CARBOHYDRATE-ENRICHED RECOMBINANT MICROORGANISMS

REFERENCE TO SEQUENCE LISTING

The "Sequence Listing" submitted electronically concurrently herewith pursuant 37 C.F.R. § 1.821 in computer readable form (CRF) via EFS-Web as file name 200206_416WO_SEQUENCE_LISTING.txt is incorporated herein by reference. The electronic copy of the Sequence Listing was created on January 16, 2015, and the size on disk is 277 kilobytes.

FIELD OF THE INVENTION

The present disclosure relates to novel recombinant Ci metabolizing microorganisms comprising an engineered metabolic pathway for the enhanced production of carbohydrates, and related compositions and methods.

BACKGROUND

Advances in the efficiency in animal feed utilization have been achieved over the past several decades through the use of feed additives. These added substances augment the nutrient-content, energy-content, and/or disease fighting properties of animal feed compositions. A growing challenge for commercial animal producers is the rising cost of grain. The rising costs are due in part to competing demands for grains for biofuel and human food use. With the rising cost of grain and protein components, coupled with limited land available for feed production, alternative low cost animal feed products with beneficial nutritive and disease fighting properties would be highly desirable.

SUMMARY OF THE INVENTION

In one embodiment, the present disclosure provides a recombinant Ci metabolizing microorganism comprising an exogenous nucleic acid selected from the group consisting of an exogenous nucleic acid that encodes a carbohydrate biosynthesis enzyme and an exogenous nucleic acid that encodes an expression control sequence that is operably linked to a nucleic acid encoding a native carbohydrate biosynthesis enzyme, wherein the recombinant Ci metabolizing microorganism is capable of converting a natural gas-derived carbon feedstock into a desired carbohydrate. Typically, the natural gas-derived carbon feedstock is natural gas or methane.

In another embodiment, the present disclosure provides a biomass derived from the recombinant Ci metabolizing microorganism of the present disclosure.

In a further embodiment, the present disclosure provides a carbohydrate composition comprising carbohydrates extracted from the biomass of the present disclosure, wherein the composition exhibits a 5 ¹³ C that is less than -30%o.

In a still further embodiment, the present disclosure provides an animal feed comprising the biomass of the present disclosure.

In another embodiment, the present disclosure provides a culture or fermentation medium comprising the biomass or composition of the present disclosure.

The present disclosure additionally provides related methods.

DETAILED DESCRIPTION

The instant disclosure provides novel recombinant C i metabolizing microorganisms that have the ability to utilize relatively low-cost carbon feedstock as an energy source, as well as related biomass, compositions, and methods. The recombinant microorganisms of the present disclosure are engineered for the enhanced production of certain carbohydrates that are commercially desirable. These recombinant microorganisms, as well as the biomass and carbohydrate compositions that are derived from them, are useful as a source of nutrition for animals (such as, for example, livestock, fish, poultry, and the like), as well as cultured or fermented microorganisms.

In one embodiment, the present disclosure provides a recombinant Ci metabolizing microorganism, wherein the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid selected from the group consisting of an exogenous nucleic acid that encodes a carbohydrate biosynthesis enzyme and an exogenous nucleic acid that encodes an expression control sequence that is operably linked to a nucleic acid encoding a native carbohydrate biosynthesis enzyme, wherein the recombinant Ci metabolizing microorganism is capable of converting a natural gas carbon feedstock into the carbohydrate. When these recombinant microorganisms are cultured in the presence of a natural gas-derived Ci substrate, they typically exhibit a 5 ¹³ C of less than -30%o, and often less than -40%o, as described in more detail herein. Typically, the recombinant microorganism is a non-photosynthetic Ci metabolizing microorganism.

In these embodiments, the recombinant microorganisms of the present disclosure are engineered to convert a natural gas-derived feedstock, which is a relatively low cost and abundant resource (for example, natural gas, or a Ci substrate such as methane from natural gas) as compared to more costly carbohydrates, to higher valued carbohydrates. As used herein, the term "natural gas-derived feedstock" refers to natural gas, or any of the components isolated from natural gas (including Ci substrates) or converted from natural gas (i.e., syngas).

The term "natural gas" refers herein to naturally occurring gas mixtures that may be obtained by conventional processes (e.g., drilling and water flooding of porous reservoirs) or non-conventional processes (e.g., hydraulic fracturing, horizontal drilling or directional drilling of formations having low gas permeability). The gas mixtures are made up of methane and other compounds, including other Ci compounds, as well as other light alkane gases (such as, for example, ethane, propane, butane, pentane, and the like), carbon dioxide, nitrogen, hydrogen sulfide, or the like, and combinations thereof. Unconventional natural gas may be obtained from sources such as, for example, tight gas sands formed in sandstone or carbonate, coal bed methane formed in coal deposits and adsorbed in coal particles, shale gas formed in fine-grained shale rock and adsorbed in clay particles or held within small pores or microfractures, methane hydrates that are a crystalline combination of natural gas and water formed at low temperature and high pressure in places such as under oceans and permafrost.

As used herein, "Ci substrate" or "Ci compound" refers to any carbon containing molecule or composition that lacks a carbon-carbon bond. Exemplary Ci substrates include syngas, methane, methanol, formaldehyde, formic acid or a salt thereof, carbon monoxide, carbon dioxide, methylated amines (e.g., methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, methyl halogens (e.g., bromomethane, chloromethane, iodomethane, dichloromethane, etc.), cyanide, or any combination thereof. In certain embodiments of the present disclosure, a natural gas-derived feedstock may be natural gas, a Ci substrate from natural gas, or syngas. Typically, a Ci substrate is methane. Exemplary recombinant Ci metabolizing microorganisms that have utilized a natural gas-derived carbon substrate as a feedstock exhibit a distinctive isotopic carbon signature, which is described in more detail herein. This distinctive isoptopic carbon signature is also exhibited by the compositions and products of such recombinant microorganisms (e.g., biomass, carbohydrate compositions, and the like).

In another embodiment, the present disclosure provides a recombinant Ci metabolizing microorganism comprising an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme, wherein the C i metabolizing microorganism is capable of converting methane into a carbohydrate. Exemplary carbohydrates are glucans. In some embodiments, a carbohydrate is a β-(1 ,3)-glucan, and may be branched or unbranched or a mixture thereof. Usually, a Ci metabolizing microorganism is a non-photo synthetic Ci metabolizing microorganism.

As used herein, "Ci metabolizing microorganism" or "Ci metabolizing non-photosynthetic microorganism" refers to any microorganism having the ability to use a Ci substrate as a source of energy or as its primary source of energy and biomass, and may or may not use other carbon substrates (such as sugars and complex carbohydrates) for energy and biomass. For example, a Ci metabolizing microorganism may oxidize a Ci substrate, such as methane or methanol. Ci metabolizing microorganisms include bacteria (such as methanotrophs and methylotrophs) and yeast. In certain embodiments, a Ci metabolizing microorganism does not include a photosynthetic microorganism, such as algae. In some embodiments, the Ci metabolizing microorganism will be an "obligate Ci metabolizing microorganism," meaning its sole source of energy are Ci substrates. In further embodiments, a Ci metabolizing microorganism (e.g., methanotroph) will be cultured in the presence of a C i substrate feedstock (i. e. , using the C ₁ substrate as a source of energy).

Recombinant Ci metabolizing microorganisms of the present disclosure are engineered for enhanced production of a desired carbohydrate and in one embodiment, comprise an exogenous nucleic acid encoding a carbohydrate biosynthesis (CB) enzyme. The terms "carbohydrate biosynthesis enzyme" and "CB enzyme" are used interchangeably herein to refer to an enzyme that is involved in the production of a carbohydrate by the recombinant host Ci metabolizing microorganism.

Exogenous nucleic acids encoding CB enzymes that are employed in the practice of the present disclosure are typically codon optimized for optimal expression from the recombinant host Ci metabolizing microorganism and encode an enzyme that is either native to a species heterologous to the host Ci microorganism or is a mutant (i.e., variant) of an enzyme that exists in nature.

As used herein, the term "carbohydrate" refers to a monosaccharide, a disaccharide, or a polysaccharide. Suitable exogenous nucleic acids employed in the practice of the present disclosure include those which encode enzymes that are involved in the production of a monosaccharide such as, for example, glucose, fructose, ribose, glyceraldehyde, galactose and the like; a disaccharide, such as, for example lactose, sucrose, maltose, cellulobiose, and the like, and mixtures thereof; or a polysaccharide, including, for example, an unbranched or branched glucan, and the like, and mixtures thereof. Exemplary glucans include a-glucans, such as for example, dextran, glycogen, pullulan, starch, and the like, as well as β-glucans, such as, for example, P-l,4-glucan (i.e., cellulose), P-l,3-glucan, P-(l,3)(l,4)-glucan, P-(l,3)(l,6)-glucan, and the like, and mixtures thereof.

In a specific embodiments, the CB enzyme is an enzyme involved in the production of an unbranched or a branched glucan, or mixture thereof, β-glucans are known to have beneficial therapeutic properties, including as a powerful immune stimulant and a powerful antagonist to both benign and malignant tumors, β-glucans are also known to lower cholesterol and triglyceride levels. See D. Akramiene et al, Medicina (kaunas), 2007; 43 (8): 597. The β-glucans are a heterogeneous group of glucose polymers made up of β-D- glucopyranosyl units having β-(1,3) and/or β-(1,4), and/or β-(1,6) linkages. They have been isolated from a number of sources, including plants (oat, barley, bran, seaweed, corn, soy, and the like), bacteria (e.g., Pneumocystis carinii, Cryptococcus neoformans, Aspergillus fumigatus, Histoplasma capsulatum, Candida albicans, and the like), and fungi (i.e., Saccharomyces cerevisiae and mushrooms, such as, for example shiitake (Lentinus edodes), maitake (Grifola frondosa), schizophylan (Schizophillum commune), and SSG {Sclerotinia sclerotiorum). β-glucan extracts from Lentinus edodes and Schizophillum commune have been used for the treatment of cancer in Japan since 1980. Id.

Exogenous nucleic acids that are suitable for use in the practice of the present disclosure include those which encode enzymes involved in gluconeogenesis, glycogenesis, a- or β-glucan biosynthesis, and other metabolic pathways known to produce a carbohydrate.

Suitable exogenous nucleic acids include those which encode a gluconeogenesis enzyme selected from the group consisting of a pyruvate carboxylase, a phosphoenolpyruvate carboxykinase, an enolase, a phosphoglycerate mutase, a phosphoglycerate kinase, a glyceraldehyde-3 -phosphate dehydrogenase, a Type A aldolase, a fructose 1 ,6-bisphosphatase, a phosphofructokinase, a phosphoglucose isomerase, a hexokinase, a glucose-6-phosphate, and the like.

Other suitable exogenous nucleic acids include those which encode a glycogenesis enzyme selected from the group consisting of a glucose- 1 -phosphate adenyltransferase, a glycogen synthase, and the like.

The above enzymes can be found in a number of heterologous species, including microorganisms, such as, for example, bacteria and yeast, including, for example, E. coli, C. glutamicum, Saccharomyces cerevisiae, and the like, as well as higher order fungi, such as mushrooms, and the like, as well as algae, and plants.

Suitable exogenous nucleic acids include those which encode a glucan biosynthesis enzyme, such as, for example, a glucan synthase. An exemplary glucan synthase is β-1,3- glucan synthase. The exogenous nucleic acid may encode a glucan biosynthesis enzyme (e.g., a glucan synthase (such as, for example a P-l,3-glucan synthase)) from a plant (oat, barley, bran, seaweed, corn, soy, and the like), a bacteria (e.g., Pneumocystis carinii, Cryptococcus neoformans, Aspergillus fumigatus, Histoplasma capsulatum, Candida albicans, and the like), or a fungi (i.e., Saccharomyces cerevisiae and mushrooms, such as, for example shiitake {Lentinus edodes), maitake {Grifola frondosa), schizophylan {Schizophillum commune), and SSG {Sclerotinia sclerotiorum). The amino acid and nucleic acid sequences of a number of β-(1 ,3)-glucan synthases are known. See, e.g., U.S. Pat. No. 5,194,600, WO99/49047, and EP 0 724 644 Bl, all of which are incorporated herein by reference. In certain specific embodiments, the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme having the amino acid sequence of any of SEQ NOs: 2, 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, 36, or 38, shown in Table A, hereinbelow. As described above, the exogenous nucleic acid is typically codon optimized for optimal expression from the recombinant Ci microorganism. Exemplary nucleic acid sequences encoding these CB enzymes are also provided in Table A. These nucleic acid sequences have been codon optimized for expression in Methylococcus capsulatus Bath.

Table A. Exemplary Carbohydrate Biosynthesis Enzymes

Amino Acid Sequence Nucleic Acid Sequence

Source/Enzyme Name

(SEQ ID NO.) (SEQ ID NO.)

