherein the protease has a themostability between 60-120, such as between 70-120%, such as between 80-120%, such as between 90-120%, such as between 100-120%, such as 110-120% at 85°C as determined using the Zein-BCA assay. Paragraph 55. The process of any of paragraphs 46-54, wherein the protease is of fungal origin.

Paragraph 56. The process of any of paragraphs 46-55, wherein the protease is a variant of the metallo protease derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially Thermoascus aurantiacus CGMCC No. 0670.

Paragraph 57. The process of any of paragraphs 46-56, wherein the protease is a variant of the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in W02003/048353 or the mature part of SEQ ID NO: 1 in WO2010/008841 or SEQ ID NO: 3 herein, with one of the following substitutions or combinations of substitutions:

S5*+D79L+S87P+A112P+D142L;

D79L+S87P+A112P+T 124V+D142L;

S5*+N26R+D79L+S87P+A1 12P+D142L;

N26R+T46R+D79L+S87P+A1 12P+D142L;

T46R+D79L+S87P+T 1 16V+D142L;

D79L+P81 R+S87P+A1 12P+D142L;

A27K+ D79L+S87P+A 112 P+T 124V+ D 142 L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+S87P+A112P+T 124V+A126V+D142L;

D79L+S87P+A112P+D142L;

D79L+Y82F+S87P+A1 12P+D142L;

S38T+D79L+S87P+A1 12P+A126V+D142L;

D79L+Y82F+S87P+A1 12P+A126V+D142L;

A27K+ D79L+S87P+A 112 P+A 126V+ D142L;

D79L+S87P+N98C+A112P+G135C+D142L;

D79L+S87P+A112P+D142L+T141 C+M161 C;

S36P+D79L+S87P+A112P+D142L;

A37P+D79L+S87P+A112P+D142L;

S49P+D79L+S87P+A112P+D142L;

S50P+D79L+S87P+A112P+D142L;

D79L+S87P+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+D142L;

S70V+ D79 L+Y82 F+S87G+ Y97W+A 112 P+ D 142 L;

D79L+Y82F+S87G+Y97W+D104P+A112P+D142L; S70V+ D79 L+Y82 F+S87G+ A 1 12 P+ D 142 L;

D79L+Y82F+S87G+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+A126V+D142L;

Y82F+S87G+S70V+D79L+D104P+A1 12P+D142L;

Y82F+S87G+D79L+D104P+A112P+A126V+D142L;

A27K+ D79L+Y82 F+S87G+D 104P+A1 12 P+A126V+ D 142 L;

A27K+Y82F+S87G+D104P+A112P+A126V+D142L;

A27K+D79L+Y82F+ D104P+A112P+A126V+D142L;

A27K+Y82F+ D 104 P+ A 112 P+ A 126V+ D 142 L;

A27K+D79L+S87P+A112P+D142L; and

D79L+S87P+D142L.

Paragraph 58. The process of any of paragraphs 46-57, wherein the protease is a variant of the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in W02003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein with one of the following substitutions or combinations of substitutions:

D79L+S87P+A112P+D142L:

D79L+S87P+D142L; and

A27K+ D79L+ Y82F+S87G+D104P+A112P+A126V+D142L.

Paragraph 59. The process of any of paragraphs 46-58, wherein the protease variant has at least 75% identity, e.g., at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein.

Paragraph 60. The process of any of paragraphs 46-59, wherein the protease variant of the Thermoascus aurantiacus protease shown in SEQ ID NO: 3 herein comprises one of the following substitutions or combinations of substitutions:

D79L S87P D142L; D79L S87P A1 12P D142L; D79L Y82F S87P A112P D142L; S38T D79L S87P A112P A 126V D142L; D79L Y82F S87P A112P A126V D142L; A27K D79L S87P A112P A 126V D142L; S49P D79L S87P A1 12P D142L; S50P D79L S87P A1 12P D142L; D79L S87P D104P A112P D142L; D79L Y82F S87G A1 12P D142L; S70V D79L Y82F S87G Y97WA112P D142L; D79L Y82F S87G Y97W D104P A112P D142L; S70V D79L Y82F S87G A112P D142L; D79L Y82F S87G D104P A1 12P D142L; D79L Y82F S87G A1 12P A126V D142L; Y82F S87G S70V D79L D104P A1 12P D142L; Y82F S87G D79L D104P A1 12P A 126V D142L; and A27K D79L Y82F S87G D104P A112P A126V D142L

Paragraph 61. The process of any of paragraphs 46-60, wherein the protease is of bacterial origin.

Paragraph 62. The process of any of paragraphs 46-61 , wherein the protease is derived from a strain of Pyrococcus, preferably a strain of Pyrococcus furiosus.

Paragraph 63. The process of any of paragraphs 46-62, wherein the protease is the one shown in SEQ ID NO: 1 in US 6,358,726, or SEQ ID NO: 13 herein.

Paragraph 64. The process of any of paragraphs 46-63, wherein the protease is one having at least 80%, e.g., at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99% identity to in SEQ ID NO: 1 in US 6,358,726 or SEQ ID NO: 13 herein.

Paragraph 65. The process of any of paragraph 46-64, wherein 0.5-100 micro gram Pyrococcus furiosus protease per gram DS, such as 1-50 micro gram Pyrococcus furiosus protease per gram DS, such as 1-10 micro gram Pyrococcus furiosus protease per gram DS, such as 1.5-5 micro gram Pyrococcus furiosus protease per gram DS, such as about or more than 1.5 micro gram Pyrococcus furiosus protease per gram DS are present and/or added in liquefaction step i).

Paragraph 66. The process of any of paragraphs 46-65, wherein 2-100 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-50 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-10 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-5 micro gram Pyrococcus furiosus protease gram DS, especially about 3 micro gram Pyrococcus furiosus protease per gram DS are present and/or added in liquefaction step i).

Paragraph 67. The process of any of paragraphs 1-66, wherein a glucoamylase is present and/or added during liquefaction step i).

Paragraph 68. The process of paragraph 67, wherein the glucoamylase present and/or added in liquefaction has a heat stability at 85°C, pH 5.3, of at least 20%, such as at least 30%, or at least 35%. Paragraph 69. The process of paragraph 67 or 68, wherein the glucoamylase present and/or added in liquefaction has a relative activity pH optimum at pH 5.0 of at least 90%, preferably at least 95%, preferably at least 97%.

Paragraph 70. The process of any of paragraphs 67-68, wherein the glucoamylase present and/or added in liquefaction has pH stability at pH 5.0 of at least at least 80%, at least 85%, at least 90%.

Paragraph 71. The process of any of paragraphs 67-70, wherein the glucoamylase present and/or added in liquefaction step i) is derived from a strain of the genus Penicillium, especially a strain of Penicillium oxalicum disclosed as SEQ ID NO: 2 in WO 201 1/127802 or SEQ ID NOs: 9 or 14 herein.

Paragraph 72. The process of any of paragraphs 67-71 , wherein the glucoamylase has at least 80%, more preferably at least 85%, more preferably at least 90%, more preferably at least 91 %, more preferably at least 92%, even more preferably at least 93%, most preferably at least 94%, and even most preferably at least 95%, such as even at least 96%, at least 97%, at least 98%, at least 99% or 100% identity to the mature polypeptide shown in SEQ ID NO: 2 in WO 2011/127802 or SEQ ID NOs: 9 or 14 herein.

Paragraph 73. The process of any of paragraphs 67-72, wherein the glucoamylase is a variant of the Penicillium oxalicum glucoamylase shown in SEQ ID NO: 2 in WO 2011/127802 having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 herein for numbering), such as a variant disclosed in WO 2013/053801.

Paragraph 74. The process of any of paragraph 67-73, wherein the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 for numbering) and further one of the following substitutions or combinations of substitutions:

T65A; Q327F; E501V; Y504T; Y504*; T65A + Q327F; T65A + E501V; T65A + Y504T; T65A + Y504*; Q327F + E501 V; Q327F + Y504T; Q327F + Y504*; E501V + Y504T; E501V + Y504*; T65A + Q327F + E501V; T65A + Q327F + Y504T; T65A + E501V + Y504T; Q327F + E501V + Y504T ; T65A + Q327F + Y504*; T65A + E501V + Y504*; Q327F + E501V + Y504*; T65A + Q327F + E501V + Y504T; T65A + Q327F + E501V + Y504*; E501V + Y504T; T65A + K161 S; T65A + Q405T ; T65A + Q327W; T65A + Q327F; T65A + Q327Y; P11 F + T65A + Q327F; R1 K + D3W + K5Q + G7V + N8S + T10K + P1 1S + T65A + Q327F; P2N + P4S + P1 1 F + T65A + Q327F; P11 F + D26C + K33C + T65A + Q327F; P2N + P4S + P1 1 F + T65A + Q327W + E501V + Y504T; R1 E + D3N + P4G + G6R + G7A + N8A + T10D+ P1 1 D + T65A + Q327F; P1 1 F + T65A + Q327W; P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; P1 1 F + T65A + Q327W + E501V + Y504T; T65A + Q327F + E501V + Y504T; T65A + S105P + Q327W; T65A + S105P + Q327F; T65A + Q327W + S364P; T65A + Q327F + S364P; T65A + S103N + Q327F; P2N + P4S + P11 F + K34Y + T65A + Q327F; P2N + P4S + P11 F + T65A + Q327F + D445N + V447S; P2N + P4S + P11 F + T65A + 1172V + Q327F; P2N + P4S + P1 1 F + T65A + Q327F + N502*; P2N + P4S + P11 F + T65A + Q327F + N502T + P563S + K571 E; P2N + P4S + P11 F + R31S + K33V + T65A + Q327F + N564D + K571S; P2N + P4S + P11 F + T65A + Q327F + S377T ; P2N + P4S + P1 1 F + T65A + V325T+ Q327W; P2N + P4S + P1 1 F + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11 F + T65A + 1172V + Q327F + E501V + Y504T ; P2N + P4S + P1 1 F + T65A + Q327F + S377T + E501V + Y504T; P2N + P4S + P11 F + D26N + K34Y + T65A + Q327F; P2N + P4S + P11 F + T65A + Q327F + I375A + E501V + Y504T; P2N + P4S + P11 F + T65A + K218A + K221 D + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + S103N + Q327F + E501V + Y504T; P2N + P4S + T10D + T65A + Q327F + E501V + Y504T; P2N + P4S + F12Y + T65A + Q327F + E501V + Y504T; K5A + P1 1 F + T65A + Q327F + E501V + Y504T; P2N + P4S + T10E + E18N + T65A + Q327F + E501 V + Y504T; P2N + T10E + E18N + T65A + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T + T568N; P2N + P4S + P1 1 F + T65A + Q327F + E501V + Y504T + K524T + G526A; P2N + P4S + P11 F + K34Y + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P1 1 F + R31 S + K33V + T65A + Q327F + D445N + V447S + E501V + Y504T ; P2N + P4S + P1 1 F + D26N + K34Y + T65A + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + F80* + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + K1 12S + Q327F + E501 V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + E501 V + Y504T + T516P + K524T + G526A; P2N + P4S + P1 1 F + T65A + Q327F + E501V + N502T + Y504*; P2N + P4S + P1 1 F + T65A + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + S103N + Q327F + E501V + Y504T; K5A + P11 F + T65A + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + E501V + Y504T + T516P + K524T + G526A; P2N + P4S + P1 1 F + T65A + K79A + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + K79G + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + K79I + Q327F + E501 V + Y504T; P2N + P4S + P1 1 F + T65A + K79L + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + K79S + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + L72V + Q327F + E501V + Y504T; S255N + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + E74N + V79K + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + G220N + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + Y245N + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q253N + Q327F + E501V + Y504T; P2N + P4S + P1 1 F + T65A + D279N + Q327F + E501V + Y504T; P2N + P4S + P11 F + T65A + Q327F + S359N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + D370N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + V460S + E501V + Y504T; P2N + P4S + P11 F + T65A + Q327F + V460T + P468T + E501 V + Y504T; P2N + P4S + P11 F + T65A + Q327F + T463N + E501V + Y504T; P2N + P4S + P1 1 F + T65A + Q327F + S465N + E501V + Y504T; andP2N + P4S + P1 1 F + T65A + Q327F + T477N + E501V + Y504T.

Paragraph 75. The process of any of paragraphs 67-74, wherein the glucoamylase present and/or added in liquefaction is the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 herein for numbering) and further one of the following substitutions or combinations of substitutions: P1 1 F + T65A + Q327F; and P2N + P4S + P11 F + T65A + Q327F (using SEQ ID NO: 14 herein for numbering).

Paragraph 76. The process of any of paragraphs 67-75, wherein the glucoamylase variant has at least 75% identity, e.g., at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 14 herein.

Paragraph 77. The process of any of paragraphs 1-76, further wherein a pullulanase is present during liquefaction and/or saccharification.

Paragraph 78. The process of any of paragraphs 1-77, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus ; ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 79. The process of any of paragraphs 1-78, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution (using SEQ ID NO: 1 herein for numbering); ii) saccharifying using a glucoamylase derived from a strain of Gloephyllum, such as Gloephyllum serpiarium or Gloephyllum trabeum.

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 80. The process of any of paragraphs 1-79, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus ;

a protease having a thermostability value of more than 20% determined as Relative

Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or

Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 81. A process of paragraphs 1-80, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase, preferably derived from Bacillus stearothermophilus, comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution (using SEQ ID NO: 1 for numbering) and having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ of at least 10;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 82. A process of paragraphs 1-81 , comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase, preferably derived from Bacillus stearothermophilus, having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

a protease, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus, having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C; and

optionally a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 83. A process of paragraphs 1-82, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions: E129V+K177L+R179E; V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V;

and E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

ii) saccharifying using a glucoamylase, such as one from a strain of Gloephyllum, such as a strain of Gloephyllum serpiarium ;

iii) fermenting using a fermenting organism; wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 84. A process of paragraphs 1-83, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F, and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 85. A process of paragraphs 1-84, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optionally substitution N193F, and further optionally one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering),

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038. Paragraph 86. The process of any of paragraphs 1-85, comprising the steps of: i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optionally substitution N193F (using SEQ ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase having a K79V substilution (using SEQ ID NO: 14 herein for numbering); and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 87. A process of paragraphs 1-86, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase, preferably derived from Bacillus stearothermophilus, having a T½

(min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus, preferably A. niger, A. awamori, or A. oryzae ; or a strain of Trichoderma, preferably T. reesel·, or a strain of Talaromyces, preferably T. emersonii, or a strain of Pycnoporus, or a strain of Gloephyllum, such as G. serpiarium or G. trabeum, or a strain of the Nigrofomes;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 88. A process of paragraphs 1-87, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using;

an alpha-amylase, preferably derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F and having a T ½ (min) at pH 4.5, 85°C, 0.12 mM CaC of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

a Penicillium oxalicum glucoamylase; and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 89. A process of paragraphs 1-88, comprising the steps of:

i) liquefying the starch-containing material at a temperature a temperature between 80-

90°C using;

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS; a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F; K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering); and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 90. A process of paragraphs 1-89, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182, and optional substitution N193F; and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+C89R+E129V+K177L+R179E+H208Y+K220P+N224L+C254S;

V59A+C89R+ E129V+ K177L+ R179E+ C254S+ M284V;

V59A+E129V+ K177L+ R179E+ C254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242C+C254S (using SEC ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase shown in SEC ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + C327F;

K79V+P2N + P4S + P11 F + T65A + C327F;

K79V +P11 F + D26C + K33C + T65A + C327F;

K79V +P2N + P4S + P11 F + T65A + C327W + E501V + Y504T; K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering); and

optionally a pullulanase;

ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus ; or a strain of Trichoderma; a strain of Talaromyces, a strain of Pycnoporus ; a strain of Gloephyllum; and a strain of the Nigrofomes;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 91. A process of any of paragraphs 1-90, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optionally substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+C89R+E129V+K177L+R179E+H208Y+K220P+N224L+C254S;

V59A+C89R+ E129V+ K177L+ R179E+ C254S+ M284V;

V59A+E129V+ K177L+ R179E+ C254S+ M284V;

E129V+K177L+R179E+K220P+N224L+S242C+C254S (using SEC ID NO: 1 herein for numbering);

a protease derived from Pyrococcus furiosus, preferably the one shown in SEC ID NO: 13 herein;

a Penicillium oxalicum glucoamylase shown in SEC ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + C327F; or

K79V+P2N + P4S + P11 F + T65A + C327F; or

K79V +P11 F + D26C + K33C + T65A + C327F; or

K79V +P2N + P4S + P11 F + T65A + C327W + E501V + Y504T; or

K79V +P2N + P4S + P11 F + T65A + C327F + E501V + Y504T; or K79V +P1 1 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 92. The process of any of paragraphs 1-91 , wherein a cellulolytic enzyme composition is present in saccharification, fermentation or simultaneous saccharification and fermentation (SSF).

