Formation of L-2-aminobutyric acid from citramalic acid, citraconic acid or 2-oxobutyric acid

Abstract

The present invention relates to the preparation of an important pharmaceutical intermediate, L-2-aminobutyric acid (L-2-ABA), from readily available and economical substrates such as citramalate or citraconic acid and enzymes such as LeuCD, LeuB, and ValDH or IlvE by cell-free systems and biotransformation methods using genetically engineered strains.

Description

[Technical field]

[0001] The present invention relates to the preparation of an important pharmaceutical intermediate, L-2-aminobutyric acid (L-2-ABA), by a cell-free system and biotransformation method using genetically engineered strains and its cost-effective application. [Background technology]

[0002] L-2-ABA is an unnatural 4C aliphatic amino acid, also known as L-homoalanine, and is a key chiral intermediate in the synthesis of important drugs, namely the antiepileptic drugs levetiracetam, brivaracetam, and the antituberculosis drug ethambutol. L-2-ABA has been produced by chemical methods, but such methods result in undesirable racemic mixtures. L-2-ABA has also been produced by glucose fermentation, but such methods have low productivity levels of 5 g / l.

[0003] EP2539444 discloses inoculation of wild-type E. coli BW25113 culture in M9 medium supplemented with 10 g / L 2-ketobutyrate and incubation at 37° C. for 24 hours. After 24 hours, HPLC analysis showed that only 182 mg / L L-homoalanine was produced. Branched-chain amino acid aminotransferase IlvE was cloned and overexpressed in BW25113, which increased L-homoalanine production to 1.2 g / L. By providing an additional 10 g / L amino donor glutamate, the L-homoalanine titer was further increased to 3.2 g / L. This experiment demonstrated that transaminases such as IlvE2 were able to animate ketobutyrate to L-homoalanine. However, because transamination is a reversible reaction process, a high concentration of glutamate was required to control the reaction equilibrium. Even under such extreme conditions, the conversion rate of transamination of 2-ketobutyrate to L-homoalanine was only 32%.

[0004] CN109777788 discloses a kind of leucine dehydrogenase mutant and recombinant bacteria E. coli BL21-pET28a-BtLDH007 for expressing the enzyme activity of leucine dehydrogenase. E. coli BL21-pET28a-BtLDH007 was used for transformation of 2-ketobutyric acid to produce L-2-aminobutyric acid. In a 1L transformation system, 80g / L of 2-ketobutyric acid was dissolved in 0.015-0.02mol / L NaH2PO4-Na2HPO4 buffer (pH 8.0), 20g / L of wet cell mass, 10g / L of ammonium formate, 1.0g / L of NAD, and 1.0g / L of ammonium formate were added. + Up to 1500 U / L of formate dehydrogenase enzyme is added, the pH is adjusted to 8.0 with 4 mol / L NaOH solution, a temperature of 30° C., an aeration of 3 vvm, and an agitation speed of 300 rpm are used.

[0005] CN107012178 discloses catalyzing 2-ketobutyric acid with the aid of alanine dehydrogenase and formate dehydrogenase to produce L-2-aminobutyric acid.

[0006] EP0983372 discloses a method for making L-2-aminobutyric acid, comprising the steps of a) reacting L-threonine with threonine deaminase under conditions suitable for producing 2-ketobutyric acid, b) reacting 2-ketobutyric acid, L-aspartic acid, and a transaminase enzyme under conditions suitable for producing oxaloacetate and L-2-aminobutyric acid, c) forming oxaloacetate to pyruvate, d) reacting pyruvate with acetolactate synthase enzyme under conditions suitable for producing acetolactate, e) forming acetolactate to acetoin, and f) separately recovering acetoin and L-2-aminobutyric acid.

[0007] CN105331650 discloses a method for co-producing α-aminobutyric acid and dihydroxyacetone by recombinant Escherichia coli in which glycerol dehydrogenase and L-amino acid dehydrogenase react stepwise. The method is characterized by establishing a recombinant co-expression vector through glycerol dehydrogenase gene and L-amino acid dehydrogenase gene, and transforming it into genetically modified bacteria, Escherichia coli; meanwhile, reliably establishing a recombinant Escherichia coli expressing L-threonine deaminase; and efficiently co-expressing glycerol dehydrogenase and L-amino acid dehydrogenase in Escherichia coli can promote the circulation of cofactors, without the need to add any exogenous cofactors, and using a cofactor circulation regeneration system, it can co-produce high-value-added α-aminobutyric acid and dihydroxyacetone through inexpensive substrates, i.e., L-threonine deaminase and glycerin. The yield of α-aminobutyric acid in a 5L fermentation tank reached 41.2g / L.

