The present invention relates to a method for producing a monoalkene comprising the step of enzymatically converting an alkyl monoester. The conversion preferably makes use of an enzyme which belongs to the family of terpene synthases or to the family of prenyltransferases. Moreover, the present invention relates to the use of a terpene synthase or a prenyltransferase for enzymatically converting an alkyl monoester into a monoalkene.

A large number of chemical compounds are currently derived from petrochemicals. Alkenes (such as ethylene, propylene, the different butenes, or else the pentenes, for example) are used in the plastics industry, for example for producing polypropylene or polyethylene, and in other areas of the chemical industry and that of fuels. Ethylene, the simplest alkene, lies at the heart of industrial organic chemistry: it is the most widely produced organic compound in the world. It is used in particular to produce polyethylene, a major plastic. Ethylene can also be converted to many industrially useful products by reaction (e.g. by oxidation or halogenation). Propylene plays a similarly important role: its polymerization results in a plastic material, polypropylene. The technical properties of this product in terms of resistance, density, solidity, deformability, and transparency are unequalled. The worldwide market for polypropylene has grown continuously since its invention in 1954. Butylene exists in four forms, one of which, isobutylene, enters into the composition of methyl-tert-butyl-ether (MTBE), an anti-knock additive for automobile fuel. Isobutylene can also be used to produce isooctene, which in turn can be reduced to isooctane (2,2,4-trimethylpentane); the very high octane rating of isooctane makes it the best fuel for so-called "gasoline" engines. Amylene, hexene and heptene exist in many forms according to the position and configuration of the double bond. These products have real industrial applications but are less important than ethylene, propylene or butenes. All these alkenes are currently produced by catalytic cracking of petroleum products (or by a derivative of the Fischer-Tropsch process in the case of hexene, from coal or gas). Their production costs are therefore tightly linked to the price of oil. Moreover, catalytic cracking is sometimes associated with considerable technical difficulties which increase process complexity and production costs.

The production by a biological pathway of alkenes or other organic molecules that can be used as fuels or as precursors of synthetic resins is called for in the context of a sustainable industrial operation in harmony with geochemical cycles. The first generation of biofuels consisted in the fermentative production of ethanol, as fermentation and distillation processes already existed in the food processing industry. The production of second generation biofuels is in an exploratory phase, encompassing in particular the production of long chain alcohols (butanol and pentanol), terpenes, linear alkanes and fatty acids. Two recent reviews provide a general overview of research in this field: Ladygina et al. (Process Biochemistry 41 (2006), 1001 ) and Wackett (Current Opinions in Chemical Biology 21 (2008), 187).

The production of ethylene by plants has long been known (Meigh et al. (Nature 186 (1960), 902)). According to the metabolic pathway elucidated, methionine is the precursor of ethylene (Adams and Yang (PNAS 76 (1979), 170)). Conversion of 2- oxoglutarate has also been described (Ladygina et al. (Process Biochemistry 41 (2006), 1001 ). Since a single ethylene molecule requires the previous production of a four- or five-carbon chain, the equipment and energy needs of all these pathways are unfavorable and do not bode well for their industrial application for alkene bioproduction.

Moreover, many microorganisms are capable of producing propylene, however, with an extremely low yield

The conversion of isovalerate to isobutylene by the yeast Rhodotorula minuta has been described (Fujii et al. (Appl. Environ. Microbiol. 54 (1988), 583)), but the efficiency of this reaction, less than 1 millionth per minute, or about 1 for 1000 per day, is far from permitting an industrial application. The reaction mechanism was elucidated by Fukuda et al. (BBRC 201 (1994), 516) and involves a cytochrome P450 enzyme which decarboxylates isovalerate by reduction of an oxoferryl group Fe ^v =0. Large-scale biosynthesis of isobutylene by this pathway seems highly unfavorable, since it would require the synthesis and degradation of one molecule of leucine to form one molecule of isobutylene. Also, the enzyme catalyzing the reaction uses heme as cofactor, poorly lending itself to recombinant expression in bacteria and to improvement of enzyme parameters. For all these reasons, it appears very unlikely that this pathway can serve as a basis for industrial exploitation. Other microorganisms have been described as being marginally capable of naturally producing isobutylene from isovalerate; the yields obtained are even lower than those obtained with Rhodotorula minuta (Fukuda et al. (Agric. Biol. Chem. 48 (1984), 1679)).

Isoprene is produced at a significant level in higher plants, such as poplars. The production of isoprene in this context remains however low and the pathway which leads to isoprene production, which is based on the mevalonate-isopentenyl- pyrophosphate pathway, poorly complies with the demands for industrial scale production.

Thus, there is still a need for efficient and environmentally friendly methods of producing alkenes, in particular monoalkenes.

The present invention meets this demand by providing a method for producing a monoalkene from an alkyl monoester by employing an enzymatic reaction. More specifically, the present invention relates to a method for producing a monoalkene, the method comprising a step of converting an alkyl monoester into a monoalkene, wherein: the alkyl monoester is a compound of formula (I)

(I) wherein R ¹ , R ² , R ³ and R ⁴ are each independently selected from hydrogen (-H), methyl (-CH3) or ethyl (-C2H5); and wherein X is selected from:

O— PO ₃ H ₂ monophosphate 0-P0 ₂ H— O— P0 ₃ H ₂ diphosphate

O— S0 ₃ H sulfate and wherein

the monoalkene is a compound of formula (II)

(ll)

wherein R ¹ , R ² , R ³ and R ⁴ have the same meanings as defined for the compound of formula (I),

the method being characterized in that the conversion from the alkyl monoester into the monoalkene is achieved by enzymatic elimination of molecule XH.

The present invention teaches for the first time that it is possible to enzymatically convert an alkyl monoester having formula (I) as shown above into a corresponding monoalkene by eliminating the phosphorus or sulphur containing molecule XH with the help of an enzyme.

In particular, it has been found that enzymes which belong to the family of terpene synthases or to the family of prenyl transferases are capable of catalyzing the conversion of an alkyl monoester into a monoalkene as described above.

The conversion of an alkyl monoester according to formula (I) into a monoalkene according to formula (II) by elimination of molecule XH can in principle be achieved by any enzyme which is capable of eliminating the phosphorus or sulphur containing molecule XH from an alkyl monoester of the formula (I). Preferably, such an enzyme is an enzyme which can be classified as belonging to the terpene synthase family, more preferably the terpene synthase is a plant terpene synthase. In another preferred embodiment such an enzyme is an enzyme which can be classified as belonging to the prenyltransferase family.

The terpene synthases constitute an enzyme family which comprises enzymes catalyzing the formation of numerous natural products always composed of carbon and hydrogen (terpenes) and sometimes also of oxygen or other elements (terpenoids). Terpenoids are structurally diverse and widely distributed molecules corresponding to well over 30000 defined natural compounds that have been identified from all kingdoms of life. In plants, the members of the terpene synthase family are responsible for the synthesis of the various terpene molecules from two isomeric 5-carbon precursor "building blocks", isoprenyl diphosphate and prenyl diphosphate, leading to 5-carbon isoprene, 10-carbon monoterpene, 15-carbon sesquiterpene and 20-carbon diterpenes" (Chen et al.; The Plant Journal 66 (2011 ), 212-229).

The ability of terpene synthases to convert a prenyl diphosphate containing substrate to diverse products during different reaction cycles is one of the most unique traits of this enzyme class. The common key step for the biosynthesis of all terpenes is the reaction of terpene synthase on corresponding diphosphate esters. The general mechanism of this enzyme class induces the removal of the diphosphate group and the generation of an intermediate with carbocation as the first step. In the various terpene synthases, such intermediates further rearrange to generate the high number of terpene skeletons observed in nature. In particular, the resulting cationic intermediate undergoes a series of cyclizations, hydride shifts or other rearrangements until the reaction is terminated by proton loss or the addition of a nucleophile, in particular water for forming terpenoid alcohols (Degenhardt et al., Phytochemistry 70 (2009), 1621-1637).

The different terpene synthases share various structural features. These include a highly conserved C-terminal domain, which contains their catalytic site and an aspartate-rich DDXXD motif essential for the divalent metal ion (typically Mg2+ or Mn2+) assisted substrate binding in these enzymes (Green et al. Journal of biological chemistry, 284, 13, 8661-8669). In principle, any known enzyme which can be classified as belonging to the EC 4.2.3 enzyme superfamily can be employed. Even more preferably the method according to the invention makes use of an isoprene synthase (EC 4.2.3.27), a myrcene/ocimene synthase (EC 4.2.3.15), a farnesene synthase (EC 4.2.3.46 or EC 4.2.3.47) or a pinene synthase (EC 4.2.3.14). Also enzymes which are generally classified as monoterpene synthases can be used.