Paragraph 93. The process of any of paragraphs 1-92, wherein the fermenting organism has properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038, or a derivative of Saccharomyces cerevisiae strain MBG5038 having the defining characteristics of Saccharomyces cerevisiae strain MBG5038, as it provides one or more, such as all of, the following properties or defining characteristics

an increase in ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions e.g., as described herein; and/or decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., as described herein.

Paragraph 94. The process of any of paragraphs 1-93, wherein the fermenting organism, provides an ethanol yield boost over Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) of more than 0.5%, e.g., more than 1.0%, more than 2.0%, more than 2.5%, about 2.9%, such as between 0.5 and 5%, such as 1-3%, under the same process conditins, e.g., conditions described herein.

Paragraph 95. The process of any of paragraphs 1-94, wherein the fermenting organism reduces acetaldehyde production more than 10%, e.g., more than 20%, more than 30%, more than 40%, more than 45%, such as 5-60%, such as 30-50%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 96. The process of any of paragraphs 1-95, wherein the fermenting organism increases temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 97. The process of any of paragraphs 1-96, wherein the fermenting organism decreases glycerol production by more than 3%, e.g., more than 4%, more than 5%, more than 6%, more than 7%, such as 2-15%, such as 5-10%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 98. The process of any of paragraphs 1-97, wherein the fermenting organism is a non-recombinant Saccharomyces strain, e.g., a non-recombinant Saccharomyces cerevisiae strain.

Paragraph 99. The process of any of paragraphs 1-98, wherein the fermenting organism is capable of utilizing cysteine as the sole nitrogen source.

Paragraph 100. A process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus ; ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism has one or more, such as all, of the following properties and defining characteristics:

increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein.

Paragraph 101. The process of paragraph 100, wherein the fermenting organism is a Saccharomyces cerevisiae yeast

Paragraph 102. The process of paragraphs 100 or 101 , wherein the fermenting organism is a non-recombinant Saccharomyces cerevisiae yeast.

Paragraph 103. A process of any of paragraphs 1-102, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

a protease derived from Pyrococcus furiosus, preferably the one shown in SEQ ID NO: 13 herein present and/or added in a dosage of 1-5 micro gram protease per gram DS, such as about 1.5 or 3 micro gram protease per gram DS;

optionally a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F; or

K79V+P2N + P4S + P11 F + T65A + Q327F; or

K79V +P11 F + D26C + K33C + T65A + Q327F; or K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T; or

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; or

K79V +P1 1 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 104. The process of any of paragraphs 100-103, wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative of Saccharomyces strain MBG5038 having defining characteristics of strain MBG5038.

Paragraph 105. The process of paragraphs 104, wherein a protease is present or added in saccharification and/or fermentation or simultaneous saccharification and fermentation (SSF).

Paragraph 106. A Saccharomyces yeast strain deposited under the Budapest Treaty and having NRRL accession no. NRRL Y67549, or a derivative of strain NRRL Y67549.

Paragraph 107. A method of producing a derivative of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA), comprising:

a. culturing a first yeast strain with a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 or a derivative thereof, under conditions which permit combining of DNA between the first yeast strain and the second yeast strain; and

b. isolating hybrid strains; and

c. optionally repeating steps (a) and (b) using a hybrid strain isolated in step (b) as the first yeast strain and/or the second yeast strain.

Paragraph 108. A method of producing a derivative of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) which exhibits the defining characteristics of

Saccharomyces cerevisiae strain MBG5038, comprising:

(a) providing:

(i) a first yeast strain; and

(ii) a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5038 or a derivative thereof;

(b) culturing the first yeast strain and the second yeast strain under conditions which permit combining of DNA between the first and second yeast strains;

(c) screening or selecting for a derivative of Saccharomyces cerevisiae strain MBG5038.

Paragraph 109. The method of paragraph 108, wherein step (c) comprises screening or selecting for a hybrid strain which exhibits one or more defining characteristic of

Saccharomyces cerevisiae strain MBG5038.

Paragraph 110. The method of paragraph 108, comprising the further step of:

(d) repeating steps (b) and (c) with the screened or selected strain from step (c) as the first and/or second strain, until a derivative is obtained which exhibits the defining characteristics of Saccharomyces cerevisiae strain MBG5038.

Paragraph 111. The method of paragraph 109 or 110, wherein the culturing step (b) comprises:

(i) sporulating the first yeast strain and the second yeast strain;

(ii) hybridizing germinated spores produced by the first yeast strain with germinated spores produced by the second yeast strain.

Paragraph 112. A Saccharomyces strain produced by the method of any one of paragraphs 107 to 111.

Paragraph 113. A Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA). Paragraph 114. A method of producing ethanol, comprising incubating a strain of any of paragraphs 106, 112 or 113 with a substrate comprising a fermentable sugar under conditions which permit fermentation of the fermentable sugar to produce ethanol.

Paragraph 115. Use of a strain of any of paragraphs 106, 112 or 113 in the production of ethanol.

Paragraph 116. A method of producing distiller’s grain, comprising:

(a) incubating a Saccharomyces strain of any of paragraphs 106, 112 or 113 with a substrate comprising fermentable sugar under conditions which allow fermentation of the fermentable sugar to produce ethanol and distiller’s grains;

(b) isolating the distiller’s grains.

Paragraph 117. Distiller’s grain produced by the method of paragraph 116.

Paragraph 118. Use of a strain of paragraph 106, 112 or 113 in the production of distiller’s grains.

Paragraph 119. Use of a strain of paragraphs 106, 112 or 113 in the production of a Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

Paragraph 120. Use of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) in the production of a Saccharomyces strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5038.

Paragraph 121. Use of Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5038 or a derivative thereof in a process according to any of paragraphs 1-120. Paragraph 122. A composition comprising a Saccharomyces yeast of any of claims 106, 112 or 113 and one or more naturally occurring and/or non-naturally occurring components.

Paragraph 123. The composition of claim 122, wherein the components are selected from the group consisting of: surfactants, emulsifiers, gums, swelling agents, and antioxidants.

Paragraph 124. The composition of paragraph 122 or 123, wherein the Saccharomyces yeast is Saccharomyces cerevisiae strain MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

Paragraph 125. The composition of any of paragraphs 122- 124, wherein the Saccharomyces yeast is in a viable form, in particular in dry, cream or compressed form.

Paragraph 126. A process of producing ethanol from starch-containing material comprising:

(a) saccharifying the starch-containing material; and

(b) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of at least a glucoamylase and optionally an alpha-amylase;

the fermenting organism is Saccharomyces cerevisiae;

and wherein a glucoamylase and/or an alpha-amylase is expressed from the fermenting organism.

Paragraph 127. The process according to paragraph 126, wherein the starch containing material is either gelatinized or ungelatinized starch.

Paragraph 128. The process according to paragraph 127, wherein a liquefaction step precedes the saccharification step, and wherein the liquefaction step is performed in the presence of at least a bacterial alpha-amylase, such as an alpha-amylase from Bacillus sp., particularly Bacillus stearothermophilus.

Paragraph 129. The process according to any of paragraphs 126-128, wherein the Saccharomyces cerevisiae is MBG5038 (deposited under Accession No. NRRL Y67549 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of MBG5038 or a derivative of MBG5038 having defining characteristics of strain MBG5038.

Paragraph 130. The process of paragraphs 126-129, wherein the fermenting organism is a recombinant derivative of MBG5038 that expresses the glucoamylase.

Paragraph 131. The process of paragraphs 126-130, wherein the glucocamylase is a Gloeophyllum glucoamylase, preferably Gloeophyllum trabeum, Gloeophyllum sepiarium, or Gloeophyllum abietinum glucoamylase.

Paragraph 132. The process of paragraphs 126-131 , wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17.

Paragraph 133. The process of paragraph 131 or 132, wherein the glucoamylase is the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 having one of the following substitutions: V59A; S95P; A121 P; T1 19W; S95P+A121 P; V59A+S95P; S95P+T1 19W; V59A+S95P+A121 P; or S95P+T119W+A121 P, especially S95P+A121 P.

Paragraph 134. The process of any of paragraphs 126-130, wherein the glucoamylase is expressed from the fermenting organism and is a Trametes glucoamylase, preferably a Trametes cingulata glucoamylase.

Paragraph 135. The process of paragraph 134, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 20;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 20.

Paragraph 136. The process of any of paragraphs 126-130, wherein the glucoamylase is expressed from the fermenting organism and is a Pycnoporus glucoamylase, particularly Pycnoporus sanguineus glucoamylase. Paragraph 137. The process of paragraph 136, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 18;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 18.

Paragraph 138. The process of any of paragraphs 126-137, wherein the fermenting organism is a recombinant derivative of MBG5038 that expresses the alpha-amylase.

Paragraph 139. The process of paragraphs 126-138, wherein the alpha-amylase expressed from the fermenting organism and is derived from Rhizomucor pusillus or Aspergillus terreus.

Paragraph 140. The process of paragraph 139, wherein the alpha-amylase is Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) as shown in SEQ ID NO: 16, preferably one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N, and wherein the alpha-amylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 16.

Paragraph 141. The process of paragraph 139, wherein the alpha-amylase is an Aspergillus terreus alpha-amylase selected from the group consisting of:

(i) an alpha-amylase comprising the polypeptide of SEQ ID NO: 6 of WO2017/087330;

(ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 6 of WQ2017/087330. Paragraph 142. A Saccharomyces cerevisiae yeast strain, wherein the strain is a derivative of MBG5038 comprising one or more expression vectors encoding a glucoamylase and/or an alpha-amylase.

Paragraph 143. The yeast strain according to paragraph 142, wherein the glucoamylase is selected from glucoamylases obtainable from Gloeophyllum, Pycnoporous, or Trametes.

Paragraph 144. The yeast strain according to paragraph 143, wherein the glucoamylase is selected from a Gloeophyllum trabeum, Gloeophyllum sepiarium, or Gloeophyllum abietinum glucoamylase.

Paragraph 145. The yeast strain of paragraph 144, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17.

Paragraph 146. The yeast strain of any of paragraphs 143-145, wherein the glucoamylase is the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 having one of the following substitutions: V59A; S95P; A121 P; T1 19W; S95P+A121 P; V59A+S95P; S95P+T1 19W; V59A+S95P+A121 P; or S95P+T119W+A121 P, especially S95P+A121 P.

Paragraph 147. The yeast strain of paragraph 143, wherein the glucoamylase is a Trametes cingulata glucoamylase.

Paragraph 148. The yeast strain of paragraph 147, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 20;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 20. 149: The yeast strain of paragraph 143, wherein the glucoamylase is s a Pycnoporus sanguineus glucoamylase.

Paragraph 150. The yeast strain of paragraph 149, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 18;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 18.

Paragraph 151. The yeast strain of paragraph 142 expression vectorwherein the alpha- amylase is selected from a Rhizomucor pusillus or Aspergillus terreus alpha-amylase.

Paragraph 152. The yeast strain of paragraph 151 , wherein the alpha-amylase is Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) as shown in SEQ ID NO: 16, preferably one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N, and wherein the alpha-amylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 16.

Paragraph 153. The yeast strain of paragraph 151 , wherein the alpha-amylase is Aspergillus terreus alpha-amylase selected from the group consisting of:

(i) an alpha-amylase comprising the polypeptide of SEQ ID NO: 6 of WO2017/087330;

(ii) an alpha-amylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 6 of WO2017/087330.

Paragraph 154. A process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism; wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 155. The process of paragraph 155, wherein the fermenting organism has at least one or more, such as all, of the following properties and defining characteristics:

increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein; and/or

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein.

Paragraph 156. The process of paragraph 154 or 155, wherein the fermenting organism provides an ethanol yield boost over Saccharomyces cerevisiae strain Ethanol Red®

(deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) of more than 0.5%, e.g., more than 1.0%, more than 2.0%, more than 2.5%, such as about 2.9%, such as between 0.5 and 5%, such as between 1-3%, under the same process conditins, e.g., conditions as described herein.

Paragraph 157. The process of any of paragraphs 154-156, wherein the fermenting organism reduces acetaldehyde production more than 10%, e.g., more than 20%, more than 30%, more than 40%, more than 45%, such as 5-60%, such as 30-50%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein.

Paragraph 158. The process of any of paragraphs 154-157, wherein the fermenting organism increases temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., process conditions described herein. Paragraph 159. The process of any of paragraphs 154-158, wherein the fermenting organism decreases glycerol production by more than 3%, e.g., more than 4%, more than 5%, more than 6%, more than 7%, such as 2-15%, such as 5-10%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 160. The process of any of paragraphs 154-159, wherein the fermenting organism:

(a) produces a higher titre of ethanol in the first 20 hours of fermentation than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia), under the same conditions in a corn mash fermentation, e.g., conditions described herein;

(b) leaves less glucose remaining following 50 hours of fermentation than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia), under the same conditions in a corn mash fermentation, e.g., conditions described herein;

(c) has a higher ethanol yield than Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) following 50 hours of fermentation under the same conditions in a corn mash fermentation, e.g., conditions described herein.

Paragraph 161. The process of any of paragraphs 154-160, wherein a protease is added in saccharification or fermentation or SSF.

Paragraph 162. The process of any of paragraphs 154-161 , further comprises, prior to the liquefaction step i), the steps of:

x) reducing the particle size of the starch-containing material, preferably by dry milling; y) forming a slurry comprising the starch-containing material and water.

Paragraph 163. The process of any of paragraphs 154-162, wherein at least 50%, e.g., at least 70%, at least 80%, at least 90% of the starch-containing material fits through a sieve with # 6 screen.

Paragraph 164. The process of any of paragraphs 154-163, wherein the pH in liquefaction is between 4-7, such as pH 4.5-6.5, such as pH 5.0-6.5, such as pH 5.0-6.0, such as pH 5.2-6.2, such as about 5.2, such as about 5.4, such as about 5.6, such as about 5.8. Paragraph 165. The process of any of paragraphs 154-164, wherein the temperature in liquefaction is in the range of 70-100°C, such as 75-95°C, 75-90°C, 80-90°C, or 82-88°C, such as about 85°C.

Paragraph 166. The process of any of paragraphs 154-165, wherein a jet-cooking step is carried out prior to liquefaction in step i).

Paragraph 167. The process of paragraph 166, wherein the jet-cooking is carried out at a temperature of 1 10-145°C, e.g, 120-140°C, such as 125-135°C, or about 130°C for about 1- 15 minutes, e.g., for about 3-10 minutes, or about 5 minutes.

Paragraph 168. The process of any of paragraphs 154-167, wherein saccharification and fermentation is carried out sequentially or simultaneously (SSF).

Paragraph 169. The process of any of paragraphs 154-168, wherein saccharification is carried out at a temperature from 20-75°C, e.g., from 40-70°C, such as about 60°C, and at a pH between 4 and 5.

Paragraph 170. The process of any of paragraphs 154-169, wherein fermentation or simultaneous saccharification and fermentation (SSF) is carried out carried out at a temperature from 25°C to 40°C, such as from 28°C to 35°C, such as from 30°C to 34°C, or about 32°C. In one embodiment, fermentation is ongoing for 6 to 120 hours, in particular 24 to 96 hours.

Paragraph 171. The process of any of paragraphs 154-170, wherein the fermentation product is recovered after fermentation, such as by distillation.

Paragraph 172. The process of any of paragraphs 154-171 , wherein the fermentation product is an alcohol, preferably ethanol, especially fuel ethanol, potable ethanol and/or industrial ethanol.

Paragraph 173. The process of any of paragraphs 154-172, wherein the starch-containing starting material is whole grains. Paragraph 174. The process of any of paragraphs 154-173, wherein the starch-containing material is derived from corn, wheat, barley, rye, milo, sago, cassava, manioc, tapioca, sorghum, oats, rice or potatoes.

Paragraph 175. The process of any of paragraphs 154-174, wherein the alpha-amylase used or added in liquefaction step i) is of bacterial origin.