[0008] Note: This patent proposes utilizing glycerol dehydrogenase to recycle the cofactor NADH. If another substrate for glycerol dehydrogenase must be added to recycle the cofactor, the method becomes less cost-effective.

[0009] CN102517351, CN102212567B, and CN109679978 disclose methods for producing L-2-aminobutyric acid from threonine. [Prior art documents] [Patent documents]

[0010] [Patent Document 1] EP2539444 [Patent Document 2] CN109777788 [Patent Document 3] CN107012178 [Patent Document 4] EP0983372 [Patent Document 5] CN105331650 [Patent Document 6] CN102517351 [Patent Document 7] CN102212567B [Patent Document 8] CN109679978 Summary of the Invention [Problem to be solved by the invention]

[0011] The present invention solves the problems faced in the prior art by producing L-2-ABA through a cell-free system and biotransformation process using cheaper substrates by using enzyme or recombinant cell-based production methods. The production of valuable and important pharmaceutical intermediate L-2-ABA from cheaper substrates brings great economic value.

[0012] L-2-ABA has been produced using enzymatic conversion of substrates, but the methods are inefficient and use starting materials that are expensive and not easily available in large quantities.

[0013] Therefore, there remains a need for efficient and less costly methods for producing high yields of L-2-ABA.

[0014] Thus, the inventors provide a feasible technology using cell-free and whole-cell biotransformation that utilizes cheaper substrates for the production of L-2-ABA via a highly efficient enzyme-catalyzed redox balanced pathway.

[0015] It is an object of the present invention to provide an efficient and cost-effective method for producing high yields of L-2-ABA.

[0016] Another object of the present invention is to provide a method for producing L-2-ABA using cheaper substrates such as citramalic acid or citraconic acid.

[0017] It is a further object of the present invention to provide a method for producing L-2-ABA using cheaper substrates such as citramalate or citraconic acid by enzymatic biotransformation in a cell-free system.

[0018] Yet another object of the present invention is to provide a method for producing L-2-ABA using an efficient enzyme.

[0019] Yet another object of the present invention is to prepare the important pharmaceutical intermediate L-2-ABA by biotransformation using genetically modified strains.

[0020] Yet another object of the present invention is to provide a method for producing L-2-ABA that is easily scalable to large scale production and industrial manufacturing. [Means for solving the problem]

[0021] In one aspect, the present invention provides a method for producing high yields of L-2-ABA by enzymatic biotransformation from a substrate selected from citramalic acid or citraconic acid in a cell-free system.

[0022] In another embodiment, the present invention provides methods that use the enzymes isopropylmalate isomerase, isopropylmalate dehydrogenase, amino acid dehydrogenase / transaminase B.

[0023] In a further aspect, the present invention provides a method for producing high yields of L-2-ABA using a cell-free system, comprising the steps of: a) transforming a microbial host cell to incorporate leu B, leu CD, and valDH to express the enzymes LeuCD, LeuB, and ValDH; b) harvesting and lysing the host cells to obtain a crude lysate; c) optionally isolating, purifying and / or immobilizing the enzyme from the crude lysate; d) converting a substrate selected from citramalic acid or citraconic acid using a crude lysate or purified enzyme or an immobilized enzyme at a pH between 7 and 9; The present invention provides a method comprising:

[0024] In another aspect, the present invention provides a method for producing high yields of L-2-ABA by a cell-free system, comprising: a) transforming a microbial host cell to incorporate leu B, leu CD, and ilvE for expression of the enzymes LeuCD, LeuB, and IlvE; b) harvesting and lysing the host cells to obtain a crude lysate; c) optionally isolating, purifying and / or immobilizing the enzyme from the crude lysate; d) converting a substrate selected from citramalic acid or citraconic acid using a crude lysate or purified enzyme or an immobilized enzyme at a pH between 7 and 9; The present invention provides a method comprising:

[0025] In yet another aspect, the present invention provides a method for producing high yields of L-2-ABA from a substrate selected from citramalic acid, citraconic acid, or 2-oxobutyric acid by whole cell biotransformation in a suitable host.