Isoprene synthase (EC 4.2.3.27) is an enzyme which naturally catalyzes the following reaction:

Dimethylallyl diphosphate -=-> isoprene + diphosphate

This enzyme occurs in a number of organisms, in particular in plants and some bacteria. The occurrence of this enzyme has, e.g., been described for Arabidopsis thaliana, a number of Populus species like P. alba (UniProt accession numbers Q50L36, A9Q7C9, D8UY75 and D8UY76), P. nigra (UniProt accession number A0PFK2), P. canescence (UniProt accession number Q9AR86; see also Koksal et al., J. Mol. Biol. 402 (2010), 363-373), P. tremuloides, P. trichocarpa, in Quercus petraea, Quercus robur, Salix discolour, Pueraria montana (UniProt accession number Q6EJ97), Pueraria lobata, Mucuna pruriens, Vitis vinifera, Embryophyta and Bacillus subtilis. In principle, any known isoprene synthase can be employed in the method according to the invention. In a preferred embodiment, the isoprene synthase employed in a method according to the present invention is an isoprene synthase from a plant of the genus Populus, more preferably from Populus trichocarpa or Populus alba. In another preferred embodiment the isoprene synthase employed in a method according to the present invention is an isoprene synthase from Pueraria montana, preferably from Pueraria Montana var. lobata, or from Vitis vinifera. Preferred isoprene synthases to be used in the context of the present invention are the isoprene synthase of Populus alba (Sasaki et al.; FEBS Letters 579 (2005), 2514- 2518) or the isoprene synthases from Populus trichocarpa and Populus tremuloides which show very high sequence homology to the isoprene synthase from Populus alba. Another preferred isoprene synthase is the isoprene synthase from Pueraria montana var. lobata (kudzu) (Sharkey et al.; Plant Physiol. 137 (2005), 700-712). The activity of an isoprene synthase can be measured according to methods known in the art, e.g. as described in Silver and Fall (Plant Physiol ( 991 ) 97, 1588-1591 ). In a typical assay, the enzyme is incubated with dimethylallyl diphosphate in the presence of the required co-factors, Mg ²⁺ or Mn ²⁺ and K ⁺ in sealed vials. At appropriate time volatiles compound in the headspace are collected with a gas-tight syringe and analyzed for isoprene production by gas chromatography (GC).

Myrcene/ocimene synthases (EC 4.2.3.15) are enzymes which naturally catalyze the following reaction:

Geranyl diphosphate t= (E)-beta-ocimene + diphosphate

or

Geranyl diphosphate i=-> myrcene + diphosphate

These enzymes occur in a number of organisms, in particular in plants and animals, for example in Lotus japanicus, Phaseolus lunatus, Abies grandis, Arabidopsis thaliana (UniProt accession number Q9ZUH4), Actinidia chinensis, Perilla fructescens, Ochtodes secundiramea and in Ips pini (UniProt accession number Q58GE8. In principle, any known myrcene/ocimene synthase can be employed in the method according to the invention. In a preferred embodiment, the myrcene/ocimene synthase employed in a method according to the present invention is a myrcene/ocimene synthase from Lotus japanicus (Arimura et al.; Plant Physiol. 135 (2004), 1976-1983) or from Phaseolus lunatus (UniProt accession number B1 P189). The activity of an ocimene/myrcene synthase can be measured as described, for example, in Arimura et al. (Plant Physiology 135 (2004), 1976-1983. In a typical assay for determining the activity, the enzyme is placed in screwcapped glass test tube containing divalent metal ions, e.g. Mg ²⁺ and/or Mn ²⁺ , and substrate, i.e. geranyl diphosphate. The aqueous layer is overlaid with pentane to trap volatile compounds. After incubation, the assay mixture is extracted with pentane a second time, both pentane fractions are pooled, concentrated and analyzed by gas chromatography to quantify ocimene/myrcene production.

Farnesene synthases are generally classified into two different groups, i.e. alpha- farnesene synthases (EC 4.2.3.46) and beta farnesene synthases (EC 4.2.3.47). Alpha-farnesene synthases (EC 4.2.3.46) naturally catalyze the following reaction: (2E, 6E)-farnesyl diphosphate => (3E, 6E)-alpha-farnesene + diphosphate

This enzyme occurs in a number of organisms, in particular in plants, for example in Malus x domestica (UniProt accession numbers Q84LB2, B2ZZ11 , Q6Q2J2, Q6QWJ1 and Q32WI2), Populus trichocarpa, Arabidopsis thaliana (UniProt accession numbers A4FVP2 and P0CJ43), Cucumis melo (UniProt accession number B2KSJ5) and Actinidia deliciosa (UniProt accession number C7SHN9). In principle, any known alpha-farnesene synthase can be employed in the method according to the invention. In a preferred embodiment, the alpha-farnesene synthase employed in a method according to the present invention is an alpha-farnesene synthase from Malus x domestica (UniProt accession numbers Q84LB2, B2ZZ11 , Q6Q2J2, Q6QWJ1 and Q32WI2; see also Green et al.; Photochemistry 68 (2007), 176-188).

Beta-fa rnesene synthases (EC 4.2.3.47) naturally catalyze the following reaction:

(2E, 6E)-farnesyl diphosphate _ _ (E)-beta-farnesene + diphosphate

This enzyme occurs in a number of organisms, in particular in plants and in bacteria, for example in Artemisia annua (UniProt accession number Q4VM12), Citrus junos (UniProt accession number Q94JS8), Oryza sativa (UniProt accession number Q0J7R9), Pinus sylvestris (UniProt accession number D7PCH9), Zea diploperennis (UniProt accession number C7E5V9), Zea mays (UniProt accession numbers Q2NM15, C7E5V8 and C7E5V7), Zea perennis (UniProt accession number C7E5W0) and Streptococcus coelicolor (Zhao et al., J. Biol. Chem. 284 (2009), 36711-36719). In principle, any known beta-farnesene synthase can be employed in the method according to the invention. In a preferred embodiment, the beta- farnesene synthase employed in a method according to the present invention is a beta-farnesene synthase from Mentha piperita (Crock et al.; Proc. Natl. Acad. Sci. USA 94 (1997), 12833-12838).

Methods for the determination of farnesene synthase activity are known in the art and are described, for example, in Green et al. (Phytochemistry 68 (2007), 176-188). In a typical assay farnesene synthase is added to an assay buffer containing 50 mM BisTrisPropane (BTP) (pH 7.5), 10% (v/v) glycerol, 5 mM DTT. Tritiated farnesyl diphosphate and metal ions are added. Assays containing the protein are overlaid with 0.5 ml pentane and incubated for 1 h at 30 °C with gentle shaking. Following addition of 20 mM EDTA (final concentration) to stop enzymatic activity an aliquot of the pentane is removed for scintillation analysis. The olefin products are also analyzed by GC-MS.

Pinene synthase (EC 4.2.3.14) is an enzyme which naturally catalyzes the following reaction:

Geranyl diphosphate c=i alpha-pinene + diphosphate

This enzyme occurs in a number of organisms, in particular in plants, for example in Abies grandis (UniProt accession number 0244475), Artemisia annua, Chamaecyparis formosensis (UniProt accession number C3RSF5), Salvia officinalis and Picea sitchensis (UniProt accession number Q6XDB5).

For the enzyme from Abies grandis a particular reaction was also observed (Schwab et al., Arch. Biochem. Biophys. 392 (2001 ), 123-136), namely the following:

6,7-dihydrogeranyl diphosphate 6,7-dihydromyrcene + diphosphate

In principle, any known pinene synthase can be employed in the method according to the invention. In a preferred embodiment, the pinene synthase employed in a method according to the present invention is a pinene synthase from Abies grandis (UniProt accession number 0244475; Schwab et al., Arch. Biochem. Biophys. 392 (2001 ), 123-136).

Methods for the determination of pinene synthase activity are known in the art and are described, for example, in Schwab et al. (Archives of Biochemistry and Biophysics 392 (2001 ), 123-136). In a typical assay, the assay mixture for pinene synthase consists of 2 ml assay buffer (50 mM Tris/HCI, pH 7.5, 500 mM KCI, 1 mM MnCI2, 5 mM dithiothreitol, 0.05% NaHSO3, and 10% glycerol) containing 1 mg of the purified protein. The reaction is initiated in a Teflon-sealed screw-capped vial by the addition of 300 mM substrate. Following incubation at 25°C for variable periods (0.5-24 h), the mixture is extracted with 1 ml of diethyl ether. The biphasic mixture is vigorously mixed and then centrifuged to separate the phases. The organic extract is dried (MgS04) and subjected to GC-MS and MDGC analysis.

As indicated above, it is also possible to employ other monoterpene synthases in a method according to the invention, for example the monoterpene synthase from Melaleuca alternifolia described in Shelton et al. (Plant Physiol. Biochem. 42 (2004), 875-882) or the monoterpene synthase from Eucalyptus globulus (UniProt accession number Q0PCI4).

The present inventors have shown that different types of terpene synthases, e.g. isoprene synthases, (E,E)-alpha-farnesene synthases and beta-ocimene synthases from different plant organisms are able to convert propan-2-yl into propylene (see Example 2).

The reactions catalyzed by the various terpene synthases, in particular the terpene synthases mentioned above, show certain common features. For example, the reactions catalyzed by isoprene synthases, by myrcene/ocimene synthases, by farnesene synthases, by pinene synthase and by other monoterpene synthases, respectively, are all believed to proceed through a common mechanism in which, in a first step a carbocation is created by elimination of the diphosphate (PP,), which is then followed by direct deprotonation so as to form the corresponding diene.

It could be shown by the present inventors that enzymes which belong to the family of terpene synthases are able to carry out the corresponding reaction by using an alkyl monoester as specified in formula (I), above, so as to form a monoalkene. The natural reaction catalyzed by the terpene synthases is depicted in a schematic form in Figure 1 as well as the reaction when it is applied to an alkyl monoester as defined in formula (I), above.

