ENZYMATIC PROCESS FOR THE MANUFACTURE OF ASCORBIC ACID, 2-KETO-L-GULONIC ACID AND ESTERS OF 2-KETO-L-GULONIC ACID

Abstract: The present invention is directed toward efficient, high-yield processes for making ascorbic acid, 2-keto-L-gulonic acid, and esters of 2-keto-L-gulonic acid. The processes comprise reacting the appropriate starting materials with a hydrolase enzyme catalyst such as a protease, an esterase, a lipase or an amidase.

Description: ENZYMATIC PROCESS FOR THE MANUFACTURE OF ASCORBIC ACID, 2-KETO-L-GULONIC ACID AND ESTERS OF 2-KETO-L-GULONIC ACID FIELD OF THE INVENTION This invention relates to processes for the manufacture of ascorbic acid, 2-keto-L-gulonic acid {KLG) , and esters of KLG. More particularly, the present invention relates to the use of enzyme catalysts m the manufacture of ascorbic acid, KLG or esters of KLG. BACKGROUND OF THE INVENTION Ascorbic acid, also known as vitamin C, is a dietary factor which must be present in the human diet to prevent scurvy and which has been identified as an agent that increases resistance to infection. Ascorbic acid is used commercially, for example, as a nutrition supplement, color fixing agent, flavoring and preservative in meats and other foods, oxidant m bread doughs, abscission of citrus fruit in harvesting and reducing agent in analytical chemistry. One current method for the manufacture of ascorbic acid utilizes a modification of the original Reichstein-Grossner synthesis (Reichstein et al., Helv. Chim . Acta, 27:311 (1934) ; U.S. Pat. No. 2,301,811 to Reichstein; all references cited herein are specifically incorporated by reference) . In this process a glucose source is converted to ascorbic acid. During conversion an intermediate of a diacetonide of KLG is produced. Several two stage methods exist for the manufacture of ascorbic acid. In the first stage, glucose is converted via fermentation processes to either an isolated intermediate of KLG (Sonoyama et al . , Appli ed and Envtl . Mi crobi ology, 43:1064-1069 (1982) ; Anderson et al., Science, 230:144-149 (1985) ; Shmηoh et al., Applied and Envtl . Mi crobi ol ogy, 61:413-420 (1995) ) or the intermediate of the Reichstem- Grossner synthesis, the diacetonide of KLG. The second stage, which converts either of the intermediates to ascorbic acid, proceeds by one of two reported routes. The first route, a modification of the latter steps of the Reichstem-Grossner synthesis, requires a multitude of steps whereby the intermediate is esterified with methanol under strongly acidic conditions to produce methyl-2-keto-L-gulonate (MeKLG) . The MeKLG is then reacted with base to produce a metal ascorbate salt. Finally, the metal ascorbate salt is treated with an acidulant to obtain ascorbic acid. The second route is a one-step method comprising acid-catalyzed cyclization of KLG, as originally disclosed m GB Patent No. 466548 to Reichstein) and later modified by Yamazaki (Yamazaki, J. Agri . Chem . Soc . Japan, 28:890-894 (1954), and Chem. Abs . , 50:5992d) and again by Yodice (WO 87/00839) . The Yodice method is commercially undesirable because it uses large amounts of gaseous hydrogen chloride, requires very expensive process equipment and produces an ascorbic acid product requiring extensive purification. Lipases, a group of hydrolase enzymes, have been used with some success in the synthesis of esters of organic acids. In particular, lipases have been utilized m the transesterification of alcohols in which the esterifymg agent is irreversible, such as when vinyl acetate is used as the esterifymg agent (Thiel, Catalysis Today, 517-536 (1994) ) . Gutman et. al., Tetrahedron Let t . , 28:3861-3864 (1987), describes a process for preparing simple 5-membered ring lactones from gamma-hydroxy methyl esters using porcine pancreatic lipase as the catalyst. However, Gutman et al . , Tetrahedron Lett . , 28:5367-5368 (1987), later reported that substituting delta-hydroxy methyl esters for gamma-hydroxy methyl esters and using the same catalyst produced only polymers. In EP 0 515 694 Al to Sakashita et. al., a synthesis of esters of ascorbic acid, which are acylated on the primary hydroxyl group, comprises reacting ascorbic acid with a variety of fatty acid active esters (i.e., fatty acid vinyl esters) in a polar organic solvent in the presence of a lipase. Thus, there exists a need in the art for methods of producing (a) ascorbic acid or metal salts thereof from KLG or esters of KLG, (b) KLG from esters of KLG and (c) esters of KLG from KLG, which have high yield and high purity with little or no by-product formation and are conducted under mild conditions. Accordingly, it is to the provision of such that the present invention is primarily directed. SUMMARY OF THE INVENTION The present invention discloses an advancement in the chemical and biological arts in which a process for preparing ascorbic acid comprises contacting KLG or an ester of KLG with a hydrolase enzyme catalyst. In another embodiment of the present invention, a process for producing KLG comprises contacting an ester of KLG in an aqueous solution with a hydrolase enzyme catalyst. In still another embodiment of the present invention, a process for producing esters of KLG from KLG comprises contacting an alcoholic solution of KLG with a hydrolase enzyme catalyst. The alcoholic solution contains an alcohol corresponding to an alkyl moiety of the ester of KLG to be prepared. In still another embodiment of the present invention, a process for producing esters of KLG from esters of KLG comprises contacting an alcoholic solution of a first ester of KLG with a hydrolase enzyme catalyst. The alcoholic solution contains an alcohol corresponding to an alkyl moiety of a second ester of KLG which is to be prepared. DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to the unexpected discovery that ascorbic acid can be formed from KLG or, more preferably, esters of KLG by inducing ring closure of KLG or esters of KLG using a hydrolase enzyme as a catalyst. The process for producing the ascorbic acid may be performed in the melt or in solution. The process may also be performed m vivo or m vi tro . For m vi vo processes, the hydrolase enzyme catalyst may be naturally occurring within a host cell or may be introduced into a host cell or organism by recombinant DNA methods. The present invention is also directed to the unexpected discovery that KLG can be prepared in a reversible reaction by reacting an ester of KLG in an aqueous solution using a hydrolase enzyme as a catalyst. Moreover, the present invention is directed to the unexpected discovery that an ester of KLG can be prepared by reacting KLG or another ester of KLG in an alcoholic solution using a hydrolase enzyme as a catalyst. The alcohol used to prepare the solution corresponds to the alkyl moiety of the ester of KLG being prepared. The hydrolase enzymes for use as catalysts in the processes of the present invention may be derived from or isolated from any appropriate source organisms. Examples of which include, but are not limited to, plants, microorganisms, and animals, such as yeast, bacteria, mold, fungus, birds, reptiles, fish, and mammals. Hydrolase enzymes for the purposes of this invention are defined generally by the enzyme class E.C.3.