[0026] In yet another aspect, the present invention provides a method for producing high yields of L-2-ABA from a substrate selected from citramalic acid, citraconic acid, or 2-oxobutyric acid by whole cell biotransformation in a suitable host, which is a permeabilized cell.

[0027] In yet another aspect, the present invention provides a method for producing L-2-ABA comprising biotransformation in whole cells or permeabilized cells, comprising: a) transforming a microbial host to incorporate valDH or ilvE; b) optionally incorporating leu B or leu CD; b) adding a substrate selected from citramalic acid or citraconic acid or 2-oxobutyric acid; and c) culturing the host at a temperature between 20°C and 37°C in a suitable medium to express the enzyme in order to obtain L-2-ABA; The present invention provides a method comprising the steps of:

[0028] In yet another aspect, the present invention provides a method for producing high yields of L-2-ABA in whole cells or permeabilized cells by enzymatic biotransformation in a suitable host from a substrate selected from citramalate, citraconic acid, or 2-oxobutyric acid, which may include knocking out ilvD and ilvIH.

[0029] In yet another aspect, the present invention provides a method for producing high yields of L-2-ABA in whole cells or permeabilized cells by enzymatic biotransformation in a suitable host from a substrate selected from citramalate, citraconic acid, or 2-oxobutyric acid, which may include knocking out ackA, tdcD, and pta.

[0030] For a more complete understanding of the present invention, reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which: [Brief description of the drawings]

[0031] [Figure 1] FIG. 1 shows an exemplary embodiment of the preparation of L-2-aminobutyric acid via an alternative isoleucine biosynthetic pathway (b) compared to the preparation from threonine (a). [Diagram 2] FIG. 1 shows an exemplary embodiment of a cell-free enzymatic biotransformation for the preparation of L-2-aminobutyric acid. [Diagram 3] FIG. 1 shows an exemplary embodiment of whole cell enzymatic biotransformation for the preparation of L-2-aminobutyric acid. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0032] It will be understood that the present disclosure is not limited to the particular systems and methodologies described, as there may be many possible embodiments of the present disclosure that are not explicitly exemplified in this disclosure. It should also be understood that the terminology used in the description is for the purpose of describing particular variations or embodiments only, and is not intended to limit the scope of the present disclosure.

[0033] The present invention relates to the construction of an enzymatic pathway that performs a series of reactions to convert cheaper substrates such as citraconic acid or citramalic acid into a more valuable product (L-2-ABA), which is believed to add value to the process.

[0034] In the present invention, the method for producing L-2-ABA from substrates such as citraconic acid or citramalic acid comprises isolating the genes, i.e., leu B, leu CD, valDH, or ilvE, from various sources and transforming suitable host cells with said genes to express the corresponding enzymes. Hosts for biotransformation can include those of bacterial and eukaryotic origin, such as Escherichia coli, Lactobacillus, and Clostridium sp., as well as various yeasts.

[0035] In the present invention, the multi-step synthetic pathway for producing L-2-ABA is the alternative isoleucine pathway, in which citramalate (2-methylmalate) is formed from the condensation of pyruvate with acetyl-CoA by the enzyme citramalate synthase (CimA). Citramalate is converted to citraconic acid (2-methylmaleate) by isopropylmalate isomerase (Leu CD complex) and then to D-erythro 3-methylmalate, which is converted to NAD by isopropylmalate isomerase (Leu CD complex). +It is further oxidized to 2-OB (2-oxobutyrate) by isopropylmalate dehydrogenase (Leu B), which requires 2-OB and releases CO2. The enzymes involved in leucine biosynthesis, Leu CD and Leu B, can catalyze the formation of 2-OB from citramalate. 2-OB is the immediate precursor of L-2-ABA. Since L-2-ABA is an unnatural amino acid, natural enzymes are not available for efficient conversion. However, amino acid dehydrogenases and branched-chain aminotransferases, which catalyze substrates with similar structures, can convert 2-OB (a keto acid substrate) to each amino acid and L-2ABA, respectively.