As mentioned above, in another preferred embodiment the enzyme employed in a method according to the present invention is an enzyme which can be classified as belonging to the prenyltransferase family. Prenyltransferases are a class of enzymes that transfer allylic prenyl groups to acceptor molecules. Prenyltransferases can be classified as EC 2.5.1. The prenyltransferases and terpene synthases are mechanistically linked by a common early step in their catalyzed reactions. The reaction catalyzed by prenyltransferases starts with the elimination of the diphosphate ion from an allylic diphosphate to form an allylic cation. Namely, both groups of enzymes employ a divalent metal ion (coordinated by a conserved DDXXD/E motif) to facilitate cleavage of the pyrophosphate bond of an allylic diphosphate substrate (Christianson DW Chem Rev. 106 (2006), 3412-3442). In the Gene Ontology database these enzymes are identified under the identification number GO:0004659. Prenyltransferases are commonly divided into two classes, i.e. cis (or Z) and trans (or E) depending upon the stereochemistry of the resulting products. In the scope of the present invention both classes can be employed. The term "prenyltransferase" as used herein comprises in particular the following three main classes of prenyltransferases:

- Isoprenyl pyrophosphate synthases, which catalyze the chain elongation of allylic pyrophosphate substrates via consecutive condensation reactions with isopentenyl pyrophosphate to generate linear polymers with defined chain lengths;

- Protein prenyltransferases, which catalyze the transfer of an isoprenyl pyrophosphate to a protein or peptide; and

- Prenyltransferases which catalyze the cyclization of isoprenyl pyrophosphate (see Liang et al., Eur. J. Biochem. 269 (2002), 3339-3354, for a review). Prenyltransferases have been studied in detail as regards their structure and function and crystal data as well as information on the reaction mechanism are available for a variety of prenyltransferases (see e.g. Chang et al., J. Biol. Chem. 278 (2003), 29298-29397; Chang et al., Protein Science 13 (2004), 971-977).

In principle, any prenyltransferase can be employed in the method according to the present invention, in particular any prenyltransferase of the three classes mentioned above.

In a preferred embodiment the prenyltransferase employed in a method according to the present invention is a dimethylallyltranstransferase (EC 2.5.1.1 ), a (2E,6E)- farnesyl diphosphate synthase (EC 2.5.1.10), a geranylgeranyl diphosphate synthase (EC 2.5.1.29), a ditrans.polycis-undecaprenyl-diphosphate synthase [(2E.6E)- farnesyl-diphosphate specific (EC 2.5.1.31 ) or a squalen synthase (EC 2.5.1.21). Dimethylallyltranstransferase catalyzes the reaction:

Dimethylallyl diphosphate + isopentenyl diphosphate .=-> diphosphate + geranyl diphosphate

In principle any dimethylallyltranstransferase can be employed in the method according to the invention. This enzyme is known from a number of organisms, including animals, plants, fungi and bacteria and has been described, e.g., in Sacharomyces cerevisiae, Rhizobium loti, Acyrthosiphon pisum, Geobacillus stearothermophilus, Ips pini, Mentha x piperita, Myzus persicae, Picea abies, Gallus gallus, Homo sapiens and Sus scrofa.

(2E,6E)-farnesyl diphosphate synthase catalyzes the reaction:

Geranyl diphosphate + isopentenyl diphosphate i= diphosphate + (2E,6E)- farnesyl diphosphate

In principle any 2E,6E)-farnesyl diphosphate synthase can be employed in the method according to the invention. This enzyme is known from a number of organisms, including animals, plants, fungi and bacteria and has been described, e.g., in Streptomyces argenteolus, Mycobacterium tuberculosis, E. coli, Geobacillus stearothermophilus, Abies grandis, Acyrthosiphon grandis, Anthonomus grandis, Artemisia tridentate, Bacillus subtilis, Myzus persica, Ricinus communis, Panax ginseng, Plasmodium vivax, S. cerevisiae, Toxoplasma gondii, Trypanosoma cruzi, Rattus norvegicus, Gallus gallus, Homo sapiens and Sus scrofa.

Geranylgeranyl diphosphate synthase catalyzes the reaction:

(2E,6E)-farnesyl diphosphate+ isopentenyl diphosphate t=_> diphosphate + geranylgeranyl diphosphate

In principle any geranylgeranyl diphosphate synthase can be employed in the method according to the invention. This enzyme is known from a multitude of organisms, including animals, plants, fungi and bacteria and has been described, e.g., in Methanothermobacter thermautotrophicus, S. cerevisiae, Schizosaccharomyces pombe, Sulfolobus acidocaldarius, Thermus tthermopilus, Toxoplasma gondii, Thermococcus kodakarensis, Ginko biloba, Taxus x media, Cistus creticus, Sinapis alba, Zea mays, Solanum lycopersicum, Rattus norvegicus, Homo sapiens and Mus musculus to name just some.

Ditrans,polycis-undecaprenyl-diphosphate synthase [(2E,6E)-farnesyl-diphosphate specific] catalyzes the reaction:

(2E,6E)-farnesyl-diphosphate + 8 isopentenyl diphosphate i=-> 8 diphosphate + ditrans, octacis-undecapemyl diphosphate

In principle any ditrans.polycis-undecaprenyl-diphosphate synthase [(2E,6E)- farnesyl-diphosphate specific] can be employed in the method according to the invention. This enzyme is known from several organisms, including fungi and bacteria and has been described, e.g., in Micrococcus luteus, E. coli, Haemophilus influenza, Streptococcus pneumonia, Bacillus subtilis, Helicobacter pyloris, Lactobacillus plantarum, Salmonella Newington and S. cerevisiae.

Squalen synthase catalyzes the reaction:

2 farnesyl diphosphate t=> diphosphate + presqualen diphosphate

In principle any squalen synthase can be employed in the method according to the invention. This enzyme is known from a multitude of organisms, including animals, plants, fungi and bacteria and has been described, e.g., in Trypanosoma cruzi, S. cerevisiae, Arabidopsis thaliana, Euphorbia tirucalli, Panax ginseng, Cavia porcellus, Macaca mulatta, Mus musculus, Rattus norvegicus, Oryctolagus cuniculus, Cricetus cricetus and Homo sapiens to name just some.

The alkyl monoester which is used as a starting material in a method according to the present invention is a compound of formula (I)

(I)

wherein R ¹ , R ² , R ³ and R ⁴ are each independently selected from hydrogen, methyl or ethyl; and wherein X is selected from:

O— PO ₃ H ₂ monophosphate 0-P0 ₂ H— O— P0 ₃ H ₂ diphosphate

O— SO3H sulfate

It is particularly preferred that the alkyl monoester of formula (I)) is selected from: ethyl diphosphate, propan-1-yl diphosphate (propyl diphosphate), propan-2-yl diphosphate (isopropyl diphosphate), butan-1-yl diphosphate (1 -butyl diphosphate), butan-2-yl diphosphate (2-butyl diphosphate), 2-methylpropan-1-yl diphosphate (isobutyl diphosphate), 1 ,1-dimethylethyl diphosphate (ferf-butyl diphosphate), ethyl monophosphate, propan-1-yl monophosphate (propyl monophosphate), propan-2-yl monophosphate (isopropyl monophosphate), butan-1-yl monophosphate (1 -butyl monophosphate), (2-butyl monophosphate), (isobutyl monophosphate), (terf-butyl monophosphate), ethyl sulfate, propan-1-yl sulfate (propyl sulfate), propan-2-yl sulfate (isopropyl sulfate), butan-1-yl sulfate (1 -butyl sulfate), butan-2-yl sulfate (2- butyl sulfate), 2-methylpropan-1-yl sulfate (isobutyl sulfate) and 1 ,1-dimethylethyl sulfate (ferf-butyl sulfate).

The following Table 1 gives an overview over alkyl monoesters preferably to be employed in the method according to the invention and the resulting alkenes:

Table 1

(i.e. ethylene)

propan-1-yl diphosphate (propyl propene (i.e. propylene; diphosphate) methylethylene)

propan-2-yl diphosphate propene (i.e. propylene; (isopropyl diphosphate) methylethylene)

butan-1-yl diphosphate (1 -butyl but-1-ene

diphosphate) (i.e. a-butylene)

butan-2-yl diphosphate (2-butyl but-1-ene (i.e. a-butylene) and diphosphate) but-2-ene (i.e. β-butylene)

2-methylpropan-1 -yl 2-methylprop-1-ene

diphosphate (isobutyl (isobutene);

diphosphate)

1 , 1 -dimethylethyl diphosphate 2-methylprop-1-ene (i.e. (feri-butyl diphosphate) isobutene; isobutylene) ethyl monophosphate ethene

(i.e. ethylene)

propan-1-yl monophosphate propene (i.e. propylene; (propyl monophosphate) methylethylene)

propan-2-yl monophosphate propene (i.e. propylene; (isopropyl monophosphate) methylethylene)

butan-1-yl monophosphate (1- but-1-ene (i.e. a-butylene) butyl monophosphate)

butan-2-yl monophosphate (2- but-1-ene (i.e. a-butylene) and butyl monophosphate) but-2-ene (i.e. β-butylene)

2-methylpropan-1 -yl 2-methylprop-1-ene (i.e. monophosphate (isobutyl isobutene; isobutylene) monophosphate)

1 ,1-dimethylethyl 2-methylprop-1-ene (isobutene) monophosphate (feri-butyl

monophosphate)

ethyl sulfate ethene

(i.e. ethylene)

propan-1-yl sulfate (propyl propene (i.e. propylene; sulfate) methylethylene)

propan-2-yl sulfate (isopropyl propene (i.e. propylene; sulfate) methylethylene)

butan-1-yl sulfate ( -butyl but-1-ene (i.e. a-butylene) sulfate)

butan-2-yl sulfate (2-butyl but-2-ene (i.e. β-butylene) sulfate)

2-methylpropan-1-yl sulfate 2-methylprop-1-ene (i.e. (isobutyl sulfate) isobutene; isobutylene)

21 1 ,1-dimethylethyl sulfate (tert- 2-methylprop-l-ene (i.e.

butyl sulfate) isobutene; isobutylene)

In one preferred embodiment the alkyl monoester according to formula (I) is an alkyl monoester in which group X is diphosphate and R ¹ , R ² , R ³ and R ⁴ are each independently selected from hydrogen, methyl or ethyl. In a particularly preferred embodiment the alkyl monoester is selected from the group consisting of ethyl diphosphate, propan-1-yl diphosphate (propyl diphosphate), propan-2-yl diphosphate (isopropyl diphosphate), butan-1 -yl diphosphate (1 -butyl diphosphate), butan-2-yl diphosphate (2-butyl diphosphate), 2-methylpropan-1-yl diphosphate (isobutyl diphosphate) and 1 ,1-dimethylethyl diphosphate (terf-butyl diphosphate).