Horderum vulgar s (barley):

26 25

1,3-beta-D-glucan synthase

E.coli: Glucose- 1 -phosphate

adenyltransfersase (Acc. No. 28 27

YP 49003.1)

Cornebacterium. Glutamicum

(ATCC 13032): Glucose-1- 30 29

phosphate adenylyltransferase

Escherichia coli str. K-12

substr. W3110: Glycogen 32 31

Synthase

Cornebacterium glutamicum

(ATCC 13032): 34 33

Glycosyltransferase

E. coli: 1 ,4-alpha-glucan

branching enzyme (Acc. No. 36 35

YP 492001.1)

Cory neb acterium glutamicum

(ATCC 13032): Glycogen 38 37

branching enzyme

Suitable exogenous nucleic acids employed in the practice of the present disclosure include those which encode a variant CB enzyme sequence that is 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%o, or at least 99% identical to a reference or parental wild-type polypeptide sequence, such as, for example a reference sequence corresponding to any one of SEQ ID NOs:2, 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, 36, or 38, provided that the variant retains the carbohydrate biosynthesis enzyme activity of interest. In certain embodiments, the CB enzyme variant polypeptides will include at least one amino acid substitution (e.g., 1, 2, 3, 5, 6, 7, 8, 9 or 10 ormore or up to 20, 25, or 30 substitutions) at a pre-determined position relative to a reference or parental wild-type CB enzyme, provided that a variant retains the CB enzyme activity of interest. The CB enzyme variant polypeptides may further comprise one or more conservative substitutions. A "conservative substitution" is recognized in the art as a substitution of one amino acid for another amino acid that has similar properties. Exemplary conservative substitutions are well known in the art (see, e.g., WO 97/09433, p. 10; Lehninger, Biochemistry, 2 ^nd Edition; Worth Publishers, Inc. NY:NY (1975), pp.71-77; Lewin, Genes IV, Oxford University Press, NY and Cell Press, Cambridge, MA (1990), p. 8, which are incorporated herein by reference). Methods for generating suitable exogenous nucleic acids encoding such variant enzymes are described in more detail herein.

The "percent identity" between two or more nucleic acid or amino acid sequences is a function of the number of identical positions shared by the sequences (i.e., % identity=number of identical positions/total number of positions x 100), taking into account the number of gaps, and the length of each gap that needs to be introduced to optimize alignment of two or more sequences. The comparison of sequences and determination of percent identity between two or more sequences can be accomplished using a mathematical algorithm, such as BLAST and Gapped BLAST programs at their default parameters (e.g., Altschul et al., J. Mol. Biol. 215:403, 1990; see also BLASTN at the world wide web at ncbi.nlm.nih.gov/BLAST, which are incorporated herein by reference).

As indicated above, the exogenous nucleic acids encoding CB enzymes employed in the practice of the present disclosure may be codon optimized for expression in the Ci metabolizing microorganism. Expression of recombinant proteins may be difficult outside their original host. For example, variation in codon usage bias has been observed across different species of bacteria (Sharp et al., Nucl. Acids. Res. 33: 1 141 , 2005, which is incorporated herein by reference). Overexpression of recombinant proteins even within their native host may also be difficult. In certain embodiments, the nucleic acid to be introduced into a host as described herein may be subjected to codon optimization prior to introduction into the host to ensure protein expression is effective or enhanced. Codon optimization refers to alteration of codons in genes or coding regions of nucleic acids before transformation to reflect the typical codon usage of the host without altering the polypeptide encoded by the non-natural DNA molecule. Codon optimization methods for optimum gene expression in heterologous hosts have been previously described (see, e.g., Welch et al., PLoS One 4:e7002, 2009; Gustafsson et al., Trends Biotechnol. 22:346, 2004; Wu et al., Nucl. Acids Res. 35:D76, 2007; Villalobos et al., BMC Bioinformatics 7:285, 2006; U.S. Patent Publication Nos. 2011/0111413 and 2008/0292918; disclosure ofwhich methods are incorporated herein by reference, in their entirety). Exogenous nucleic acids encoding CB enzymes that are suitable for use in the practice of the present disclosure include those having a nucleic acid sequence that is at least about 85% identical to a nucleic acid reference sequence selected from the group consisting of SEQ ID NO. : 1, 3, 5, 7, 9, 11, 13, 15, 17, 19, 21, 23, 25, 27, 29, 31, 33, 35, and 37. In some embodiments, the exogenous nucleic acid encoding the CB enzyme has a nucleic acid sequence that is at least about 85%, at least about 86%>, at least about 87%>, at least about 88%>, at least about 89%>, at least about 90%, at least about 91%, at least about 92%, at least about 93%, at least about 94%, at least about 95%, at least about 96%, at least about 97%, at least about 98% and at least about 99%> sequence identity to a nucleic acid reference sequence selected from the group consisting of SEQ ID NO.: l, 3, 5, 7, 9, 11, 13, 15, 17, 19, 21, 23, 25, 27, 29, 31, 33, 35, and 37. Illustrative exogenous nucleic acids that encode a CB enzyme which are suitable for use in the practice of the invention include sequences which have been codon optimized for optimal expression in Methylococcus capsulatus Bath, such as, for example, any one of SEQ ID NO.: l, 3, 5, 7, 9, 11, 13, 15, 17, 19, 21, 23, 25, 27, 29, 31, 33, 35, and 37.

Similarly, exogenous nucleic acid molecules of this disclosure encoding polypeptide variants may be designed using the phylogenetic-based methods described in the references noted above (U.S. Patent No. 8,005,620; Gustafsson et al.; Welch et al.; Villalobos et al.; Minshull et al., all of which are incorporated herein by reference.).

An exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme includes polynucleotides that encode a polypeptide, a polypeptide fragment, a peptide, or a fusion polypeptide that has or retains the corresponding carbohydrate biosynthesis enzyme activity. Methods to determine whether a polypeptide has a particular activity by measuring the ability of the polypeptide to convert a substrate into a product are known in the art.

In some embodiments, the exogenous nucleic acid encodes an expression control sequence that is operably linked to a nucleic acid encoding a native carbohydrate biosynthesis enzyme. Typically, the expression control sequence is one that results in the overexpression of a native carbohydrate biosynthesis enzyme. As used herein, "overexpressed" and "overexpression" when referring to a gene or a protein means an increase in expression or activity of the gene or protein. Increased expression or activity includes expression or activity of a gene or protein being increased above the level of a wildtype (native or non-genetically engineered) control or reference microorganism. A gene or protein is overexpressed if the expression or activity is in a microorganism where it is not normally expressed or active. A gene or protein is overexpressed if the expression or activity is extended or present longer in the recombinant microorganism than in a wild-type control or reference microorganism.

In addition to the exogenous nucleic acids described hereinabove, recombinant Ci metabolizing microorganisms of the present disclosure may comprise further genetic modifications which enhance the production of the desired carbohydrate. For example, when the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme, the recombinant Ci metabolizing microorganism may further comprise an exogenous expression control sequence that is operatively linked to the exogenous nucleic acid encoding the carbohydrate biosynthesis enzyme to enhance production of the desired carbohydrate. Expression control sequences suitable for use in the practice of the present disclosure are described in more detail herein.

Alternatively, or in addition, the recombinant Ci metabolizing microorganism of the present disclosure may further comprise an exogenous expression control sequence operatively linked to an endogenous nucleic acid encoding an endogenous enzyme that utilizes one or more of the same substrates utilized by carbohydrate biosynthesis enzymes, or utilizes the desired carbohydrate as a substrate (i.e., a "competing" endogenous enzyme). This may be done to downregulate the competing endogenous enzyme.

In some embodiments, it may be desirable to reduce or inhibit a competing endogenous enzyme activity by mutating the competing endogenous enzyme to delete or attenuate its activity. "Inhibit" or "inhibited," as used herein, refers to an alteration, reduction, down regulation, abrogation or deletion, directly or indirectly, in the expression of a target gene or in the activity of a target molecule relative to a control, endogenous or reference molecule, wherein the alteration, reduction, down regulation or abrogation is statistically, biologically, industrially, or clinically significant.

Various methods for downregulating, inactivating, knocking-out, or deleting endogenous gene function in Ci metabolizing microorganisms are known in the art. For example, targeted gene disruption is an effective method for gene down-regulation where an exogenous polynucleotide is inserted into a structural gene to disrupt transcription. Genetic cassettes comprising the exogenous insertion DNA (e.g., a genetic marker) flanked by sequence having a high degree of homology to a portion of the target host gene to be disrupted are introduced into the host Ci metabolizing microorganism. Exogenous DNA disrupts the target host gene via native DNA replication mechanisms. Allelic exchange to construct deletion/insertional mutants in Ci metabolizing microorganisms, including methanotrophic bacteria, have been described in, for example, Toyama and Lidstrom, Microbiol. 144: 183, 1998; Stoylar et ah, Microbiol. 145 : 1235, 1999; Ali et al, Microbiol. 152:2931 , 2006; Van Dien et al, Microbiol. 149:601 , 2003; Martin and Murrell, FEMS Microbiol. Lett. 127:243, 2006, all of which are incorporated herein by reference.

For example, in some embodiments of the present disclosure, a recombinant Ci metabolizing microorganisms may further comprise a deletion of endogenous glycogen synthase activity and/or endogenous phosphoglucomutase activity. Enzymes involved in other pathways, such as an amino acid synthesis pathway, may also be targeted for down regulation to focus metabolic activities of the host microorganism on carbohydrate biosynthesis.

The recombinant Ci metabolizing microorganism may thus be engineered to have the ability to produce the desired carbohydrate at enhanced levels. In some of these embodiments, a recombinant Ci metabolizing microorganism produces the desired carbohydrate at a level that is at least about 10% greater than that produced by the native Ci metabolizing microorganism and up to about 2-fold, to about 3-, 4-, 5-, 10-, 20-, 30-, 40-, 50-, 60-, 70-, 80-, 90-, 100-, and up to about 500- or about 1000-fold the level produced by a native Ci metabolizing microorganism, when cultured in the presence of a natural gas-derived feedstock (e.g., natural gas, methane, and the like) under at least one set of culture conditions. In other embodiments, a recombinant Ci metabolizing microorganism produces the desired carbohydrate at a level that is from at least about 15%, at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%), at least about 45%, at least about 50%>, at least 55%, at least about 60%>, at least about 65%o, at least about 70%>, at least about 75%, at least about 80%>, at least about 85%, at least about 90%, or is at least about 95% greater than that produced by a native Ci metabolizing microorganism, and up to about 2-fold, to about 3-, 4-, 5-, 10-, 20-, 30-, 40-, 50-, 60-, 70-, 80-, 90-, 100-, to about 500- or about 1000-fold the level produced by the native Ci metabolizing microorganism, when cultured in the presence of a natural gas-derived feedstock under at least one set of culture conditions. Typically, the enhanced level of production of a desired carbohydrate by a recombinant C i metabolizing microorganism of the present invention is at least about 2-fold, 3-, 4-, 5-, 10-, 20-, 30-, 40-, 50-, 60-, 70-, 80-, 90-, or 100-fold that of the native Ci metabolizing microorganism, when cultured in the presence of a natural gas-derived feedstock under at least one set of culture conditions.

Recombinant methods for expression of exogenous nucleic acids in microbial organisms are well known in the art. Such methods can be found described in, for example, Sambrook et al., Molecular Cloning: A Laboratory Manual, Third Ed., Cold Spring Harbor Laboratory, New York (2001); and Ausubel et al., Current Protocols in Molecular Biology, John Wiley and Sons, Baltimore, MD (1999), all of which are incorporated herein by reference. Genetic modifications to nucleic acid molecules encoding enzymes, or functional fragments thereof, can confer a biochemical or metabolic capability to a recombinant cell that is altered from its naturally occurring state.

As used herein, the terms "endogenous" and "native" when referring to a nucleic acid, polypeptide, such as an enzyme, compound or activity refers to a nucleic acid, polypeptide, compound or activity that is normally present in a host cell. The term "homologous" or "homolog" refers to a molecule or activity from an exogenous (non- native) source that is the same or similar molecule or activity as that found in or derived from a host cell, species or strain.

As used herein, the term "exogenous" when referring to a nucleic acid molecule, construct or sequence refers to a nucleic acid molecule or portion of a nucleic acid molecule sequence that is not native to a cell in which it is expressed, a nucleic acid molecule or portion of a nucleic acid molecule native to a host cell that has been altered or mutated, or a nucleic acid molecule with an altered expression as compared to the native expression levels under similar conditions. For example, an exogenous control sequence (e.g., promoter, enhancer) may be used to regulate expression of a gene or a nucleic acid molecule in a way that is different than the gene or a nucleic acid molecule that is normally expressed in nature or culture. In certain embodiments, an exogenous nucleic acid molecule may be homologous to a native host cell gene, but may have an altered expression level or have a different sequence or both. In other embodiments, exogenous nucleic acid molecules may not be endogenous to a host cell or host genome, but instead may have been added to a host cell by conjugation, transformation, transfection, electroporation, or the like, wherein the added molecule may integrate into the host genome or can exist as extra-chromosomal genetic material (e.g., plasmid or other self-replicating vector).

In certain embodiments, more than one exogenous nucleic acid molecule can be introduced into a host cell as separate nucleic acid molecules, as a polycistronic nucleic acid molecule, as a single nucleic acid molecule encoding a fusion protein, or any combination thereof, and still be considered as more than one exogenous nucleic acid. For example, a Ci metabolizing microorganism can be modified to express two or more exogenous nucleic acid molecules, which may be the same or different, that encode one or more carbohydrate biosynthesis enzyme as disclosed herein. In certain embodiments, multiple copies of a carbohydrate biosynthesis enzyme- encoding polynucleotide molecule are introduced into a host cell, which may be two, three, four, five, six, seven, eight, nine, ten or more copies of the same carbohydrate biosynthesis enzyme or different carbohydrate biosynthesis enzyme encoding polynucleotides. Host Cells and Transformation Methods

In carrying out the practice of the present invention, the exogenous nucleic acids described hereinabove are transformed into a host cell that is a Ci metabolizing microorganism. The Ci metabolizing microorganism employed may be natural, strain adapted (e.g., performing fermentation to select for strains with improved growth rates and increased total biomass yield compared to the parent strain), or recombinantly modified to produce or overexpress the carbohydrate biosynthesis enzyme of interest and/or to have increased growth rates. Typically, the Ci metabolizing microorganism is a non- photosynthetic Ci microorganism (e.g., is not an algae or a plant).