-.-.-, as defined in Enzyme Nomencla ture (Academic Press, 1992), and are commercially available. Preferred hydrolase enzymes are those capable of effecting hydrolysis of molecules containing carbonyl or phosphate groups. More specifically, the preferred hydrolases are capable of effecting hydrolysis at a carbonyl carbon bearing a heteroatom single bond. Examples of such carbonyl carbons bearing a heteroatom single bond include, but are not limited to, esters, thioesters, amides, acids, acid halides, and the like. The preferred hydrolases include the enzyme class E.C.3.1.-.-, which includes hydrolases acting on ester bonds, such as esterases and lipases; the enzyme class E.C.3.2-.-, which includes glycosidases; the enzyme class E.C.3.4-.-, which includes peptide hydrolases, such as proteases; and the enzyme class E.C.3.5.-.-, which includes amidases acting on bonds other than peptide bonds. Most preferred hydrolases include proteases, amidases, lipases, and esterases. More preferred hydrolases contain an active site serine residue which is capable of undergoing esterification or transesterification with KLG or esters of KLG. Even more preferred are those hydrolases which contain the catalytic triad of serine, histidine and apartic acid. Preferred proteases include those derived from bacteria of the genera Bacill us or Aspergill us . Particularly preferred proteases are those obtained from the bacteria Bacill us li cheniformi s . Preferred proteases are those containing at least 70% sequence homology with Subtili sin . Proteases having sequence homology with Subtilisin are used in the detergent industry and, therefore, are readily available. More preferred are proteases having at least 80% sequence homology with Sujbtiiisin, even more preferred are proteases having at least 90% sequence homology with Subtili sin and, in particular, proteases having at least 95% sequence homology to Subtilisin . A highly preferred protease is Subtili sin itself having an amino acid sequence (SEQ ID NO: 1) described by Smith et al. , J. Bi ol . Chem . , 243: 2184- 2191 (1968), and given below: MMRKKSFWLG MLTAFMLVFT MAFSDSASAA QPAKNVEKDY IVGFKSGVKT ASVKKDIIKE SGGKVDKQFR IINAAKAKLD KEALKEVKND PDVAYVEEDH VAHALAQTVP YGIPLIKADK VQAQGFKGAN VKVAVLDTGI QASHPDLNW GGASFVAGEA YNTDGNGHGT HVAGTVAALD NTTGVLGVAP SVSLYAVKVL NSSGSGTYSG IVSGIEWATT NGMDVINMSL GGPSGSTAMK QAVDNAYARG WWAAAGNS GSSGNTNTIG YPAKYDSVIA VGAVDSNSNR ASFSSVGAEL EVMAPGAGVY STYPTSTYAT LNGTSMASPH VAGAAALILS KHPNLSASQV RNRLSSTATY LGSSFYYGKG LINVEAAAQ. For the convenience of the reader, Table 1 provides a summary of amino acid shorthand used above and in the remainder of the specification. Table 1 Amino Acid Three-Letter One-Letter Symbol Abbreviation Alanine Ala A Arginine Arg R Asparagine Asn N Aspartic Acid Asp D Cysteine Cys C Glutamine Gin Q Glutamic Acid Glu E Glycine Gly G Histidine His H Isoleucine He I Leucine Leu L Lysine Lys K Methionine Met M Phenylalanine Phe F Proline Pro P Serine Ser S Threonine Thr T Tryptophan Trp W Tyrosine Tyr Y Valine Val V Also encompassed by the scope of the present invention are proteases corresponding to one to six site-specific mutants, sequence additions, and sequence deletions of the sequence given above. Even more preferred are proteases corresponding to zero to two site-specific mutants of the Subtili sin sequence given above. Esterases suitable for the present invention include those obtained from pig liver extract. Preferred esterases are those having at least 70% sequence homology with pig liver esterase having an amino acid sequence (SEQ ID NO: 2 described in Matsushima et al . , FEBS Lett . , 293 : 31 (1991), and given below: MWLLPLVLTS LASSATWAGQ PASPPWDTA QGRVLGKYVS LEGLAFTQPV AVFLGVPFAK PPLGSLRFAP PQPAEPWSFV KNTTSYPPMC CQDPWEQMT SDLFTNFTGK ERLTLEFSED CLYLNIYTPA DLTKRGRLPV MVWIHGGGLV LGGAPMYDGV VLAAHENFTV VWAIQYRLG IWGFFSTGDE HSRGNWGHLD QVAALHWVQE NIANFGGDPG SVTIFGESFT AGGESVSVLV LSPLAKNLFH RAISESGVAL TVALVRKDMK AAAKQIAVLA GCKTTTSAVF TFVHCLRQKS EDELLDLTLK MKFLTLDFHG DQRESHPFLP TWDGVLLPK MPEEILAEKD FTFNTVPYIV GI KQEFGWL LPTMMGFPLS EGKLDQKTAT SLLWKSYPIA NIPEELTPVA TFTDKYLGGT DDPVKKKDLF LDLMGDWFG VPSVTVARQH RDAGAPTYMY EFQYRPSFSS DKFTKPKTVI GDHGDEIFSV FGFPLLKGDA PEEEVSLSKT VMKFWANFAR SGNPNGEGLP HWPFTMYDQE EGYLQIGVNT QAAKRLKGEE VAFWNDLLSK EAA KPPKIK HAEL. Esterases more preferably have at least 80% sequence homology with the sequence of the pig liver esterase given above, even more preferably at least 90% sequence homology, especially preferred at least 95% sequence homology. Highly preferred is the pig liver esterase having the sequence given above. Also encompassed by the scope of the present invention are esterases corresponding to one to six site-specific mutants, sequence additions, and sequence deletions of the sequence given above. Even more preferred are esterases corresponding to zero to two site-specific mutants of the pig liver esterase sequence given above. Preferred lipases include those isolated from pigs and other mammals, microorganisms, and plants. This includes, but is not limited to, lipases obtained from the genera Aspergill us , Mucor, Candida , Pseudomonas , Humi cola , Rhi zopus , Chromobacteri um, Alcaligenes, Geotri cum, and Pem cilli um . Preferred lipases also include extracellular lipases, such as cut ases. More preferred lipases have at least 70% sequence homology with Candida Antartica type B lipase, even more preferred have at least 80% sequence homology, still more preferred have at least 90% sequence homology, and even more preferred have at least 95% sequence homology. A highly preferred lipase is the Candi da Antarti ca type B lipase itself which has an ammo acid sequence (SEQ ID NO: 3) described by Uppenberg et al., Structure, 2:293, 453 (1994), and given below: MKLLSLTGVA GVLATCVAAT PLVKRLPSGS DPAFSQPKSV LDAGLTCQGA SPSSVSKPIL LVPGTGTTGP QSFDSNWIPL STQLGYTPCW ISPPPFMLND TQVNTEYMV AITALYAGSG NNKLPVLTWS QGGLVAQWGL TFFPSIRSKV DRLMAFAPDY KGTVLAGPLD ALAVSAPSVW QQTTGSALTT ALRNAGGLTQ IVPTTNLYSA TDEIVQPQVS NSPLDSSYLF NGKNVQAQAV CGPLFVIDHA GSLTSQFΞYV VGRSALRSTT GQARSADYGI TDCNPLPAND