In another preferred embodiment the alkyl monoester according to formula (I) is an alkyl monoester in which group X is phosphate and R , R ² , R ³ and R ⁴ are each independently selected from hydrogen, methyl or ethyl. In a particularly preferred embodiment the alkyl monoester is selected from the group consisting of ethyl monophosphate, propan-1-yl monophosphate (propyl monophosphate), propan-2-yl monophosphate (isopropyl monophosphate), butan-1-yl monophosphate (1 -butyl monophosphate), (2-butyl monophosphate), (isobutyl monophosphate) and (terf-butyl monophosphate).

In another preferred embodiment the alkyl monoester according to formula (I) is an alkyl monoester in which group X is sulfate and R ¹ , R ² , R ³ and R ⁴ are each independently selected from hydrogen, methyl or ethyl. In a particularly preferred embodiment the alkyl monoester is selected from the group consisting of ethyl sulfate, propan-1-yl sulfate (propyl sulfate), propan-2-yl sulfate (isopropyl sulfate), butan-1 -yl sulfate (1 -butyl sulfate), butan-2-yl sulfate (2-butyl sulfate), 2-methylpropan-1-yl sulfate (isobutyl sulfate) and 1 ,1-dimethylethyl sulfate (terf-butyl sulfate).

In a particularly preferred embodiment the monoalkene to be produced is propylene and the alky monoester according to formula (I) is propan-1-yl diphosphate (propyl diphosphate), propan-2-yl diphosphate (isopropyl diphosphate), propan-1-yl monophosphate (propyl monophosphate), propan-2-yl monophosphate (isopropyl monophosphate), propan-1-yl sulfate (propyl sulfate) or propan-2-yl sulfate (isopropyl sulfate). It is to be understood that the alkyl monoester to be used in the method according to the invention may also be a mixture of different compounds of formula (I).

In a preferred embodiment of the present invention the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence selected from the group consisting of SEQ ID NOs: 1 to 10 or a sequence which is at least n % identical to any of SEQ ID NOs: 1 to 10 and having the activity of a terpene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. The term "sequence identity" preferably means the same amino acid residues in the same N- to C-terminal direction.

In one preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 1 or a sequence which is at least n % identical to SEQ ID NO: 1 and having the activity of an isoprene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 1 shows the isoprene synthase from Pueraris monotana var. lobata (Uniprot Q6EJ97).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 2 or a sequence which is at least n % identical to SEQ ID NO: 2 and having the activity of an (E)-beta-ocimene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 2 shows the (E)-beta-ocimene synthase from Vitis vinifera (Uniprot E5GAG5).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 3 or a sequence which is at least n % identical to SEQ ID NO: 3 and having the activity of an (E,E)-alpha-farnesene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 3 shows the (E.E)-alpha- farnesene synthase from Malus domestica (Uniprot Q84LB2).. In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 4 or a sequence which is at least n % identical to SEQ ID NO: 4 and having the activity of an monoterpene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 4 shows a monoterpene synthase from Melaleuca alternifolia (Uniprot Q7Y1V1).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 5 or a sequence which is at least n % identical to SEQ ID NO: 5 and having the activity of an beta-ocimene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90,

91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 5 shows a beta-ocimene synthase from Phaseolus lunatus (Uniprot B1 P189).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 6 or a sequence which is at least n % identical to SEQ ID NO: 6 and having the activity of an pinene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 ,

92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 6 shows a chloroplastic pinene synthase from Abies grandis (Uniprot 024475).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 7 or a sequence which is at least n % identical to SEQ ID NO: 7 and having the activity of an pentalenene synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 7 shows a pentalenene synthase from Streptomyces sp. (strain UC5319) (Uniprot P33247).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 8 or a sequence which is at least n % identical to SEQ ID NO: 8 and having the activity of an germacrene-D synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 8 shows a germacrene-D synthase from Ocimum basilicum (Uniprot Q5SBP6).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 9 or a sequence which is at least n % identical to SEQ ID NO: 9 and having the activity of an beta-eudesmol synthase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 9 shows a beta-eudesmol synthase from Zingiber zerumbet (Uniprot B1 B1 U4).

In another preferred embodiment, the enzyme employed in a method according to the present invention is an enzyme comprising an amino acid sequence as shown in SEQ ID NO: 10 or a sequence which is at least n % identical to SEQ ID NO: 10 and having the activity of an squalene-hopene cyclase with n being an integer between 10 and 100, preferably 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91 , 92, 93, 94, 95, 96, 97, 98 or 99. SEQ ID NO: 10 shows a squalene-hopene cyclase from Alicyclobacillus acidocaldarius subsp. acidocaldarius (Uniprot P33247).

Preferably, the degree of identity is determined by comparing the respective sequence with the amino acid sequence of any one of the above-mentioned SEQ ID NOs. When the sequences which are compared do not have the same length, the degree of identity preferably either refers to the percentage of amino acid residues in the shorter sequence which are identical to amino acid residues in the longer sequence or to the percentage of amino acid residues in the longer sequence which are identical to amino acid residues in the shorter sequence. The degree of sequence identity can be determined according to methods well known in the art using preferably suitable computer algorithms such as CLUSTAL.

When using the Clustal analysis method to determine whether a particular sequence is, for instance, 80% identical to a reference sequence default settings may be used or the settings are preferably as follows: Matrix: blosum 30; Open gap penalty: 10.0; Extend gap penalty: 0.05; Delay divergent: 40; Gap separation distance: 8 for comparisons of amino acid sequences. For nucleotide sequence comparisons, the Extend gap penalty is preferably set to 5.0.

Other algorithms which can be used for calculating sequence identity are those of Needleman and Wunsch or of Smith and Watermann. For sequence comparisons the program PileUp (Feng and Doolittle, J. Mol. Evolution 25 (1987), 351-360; Higgins et al., CABIOS 5 (1989), 151-153) or the programs Gap and Best Fit (Needleman and Wunsch, J. Mol. Biol. 48 (1970), 443-453; Smith and Waterman, Adv. Appl. Math. 2 (1981 ), 482-489) can be used, which are contained in the GCG software package (Genetics Computer Group, 575 Science Drive, Madison, Wisconsin, USA). Preferably, the settings which are used are the standard settings for sequence comparisons.

Preferably, the degree of identity is calculated over the complete length of the sequence.

The enzyme, preferably the terpene synthase or prenyltransferase, employed in the process according to the invention can be a naturally occurring enzyme or it can be an enzyme which is derived from a naturally occurring enzyme, preferably a terpene synthase or a prenyltransferase, e.g. by the introduction of mutations or other alterations which, e.g., alter or improve the enzymatic activity, the stability, etc.

The term "terpene synthase" or "a protein/enzyme having the activity of a terpene synthase" in the context of the present application also covers enzymes which are derived from a terpene synthase, which are capable of eliminating the phosphorus or sulfur containing molecule XH from the alkyl monoester of formula (I) so as to convert it into a monoalkene but which only have a low affinity to their natural substrate or do no longer accept their natural substrate.

Similarly, the term "prenyltransferase" or "a protein/enzyme having the activity of a prenyltransferase" in the context of the present application also covers enzymes which are derived from a prenyltransferase, which are capable of eliminating the phosphorus or sulfur containing molecule XH from the alkyl monoester of formula (I) so as to convert it into a monoalkene but which only have a low affinity to their natural substrate or do no longer accept their natural substrate.

Thus, the term "terpene synthase" or "a protein/enzyme having the activity of a terpene synthase" in the context of the present application also covers enzymes which are derived from a terpene synthase as described herein-above, which are capable of eliminating the phosphorus or sulfur containing molecule XH from the alkyl monoester of formula (I) so as to convert it into a monoalkene but which only have a low affinity to their natural substrate as described herein-above in connection with the different terpene synthases or do no longer accept their natural substrate.

Accordingly, the term "prenyltransferase" or "a protein/enzyme having the activity of a prenyltransferase" in the context of the present application also covers enzymes which are derived from a prenyltransferase as described herein-above, which are capable of eliminating the phosphorus or sulfur containing molecule XH from the alkyl monoester of formula (I) so as to convert it into a monoalkene but which only have a low affinity to their natural substrate as described herein-above in connection with the different prenyltransferases or do no longer accept their natural substrate.

Such a modification of the preferred substrate of a terpene synthase or a prenyltransferase allows to improve the conversion of the alkyl monoester into the monoalkene and to reduce the production of unwanted by-product due to the action of the enzyme on their natural substrate(s). Methods for modifying and/or improving the desired enzymatic activities of proteins are well-known to the person skilled in the art and include, e.g., random mutagenesis or site-directed mutagenesis and subsequent selection of enzymes having the desired properties or approaches of the so-called "directed evolution".