In certain embodiments, the present disclosure employs Ci metabolizing microorganisms that are prokaryotes or bacteria, such as Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylophilus, Methylobacillus, Methylobacterium, Hyphomicrobium, Xanthobacter, Bacillus, Paracoccus, Nocardia, Arthrobacter, Rhodopseudomonas, or Pseudomonas.

In further embodiments, the Ci metabolizing bacteria employed is a methanotroph or a methylotroph. Exemplary methanotrophs include Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylocella, or a combination thereof. Exemplary methylotrophs include Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, Methylobacterium nodulans, or a combination thereof. As used herein, the term "methylotrophic bacteria" refers to any bacteria capable of oxidizing any compound in any form (e.g., solid, liquid, gas) that contains at least one carbon and that do not contain carbon-carbon bonds. In certain embodiments, a methylotrophic bacterium may be a methanotroph. For example, "methanotrophic bacteria" refers to any methylotrophic bacteria that have the ability to oxidize methane as a source of carbon and energy, which may be the primary source of carbon and energy. Exemplary methanotrophic bacteria include Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, or Methanomonas.

Methanotrophic bacteria are classified into three groups based on their carbon assimilation pathways and internal membrane structure: type I (gamma proteobacteria), type II (alpha proteobacteria, and type X (gamma proteobacteria). Type I methanotrophs use the ribulose monophosphate (RuMP) pathway for carbon assimilation whereas type II methanotrophs use the serine pathway. Type X methanotrophs use the RuMP pathway but also express low levels of enzymes of the serine pathway. Methanotrophic bacteria employed in the practice of the present invention include obligate methanotrophs, which can only utilize Ci substrates for carbon and energy sources, and facultative methanotrophs, which naturally have the ability to utilize some multi-carbon substrates as a carbon and energy source.

Exemplary facultative methanotrophs employed in the practice of the present invention include some species of Methylocella, Methylocystis, and Methylocapsa {e.g., Methylocella silvestris, Methylocella palustris, Methylocella tundrae, Methylocystis daltona strain SB2, Methylocystis bryophila, and Methylocapsa aurea KYG), Methylobacterium organophilum (ATCC 27,886), Methylibium petroleiphilum, or high growth variants thereof. Exemplary obligate methanotrophic bacteria useful in the practice of the present invention include Methylococcus capsulatus Bath (NCIMB 1 1 132), Methylomonas sp. 16a (ATCC PTA 2402), Methylosinus trichosporium OB3b (NRRL B- 1 1 , 196), Methylosinus sporium (NRRL B- 1 1 , 197), Methylocystis parvus (NRRL B- 1 1 , 198), Methylomonas methanica (NRRL B- 1 1 ,199), Methylomonas albus (NRRL B-l 1 ,200), Methylobacter capsulatus Y (NRRL B-l 1 ,201), Methylomonas flagellata sp. AJ-3670 (FERM P-2400), Methylacidiphilum infernorum, Methylacidiphilum fumariolicum, Methylomicrobium alcaliphilum, Methyloacida kamchatkensis, or high growth variants thereof.

Suitable Ci metabolizing microorganisms useful in the practice of the present invention include syngas metabolizing bacteria such as, for example, Clostridium, Moorella, Pyrococcus, Eubacterium, Desulfobacterium, Carboxydothermus, Acetogenium, Acetobacterium, Acetoanaerobium, Butyribaceterium, Peptostreptococcus, and the like. Exemplary syngas metabolizing bacteria include Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium woodii, Clostridium neopropanologen, and the like.

Other suitable Ci metabolizing microorganisms useful in the practice of the present invention include eukaryotes such as, for example, yeast, including Candida, Yarrowia, Hansenula, Pichia, Torulopsis, Rhodotorula, and the like.

Each of the microorganisms of this disclosure may be grown as an isolated culture, with a heterologous organism that may aid with growth, or one or more of these bacteria may be combined to generate a mixed culture. The term "heterologous" when referring to an organism refers to a species that is different from the host cell. In still further embodiments, Ci metabolizing non-photosynthetic microorganisms of this disclosure are obligate Ci metabolizing non-photosynthetic microorganisms, such as an obligate methanotroph or methylotroph.

Any one of the aforementioned Ci metabolizing microorganisms can be used as a parent or reference host cell to make a recombinant Ci metabolizing microorganisms of this disclosure. As used herein, "recombinant" refers to a non-naturally-occurring organism, microorganism, cell, nucleic acid molecule, or vector that has at least one genetic alteration or has been modified by the introduction of a exogenous nucleic acid molecule, or refers to a cell that has been altered such that the expression of an endogenous nucleic acid molecule or gene can be controlled. Recombinant also refers to a cell that is derived from a cell or is progeny of a cell having one or more such modifications. Genetic alterations include, for example, modifications introducing expressible nucleic acid molecules encoding proteins or enzymes, or other nucleic acid molecule additions, deletions, substitutions or other functional alteration of a cell's genetic material. For example, recombinant cells may express genes or other nucleic acid molecules that are not found in identical form within the native cell (i.e. , unmodified or wild type cell), or may provide an altered expression pattern of endogenous genes, such genes that may otherwise be over-expressed, under-expressed, minimally expressed, or not expressed at all.

Any of the recombinant Ci metabolizing microorganisms or methanotrophic bacteria described herein may be transformed to comprise at least one exogenous nucleic acid to provide the host with a new or enhanced activity (e.g., enzymatic activity) or may be genetically modified to remove or substantially reduce an endogenous gene function using any of a variety of methods known in the art.

Transformation refers to the introduction of a nucleic acid molecule (e.g. , exogenous nucleic acid molecule) into a host cell. The transformed host cell may carry the exogenous nucleic acid molecule extra-chromosomally or integrated in the chromosome. Integration into a host cell genome and self-replicating vectors generally result in genetically stable inheritance of the transformed nucleic acid molecule. Host cells containing the transformed nucleic acid molecules are referred to as "non-naturally occurring" or "genetically engineered" or "recombinant" or "transformed" or "transgenic" cells (e.g., bacteria).

Expression systems and expression vectors useful for the expression of exogenous nucleic acids in Ci metabolizing microorganisms (e.g., methanotrophic bacteria) are known.

Electroporation of Ci metabolizing bacteria is described herein and has been previously described in, for example, Toyama et al., FEMS Microbiol. Lett. 166: 1 , 1998; Kim and Wood, Appl. Microbiol. Biotechnol. 45: 105, 1997; Yoshida et al., Biotechnol. Lett. 23:181, 2001 , and U.S. Patent Appl. Pub. No. 2008/0026005.

Bacterial conjugation, which refers to a particular type of transformation involving direct contact of donor and recipient cells, is more frequently used for the transfer of nucleic acid molecules into Ci metabolizing bacteria. Bacterial conjugation involves mixing "donor" and "recipient" cells together in close contact with each other. Conjugation occurs by formation of cytoplasmic connections between donor and recipient bacteria, with unidirectional transfer of newly synthesized donor nucleic acid molecules into the recipient cells. A recipient in a conjugation reaction is any cell that can accept nucleic acids through horizontal transfer from a donor bacterium. A donor in a conjugation reaction is a bacterium that contains a conjugative plasmid, conjugative transposon, or mobilized plasmid. The physical transfer of the donor plasmid can occur through a self-transmissible plasmid or with the assistance of a "helper" plasmid. Conjugations involving Ci metabolizing bacteria is described herein and have been previously described in Stolyar et al., Mikrobiologiya 64:686, 1995; Motoyama et al., Appl. Micro. Biotech. 42:61, 1994; Lloyd et al, Arch. Microbiol. 171 :364, 1999; PCT Publication No. WO 02/18617; and Ali et al., Microbiol. 152:2931 , 2006.

Expression control sequences suitable for use in the practice of the present invention include, for example, promoters, terminators, enhancers, repressors, inducers, and the like. Promoters suitable for use in the practice of the present invention may be constitutive, leaky, or inducible, and native or non-native to the host cell employed. Exemplary promoters include a pyruvate decarboxylase (PDC) a promoter, a deoxy- xylulose phosphate synthase promoter, a methanol dehydrogenase promoter (MDH) (such as, for example, the promoter in the upstream intergenic region of the mxaF gene from Methylococcus capsulatus Bath (Acc. No. MCA0779) or the MDH promoter from M. extorquens (See Springer et al, FEMS Microbiol. Lett. 160: 1 19 (1998)), a hexulose 6- phosphate synthase promoter, a ribosomal protein S16 promoter, a serine hydroxymethyl transferase promoter, a serine-glyoxylate aminotransferase promoter, a phosphoenolpyruvate carboxylase promoter, a T5 promoter, Trc promoter, a promoter for PHA synthesis (Foellner et al., Appl. Microbiol. Biotechnol. 40:284, 1993), a pyruvate decarboxylase promoter (Tokuhiro et al., Appl. Biochem. Biotechnol. 131 :795, 2006), the lac operon Plac promoter (Toyama et al., Microbiol. 143:595, 1997), a hybrid promoter such as Ptrc (Brosius et al., Gene 27: 161 , 1984), promoters identified from native plasmid in methylotrophs (EP 296484), methanotrophs, and the like.

Additionally, suitable homologous or heterologous promoters for high expression of exogenous nucleic acid molecules may be utilized. For example, U.S. Patent No. 7,098,005 describes the use of promoters for high expression in the presence of methane or methanol of a heterologous coding nucleic acid in Ci metabolizing bacteria.

In certain embodiments, regulated expression of exogenous nucleic acids encoding a carbohydrate biosynthesis enzyme may be desirable to optimize growth rate of the non- naturally occurring Ci metabolizing microorganism and may improve bacterial growth in a variety of carbon source conditions. This may be achieved through the use of an inducible promoter system.

In certain embodiments, a nucleic acid encoding CB enzyme is operatively linked to an inducible promoter. Inducible promoter systems employed in the practice of the present invention include those known in the art and include tetracycline inducible promoter system; IPTG/lac operon inducible promoter system, heat shock inducible promoter system; metal-responsive promoter systems; nitrate inducible promoter system; light inducible promoter system; ecdysone inducible promoter system, the inducible/regulatable system described for use in methylotrophic and methanotrophic bacteria (see, e.g., U.S. Patent Appl. No. US 2010/0221813, which is incorporated herein by reference), and the like. For example, in one embodiment, the non-naturally occurring Ci metabolizing microorganism (e.g., methanotroph, methylotroph) comprises: (1) an exogenous nucleic acid encoding CB enzyme, operatively linked to a promoter flanked by lacO operator sequences, and (2) an exogenous nucleic acid encoding a lacl repressor protein operatively linked to a constitutive promoter (e.g., hexulose-6-phosphate synthase promoter). Induction is initiated when Lacl repressor protein binds to lacO operator sequences flanking the LDH or other promoter, preventing transcription. IPTG binds lacl repressor and releases it from lacO sequences, allowing transcription. By using an inducible promoter system, lactate synthesis may be controlled by the addition of an inducer.

The expression systems and expression vectors employed in the practice of the present invention optionally contain genetic elements, such as, for example, one or more ribosome binding sites for translation initiation and a transcription termination site, polyadenylation signals, restriction enzyme sites, multiple cloning sites, other coding segments, and the like. In certain embodiments, promoters and/or codon optimization (described in more detail hereinabove) are used for high constitutive expression of exogenous polynucleotides encoding one or more carbohydrate biosynthesis enzymes in host methanotrophic bacteria. Regulated expression of an exogenous nucleic acid in a host methanotrophic bacterium may also be utilized. For example, an inducible/regulatable system of recombinant protein expression in methylotrophic and methanotrophic bacteria as described in, for example, U.S. Patent Appl. No. US 2010/0221813 may be used.

Methods of Producing a Desired Carbohydrate

The present disclosure provides a method of producing a carbohydrate by culturing a recombinant Ci metabolizing microorganism of the present disclosure in the presence of methane (from any source), or a natural gas-derived carbon feedstock under conditions sufficient to produce the carbohydrate. In a specific embodiment, the present disclosure provides a method of producing a carbohydrate by culturing a recombinant Ci metabolizing microorganism in the presence of a natural gas-derived carbon feedstock under conditions sufficient to produce the carbohydrate, wherein the Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme. Typically, the natural gas-derived carbon feedstock is natural gas, methane, or syngas. Conditions for culturing exemplary Ci metabolizing microorganisms are illustrated in Example 1.

In a further embodiment, the present disclosure provides a method of producing a carbohydrate, said method comprising culturing a recombinant Ci metabolizing microorganism in the presence of methane under conditions sufficient to produce the carbohydrate, wherein the Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme. In this embodiment, methane from any source is suitable for use in the practice of the present invention, including natural gas, bio- methane, and the like. As used herein, the term "bio-methane" refers to methane generated by fermentation of organic matter such as, for example, manure, waste water sludge, municipal solid waste, and the like, under anaerobic conditions.