[0036] For the conversion of 2-OB to L-2ABA, valine dehydrogenase (ValDH) from Streptomyces sp. and branched-chain aminotransferase (IlvE) from E. coli and Clostridium sp. were selected.

[0037] The pathway from citramalate or citraconic acid to L-2-ABA is thermodynamically favorable. The reaction catalyzed by Leu B is + to NADH, releasing CO2 。 The final reaction catalyzed by valine dehydrogenase is ammonia and NAD + The reductive amination of 2-OB to L-2-ABA requires the reductant NADH to regenerate 2-ABA. Thus, the redox is balanced in the last two steps, as the cofactor can be recycled, and the continuous removal of released CO2 drives the multi-step synthesis pathway for higher yields, facilitating synthesis in both cell-free and biotransformation systems.

[0038] The inventors have surprisingly found that the construction of a synthetic pathway containing the genes leu CD, leu B, valDH / ilvE allows the conversion of substrates to L-2-ABA, and that this pathway is 10 5 s -1 M -1 k in the range cat / k mIt has been shown that the method is very efficient with

[0039] In one embodiment, the present invention relates to a method for the preparation of L-2-ABA in a cell-free system utilizing isopropylmalate dehydrogenase (LeuB), isopropylmalate isomerase (Leu CD complex), valine dehydrogenase (ValDH), which may also utilize branched-chain aminotransferase (IlvE) instead of valine dehydrogenase (ValDH). The enzymes are either in crude or immobilized form, including the necessary cofactors and other components to effect the desired transformation.

[0040] The host cells were transformed with the recombinant plasmids carrying the genes, namely pColaDuet-1LeuCD, pETDuet-1LeuB and pETDuet-1ValDH, respectively. The cells were cultivated in a natural medium and the enzyme expression was induced by IPTG (isopropyl-β-D-thiogalactoside). The cultivation conditions were provided to obtain maximum soluble expression of the enzyme. The cells were harvested and lysed to release the enzyme. Either the crude lysate or the purified enzyme was used for the transformation method. The cultivation, harvesting, lysis and enzyme isolation techniques are known to those skilled in the art. In the above embodiment, the method for producing L-2-ABA comprises: a) transforming a microbial host cell to incorporate leuB, leuCD, valDH, and ilvE for expressing the enzymes LeuCD, LeuB, and ValDH; b) harvesting and lysing the host cells to obtain a crude lysate; c) optionally isolating and purifying the enzyme from the crude lysate; d) converting a substrate selected from citramalic acid or citraconic acid using the crude lysate or the purified enzyme at a pH between 7 and 9; Includes.

[0041] The method can also utilize branched-chain aminotransferase (IlvE) instead of valine dehydrogenase (ValDH). The enzyme is overproduced in a recombinant expression host under conditions that result in maximum specific activity.

[0042] For conversion of substrates using conventional techniques and techniques, immobilized enzymes can also be used instead of purified enzymes.

[0043] The conversion of the substrate is carried out in a system that contains all the cofactors and components required for efficient conversion. Such cofactors and components include MnCl2, KCl, NAD + , ammonium salts, and buffer solutions.

[0044] Methods using crude, purified, or immobilized enzymes produce at least 80 g / L or at least 100 g / L in 12-18 hours.

[0045] Isopropylmalate isomerase has been obtained from Methanocaldococcus jannaschii, Escherichia coli, and Neurospora crassa. Isopropylmalate dehydrogenase has been sought from Methanocaldococcus jannaschii, Thermophilus sp., Escherichia coli, Acidothiobacillus ferroxidans, Sulfolobus sp., and Bacillus subtilis. The amino acid dehydrogenase may be a valine dehydrogenase identified from Streptomyces sp., Alcaligenes faecalis, Kitasatospora aureofaciens, or a leucine dehydrogenase identified from Bacillus sp.