Paragraph 176. The process of any of paragraphs 154-175, wherein the alpha-amylase is from the genus Bacillus, such as a strain of Bacillus stearothermophilus, in particular a variant of a Bacillus stearothermophilus alpha-amylase, such as the one shown in SEQ ID NO: 3 in WO 99/019467 or SEQ ID NO: 1 herein.

Paragraph 177. The process of paragraph 176, wherein the Bacillus stearothermophilus alpha-amylase or variant thereof is truncated at the C-terminal, preferably to be from 485-495 amino acids long, such as about 491 amino acids long.

Paragraph 178. The process of any of paragraphs 176 or 177, wherein the Bacillus stearothermophilus alpha-amylase has a double deletion at positions 1181 + G182, and optionally substitution N193F, or deletion of R179 + G180 (using SEQ ID NO: 1 for numbering).

Paragraph 179. The process of any of paragraphs 176-178, wherein the Bacillus stearothermophilus alpha-amylase has a substitution in position S242, e.g., S242Q substitution (using SEQ ID NO: 1 for numbering).

Paragraph 180. The process of any of paragraphs 176-179, wherein the Bacillus stearothermophilus alpha-amylase has a substitution in position E188, e.g., E188P substitution (using SEQ ID NO: 1 for numbering).

Paragraph 181. The process of any of paragraphs 154-180, wherein the alpha-amylase has a T½ (min) at pH 4.5, 85°C, 0.12 mM CaC ) of at least 10, such as at least 15, such as at least 20, such as at least 25, such as at least 30, such as at least 40, such as at least 50, such as at least 60, such as 10-70, such as 15-70, such as 20-70, such as 25-70, such as 30-70, such as 40-70, such as 50-70, such as 60-70.

Paragraph 182. The process of any of paragraphs 154-181 , wherein the alpha-amylase present and/or added in liquefaction step i) is selected from the group of Bacillus stearothermophilus alpha-amylase variants with one of the following substitutions or combinations of substitutions in addition to I 181*+G182*, and optionally substitution N193F: V59A+Q89R+G1 12D+E129V+K177L+R179E+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+D269E+D281 N;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+I270L;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+H274K;

V59A+Q89R+E129V+K177L+R179E+K220P+N224L+Q254S+Y276F;

V59A+E129V+R157Y+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+H208Y+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+H274K;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+D281 N;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

V59A+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+G416V;

V59A+E129V+K177L+R179E+K220P+N224L+Q254S;

V59A+E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

A91 L+M96I+E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+Y276F+L427M;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+M284T;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S+N376*+I377*;

E129V+K177L+R179E+K220P+N224L+Q254S;

E129V+K177L+R179E+K220P+N224L+Q254S+M284T;

E129V+K177L+R179E+S242Q;

E129V+K177L+R179V+K220P+N224L+S242Q+Q254S;

K220P+N224L+S242Q+Q254S;

M284V;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V; and

V59A+E129V+K177L+R179E+Q254S+ M284V;

Paragraph 183. The process of any of paragraphs 154-182, wherein the alpha-amylase present and/or added in liquefaction step i) is selected from the following group of Bacillus stearothermophilus alpha-amylase variants comprising the following mutations: I 181*+G182*, and optionally substitution N193F, and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S

V59A+ Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+ E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

Paragraph 184. The process of any of paragraphs 154-183, wherein a glucoamylase is present and/or added in saccharification and/or fermentation.

Paragraph 185. The process of paragraph 184, wherein the glucoamylase present and/or added in saccharification, fermentation or simultaneous saccharification and fermentation (SSF) is of fungal origin, preferably from a strain of Aspergillus, preferably A. niger, A. awamori, or A. oryzae ; or a strain of Trichoderma, preferably Trichoderma reesel·, or a strain of Talaromyces, preferably Talaroomyces emersonii, or a strain of Pycnoporus, or a strain of Gloeophyllum, such as Gloeophyllum serpiarium or Gloeophyllum trabeum, or a strain of the Nigrofomes.

Paragraph 186. The process of any of paragraphs 154-185, wherein the glucoamylase is derived from Talaromyces emersonii, such as the one shown in SEQ ID NO: 19 herein.

Paragraph 187. The process of any of paragraphs 154-186, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 19 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 19 herein.

Paragraph 188. The process of any of paragraphs 154-187, wherein the glucoamylase present and/or added in saccharification is derived from Gloeophyllum serpiarium, such as the one shown in SEQ ID NO: 15 herein.

Paragraph 189. The process of any of paragraphs 154-188, wherein the glucoamylase present and/or added in saccharification is selected from the group consisting of: (i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 15 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 15 herein.

Paragraph 190. The process of any of paragraphs 154-189, wherein the glucoamylase present and/or added in saccharification is derived from Gloeophyllum trabeum such as the one shown in SEQ ID NO: 17 herein.

Paragraph 191. The process of any of paragraphs 154-190, wherein the glucoamylase present and/or added in saccharification is selected from the group consisting of:

(i) a glucoamylase comprising the mature polypeptide of SEQ ID NO: 17 herein;

(ii) a glucoamylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 17 herein.

Paragraph 192. The process of any of paragraphs 154-191 , wherein the glucoamylase is present and/or added in saccharification and/or fermentation in combination with an alpha- amylase.

Paragraph 193. The process of paragraph 192, wherein the alpha-amylase is present and/or added in saccharification and/or fermentation is of fungal or bacterial origin.

Paragraph 194. The process of paragraph 192 or 193, wherein the alpha-amylase present and/or added in saccharification and/or fermentation is derived from a strain of the genus Rhizomucor, preferably a strain the Rhizomucor pusillus, such as the one shown in SEQ ID NO: 3 in WO 2013/006756, such as a Rhizomucor pusillus alpha-amylase hybrid having a linker and a starch-binding domain, in particular having an Aspergillus niger linker and starch bonding domain, such as the one shown in SEQ ID NO: 16 herein.

Paragraph 195. The process of any of paragraphs 192-194, wherein the alpha-amylase present and/or added in saccharification and/or fermentation is selected from the group consisting of:

(i) an alpha-amylase comprising the mature polypeptide of SEQ ID NO: 16 herein; (ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the mature polypeptide of SEQ ID NO: 16 herein.

Paragraph 196. The process of any of paragraphs 192-195, wherein the alpha-amylase is a variant of the alpha-amylase shown in SEQ ID NO: 16 having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H + Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; and G128D + Y141W + D143N + K192R; or G128D + Y141 W+ D143N + K192R + P219C (using SEQ ID NO: 16 for numbering).

Paragraph 197. The process of any of paragraphs 192-196, wherein the alpha-amylase is derived from a Rhizomucor pusillus with an Aspergillus n/ger glucoamylase linker and starch binding domain (SBD), preferably disclosed as SEQ ID NO: 16 herein, e.g., having one or more of the following substitutions: G128D, D143N, such as G128D+D143N (using SEQ ID NO: 16 for numering).

Paragraph 198. The process of any of paragraphs 192-197, wherein the alpha-amylase variant has at least 75% identity preferably at least 80%, e.g., at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 16 herein.

Paragraph 199. The process of any of paragraphs 154-198, wherein liquefaction step i) is carried out using:

an alpha-amylase;

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C; and

optionally a glucoamylase.

Paragraph 200. The process of 199, wherein the protease with a thermostability value of more than 25% determined as Relative Activity at 80°C/70°C. Paragraph 201. The process of paragraph 199 or 200, wherein the protease has a thermostability of more than 30%, e.g., more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, such as more than 105%, such as more than 1 10%, such as more than 1 15%, such as more than 120% determined as Relative Activity at 80°C/70°C.

Paragraph 202. The process of any of paragraphs 199-201 , wherein the protease has a thermostability of between 20 and 50%, such as between 20 and 40%, such as 20 and 30% determined as Relative Activity at 80°C/70°C.

Paragraph 203. The process of any of paragraphs 199-202, wherein the protease has a thermostability of between 50 and 115%, such as between 50 and 70%, such as between 50 and 60%, such as between 100 and 120%, such as between 105 and 1 15% determined as Relative Activity at 80°C/70°C.

Paragraph 204. The process of any of paragraphs 199-203, wherein the protease has a thermostability of more than 10%, e.g., more than 12%, more than 14%, more than 16%, more than 18%, more than 20%, more than 30%, more than 40%, more that 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, more than 110% determined as Relative Activity at 85°C/70°C.

Paragraph 205. The process of any of paragraphs 199-204, wherein the protease has a thermostability of between 10 and 50%, such as between 10 and 30%, such as between 10 and 25% determined as Relative Activity at 85°C/70°C.

Paragraph 206. The process of any of paragraphs 199-205, wherein the protease has a themostability above 60%, such as above 90%, such as above 100%, such as above 110% at 85°C as determined using the Zein-BCA assay.

Paragraph 207. The process of any of paragraphs 199-206, wherein the protease has a themostability between 60-120, such as between 70-120%, such as between 80-120%, such as between 90-120%, such as between 100-120%, such as 1 10-120% at 85°C as determined using the Zein-BCA assay.

Paragraph 208. The process of any of paragraphs 199-207, wherein the protease is of fungal origin. Paragraph 209. The process of any of paragraphs 199-208, wherein the protease is a variant of the metallo protease derived from a strain of the genus Thermoascus, preferably a strain of Thermoascus aurantiacus, especially Thermoascus aurantiacus CGMCC No. 0670.

Paragraph 210. The process of any of paragraphs 199-209, wherein the protease is a variant of the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in W02003/048353 or the mature part of SEQ ID NO: 1 in WO2010/008841 or SEQ ID NO: 3 herein, with one of the following substitutions or combinations of substitutions:

S5*+D79L+S87P+A112P+D142L;

D79L+S87P+A112P+T 124V+D142L;

S5*+N26R+D79L+S87P+A1 12P+D142L;

N26R+T46R+D79L+S87P+A1 12P+D142L;

T46R+D79L+S87P+T 1 16V+D142L;

D79L+P81 R+S87P+A1 12P+D142L;

A27K+ D79L+S87P+A 112 P+T 124V+ D 142 L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+Y82F+S87P+A1 12P+T124V+D142L;

D79L+S87P+A112P+T 124V+A126V+D142L;

D79L+S87P+A112P+D142L;

D79L+Y82F+S87P+A1 12P+D142L;

S38T+D79L+S87P+A1 12P+A126V+D142L;

D79L+Y82F+S87P+A1 12P+A126V+D142L;

A27K+ D79L+S87P+A 112 P+A 126V+ D142L;

D79L+S87P+N98C+A112P+G135C+D142L;

D79L+S87P+A112P+D142L+T141 C+M161 C;

S36P+D79L+S87P+A112P+D142L;

A37P+D79L+S87P+A112P+D142L;

S49P+D79L+S87P+A112P+D142L;

S50P+D79L+S87P+A112P+D142L;

D79L+S87P+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+D142L;

S70V+ D79 L+Y82 F+S87G+ Y97W+A 112 P+ D 142 L;

D79L+Y82F+S87G+Y97W+D104P+A112P+D142L;

S70V+ D79 L+Y82 F+S87G+ A 1 12 P+ D 142 L;

D79L+Y82F+S87G+D104P+A112P+D142L;

D79L+Y82F+S87G+A1 12P+A126V+D142L;

Y82F+S87G+S70V+D79L+D104P+A1 12P+D142L; Y82F+S87G+D79L+D104P+A112P+A126V+D142L;

A27K+ D79L+Y82 F+S87G+D 104P+A1 12 P+A126V+ D 142 L;

A27K+Y82F+S87G+D104P+A112P+A126V+D142L;

A27K+D79L+Y82F+ D104P+A112P+A126V+D142L;

A27K+Y82F+ D 104 P+ A 112 P+ A 126V+ D 142 L;

A27K+D79L+S87P+A112P+D142L; and

D79L+S87P+D142L.

Paragraph 21 1. The process of any of paragraphs 199-210, wherein the protease is a variant of the metallo protease disclosed as the mature part of SEQ ID NO: 2 disclosed in W02003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein with one of the following substitutions or combinations of substitutions:

D79L+S87P+A112P+D142L:

D79L+S87P+D142L; and

A27K+ D79L+ Y82F+S87G+D104P+A112P+A126V+D142L.

Paragraph 212. The process of any of paragraphs 199-21 1 , wherein the protease variant has at least 75% identity, e.g., at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 2 disclosed in WO 2003/048353 or the mature part of SEQ ID NO: 1 in WO 2010/008841 or SEQ ID NO: 3 herein.

Paragraph 213. The process of any of paragraphs 199-212, wherein the protease variant of the Thermoascus aurantiacus protease shown in SEQ ID NO: 3 herein comprises one of the following substitutions or combinations of substitutions:

D79L S87P D142L; D79L S87P A1 12P D142L; D79L Y82F S87P A112P D142L; S38T D79L S87P A1 12P A 126V D142L; D79L Y82F S87P A1 12P A126V D142L; A27K D79L S87P A1 12P A 126V D142L; S49P D79L S87P A1 12P D142L; S50P D79L S87P A112P D142L; D79L S87P D104P A1 12P D142L; D79L Y82F S87G A1 12P D142L; S70V D79L Y82F S87G Y97W A1 12P D142L; D79L Y82F S87G Y97W D104P A112P D142L; S70V D79L Y82F S87G A1 12P D142L; D79L Y82F S87G D104P A1 12P D142L; D79L Y82F S87G A112P A126V D142L; Y82F S87G S70V D79L D104P A1 12P D142L; Y82F S87G D79L D104P A1 12P A 126V D142L; and A27K D79L Y82F S87G D104P A112P A126V D142L.

Paragraph 214. The process of any of paragraphs 199-213, wherein the protease is of bacterial origin. Paragraph 215. The process of any of paragraphs 199-214, wherein the protease is derived from a strain of Pyrococcus, preferably a strain of Pyrococcus furiosus.

Paragraph 216. The process of any of paragraphs 199-215, wherein the protease is the one shown in SEQ ID NO: 1 in US 6,358,726, or SEQ ID NO: 13 herein.

Paragraph 217. The process of any of paragraphs 199-216, wherein the protease is one having at least 80%, e.g., at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99% identity to in SEQ ID NO: 1 in US 6,358,726 or SEQ ID NO: 13 herein.

Paragraph 218. The process of any of paragraph 199-217, wherein 0.5-100 micro gram Pyrococcus furiosus protease per gram DS, such as 1-50 micro gram Pyrococcus furiosus protease per gram DS, such as 1-10 micro gram Pyrococcus furiosus protease per gram DS, such as 1.5-5 micro gram Pyrococcus furiosus protease per gram DS, such as about or more than 1.5 micro gram Pyrococcus furiosus protease per gram DS are present and/or added in liquefaction step i).

Paragraph 219. The process of any of paragraphs 199-218, wherein 2-100 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-50 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-10 micro gram Pyrococcus furiosus protease per gram DS, such as 2.5-5 micro gram Pyrococcus furiosus protease gram DS, especially about 3 micro gram Pyrococcus furiosus protease per gram DS are present and/or added in liquefaction step i).

Paragraph 220. The process of any of paragraphs 154-219, wherein a glucoamylase is present and/or added during liquefaction step i).

Paragraph 221. The process of paragraph 220, wherein the glucoamylase present and/or added in liquefaction has a heat stability at 85°C, pH 5.3, of at least 20%, such as at least 30%, or at least 35%.

Paragraph 222. The process of paragraph 220 or 221 , wherein the glucoamylase present and/or added in liquefaction has a relative activity pH optimum at pH 5.0 of at least 90%, preferably at least 95%, preferably at least 97%. Paragraph 223. The process of any of paragraphs 220-222, wherein the glucoamylase present and/or added in liquefaction has pH stability at pH 5.0 of at least at least 80%, at least 85%, at least 90%.

Paragraph 224. The process of any of paragraphs 220-223, wherein the glucoamylase present and/or added in liquefaction step i) is derived from a strain of the genus Penicillium, especially a strain of Penicillium oxalicum disclosed as SEQ ID NO: 2 in WO 201 1/127802 or SEQ ID NOs: 9 or 14 herein.

Paragraph 225. The process of any of paragraphs 220-224, wherein the glucoamylase has at least 80%, more preferably at least 85%, more preferably at least 90%, more preferably at least 91 %, more preferably at least 92%, even more preferably at least 93%, most preferably at least 94%, and even most preferably at least 95%, such as even at least 96%, at least 97%, at least 98%, at least 99% or 100% identity to the mature polypeptide shown in SEQ ID NO: 2 in WO 2011/127802 or SEQ ID NOs: 9 or 14 herein.