LTPEQKVAAA ALLAPAAAAI VAGPKQNCEP DLMPYARPFA VGKRTCSGIV TP. Also encompassed by the scope of the present invention are lipases corresponding to one to six site-specific mutants, sequence additions, and sequence deletions of the sequence given above. Even more preferred are lipases corresponding to zero to two site-specific mutants of the Candida Antarti ca type B sequence given above. Preferred amidases include those isolated from bacteria of the genus Peni cilli um . A more preferred amidase has at least 80% sequence homology with Penicillin acylase . A particularly preferred amidase is Peni cillin acylase, which is also referred to as Penicillin amidohydrol ase, E.C. 3.5.1.11 (Duggleby et al. , Na t ure, 373:264-268 (1995) ) . For hydrolases containing serine at their active site, the first step m the reaction of either KLG or esters of KLG is believed to involve formation of a KLG-enzyme ester via acylation by KLG of the active site serine. Intra-molecular ring closure is believed to yield ascorbic acid (or its salts), whereas alcoholysis yields an ester of KLG and hydrolysis yields KLG. The process of the present invention comprises contacting either KLG or an ester of KLG with a hydrolase enzyme to form ascorbic acid. Preferably, this reaction is performed in the presence of an organic solvent system, an aqueous solvent system or a mixture thereof. The organic solvent is preferably a Ci-Cβ alcohol. The aqueous solvent system or mixed aqueous and organic solvent systems are more preferable because ascorbic acid, KLG, and esters of KLG are generally more soluble m aqueous solvent systems. For the in vi tro production of ascorbic acid from esters of KLG, the mixed aqueous and organic solvent systems or organic solvent systems are preferable to minimize competing hydrolysis reactions which can produce KLG as a byproduct. Aqueous solvent systems are especially preferable when utilizing whole cell systems for the production of ascorbic acid n vi vo . In one aspect of the present invention, the ascorbic acid is produced from KLG or esters of KLG in in vi vo, whole cell, and whole organism production systems in the presence of the hydrolase enzyme catalyst. In one embodiment, the hydrolase enzyme is naturally produced by the host organism. In another embodiment, the hydrolase enzyme is produced by the host organism through recombinant DNA technology. For example, a gene sequence encoding a hydrolase enzyme is inserted in a host organism wherein the host organism may be a microorganism, plant, or animal which is capable of expressing the hydrolase enzyme. The host organism producing the hydrolase enzyme is cultured, i.e. provided with nutrients and a suitable environment for growth, in the presence of KLG or esters of KLG to produce the asccrbic acid. Preferably, the host organism is Pantoea ci trea, previously referred to as Erwinia herbi cola as disclosed in U.S. Patent No. 5,008,193 to Anderson et al. Also preferably, the host organism is one that produces KLG in addition to producing the hydrolase enzyme. Representative organisms are from the genera Pantoea or G uconoj acter, such as disclosed in Shinjoh et al . , Appli ed and Envtl . Mi crobi ol ogy, 61 : 413-420 (1995), and the genus Corynebacteri um as disclosed in Sonoyama et al., Appli ed and Envtl . Mi crobi ol ogy, 43:1064-1069 (1982) . As used herein, recombinant DNA technology includes in vi tro recombinant DNA techniques, synthetic techniques and in vi vo recombinant/ genetic recombination and is well known in the art. See, for example, the techniques described in Maniatis et al . , Mol ecular Cl oning A Labora tory Manual , Cold Spring Harbor Laboratory, N.Y. (1989); Ausubel et al., Current Protocol s in Mol ecular Bi ol ogy, Greene Publishing Assoc. and Wiley Interscience, N.Y. (1989); Anderson et al . , Sci ence, 230:144-149 (1985); and U.S. Patent No. 5,441,882 to Estell et. al. For preparations of KLG from esters of KLG, an aqueous solution of the ester of KLG is reacted with the hydrolase enzyme. A co-solvent may be used in the preparation of KLG and is preferably a C]-C 6 alcohol. For preparations of the esters of KLG from KLG or from other esters of KLG, the starting material is in an alcoholic solution wherein the alcohol corresponds to the alkyl moiety of the ester of KLG to be prepared. The alkyl moiety R of the alcohol ROH from which the preferred ester of KLG is derived may be chosen from branched or straight chain, saturated or unsaturated, alkyl, arylalkyls, aryls, and substituted aryls. Preferred R groups include Ci to C 6 straight or branched chain, saturated or unsaturated alkyls. Even more preferred esters of KLG that are derived for alkyl moieties include MeKLG, ethyl-KLG, n-propyl-KLG, iεopropyl- KLG, n-butyl-KLG, isobutyl-KLG, t-butyl-KLG, and n-pentyl- KLG. The most preferred esters of KLG produced are MeKLG due to its ease of manufacture and butyl-KLG due to the advantageous use of the butanol water azeotroph in water removal. A co-solvent may be used in the preparation of the esters of KLG and is preferably water, a Cι-C 6 alcohol or a mixture thereof. Preferred temperatures for conducting the reactions of the present invention are from 5°C to 120°C. Even more preferred temperatures are from 25°C to 100°C, and especially preferred temperatures are from 38°C to 80°C. The preferred pH for the process of the present invention is between 1.5 and 10, and a more preferred pH is between 3 and 10. For the preparation of ascorbic acid salts from esters of KLG, a particularly preferred pH range is between 6 and 10. For the preparation of ascorbic acid as the free acid, a preferred pH is that under the pKa of ascorbic acid and, more preferred, is that under 4.2. For the preparation of KLG from esters of KLG, a particularly preferred pH range is between 5 and 10 due to the generally enhanced rates of enzyme assisted hydrolysis in this pH range. Alternatively, a pH of between 1.5 and 2.5 is particularly desirable for the generation of KLG in protonated form. Finally, for the preparation of esters of KLG from KLG, a particularly preferred pH range is between 3 and 6. Each hydrolase has a temperature optimum, a pH optimum, and a pH and temperature range associated with activity. Thus, the appropriate pH and temperature range for a given hydrolase is that which allows for activity of the hydrolase and avoids conditions which are denaturing or inactivating to the hydrolase. For conditions which may be denaturing, such as high temperature or the use of denaturing solvents such as methanol or the like, a minimal amount of testing may be required to define those hydrolases which remain active under a given set