For example, for genetic engineering in prokaryotic cells, a nucleic acid molecule encoding an enzyme, preferably a terpene synthase or a prenyltransferase, can be introduced into plasmids which permit mutagenesis or sequence modification by recombination of DNA sequences. Standard methods (see Sambrook and Russell (2001 ), Molecular Cloning: A Laboratory Manual, CSH Press, Cold Spring Harbor, NY, USA) allow base exchanges to be performed or natural or synthetic sequences to be added. DNA fragments can be connected to each other by applying adapters and linkers to the fragments. Moreover, engineering measures which provide suitable restriction sites or remove surplus DNA or restriction sites can be used. In those cases, in which insertions, deletions or substitutions are possible, in vitro mutagenesis, "primer repair", restriction or ligation can be used. In general, a sequence analysis, restriction analysis and other methods of biochemistry and molecular biology are carried out as analysis methods. The resulting enzyme, preferably terpene synthase or prenyltransferase variants, are then tested for their enzymatic activity and in particular for their capacity to convert an alkyl monoester according to formula (I) into a monoalkene by eliminating molecule XH and prefer an alkyl monoester according to formula (I) as a substrate rather than their natural substrate(s) as described above in connection with the description of the different terpene synthases or prenyltransferases which can be used in the context of the present invention.

Assays for measuring the capacity of a terpene synthase or a prenyltransferase to convert an alkyl monoester according to formula (I) into a monoalkene by eliminating molecule XH are describe in the appended Examples.

Methods for identifying variants with improved enzymatic properties as regards the production of monoalkenes may also be carried out in the presence of a "cofactor" which allows for a steric and/or electronic complementation in the catalytic site of the enzyme due to the fact that the alkyl monoester used as a substrate may be shorter than the natural substrate of the terpene synthase or prenyltransferase employed in the method according to the invention. The cofactor may depend on the natural substrate of the enzyme to be employed in the method according to the invention.

Moreover, it is described for terpene synthases and for prenyltransferases that they require monovalent and/or divalent cations as co-factors (Green et al., J. Biol. Chem. 284 (2009), 8661-8669). Thus, in a further embodiment, a suitable amount of a suitable monovalent (e.g. K ⁺ ) and/or divalent cation is added to the reaction when carrying out the method according to the invention. The divalent cation is preferably Mg ²⁺ or Mn ²⁺ .

The modified version of the enzyme, preferably a terpene synthase or a prenyltransferase, accepting an alkyl monoester according to formula (I), above as a substrate but having a low affinity to its natural substrate or no longer accepting its natural substrate may be derived from a naturally occurring enzyme, preferably a terpene synthase or a prenyltransferase, or from an already modified, optimized or synthetically produced enzyme, preferably a terpene synthase or a prenyltransferase.

The enzyme employed in the process according to the present invention can be a natural version of the protein or a synthetic protein as well as a protein which has been chemically synthesized or produced in a biological system or by recombinant processes. The enzyme may also be chemically modified, for example in order to improve its/their stability, resistance, e.g. to temperature, for facilitating its purification or its immobilization on a support. The enzyme may be used in isolated form, purified form, in immobilized form, as a crude or partially purified extract obtained from cells synthesizing the enzyme, as chemically synthesized enzyme, as recombinantly produced enzyme, in the form of microorganisms producing them etc.

The process according to the present invention may be carried out in vitro or in vivo. An in vitro reaction is understood to be a reaction in which no cells are employed, i.e. an acellular reaction.

For carrying out the process in vitro the substrates for the reaction and the enzyme are incubated under conditions (buffer, temperature, cofactors etc.) allowing the enzyme to be active and the enzymatic conversion to occur. The reaction is allowed to proceed for a time sufficient to produce the monoalkene. The production of the monoalkene can be detected by gas chromatography (GC) or GC/MS analysis.

The enzyme may be in any suitable form allowing the enzymatic reaction to take place. It may be purified or partially purified or in the form of crude cellular extracts or partially purified extracts. It is also possible that the enzyme is immobilized on a suitable carrier.

Since the alkyl monoester according to formula (I), above, used as a substrate may be shorter than the natural substrate used by the enzyme, it may be advantageous to add to the reaction mixture a "cofactor" which allows for a steric and/or electronic complementation in the catalytic site of the enzyme as mentioned above.

In general, if the monoalkene product is a gaseous and scarcely soluble in water under the conditions of temperature at which the process is conducted, the equilibrium of the reaction catalyzed by the enzyme employed is shifted and the reaction goes to completion in the direction of the formation of the gasous alkene , in particular if that gas is permanently removed from the reaction vessel.

In one particularly preferred embodiment, the enzyme (preferably a terpene synthase or a prenyltransferase) used in the process according to the invention is a thermophilic enzyme, i.e. an enzyme which is capable of catalyzing the reaction at elevated temperatures. The term "elevated temperatures" means temperatures above 37°C. Such enzymes can e.g. be obtained by mutagenizing available enzyme sequences, in particular terpene synthase sequences or prenyltransferase sequences, and testing them for an increased enzymatic activity under increased temperature conditions. The advantage of using an enzyme which is functional at elevated temperatures is that the produced monoalkene can immediately go into the gaseous phase and can be constantly removed from the reaction thereby driving the reaction into the direction of product formation. This advantage exists for all the produced monoalkenes which are in gaseous form at or below the temperature at which the reaction is carried out. Accordingly, in the method of the present invention the step of enzymatically converting an alkyl monoester according to formula (I), above, into a monoalkene by eliminating molecule XH is preferably carried out at an elevated temperature (i.e. at a temperature above 37°C, including a temperature above 37°C and below 100°C, such as, e.g., at a temperature of 38°C, 40°C, 50°C, 70°C or 90°C) and the enzymatic conversion is catalyzed by a thermophilic enzyme as described herein above. The use of elevated temperatures also allows producing monoalkenes in a manner that they directly degas from the reaction mixture.

For carrying out the process in vivo use is made of a suitable organism/microorganism which is capable of expressing an enzyme as defined above, preferably a terpene synthase or a prenyltransferase. In a preferred embodiment, the organism/microorganism is capable of secreting the enzyme. In such an embodiment, the substrate for the reaction can be provided in the culture medium and the produced monoalkene can be recovered from the culture. In another preferred embodiment the organism/microorganism is also capable of producing the substrate, i.e. the alkyl monoester according to formula (I), above, to be converted. Thus, in the case of this embodiment the method according to the invention is characterised in that the conversion of the alkyl monoester according to formula (I), above, into the monoalkene is realized in the presence of an organism/ microorganism capable of expressing, preferably secreting, an enzyme as defined above, preferably a terpene synthase or a prenyltransferase. In another preferred embodiment of such a method the organism/microorganism is also capable of producing an alkyl monoester according to formula (I), above, which should be converted.

The term "which is capable of producing an alkyl monoester according to formula (I)" in the context of the present invention means that the organism/microorganism has the capacity to produce such an alkyl monoester within the cell due to the presence of enzymes providing enzymatic activities allowing the production of such an alkyl monoester from metabolic precursors. The organism/microorganism can be an organism/microorganism which naturally has the capacity to produce the corresponding alkyl monoester or it can be an organism/microorganism which has been genetically modified so as to be capable of producing the corresponding alkyl monoester.

In a preferred embodiment, the organism employed in the method according to the invention is an organism, preferably a microorganism, which has the capacity to produce the respective alkyl monoester according to formula (I), above, to be converted into the corresponding monoalkene and which is recombinant in the sense that it has further been genetically modified so as to express an enzyme as defined above, preferably a terpene synthase or a prenyltransferase as described above. The term "recombinant" in one embodiment means that the organism is genetically modified so as to contain a foreign nucleic acid molecule encoding said enzyme as defined above. In a preferred embodiment the organism has been genetically modified so as to contain a foreign nucleic acid molecule encoding said enzyme as defined above. The term "foreign" in this context means that the nucleic acid molecule does not naturally occur in said organism/microorganism. This means that it does not occur in the same structure or at the same location in the organism/microorganism. In one preferred embodiment, the foreign nucleic acid molecule is a recombinant molecule comprising a promoter and a coding sequence encoding the enzyme in which the promoter driving expression of the coding sequence is heterologous with respect to the coding sequence. Heterologous in this context means that the promoter is not the promoter naturally driving the expression of said coding sequence but is a promoter naturally driving expression of a different coding sequence, i.e., it is derived from another gene, or is a synthetic promoter or a chimeric promoter. Preferably, the promoter is a promoter heterologous to the organism/microorganism, i.e. a promoter which does not naturally occur in the respective organism/microorganism. Even more preferably, the promoter is an inducible promoter. Promoters for driving expression in different types of organisms, in particular in microorganisms, are well known to the person skilled in the art.

In another preferred embodiment the nucleic acid molecule is foreign to the organism/microorganism in that the encoded enzyme is not endogenous to the organism/microorganism, i.e. is naturally not expressed by the organism/microorganism when it is not genetically modified. In other words, the encoded enzyme is heterologous with respect to the organism/microorganism.

The term "recombinant" in another embodiment means that the organism is genetically modified in the regulatory region controlling the expression of an enzyme as defined above which naturally occurs in the organism so as to lead to an increase in expression of the respective enzyme in comparison to a corresponding non- genetically modified organism. The meaning of the term high "higher expression" is described further below.

Such a modification of a regulatory region can be achieved by methods known to the person skilled in the art. One example is to exchange the naturally occurring promoter by a promoter which allows for a higher expression or to modify the naturally occurring promoter so as to show a higher expression. Thus, in this embodiment the organism contains in the regulatory region of the gene encoding an enzyme as defined above a foreign nucleic acid molecule which naturally does not occur in the organism and which leads to a higher expression of the enzyme in comparison to a corresponding non-genetically modified organism.