Paragraph 226. The process of any of paragraphs 220-225, wherein the glucoamylase is a variant of the Penicillium oxalicum glucoamylase shown in SEQ ID NO: 2 in WO 201 1/127802 having a K79V substitution (using the mature sequence shown in SEQ ID NO: 14 herein for numbering), such as a variant disclosed in WO 2013/053801.

Paragraph 227. The process of any of paragraph 220-226, wherein the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 for numbering) and further one of the following substitutions or combinations of substitutions:

T65A; Q327F; E501V; Y504T; Y504*; T65A + Q327F; T65A + E501V; T65A + Y504T; T65A + Y504*; Q327F + E501 V; Q327F + Y504T; Q327F + Y504*; E501V + Y504T; E501V + Y504*; T65A + Q327F + E501V; T65A + Q327F + Y504T; T65A + E501V + Y504T; Q327F + E501V + Y504T ; T65A + Q327F + Y504*; T65A + E501 V + Y504*; Q327F + E501V + Y504*; T65A + Q327F + E501V + Y504T; T65A + Q327F + E501V + Y504*; E501V + Y504T; T65A + K161 S; T65A + Q405T ; T65A + Q327W; T65A + Q327F; T65A + Q327Y; P11 F + T65A + Q327F; R1 K + D3W + K5Q + G7V + N8S + T10K + P1 1S + T65A + Q327F; P2N + P4S + P1 1 F + T65A + Q327F; P11 F + D26C + K33C + T65A + Q327F; P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T; R1 E + D3N + P4G + G6R + G7A + N8A + T10D+ P1 1 D + T65A + Q327F; P11 F + T65A + Q327W; P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; P1 1 F + T65A + Q327W + E501V + Y504T; T65A + Q327F + E501V + Y504T; T65A + S105P + Q327W; T65A + S105P + Q327F; T65A + Q327W + S364P; T65A + Q327F + S364P; T65A + S103N + Q327F; P2N + P4S + P11 F + K34Y + T65A + Q327F; P2N + P4S + P11 F + T65A + Q327F + D445N + V447S; P2N + P4S + P11F + T65A + 1172V + Q327F; P2N + P4S + P11F + T65A + Q327F + N502*; P2N + P4S + P11F + T65A + Q327F + N502T + P563S + K571E; P2N + P4S + P11F + R31S + K33V + T65A + Q327F + N564D + K571S; P2N + P4S + P11F + T65A + Q327F + S377T ; P2N + P4S + P11 F + T65A + V325T+ Q327W; P2N + P4S + P11 F + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11F + T65A + 1172V + Q327F + E501V + Y504T ; P2N + P4S + P11F + T65A + Q327F + S377T + E501V + Y504T; P2N + P4S + P11F + D26N + K34Y + T65A + Q327F; P2N + P4S + P11F + T65A + Q327F + I375A + E501V + Y504T; P2N + P4S + P11F + T65A + K218A + K221D + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + S103N + Q327F + E501V + Y504T; P2N + P4S + T10D + T65A + Q327F + E501V + Y504T; P2N + P4S + F12Y + T65A + Q327F + E501V + Y504T; K5A + P11F + T65A + Q327F + E501V + Y504T; P2N + P4S + T10E + E18N + T65A + Q327F + E501 V + Y504T; P2N + T10E + E18N + T65A + Q327F + E501 V + Y504T; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T + T568N; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T + K524T + G526A; P2N + P4S + P11F + K34Y + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11 F + R31 S + K33V + T65A + Q327F + D445N + V447S + E501V + Y504T; P2N + P4S + P11F + D26N + K34Y + T65A + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + F80* + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + K112S + Q327F + E501 V + Y504T; P2N + P4S + P11 F + T65A + Q327F + E501 V + Y504T + T516P + K524T + G526A; P2N + P4S + P11F + T65A + Q327F + E501V + N502T + Y504*; P2N + P4S+ P11F + T65A + Q327F+ E501V + Y504T; P2N + P4S + P11F + T65A + S103N + Q327F + E501V + Y504T; K5A + P11F + T65A + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + E501V + Y504T + T516P + K524T + G526A; P2N + P4S + P11F + T65A + K79A + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + K79G + Q327F + E501 V + Y504T; P2N + P4S + P11F + T65A + K79I + Q327F + E501 V + Y504T; P2N + P4S + P11F + T65A + K79L + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + K79S + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + L72V + Q327F + E501V + Y504T; S255N + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + E74N + V79K + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + G220N + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Y245N + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Q253N + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + D279N + Q327F + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + S359N + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + D370N + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + V460S + E501V + Y504T; P2N + P4S + P11F + T65A + Q327F + V460T + P468T + E501 V + Y504T; P2N + P4S + P11F + T65A + Q327F + T463N + E501 V + Y504T; P2N + P4S + P11F + T65A + Q327F + S465N + E501V + Y504T; andP2N + P4S + P11F + T65A + Q327F + T477N + E501V + Y504T. Paragraph 228. The process of any of paragraphs 220-227, wherein the glucoamylase present and/or added in liquefaction is the Penicillium oxalicum glucoamylase has a K79V substitution (using SEQ ID NO: 14 herein for numbering) and further one of the following substitutions or combinations of substitutions: P1 1 F + T65A + Q327F; and P2N + P4S + P11 F + T65A + Q327F (using SEQ ID NO: 14 herein for numbering).

Paragraph 229. The process of any of paragraphs 220-228, wherein the glucoamylase variant has at least 75% identity, e.g., at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, at least 99%, but less than 100% identity to the mature part of the polypeptide of SEQ ID NO: 14 herein.

Paragraph 230. The process of any of paragraphs 154-229, further wherein a pullulanase is present during liquefaction and/or saccharification.

Paragraph 231. The process of any of paragraphs 154-230, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus ; ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 232. The process of any of paragraphs 154-231 , comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution (using SEQ ID NO: 1 herein for numbering);

ii) saccharifying using a glucoamylase derived from a strain of Gloephyllum, such as Gloephyllum serpiarium or Gloephyllum trabeum.

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 233. The process of any of paragraphs 154-232, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus ;

a protease having a thermostability value of more than 20% determined as Relative

Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or

Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 234. A process of paragraphs 154-233, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase, preferably derived from Bacillus stearothermophilus, comprising a double deletion at positions 1181 + G182, and optionally a N193F substitution (using SEQ ID NO: 1 for numbering) and having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCI ₂ of at least 10;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012. Paragraph 235. A process of paragraphs 154-234, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase, preferably derived from Bacillus stearothermophilus, having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCL of at least 10;

a protease, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus, having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C; and

optionally a Penicillium oxalicum glucoamylase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 236. A process of paragraphs 154-235, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions: E129V+K177L+R179E; V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V;

and E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

ii) saccharifying using a glucoamylase, such as one from a strain of Gloephyllum, such as a strain of Gloephyllum serpiarium ;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012. Paragraph 237. A process of paragraphs 154-236, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F, and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+E129V+K177L+R179E+Q254S+M284V;

V59A+ E129V+ K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ; and

optionally a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 238. A process of paragraphs 154-237, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optionally substitution N193F, and further optionally one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+K177L+R179E+Q254S+M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering),

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 239. The process of any of paragraphs 154-238, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optionally substitution N193F (using SEQ ID NO: 1 herein for numbering); a protease having a thermostability value of more than 20% determined as

Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or

Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase having a K79V substilution (using SEQ

ID NO: 14 herein for numbering); and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 240. A process of paragraphs 154-239, comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using:

an alpha-amylase, preferably derived from Bacillus stearothermophilus, having a T½

(min) at pH 4.5, 85°C, 0.12 mM CaCL of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus, preferably A. niger, A. awamori, or A. oryzae\ or a strain of Trichoderma, preferably T. reesel·, or a strain of Talaromyces, preferably T. emersonii, or a strain of Pycnoporus, or a strain of Gloephyllum, such as G. serpiarium or G. trabeum, or a strain of the Nigrofomes;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 241. A process of paragraphs 154-240, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using; an alpha-amylase, preferably derived from Bacillus stearothermophilus having a double deletion at positions 1181 + G182, and optional substitution N193F and having a T½ (min) at pH 4.5, 85°C, 0.12 mM CaCh of at least 10;

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS;

a Penicillium oxalicum glucoamylase; and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 242. A process of paragraphs 154-241 , comprising the steps of:

i) liquefying the starch-containing material at a temperature a temperature between 80-

90°C using;

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

between 0.5 and 10 micro grams Pyrococcus furiosus protease per g DS; a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F;

K79V+P2N + P4S + P11 F + T65A + Q327F;

K79V +P11 F + D26C + K33C + T65A + Q327F;

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; and K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering); and

optionally a pullulanase;

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 243. A process of paragraphs 154-242, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C using: an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182, and optional substitution N193F; and further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+C89R+E129V+K177L+R179E+H208Y+K220P+N224L+C254S;

V59A+C89R+ E129V+ K177L+ R179E+ C254S+ M284V;

V59A+E129V+ K177L+ R179E+ C254S+ M284V; and

E129V+K177L+R179E+K220P+N224L+S242C+C254S (using SEC ID NO: 1 herein for numbering);

a protease having a thermostability value of more than 20% determined as Relative Activity at 80°C/70°C, preferably derived from Pyrococcus furiosus and/or Thermoascus aurantiacus ;

a Penicillium oxalicum glucoamylase shown in SEC ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + C327F;

K79V+P2N + P4S + P11 F + T65A + C327F;

K79V +P11 F + D26C + K33C + T65A + C327F;

K79V +P2N + P4S + P11 F + T65A + C327W + E501V + Y504T;

K79V +P2N + P4S + P11 F + T65A + C327F + E501V + Y504T; and

K79V +P11 F + T65A + C327W + E501V + Y504T (using SEC ID NO: 14 for numbering); and

optionally a pullulanase; ii) saccharifying using a glucoamylase selected from the group of glucoamylase derived from a strain of Aspergillus ; or a strain of Trichoderma; a strain of Talaromyces, a strain of Pycnoporus ; a strain of Gloephyllum; and a strain of the Nigrofomes;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 244. A process of any of paragraphs 154-243, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182 and optionally substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering);

a protease derived from Pyrococcus furiosus, preferably the one shown in SEQ ID NO: 13 herein;

a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F; or

K79V+P2N + P4S + P11 F + T65A + Q327F; or

K79V +P11 F + D26C + K33C + T65A + Q327F; or

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T; or

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; or

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering);

ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism; wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 245. The process of any of paragraphs 154-244, wherein a cellulolytic enzyme composition is present in saccharification, fermentation or simultaneous saccharification and fermentation (SSF).

Paragraph 246. The process of any of paragraphs 154-245, wherein the fermenting organism has properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012, or a derivative of Saccharomyces cerevisiae strain MBG5012 having the defining characteristics of Saccharomyces cerevisiae strain MBG5012, as it provides one or more, such as all of, the following properties or defining characteristics

an increase in ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions e.g., as described herein; and/or

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., as described herein.

Paragraph 247. The process of any of paragraphs paragraph 154-246, wherein the fermenting organism, provides an ethanol yield boost over Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) of more than 0.5%, e.g., more than 1.0%, more than 2.0%, more than 2.5%, about 2.9%, such as between 0.5 and 5%, such as 1-3%, under the same process conditins, e.g., conditions described herein.

Paragraph 248. The process of any of paragraphs 154-247, wherein the fermenting organism reduces acetaldehyde production more than 10%, e.g., more than 20%, more than 30%, more than 40%, more than 45%, such as 5-60%, such as 30-50%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein. Paragraph 249. The process of any of paragraphs 154-248, wherein the fermenting organism increases temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 250. The process of any of paragraphs 154-249, wherein the fermenting organism decreases glycerol production by more than 3%, e.g., more than 4%, more than 5%, more than 6%, more than 7%, such as 2-15%, such as 5-10%, compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions described herein.

Paragraph 251. The process of any of paragraphs 154-250, wherein the fermenting organism is a non-recombinant Saccharomyces strain, e.g., a non-recombinant Saccharomyces cerevisiae strain.

Paragraph 252. The process of any of paragraphs 154-251 , wherein the fermenting organism is capable of utilizing cysteine as the sole nitrogen source.

Paragraph 253. A process for producing ethanol from starch-containing material comprising the steps of:

i) liquefying the starch-containing material at a temperature above the initial gelatinization temperature using an alpha-amylase derived from Bacillus stearothermophilus ; ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism has one or more, such as all, of the following properties and defining characteristics:

increases ethanol yield compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

reduced acetaldehyde production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

increased temperature tolerance compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein;

decreased glycerol production compared to Saccharomyces cerevisiae strain Ethanol Red® (deposited under Accession No. V14/007039 at National Measurement Institute, Victoria, Australia) under the same process conditions, e.g., conditions as described herein.

Paragraph 254. The process of paragraph 253, wherein the fermenting organism is a Saccharomyces cerevisiae yeast

Paragraph 255. The process of paragraphs 253 or 254, wherein the fermenting organism is a non-recombinant Saccharomyces cerevisiae yeast.

Paragraph 256. A process of any of paragraphs 154-255, comprising the steps of:

i) liquefying the starch-containing material at a temperature between 80-90°C at a pH between 5.0 and 6.5 using:

an alpha-amylase derived from Bacillus stearothermophilus having a double deletion 1181 + G182, and optional substitution N193F; and optionally further one of the following substitutions or combinations of substitutions:

E129V+K177L+R179E;

V59A+Q89R+E129V+K177L+R179E+H208Y+K220P+N224L+Q254S;

V59A+Q89R+ E129V+ K177L+ R179E+ Q254S+ M284V;

V59A+E129V+ K177L+ R179E+ Q254S+ M284V;

E129V+K177L+R179E+K220P+N224L+S242Q+Q254S (using SEQ ID NO: 1 herein for numbering).

a protease derived from Pyrococcus furiosus, preferably the one shown in SEQ ID NO: 13 herein present and/or added in a dosage of 1-5 micro gram protease per gram DS, such as about 1.5 or 3 micro gram protease per gram DS;

optionally a Penicillium oxalicum glucoamylase shown in SEQ ID NO: 14 having one of the following substitutions or combinations of substitutions:

K79V;

K79V+ P11 F + T65A + Q327F; or

K79V+P2N + P4S + P11 F + T65A + Q327F; or

K79V +P11 F + D26C + K33C + T65A + Q327F; or

K79V +P2N + P4S + P11 F + T65A + Q327W + E501V + Y504T; or

K79V +P2N + P4S + P11 F + T65A + Q327F + E501V + Y504T; or

K79V +P11 F + T65A + Q327W + E501V + Y504T (using SEQ ID NO: 14 for numbering); ii) saccharifying using a glucoamylase;

iii) fermenting using a fermenting organism;

wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 257. The process of any of paragraphs 153-256, wherein the fermenting organism is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative of Saccharomyces strain MBG5012 having defining characteristics of strain MBG5012.

Paragraph 258. The process of paragraphs 257, wherein a protease is present or added in saccharification and/or fermentation or simultaneous saccharification and fermentation (SSF).

Paragraph 259. A Saccharomyces yeast strain deposited under the Budapest Treaty and having NRRL accession no. NRRL Y67700, or a derivative of strain NRRL Y67700.

Paragraph 260. A method of producing a derivative of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA), comprising:

d. culturing a first yeast strain with a second yeast strain, wherein the second yeast strain is Saccharomyces cerevisiae strain MBG5012 or a derivative thereof, under conditions which permit combining of DNA between the first yeast strain and the second yeast strain; and

e. isolating hybrid strains; and

f. optionally repeating steps (a) and (b) using a hybrid strain isolated in step (b) as the first yeast strain and/or the second yeast strain.

Paragraph 261. A method of producing a derivative of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) which exhibits the defining characteristics of

Saccharomyces cerevisiae strain MBG5012, comprising:

(d) providing:

(j) a first yeast strain; and

(iii) a second yeast strain, wherein the second yeast strain is

Saccharomyces cerevisiae strain MBG5012 or a derivative thereof;

(e) culturing the first yeast strain and the second yeast strain under conditions which permit combining of DNA between the first and second yeast strains;

(f) screening or selecting for a derivative of Saccharomyces cerevisiae strain MBG5012.