of conditions. The following examples are offered by way of illustration and are not intended to limit the scope of the claimed invention. EXAMPLES Proton and carbon nuclear magnetic resonance (NMR) spectra were recorded on a Varian Gemini 300 NMR instrument operating at 300 MHZ proton mode and 75 MHZ in carbon mode. All NMR spectra were referenced to tetramethylsilane (TMS) at 0 parts per million (ppm) and peak frequencies were recorded ppm unless otherwise specified. HPLC (high- performance liquid chromatography) analysis was carried out using ultraviolet (UV) detection. Mass spectra (MS) were obtained using a Fisons VG Analytical Ltd. Autospec Mass Spectrometer in FD (field desorption) mode. The KLG used in the experiments was obtained by fermentation according to the method of Lazarus et. al., Anderson et al.. Science, 230:144-149 (1985), and was purified by concentration and crystallization. KLG may alternatively be prepared by chemical conversion from L-sorbose according to methods well known in the art [ see e.g.,U.S. Pat. No. 2,301,811 to Reichstein). A standard of methyl-2-keto-L-gulonate was purchased from Aldrich Chemical Company (Rare and Specialty Chemicals Catalog) , in addition to being prepared by esterification of KLG by methods similar to the procedure used for the preparation of butyl-KLG, described below. Enzyme hydrolase samples were obtained from commercial sources, including Sigma Chemical Company, Altus Biologies, Recombinant Biocatalysis, Boehringer Mannheim, Novo Nordisk, Genencor International, Thermogen, and Fluka. Example 1 This example describes the preparation and purification of butyl 2-ket -L-gulonate. KLG hydrate (51.62 g) was charged in a 500 ml reaction vessel under argon. The reactor was equipped with a 30.48 cm (12") vigreux column attached to a Dean Stark trap. The reactor was then charged with n-butanol (310 g) and p-toluene sulfonic acid (2.3 g) . The reaction mixture was brought to reflux (81-82°C) under mild vacuum [(approximately 19.95 kPa (150 mm Hg) ] with stirring. Reflux was maintained for a total of two hours and 40 minutes. Heating was discontinued. The reaction was allowed to cool and remain at room temperature for approximately 3 days. The resulting crystals were filtered through a coarse fritted glass filter and washed with two portions of n-butyl alcohol (139 g followed by 37 g) . The resulting solids (24.4 g) were dissolved in hot ethyl acetate (250 ml) and recrystallized by standing overnight at room temperature. The recrystallized butyl-KLG was isolated by filtration and dried under vacuum [0.1995 kPa (1.5 mm Hg) ] until constant weight (15.97 g) was achieved. The butyl-KLG thus prepared was found to have a solubility of at least 50 weight percent in water as it was soluble at all concentrations under 50 weight percent in water. The recrystallized butyl-KLG of this example had satisfactory proton and carbon NMR spectra and gave the predicted molecular weight by field desorption mass spectrometry. : H NMR (DMSO, digital resolution = 0.11 Hz, TMS at half height = 0.5 Hz) : 6.49 (OH, d, J = 1.4 Hz), 4.96 (OH, d, J = 5.0 Hz), 4.84 (OH, d, J = 4.8 Hz), 4.78 (OH, d, J = 7.4 Hz), 4.17-4.0 ( , 2 H) , 3.5-3.2 (m, approximately 5 H) , 1.64-1.5 ( , 2 H) , 1.4-1.35 (m, 2 H) , 0.89 (CH 3 , t, J = 7.3) . i3 C NMR (DMSO, decoupled) : 169.4, 96.3, 73.8, 72.8, 69.8, 64.5, 62.8, 30.0, 18.4, 13.5. FDMS: M = 250 Example 2 The following procedure was used to demonstrate enzymes for activity under specific pH and aqueous solvent composition conditions. Initial enzyme screens were carried out as follows. Enzyme (typically 10 mg) , aqueous buffer (typically 860 microliters (ul) or 550 ul), aqueous 0.2 M CaCl 2 (10 ul), methanol (typically 90 ul or 400 ul) , and an aqueous solution of substrate (typically 90 ul of butyl-KLG at a typical concentration of 110,000 ppm) were added to a 2 ml polypropylene centrifuge tube. The resulting solution was vortexed briefly and placed on a shaker bath at 300 rpm at 38°C (typically for 18 hours or more) . After incubation, samples were centrifuged at 14,000 G' s (14,000 times gravity) for 20 minutes to remove enzyme, sampled (300 ul), and diluted to one milliliter with distilled water. If not analyzed by HPLC within the day, samples were frozen prior to analysis. Summarized below in Table 2 is the HPLC data of the products (and remaining substrate) upon reaction of butyl-KLG (BuKLG) with a variety of enzyme hydrolases in water/methanol solution. The data were reported in terms of parts per million of KLG, MeKLG, ascorbic acid (ASA) and butyl-KLG. The reporting of a 0 (zero) indicated that the amount of material present was below the detection threshold of the instrument. Samples labeled as "no enzyme" were controls within a given run. The controls contained substrate but no enzyme and thus represented experimental and HPLC background data. T abl e 2 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 41 Hours/38% Methanol- Water/0.1 MES Buffer) Table 2 illustrates that the hydrolases provided by Recombinant Biocatalysis (ESL-001-01 through ESL-001-07) showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 38% methanol-water solution buffered with morpholinoethane sulfonic acid (MES) hemisodium salt at a pH controlled between 5.5 and 6. These hydrolase enzymes are sold commercially by Recombinant Biocatalysis as recombinant esterases and lipases from thermophilic organisms under the tradename CloneZyme (trademark) . Example 3 Table 3 below illustrates that a variety of acylases, esterases, lipases, and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 38% methanol-water solution buffered at pH 4.8 to 5.8 with MES buffer. The enzymes labeled as ChiroClec (trademark) are crystalline crosslinked enzymes sold commercially by Altus Biologies. ChiroClec -CR is a lipase from Candida rugosa , ChiroClec -BL is a crystalline form of Subtilisi n (a protease) , and ChiroClec -PC is a lipase from Pseudomonas cepacia . Candi da Antarti ca B (a lipase), pig liver esterase (a hydrolase) , and Bacill us Species protease showed particularly high levels of activity. Table 3 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 16 Hours/38% Methanol-Water/O .1 M MES Buffer) Enzyme Pig Liver Esterase Pseudomonas cepacia Lipase Porcine Pancreatic Lipase Candida Rugosa Lipase Alpha-Chymotrypsin Penicillin Acylase Aspergillus niger Lipase no enzyme no enzyme Candida Antartica 'A' Lipase Candida lipolytica Lipase Candida antartica Λ B' Lipase Humicola lanugmosa Lipase Bacillus Species Protease no enzyme ChiroCLEC-CR (Dry) ChiroCLEC-BL (Dry) ChiroCLEC-PC (Pseudomonas cepacia) Rhizoipus Delmar Lipase Rhizopus Niveus Lipase