The foreign nucleic acid molecule may be present in the organism/microorganism in extrachromosomal form, e.g. as a plasmid, or stably integrated in the chromosome. A stable integration is preferred.

In another preferred embodiment the organism/microorganism is characterized in that the expression/activity of an enzyme as defined above is higher in the organism/microorganism genetically modified with the foreign nucleic acid molecule in comparison to the corresponding non-genetically modified organism/microorganism. A "higher" expression/activity means that the expression/activity of the enzyme in the genetically modified microorganism is at least 10%, preferably at least 20%, more preferably at least 30% or 50%, even more preferably at least 70% or 80% and particularly preferred at least 90% or 100% higher than in the corresponding non-genetically modified organism/microorganism. In even more preferred embodiments the increase in expression/activity may be at least 150%, at least 200% or at least 500%. In particularly preferred embodiments the expression is at least 10-fold, more preferably at least 100-fold and even more preferred at least 1000-fold higher than in the corresponding non-genetically modified organism/microorganism. The term "higher" expression/activity also covers the situation in which the corresponding non-genetically modified organism/microorganism does not express a corresponding enzyme so that the corresponding expression/activity in the non- genetically modified organism/microorganism is zero.

Methods for measuring the level of expression of a given protein in a cell are well known to the person skilled in the art. In one embodiment, the measurement of the level of expression is done by measuring the amount of the corresponding protein. Corresponding methods are well known to the person skilled in the art and include Western Blot, ELISA etc. In another embodiment the measurement of the level of expression is done by measuring the amount of the corresponding RNA. Corresponding methods are well known to the person skilled in the art and include, e.g., Northern Blot.

Methods for measuring the enzymatic activity of the described enzymes are known in the art and have already been described above.

Methods for preparing an organism which is genetically modified so as to produce an enzyme as described above, preferably a microorganism, are well known in the art. Thus, generally, the organism/microorganism is transformed with a DNA construct allowing expression of the respective enzyme in the microorganism. Such a construct normally comprises the coding sequence in question linked to regulatory sequences allowing transcription and translation in the respective host cell, e.g. a promoter and/or enhancer and/or transcription terminator and/or ribosome binding sites etc.

The term "organism" as used in the context of the present invention refers in general to any possible type of organism, in particular eukaryotic organisms, prokaryotic organisms and archaebacteria. The term includes animal, plants, fungi, bacteria and archaebacteria. The term also includes isolated cells or cell aggregates of such organisms, like tissue or ca Hi.

In one preferred embodiment, the organism is a microorganism. The term "microorganism" in the context of the present invention refers to prokaryotic cells, in particular bacteria, as well as to fungi, such as yeasts, and also to algae and archaebacteria. In one preferred embodiment, the microorganism is a bacterium. In principle any bacterium can be used. Preferred bacteria to be employed in the process according to the invention are bacteria of the genus Bacillus, Clostridium, Pseudomonas, Zymomonas or Escherichia. In a particularly preferred embodiment the bacterium belongs to the genus Escherichia and even more preferred to the species Escherichia coli.

In another preferred embodiment the microorganism is a fungus, more preferably a fungus of the genus Saccharomyces, Schizosaccharomyces, Aspergillus or Trichoderma and even more preferably of the species Saccharomyces cerevisiae, Schizosaccharomyces pombe, Aspergillus niger or of the species Trichoderma reesei.

In still another preferred embodiment the microorganism is a photosynthetically active microorganism such as bacteria which are capable of carrying out photosynthesis or micro-algae.

In a particularly preferred embodiment the microorganism is an algae, more preferably an algae belonging to the diatomeae.

If microorganisms are used in the context of the method of the present invention, it is also conceivable to carry out the method according to the invention in a manner in which two types of microorganisms are employed, i.e. one type which produces the alkyl monoester according to formula (I), above, which should be converted into a monoalkene and one type which uses the alkyl monoester produced by the first type of microorganisms to convert it with the help of an enzyme as defined herein above into the respective monoalkene.

When the process according to the invention is carried out in vivo by using microorganisms providing the respective enzyme activity, the microorganisms are cultivated under suitable culture conditions allowing the occurrence of the enzymatic reaction. The specific culture conditions depend on the specific microorganism employed but are well known to the person skilled in the art. The culture conditions are generally chosen in such a manner that they allow the expression of the genes encoding the enzymes for the respective reactions. Various methods are known to the person skilled in the art in order to improve and fine-tune the expression of certain genes at certain stages of the culture such as induction of gene expression by chemical inducers or by a temperature shift. In another preferred embodiment the organism employed in the method according to the invention is an organism which is capable of photosynthesis, such as a plant or microalgae. In principle any possible plant can be used, i.e. a monocotyledonous plant or a dicotyledonous plant. It is preferable to use a plant which can be cultivated on an agriculturally meaningful scale and which allows to produce large amounts of biomass. Examples are grasses like Lolium, cereals like rye, barley, oat, millet, maize, other starch storing plants like potato or sugar storing plants like sugar cane or sugar beet. Conceivable is also the use of tobacco or of vegetable plants such as tomato, pepper, cucumber, egg plant etc. Another possibility is the use of oil storing plants such as rape seed, olives etc. Also conceivable is the use of trees, in particular fast growing trees such as eucalyptus, poplar or rubber tree (Hevea brasiliensis).

In a particularly preferred embodiment the organism/microorganism employed in the method according to the invention is an organism/microorganism which is thermophilic in the sense that it can survive and catalyze the conversion of the alkyl monoester of formula (I) into a monoalkene of formula (II) at elevated temperatures. The term "elevated" temperature means a temperature over 37°C. Examples for such organism/microorganism are bacteria of the genus Thermus, e.g. Thermus thermophilus or Thermus aquaticus, or bacteria of the genus Clostridium, such as Clostridium thermocellum. Other examples are microorganisms which are extremely heat-tolerant, e.g. microorganisms of the genus Thermotoga, such as Thermotoga maritime, or microorganisms of the genus Aquifex, such as Aquifex aeolicus.

The present invention also relates to an organism, preferably a microorganism, which is characterized by the following features:

(a) it is capable of producing an alkyl monoester according to formula (I), above; and

(b) it expresses an enzyme which is capable of catalyzing the conversion of said alkyl monoester into a monoalkene by elimination of molecule XH in formula (I), preferably a terpene synthase or a prenyltransferase. As regards the source, nature, properties, sequence etc. of the enzyme expressed in the organism according to the invention, the same applies as has been set forth above in connection with the method according to the invention.

In one preferred embodiment, the organism according to the invention is an organism, preferably a microorganism, which naturally has the capacity to produce the alkyl monoester according to formula (I), above, i.e., feature (a) mentioned above is a feature which the organism, preferably microorganism, shows naturally.

In another preferred embodiment, the organism, preferably microorganism, according to the invention is a genetically modified organism/microorganism derived from an organism/microorganism which naturally does not produce the respective alkyl monoester according to formula (I), above, but which has been genetically modified so as to produce said alkyl monoester, i.e. by introducing the gene(s) necessary for allowing the production of the alkyl monoester in the organism/microorganism. In principle any organism/microorganism can be genetically modified in this way. The enzymes responsible for the synthesis of the respective alkyl monoester are generally known. Genes encoding corresponding enzymes are known in the art and can be used to genetically modify a given organism, preferably microorganism so as to produce the alkyl monoester.

In a further preferred embodiment the organism, preferably a microorganism, according to the invention is genetically modified so as to express an enzyme which is capable of catalyzing the conversion of an alkyl monoester according to formula (I), above, into a monoalkene as described herein-above. In this context, the term "recombinant" means in a first aspect that the organism contains a foreign nucleic acid molecule encoding a corresponding enzyme. The term "foreign" in this context means that the nucleic acid molecule does not naturally occur in said organism/microorganism. This means that it does not occur in the same structure or at the same location in the organism/microorganism. In one preferred embodiment, the foreign nucleic acid molecule is a recombinant molecule comprising a promoter and a coding sequence encoding said enzyme in which the promoter driving expression of the coding sequence is heterologous with respect to the coding sequence. Heterologous in this context means that the promoter is not the promoter naturally driving the expression of said coding sequence but is a promoter naturally driving expression of a different coding sequence, i.e., it is derived from another gene, or is a synthetic promoter or a chimeric promoter. Preferably, the promoter is a promoter heterologous to the organism/microorganism, i.e. a promoter which does naturally not occur in the respective organism/microorganism. Even more preferably, the promoter is an inducible promoter. Promoters for driving expression in different types of organisms, in particular microorganisms, are well known to the person skilled in the art.

In another preferred embodiment the nucleic acid molecule is foreign to the organism/microorganism in that the encoded enzyme is not endogenous to the organism/microorganism, i.e. is naturally not expressed by the organism/microorganism when it is not genetically modified. In other words, the encoded enzyme is heterologous with respect to the organism/microorganism.

The term "recombinant" in another aspect means that the organism is genetically modified in the regulatory region controlling the expression of an enzyme as defined above which naturally occurs in the organism so as to lead to an increase in expression of the respective enzyme in comparison to a corresponding non- genetically modified organism. The meaning of the term high "higher expression" is described further below.

Such a modification of a regulatory region can be achieved by methods known to the person skilled in the art. One example is to exchange the naturally occurring promoter by a promoter which allows for a higher expression or to modify the naturally occurring promoter so as to show a higher expression. Thus, in this embodiment the organism contains in the regulatory region of the gene encoding an enzyme as defined above a foreign nucleic acid molecule which naturally does not occur in the organism and which leads to a higher expression of the enzyme in comparison to a corresponding non-genetically modified organism.