Paragraph 262. The method of paragraph 261 , wherein step (c) comprises screening or selecting for a hybrid strain which exhibits one or more defining characteristic of

Saccharomyces cerevisiae strain MBG5012.

Paragraph 263. The method of paragraph 261 , comprising the further step of:

(d) repeating steps (b) and (c) with the screened or selected strain from step (c) as the first and/or second strain, until a derivative is obtained which exhibits the defining characteristics of Saccharomyces cerevisiae strain MBG5012.

Paragraph 264. The method of paragraph 262 or 263, wherein the culturing step (b) comprises:

(i) sporulating the first yeast strain and the second yeast strain;

(ii) hybridizing germinated spores produced by the first yeast strain with germinated spores produced by the second yeast strain.

Paragraph 265. A Saccharomyces strain produced by the method of any one of paragraphs 260-264.

Paragraph 266. A Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

Paragraph 267. A method of producing ethanol, comprising incubating a strain of any of paragraphs 259, 265 or 266 with a substrate comprising a fermentable sugar under conditions which permit fermentation of the fermentable sugar to produce ethanol. Paragraph 268. Use of a strain of any of paragraphs 259, 265 or 266 in the production of ethanol.

Paragraph 269. A method of producing distiller’s grain, comprising:

(c) incubating a Saccharomyces strain of any of paragraphs 259, 265 or 266 with a substrate comprising fermentable sugar under conditions which allow fermentation of the fermentable sugar to produce ethanol and distiller’s grains;

(d) isolating the distiller’s grains.

Paragraph 270. Distiller’s grain produced by the method of paragraph 269.

Paragraph 271. Use of a strain of paragraph 259, 265 or 266 in the production of distiller’s grains.

Paragraph 272. Use of a strain of paragraphs 259, 265 or 266 in the production of a Saccharomyces strain having the defining characteristics of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

Paragraph 273. Use of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) in the production of a Saccharomyces strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or which exhibits one or more defining characteristics of Saccharomyces cerevisiae strain MBG5012.

Paragraph 274. Use of Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a strain having properties that are about the same as that of Saccharomyces cerevisiae strain MBG5012 or a derivative thereof in a process according to any of paragraphs 154-273.

Paragraph 275. A composition comprising a Saccharomyces yeast of any of paragraphs 259, 265 or 266 and one or more naturally occurring and/or non-naturally occurring components. Paragraph 276. The composition of paragraph 275, wherein the components are selected from the group consisting of: surfactants, emulsifiers, gums, swelling agents, and antioxidants.

Paragraph 277. The composition of paragraph 275 or 276, wherein the Saccharomyces yeast is Saccharomyces cerevisiae strain MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA).

Paragraph 278. The composition of any of paragraphs 275-277, wherein the Saccharomyces yeast is in a viable form, in particular in dry, cream or compressed form.

Paragraph 279. A process of producing ethanol from starch-containing material comprising:

(a) saccharifying the starch-containing material; and

(b) fermenting using a fermentation organism;

wherein

saccharification and/or fermentation is done in the presence of at least a glucoamylase and optionally an alpha-amylase;

the fermenting organism is Saccharomyces cerevisiae;

and wherein a glucoamylase and/or an alpha-amylase is expressed from the fermenting organism.

Paragraph 280. The process according to paragraph 279, wherein the starch containing material is either gelatinized or ungelatinized starch.

Paragraph 281. The process according to paragraph 280, wherein a liquefaction step precedes the saccharification step, and wherein the liquefaction step is performed in the presence of at least a bacterial alpha-amylase, such as an alpha-amylase from Bacillus sp., particularly Bacillus stearothermophilus.

Paragraph 282. The process according to any of paragraphs 279-281 , wherein the Saccharomyces cerevisiae is MBG5012 (deposited under Accession No. NRRL Y67700 at the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA) or a fermenting organism having properties that are about the same as that of MBG5012 or a derivative of MBG5012 having defining characteristics of strain MBG5012.

Paragraph 283. The process of paragraphs 279-282, wherein the fermenting organism is a recombinant derivative of MBG5012 that expresses the glucoamylase.

Paragraph 284. The process of paragraphs 279-283, wherein the glucocamylase is a Gloeophyllum glucoamylase, preferably Gloeophyllum trabeum, Gloeophyllum sepiarium, or Gloeophyllum abietinum glucoamylase.

Paragraph 285. The process of paragraphs 279-284, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17.

Paragraph 286. The process of paragraph 284 or 285, wherein the glucoamylase is the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 having one of the following substitutions: V59A; S95P; A121 P; T1 19W; S95P+A121 P; V59A+S95P; S95P+T1 19W; V59A+S95P+A121 P; or S95P+T119W+A121 P, especially S95P+A121 P.

Paragraph 287. The process of any of paragraphs 279-283, wherein the glucoamylase is expressed from the fermenting organism and is a Trametes glucoamylase, preferably a Trametes cingulata glucoamylase.

Paragraph 288. The process of paragraph 287, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 20;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 20.

Paragraph 289. The process of any of paragraphs 279-283, wherein the glucoamylase is expressed from the fermenting organism and is a Pycnoporus glucoamylase, particularly Pycnoporus sanguineus glucoamylase.

Paragraph 290. The process of paragraph 289, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 18; (ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 18.

Paragraph 291. The process of any of paragraphs 279-290, wherein the fermenting organism is a recombinant derivative of MBG5012 that expresses the alpha-amylase.

Paragraph 292. The process of paragraphs 279-291 , wherein the alpha-amylase expressed from the fermenting organism and is derived from Rhizomucor pusillus or Aspergillus terreus.

Paragraph 293. The process of paragraph 292, wherein the alpha-amylase is Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) as shown in SEQ ID NO: 16, preferably one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N, and wherein the alpha-amylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 16.

Paragraph 294. The process of paragraph 292, wherein the alpha-amylase is an Aspergillus terreus alpha-amylase selected from the group consisting of:

(i) an alpha-amylase comprising the polypeptide of SEQ ID NO: 6 of WO2017/087330;

(ii) an alpha-amylase comprising an amino acid sequence having at least 60%, at least 70%, e.g., at least 75%, at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 6 of WO2017/087330.

Paragraph 295. A Saccharomyces cerevisiae yeast strain, wherein the strain is a derivative of MBG5012 comprising one or more expression vectors encoding a glucoamylase and/or an alpha-amylase. Paragraph 296. The yeast strain according to paragraph 295, wherein the glucoamylase is selected from glucoamylases obtainable from Gloeophyllum, Pycnoporous, or Trametes.

Paragraph 297. The yeast strain according to paragraph 296, wherein the glucoamylase is selected from a Gloeophyllum trabeum, Gloeophyllum sepiarium, or Gloeophyllum abietinum glucoamylase.

Paragraph 298. The yeast strain of paragraph 297, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 15 or SEQ ID NO: 17.

Paragraph 299. The yeast strain of any of paragraphs 296-298, wherein the glucoamylase is the Gloeophyllum trabeum glucoamylase shown in SEQ ID NO: 17 having one of the following substitutions: V59A; S95P; A121 P; T1 19W; S95P+A121 P; V59A+S95P; S95P+T1 19W; V59A+S95P+A121 P; or S95P+T119W+A121 P, especially S95P+A121 P.

Paragraph 300. The yeast strain of paragraph 296, wherein the glucoamylase is a Trametes cingulata glucoamylase.

Paragraph 301. The yeast strain of paragraph 300, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 20;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 20.

Paragraph 302: The yeast strain of paragraph 296, wherein the glucoamylase is s a Pycnoporus sanguineus glucoamylase.

Paragraph 303. The yeast strain of paragraph 302, wherein the glucoamylase is selected from the group consisting of:

(i) a glucoamylase comprising the polypeptide of SEQ ID NO: 18;

(ii) a glucoamylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 18.

Paragraph 304. The yeast strain of paragraph 295 expression vectorwherein the alpha- amylase is selected from a Rhizomucor pusillus or Aspergillus terreus alpha-amylase.

Paragraph 305. The yeast strain of paragraph 304, wherein the alpha-amylase is Rhizomucor pusillus alpha-amylase with an Aspergillus niger glucoamylase linker and starch-binding domain (SBD) as shown in SEQ ID NO: 16, preferably one having at least one of the following substitutions or combinations of substitutions: D165M; Y141W; Y141 R; K136F; K192R; P224A; P224R; S123H+Y141W; G20S + Y141W; A76G + Y141W; G128D + Y141W; G128D + D143N; P219C + Y141W; N142D + D143N; Y141W + K192R; Y141W + D143N; Y141W + N383R; Y141W + P219C + A265C; Y141W + N142D + D143N; Y141W + K192R V410A; G128D + Y141W + D143N; Y141W + D143N + P219C; Y141W + D143N + K192R; G128D + D143N + K192R; Y141W + D143N + K192R + P219C; G128D + Y141W + D143N + K192R; or G128D + Y141W + D143N + K192R + P219C, especially G128D+D143N, and wherein the alpha-amylase has at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 16.

Paragraph 306. The yeast strain of paragraph 304, wherein the alpha-amylase is Aspergillus terreus alpha-amylase selected from the group consisting of:

(i) an alpha-amylase comprising the polypeptide of SEQ ID NO: 6 of WO2017/087330;

(ii) an alpha-amylase comprising an amino acid sequence having at least 80%, at least 85%, at least 90%, at least 91 %, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% identity to the polypeptide of SEQ ID NO: 6 of WQ2017/087330.

The invention described and claimed herein is not to be limited in scope by the specific aspects herein disclosed, since these aspects are intended as illustrations of several aspects of the invention. Any equivalent aspects are intended to be within the scope of this invention. Indeed, various modifications of the invention in addition to those shown and described herein will become apparent to those skilled in the art from the foregoing description. Such modifications are also intended to fall within the scope of the appended claims. In the case of conflict, the present disclosure including definitions will control.

Various references are cited herein, the disclosures of which are incorporated by reference in their entireties. Deposit of Biological Material

The following biological material has been deposited under the terms of the Budapest Treaty with the Agricultural Research Service Patent Culture Collection (NRRL), Northern Regional Research Center, 1815 University Street, Peoria, IL, USA, and given the following accession number:

Deposit Accession Number Date of Deposit

Saccharomyces cerevisiae strain MBG5038 NRRL Y-67549 February 1 , 2018

Saccharomyces cerevisiae strain MBG5012 NRRL Y-67700 November 29, 2018

The following biological material has been deposited under the terms of the Budapest Treaty with the National Measurement Institute, Victoria, Australia and given the following accession number:

Deposit Accession Number Date of Deposit

Ethanol Red® V14/007039 March 19, 2014

The strains were deposited under conditions that assure that access to the culture will be available during the pendency of this patent application to one determined by the Commissioner of Patents and Trademarks to be entitled thereto under 37 C.F.R. §1.14 and 35 U.S.C. §122. The deposit represents a substantially pure culture of the deposited strain. The deposit is available as required by foreign patent laws in countries wherein counterparts of the subject application, or its progeny are filed. However, it should be understood that the availability of a deposit does not constitute a license to practice the subject invention in derogation of patent rights granted by governmental action.

Materials & Methods

Materials:

Alpha-Amylase 369 (“AA369”): Bacillus stearothermophilus alpha-amylase with the mutations: I181*+G182*+N193F+V59A+Q89R+E129V+K177L+R179E+Q254S+M284V truncated to 491 amino acids (using SEQ ID NO: 1 herein for numbering);

Penicillium oxalicum qlucoamylase variant PE498 (“PoAMG498”): Penicillium oxalicum glucoamylase variant having the following mutations: K79V+ P2N+ P4S+ P11 F+ T65A+ Q327F (using SEQ ID NO: 14 herein for numbering):

Protease Pfu (“PFU”): Protease derived from Pyrococcus furiosus shown in SEQ ID NO: 13 herein. Glucoamylase SA (“GSA”) comprises a blend comprising Talaromyces emersonii glucoamylase disclosed in W099/28448 (SEQ ID NO: 19 herein), Trametes cingulata glucoamylase disclosed as SEQ ID NO: 2 in WO 06/69289 and SEQ ID NO: 20 herein, and Rhizomucor pusillus alpha-amylase with Aspergillus niger glucoamylase linker and SBD disclosed as SEQ ID NO: 16 herein with the following substitutions: G128D+D143N (activity ratio AGU:AGU:FAU(F): approx. 30:7: 1).

Yeast:

ETHANOL RED™ (“ER”): Saccharomyces cerevisiae yeast available from Fermentis/Lesaffre, USA.

Methods

Identity: The relatedness between two amino acid sequences or between two nucleotide sequences is described by the parameter“identity”.

For purposes described herein, the degree of identity between two amino acid sequences, as well as the degree of identity between two nucleotide sequences, may be determined by the program "align" which is a Needleman-Wunsch alignment (i.e. a global alignment). The program is used for alignment of polypeptide, as well as nucleotide sequences. The default scoring matrix BLOSUM50 is used for polypeptide alignments, and the default identity matrix is used for nucleotide alignments. The penalty for the first residue of a gap is -12 for polypeptides and -16 for nucleotides. The penalties for further residues of a gap are -2 for polypeptides, and -4 for nucleotides.

"Align" is part of the FASTA package version v20u6 (see W. R. Pearson and D. J. Lipman (1988), "Improved Tools for Biological Sequence Analysis", PNAS 85:2444-2448, and W. R. Pearson (1990) "Rapid and Sensitive Sequence Comparison with FASTP and FASTA," Methods in Enzymology 183:63- 98). FASTA protein alignments use the Smith- Waterman algorithm with no limitation on gap size (see "Smith-Waterman algorithm", T. F. Smith and M. S. Waterman (1981) J. Mol. Biol. 147: 195-197).

Protease assays

AZCL-casein assay

A solution of 0.2% of the blue substrate AZCL-casein is suspended in Borax/NaH ₂ P0 ₄ buffer pH9 while stirring. The solution is distributed while stirring to microtiter plate (100 microL to each well), 30 microL enzyme sample is added and the plates are incubated in an Eppendorf Thermomixer for 30 minutes at 45° C and 600 rpm. Denatured enzyme sample (100° C boiling for 20min) is used as a blank. After incubation the reaction is stopped by transferring the microtiter plate onto ice and the coloured solution is separated from the solid by centrifugation at 3000rpm for 5 minutes at 4° C. 60 microL of supernatant is transferred to a microtiter plate and the absorbance at 595nm is measured using a BioRad Microplate Reader.

pNA-assav

50 microL protease-containing sample is added to a microtiter plate and the assay is started by adding 100 microL 1mM pNA substrate (5 mg dissolved in 100 microL DMSO and further diluted to 10 mL with Borax/NaH ₂ P0 ₄ buffer pH 9.0). The increase in OD405 at room temperature is monitored as a measure of the protease activity.

Glucoamylase activity (AGU) Glucoamylase activity may be measured in Glucoamylase Units (AGU).

The Novo Glucoamylase Unit (AGU) is defined as the amount of enzyme, which hydrolyzes 1 micromole maltose per minute under the standard conditions 37°C, pH 4.3, substrate: maltose 23.2 mM, buffer: acetate 0.1 M, reaction time 5 minutes.

An autoanalyzer system may be used. Mutarotase is added to the glucose dehydrogenase reagent so that any alpha-D-glucose present is turned into beta-D-glucose. Glucose dehydrogenase reacts specifically with beta-D-glucose in the reaction mentioned above, forming NADH which is determined using a photometer at 340 nm as a measure of the original glucose concentration.

AMG incubation

Substrate: maltose 23.2 mM

Buffer: acetate 0.1 M

pH: 4.30 ± 0.05

Incubation temperature: 37°C ± 1

Reaction time: 5 minutes

Enzyme working range: 0.5-4.0 AGU/mL

Color reaction

GlucDH: 430 U/L

Mutarotase: 9 U/L

NAD: 0.21 mM

Buffer: phosphate 0.12 M; 0.15 M NaCI

pH: 7.60 ± 0.05

Incubation temperature: 37°C ± 1

Reaction time: 5 minutes

Wavelength: 340 nm

A folder (EB-SM-0131.02/01) describing this analytical method in more detail is available on request from Novozymes A/S, Denmark, which folder is hereby included by reference. Acid alpha-amylase activity (AFAU)

Acid alpha-amylase activity may be measured in AFAU (Acid Fungal Alpha-amylase Units), which are determined relative to an enzyme standard. 1 AFAU is defined as the amount of enzyme which degrades 5.260 mg starch dry matter per hour under the below mentioned standard conditions.