Rhizopus Oryzae Lipase Chromobacterium Viscosum Lipase Geotricum Candidum Lipase Mucor Javanicus Lipase Aspergillus Oryzae Protease Amano-Lipase PS30 (Pseudomonas) Amano-Lipase AK 5.6 74 167 93 11372 (Pseudomonas) Example 4 Table 4 below illustrates that a variety of acylases, esterases, lipases, and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 38% methanol-water solution buffered at pH 5 to 5.8 with MES buffer. Pig liver esterase, Subtili sin Carlsberg (a protease) , Bacill us speci es protease, ChiroClec -BL, and Candida Antartica B lipase all show particularly high levels of activity. Table 4 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 47.5 Hours/38% Methanol-Water/O.1 M MES Buffer) Enzyme Pig Liver Esterase Pseudomonas cepacia Lipase Porcine Pancreatic Lipase Candida rugosa Lipase Alpha-Chymotrypsin Penicillin Acylase Aspergillus niger Lipase Mucor meihei Lipase ChiroCLEC-CR Subtilisin Carlsberg Candida antarctica A Candida lipolytica Lipase Candida antartica B Humicola lanuginosa Lipase Bacillus Sp Protease ChiroCLEC-BL protease ChiroCLEC PC lipase Candida Kugosa esterase L-l (Pseudomonas sp) ) L-2 (Candida antartica B) L-3 (Candida cylindracea) L-5 (Candida antartica A) L-6 (Pseudomonas sp) L-7 (Porcine pancreas) L-8 (Humicola sp) no enzyme no enzyme no enzyme Example 5 Table 5 below illustrates that a variety of lipases and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG m a 38% methanol-water solution buffered at pH 5.7 to 6.1 with MES buffer. On comparison with the other enzymes in this table, Prozyme 6 (a protease from Aspergill us oryzae) , Protease 2A (from Aspergill us oryzae) , and GC899 (a commercial detergent protease from Genencor International) showed higher levels of activity. Table 5 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 19 Hours/38?, Methanol-Water/0.1 M MES Buffer) Enzyme Comment Measured pH KLG MeKLG ASA BuKLG (ppm) PS30 (Pseudomonas) Lipase 5.9 10424 GC4 (Geotricum candidum) Lipase 5.7 7475 AK (Pseudomonas) Lipase 6 9815 G (Penicillium) Lipase 5.8 9441 Newlase A (Aspergillus) Protease 5.9 10368 Protease M (Aspergillus) Protease 6 6990 Prozyme 6 (Aspergillus) Protease 6 4965 MAP10 (Mucor) Lipase 6.1 8968 No enzyme 5.9 9463 No enzyme 5, 9391 No enzyme 5, 9539 D( Rhizopus) Lipase 5. 8562 Newlase II (Rhizopus) Protease 5, 9586 o AY30 (Candida) Lipase 6 8725 L-10 (Candida) Lipase 5.7 9608 CES (Pseudomonas) Lipase 5.8 9491 N (Rhizopus) Lipase 5.8 9834 2A (Protease, Aspergillus) Protease 6.1 8951 Hog Pancreatic Lipase Fluka 6 11114 Lipase (Sigma-1754) Lipase 5.8 9845 Lipase (Sigma-1754) Lipase 5.8 9428 Lipase (Sigma-8525) Lipase 5, 9041 Lipase (Sigma-1754) Lipase 5, 14257 Lipase (Sigma-3126) Lipase 5, 12756 F-15 (Rhizopus) Lipase 5. 10262 Lipozyme (Novo-Liquid) Lipase 9100 GC899 (protease) Protease 11607 Example 6 Table 6 below illustrates that a variety of lipases and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 8.6% methanol-water solution buffered at a pH of 5.3 to 6 with MES buffer. Protease M (Aspergiiius oryzae) , Prozyme 6 (a protease from Aspergill us oryzae) , Protease N ( Subtilisin) , and Protease 2A (Aspergill us oryzae) all showed particularly high levels of activity. Table 6 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38° for 19 Hours/8.6% Methanol-Water/O.1 M MES) Enzyme PS30 (Pseudomonas) GC4 (Geotricum candidum) AK (Pseudomonas) G (Penicillium) Newlase A (Aspergillus) R-10 (Penicillium) Protease M (Aspergillus) Prozyme 6 (Aspergillus) MAP10 (Mucor) No enzyme No enzyme No enzyme D( Rhizopus) Newlase II (Rhizopus) AY30 (Candida) L-10 (Candida) AP12 (Aspergillus) CES (Pseudomonas) N (Rhizopus) N (Protease, Bacillus) 2A (Protease, Aspergillus; Hog Pancreatic Lipase Lipase (Sigma-1754) Lipase (Sigma-1754) Lipase (Sigma-8525) Lipase (Sigma-1754) Lipase (Sigma-3126) F-15 (Rhizopus) Lipozyme (Novo-Liquid) GC899 (protease) 00 Example 7 Table 7 below illustrates that a variety of acylases, esterases, lipases, and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 8.6% methanol-water solution buffered at a pH of approximately 5 to 6 with MES buffer. Candida Antarti ca B lipase, pig liver esterase, and Bacill us species protease showed particularly high levels of activity. Table 7 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 19 Hours/8.6% Methanol-Water/O.1 M MES) Enzyme Comment KLG MeKLG ASA BuKLG L-l (Pseudomonas sp) ) Lipase 137 116 47 7601 L-2 (Candida antartica B) Lipase 5249 1921 0 768 L-3 (Candida cylindracea) Lipase 183 64 107 6920 L-4 (Pseudomonas sp) Lipase 239 163 9957 L-5 (Candida antartica A) Lipase 278 344 0 6245 L-6 (Pseudomonas sp) Lipase 90 219 15 6613 L-7 (Porcine pancreas) Lipase 1007 575 106 5392 L-8 (Humicola sp) Lipase 209 70 150 7957 J no enzyme 168 152 6 8753 o no enzyme 152 144 3 8233 no enzyme 170 137 18 8157 ESL-OOl-01 Recombinant 1271 906 375 4635 ESL-001-02 Biocatalysis 883 329 332 5949 ESL-001-03 Enzymes 290 123 447 7333 ESL-001-04 511 161 306 6207 ESL-001-05 364 124 299 6402 ESL-001-06 329 117 118 6934 ESL-001-07 0 122 430 15752 Pig Liver Esterase 2726 3731 423 10 Pseudomonas cepacia Lipase 241 109 224 9135 Porcine Pancreatic Lipase 333 2 1 314 7888 Candida rugosa Lipase 296 86 451 8697 no enzyme 153 116 8234 Alpha-Chymotrypsin protease 330 Penicillin Acylase 187 no enzyme 100 no enzyme 144 Aspergillus niger Lipase 479 Mucor eihei Lipase 229 ChiroCLEC-CR lipase 233 Subtilisin Carlsberg 4463 Candida antarctica A lipase 215 Candida lipolytica Lipase 198 Bacillus Sp Protease 4920 ChiroCLEC-BL protease 2860 I ChiroCLEC PC lipase 127 > Candida Rugosa esterase 178 Example 8 Table 8 below illustrates that a variety of acylases, esterases, lipases, and proteases showed appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 8.6% methanol-water solution buffered at a pH of approximately 5.8 to 6.2 with MES buffer. Pig liver esterase, Candida Antarti ca B lipase, Bacill us speci es protease, and lightly crosslinked crystalline Subtili sin (ChirClec-BL) sr.owed particularly high levels of activity. Table 8 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 21 Hours/8.6% Methanol-Water/O.2M MES Enzyme Pig Liver Esterase Pseudomonas cepacia Lipase Porcine Pancreatic Lipase Candida rugosa Lipase Alpha-Chymotrypsin Penicillin Acylase Aspergillus niger Lipase Mucor meihei Lipase no enzyme no enzyme no enzyme Candida antartica A' Lipase Candida lipolytica Lipase Candida antartica B' Lipase Humicola lanuginosa Lipase Bacillus Species Protease ChiroCLEC-CR (Dry) ChiroCLEC-BL (Dry) ChiroCLEC-PC (P. cepacia-Dry) Rhizoipus Delmar Lipase Rhizopus Niveus Lipase Rhizopus Oryzae Lipase Chromobacterium Viscosum Lipase Geotricum Candidum Lipase Mucor Javanicus Lipase Aspergillus