A variety of culture methodologies may be used for the microorganisms described herein. For example, Ci metabolizing microorganisms (such as methanotroph or methylotroph bacteria) may be grown by batch culture or continuous culture methodologies. In certain embodiments, the cultures are grown in a controlled culture unit, such as a fermentor, bioreactor, hollow fiber cell, or the like. Generally cells in log phase are often responsible for the bulk production of a product or intermediate of interest in some systems, whereas stationary or post-exponential phase production can be obtained in other systems.

A classical batch culturing method is a closed system in which the media composition is set when the culture is started and is not altered during the culture process. That is, media is inoculated at the beginning of the culturing process with one or more microorganisms of choice and then are allowed to grow without adding anything to the system. As used herein, a "batch" culture is in reference to not changing the amount of a particular carbon source initially added, whereas control of factors such as pH and oxygen concentration can be monitored and altered during the culture. In batch systems, metabolite and biomass compositions of the system change constantly up to the time the culture is terminated. Within batch cultures, cells (e.g., bacteria such as methylotrophs) will generally move from a static lag phase to a high growth logarithmic phase to a stationary phase where growth rate is reduced or stopped (and will eventually lead to cell death if conditions do not change).

A fed-batch system is a variation on the standard batch system in which a carbon substrate of interest is added in increments as the culture progresses. Fed-batch systems are useful when cell metabolism is likely to be inhibited by catabolite repression and when it is desirable to have limited amounts of substrate in the media. Since it is difficult to measure actual substrate concentration in fed-batch systems, an estimate is made based on changes of measureable factors such as pH, dissolved oxygen, and the partial pressure of waste gases. Batch and fed-batch culturing methods are common and known in the art (see, e.g., Thomas D. Brock, Biotechnology: A Textbook of Industrial Microbiology, 2 ^nd Ed. (1989) Sinauer Associates, Inc., Sunderland, MA; Deshpande, Appl. Biochem. Biotechnol. 36:221, 1992).

Continuous cultures are "open" systems in the sense that defined culture media is continuously added to a bioreactor while an equal amount of used ("conditioned") media is removed simultaneously for processing. Continuous cultures generally maintain the cells at a constant high, liquid phase density where cells are primarily in logarithmic growth phase. Alternatively, continuous culture may be practiced with immobilized cells {e.g., biofilm) where carbon and nutrients are continuously added and valuable products, byproducts, and waste products are continuously removed from the cell mass. Cell immobilization may be achieved with a wide range of solid supports composed of natural materials, synthetic materials, or a combination thereof.

Continuous or semi-continuous culture allows for the modulation of one or more factors that affect cell growth or end product concentration. For example, one method may maintain a limited nutrient at a fixed rate {e.g., carbon source, nitrogen) and allow all other parameters to change over time. In other embodiments, several factors affecting growth may be continuously altered while cell concentration, as measured by media turbidity, is kept constant. The goal of a continuous culture system is to maintain steady state growth conditions while balancing cell loss due to media being drawn off against the cell growth rate. Methods of modulating nutrients and growth factors for continuous culture processes and techniques for maximizing the rate of product formation are well known in the art (see Brock, 1992).

Liquid phase bioreactors (e.g., stirred tank, packed bed, one liquid phase, two liquid phase, hollow fiber membrane) are well known in the art and may be used for growth of non-naturally occurring microorganisms and biocatalysis.

By using gas phase bioreactors, substrates for bioproduction are absorbed from a gas by non-naturally occurring microorganisms, cell lysates or cell-free fractions thereof, rather than from a liquid. Use of gas phase bioreactors with microorganisms is known in the art (e.g., U.S. Patent Nos. 2,793,096; 4,999,302; 5,585,266; 5,079,168; and 6,143,556; U.S. Statutory Invention Registration H1430; U.S. Patent Application Publication No. 2003/0032170; Emerging Technologies in Hazardous Waste Management III, 1993, eds. Tedder and Pohland, pp 411-428). Exemplary gas phase bioreactors include single pass system, closed loop pumping system, and fiuidized bed reactor. By utilizing gas phase bioreactors, methane or other gaseous substrates are readily available for bioconversion by polypeptides with, for example, monooxygenase activity. In certain embodiments, methods for converting a gas into a carbohydrate are performed in gas phase bioreactors. In further embodiments, methods for converting a gas into a carbohydrate are performed in fiuidized bed reactors. In a fiuidized bed reactor, a fluid (i.e., gas or liquid) is passed upward through particle bed carriers, usually sand, granular-activated carbon, or diatomaceous earth, on which microorganisms can attach and grow. The fluid velocity is such that particle bed carriers and attached microorganisms are suspended (i.e., bed fluidization). The microorganisms attached to the particle bed carriers freely circulate in the fluid, allowing for effective mass transfer of substrates in the fluid to the microorganisms and increased microbial growth. Exemplary fiuidized bed reactors include plug-flow reactors and completely mixed reactors. Uses of fiuidized bed reactors with microbial bio films are known in the art (e.g., Pfluger et al., Bioresource Technol. 102:9919, 20\ \; Fenndl et al., Biotechnol, Bioengin. 40: 1218, 1992; Ruggeri etal, Water Sci. Technol. 29:341, 1994; U.S. Patent Nos. 4,032,407; 4,009, 098; 4,009,105; and 3,846,289). Recombinant Ci metabolizing microorganisms described in the present disclosure may be grown as an isolated pure culture, with a heterologous non-Ci metabolizing microorganism(s) that may aid with growth, or with one or more different strains or species of Ci metabolizing microorganisms may be combined to generate a mixed culture.

In certain embodiments, carbohydrates of the present disclosure are produced during a specific phase of cell growth (e.g., lag phase, log phase, stationary phase, or death phase). It may be desirable for carbon from feedstock to be converted to the carbohydrate rather than to growth and maintenance of Ci metabolizing microorganism. In some embodiments, non-naturally occurring Ci metabolizing microorganism (e.g., methanotrophs, methylotrophs) as provided herein are cultured to a low to medium cell density (OD ₆ oo) and then production of carbohydrate is initiated. In some embodiments, a carbohydrate is produced while methanotrophic bacteria are no longer dividing or dividing very slowly. In some embodiments, the carbohydrate is produced only during stationary phase. In some embodiments, the carbohydrate is produced during log phase and stationary phase.

The fermenter composition comprising the carbohydrate produced by a recombinant Ci metabolizing microorganism (e.g. , methanotrophs, methylotrophs) provided herein may further comprise other organic compounds associated with biological fermentation processes. For example, biological by-products of fermentation may include one or more of alcohols, epoxides, aldehydes, ketones, esters, or a combination thereof. In certain embodiments, the fermenter composition may contain one or more of the following alcohols: methanol, ethanol, butanol, or propanol. Other compounds, such as H ₂ 0, CO, C0 ₂ , CO N ₂ , H ₂ , 0 ₂ , and unutilized carbon feedstocks, such as methane, ethane, propane, and butane, may also be present in the fermenter off-gas.

In certain embodiments, the recombinant Ci metabolizing microorganisms (e.g. , methanotrophs, methylotrophs) provided herein produce a carbohydrate of the present invention at about 0.00 lg/L of culture to about 500g/L of culture. In some embodiments, the amount of carbohydrate produced is about lg/L of culture to about lOOg/L of culture. In some embodiments, the amount of carbohydrate produced is about 0.00 lg/L, 0.0 lg/L, 0.025g/L, 0.05g/L, O. lg/L, 0.15g/L, 0.2g/L, 0.25g/L, 0.3g/L, 0.4g/L, 0.5g/L, 0.6g/L, 0.7g/L, 0.8g/L, 0.9g/L, lg/L, 2.5g/L, 5g/L, 7.5g/L, lOg/L, 12.5g/L, 15g/L, 20g/L, 25g/L, 30g/L, 35g/L, 40g/L, 45g/L, 50g/L, 60g/L, 70g/L, 80g/L, 90g/L, lOOg/L, 125g/L, 150g/L, 175g/L, 200g/L, 225g/L, 250g/L, 275g/L, 300g/L, 325g/L, 350g/L, 375g/L, 400g/L, 425g/L, 450g/L, 475g/L, or 500g/L. Products

The present disclosure provides other useful products in addition to the recombinant Ci metabolizing cells described herein. In one embodiment, the present disclosure provides a biomass comprising a recombinant Ci metabolizing microorganism as described herein. In a specific embodiment, the present disclosure provides a biomass comprising a recombinant Ci metabolizing microorganism, wherein the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme and wherein the recombinant Ci metabolizing microorganism is capable of converting a natural gas-derived feedstock into a desired carbohydrate. In a specific embodiment, the exogenous nucleic acid encodes a β-glucan biosynthesis enzyme, for example, a P-(l ,3)-glucan synthase. In some embodiments, the biomass comprises a recombinant Ci metabolizing microorganism and a desired carbohydrate, wherein the desired carbohydrate is a β-glucan and the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a β-glucan biosynthesis enzyme, and wherein the Ci metabolizing microorganism is capable of converting a natural gas-derived feedstock into a β-glucan. Exemplary β-glucans inlcude a β-(l ,3)-glucan, a β-(1 ,3)(1 ,6)- glucan, a P-(l ,3)(l -4)-glucan, and a β-(l ,4)-glucan. In certain embodiments, the desired carbohydrate is selected from a β-(1 a P-(l ,3)(l ,6)-glucan, or a β-(1 ,3)(1.4)- glucan. In other embodiments, the desired carbohydrate is a β-(1

In a further embodiment, the present disclosure provides a biomass comprising a recombinant Ci metabolizing microorganism, wherein the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme and wherein the recombinant Ci metabolizing microorganism is capable of converting methane into a desired carbohydrate. In a specific embodiment, the exogenous nucleic acid encodes a β-glucan biosynthesis enzyme, for example, a β-(1 synthase, and the Ci metabolizing microorganism is capable of converting methane into a β-glucan. Typically the β-glucan is selected from the group consisting of a β-glucan, such as, for example, a P-(l ,3)-glucan, a P-(l ,3)(l ,6)-glucan, a P-(l ,3)(l ,4)-glucan, and a β- (1 ,4)-glucan. In certain embodiments, the desired carbohydrate is selected from the group consisting of a P-(l ,3)-glucan, a P-(l ,3)(l ,6)-glucan, a P-(l ,3)(l ,4)-glucan. In other embodiments, the desired carbohydrate is a P-(l ,3)-glucan.

As used herein, "biomass" refers to organic material having a biological origin, which may include one or more of whole cells, lysed cells, extracellular material, or the like. For example, the material harvested from a cultured microorganism (e.g., bacterial or yeast culture) is considered the biomass, which can include cells, cell membranes, cell cytoplasm, inclusion bodies, products secreted or excreted into the culture medium, or any combination thereof. In certain embodiments, biomass comprises the Ci metabolizing microorganisms of this disclosure together with the media of the culture in which the Ci metabolizing microorganisms of this disclosure were grown. In other embodiments, biomass comprises a Ci metabolizing microorganisms (whole or lysed or both) of this disclosure recovered from a culture grown on a Ci substrate (e.g., natural gas, methane, and the like). In still other embodiments, biomass comprises the spent media supernatant from a culture of Ci metabolizing microorganism cultured on a Ci substrate. Such a culture may be considered a renewable resource. Biomass of the present invention is enriched with respect to levels of the desired carbohydrate.

Recombinant Ci metabolizing microorganism of the present disclosure that are provided with a natural gas-derived substrate for cell growth are distinctive with respect to their carbon fingerprint as represented by their 5 ¹³ C values (as are the products derived from such recombinant Ci metabolizing microorganisms). By way of background, stable isotopic measurements and mass balance approaches are widely used to evaluate global sources and sinks of methane (see Whiticar and Faber, Org. Geochem. 10:159, 1986; Whiticar, Org. Geochem. 16: 531 , 1990). To use 5 ¹³ C values of residual methane to determine the amount oxidized, it is necessary to know the degree of isotopic fractionation caused by microbial oxidation of methane. For example, aerobic methanotrophs can metabolize methane through a specific enzyme, methane monooxygenase (MMO). Methanotrophs convert methane to methanol and subsequently formaldehyde. Formaldehyde can be further oxidized to C0 ₂ to provide energy to the cell in the form of reducing equivalents (NADH), or incorporated into biomass through either the RuMP or Serine cycles (Hanson and Hanson, Microbiol. Rev. 60:439, 1996), which are directly analogous to carbon assimilation pathways in photosynthetic organisms. More specifically, a Type I methanotroph uses the RuMP pathway for biomass synthesis and generates biomass entirely from CH ₄ , whereas a Type II methanotroph uses the serine pathway that assimilates 50-70% of the cell carbon from CH ₄ and 30-50% from C0 ₂ (Hanson and Hanson, 1996). Methods for measuring carbon isotope compositions are provided in, for example, Templeton etal. (Geochim. Cosmochim. Acta 70:1739, 2006), which methods are hereby incorporated by reference in their entirety. Examples 2 describes the characterization of stable carbon isotope distribution in the cells of different Ci metabolizing microorganisms. The highly negative 5 ¹³ C values for the cells was similarly reflected in the 5 ¹³ C of compounds extracted from these cells, i.e., lipid fractions. The 5 ¹³ C of the invention products described herein (i.e., a recombinant Ci metabolizing microorganism of the present disclosure as described herein), related biomass and carbohydrate compositions derived therefrom) can vary depending on the source and purity of the Ci substrate used as demonstrated in Example 2.