Acid alpha-amylase, an endo-alpha-amylase (1 ,4-alpha-D-glucan-glucanohydrolase, E.C. 3.2.1.1) hydrolyzes alpha-1 , 4-glucosidic bonds in the inner regions of the starch molecule to form dextrins and oligosaccharides with different chain lengths. The intensity of color formed with iodine is directly proportional to the concentration of starch. Amylase activity is determined using reverse colorimetry as a reduction in the concentration of starch under the specified analytical conditions.

ALPHA - AMYLASE

STARCH + IODINE - 40 _{; -} , pH 2,5 > DEXTRINS + OLIGOSACCHARIDES

l = 590 nm

blue/violet t = 23 sec. decoloration

Standard conditions/reaction conditions

Substrate: Soluble starch, approx. 0.17 g/L

Buffer: Citrate, approx. 0.03 M

Iodine (l ₂ ): 0.03 g/L

CaCh: 1.85 mM

pH: 2.50 ± 0.05

Incubation temperature: 40°C

Reaction time: 23 seconds

Wavelength: 590nm

Enzyme concentration: 0.025 AFAU/mL

Enzyme working range: 0.01-0.04 AFAU/mL

A folder EB-SM-0259.02/01 describing this analytical method in more detail is available upon request to Novozymes A/S, Denmark, which folder is hereby included by reference.

Alpha-amylase activity (KNU)

The alpha-amylase activity may be determined using potato starch as substrate. This method is based on the break-down of modified potato starch by the enzyme, and the reaction is followed by mixing samples of the starch/enzyme solution with an iodine solution. Initially, a blackish-blue color is formed, but during the break-down of the starch the blue color gets weaker and gradually turns into a reddish-brown, which is compared to a colored glass standard.

One Kilo Novo alpha amylase Unit (KNU) is defined as the amount of enzyme which, under standard conditions (i.e., at 37°C +/- 0.05; 0.0003 M Ca ²⁺ ; and pH 5.6) dextrinizes 5260 mg starch dry substance Merck Amylum solubile. A folder EB-SM-0009.02/01 describing this analytical method in more detail is available upon request to Novozymes A/S, Denmark, which folder is hereby included by reference.

Alpha-amylase Activity (KNU-A)

Alpha amylase activity is measured in KNU(A) Kilo Novozymes Units (A), relative to an enzyme standard of a declared strength.

Alpha amylase in samples and a-glucosidase in the reagent kit hydrolyze the substrate (4,6- ethylidene(G ₇ )-p-nitrophenyl(Gi)-a,D-maltoheptaoside (ethylidene-G ₇ PNP) to glucose and the yellow-colored p-nitrophenol.

The rate of formation of p-nitrophenol can be observed by Konelab 30. This is an expression of the reaction rate and thereby the enzyme activity.

Ethyli dene-G-^p-ni tnophenyl-maltoheptaosi de

Ethylidene-G _n G _n -p-nitrophenyl

alpha-glucosidasc

G +

p-Nitrophenol

Glucose

yellow, 405 nm

The enzyme is an alpha-amylase with the enzyme classification number EC 3.2.1.1.

Parameter Reaction conditions

A folder EB-SM-5091.02-D on determining KNU-A actitvity is available upon request to Novozymes A/S, Denmark, which folder is hereby included by reference.

Alpha-Amylase Activity KNU(S)

BS-amylase in samples and the enzyme alpha-glucosidase in the reagent kit hydrolyze substrate (4,6-ethylidene(G7)-p-nitrophenyl(G1)-alpha-D-maltoheptaosid e (ethylidene- G7PNP)) to glucose and the yellow-colored p-nitrophenol.

The rate of formation of p-nitrophenol can be observed by Konelab 30. This is an expression of the reaction rate and thereby the enzyme activity.

Reaction conditions

Reaction:

pH: 7.15

Temperature: 37 °C

Reaction Time: 180 sec

Detection:

Wavelength: 405 nm

Measuring Time: 120 sec

Unit definition

Bacillus stearothermophilus amylase (BS-amylase) activity is measured in KNU(S), Kilo Novo Units (sterarothermophilus), relative to an enzyme standard of a declared strength.

This analytical method is described in more details in EB-SM-0221.02 (incorporated by reference) available from Novozymes A/S, Denmark, on request.

Determination of FAU(F)

FAU(F) Fungal Alpha-Amylase Units (Fungamyl) is measured relative to an enzyme standard of a declared strength.

Reaction conditions

Temperature: 37°C

pH: 7.15

Wavelength: 405 nm

Reaction time: 5 min

Measuring time: 2 min A folder (EB-SM-0216.02) describing this standard method in more detail is available on request from Novozymes A/S, Denmark, which folder is hereby included by reference.

Determination of Pullulanase Activity (NPUN)

Endo-pullulanase activity in NPUN is measured relative to a Novozymes pullulanase standard. One pullulanase unit (NPUN) is defined as the amount of enzyme that releases 1 micro mol glucose per minute under the standard conditions (0.7% red pullulan (Megazyme), pH 5, 40°C, 20 minutes). The activity is measured in NPUN/ml using red pullulan.

1 ml_ diluted sample or standard is incubated at 40°C for 2 minutes. 0.5 ml_ 2% red pullulan, 0.5 M KCI, 50 mM citric acid, pH 5 are added and mixed. The tubes are incubated at 40°C for 20 minutes and stopped by adding 2.5 ml 80% ethanol. The tubes are left standing at room temperature for 10-60 minutes followed by centrifugation 10 minutes at 4000 rpm. OD of the supernatants is then measured at 510 nm and the activity calculated using a standard curve.

The present invention is described in further detail in the following examples which are offered to illustrate the present invention, but not in any way intended to limit the scope of the invention as claimed. All references cited herein are specifically incorporated by reference for that which is described therein.

EXAMPLES

Example 1 : Stability of Alpha-Amylase Variants

The stability of a reference alpha-amylase ( Bacillus stearothermophilus alpha-amylase with the mutations I 181*+G182*+N193F truncated to 491 amino acids (SEQ ID NO: 1 numbering)) and alpha-amylase variants thereof was determined by incubating the reference alpha-amylase and variants at pH 4.5 and 5.5 and temperatures of 75°C and 85°C with 0.12 mM CaCl2 followed by residual activity determination using the EnzChek® substrate (EnzChek® Ultra Amylase assay kit, E33651 , Molecular Probes).

Purified enzyme samples were diluted to working concentrations of 0.5 and 1 or 5 and 10 ppm (micrograms/ml) in enzyme dilution buffer (10 mM acetate, 0.01 % Triton X100, 0.12 mM CaCl2, pH 5.0). Twenty microliters enzyme sample was transferred to 48-well PCR MTP and 180 microliters stability buffer (150 mM acetate, 150 mM MES, 0.01 % Triton X100, 0.12 mM CaCl2, pH 4.5 or 5.5) was added to each well and mixed. The assay was performed using two concentrations of enzyme in duplicates. Before incubation at 75°C or 85°C, 20 microliters was withdrawn and stored on ice as control samples. Incubation was performed in a PCR machine at 75°C and 85°C. After incubation samples were diluted to 15 ng/mL in residual activity buffer (100 mM Acetate, 0.01 % Triton X100, 0.12 mM CaCh, pH 5.5) and 25 microliters diluted enzyme was transferred to black 384-MTP. Residual activity was determined using the EnzChek substrate by adding 25 microliters substrate solution (100 micrograms/ml) to each well. Fluorescence was determined every minute for 15 minutes using excitation filter at 485- P nm and emission filter at 555 nm (fluorescence reader is Polarstar, BMG). The residual activity was normalized to control samples for each setup.

Assuming logarithmic decay half life time (T ½ (min)) was calculated using the equation:

T½ (min) = T(min)*LN(0.5)/LN(%RA/100), where T is assay incubation time in minutes, and %RA is % residual activity determined in assay.

Using this assay setup the half life time was determined for the reference alpha- amylase and variant thereof as shown in Table 1.

Table 1.

ND: not determined

The results demonstrate that the alpha-amylase variants have a significantly greater half-life and stability than the reference alpha-amylase.

Example 2: Preparation of Protease Variants and Test of Thermostability

Strains and plasmids E.coli DH12S (available from Gibco BRL) was used for yeast plasmid rescue. pJTPOOO is a S. cerevisiae and E.coli shuttle vector under the control of TPI promoter, constructed from pJC039 described in WO 01/92502, in which the Thermoascus aurantiacus M35 protease gene (WO 03048353) has been inserted.

Saccharomyces cerevisiae YNG318 competent cells: MATa Dpep4[cir+] ura3-52, Ieu2-D2, his 4-539 was used for protease variants expression. It is described in J. Biol. Chem. 272 (15), pp 9720-9727, 1997.

Media and substrates

10X Basal solution: Yeast nitrogen base w/o amino acids (DIFCO) 66.8 g/l, succinate 100 g/l, NaOH 60 g/l.

SC-qlucose: 20 % glucose (i.e. , a final concentration of 2 % = 2 g/100 ml)) 100 ml/I, 5 % threonine 4 ml/l, 1 % tryptophanlO ml/l, 20 % casamino acids 25 ml/I, 10 X basal solution 100 ml/I. The solution is sterilized using a filter of a pore size of 0.20 micrometer. Agar (2%) and H ₂ 0 (approx. 761 ml) is autoclaved together, and the separately sterilized SC-glucose solution is added to the agar solution.

YPD: Bacto peptone 20 g/l, yeast extract 10 g/l, 20 % glucose 100 ml/l.

YPD+Zn: YPD+0.25 mM ZnS0 _4.

PEG/LiAc solution: 40 % PEG4000 50 ml, 5 M Lithium Acetate 1 ml.

96 well Zein micro titre plate:

Each well contains 200 microL of 0.05-0.1 % of zein (Sigma), 0.25 mM ZnS0 ₄ and 1 % of agar in 20 mM sodium acetate buffer, pH 4.5.

DNA manipulations

Unless otherwise stated, DNA manipulations and transformations were performed using standard methods of molecular biology as described in Sambrook et al. (1989) Molecular cloning: A laboratory manual, Cold Spring Harbor lab. Cold Spring Harbor, NY; Ausubel, F. M. et al. (eds.) "Current protocols in Molecular Biology ¹ ', John Wiley and Sons, 1995; Harwood, C. R. and Cutting, S. M. (Eds.).

Yeast transformation

Yeast transformation was performed using the lithium acetate method. 0.5 microL of vector (digested by restriction endonucleases) and 1 microL of PCR fragments is mixed. The DNA mixture, 100 microL of YNG318 competent cells, and 10 microL of YEAST MAKER carrier DNA (Clontech) is added to a 12 ml polypropylene tube (Falcon 2059). Add 0.6 ml PEG/LiAc solution and mix gently. Incubate for 30 min at 30 °C, and 200 rpm followed by 30 min at 42 °C (heat shock). Transfer to an eppendorf tube and centrifuge for 5 sec. Remove the supernatant and resolve in 3 ml of YPD. Incubate the cell suspension for 45 min at 200 rpm at 30 °C. Pour the suspension to SC-glucose plates and incubate 30 °C for 3 days to grow colonies. Yeast total DNA are extracted by Zymoprep Yeast Plasmid Miniprep Kit (ZYMO research).

DNA sequencing

E. coli transformation for DNA sequencing was carried out by electroporation (BIO RAD Gene Pulser). DNA Plasmids were prepared by alkaline method (Molecular Cloning, Cold Spring Harbor) or with the Qiagen® Plasmid Kit. DNA fragments were recovered from agarose gel by the Qiagen gel extraction Kit. PCR was performed using a PTC-200 DNA Engine. The ABI PRISMTM 310 Genetic Analyzer was used for determination of all DNA sequences. Construction of protease expression vector

The Thermoascus M35 protease gene was amplified with the primer pair Prot F (SEQ ID NO: 4) and Prot R (SEQ ID NO: 5). The resulting PCR fragments were introduced into S. cerevisiae YNG318 together with the pJC039 vector (described in WO 2001/92502) digested with restriction enzymes to remove the Humicola insolens cutinase gene.

The Plasmid in yeast clones on SC-glucose plates was recovered to confirm the internal sequence and termed as pJTPOOl

Construction of yeast library and site-directed variants

Library in yeast and site-directed variants were constructed by SOE PCR method (Splicing by Overlap Extension, see “PCR: A practical approach”, p. 207-209, Oxford University press, eds. McPherson, Quirke, Taylor), followed by yeast in vivo recombination. General primers for amplification and sequencing

The primers AM34 (SEQ ID NO: 6) and AM35 (SEQ ID NO: 7) were used to make DNA fragments containing any mutated fragments by the SOE method together with degenerated primers (AM34 + Reverse primer and AM35 + forward primer) or just to amplify a whole protease gene (AM34 + AM35).

PCR reaction system: Conditions:

DNA fragments were recovered from agarose gel by the Qiagen gel extraction Kit. The resulting purified fragments were mixed with the vector digest. The mixed solution was introduced into Saccharomyces cerevisiae to construct libraries or site-directed variants by in vivo recombination.

Relative activity assay

Yeast clones on SC-glucose were inoculated to a well of a 96-well micro titre plate containing YPD+Zn medium and cultivated at 28°C for 3 days. The culture supernatants were applied to a 96-well zein micro titer plate and incubated at at least 2 temperatures (ex. 60°C and 65°C, 70°C and 75°C, 70°C and 80°C) for more than 4 hours or overnight. The turbidity of zein in the plate was measured as A630 and the relative activity (higher/lower temperatures) was determined as an indicator of thermoactivity improvement. The clones with higher relative activity than the parental variant were selected and the sequence was determined.

Remaining activity assay

Yeast clones on SC-glucose were inoculated to a well of a 96-well micro titre plate and cultivated at 28°C for 3 days. Protease activity was measured at 65°C using azo-casein (Megazyme) after incubating the culture supernatant in 20 mM sodium acetate buffer, pH 4.5, for 10 min at a certain temperature (80°C or 84°C with 4°C as a reference) to determine the remaining activity. The clones with higher remaining activity than the parental variant were selected and the sequence was determined.

Azo-casein assay

20 microL of samples were mixed with 150 microL of substrate solution (4 ml of 12.5% azo-casein in ethanol in 96 ml of 20 mM sodium acetate, pH 4.5, containing 0.01 % triton-100 and 0.25 mM ZnS0 ₄ ) and incubated for 4 hours or longer.

After adding 20 microL/well of 100 % trichloroacetic acid (TCA) solution, the plate was centrifuge and 100 microL of supernatants were pipette out to measure A440.

Expression of protease variants in Aspergillus oryzae

The constructs comprising the protease variant genes were used to construct expression vectors for Aspergillus. The Aspergillus expression vectors consist of an expression cassette based on the Aspergillus niger neutral amylase II promoter fused to the Aspergillus nidulans triose phosphate isomerase non translated leader sequence (Pna2/tpi) and the Aspergillus niger amyloglucosidase terminator (Tamg). Also present on the plasmid was the Aspergillus selective marker amdS from Aspergillus nidulans enabling growth on acetamide as sole nitrogen source. The expression plasmids for protease variants were transformed into Aspergillus as described in Lassen et al. (2001), Appl. Environ. Microbiol. 67, 4701-4707. For each of the constructs 10-20 strains were isolated, purified and cultivated in shake flasks.

Purification of expressed variants

1. Adjust pH of the 0.22 pm filtered fermentation sample to 4.0.

2. Put the sample on an ice bath with magnetic stirring. Add (NH4)2S04 in small aliquots (corresponding to approx. 2.0-2.2 M (NH4)2S04 not taking the volume increase into account when adding the compound).

3. After the final addition of (NH4)2S04, incubate the sample on the ice bath with gentle magnetic stirring for min. 45 min.

4. Centrifugation: Hitachi himac CR20G High-Speed Refrigerated Centrifuge equipped with R20A2 rotor head, 5°C, 20,000 rpm, 30 min.

5. Dissolve the formed precipitate in 200 ml 50 mM Na-acetate pH 4.0.

6. Filter the sample by vacuum suction using a 0.22 pm PES PLUS membrane (IWAKI).

7. Desalt/buffer-exchange the sample to 50 mM Na-acetate pH 4.0 using ultrafiltration (Vivacell 250 from Vivascience equipped with 5 kDa MWCO PES membrane) overnight in a cold room. Dilute the retentate sample to 200 ml using 50 mM Na-acetate pH 4.0. The conductivity of sample is preferably less than 5 mS/cm.