Oryzae Protease Candida Rugosa Esterase 4 - Example 9 Table 9 below demonstrates the statistical reproduction of the activity detected for highly active enzymes in the preceding examples. Eight of the enzymes from the previous examples, which were identified as showing particularly high levels of activity, were compared under tight pH control. All of the previously identified enzymes with high levels of activity maintained this high level of activity on reanalysis. The enzymes exhibited appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 8.6% methanol-water solution buffered at a pH of approximately 5.6 to 6 with 0.2 M MES buffer. Candida Antartica B lipase, pig liver esterase, and Bacill us speci es protease showed particularly high levels of activity within this comparative example. Pig liver esterase showed a selectivity toward transesterification as well as significant conversions to ascorbic acid. Table 9 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 19 Hours/8.6% Metanol-Water/O.2 M MES Buffer) Example 10 Table 10 below compares the same enzymes as in Example 9 except at a higher concentration of organic solvent. Candida Antarti ca B and Bacill us species protease showed particularly high levels of activity in that they exhibited appreciable conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG a 38% methanol-water solution buffered at a pH of approximately 5.6 to 6.2 with 0.2 M MES buffer. Decreased, although still appreciable, activity is observed for pig liver esterase relative to that shown in Example 9. Table 10 Enzyme Screen for Hydrolysis/Methanolysis of Butyl-KLG (38°C for 19 Hours/38% Methanol-Water/O .2 M MES Buffer) 00 Example 11 Table 11 below compares the same enzymes as Example 9 except at a pH buffered around 5.2. Candi da Antarti ca B and pig liver esterase showed particularly high levels of activity in that they exhibited appreciable conversion of butyl-KLG to MeKLG and KLG in a 8.6% methanol-water solution buffered at a pH of approximately 4.9 to 5.3 with 0.2 M pyridine/pyridmium hydrochloride buffer. Decreased, although still appreciable, activity is observed for Bacill us species protease relative to Example 9. Table 11 Enzyme Screen for Hydrolysis/Methanolysis of BUKLG (38°C for ca. 19 Hours/8.6% Methanol-Water/O .2 M Pyridine/ Pyridiniuym Hydrochloride) Example 12 Table 12 below compares the same enzymes as in Example 11 except at a higher concentration of organic solvent. Candida Antartica B showed particularly high levels of activity in that it exhibited appreciable conversion of butyl-KLG to MeKLG and KLG in 38% methanol-water solution buffered at a pH of approximately 4.7 to 5.1 with 0.2 M pyridine/pyridinium hydrochloride buffer. All of the enzymes showed reduced activity relative to Examples 9 and 11. Table 12 Enzyme Screen for Hydrolysis/Methanolysis of BuKLG (38°C for ca. 19 Hours/H 4.9/38% Methanol-Water) h Example 13 Table 13 below compares the same enzymes as in Examples 9 and 11 except at a j-H buffered around 2.3. All enzymes tested showed reduced activity relative to Examples 9 and 11 for conversion of butyl-KLG to ascorbic acid, MeKLG, and KLG in a 8.6% methanol-water solution buffered at a pH of approximately 2.3-2.7 with 0.2 M phosphate buffer. Table 13 Enzyme Screen for Hydrolysis/Methanolysis of BUKLG (38°C for 20 Hours/8.6% Methanol-Water/pH 2.3 0.2 M Phosphate Buffer) Example 14 Table 14 below compares the first 5 enzymes of Examples 9 and 11 at a buffered pH of about 6 in their ability to catalyze the esterification of KLG to methyl KLG (MeKLG) or their ability to catalyze ring closure of KLG to ascorbic acid. Low levels of activity are observed relative to examples 9 and 11. Table 14 Enzyme Screen for Methanolysis of KLG 38°C for 19 Hours/8.6% Methanol-Water/O.2 M MES Buffer) Example 15 Table 15 below demonstrates the production of MeKLG from KLG using Candida Antarti ca B lipase as catalyst in 8.6% aqueous methanol at a pH of 3-3.2. The buffer was chosen as a mixture of KLG and its sodium salt (approximately 1/9) . The first three entries include enzyme catalyst and are the same conditions in triplicate. The second three entries also run in triplicate and are the same conditions as the first three entries except that no enzyme was present. The first three entries show significant esterification of KLG to MeKLG in the presence of Candi da Antarti ca B lipase. The second three entries demonstrate that the conversion does not proceed in the absence of Candida Antarti ca B lipase. Table 15 Enzyme Screen for Esterification of KLG 68 Hours at 38°C/8.6% Methanol in Aqueous Phase/Buffer KLG + NaKLG Enzyme Comment PH KLG MeKLG ASA BuKLG Candida Antartica B 0 0 Candida Antartica B 0 0 Candida Antartica B 0 0 no enzyme 0 0 no enzyme 0 0 no enzyme 0 0 00 Example 16 This example demonstrates the slow decomposition of ascorbic acid under the conditions of HPLC analysis. HPLC sample standards were prepared by dissolving KLG, MeKLG, ascorbic acid (ASA) , and butyl-KLG to the appropriate concentration in water. Samples of these standards were placed m filled and sealed vials, stored at room temperature, and analyzed periodically. The HPLC was calibrated on the area response for standards that were injected onto the HPLC as soon as possible after the preparation of the standards. Table 16 below shows the recorded responses for KLG, MeKLG, ascorbic acid, and butyl-KLG standards of 50, 100, and 500 ppm at time 0 (calibration time), at approximately 6.5 hours, and at approximately 12 hours after sample preparation. Table 16 Amount Prepared Amount Found Time KLG MeKLG ASA BuKLG (minutes ' , 0 50ppm standard 400 715 0 100 ppm standard 400 715 0 500 ppm standard 400 715 The ascorbic acid responses were non-linear over time with respect to the other standards and, particularly, with respect to standards of 100 ppm or less. Given that the treatment for Examples 2-16 included approximately 16 hours or more at 38°C on a shaker bath prior to HPLC analysis, it follows that the actual level of ascorbic acid formed was greater than reported. This invention has been described in detail with particular reference to preferred embodiments thereof, but it will be understood that variations and modifications can be effected within the spirit and scope of the invention. SEQUENCE LISTING GENERAL INFORMATION (i) APPLICANT: Hubbs, John C. (ii) TITLE OF INVENTION: Enzymatic Process for the Manufacture of Ascorbic Acid, 2-Keto-L-Gulonιc Acid, and Esters of 2-Keto-L-Gulonic Acid (iii) NUMBER OF SEQUENCES: 3 (iv) CORRESPONDENCE ADDRESS: (A) ADDRESSEE: Eastman Chemical Company (B) STREET: P.O. Box 511 (C) CITY: Kingsport (D) STATE: Tennessee (E) COUNTRY: USA (F) ZIP: 37662-5075 (v) COMPUTER READABLE FORM: (A) MEDIUM TYPE: * (B) COMPUTER: * (C) OPERATING SYSTEM: * (D) SOFTWARE: * (vi) CURRENT APPLICATION DATA: (A) APPLICATION NUMBER: * (B) FILING DATE: * (C) CLASSIFICATION: * (vii) PRIOR APPLICATION DATA: (A) APPLICATION NUMBER: US 60/017,879 (B) FILING DATE: 17-MAY-1996 (vni) ATTORNEY/AGENT INFORMATION: (A) NAME: Cheryl J. Tubach (B) REGISTRATION NUMBER: * (C) REFERENCE/DOCKET NUMBER: 70432 (ix) TELECOMMUNICATION INFORMATION: (A) TELEPHONE: 423-229-6189 (B) TELEFAX: 423-229-1239 (2) INFORMATION FOR SEQ ID NO: 1 : (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 379 amino acids (B) TYPE: Amino Acid (D) TOPOLOGY: Linear (ii) MOLECULE TYPE: protein (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 1 : Met Met Arg Lys Lys Ser Phe Trp Leu Gly Met Leu Thr Ala Phe Met 1 5 10 15 Leu Val Phe Thr Met Ala Phe Ser Asp Ser Ala Ser Ala Ala Gin Pro 20 25 30 Ala Lys Asn Val Glu Lys Asp Tyr He Val Gly Phe Lys Ser Gly Val 35 40 45 Lys Thr Ala Ser Val Lys Lys Asp He He Lys Glu Ser Gly Gly Lys 50 55 60 Val Asp Lys Gin Phe Arg He He Asn Ala Ala Lys Ala Lys Leu Asp 65 70 75 80 Lys Glu Ala Leu Lys Glu Val Lys Asn Asp Pro Asp Val Ala Tyr Val 85 90 95 Glu Glu Asp His Val Ala His Ala Leu Ala Gin Thr Val Pro Tyr Gly 100 105 110 lie Pro Leu He Lys Ala Asp Lys Val Gin Ala Gin Gly Phe Lys Gly 115 120 125 Ala Asn Val Lys Val Ala Val Leu Asp Thr Gly He Gin Ala Ser His 130 135 140 Pro Asp Leu Asn Val Val Gly Gly Ala Ser Phe Val Ala Gly Glu Ala 145 150 155 160 Tyr Asn Thr Asp Gly Asn Gly His Gly Thr His Val Ala Gly Thr Val 165 170 175 Ala Ala Leu Asp Asn Thr Thr Gly Val Leu Gly Val Ala Pro Ser Val 180 185 190 Ser Leu Tyr Ala Val Lys Val Leu Asn Ser Ser Gly Ser Gly Thr Tyr 195 200 205 Ser Gly He Val Ser Gly He Glu Trp Ala Thr Thr Asn Gly Met Asp 210 215 220 Val He Asn Met Ser Leu Gly Gly Pro Ser Gly Ser Thr Ala Met Lys 225 230 235 240 Gin Ala Val Asp Asn Ala Tyr Ala Arg Gly Val Val Val Val Ala Ala 245 250 255 Ala Gly Asn Ser Gly Ser Ser Gly Asn Thr Asn Thr He Gly Tyr Pro 260 265 270 Ala Lys Tyr Asp Ser Val He Ala Val Gly Ala Val Asp Ser Asn Ser 275 280 285 Asn Arg Ala Ser Phe Ser Ser Val Gly Ala Glu Leu Glu Val Met Ala 290 295 300 Pro Gly Ala Gly Val Tyr Ser Thr Tyr Pro Thr Ser Thr Tyr Ala Thr 305 310 315 320 Leu Asn Gly Thr Ser Met Ala Ser Pro His Val Ala Gly Ala Ala Ala 325 330 335 Leu He Leu Ser Lys His Pro Asn Leu Ser Ala Ser Gin Val Arg Asn 340 345 350 Arg Leu Ser Ser Thr Ala Thr Tyr Leu Gly Ser Ser Phe Tyr Tyr Gly 355 360 365 Lys Gly Leu He Asn Val Glu Ala Ala Ala Gin 370 375 (2) INFORMATION FOR SEQ ID NO:2: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 584 amino acids (B) TYPE: Amino Acid (D) TOPOLOGY: Linear (ii) MOLECULE TYPE: protein (xi) SEQUENCE DESCRIPTION: SEQ ID NO:2: Met Trp Leu Leu Pro Leu Val Leu Thr Ser Leu Ala Ser Ser Ala Thr 1 5 10 15 Trp Ala Gly Gin Pro Ala Ser Pro Pro Val Val Asp Thr Ala Gin Gly 20 25 30 Arg Val Leu Gly Lys Tyr Val Ser Leu Glu Gly Leu Ala Phe Thr Gin 35 40 45 Pro Val Ala Val Phe Leu Gly Val Pro Phe Ala Lys Pro Pro Leu Gly 50 55 60 Ser Leu Arg Phe Ala Pro Pro Gin Pro Ala Glu Pro Trp Ser Phe Val 65 70 75 80 Lys Asn Thr Thr Ser Tyr Pro Pro Met Cys Cys Gin Asp Pro Val Val 85 90 95 Glu Gin Met Thr Ser Asp Leu Phe Thr Asn Phe Thr Gly Lys Glu Arg 100 105 110 Leu Thr Leu Glu Phe Ser Glu Asp Cys Leu Tyr Leu Asn He Tyr Thr 1 15 120 125 Pro Ala Asp Leu Thr Lys Arg Gly Arg Leu Pro Val Met Val Trp He 130 135 140 His Gly Gly Gly Leu Val Leu Gly Gly Ala Pro Met Tyr Asp Gly Val 145 150 155 160 Val Leu Ala Ala His Glu Asn Phe Thr Val Val Val Val Ala He Gin 165 170 175 Tyr Arg Leu Gly He Trp Gly Phe Phe Ser Thr Gly Asp Glu His Ser 180 185 190 Arg Gly Asn Trp Gly His Leu Asp Gin Val Ala Ala Leu His Trp Val 195 200 205 Gin Glu Asn He Ala Asn Phe Gly Gly Asp Pro Gly Ser Val Thr He 210 215 220 Phe Gly Glu Ser Phe Thr Ala Gly Gly Glu Ser Val Ser Val Leu Val 225 230 235 240 Leu Ser Pro Leu Ala Lys Asn Leu Phe His Arg Ala He Ser Glu Ser 245 250 255 Gly Val Ala Leu Thr Val Ala Leu Val Arg Lys Asp Met Lys Ala Ala 260 265 270 Ala Lys Gin He Ala Val Leu Ala Gly Cys Lys Thr Thr Thr Ser Ala 275 280 285 Val Phe Thr Phe Val His Cys Leu Arg Gin Lys Ser Glu Asp Glu Leu 290 295 300 Leu Asp Leu Thr Leu Lys Met Lys Phe Leu Thr Leu Asp Phe His Gly 305 310 315 320 Asp Gin Arg Glu Ser His Pro Phe Leu Pro Thr Val Val Asp Gly Val 325 330 335 Leu Leu Pro Lys Met Pro Glu Glu He Leu Ala Glu Lys Asp Phe Thr 340 345 350 Phe Asn Thr Val Pro Tyr He Val Gly He Asn Lys Gin Glu Phe Gly 355 360 365 Trp Leu Leu Pro Thr Met Met Gly Phe Pro Leu Ser Glu Gly Lys Leu 370 375 380 Asp Gin Lys Thr Ala Thr Ser Leu Leu Trp Lys Ser Tyr Pro He Ala 385 390 395 400 Asn He Pro Glu Glu Leu Thr Pro Val Ala Thr Phe Thr Asp Lys Tyr 405 410 415 Leu Gly Gly Thr Asp Asp Pro Val Lys Lys Lys Asp Leu Phe Leu Asp 420 425 430 Leu Met Gly Asp Val Val Phe Gly Val Pro Ser Val Thr Val Ala Arg 435 440 445 Gin His Arg Asp Ala Gly Ala Pro Thr Tyr Met Tyr Glu Phe Gin Tyr 450 455 460 Arg Pro Ser Phe Ser Ser Asp Lys Phe Thr Lys Pro Lys Thr Val He 465 470 475 480 Gly Asp His Gly Asp Glu He Phe Ser Val Phe Gly Phe Pro Leu Leu 485 490 495 Lys Gly Asp Ala Pro Glu Glu Glu Val Ser Leu Ser Lys Thr Val Met 500 505 510 Lys Phe Trp Ala Asn Phe Ala Arg Ser Gly Asn Pro Asn Gly Glu Gly 515 520 525 Leu Pro His Trp Pro Phe Thr Met Tyr Asp Gin Glu Glu Gly Tyr Leu 530 535 540 Gin He Gly Val Asn Thr Gin Ala Ala Lys Arg Leu Lys Gly Glu Glu 545 550 555 560 Val Ala Phe Trp Asn Asp Leu Leu Ser Lys Glu Ala Ala Lys Lys Pro 565 570 575 Pro Lys He Lys His Ala Glu Leu 580 (2) INFORMATION FOR SEQ ID NO:3 (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 342 amino acids (B) TYPE: Amino Acid (D) TOPOLOGY: Linear (ii) MOLECULE TYPE: protein (xi) SEQUENCE DESCRIPTION: SEQ ID NO:3 : Met Lys Leu Leu Ser Leu Thr Gly Val Ala Gly Val Leu Ala Thr Cys 1 5 10 15 Val Ala Ala Thr Pro Leu Val Lys Arg Leu Pro Ser Gly Ser Asp Pro 20 25 30 Ala Phe Ser Gin Pro Lys Ser Val Leu Asp Ala Gly Leu Thr Cys Gin 35 40 45 Gly Ala Ser Pro Ser Ser Val Ser Lys Pro He Leu Leu Val Pro Gly 50 55 60 Thr Gly Thr Thr Gly Pro Gin Ser Phe Asp Ser Asn Trp He Pro Leu 65 70 75 80 Ser Thr Gin Leu Gly Tyr Thr Pro Cys Trp He Ser Pro Pro Pro Phe 85 90 95 Met Leu Asn Asp Thr Gin Val Asn Thr Glu Tyr Met Val Asn Ala He 100 105 110 Thr Ala Leu Tyr Ala Gly Ser Gly Asn Asn Lys Leu Pro Val Leu Thr 1 15 120 125 Trp Ser Gin Gly Gly Leu Val Ala Gin Trp Gly Leu Thr Phe Phe Pro 130 135 140 Ser He Arg Ser Lys Val Asp Arg Leu Met Ala Phe Ala Pro Asp Tyr 145 150 155 160 Lys Gly Thr Val Leu Ala Gly Pro Leu Asp Ala Leu Ala Val Ser Ala 165 170 175 Pro Ser Val Trp Gin Gin Thr Thr Gly Ser Ala Leu Thr Thr Ala Leu 180 185 190 Arg Asn Ala Gly Gly Leu Thr Gin He Val Pro Thr Thr Asn Leu Tyr 195 200 205 Ser Ala Thr Asp Glu He Val Gin Pro Gin Val Ser Asn Ser Pro Leu 210 215 220 Asp Ser Ser Tyr Leu Phe Asn Gly Lys Asn Val Gin Ala Gin Ala Val 225 230 235 240 Cys Gly Pro Leu Phe Val He Asp His Ala Gly Ser Leu Thr Ser Gin 245 250 255 Phe Ser Tyr Val Val Gly Arg Ser Ala Leu Arg Ser Thr Thr Gly Gin 260 265 270 Ala Arg Ser Ala Asp Tyr Gly He Thr Asp Cys Asn Pro Leu Pro Ala 275 280 285 Asn Asp Leu Thr Pro Glu Gin Lys Val Ala Ala Ala Ala Leu Leu Ala 290 295 300 Pro Ala Ala Ala Ala He Val Ala Gly Pro Lys Gin Asn Cys Glu Pro 305 310 315 320 Asp Leu Met Pro Tyr Ala Arg Pro Phe Ala Val Gly Lys Arg Thr Cys 325 330 335 Ser Gly He Val Thr Pro 340