In certain embodiments, a recombinant Ci metabolizing microorganism of the present disclosure, and related biomass and carbohydrate compositions derived therefrom, exhibit a 5 ¹³ C of less than -30%o, less than -31%o, less than -32% ₀ , less than -33%o, less than -34%o, less than -35%o, less than -36%o, less than -37%o, less than -38%o, less than -39%o, less than -40%o, less than -41%o, less than -42%o, less than -43%o, less than -44%o, less than -45%o, less than -46%o, less than -47%o, less than -48%o, less than -49%o, less than -50%o, less than -51%o, less than -52%o, less than -53%o, less than -54%o, less than -55%o, less than -56%o, less than -57%o, less than -58%o, less than -59%o, less than -60%o, less than -61%o, less than -62%o, less than -63%o, less than -64%o, less than -65%o, less than -66%o, less than -67%o, less than -68%o, less than -69%o, or less than -70%o. In certain embodiments, a recombinant Ci metabolizing microorganism of the present disclosure, and related biomass and carbohydrate compositions derived therefrom, exhibit a 5 ¹³ C of about -35%o to about -50%o, -45%o to about -35%o, or about -50%o to about -40%o, or about -45%o to about -65%o, or about -60%o to about -70%o, or about -30%o to about -70%o.

In further embodiments, a Ci metabolizing non-photosynthetic microorganism biomass has a 5 ¹³ C of less than about -30%o, or ranges from about -40%o to about -60%o. In certain embodiments, the biomass comprises a recombinant Ci metabolizing non-photosynthetic microorganism together with the spent media, or the biomass comprises a spent media supernatant composition from a culture of a recombinant Ci metabolizing non-photosynthetic microorganism, wherein the 5 ¹³ C of the biomass is less than about -30%o. In certain other embodiments, the carbohydrate composition is extracted or concentrated from a biomass, which can comprise recombinant Ci metabolizing non-photosynthetic microorganisms together with the spent media from a culture, or a spent media supernatant composition from a culture of a recombinant Ci metabolizing non-photosynthetic microorganism.

In certain embodiments, a carbohydrate composition derived from a Ci metabolizing microorganism (which may optionally be an extract or isolate from the Ci metabolizing microorganism biomass) comprises hydrogen, oxygen, and carbon atoms of at least about 50% to about 80% of the weight of the composition, and wherein the 5 ¹³ C of the composition is less than about -35%o or less than about -36%o or less than about -37%o or less than about -38%o or less than about -39%o or less than about -40%o. In certain embodiments, a carbohydrate composition derived therefrom comprises molecules having hydrogen, oxygen, and carbon atoms, wherein the hydrogen, oxygen, and carbon atoms are at least 50%, at least 55%, at least 60%, at least 65%, at least 70%, at least 75%, or at least 80%, or at least 90%, or at least 95% of the weight of the composition and wherein the 5 ¹³ C of the composition ranges from about -30%o to about -70%o, or wherein the 5 ¹³ C in the biomass decreases as cell density increases by about -5%o to about -20%o, or wherein the 5 ¹³ C of the biomass is higher than that of C0 ₂ produced at the same time by an average of 5%o to 15%o when cultured in the presence or absence of copper. Typically, a carbohydrate composition comprises a polysaccharide, and in some instances, it comprises a monosaccharide. In other embodiments the carbohydrate composition comprises a disaccharide. In some embodiments, the carbohydrate comprises a β-glucan. Typically, the β-glucan is a P-(l ,3)-glucan. In other embodiments, the β- glucan is a β-(1 ,3)(1 ,6)-glucan, or a β-(1 ,3)(1 ,4)-glucan, or a β-(1 ,6)-glucan. Carbohydrate compositions derived from recombinant Ci metabolizing microorganisms cultivated in the presence of a natural gas-derived substrate exhibit the 5 ¹³ C values described hereinabove.

Characterization of 5 ¹³ C of some Ci metabolizing microorganisms cultivated in the presence of a natural gas-derived feedstock is illustrated in the examples, hereinbelow.

The present disclosure further provides an animal feed comprising the recombinant

Ci metabolizing microorganism, related biomass, and/or carbohydrate composition of the present disclosure. As contemplated in the practice of the present invention, the animal feed may be a livestock feed (such as, for example, pig feed, cattle feed, sheep feed, and the like), a poultry feed (such as, for example, chicken feed, turkey feed, and the like), or a fish feed (such as, for example, salmon feed, shell fish feed, and the like). The animal feed may further comprise an additive, such as, for example, a plant-derived material (including, for example, those derived from grains such as, for example, corn, barley, oats, rice, rye, wheat, sorghum, Brewer's spent grain, and the like; and those derived from legumes, such as, for example, alfalfa, clover, peas, beans, lentils, soybeans, and the like), an animal- derived material (such as, for example, fish meal), and/or a microorganism-derived material (including, for example, biomass from a heterologous microorganism that may be, for example, a bacteria, a yeast, or an algae). In some embodiments, the plant-derived material additive is soy meal or pea protein,

In a further embodiment, the present disclosure provides a culture or fermentation medium comprising the recombinant Ci metabolizing microorganism, related biomass, and/or carbohydrate composition of the present disclosure. Typically, the culture or fermentation medium further comprises an amino acid and/or water. In an additional embodiment, the present disclosure provides a cell culture composition comprising a culture or fermentation medium as described herein, and a second microorganism. Typically, a second microorganism is a bacteria, a yeast, or an algae. Embodiments of the present invention include the following:

1. A biomass derived from a culture of a recombinant Ci metabolizing microorganism, wherein the recombinant microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme, wherein the recombinant Ci metabolizing is capable of converting a natural gas-derived carbon feedstock into a desired carbohydrate.

2. A biomass derived from a culture of a recombinant Ci metabolizing microorganism, wherein the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme, wherein the recombinant Ci metabolizing microorganism is capable of converting methane into a desired carbohydrate.

3. The biomass of any of embodiments 1-2, wherein the recombinant Ci metabolizing microorganism is a non-photosynthetic Ci metabolizing microorganism.

4. The biomass of any of embodiments 1-3, wherein the carbohydrate is selected from the group consisting of a polysaccharide, a disaccharide, and a monosaccharide.

5. The biomass of embodiment 4, wherein the carbohydrate is a monosaccharide.

6. The biomass of embodiment 4, wherein the carbohydrate is a disaccharide. 7. The biomass of embodiment 4, wherein the carbohydrate is a polysaccharide.

8. The biomass of embodiment 7, wherein the polysaccharide is a β-glucan.

9. The biomass of embodiment 8, wherein the β-glucan is P-(l ,3)-glucan.

10. The biomass of embodiment 8, wherein the β-glucan is β-(1 ,3)(1 ,6)-glucan. 1 1. The biomass of embodiment 8, wherein the β-glucan is β-(1 ,3)(1 ,4)-glucan.

12. The biomass of embodiment 8, wherein the β-glucan is β-(l ,4)-glucan.

13. The biomass of embodiment 8, wherein the β-glucan is β-(l ,6)-glucan.

14. The biomass of any of embodiments 1-13, wherein the sequence of the exogenous nucleic acid is codon optimized for optimal expression from the recombinant Ci metabolizing microorganism. 15. The biomass of any of embodiments 1-14, wherein the exogenous nucleic acid encodes a gluconeogenesis enzyme.

16. The biomass of embodiment 15, wherein the gluconeogenesis enzyme is selected from the group consisting of a pyruvate carboxylase, a phosphoenolpyruvate carboxykinase, an enolase, a phosphoglycerate mutase, a phosphoglycerate kinase, a glyceraldehyde-3 -phosphate dehydrogenase, a Type A aldolase, a fructose 1,6- bisphosphatase, a phosphofructokinase, a phosphoglucose isomerase, a hexokinase, and a glucose-6-phosphate.

17. The biomass of any of embodiments 1-14, wherein the exogenous nucleic acid encodes a glycogenesis enzyme.

18. The biomass of embodiment 17, wherein the glycogenesis enzyme is selected from the group consisting of a glucose- 1 -phosphate adenyltransferase, a glycogen synthase, and a 1 ,4-alpha-glucan-branching protein.

19. The biomass of any of embodiments 8-14, wherein the exogenous nucleic acid is a β-glucan synthase.

20. The biomass of any of embodiments 1-19, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to a bacteria.

21. The biomass of any of embodiments 1-19, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to an organism selected from the group consisting of a yeast, a fungi, and a plant.

22. The biomass of any of embodiments 1-19, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to a microorganism selected from the group consisting of E. coli and C. glutamicum.

23. The biomass of any of embodiments 1-14, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme selected from the group consisting of any of SEQ ID NOs:2, 4, 6, 8 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, 36, and 38.

24. The biomass of any of embodiments 1-23, wherein the exogenous nucleic acid encoding carbohydrate biosynthesis pathway enzyme is operatively linked to an expression control sequence. 25. The biomass of embodiment 24, wherein the expression control sequence is an exogenous expression control sequence.

26. The biomass of any of embodiments 1-25, wherein the Ci metabolizing microorganism further comprises a deletion of an endogenous enzyme activity.

27. The biomass according to any of embodiments 1-26, wherein the Ci metabolizing microorganism is a methanotroph.

28. The biomass according to embodiment 27, wherein the methanotroph is Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylocella, or Methylocapsa.

29. The biomass of embodiment 27, wherein the methanotroph is selected from the group consisting of Methylococcus capsulatus Bath strain, Methylomonas methanica 16a (ATCC PTA 2402), Methylosinus trichosporium OB3b (NRRL B- 1 1 , 196), Methylosinus sporium (NRRL B- 1 1 , 197), Methylocystis parvus (NRRL B- 1 1 , 198), Methylomonas methanica (NRRL B- 1 1 ,199), Methylomonas albus (NRRL B- 1 1 ,200), Methylobacter capsulatus (NRRL B- 1 1 ,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P-2400), Methylocella silvestris, Methylocella palustris (ATCC 700799), Methylocella tundrae, Methylocystis daltona strain SB2, Methylocystis bryophila, Methylocapsa aurea KYG, Methylacidiphilum infernorum, Methylibium petroleiphilum, and Methylomicrobium alcaliphilum.

30. The biomass according to any one of embodiments 1 and 3-29, wherein the natural gas-derived carbon feedstock is selected from the group consisting of natural gas, syngas, methane, methanol, formaldehyde, formic acid, carbon monoxide, carbon dioxide, cyanide, a methylamine, a methylthiol, a methylhalogen, and any combination or two or more thereof.

31. The biomass of embodiment 30, wherein the natural gas-derived carbon feedstock is natural gas.

32. The biomass of any of embodiments 1 , and 3- 30, wherein the natural gas- derived carbon feedstock is methane.

33. The biomass of embodiment 30, wherein the natural gas-derived carbon feedstock is syngas. 34. The biomass of embodiment 30, wherein the Ci metabolizing microorganism is a syngas metabolizing bacteria.

35. The biomass according to embodiment 34, wherein the syngas metabolizing bacteria is selected from the group consisting of Clostridiumautoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyridbacterium methylotrophicum, Clostridium woodii, and Clostridium neopropanologen.

36. The biomass according to any one of embodiments 1 and 3-35, wherein the 5 ¹³ C of the biomass is less than -40%o.

37. The biomass of embodiment 2, wherein the methane is bio-methane. 38. A composition comprising a carbohydrate composition, wheren the carbohydrate composition exhibits a 5 ¹³ C of less than -40%o.

39. The composition of embodiment 38 , wherein the carbohydrate comprises a β- glucan.

40. The composition of embodiment 39, wherein the β-glucan is β-(1 ,3)-glucan. 41. An animal feed comprising the biomass of any of embodiments 1 -37 or the composition of any of embodiments 38-40.

42. The animal feed of embodiment 41, further comprising a plant-derived material.

43. The animal feed of embodiment 41, wherein the plant-derived material is selected from the group consisting of soybean meal and pea protein.

44. A culture or fermentation medium comprising the biomass of any of embodiments 1-37 or the composition of any of embodiments 38-40.

45. A recombinant Ci metabolizing microorganism, wherein the recombinant microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme, wherein the recombinant C i metabolizing.microorganism is capable of converting a natural gas-derived carbon feedstock into a desired carbohydrate.

46. A recombinant Ci metabolizing microorganism, wherein the recombinant Ci metabolizing microorganism comprises an exogenous nucleic acid encoding a carbohydrate biosynthesis enzyme, wherein the recombinant Ci metabolizing microorganism is capable of converting methane into a desired carbohydrate. 47. The recombinant Ci metabolizing microorganism of any of embodiments 45-46, wherein the recombinant Ci metabolizing microorganism is a non-photosynthetic Ci metabolizing microorganism.

48. The recombinant Ci metabolizing microorganism of any of embodiments 45-47, wherein the carbohydrate is selected from the group consisting of a polysaccharide, a disaccharide, and a monosaccharide.