In a further preferred embodiment the organism/microorganism is characterized in that the expression/activity of the enzyme is higher in the organism/microorganism genetically modified with the foreign nucleic acid molecule in comparison to the corresponding non-genetically modified organism/microorganism. A "higher" expression/activity means that the expression/activity of the enzyme in the genetically modified organism/microorganism is at least 10%, preferably at least 20%, more preferably at least 30% or 50%, even more preferably at least 70% or 80% and particularly preferred at least 90% or 100% higher than in the corresponding non-genetically modified organism/microorganism. In even more preferred embodiments the increase in expression/activity may be at least 150%, at least 200% or at least 500%. In particularly preferred embodiments the expression is at least 10-fold, more preferably at least 100-fold and even more preferred at least 1000-fold higher than in the corresponding non-genetically modified organism/microorganism.

The term "higher" expression/activity also covers the situation in which the corresponding non-genetically modified organism/microorganism does not express a corresponding enzyme so that the corresponding expression/activity in the non- genetically modified organism/microorganism is zero.

Methods for measuring the level of expression of a given protein in a cell are well known to the person skilled in the art. In one embodiment, the measurement of the level of expression is done by measuring the amount of the corresponding protein. Corresponding methods are well known to the person skilled in the art and include Western Blot, ELISA etc. In another embodiment the measurement of the level of expression is done by measuring the amount of the corresponding RNA. Corresponding methods are well known to the person skilled in the art and include, e.g., Northern Blot.

Methods for measuring the enzymatic activity of an enzyme as described herein are known in the art and have already been described above.

The term "organism" as used in the context of the present invention refers in general to any possible type of organism, in particular eukaryotic organisms, prokaryotic organisms and archaebacteria. The term includes animal, plants, fungi, bacteria and archaebacteria. The term also includes isolated cells or cell aggregates of such organisms, like tissue or calli.

In one preferred embodiment, the organism is a microorganism. The term "microorganism" in the context of the present invention refers to prokaryotic cells, in particular bacteria, as well as to fungi, such as yeasts, and also to algae and archaebacteria. In one preferred embodiment, the microorganism is a bacterium. In principle any bacterium can be used. Preferred bacteria to be employed in the process according to the invention are bacteria of the genus Bacillus, Clostridium, Pseudomonas, Zymomonas or Escherichia. In a particularly preferred embodiment the bacterium belongs to the genus Escherichia and even more preferred to the species Escherichia coli.

In another preferred embodiment the microorganism is a fungus, more preferably a fungus of the genus Saccharomyces, Schizosaccharomyces, Aspergillus or Trichoderma and even more preferably of the species Saccharomyces cerevisiae, Schizosaccharomyces pombe, Aspergillus niger or of the species Trichoderma reesei.

In still another preferred embodiment the microorganism is a photosynthetically active microorganism such as bacteria which are capable of carrying out photosynthesis or micro-algae.

In a particularly preferred embodiment the microorganism is an algae, more preferably an algae from the genus belonging to the diatomeae.

In another preferred embodiment the organism according to the invention is an organism which is capable of photosynthesis, such as a plant or micro-algae. In principle, it can be any possible plant, i.e. a monocotyledonous plant or a dicotyledonous plant. It is preferably a plant which can be cultivated on an agriculturally meaningful scale and which allows to produce large amounts of biomass. Examples are grasses like Lolium, cereals like rye, barley, oat, millet, maize, other starch storing plants like potato or sugar storing plants like sugar cane or sugar beet. Conceivable is also the use of tobacco or of vegetable plants such as tomato, pepper, cucumber, egg plant etc. In another preferred embodiment the plant is an oil storing plants such as rape seed, olives etc. Also conceivable is the use of trees, in particular fast growing trees such as eucalyptus, poplar or rubber tree (Hevea brasiliensis).

In a particularly preferred embodiment the organism/microorganism employed in the method according to the invention is an organism/microorganism which is thermophilic in the sense that it can survive and catalyze the dehydration of the alkyl monoester of formul (I) into a monoalkene of formula (II) at elevated temperatures. The term "elevated" temperature means a temperature over 37°C. Examples for such organism/microorganism are bacteria of the genus Thermus, e.g. Thermus thermophilus or Thermus aquaticus, or bacteria of the genus Clostridium, such as Clostridium thermocellum. Other examples are microorganisms which are extremely heat-tolerant, e.g. microorganisms of the genus Thermotoga, such as Thermotoga maritime, or microorganisms of the genus Aquifex, such as Aquifex aeolicus.

The present invention also relates to the use of an organism which expresses an enzyme as described herein-above, preferably a terpene synthase or a prenyltransferase, for converting an alkyl monoester according to formula (I), above into a monoalkene according to formula (II), above, by enzymatically eliminating molecule XH as specified in formula (I).

Preferably, in such a use, the organism is an organism according to the present invention, i.e. a (micro)organism, which is characterized by the following features:

(a) it is capable of producing an alkyl monoester according to formula (I), above; and

(b) it expresses an enzyme which is capable of catalyzing the conversion of said alkyl monoester into a monoalkene by elimination of molecule XH in formula (I), preferably a terpene synthase or a prenyltransferase.

I.e., the present invention also relates to the use of an organism/microorganism according to the invention for the production of a monoalkene from the respective alkyl monoester.

The present invention also relates to a composition comprising an organism according to the present invention.

Moreover, the present invention also relates to a composition comprising (i) an alkyl monoester according to formula (I), above; and (ii) an enzyme which is capable of catalyzing the conversion of said alkyl monoester into a monoalkene by elimination of molecule XH in formula (I), preferably a terpene synthase or a prenyltransferase, or an organism according to the present invention.

For the preferred embodiments of the enzyme and the organism, the same applies as has already been set forth above in connection with the method and the organism according to the invention. Moreover, the present invention also relates to the use of a terpene synthase or of a prenyltransferase for the conversion of an alkyl monoester according to formula (I), above, into a monoalkene by elimination of molecule XH in formula (I).

For the preferred embodiments of the enzyme the same applies as has already been set forth above in connection with the method and the organism according to the invention.

Finally, the present invention also relates to the use of an alkyl monoester according to formula (I), above, for the production of a monoalkene, comprising the enzymatic conversion of the alkyl monoester into the monoalkene by elimination of molecule XH of formula (I).

In a preferred embodiment the enzymatic conversion is achieved by an enzyme as described above in connection with the method according to the invention, more preferably with a terpene synthase or a prenyltransferase and most preferably the conversion is achieved by the use of an organism according to the invention.

Figure 1 : shows in a schematic form the natural reaction catalyzed by the terpene synthases as well as the reaction when it is applied to an alkyl monoester as defined in formula (I), above.

Figure 2: shows propylene production from propan-2-yl diphosphate using terpene synthases (Example 2).

Figure 3: shows mass spectrums of commercial propylene (a) and propylene produced from propan-2-yl diphosphate in enzymatic reaction catalyzed by isoprene synthase from Pueraria montana var. lobata (b). Characteristic ions of m/z 41 and 27, representing propylene were observed in both spectrums.

The following Examples serve to illustrate the invention.

Example 1 : Cloning, expression and purification of enzymes Cloning, bacterial cultures and expression of proteins.

The genes encoding the enzymes of interest were cloned in the pET 25b(+) vector (Novagen). Nucleotide sequences encoding chloroplast transit peptides in plant terpene synthases were removed, resulting in a DNA sequences encoding the mature proteins only. A stretch of 6 histidine codons was inserted after the methionine initiation codon to provide an affinity tag for purification. Competent E. coli BL21 (DE3) cells (Novagen) were transformed with this vector by heat shock. The transformed cells were grown with shaking (160 rpm) on ZYM-5052 auto-induction medium (Studier FW, Prot.Exp.Pur. 41 , (2005), 207-234) for 6h at 37°C and protein expression was continued at 28°C or 18° C overnight (approximately 16 h). The cells were collected by centrifugation at 4°C, 10,000 rpm for 20 min and the pellets were frozen at -80°C.

Protein purification and concentration.

The pellets from 200 ml of culture cells were thawed on ice and resuspended in 5 ml of Na ₂ HP0 ₄ pH 8 containing 300 mM NaCI, 5 mM MgCI ₂ and 1 mM DTT. Twenty microliters of lysonase (Novagen) were added. Cells were incubated 10 minutes at room temperature and then returned to ice for 20 minutes. Cell lysis was completed by sonication for 3 x 15 seconds. The bacterial extracts were then clarified by centrifugation at 4°C, 10,000 rpm for 20 min. The clarified bacterial lysates were loaded on PROTINO-1000 Ni-TED or Ni-IDA column (Macherey-Nagel) allowing adsorption of 6-His tagged proteins. Columns were washed and the enzymes of interest were eluted with 4 ml of 50 mM Na ₂ HP0 ₄ pH 8 containing 300 mM NaCI, 5 mM MgCI ₂ , 1 mM DTT, 250 mM imidazole. Eluates were then concentrated and desalted on Amicon Ultra-4 10 kDa filter unit (Millipore) and resuspended in 0.25 ml 50 mM Tris-HCI pH 7.5 containing 1 mM DTT and 10 mM MgCI ₂ . Protein concentrations were quantified by direct UV 280 nm measurement on the NanoDrop 1000 spectrophotometer (Thermo Scientific). The purity of proteins thus purified varied from 60 % to 90 %.