[0046] In another embodiment, L-2-ABA can be produced by whole cell biotransformation from citramalate or citraconic acid by cells carrying genes expressing the three enzymes of the pathway, namely LeuCD, LeuB, and ValDH. The host cell used here is E. coli. The genes were introduced into the host cell as either pCOlaDuet-1 BCD ValDH or pETDuet-1 CD, pCOlaDuet-1 LeuB ValDH. Citramalate or citraconic acid is added to recombinant cells grown in a suitable medium containing cofactors and components. The medium may contain glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and also a source of ammonia in the form of ammonium salts. For soluble expression of the enzymes, osmoprotectants such as sorbitol or glycerol may be added to the medium. Antibiotics appropriate for the particular plasmid and strain were added. Fresh medium was replaced except for MgSO4 during expression and conversion of substrate. Optionally, cells were permeabilized to improve substrate uptake. Conversion was performed at 20°C to 37°C and quantified by HPLC.

[0047] In another embodiment, the method for producing L-2-ABA comprises biotransformation in whole cells or permeabilized cells. a) transforming a microbial host to incorporate valDH or ilvE; b) optionally incorporating leu B or leu CD; b) adding a substrate selected from citramalic acid, citraconic acid, or 2-oxobutyric acid; and c) culturing the host at a temperature between 20°C and 37°C in a suitable medium to express the enzyme in order to obtain L-2-ABA; Includes.

[0048] Hosts for biotransformation can include those of bacterial and eukaryotic origin, such as E. coli, Lactobacillus, and Clostridium species, as well as various yeasts.

[0049] The host may be transformed to express all three enzymes, i.e., LeuCD, LeuB, and ValDH. In another embodiment, ilve may be integrated in place of valDH to express Ilve.

[0050] In some embodiments, the host cell may contain LeuCD or LeuB as the native enzyme. In such embodiments, the substrate may be 2-oxobutyrate or citramalate or citraconic acid.

[0051] Isopropylmalate isomerase is obtained from Methanocaldococcus jannaschii, Escherichia coli, and Neurospora crassa. Isopropylmalate dehydrogenase is discovered from Methanocaldococcus jannaschii, Thermophilus sp., Escherichia coli, Acidithiobacillus ferrooxidans, Sulfolobus sp., and Bacillus subtilis. The amino acid dehydrogenase may be valine dehydrogenase discovered from Streptomyces sp., Algaigenes faecalis, and Kitasatospora aureofaciens, or leucine dehydrogenase discovered from Bacillus sp.

[0052] The present inventors have also found that blocking the pathway leading to the by-product isoleucine should be blocking to make 2-OB available for L-2-ABA formation, thus promoting the production of higher yields of L-2-ABA. Therefore, it is desirable to use a host with a non-functional isoleucine pathway in which ilvD or ilvIH is knocked out. Alternatively, it may be desirable to use inhibitors against the AHAS complex, such as valine, sulfometuron methyl, imidazolinone, triazolopyrimidines, pyrimidinyloxobenzoates, and sulfonylaminocarbonyltriazolinones.

[0053] Additionally, to improve the availability of 2-OB for L-2-ABA formation, the pathways leading to propionyl-CoA and propionate may be blocked. Thus, it is desirable to use a host with non-functional propionyl-CoA and propionate pathways in which acetate kinase (ackA), propionate kinase (tdcD), and phosphate acetyltransferase (pta) are knocked out.

[0054] Methods for producing L-2-ABA in whole cells or permeabilized cells can result in production of 20 g / L, or at least 40 g / L in 15-20 hours.

[0055] Next, a complete method for producing L-2-ABA from citraconic acid by constructing a synthetic pathway including genes involved in amino acid biosynthesis from various sources, namely LeuB, Leu CD, ValDH, will be described step by step in the light of the accompanying experiments shown to facilitate a comprehensive understanding of the exemplary embodiment of the present invention. Although various specific details of the method are included to facilitate understanding, they should be considered as merely illustrative. It is believed that one skilled in the art can utilize the above description to the widest extent. Therefore, the preferred embodiments and examples should also be considered as merely illustrative and in no way limiting the disclosure.

[0056] The present inventors obtained pETDuet-1 and pCOLADuet-1 vectors from Novogen Inc. The E. coli strain BL21DE3 Codon plus RP was obtained from IIT Madras University upon request.