49. The recombinant Ci metabolizing microorganism of embodiment 48, wherein the carbohydrate is a monosaccharide.

50. The recombinant Ci metabolizing microorganism of embodiment 48, wherein the carbohydrate is a disaccharide.

51. The recombinant Ci metabolizing microorganism of embodiment 48, wherein the carbohydrate is a polysaccharide.

52. The recombinant Ci metabolizing microorganism of embodiment 51 , wherein the polysaccharide is a β-glucan.

53. The recombinant Ci metabolizing microorganism of embodiment 52, wherein the β-glucan is P-(l ,3)-glucan.

54. The recombinant Ci metabolizing microorganism of embodiment 52, wherein the β-glucan is P-(l ,3)(l ,6)-glucan.

55. The recombinant Ci metabolizing microorganism of embodiment 52, wherein the β-glucan is β-(1 ,3)(1 ,4) -glucan.

56. The recombinant Ci metabolizing microorganism of embodiment 52, wherein the β-glucan is P-(l ,4)-glucan.

57. The recombinant Ci metabolizing microorganism of embodiment 52, wherein the β-glucan is P-(l ,6)-glucan.

58. The recombinant Ci metabolizing microorganism of any of embodiments

45-57, wherein the sequence of the exogenous nucleic acid is codon optimized for optimal expression from the recombinant Ci metabolizing microorganism.

59. The recombinant Ci metabolizing microorganism of any of embodiments 45-58, wherein the exogenous nucleic acid encodes a gluconeogenesis enzyme. 60. The recombinant Ci metabolizing microorganism of embodiment 59, wherein the gluconeogenesis enzyme is selected from the group consisting of a pyruvate carboxylase, a phosphoenolpyruvate carboxykinase, an enolase, a phosphoglycerate mutase, a phosphoglycerate kinase, a glyceraldehyde-3 -phosphate dehydrogenase, a Type A aldolase, a fructose 1 ,6-bisphosphatase, a phosphofructokinase, a phosphoglucose isomerase, a hexokinase, and a glucose-6-phosphate.

61. The recombinant Ci metabolizing microorganism of any of embodiments 45-58, wherein the exogenous nucleic acid encodes a glycogenesis enzyme.

62. The recombinant Ci metabolizing microorganism of embodiment 61 , wherein the glycogenesis enzyme is selected from the group consisting of a glucose- 1- phosphate adenyltransferase, a glycogen synthase, and a 1 ,4-alpha-glucan-branching protein.

63. The recombinant Ci metabolizing microorganism of any of embodiments 52-57, wherein the exogenous nucleic acid is a β-glucan synthase.

64. The recombinant Ci metabolizing microorganism of any of embodiments

45-63, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to a bacteria.

65. The recombinant Ci metabolizing microorganism of any of embodiments 45-63, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to an organism selected from the group consisting of a yeast, a fungi, and a plant.

66. The recombinant Ci metabolizing microorganism of any of embodiments 45-63, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme that is endogenous to a microorganism selected from the group consisting of E. coli, and C. glutamicum.

67. The recombinant Ci metabolizing microorganism of any of embodiments 45-57, wherein the exogenous nucleic acid encodes a carbohydrate biosynthesis enzyme selected from the group consisting of any of SEQ ID NOs: 2, 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, 36, and 38. 68. The recombinant Ci metabolizing microorganism of any of embodiments 45-67, wherein the exogenous nucleic acid encoding carbohydrate biosynthesis pathway enzyme is operatively linked to an expression control sequence.

69. The recombinant Ci metabolizing microorganism of embodiment 68, wherein the expression control sequence is an exogenous expression control sequence.

70. The recombinant Ci metabolizing microorganism of any of embodiments 45-69, wherein the Ci metabolizing microorganism further comprises a deletion of an endogenous enzyme activity.

71. The recombinant Ci metabolizing microorganism according to any of embodiments 45-70, wherein the Ci metabolizing microorganism is a methanotroph.

72. The recombinant Ci metabolizing microorganism according to embodiment 71 , wherein the methanotroph is Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylocella, or Methylocapsa.

73. The recombinant Ci metabolizing microorganism of embodiment 71 , wherein the methanotroph is selected from the group consisting of Methylococcus capsulatus Bath strain, Methylomonas methanica 16a (ATCC PTA 2402), Methylosinus trichosporium OB3b (NR L B- 1 1 ,196), Methylosinus sporium (NRRL B- 1 1 , 197), Methylocystis parvus (NRRL B- 1 1 ,198), Methylomonas methanica (NRRL B- 1 1 , 199), Methylomonas albus (NRRL B-l 1 ,200), Methylobacter capsulatus (NRRL B-l 1 ,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P- 2400), Methylocella silvestris, Methylocella palustris (ATCC 700799), Methylocella tundrae, Methylocystis daltona strain SB2, Methylocystis bryophila, Methylocapsa aurea KYG, Methylacidiphilum infernorum,Methylibium petroleiphilum, and Methylomicrobium alcaliphilum.

74. The recombinant Ci metabolizing microorganism according to any one of embodiments 45 and 47-73 wherein the natural gas-derived carbon feedstock is selected from the group consisting of natural gas, syngas, methane, methanol, formaldehyde, formic acid, carbon monoxide, carbon dioxide, cyanide, a methylamine, a methylthiol, a methylhalogen, and any combination or two or more thereof. 75. The recombinant Ci metabolizing microorganism of embodiment 74, wherein the natural gas-derived carbon feedstock is natural gas.

76. The recombinant Ci metabolizing microorganism of embodiment 74, wherein the natural gas-derived carbon feedstock is methane.

77. The recombinant Ci metabolizing microorganism of embodiment 74, wherein the natural gas-derived carbon feedstock is syngas.

78. The recombinant Ci metabolizing microorganism of embodiment 77, wherein the Ci metabolizing microorganism is a syngas metabolizing bacteria.

79. The biomass according to embodiment 78, wherein the syngas metabolizing bacteria is selected from the group consisting of Clostridiumautoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyridbacterium methylotrophicum, Clostridium woodii, and Clostridium neopropanologen.

80. The recombinant Ci metabolizing microorganism according to any one of embodiments 45 and 47-79, wherein the 5 ¹³ C of the biomass is less than -40%o.

81. The recombinant Ci metabolizing microorganism of embodiment 46, wherein the methane is bio-methane.

82. A method of producing a carbohydrate, said method comprising culturing the recombinant Ci metabolizing microorganism of any of embodiments 45 and 47-68 in the presence of a natural gas-derived carbon feedstock under conditions sufficient to produce the carbohydrate.

83. A method of producing a carbohydrate, said method comprising culturing the recombinant Ci metabolizing microorganism of embodiment 46 in the presence of a methane under conditions sufficient to produce the carbohydrate.

84. The method of embodiment 83, wherein the carbohydrate is a β-glucan. 85. A carbohydrate produced by the method of embodiment 82, wherein the carbohydrate exhibits a 5 ¹³ C in the range of from about -40%o to about -60%o.

The foregoing and other aspects of the invention may be better understood in connection with the following, non-limiting examples. EXAMPLES

EXAMPLE 1

CULTURE AND BIOREACTOR CONDITIONS FOR Ci METABOLIZING MICROORGANISMS

Exemplary Ci metabolizing microorganisms of the instant disclosure (methanotrophs, methylotrophs, Clostridia) were cultured in tubes, in vials, in bottles, on plates, or in a bioreactor (fermentation). Growth conditions, media, and carbon source for various microorganisms are described in this example.

Methylosinus trichosporium strain OB3b (NCIMB 11131); Methylomonas sp. strain 16a (ATCC PTA-2402); or Methylomonas methanica

For serum bottles, the bacteria were cultured at 30°C in Higgins minimal nitrate salts medium (NSM; Cornish et al., J. Gen. Microbiol. 130:2565, 1984; Park et al., Biotechnol. Bioeng. 38:423, 1991) or MM-Wl medium. The headspace composition was adjusted to a 1 : 1 volume of methane:air. The bottles were shaken at a rate of 200-250 rpm. Alternatively, the culture was maintained on NSM-media plates containing 1.5% w/v agar grown in a gas-tight chamber containing a 1 : 1 (v/v) methane:air gas mixture, or in the presence of methanol vapor (via 0.5 mL methanol in the lid of parafilm-sealed plates) or on NSM-media plates supplemented with 0.5% methanol. Plates were incubated inverted in a humidified chamber at 30°C.

The composition of the NSM medium used was as follows: 1.0 g MgS0 ₄ *7H ₂ 0, 0.20 g CaCl ₂ *6H ₂ 0, 2.0 ml chelated iron solution (0.1 g ferric (III) ammonium citrate or 0.5 g ferric (III) chloride; 0.2 g EDTA, sodium salt; 0.3 ml HC1, concentrated; 100.0 ml distilled deionized H ₂ 0), 1.0 g KN0 ₃ , 0.5 ml trace element solution (500.0 mg EDTA, 200.0 mg FeS0 ₄ . 7H ₂ 0, 10.0 mg ZnS0 ₄ *7H ₂ 0, 3.0 mg MnCl ₂ *4H ₂ 0, 30.0 mg H ₃ B0 ₃ , 20.0 mg CoCl ₂ *6H ₂ 0, 1.0 mg CaCl ₂ *2H ₂ 0, 2.0 mgNiCl ₂ *6H ₂ 0, 3.0 mgNa ₂ Mo0 ₄ *2H ₂ 0, 1.0 L distilled water), 0.272 g KH ₂ P0 ₄ , 0.717 g Na ₂ HP0 ₄ * 12H ₂ 0, optionally 12.5 g purified agar (e.g., Oxoid L28 or Bacto™ agar; used when making plates), 1.0 L distilled deionized water, pH adjusted to 6.8 and autoclaved at 121°C for 15 minutes. For fermentation, a 2-liter bioreactor containing 1L of sterilized defined media MM-W1 was inoculated with cells from serum bottle batch cultures (10-20% v/v) grown in MM-W1 supplied with a 1 : 1 (v/v) mixture of methane and air. The composition of medium MM-W1 used was as follows: 0.8 mM MgS0 ₄ * 7H ₂ 0, 10 mM NaN0 ₃ , 0.14 mM CaCl ₂ , 1.2 mMNaHC0 ₃ , 2.35 mM KH ₂ P0 ₄ , 3.4 mM K ₂ HP0 ₄ , 20.7 μΜ Na ₂ Mo0 ₄ * 2H ₂ 0, ΙμΜ CuS0 ₄ * 5H ₂ 0, 10 μΜ Fe ⁱⁿ -Na-EDTA, and 1 mL per liter of trace metals solution (containing, per liter 500 mg FeS0 ₄ * 7H ₂ 0, 400 mg ZnS0 ₄ * 7H ₂ 0, 20 mg MnCl ₂ * 7H ₂ 0, 50 mg CoCl ₂ * 6H ₂ 0, 10 mg NiCl ₂ * 6H ₂ 0, 15 mg H ₃ B0 ₃ , 250 mg EDTA). Phosphate, bicarbonate, and Fe ⁱⁿ -Na-EDTA were added after the media was autoclaved and cooled. Bicarbonate was added up to 0.1% (w/v) in certain fermentations. The reactor contents were stirred with an overhead impeller at a constant 750 rpm. The culture was fed with a constant methane sparging at about 60 mL/min to about 120 mL/min, while concentrated oxygen (at least 85%) was supplied at a variable rate of about 10-100 mL/min to maintain a dissolved oxygen level of about 40% to about 80% (relative to air saturation of the media).

Temperature in the bioreactor was maintained at 30°C and pH was maintained at 7.1 ± 0.1 using automated addition of 0.5M NaOH and 0.5M HC1, along with other additions, to the culture about every 4 hours to about 24 hours (corresponding to an OD ₆ oo increase of approximately 5 OD units). The other additions alternated between a metal addition (10 μΜ CuS04, 5 μΜ FeS04, 5 μΜ Fe ^m -Na-EDTA final concentrations) and a nutrient addition (5.75 mM KxHyP04, 10 mM NaN03). Under these conditions, essentially linear growth was observed, with an effective biomass generation rate of about 2.7 to about 3.3 grams dry cell weight per liter per day to an OD ₆ oo of greater than 20. Culture biomass was harvested by centrifugation, washed once in MM-W1 media, and recovered biomass was either frozen at -80°C or used immediately for fractionation of cellular components (e.g., lipid extraction).

A semi-continuous fermentation approach can also be applied to maintain biomass productivity and reduce time associated with fermentation shut-down and start-up (i.e., turn-around time or lead time). Harvesting of the bacterial biomass was performed at approximately 12-24 hour intervals, as the culture density approached (but before entering) stationary phase. Approximately half of the bioreactor volume was removed by transferring to a separate container via centrifugal pump. An equal volume of sterilized or recycled media was then returned to the bioreactor such that the optical density of the reactor was approximately half of its initial value. The bioreactor fermentation was continued according to the above protocol so that multiple cycles of growth and biomass recovery could be carried out during a single fermentation run.

Methylococcus capsulatus Bath (NCIMB 11132)

The bacteria were cultured at 42°C in serum bottles containing Higgins minimal nitrate salts medium (NSM) or MM-W1 medium. The headspace composition was adjusted to a 1 : 1 volume of methane : air. The bottles were shaken at a rate of 200-250 rpm. Alternatively, the culture was maintained on NSM-media plates solidified with 1.5% w/v agar grown in a gas-tight chamber containing a 1 : 1 (v/v) methane:air gas mixture. Plates were incubated inverted in the chamber at 42°C.