Example 2: Propylene production from propan-2-yl diphosphate with purified terpene synthases

The enzymatic assays were carried out under the following conditions:

50 mM Tris-HCI pH 7.5 100 mM MgCI ₂

50 mM KCI

5 mM DTT

50 mM propan-2-yl diphosphate

5 mg of the terpene synthase was added to 0.5 ml of reaction mixture. An enzyme- free control reaction was carried out in parallel. Assays were incubated at 37°C for 60 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. One ml of the headspace phase was then collected and injected into a gas chromatograph Varian 430-GC equipped with a flame ionization detector (FID). Nitrogen was used as carrier gas with a flow rate of 1.5 mL/min. Volatile compounds were chromatographically separated on RT-Alumina Bond/Na ₂ SO ₄ column (Restek) using an isothermal mode at 130 °C. The enzymatic reaction product was identified by comparison with propylene standard (Sigma). Under these GC conditions, the retention time for propylene was 2.8 min. A significant production of propylene was observed with several purified terpene synthases (Figure 2). Gas chromatography-mass spectrometry (GC-MS) was then used to confirm the identity of the product detected by gas chromatography with flame ionization. The samples were analyzed on a Varian 3400 CX gas chromatograph equipped with Varian Saturn 3 mass selective detector. The mass spectrum of propylene obtained by enzymatic conversion of propan-2-yl diphosphate was similar to the one of commercial propylene (Figure 3).

Example 3: Propylene production from propan-2-yl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM propan-2-yl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Propylene production is analyzed using the GC/FID procedure described in example 2. Example 4: Ethylene production from ethyl diphosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM ethyl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. One ml of the headspace phase is then collected and injected into a gas chromatograph Varian 430-GC equipped with a flame ionization detector (FID). Nitrogen is used as carrier gas with a flow rate of 1.5 mL/min. Volatile compounds are chromatographically separated on RT-Alumina Bond/Na ₂ SO ₄ column (Restek) using an isothermal mode at 130 °C. The enzymatic reaction product is identified by comparison with ethylene standard (Sigma). Under these GC conditions, the retention time for ethylene is 2.2 min

Example 5: Propylene production from propan-1-yl diphosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM propan-1-yl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Propylene production is analyzed using the GC/FID procedure described in Example 2.

Example 6: Isobutene production from 2-methylpropan-1-yl diphosphate with purified terpene synthases The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM 2-methylpropan-1-yl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. One ml of the headspace phase is then collected and injected into a gas chromatograph Varian 430-GC equipped with a flame ionization detector (FID). Nitrogen is used as carrier gas with a flow rate of 1.5 mL/min. Volatile compounds are chromatographically separated on RT-Alumina Bond/Na ₂ SO ₄ column (Restek) using an isothermal mode at 130 °C. The enzymatic reaction product is identified by comparison with isobutene standard (Sigma). Under these GC conditions, the retention time for isobutene is 4.8 min.

Example 7: Isobutene production from 1 ,1-dimethylethyl diphosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM 1 ,1-dimethylethyl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Isobutene production is analyzed using the GC/FID procedure described in Example 6.

Example 8: But-1-ene production from butan-1-yl diphosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂ 20-50 mM KCI

2-5 mM DTT

50 mM butan-1-yl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 20-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. One ml of the headspace phase is then collected and injected into a gas chromatograph Varian 430-GC equipped with a flame ionization detector (FID). Nitrogen is used as carrier gas with a flow rate of 1.5 mL/min. Volatile compounds are chromatographically separated on RT-Alumina Bond/Na ₂ SO column (Restek) using an isothermal mode at 130 °C. The enzymatic reaction product is identified by comparison with but-1-ene standard (Sigma). Under these GC conditions, the retention time for but-1-ene is 4.3 min.

Example 9: But-1-ene and but-2-ene production from butan-2-yl diphosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM butan-2-yl diphosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. But-1-ene and but-2-ene production is analyzed using the GC/FID procedure described in Example 8. Under these GC conditions, the retention time for trans but-2-ene and cis but-2-ene are 4.2 min and 4.9 min, respectively.

Example 10: Ethylene production from ethyl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI 2-5 mM DTT

50 mM ethyl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Ethylene production is analyzed using the GC/FID procedure described in Example 4.

Example 11 : Propylene production from propan-1-yl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM propan-1-yl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Propylene production is analyzed using the GC/FID procedure described in Example 2.

Example 12: Isobutene production from 2-methylpropan-1-yl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM HEPES pH 8.2

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM 2-methylpropan-1-yl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Isobutene production is analyzed using the GC/FID procedure described in example 6. Example 13: Isobutene production from 1,1-dimethylethyl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions

50 mM Tris-HCI pH 7.5

50-100 mM MgCb

20-50 mM KCI

2-5 mM DTT

50 mM 1 ,1-dimethylethyl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Isobutene production is analyzed using the GC/FID procedure described in Example 6.

Example 14: But-1-ene production from butan-1-yl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM butan-1-yl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. But-1-ene production is analyzed using the GC/FID procedure described in Example.8

Example 15: But-1-ene and but-2-ene production from butan-2-yl monophosphate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT 50 mM butan-2-yl monophosphate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. But-1-ene and but-2-ene production is analyzed using the GC/FID procedure described in Example 9.

Example 16: Ethylene production from ethyl sulfate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM ethyl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Ethylene production is analyzed using the GC/FID procedure described in Example 4.

Example 17: Propylene production from propan-1-yl sulfate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM propan-1-yl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Propylene production is analyzed using the GC/FID procedure described in Example 2.

Example 18: Propylene production from propan-2-yl sulfate with purified terpene synthases The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM propan-2-yl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Propylene production is analyzed using the GC/FID procedure described in Example 2.

Example 19: Isobutene production from 2-methylpropan-1-yl sulfate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM HEPES pH 8.2

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM 2-methylpropan-1-yl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Isobutene production is analyzed using the GC/FID procedure described in Example 6.

Example 20: Isobutene production from 1 ,1-dimethylethyl sulfate with purified terpene synthases

The enzymatic assays are carried out under the following conditions

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM 1 ,1-dimethylethyl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. Isobutene production is analyzed using the GC/FID procedure described in Example 6.

Example 21: But-1-ene production from butan-1-yl sulfate with purified terpene synthases

The enzymatic assays are carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM butan-1-yl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. But-1-ene production is analyzed using the GC/FID procedure described in Example.8

Example 22: But-1-ene and but-2-ene production from butan-2-yl sulfate with purified terpene synthases

The enzymatic assays were carried out under the following conditions:

50 mM Tris-HCI pH 7.5

50-100 mM MgCI ₂

20-50 mM KCI

2-5 mM DTT

50 mM butan-2-yl sulfate

5 mg of the terpene synthase is added to 0.5 ml of reaction mixture. An enzyme-free control reaction is carried out in parallel. Assays are incubated at 37°C for 24-48 hours in a 1.5 ml sealed glass vial (Interchim) with shaking. But-1-ene and but-2-ene production is analyzed using the GC/FID procedure described in Example 9.

Example 23: Propylene production from propan-2-yl diphosphate using purified prenyltransferase

Enzyme catalyzed conversion of propan-2-yl diphosphate into propylene is carried out under the following conditions: 50 mM Tris-HCI pH 7.5

20 mM propan-2-yl diphosphate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Propylene production is analyzed using GC/FID procedure described in Example 2.

Example 24: Propylene production from propan-2-yl monophosphate using purified prenyltransferase

Enzyme catalyzed conversion of propan-2-yl monophosphate into propylene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM propan-2-yl monophosphate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Propylene production is analyzed using GC/FID procedure described in Example 2.

Example 25: Propylene production from propan-2-yl sulfate using purified prenyltransferase

Enzyme catalyzed conversion of propan-2-yl sulfate into propylene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM propan-2-yl sulfate 33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Propylene production is analyzed using GC/FID procedure described in Example 2.

Example 26: Isobutene production from 1,1-dimethylethyl diphosphate using purified prenyltransferase

Enzyme catalyzed conversion of 1 ,1-dimethylethyl diphosphate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 1 ,1-dimethylethyl diphosphate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.

Example 27: Isobutene production from 1,1-dimethylethyl monophosphate using purified prenyltransferase

Enzyme catalyzed conversion of 1 ,1-dimethylethyl monophosphate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 1 ,1-dimethylethyl monophosphate

33 mM KCI

33 mM MgCI ₂ 4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.

Example 28: Isobutene production from 1 ,1-dimethylethyl sulfate using purified prenyltransferase

Enzyme catalyzed conversion of 1 ,1-dimethylethyl sulfate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 1 ,1-dimethylethyl sulfate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.

Example 29: Isobutene production from 2-methylpropan-1-yl diphosphate using purified prenyltransferase

Enzyme catalyzed conversion of 2-methylpropan-1-yl diphosphate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 2-methylpropan-1-yl diphosphate

33 mM KCI

33 mM MgCI ₂

4 mM DTT The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.

Example 30: Isobutene production from 2-methylpropan-1-yl monophosphate using purified prenyltransferase

Enzyme catalyzed conversion of 2-methylpropan-1-yl monophosphate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 2-methylpropan-1-yl monophosphate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture.

Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.

Example 31 : Isobutene production from 2-methylpropan-1-yl sulfate using purified prenyltransferase

Enzyme catalyzed conversion of 2-methylpropan-1-yl sulfate into isobutene is carried out under the following conditions:

50 mM Tris-HCI pH 7.5

20 mM 2-methylpropan-1-yl sulfate

33 mM KCI

33 mM MgCI ₂

4 mM DTT

The reaction is started by adding 3 mg of the preparation of prenyltransferase to 0.5 ml of reaction mixture. Assays are incubated with shaking at 37-42 °C for 2-72 h in 1.5 ml sealed glass vials (Interchim). Isobutene production is analyzed using GC/FID procedure described in Example 6.