[0057] A. Cell-free enzymatic biotransformation experiments I. Conversion of Citraconic Acid to L-2-ABA Experiment 1 Enzymatic cell-free conversion experiments were set up to convert 10 mM to 2 M citraconic acid to 10 mM to 2 M L-2-ABA catalyzed by the enzymes LeuCD, LeuB, and ValDH used as crude cell lysates or partially or completely purified.

[0058] E. coli was transformed with the recombinant plasmids carrying the genes, namely: pColaDuet-1LeuCD, pETDuet-1LeuB, and pETDuet-1ValDH, respectively. These cells were cultivated in natural medium and enzyme expression was induced by IPTG (isopropyl-β-D-thiogalactoside). Culture conditions were provided to obtain maximum soluble expression of the enzyme. The cells were harvested and lysed to release the enzyme. Either crude lysate or purified enzyme was used for the transformation process.

[0059] The conversion of citraconic acid to L-2-ABA is carried out in the pH range of 7 to 9. The crude lysate or purified enzyme is added to the conversion reaction in the presence of other components required for the conversion. Citraconic acid is converted to D-erythro-3-methylmalate by LeuCD, which is then converted to 2-OB by LeuB. The conversion by the enzyme LeuB requires 1 to 50 mM MnCl2 and 10 to 300 mM KCl. In the last two steps, the reaction is in redox equilibrium, so NAD + Only 100 μM–15 mM of 2-OB is required. In the final step, catalyzed by ValDH, 2-OB is converted to L-2-ABA by reductive amination, providing 10 mM–2 M ammonium salt to the reactants. The NADH required in this step is obtained from the previous step, and NAD + Conversions were carried out in bioreactors of any volume, ranging from 10 ml to 5 L scale, at temperatures ranging from 25°C to 37°C.

[0060] Test 2: Enzymatic cell-free conversion experiments were set up to convert 10 mM to 2 M citraconic acid to 10 mM to 2 M L-2-ABA catalyzed by the enzymes LeuCD, LeuB, and IlvE used as crude cell lysates or partially or completely purified.

[0061] The recombinant plasmids carrying the genes, namely: pColaDuet-1LeuCD, pETDuet-1LeuB, and pETDuet-1IlvE, respectively, were transformed into E. coli or yeast. The cells were grown in natural medium and enzyme expression was induced by IPTG. Culture conditions were provided to obtain maximum soluble expression of the enzyme. The cells were harvested and lysed to release the enzyme. Either crude lysates or purified enzymes were used for the transformation process.

[0062] The conversion of citraconic acid to L-2-ABA is carried out in the pH range of 7 to 9. The crude lysate or purified enzyme is added to the conversion reaction in the presence of other components required for the conversion. Citraconic acid is converted to D-erythro-3-methylmalate by LeuCD, which is converted to 2-OB by LeuB. The conversion by the enzyme LeuB requires 1-50 mM MnCl2, 10 mM-300 mM KCl, and NAD. + In the final step, catalyzed by ilvE, 2-OB is converted to L-2-ABA by transamination, with the reaction supplying 10 μM to 2 mM pyridoxal PO4 and 10 mM to 2 M glutamate.

[0063] Conversions were carried out in bioreactors of any volume, scale from 10 ml to 5 L, at temperatures between 25°C and 37°C.

[0064] B. Whole-cell biotransformation experiments using recombinant cells Experiment 3: Citraconic acid biotransformation by cells containing overexpressed LeuB, LeuCD, and ValDH L-2-ABA can be produced by whole cell biotransformation from citramalate or citraconic acid by cells carrying genes expressing the three enzymes of the pathway, namely LeuCD, LeuB, and ValDH. The host cell used here is E. coli. The genes were introduced into the host cells as either pCOlaDuet-1 BCD valDH or pETDuet-1 CD, pCOlaDuet-1 LeuB valDH. Either citramalate or citraconic acid in amounts of 1 g to 100 g / L is added to recombinant cells grown in synthetic medium containing 5 to 50 g / L glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and also a source of ammonia in the form of ammonium salts. Osmoprotectants such as sorbitol or glycerol may be added to the medium for soluble expression of the enzymes. Antibiotics appropriate for the particular plasmid and strain were added. Fresh medium was replaced except for MgSO4 during expression and conversion of the substrate. Alternatively, cells were permeabilized to improve substrate uptake. Conversion was carried out at 20°C to 37°C and quantified by HPLC.