For fermentation, a 3-liter bioreactor containing 1.25L sterilized media MMF1.1 was inoculated with cells from serum bottle batch cultures (10-20%> v/v) grown in the same media supplied with a 1 : 1 (v/v) mixture of methane and air. The composition of medium MMF1.1 was as follows: 0.8 mM MgS0 ₄ * 7H ₂ 0, 40 mM NaN0 ₃ , 0.14 mM CaCl ₂ , 6 mM NaHC0 ₃ , 4.7 mM KH ₂ P0 ₄ , 6.8 mM K ₂ HP0 ₄ , 20.7 μΜ Na2Mo0 ₄ * 2H ₂ 0, 6 μΜ CuS0 ₄ * 5H ₂ 0, 10 μΜ Fe ⁱⁿ -Na-EDTA, and 1 mL per liter of trace metals solution (containing, per liter 500 mg FeS0 ₄ * 7H ₂ 0, 400 mg ZnS0 ₄ * 7H ₂ 0, 20 mg MnCl ₂ * 7H ₂ 0, 50 mg CoCl ₂ * 6H ₂ 0, 10 mg NiCl ₂ * 6H ₂ 0, 15 mg H ₃ B0 ₃ , 250 mg EDTA). Phosphate, bicarbonate, and Fe ⁱⁿ -Na-EDTA were added after media was autoclaved and cooled. The reactor contents were stirred with an overhead impeller at a constant 750 rpm. The culture was fed with a constant methane sparging at about 60 to about 200 mL/min, while concentrated oxygen (>85%) was supplied at a variable rate of 15-90 mL/min and the dissolved oxygen level was maintained below 10% (relative to air saturation of the media). Temperature in the bioreactor was maintained at 44°C and pH was maintained at 7.0 ± 0.1 using automated addition of 0.5M NaOH and 0.5M HCl, along with additions of copper and iron (5μΜ CuS04, 5 μΜ FeS0 ₄ , 10 μΜ Fe ⁱⁿ -Na-EDTA final concentration) to the culture every 3-6 hours (corresponding to an OD ₆ oo increase of approximately 3-5 OD units after reaching OD 5). Under these conditions, essentially linear growth was observed, with effective biomass generation rate of more than 5 grams dry cell weight per liter per day to an OD ₆₀ o of greater than 10. Culture biomass was harvested by centrifugation, the cells washed once in MM-W1 media and cell pellets were either frozen at -80°C or used immediately for fractionation of cellular components.

Nutrient depletion was recognized as an issue that could limit the growth yield during fermentation. To avoid limitation of nutrients, mainly nitrogen and phosphate, nutrient feeds composed of 2-fold concentrated MMF1.1 were initiated after culture OD ₆₀ o exceeded 5. The nutrient feed was initiated at dilution rates corresponding to approximately half of the cultures' growth rate to avoid wash-out and to maintain an increase in OD while expanding the culture volume. The bioreactor fermentation was continued according to the above protocol so that multiple cycles of growth and biomass recovery could be carried out during a single fermentation run.

Methylobacterium extorquens or Methylosinus trichosporium strain OB 3b

(NCIMB 11131)

The bacteria is cultured at 30°C in tubes containing Higgins minimal nitrate salts medium (NSM) supplemented with 0.5% methanol. The tubes are shaken at a rate of 200-250 rpm. Alternatively, the cultures are maintained on NSM-media plates containing 1.5% w/v agar grown in the presence of methanol vapor (via 0.5 mL methanol in the lid of parafilm-sealed plates) or supplemented with 0.5% methanol. Plates are incubated inverted in a humidified chamber under normal atmosphere at 30°C.

For fermentation, a 2-liter bioreactor containing 1L defined media MM-W1 is inoculated with cells from culture tube batch culture (10-20%) v/v). The composition of medium MM-W1 was as described above. The reactor contents are stirred with an overhead impeller at a constant 800 rpm. The culture is fed with an initial bolus of methanol to a final concentration of 0.5% and variable methanol feed, while pure oxygen was supplied at a variable rate of 30-100mL/min to maintain a dissolved oxygen level of 60-90% (relative to air saturation of the media).

Temperature in the bioreactor was maintained at 30°C and pH was maintained at 7.1±0.1 using automated addition of 0.5M NaOH and 1M HC1, along with the metal and nutrient additions as described above. Under these conditions, essentially linear growth is observed, with effective biomass generation rate 2.7 to 3.3 grams dry cell weight per liter per day to an OD ₆ oo of greater than 20. Culture biomass was harvested by centrifugation, the cells washed once in MM-Wl media and cell pellets were either frozen at -80°C or used immediately for fractionation of cellular components.

A semi-continuous fermentation approach can also be applied to maintain biomass productivity and reduce time associated with fermentation shut-down and start-up (i.e., turn-around time or lead time).

Harvesting of the accumulated bacterial biomass was performed at approximately 12-24 hour intervals, as the culture density approached (but before entering) stationary phase. Approximately half of the bioreactor volume was removed by transferring to a separate container via centrifugal pump. An equal volume of fresh or recycled media was then returned to the bioreactor such that the optical density of the reactor was approximately half of its initial value. The bioreactor fermentation was continued according to the above protocol so that multiple cycles of growth and biomass recovery was carried out during a single fermentation run.

Clostridium autoethanogenum and Clostridium liungdahlii

The Clostridium bacteria are cultivated anaerobically in 100 mL modified PETC medium (ATCC medium 1754) at 37°C in plastic-coated 500 ml-Schott Duran® GL45 bottles with butyl rubber stoppers and 200 kPa steel mill waste gas. Growth is monitored by measuring the optical density at 600 nm (OD ₆ oo).

The modified PETC medium contains (per liter) 1 g NH ₄ C1, 0.4 g KC1, 0.2 g MgS0 ₄ * 7 H ₂ 0, 0.8 g NaCl, 0.1 g KH ₂ P0 ₄ , 20 mg CaCl ₂ * 2 H ₂ 0, 10 ml trace elements solution (see below), 10 ml Wolfe's vitamin solution (see below), 2 g NaHC0 ₃ , and 1 mg resazurin. After the pH is adjusted to 5.6, the medium is boiled, dispensed anaerobically, and autoclaved at 121°C for 15 min. Steel mill waste gas (composition: 44% CO, 32% N ₂ , 22%) C0 ₂ , 2%o H ₂ ) or equivalent synthetic mixtures are used as a carbon source. The media has a final pH of 5.9 and is reduced with cysteine-HCl and Na ₂ S at a concentration of 0.008% (w/v).

The trace elements solution contains 2 g nitrilotriacetic acid (adjusted to pH 6 with KOH before addition of the remaining ingredients), 1 g MnS0 ₄ , 0.8 g Fe(S0 ₄ ) ₂ (NH ₄ ) ₂ * 6 H ₂ 0, 0.2 g CoCl ₂ * 6 H ₂ 0, 0.2 mg ZnS0 ₄ * 7 H ₂ 0, 20 mg CuCl ₂ * 2 H ₂ 0, 20 mg NiCl ₂ * 6 H ₂ 0, 20 mg Na ₂ Mo0 ₄ * 2 H ₂ 0, 20 mg Na ₂ Se0 ₄ , and 20 mg Na ₂ W0 ₄ per liter.

Wolfe's vitamin solution (Wo lin etal., J. Biol. Chem. 235:2882, 1963) contains (per liter) 2 mg biotin, 2 mg folic acid, 10 mg pyridoxine hydrochloride, 5 mg thiamine-HCl, 5 mg riboflavin, 5 mg nicotinic acid, 5 mg calcium D-(+)-pantothenate, 0.1 mg vitamin B12, 5 mg p-aminobenzoic acid, and 5 mg thioctic acid. a. Clostridium autoethanogenum Fermentation

Fermentation of Clostridium autoethanogenum is conducted using methods similar to those described in, for example, U.S. Patent Appl. No. 2011/0300593. Briefly, a 2-liter bioreactor containing 1.3 L Solution A (3.083 g NH ₄ Ac; 0.61 g MgCl ₂ * 6H ₂ 0; 0.294 g CaCl ₂ * 2H ₂ 0; 0.15 g KC1; 0.12 g NaCl (optional); up to 1 L with distilled water) is sparged with N ₂ gas. An 85% solution of H ₃ P0 ₄ (2.025 mL, 30 mM) is added and the pH adjusted to 5.3 using concentrated, aqueous NH ₄ OH. Then 13.5 mL Solution B (20.0 mg Biotin; 20.0 mg Folic acid; 10.0 mg pyridoxine HC1; 50.0 mg thiamine * HC1; 50.0 mg Riboflavin; 50.0 mg nicotinic acid; 50.0 mg calcium D-(*)- pantothenate; 50.0 mg vitamin B12; 50.0 mg p-aminobenzoic acid; 50.0 mg thioctic acid; up to 1 L with distilled water) is added and the solution sparged with N ₂ gas. Chromium (II) chloride is added until the oxidation-reduction potential (ORP) of the solution decreases to approximately -200 mV, wherein resazurin (1.35 mL of a 2 g/L solution) is added. Sodium polysulfide (5.4 mL of a 3M solution, see below) is added and the solution sparged with N ₂ and then CO containing gas (1% H ₂ ; 13% N ₂ ; 71% CO; 15% C0 ₂ ). A metal sulfide solution (150 mL, see below) is added and the solution sparged a further 30 minutes, before inoculation with an actively growing C. autoethanogenum culture at a level of approximately 5% (v/v).

The sodium polysulfide solution is prepared in a 500 ml flask that is charged with Na ₂ S (93.7 g, 0.39 mol) and 200 ml H ₂ 0. The solution is stirred until the salt dissolves and sulfur (25 g, 0.1 mol) is added under constant N ₂ flow. After stirring at room temperature for 2 hours, the sodium polysulfide solution (about 4 M with respect to Na and about 5 M with respect to sulfur), now a clear reddish brown liquid, is transferred into N ₂ purged serum bottles, and wrapped in aluminum foil.

The chromium (II) solution is prepared in a 1 L three necked flask that is fitted with a gas tight inlet and outlet to allow working under inert gas and subsequent transfer of the desired product into a suitable storage flask. The flask is charged with CrCl ₃ * 6 H ₂ 0 (40 g, 0.15 mol), zinc granules [20 mesh] (18.3 g, 0.28 mol), mercury (13.55 g, 1 mL, 0.0676 mol) and 500 mL distilled water. Following flushing with N ₂ for one hour, the mixture is warmed to about 80°C to initiate the reaction. Following two hours of stirring under a constant N ₂ flow, the mixture is cooled to room temperature and continuously stirred for another 48 hours by which time the reaction mixture turns into a deep blue solution. The solution is transferred into N ₂ purged serum bottles and stored at 4°C for future use.

The metal sulfide solution is prepared by adding about 950 mL Solution A into a 1 L fermenter and sparging with N ₂ gas. An 85% solution of H ₃ P0 ₄ (1.5 mL, 30 mM) is added and the pH adjusted to 5.3 using concentrated aqueous NH ₄ OH. Solution B (1 OmL) is added and the solution sparged with N ₂ . Chromium (II) chloride is added until the oxidation-reduction potential (ORP) of the solution decreases to approximately -200 mV, wherein resazurin (l mL ofa 2 g/L solution) is added. Solution C (1/10; 10 ml FeCl ₃ ; 5 ml CoCl ₂ ; 5 ml NiCl ₂ ; 1 ml H ₃ B0 ₃ ; 1 ml Na ₂ Mo0 ₄ ; 1 ml MnCl ₂ ; 1 ml Na ₂ W0 ₄ ; 1 ml ZnCl ₂ ; 1 ml Na ₂ Se0 ₃ ; into 1 L media) is added, then sodium polysulfide (2 mL of a 3M solution) is added, and then the solution is sparged with N ₂ gas.

Fermentation of a substrate comprising CO by C. autoethanogenum under batch conditions in the presence of polysulfide results in a substantially increased rate of accumulation and a final biomass accumulation of approximately 4 g/L over a 2-3 day period. For example, following a short lag phase of approximately 1 day, the biomass can increase from about 0.5 g/L up to at least 3.5 g/L over approximately 36 hours of fermentation. Furthermore, acetate is not produced during the growth phase in the presence of polysulfide (as is typically found in batch fermentations) and in certain circumstances some of the acetate is consumed, such that there is a net decrease in the amount of acetate in the fermenter. Culture biomass was harvested by centrifugation, the cells washed once in media and cell pellets were either frozen at -80°C or used immediately for fractionation of cellular components.

A semi-continuous fermentation approach can also be applied to maintain biomass productivity and reduce time associated with fermentation shut-down and start-up (i.e., turn-around time or lead time).