8. Load the sample onto a cation-exchange column equilibrated with 50 mM Na-acetate pH 4.0. Wash unbound sample out of the column using 3 column volumes of binding buffer (50 mM Na-acetate pH 4.0), and elute the sample using a linear gradient, 0-100% elution buffer (50 mM Na-acetate + 1 M NaCI pH 4.0) in 10 column volumes.

9. The collected fractions are assayed by an endo-protease assay (cf. below) followed by standard SDS-PAGE (reducing conditions) on selected fractions. Fractions are pooled based on the endo-protease assay and SDS-PAGE.

Endo-protease assay

1. Protazyme OL tablet/5 ml 250 mM Na-acetate pH 5.0 is dissolved by magnetic stirring (substrate: endo-protease Protazyme AK tablet from Megazyme - cat. # PRAK 11/08).

2. With stirring, 250 microL of substrate solution is transferred to a 1.5 ml Eppendorf tube.

3. 25 microL of sample is added to each tube (blank is sample buffer).

4. The tubes are incubated on a Thermomixer with shaking (1000 rpm) at 50°C for 15 minutes.

5. 250 microL of 1 M NaOH is added to each tube, followed by vortexing. 6. Centrifugation for 3 min. at 16, 100 ^c G and 25°C.

7. 200 microL of the supernatant is transferred to a MTP, and the absorbance at 590 nm is recorded.

Results

Table 2. Relative activity of protease variants. Numbering of substitution(s) starts from N- terminal of the mature peptide in amino acids 1 to 177 of SEQ ID NO: 3

Table 3. Relative activity of protease variants. Numbering of substitution(s) starts from N- terminal of the mature peptide in amino acids 1 to 177 of SEQ ID NO: 3

Table 4. Relative activity of protease variants. Numbering of substitution(s) starts from N- terminal of the mature peptide in amino acids 1 to 177 of SEQ ID NO: 3

Table 5. Relative activity of protease variants. Numbering of substitution(s) starts from N- terminal of the mature peptide in amino acids 1 to 177 of SEQ ID NO: 3

Table 6. Relative activity of protease variants. Numbering of substitution(s) starts from N- terminal of the mature peptide in amino acids 1 to 177 of SEQ ID NO: 3

Example 3: Temperature profile of selected variants using purified enzymes

Selected variants showing good thermo-stability were purified and the purified enzymes were used in a zein-BCA assay as described below. The remaining protease activity was determined at 60°C after incubation of the enzyme at elevated temperatures as indicated for 60 min.

Zein-BCA assay:

Zein-BCA assay was performed to detect soluble protein quantification released from zein by variant proteases at various temperatures. Protocol:

1 ) Mix 10ul of 10 ug/ml enzyme solutions and 100ul of 0.025% zein solution in a micro titer plate (MTP).

2) Incubate at various temperatures for 60min.

3) Add 10ul of 100% trichloroacetic acid (TCA) solution.

4) Centrifuge MTP at 3500rpm for 5min.

5) Take out 15ul to a new MTP containing 100ul of BCA assay solution (Pierce Cat#:23225, BCA Protein Assay Kit).

6) Incubate for 30min. at 60°C.

7) Measure A562.

The results are shown in Table 7. All of the tested variants showed an improved thermo stability as compared to the wt protease.

Table 1. Zein-BCA assay

Example 4: Characterization of Penicillium oxalicum qlucoamylase

The Penicillium oxalicum glucoamylase is disclosed in SEQ ID NO: 9 herein.

Substrate. Substrate: 1 % soluble starch (Sigma S-9765) in deionized water

Reaction buffer: 0.1 M Acetate buffer at pH 5.3

Glucose concentration determination kit: Wako glucose assay kit (LabAssay glucose, WAKO, Cat# 298-65701).

Reaction condition. 20 microL soluble starch and 50 microL acetate buffer at pH 5.3 were mixed. 30 microL enzyme solution (50 micro g enzyme protein/ml) was added to a final volume of 100 microL followed by incubation at 37°C for 15 min.

The glucose concentration was determined by Wako kits.

All the work carried out in parallel.

Temperature optimum. To assess the temperature optimum of the Penicillium oxalicum glucoamylase the“Reaction condition”-assay described above was performed at 20, 30, 40, 50, 60, 70, 80, 85, 90 and 95°C. The results are shown in Table 8.

Table 8. Temperature optimum

From the results it can be seen that the optimal temperature for Penicillium oxalicum glucoamylase at the given conditions is between 50°C and 70°C and the glucoamylase maintains more than 80% activity at 95°C.

Heat stability. To assess the heat stability of the Penicillium oxalicum glucoamylase the Reaction condition assay was modifed in that the the enzyme solution and acetate buffer was preincubated for 15 min at 20, 30, 40, 50, 60, 70, 75, 80, 85, 90 and 95°C. Following the incubation 20 microL of starch was added to the solution and the assay was performed as described above.

The results are shown in Table 9.

Table 9. Heat stability

From the results it can be seen that PeniciHium oxalicum glucoamylase is stable up to 70 °C after preincubation for 15 min in that it maintains more than 80% activity. pH optimum. To assess the pH optimum of the Penicillium oxalicum glucoamylase the Reaction condition assay described above was performed at pH 2.0, 3.0, 3.5, 4.0, 4.5, 5.0, 6.0 7.0, 8.0, 9.0, 10.0 and 11.0. Instead of using the acetate buffer described in the Reaction condition assay the following buffer was used 100mM Succinic acid, HEPES, CHES, CAPSO, 1 mM CaCI ₂ , 150mM KCI, 0.01 % Triton X-100, pH adjusted to 2.0, 3.0, 3.5, 4.0, 4.5, 5.0, 6.0 7.0, 8.0, 9.0, 10.0 or 11.0 with HCI or NaOH.

The results are shown in Table 10.

Table 10. pH optimum

From the results it can be seen that PeniciHium oxalicum glucoamylase at the given conditions has the highest activity at pH 5.0. The PeniciHium oxalicum glucoamylase is active in a broad pH range in the it maintains more than 50% activity from pH 2 to 7. pH stability. To assess the heat stability of the PeniciHium oxalicum glucoamylase the Reaction condition assay was modifed in that the enzyme solution (50micro g/ml_) was preincubated for 20 hours in buffers with pH 2.0, 3.0, 3.5, 4.0, 4.5, 5.0, 6.0 7.0, 8.0, 9.0, 10.0 and 11.0 using the buffers described under pH optimum. After preincubation, 20 microL soluble starch to a final volume of 100 microL was added to the solution and the assay was performed as described above.

The results are shown in Table 11.

Table 11. pH stability

From the results it can be seen that PeniciHium oxalicum glucoamylase, is stable from pH 3 to pH 7 after preincubation for 20 hours and it decreases its activity at pH 8.

Example 5: Thermostability of Protease Pfu

The thermostability of the Pyrococcus furiosus protease (Pfu S) purchased from Takara Bio Inc, (Japan) was tested using the same methods as in Example 2. It was found that the thermostability (Relative Activity) was 110% at (80°C/70°C) and 103% (90°C/70°C) at pH 4.5.

Example 6: Cloning of PeniciHium oxalicum strain glucoamylase gene

Preparation of PeniciHium oxalicum strain cDNA.

The cDNA was synthesized by following the instruction of 3’ Rapid Amplifiction of cDNA End System (Invitrogen Corp., Carlsbad, CA, USA).

Cloning of PeniciHium oxalicum strain glucoamylase gene.

The PeniciHium oxalicum glucoamylase gene was cloned using the oligonucleotide primer shown below designed to amplify the glucoamylase gene from 5’ end.

Sense primer: 5’- ATGCGT CT CACTCT ATT ATCAGGT G-3’ (SEQ ID NO: 22)

The full length gene was amplified by PCR with Sense primer and AUAP (supplied by 3’ Rapid Amplifiction of cDNA End System) by using Platinum HIFI Tag DNA polymerase (Invitrogen Corp., Carlsbad, CA, USA). The amplification reaction was composed of 5 pi of 10x PCR buffer, 2 mI of 25mM MgCh, 1 mI of 10mM dNTP, 1 mI of 10uM Sense primer, 1 mI of 10 uM AUAP, 2 mI of the first strand cDNA, 0.5 mI of HI FI Taq, and 37.5 mI of deionized water. The PCR program was: 94°C, 3mins; 10 cycles of 94°C for 40secs, 60°C 40secs with 1 °C decrease per cycle, 68°C for 2min; 25 cycles of 94°C for 40secs, 50°C for 40secs, 68°C for 2min; final extension at 68°C for 10 mins.

The obtained PCR fragment was cloned into pGEM-T vector (Promega Corporation, Madison, Wl, USA) using a pGEM-T Vector System (Promega Corporation, Madison, Wl, USA) to generate plasmid AMG 1. The glucoamylase gene inserted in the plasmid AMG 1 was sequencing confirmed. E. coli strain TOP10 containing plasmid AMG 1 (designated NN059173), was deposited with the Deutsche Sammlung von Mikroorganismen und Zellkulturen GmbH (DSMZ) on November 23, 2009, and assigned accession number as DSM 23123.

Example 7: Expression of cloned Penicillium oxalicum glucoamylase

The Penicillium oxalicum glucoamylase gene was re-cloned from the plasmid AMG 1 into an Aspergillus expression vector by PCR using two cloning primer F and primer R shown below, which were designed based on the known sequence and added tags for direct cloning by IN-FUSION™ strategy.

Primer F: 5’ ACACAACTGGGG ATCCACCAT GCGTCT CACT CT ATT AT C (SEQ ID NO: 23) Primer R: 5’ AGATCTCGAGAAGCTT AAAACTGCCACACGT CGTTGG (SEQ ID NO: 24)

A PCR reaction was performed with plasmid AMG 1 in order to amplify the full-length gene. The PCR reaction was composed of 40 pg of the plasmid AMG 1 DNA, 1 mI of each primer (100 mM); 12.5 pi of 2X Extensor Hi-Fidelity master mix (Extensor Hi-Fidelity Master Mix, ABgene, United Kingdom), and 9.5 mI of PCR-grade water. The PCR reaction was performed using a DYAD PCR machine (Bio-Rad Laboratories, Inc., Hercules, CA, USA) programmed for 2 minutes at 94°C followed by a 25 cycles of 94°C for 15 seconds, 50°C for 30 seconds, and 72°C for 1 minute; and then 10 minutes at 72°C.

The reaction products were isolated by 1.0% agarose gel electrophoresis using 1 x TAE buffer where an approximately 1.9 kb PCR product band was excised from the gel and purified using a GFX® PCR DNA and Gel Band Purification Kit (GE Healthcare, United Kingdom) according to manufacturer’s instructions. DNA corresponding to the Penicillium oxalicum glucoamylase gene was cloned into an Aspergillus expression vector linearized with SamHI and Hind\\\, using an IN-FUSION™ Dry-Down PCR Cloning Kit (BD Biosciences, Palo Alto, CA, USA) according to the manufacturer’s instructions. The linearized vector construction is as described in WO 2005/042735 A1. A 2 mI volume of the ligation mixture was used to transform 25 mI of Fusion Blue E. coli cells (included in the IN-FUSION™ Dry-Down PCR Cloning Kit). After a heat shock at 42°C for 45 sec, and chilling on ice, 250 mI of SOC medium was added, and the cells were incubated at 37°C at 225 rpm for 90 min before being plated out on LB agar plates containing 50 pg of ampicillin per ml, and cultivated overnight at 37°C. Selected colonies were inoculated in 3 ml of LB medium supplemented with 50 pg of ampicillin per ml and incubated at 37°C at 225 rpm overnight. Plasmid DNA from the selected colonies was purified using Mini JETSTAR (Genomed, Germany) according to the manufacturer’s instructions. Penicillium oxalicum glucoamylase gene sequence was verified by Sanger sequencing before heterologous expression. One of the plasmids was selected for further expression, and was named XYZ XYZ1471-4.

Protoplasts of Aspergillus n/ger MBinl 18 were prepared as described in WO 95/02043. One hundred pi of protoplast suspension were mixed with 2.5 pg of the XYZ1471-4 plasmid and 250 microliters of 60% PEG 4000 (Applichem) (polyethylene glycol, molecular weight 4,000), 10 mM CaCL, and 10 mM Tris-HCI pH 7.5 were added and gently mixed. The mixture was incubated at 37°C for 30 minutes and the protoplasts were mixed with 6% low melting agarose (Biowhittaker Molecular Applications) in COVE sucrose (Cove, 1996, Biochim. Biophys. Acta 133:51-56) (1 M) plates supplemented with 10 mM acetamide and 15 mM CsCI and added as a top layer on COVE sucrose (1 M) plates supplemented with 10 mM acetamide and 15 mM CsCI for transformants selection (4 ml topagar per plate). After incubation for 5 days at 37°C spores of sixteen transformants were picked up and seed on 750 mI YP-2% Maltose medium in 96 deepwell MT plates. After 5 days of stationary cultivation at 30°C, 10 pi of the culture-broth from each well was analyzed on a SDS-PAGE (Sodium dodecyl sulfate- polyacrylamide gel electrophoresis) gel, Griton XT Precast gel (BioRad, CA, USA) in order to identify the best transformants based on the ability to produce large amount of glucoamylase. A selected transformant was identified on the original transformation plate and was preserved as spores in a 20% glycerol stock and stored frozen (-80°C).

Cultivation. The selected transformant was inoculated in 100ml of MLC media and cultivated at 30 °C for 2 days in 500 ml shake flasks on a rotary shaker. 3 ml of the culture broth was inoculated to 100ml of M410 medium and cultivated at 30°C for 3 days. The culture broth was centrifugated and the supernatant was filtrated using 0.2 pm membrane filters.

Alpha-cyclodextrin affinity gel. Ten grams of Epoxy-activated Sepharose 6B (GE Healthcare, Chalfont St. Giles, U.K) powder was suspended in and washed with distilled water on a sintered glass filter. The gel was suspended in coupling solution (100 ml of 12.5 mg/ml alpha-cyclodextrin, 0.5 M NaOH) and incubated at room temperature for one day with gentle shaking. The gel was washed with distilled water on a sintered glass filter, suspended in 100 ml of 1 M ethanolamine, pH 10, and incubated at 50 ^° C for 4 hours for blocking. The gel was then washed several times using 50 mM Tris-HCI, pH 8 and 50 mM NaOAc, pH 4.0 alternatively. The gel was finally packed in a 35-40 ml column using equilibration buffer (50 mM NaOAc, 150 mM NaCI, pH 4.5).

Purification of glucoamylase from culture broth. Culture broth from fermentation of A. niger MBinl 18 harboring the glucoamylase gene was filtrated through a 0.22 pm PES filter, and applied on a alpha-cyclodextrin affinity gel column previously equilibrated in 50 mM NaOAc, 150 mM NaCI, pH 4.5 buffer. Unbound material was washed off the column with equilibration buffer and the glucoamylase was eluted using the same buffer containing 10 mM beta-cyclodextrin over 3 column volumes.

The glucoamylase activity of the eluent was checked to see, if the glucoamylase had bound to the alpha-cyclodextrin affinity gel. The purified glucoamylase sample was then dialyzed against 20 mM NaOAc, pH 5.0. The purity was finally checked by SDS-PAGE, and only a single band was found.

Example 8: Construction and expression of a site-directed variant of Penicillium oxalicum glucoamylase

Two PCR reactions were performed with plasmid XYZ1471-4, described in Example 7, using primers K79V F and K79VR shown below, which were designed to substitute lysine K at position 79 from the mature sequence to valine (V) and primers F-NP003940 and R- NP003940 shown below, which were designed based on the known sequence and added tags for direct cloning by IN-FUSION™ strategy.

Primer K79V F 18mer GCAGTCTTTCCAATT G AC (SEQ ID NO: 25)

Primer K79V R 18mer AATTGGAAAGACTGCCCG (SEQ ID NO: 26)

Primer F-NP003940: 5’ ACACAACTGGGGAT CCACCATGCGTCTCACT CT ATT AT C (SEQ ID NO: 27)

Primer R-NP003940: 5’ AGAT CT CGAGAAGCTT AAAACT GCCACACGTCGTT GG (SEQ ID NO: 28)

The PCR was performed using a PTC-200 DNA Engine under the conditions described below.