[0065] Experiment 4: Citraconic acid biotransformation by cells containing overexpressed LeuB, LeuCD, and IlvE L-2-ABA can be produced by whole cell biotransformation from citramalate or citraconic acid by cells carrying genes expressing the three enzymes of the pathway, namely LeuCD, LeuB, and ilvE. The host cell used here is E. coli. The genes were introduced into the host cells as either pCOlaDuet-1 BCD IlvE or pETDuet-1 CD, pCOlaDuet-1 LeuBIlvE. Amounts of 1 g to 100 g / L of either citramalate or citraconic acid are added to recombinant cells grown in synthetic medium containing 5 to 50 g / L of glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and glutamic acid. Osmoprotectants such as sorbitol or glycerol may be added to the medium for soluble expression of the enzymes. Antibiotics appropriate for the particular plasmid and strain were added. Alternatively, cells are permeabilized using reagents such as toluene, Tween, chelators, etc., using routine techniques to improve substrate uptake. Conversion was performed at 20°C to 37°C and quantified by HPLC. When host cells were fed with 2.7 g / L citraconic acid, the host's native enzymes, i.e., LeuCD, LeuB, and IlvE, converted the substrate to L-2-ABA (Table 2).

[0066] Experiment 5: Citraconic acid biotransformation by cells containing overexpressed ValDH (native LeuB and LeuCD) L-2-ABA can be produced from citramalate or citraconic acid by whole cell biotransformation by cells carrying the gene valDH. Conversion of the substrate to 2-OB is carried out in the host cell by the native enzymes LeuCD, LeuB. The host cell used here is E. coli. The genes were introduced into the host cell as either pCOlaDuet-1 valDH or pETDuet-1valDH. Either citramalate or citraconic acid in amounts of 1 g to 100 g / L is added to recombinant cells grown in natural medium such as glucose yeast extract or synthetic medium which may contain 5 to 50 g / L glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and also a source of ammonia in the form of ammonium salts. Osmoprotectants such as sorbitol or glycerol may be added to the medium for soluble expression of the enzyme. Fresh medium was replaced during expression and conversion of the substrate, except for MgSO4. Antibiotics were added appropriate for the particular plasmid and strain. Alternatively, cells were permeabilized to improve substrate uptake. Conversion was carried out at 20°C to 37°C and quantified by HPLC.

[0067] Experiment 6: Citraconic acid biotransformation by cells containing native / overexpressed IlvE (native LeuB and LeuCD) L-2-ABA can be produced by whole-cell biotransformation of citraconic acid or citramalic acid by host cells containing native LeuCD, LeuB, and IlvE (Table 2).

[0068] L-2-ABA can also be produced from citramalate or citraconic acid by whole cell biotransformation by cells carrying overexpressed IlvE. Conversion of the substrate to 2-OB is carried out by the native enzymes LeuCD, LeuB present in the host. The host cell used here is E. coli. The genes were introduced into the host cell as either pCOlaDuet-1 ilvE or pETDuet-1 ilvE. Either citramalate or citraconic acid in amounts of 1 g to 100 g / L is added to recombinant cells grown in natural medium such as glucose yeast extract or synthetic medium containing 5 to 50 g / L glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and also glutamic acid. Osmoprotectants such as sorbitol or glycerol may be added to the medium for soluble expression of the enzymes. Antibiotics appropriate for the particular plasmid and strain were added. Alternatively, cells were permeabilized to improve substrate uptake. Conversion was carried out at 20°C to 37°C and quantified by HPLC.

[0069] Experiment 7: 2-oxobutyrate biotransformation by cells containing overexpressed ValDH (native LeuB and LeuCD) L-2-ABA can be produced by whole cell biotransformation from 2-oxobutyric acid by cells carrying the gene valDH. The host cell used here is E. coli. The gene was introduced into the host cell as either pCOlaDuet-1 valDH or pETDuet-1valDH. 2-oxobutyric acid in amounts of 1 g to 100 g / L is added to recombinant cells grown in natural medium such as glucose yeast extract or synthetic medium that may contain 5 to 50 g / L glucose, KH2PO4, (NH4)2HPO4, Na2EDTA, MgSO4, thiamine HCl, trace metals, and also a source of ammonia in the form of ammonium salts. Osmoprotectants such as sorbitol or glycerol may be added to the medium for soluble expression of the enzyme. Fresh medium was replaced during expression and conversion of the substrate, except for MgSO4. Antibiotics appropriate for the particular plasmid and strain were added. Alternatively, cells were permeabilized to improve uptake of the substrate. The conversion was carried out at 20°C to 37°C and quantified by HPLC (Table 2).