Harvesting of the accumulated bacterial biomass was performed at approximately 12-24 hour intervals, as the culture density approached (but before entering) stationary phase. Approximately half of the bioreactor volume was removed by transferring to a separate container via centrifugal pump. An equal volume of fresh or recycled media was then returned to the bioreactor such that the optical density of the reactor was approximately half of its initial value. The bioreactor fermentation was continued according to the above protocol so that multiple cycles of growth and biomass recovery was carried out during a single fermentation run. b. Clostridium ljungdahlii Fermentation

Fermentation of Clostridium ljungdahlii is performed using similar methods to those described in, for example, U.S. Patent Nos, 5,173,429 and 5,593,886. Briefly, batch fermentations are conducted using a biologically pure culture of C. ljungdahlii. Preparation of the medium ((1) 80.0 mL of a salt comprising KH ₂ PO ₄ 3.00 g/L, K ₂ HPO ₄ 3.00 g/L, (NH ₄ ) ₂ S0 ₄ 6.00 g/L, NaCl 6.00 g/L, MgS0 ₄ *2H ₂ 0 1.25 g/L; (2) 1.0 g of yeast extract; (3) 1.0 g of trypticase; (4) 3.0 ml of PFN (Pfenning) trace metal solution comprising FeCl ₂ * 4H ₂ 0 1500 mg, ZnS0 ₄ * 7H ₂ 0 100 mg, MnCl ₂ * 4H ₂ 0 30 mg, H ₃ BO ₃ 300 mg, CoCl ₂ * 6H ₂ 0 200 mg, CuCl ₂ * H ₂ 0 10 mg, NiCl ₂ * 6H ₂ 0 20 mg, NaMo0 ₄ * 2H ₂ 0 30 mg, Na ₂ Se0 ₃ 10 mg, and distilled water up to 1 L; (5) 10.0 ml of B vitamins comprising Pyridoxal HC1 10 mg, Riboflavin 50 mg, Thiamine HC150 mg, Nictotinic acid 50 mg, Ca-D-Pantotheinate 50 mg, Lipoic acid 60 mg, p-aminobenzoic acid 50 mg, Folic acid 20 mg, Biotin 20 mg, cyanocobalamin 50 mg, and distilled water up to 1 L; (6) 0.5 g of cysteine HC1; (7) 0.06 g CaCl ₂ * 2H ₂ 0; (8) 2.0 g NaHC0 ₃ ; (9) 1.0 mL resazurin (0.01%); and (10) 920.0 mL distilled water) is carried out anaerobically in an atmosphere of 80% nitrogen and 20% C0 ₂ . The pH of the medium is controlled during fermentation and maintained at 5.0 with HC1. If required, adjustments to the pH are made with sterile 10% NaOH or 1.0% acetic acid solution. The medium is transferred to 157.5 mL serum bottles and sealed with butyl rubber stoppers and aluminum seals. The bottles are then autoclaved at 121°C for 20 minutes.

Approximately 48 hours before commencing the experiment, a seed culture is prepared from a stock culture of the C. ljungdahlii in a bottle similar to those as described above. The seed culture is grown in a shaker incubator at 37°C and shaken at 100 rpm. Reducing solutions (2.0 ml Na ₂ S, 2.5% solution and 2.0 ml cysteine-HCl, 3.5% solution) are added to the culture, which is placed in the shaker incubator for approximately 15 minutes to allow for complete oxygen removal and temperature acclimation. Unlike the procedure used for isolating a biologically pure culture of the organism, addition of methane inhibitors is not required in batch fermentations.

Fermentation with C. ljungdahlii is performed in a New Brunswick Scientific Bioflow lie 2.5-liter fermenter containing nutrient media at 37°C, and a constant fluid level of 1.5 liters is maintained while the fluid is agitated at variable rates of up to 1,000 revolutions per minute with gas introduced at a rate of approximately 500 cubic centimeters per minute. Optimal gas retention times are in the range of three minutes. The gas feed is varied with its uptake by the bacteria, which is in turn a function of the cell density.

Harvesting of the accumulated bacterial biomass was performed at approximately 12-24 hour intervals, as the culture density approached (but before entering) stationary phase. Approximately half of the bioreactor volume was removed by transferring to a separate container via centrifugal pump. An equal volume of fresh or recycled media was then returned to the bioreactor such that the optical density of the reactor was approximately half of its initial value. The bioreactor fermentation was continued according to the above protocol so that multiple cycles of growth and biomass recovery was carried out during a single fermentation run.

EXAMPLE 2

STABLE CARBON ISOTOPE DISTRIBUTION IN LIPIDS

FROM Ci METABOLIZING MICROORGANISMS

Dry samples of M. trichosporium biomass and lipid fractions were analyzed for carbon and nitrogen content (% dry weight), and carbon ( ¹³ C) and nitrogen ( ¹⁵ N) stable isotope ratios via elemental analyzer/continuous flow isotope ratio mass spectrometry using a CHNOS Elemental Analyzer (vario ISOTOPE cube, Elementar, Hanau, Germany) coupled with an IsoPrimel 00 IRMS (Isoprime, Cheadle, UK). Samples of methanotrophic biomass cultured in fermenters or serum bottles were centrifuged, resuspended in deionized water and volumes corresponding to 0.2-2 mg carbon (about 0.5-5 mg dry cell weight) were transferred to 5 x 9 mm tin capsules (Costech Analytical Technologies, Inc., Valencia, CA) and dried at 80°C for 24 hours. Similarly, previously extracted lipid fractions were suspended in chloroform and volumes containing 0.1-1.5 mg carbon were transferred to tin capsules and evaporated to dryness at 80°C for 24 hours. Standards containing 0.1 mg carbon provided reliable 5 ¹³ C values.

The isotope ratio is expressed in "delta" notation (%o), wherein the isotopic composition of a material relative to that of a standard on a per million deviation basis is given by 5 ¹³ C (or δ ¹⁵ Ν) = (Rsampie / Rstandard-i) 1 ,000, wherein R is the molecular ratio of heavy to light isotope forms. The standard for carbon is the Vienna Pee Dee Belemnite (V-PDB) and for nitrogen is air. The NIST (National Institute of Standards and Technology) proposed SRM (Standard Reference Material) No. 1547, peach leaves, was used as a calibration standard. All isotope analyses were conducted at the Center for Stable Isotope Biogeochemistry at the University of California, Berkeley. Long-term external precision for C and N isotope analyses is 0.10%o and 0.15%o, respectively.

M. trichosporium strain OB3b was grown on methane in three different fermentation batches, M. capsulatus Bath was grown on methane in two different fermentation batches, and Methylomonas sp. 16a was grown on methane in a single fermentation batch. The biomass from each of these cultures was analyzed for stable carbon isotope distribution (5 ¹³ C values; see Table 3).

Table 3. Stable Carbon Isotope Distribution in Different Methanotrophs

Methanotroph Batch No. EFT (h)† OD ₆ „o DCW* 5 ¹³ C Cells

20.3 3.62 1.52 -65.5

27 5.50 2.31 -66.2

40.5 9.80 4.12 -66.3

* DCW, Dry Cell Weight is reported in g/L calculated from the measured optical densities (OD ₆ oo) using specific correlation factors relating OD of 1.0 to 0.558 g/L for Mt OB3b, OD of 1.0 to 0.355 g/L for Mc Bath, and OD of 1.0 to 0.42 g/L for Mms 16a. For Mt OB3b, the initial concentration of bicarbonate used per fermentation was 1.2 mM or 0.01 % (Batch No. 68C) and 0.1 % or 12 mM (Batch

Nos. 68A and 68B).

† EFT = effective fermentation time in hours

In addition, stable carbon isotope analysis was performed for biomass and corresponding lipid fractions (see Table 4) from strains Methylosinus trichosporium OB3b (Mt OB3b), Methylococcus capsulatus Bath (Mc Bath), and Methylomonas sp. 16a (Mms 16a) grown on methane in bioreactors as described in Example 1.

Table 4. Stable Carbon Isotope Distribution in Cells and Lipids

Biomass from strains Mt OB3b, Mc Bath and Mms 16a were harvested at 94 h (3.14 g DCW/L), 26 h (2.2 g DCW/L) and 39 h (1.14 g DCW/L), respectively. The 5 ¹³ C values for lipids in Table 4 represent an average of duplicate determinations.

EXAMPLE 3

EFFECT OF METHANE SOURCE AND PURITY ON STABLE CARBON ISOTOPE DISTRIBUTION IN LIPIDS To examine methanotroph growth on methane containing natural gas components, a series of 0.5-liter serum bottles containing 100 mL defined media MMS 1.0 were inoculated with Methylosinus trichosporium OB3b or Methylococcus capsulatus Bath from a serum bottle batch culture (5% v/v) grown in the same media supplied with a 1 : 1 (v/v) mixture of methane and air. The composition of medium MMS 1.0 was as follows: 0.8 mM MgS0 ₄ * 7H ₂ 0, 30 mM NaN0 ₃ , 0.14 mM CaCl ₂ , 1.2 mM NaHC0 ₃ , 2.35 mM KH ₂ P0 ₄ , 3.4 mM K ₂ HP0 ₄ , 20.7 μΜ Na ₂ Mo0 ₄ * 2H ₂ 0, 6 μΜ CuS0 ₄ * 5H ₂ 0, 10 μΜ Fe ⁱⁿ -Na-EDTA, and 1 mL per liter of a trace metals solution (containing, per L : 500 mg FeS04 * 7H ₂ 0, 400 mg ZnS0 ₄ * 7H ₂ 0, 20 mg MnCl ₂ * 7H20, 50 mg CoCl ₂ * 6H ₂ 0, 10 mg NiCl ₂ * 6H ₂ 0, 15 mg H ₃ B0 ₃ , 250 mg EDTA). Phosphate, bicarbonate, and Fe ⁱⁿ -Na-EDTA were added after media was autoclaved and cooled. The final pH of the media was 7.0±0.1.

The inoculated bottles were sealed with rubber sleeve stoppers and injected with 60 mL methane gas added via syringe through sterile 0.45 μιη filter and sterile 27G needles. Duplicate cultures were each injected with 60 mL volumes of (A) methane of 99% purity (grade 2.0, Praxair through Alliance Gas, San Carlos, CA), (B) methane of 70% purity representing a natural gas standard (Sigma- Aldrich; also containing 9% ethane, 6% propane, 3% methylpropane, 3% butane, and other minor hydrocarbon components), (C) methane of 85% purity delivered as a 1 : 1 mixture of methane sources A and B; and (D) >93%> methane (grade 1.3, Specialty Chemical Products, South Houston, TX; in-house analysis showed composition >99%> methane). The cultures were incubated at 30°C (M. trichosporium strain OB3b) or 42°C (M. capsulatus Bath) with rotary shaking at 250 rpm and growth was measured at approximately 12 hour intervals by withdrawing 1 mL samples to determine OD ₆ oo- At these times, the bottles were vented and headspace replaced with 60 mL of the respective methane source (A, B, C, or D) and 60 mL of concentrated oxygen (at least 85% purity). At about 24 hour intervals, 5 mL samples were removed, cells recovered by centrifugation (8,000 rpm, 10 minutes), and then stored at -80°C before analysis.

Analysis of carbon and nitrogen content (% dry weight), and carbon ( ¹³ C) and nitrogen ( ¹⁵ N) stable isotope ratios, for methanotrophic biomass derived from M. trichosporium strain OB3b and M. capsulatus Bath were carried out. Table 5 shows the results of stable carbon isotope analysis for biomass samples from M. capsulatus Bath grown on methane having different levels of purity and in various batches of bottle cultures. Table 5. Stable Carbon Isotope Distribution of M. capsulatus Bath Grown on

Different Methane Sources having Different Purity

* Methane purity: A: 99% methane, grade 2.0 (min. 99%); B: 70%

methane, natural gas standard (contains 9% ethane, 6% propane, 3%

methylpropane, 3% butane); C: 85% methane (1 : 1 mix of A and B

methane)

† Time = bottle culture time in hours

The average 5 ¹³ C for M. capsulatus Bath grown on one source of methane (A, 99%) was -41.2 ± 1.2, while the average 5 ¹³ C for M. capsulatus Bath grown on a different source of methane (B, 70%) was -44.2 ± 1.2. When methane sources A and B were mixed, an intermediate average 5 ¹³ C of -43.8 ± 2.4 was observed. These data show that the 5 ¹³ C of cell material grown on methane sources A and B are significantly different from each other due to the differences in the 5 ¹³ C of the input methane. But, cells grown on a mixture of the two gasses preferentially utilize C and, therefore, show a trend to more negative δ C values.

A similar experiment was performed to examine whether two different methanotrophs, Methylococcus capsulatus Bath and Methylosinus trichosporium OB3b, grown on different methane sources and in various batches of bottle cultures showed a difference in 5 ¹³ C distribution (see Table 6).

Table 6. Stable Carbon Isotope Distribution of Different Methanotrophs Grown on Different Methane Sources of Different Purity

* Methane sources and purity: A: 99% methane (grade 2.0); D: >93% methane (grade 1.3) † Time = bottle culture time in hours The average δ C for M. capsulatus grown on a first methane source (A) was -44.5 ± 8.8, while the average 5 ¹³ C for M. trichosporium was -47.8 ± 2.0 grown on the same methane source. The average 5 ¹³ C for M. capsulatus grown on the second methane source (B) was -37.9 ± 0.4, while the average 5 ¹³ C forM trichosporium was -39.8 ± 4.5. These data show that the 5 ¹³ C of cell material grown on a methane source is highly similar to the 5 ¹³ C of cell material from a different strain grown on the same source of methane. Thus, the observed 5 ¹³ C of cell material appears to be primarily dependent on the composition of the input gas rather than a property of a particular bacterial strain being studied.

The various embodiments described above can be combined to provide further embodiments. All of the patent and non-patent publications referred to in this specification or listed in the Application Data Sheet, including the disclosure of U.S. provisional application number 61/928,366, filed January 16, 2014, are incorporated herein by reference in their entirety. Aspects of the embodiments can be modified, if necessary to employ concepts of the various patents, applications and publications to provide further embodiments.

These and other changes can be made to the embodiments in light of the above- detailed description. In general, in the following embodiments, the terms used should not be construed to limit the embodiments to the specific embodiments disclosed in the specification and the embodiments, but should be construed to include all possible embodiments along with the full scope of equivalents to which such embodiments are entitled. Accordingly, the embodiments are not limited by the disclosure.