PCR reaction system: Conditions:

48.5 micro L H20 1 94°C 2 min

2 beads puRe Taq Ready-To- 2 94° C 30 sec

Go PCR Beads (Amersham Biosciences) 3 55°C 30 sec

0.5micro L X 2100 pmole/micro L Primers 4 72°C 90 sec

2-4 25 cycles (K79V F + Primer R-NP003940 K79V R + 5 72°C 10 min

Primer F-NP003940)

0.5 micro L Template DNA

DNA fragments were recovered from agarose gel by the Qiagen gel extraction Kit according to the manufacturer’s instruction. The resulting purified two fragments were cloned into an Aspergillus expression vector linearized with Bamb\ and Hind\\\, using an IN FUSION™ Dry-Down PCR Cloning Kit (BD Biosciences, Palo Alto, CA, USA) according to the manufacturer’s instructions. The linearized vector construction is as described in WO 2005/042735 A1.

The ligation mixture was used to transform E. coli DH5a cells (TOYOBO). Selected colonies were inoculated in 3 ml of LB medium supplemented with 50 pg of ampicillin per ml and incubated at 37°C at 225 rpm overnight. Plasmid DNA from the selected colonies was purified using Qiagen plasmid mini kit (Qiagen) according to the manufacturer’s instructions. The sequence of Penicillium oxalicum glucoamylase site-directed variant gene sequence was verified before heterologous expression and one of the plasmids was selected for further expression, and was named pPoPEOOI .

Protoplasts of Aspergillus niger MBinl 18 were prepared as described in WO 95/02043. One hundred pi of protoplast suspension were mixed with 2.5 pg of the pPoPEOOI plasmid and 250 microliters of 60% PEG 4000 (Applichem) (polyethylene glycol, molecular weight 4,000), 10 mM CaC , and 10 mM Tris-HCI pH 7.5 were added and gently mixed. The mixture was incubated at 37°C for 30 minutes and the protoplasts were mixed with 1 % agarose L (Nippon Gene) in COVE sucrose (Cove, 1996, Biochim. Biophys. Acta 133:51-56) supplemented with 10 mM acetamide and 15 mM CsCI and added as a top layer on COVE sucrose plates supplemented with 10 mM acetamide and 15 mM CsCI for transformants selection (4 ml topagar per plate). After incubation for 5 days at 37°C spores of sixteen transformants were picked up and seed on 750 mI YP-2% Maltose medium in 96 deepwell MT plates. After 5 days of stationary cultivation at 30°C, 10 mI of the culture-broth from each well was analyzed on a SDS-PAGE gel in order to identify the best transformants based on the ability to produce large amount of the glucoamylase.

Example 9: Purification of site-directed Po AMG variant PE001

The selected transformant of the variant and the strain expressing the wild type Penicillium oxalicum glucoamylase described in Example 6 was cultivated in 100 ml of YP- 2% maltose medium and the culture was filtrated through a 0.22 pm PES filter, and applied on a alpha-cyclodextrin affinity gel column previously equilibrated in 50 mM NaOAc, 150 mM NaCI, pH 4.5 buffer. Unbound materials was washed off the column with equilibration buffer and the glucoamylase was eluted using the same buffer containing 10 mM beta-cyclodextrin over 3 column volumes.

The glucoamylase activity of the eluent was checked to see, if the glucoamylase had bound to the alpha-cyclodextrin affinity gel. The purified glucoamylase samples were then dialyzed against 20 mM NaOAc, pH 5.0.

Example 10: Characterization of PE001 Protease stability

40 pi enzyme solutions (1 mg/ml) in 50 mM sodium acetate buffer, pH 4.5, were mixed with 1/10 volume of 1 mg/ml protease solutions such as aspergillopepsin I described in Biochem J. 1975 Apr; 147(1):45-53, or the commercially available product from Sigma and aorsin described in Biochemical journal [0264-6021] lchishima yr: 2003 vol:371 iss: Pt 2 pg:541 and incubated at 4 or 32°C overnight. As a control experiment, H ₂ 0 was added to the sample instead of proteases. The samples were loaded on SDS-PAGE to see if the glucoamylases are cleaved by proteases.

In SDS-PAGE, PE001 only showed one band corresponding to the intact molecule, while the wild type glucoamylase was degraded by proteases and showed a band at lower molecular size at 60 kCa.

Table 12. The result of SDS-PAGE after protease treatment

N.D.: not detected.

Example 11 : Less cleavage during cultivation

Aspergillus transformant of the variant and the wild type Penicillium oxalicum glucoamylase were cultivated in 6-well MT plates containing 4X diluted YP-2% maltose medium supplemented with 10 mM sodium acetate buffer, pH4.5, at 32°C for 1 week.

The culture supernatants were loaded on SDS-PAGE. Table 13. The result of SDS-PAGE of the culture supernatants

N.D.: not detected.

The wild type glucoamylase was cleaved by host proteases during fermentation, while the variant yielded only intact molecule.

Example 12: Glucoamylase activity of variant compared to parent

The glucoamylase activity measures as AGU as described above was checked for the purified enzymes of the wild type Penicillium oxalicum and the variant glucoamylase.

The Glucoamylase Unit (AGU) was defined as the amount of enzyme, which hydrolyzes 1 micromole maltose per minute under the standard conditions (37°C, pH 4.3, substrate: maltose 100 mM, buffer: acetate 0.1 M, reaction time 6 minutes).

Table 14.

Example 13: Purification of Glucoamylase variants having increased thermostability

The variants showing increased thermostability may be constructed and expressed similar to the procedure described in Example 8. All variants were derived from the PE001. After expression in YPM medium, variants comprising the T65A or Q327F substitution was micro-purified as follows:

Mycelium was removed by filtration through a 0.22 pm filter. 50 pi column material (alpha-cyclodextrin coupled to Mini-Leak divinylsulfone-activated agarose medium according to manufacturer’s recommendations) was added to the wells of a filter plate (Whatman, Unifilter 800 pi, 25-30 pm MBPP). The column material was equilibrated with binding buffer (200 mM sodium acetate pH 4.5) by two times addition of 200 pi buffer, vigorous shaking for 10 min (Heidolph, Titramax 101 , 1000 rpm) and removal of buffer by vacuum (Whatman, UniVac 3). Subsequently, 400 pi culture supernatant and 100 pi binding buffer was added and the plate incubated 30 min with vigorous shaking. Unbound material was removed by vacuum and the binding step was repeated. Normally 4 wells were used per variant. Three washing steps were then performed with 200 pi buffer of decreasing ionic strength added (50/10/5 mM sodium acetate, pH 4.5), shaking for 15 min and removal of buffer by vacuum. Elution of the bound AMG was achieved by two times addition of 100 pi elution buffer (250 mM sodium acetate, 0.1 % alpha-cyclodextrin, pH 6.0), shaking for 15 min and collection of eluted material in a microtiter plate by vacuum. Pooled eluates were concentrated and buffer changed to 50 mM sodium acetate pH 4.5 using centrifugal filter units with 10 kDa cut-off (Millipore Microcon Ultracel YM-10). Micropurified samples were stored at -18°C until testing of thermostability.

Example 14: Protein thermal unfolding analysis (TSA, Thermal shift assay)

Protein thermal unfolding of the T65A and Q327F variants, was monitored using Sypro Orange (ln-vitrogen, S-6650) and was performed using a real-time PCR instrument (Applied Biosystems; Step-One-Plus).

In a 96-well plate, 25 microliter micropurified sample in 50 mM Acetate pH4,5 at approx. 100 microgram/ml was mixed (5: 1) with Sypro Orange (resulting cone. = 5X; stock solution from supplier = 5000X). The plate was sealed with an optical PCR seal. The PCR instrument was set at a scan-rate of 76°C pr. hr, starting at 25°C and finishing at 96°C.

Protein thermal unfolding of the E501V + Y504T variant, was monitored using Sypro Orange (ln-vitrogen, S-6650) and was performed using a real-time PCR instrument (Applied Biosystems; Step-One-Plus).

In a 96-well plate, 15 microliter purified sample in 50 mM Acetate pH4,5 at approx. 50 microgram/ml was mixed (1 : 1) with Sypro Orange (resulting cone. = 5X; stock solution from supplier = 5000X) with or without 200 ppm Acarbose (Sigma A8980). The plate was sealed with an optical PCR seal. The PCR instrument was set at a scan-rate of 76 degrees C pr. hr, starting at 25°C and finishing at 96°C.

Fluorescence was monitored every 20 seconds using in-built LED blue light for excitation and ROX-filter (610 nm, emission).

Tm-values were calculated as the maximum value of the first derivative (dF/dK) (ref.: Gregory et al; J Biomol Screen 2009 14: 700.)

Table 15a.

Sample Tm (Deg. Celsius) +/-0.4

PO-AMG (PE001) 80.3

Variant Q327F 82.3

Variant T65A 81.9

Table 15b.

Sample Tm (Deg. Celsius) +/-0.4

Acarbose: +

PO-AMG (PE001) 79.5 86.9

Variant E501V Y504T 79.5 95.2 Example 15: Thermostability analysis by Differential Scanning Calorimetry (DSC)

Additional site specific variants having substitutions and /or deletions at specific positions were constructed basically as described in Example 8 and purified as described in Example 11.

The thermostability of the purified Po-AMG PE001 derived variants were determined at pH 4.0 or 4.8 (50 mM Sodium Acetate) by Differential Scanning Calorimetry (DSC) using a VP-Capillary Differential Scanning Calorimeter (MicroCal Inc., Piscataway, NJ, USA). The thermal denaturation temperature, Td (°C), was taken as the top of the denaturation peak (major endothermic peak) in thermograms (Cp vs. T) obtained after heating enzyme solutions in selected buffers (50 mM Sodium Acetate, pH 4.0 or 4.8)at a constant programmed heating rate of 200 K/hr.

Sample- and reference-solutions (approximately 0.3 ml) were loaded into the calorimeter (reference: buffer without enzyme) from storage conditions at 10°C and thermally pre-equilibrated for 10 minutes at 20°C prior to DSC scan from 20°C to 110°C. Denaturation temperatures were determined with an accuracy of approximately +/- 1°C.

The isolated variants and the DSC data are disclosed in Table 16 below.

Table 16.

Example 16: Thermostability analysis by thermo-stress test and pNPG assay

Starting from one of the identified substitution variants from Example 15, identified as GA008, additional variants were tested by a thermo-stress assay in which the supernatant from growth cultures were assayed for glucoamylase (AMG) activity after a heat shock at 83°C for 5 min.

After the heat-shock the residual activity of the variant was measured as well as in a non-stressed sample.

Description of Po-AMG pNPG activity assay:

The Penicillium oxalicum glucoamylase pNPG activity assay is a spectrometric endpoint assay where the samples are split in two and measured thermo-stressed and non- thermo-stressed. The data output is therefore a measurement of residual activity in the stressed samples.

Growth:

A sterile micro titer plate (MTP) was added 200mI_ rich growth media (FT X-14 without Dowfax) to each well. The strains of interest were inoculated in triplicates directly from frozen stocks to the MTP. Benchmark was inoculated in 20 wells. Non-inoculated wells with media were used as assay blanks. The MTP was placed in a plastic box containing wet tissue to prevent evaporation from the wells during incubation. The plastic box was placed at 34°C for 4 days.

Assay:

50 mI_ supernatant was transferred to 50 pL 0.5 M NaAc pH 4.8 to obtain correct sample pH.

50 mI_ dilution was transferred to a PCR plate and thermo-stressed at 83°C for 5 minutes in a PCR machine. The remaining half of the dilution was kept at RT.

20 mI_ of both stressed and unstressed samples was transferred to a standard MTP. 20mI_ pNPG-substrate was added to start the reaction. The plate was incubated at RT for 1 hour.

The reaction was stopped and the colour developed by adding 50 mI_ 0.5M Na ₂ C0 _3. The yellow colour was measured on a plate reader (Molecular Devices) at 405 nm. Buffers:

0.5 M NaAc pH 4.8

0.25 M NaAc pH 4.8

Substrate, 6mM pNPG:

15mg 4-nitrophenyl D-glucopyranoside in 10 mL 0.25 NaAc pH 4.8

Stop/developing solution:

0.5 M Na ₂ C0 ₃

Data treatment:

In Excel the raw Abs405 data from both stressed and unstressed samples were blank subtracted with their respective blanks. The residual activity (% res. act. = (Abs _un stressed - (AbSunstressed - Abs _s tressed))/Abs _U nstressed ^* 100%) was calculated and plotted relative to benchmark, Po-amg0008.

Table 17.

Table 18.

Example 17: Test for Glucoamylase activity of thermo-stable variants

All of the above described variants disclosed in tables 15, 16, and 17 have been verified for Glucoamylase activity on culture supernatants using the pNPG assay described in Example 16.

Example 18: Production of Saccharomvces cerevisiae strain MBG5038 and MBG5012

Strains MBG5038 and MBG5012 were derived from breeding and evolutionary programs that targeted improved fermentation performance with regards to features of importance to the industrial production of corn ethanol. Strains from a population with the ability to utilize cysteine as a sole nitrogen source, and demonstrating improved ethanol and temperature tolerance were mated with strains derived from a population which combined xylose utilization with low byproduct yields (e.g., according the breeding procedures described in US Patent No. 8,257,959). These strains were mated with strains derived from Ethanol Red® and the offspring screened to identify strains with increased temperature tolerance combined with reduced by-products to maximize the yield of ethanol from corn mash fermentations. Haploids derived from this breeding program were screened for their ability to utilize cysteine and used to generate MBG5038 (NRRLY67549) and MBG5038 (NRRLY67700).

Example 19: Fermentation of Saccharomvces cerevisiae strain MBG5038 under nonstress conditions

Saccharomyces cerevisiae strains MBG5038 and Ethanol Red® were fermented under the following conditions:

Mash: Liquozyme LpH Solids: varied

pH: 5.0

Glucoamylose: Spirizyme Achieve (Novozymes A/S)

Glucoamylose dose 0.6 AGU/g DS

Glucoamylose split: 50/50 with remainder added at 8 h

Fermentation time: 55 h

Temp. 32°C

Scale: 50 g Ankom bottle

As shown in Figures 1 and 2, Saccharomyces cerevisiae strain MBG5038 demonstrated improved ethanol yields and decreased glycerol levels when compared to Ethanol Red®.

Example 20: Fermentation of Saccharomyces cerevisiae strain MBG5038 under stress conditions

Saccharomyces cerevisiae strains MBG5038 and Ethanol Red® were fermented under the following conditions:

Mash: Avantec Amp

Solids 34.51 %

Glucoamylose: Spirizyme Excel (Novozymes A/S)

Glucoamylose dose: 0.6 AGU/g DS

Fermentation time: 54 h

Temp.: 32°C (7 h) 35°C (16 h) 32°C (31 h)

Scale: 5 g tube

As shown in Figures 3 and 4, Saccharomyces cerevisiae strain MBG5038 demonstrated improved ethanol yield and decreased residual glucose when compared to Ethanol Red® in the prescence of organic acid (lactic acid/acetic acid).

Example 21 : Fermentation of Saccharomyces cerevisiae strain MBG5012 under nonstress conditions

Saccharomyces cerevisiae strains MBG5038 and Ethanol Red® were fermented under the following conditions:

Mash: Avantec Amp supplemented with maltodextrin

Solids: 35% final (35% solids liquefact + maltodextrin to achieve 38% total solids) pH: 5.0

Glucoamylose: Spirizyme Excel (Novozymes A/S)

Glucoamylose dose 0.6 AGU/g DS

Glucoamylose split: 50/50 with remainder added at 8 h Fermentation time: 54 h

Temp. 32°C

Scale: 5 g tube

As shown in Figures 5 and 6, Saccharomyces cerevisiae strain MBG5012 demonstrated improved ethanol yields and decreased residual glucose when compared to Ethanol Red®.

Example 22: Fermentation of Saccharomyces cerevisiae strain MBG5012 under stress conditions

Saccharomyces cerevisiae strains MBG5012 and Ethanol Red® were fermented under the following conditions:

Mash: Avantec Amp

Solids 34.51 %

pH: 5.0

Glucoamylose: Spirizyme Excel (Novozymes A/S)

Glucoamylose dose: 0.6 AGU/g DS

Fermentation time: 54 h

Temp.: 32°C (7 h) 35°C (16 h) 32°C (31 h)

Scale: 5 g tube

As shown in Figures 7 and 8, Saccharomyces cerevisiae strain MBG5012 demonstrated improved ethanol yield and decreased residual glucose when compared to Ethanol Red® in the prescence of organic acid (lactic acid/acetic acid).