[0070] [Table 1]

[0071] Results and Discussion: Table 1 shows the production of 2-ABA from citraconic acid in a cell-free system catalyzed by the enzymes LeuCD, LeuB, and ValDH. At 250 mM citraconic acid, 99.6% conversion was obtained, whereas at 100 mM and 50 mM citraconic acid, 96% and 86% were obtained, respectively.

[0072] [Table 2]

[0073] Table 2 shows the production of 2-ABA from citraconic acid in whole cell biotransformation catalyzed by native enzymes of the host cell, i.e., LeuCD, LeuB, and IlvE. At 24 h, a product titer of 100 mg / L was obtained from 2.1 g / L of citraconic acid consumed. The remaining citraconic acid consumed was diverted to the production of isoleucine and propionate. This can be reduced by carrying out the same experiment with the proposed knockout strain (knocking out isoleucine and propionate production pathway enzymes).

[0074] Table 2 shows the production of 2-ABA from 2-oxobutyrate in whole cell biotransformation catalyzed by native ilvE in the host and by overexpressed valine dehydrogenase in the clone. At 24 hours, product titers of 0.25 g / L and 6 g / L were obtained from 10 g / L of 2-oxobutyrate in the host and clone, respectively. The remaining 2-oxobutyrate consumed was diverted to the production of isoleucine and propionate. This could be reduced by carrying out the same experiment with the proposed knockout strain (knocking out isoleucine and propionate production pathway enzymes).

[0075] Advantages of the invention: The present invention provides an alternative method for producing L-2-ABA in high yield. The method is economical since it utilizes cheaper substrates such as citramalic acid or citraconic acid. The price of citramalic acid or citraconic acid is about US$0.5-US$15 per kg. In contrast, currently available methods use expensive substrates such as food and pharmaceutical grade. Moreover, food grade threonine makes the purification process difficult.

[0076] Furthermore, as disclosed above, the present method engineered a pathway for the preparation of L-2-ABA that is redox balanced, whereas the process from threonine is not redox balanced and therefore requires an additional enzyme to recycle the cofactor NADH.

[0077] The enzymes utilized in the preparation of L-2-ABA from citraconic acid are 5 s -1 M -1 k in the range cat / k m and is highly efficient compared to the enzyme utilized in the threonine process. Because this enzyme is efficient, the scale of enzyme production can be reduced, thus reducing the cost of production. Thus, the preparation of L-2-ABA from citraconic or citramalic acid is highly feasible on an industrial scale.

Claims

1. A method for producing L-2-aminobutyric acid in a cell-free system by enzymatic biotransformation of a substrate selected from citramalate or citraconic acid, wherein the enzymes are isopropylmalate isomerase, isopropylmalate dehydrogenase, and valine dehydrogenase.

2. 2. The method of claim 1, wherein the enzyme is in crude or purified form or in immobilized form.

3. A method for producing L-2-aminobutyric acid by enzymatic biotransformation according to claim 1 or 2, comprising: a) transforming a microbial host cell to incorporate leu B, leu CD, and valDH to express the enzymes LeuCD, LeuB, and ValDH; b) harvesting and lysing the host cells to obtain a crude lysate; c) optionally isolating, purifying and / or immobilizing the enzyme from the crude lysate; d) converting a substrate selected from citramalic acid or citraconic acid using a crude lysate or purified enzyme or an immobilized enzyme at a pH between 7 and 9; The method includes:

4. MnCl 2 , KCl, NAD + The method of claim 1 or 3, further comprising cofactors such as ammonium salts and buffers.

5. 5. The method according to any one of claims 1 to 4, wherein the L-2-aminobutyric acid production is at least 80 g / L in 12 to 18 hours.

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