Claims: CLAIMS What is claimed is: 1. A process for preparing ascorbic acid comprising contacting a compound selected from the group consisting of 2-keto-L-gulonic acid and an ester of 2-keto-L- gulonic acid with a hydrolase enzyme catalyst to form ascorbic acid. 2. The process of claim 1 wherein the hydrolase enzyme catalyst is selected from the group consisting of a protease, an esterase, a lipase and an amidase. 3. The process of claim 2 wherein the protease is obtained from a genera selected from the group consisting of Bacill us or Aspergill us . . The process of claim 3 wherein the protease is obtained from a Bacill us li cheniformis bacteria. 5. The process of claim 4 wherein the protease has at least 70 percent sequence homology with a Subtilisin protease having a sequence as shown in SEQ ID NO: 1. 6. The process of claim 5 wherein the protease is the Subtilisin protease having the sequence as shown in SEQ ID NO: 1. 7. The process of claim 2 wherein the esterase is obtained from pig liver extract. 8. The process of claim 7 wherein the esterase has at least 70 percent sequence homology with a pig liver esterase having a sequence as shown in SEQ ID NO: 2. 9. The process of claim 8 wherein the esterase is the pig liver esterase having the sequence as shown in SEQ ID NO: 2. 10. The process of claim 2 wherein the lipase is obtained from a genera selected from the group consisting of Aspergillus, Mucor, Candida, Pseudomonas, Humicola, Rhizopus, Chromobacteri um, Alcaligenes, Geotricum and Penicillium. 11. The process of claim 10 wherein the lipase obtained from the genus Candida is a lipase having at least 70 percent sequence homology with a Candida Antartica B lipase having a sequence as shown in SEQ ID NO: 3. 12. The process of claim 11 wherein the lipase is the Candida Antartica B lipase having the sequence as shown in SEQ ID NO: 3. 13. The process of claim 2 wherein the amidase is obtained from a genus Peni cilli um. 14. The process of claim 13 wherein the amidase has at least 80% sequence homology with a Penicillin acylase. 15. The process of claim 14 wherein the amidase is the Penicillin acylase . 16. The process of claim 1 wherein the hydrolase enzyme catalyst contains an active site serine residue. 17. The process of claim 16 wherein the hydrolase enzyme catalyst contains a catalytic triad of serine, histidine and aspartic acid. 18. The process of claim 1 wherein, prior to contacting the compound with the hydrolase enzyme catalyst, the compound is formed into a solution with a solvent. 19. The process of claim 18 wherein the solvent is selected from the group consisting of water, a Ci to Cβ alcohol and a mixture thereof. 20. The process of claim 1 wherein contacting the compound with the hydrolase enzyme catalyst occurs at a pH between 1.5 and 10. 21. The process of claim 1 wherein contacting the compound with the hydrolase enzyme catalyst occurs at a temperature from 5°C to 120°C. 22. The process of claim 1 wherein, prior to contacting the compound with the hydrolase enzyme catalyst, the hydrolase enzyme catalyst is naturally expressed from a host organism in vi vo . 23. The process of claim 1 wherein, prior to contacting the compound with the hydrolase enzyme catalyst, a gene sequence encoding the hydrolase enzyme catalyst is inserted into a host organism and the host organism is cultured to express the hydrolase enzyme catalyst in vivo. 24. The process of claim 23 wherein the host organism is Pantoea ci trea . 25. The process of claim 22 or claim 23 wherein the host organism produces KLG. 26. A mixture containing ascorbic acid prepared according to the process of claim 1. 27. A process for preparing 2-keto-L-gulonic acid comprising the steps of: (a) preparing an aqueous solution of an ester of 2-keto-L-gulonic acid, and (b) then contacting the ester of 2-keto-L-gulonic acid in solution with a hydrolase enzyme catalyst to form 2-keto-L-gulonic acid. 28. The process of claim 27 wherein the hydrolase enzyme catalyst is selected from the group consisting of a protease, an esterase, a lipase and an amidase. 29. The process of claim 27 wherein a co-solvent is used in preparing the aqueous solution. 30. The process of claim 29 wherein the co-solvent is a Ci to C 6 alcohol. 31. A process for preparing an ester of 2-keto-L- gulonic acid comprising the steps of: (a) preparing an alcoholic solution of 2-keto-L- guionic acid and an alcohol corresponding to an alkyl moiety of an ester of 2-keto-L-gulonic acid to be formed; and (b) then contacting the 2-keto-L-gulonic acid in solution with a hydrolase enzyme catalyst to form the ester of 2-keto-L-gulonic acid. 32. The process of claim 31 wherein the hydrolase enzyme catalyst is selected from the group consisting of a protease, an esterase, a lipase and an amidase. 33. The process of claim 31 wherein a co-solvent is used in preparing the alcoholic solution. 34. The process of claim 33 wherein the co-solvent is selected from the group consisting of water, a Ci to C 6 alcohol and a mixture thereof. 35. A process for preparing an ester of 2-keto-L- gulonic acid comprising the steps of: (a) preparing an alcoholic solution of a first ester of 2-keto-L-gulonic acid and an alcohol corresponding to an alkyl moiety of a second ester of 2- keto-L-gulonic acid to be formed; and (b) then contacting the first ester of 2-keto-L- gulonic acid in solution with a hydrolase enzyme catalyst to form the second ester of 2-keto-L-gulonic acid. 36. The process of claim 35 wherein the hydrolase enzyme catalyst is selected from the group consisting of a protease, an esterase, a lipase and an amidase. 37. The process of claim 35 wherein a co-solvent is used in preparing the alcoholic solution. 38. The process of claim 37 wherein the co-solvent is selected from the group consisting of water, a Ci to Cβ alcohol and a mixture thereof.

Inventors: HUBBS JOHN CLARK, HUBBS, JOHN, CLARK
Applicants: EASTMAN CHEM CO, EASTMAN CHEMICAL COMPANY
Application year: 1997
Main classification: C12P17
IPC codes: C12N9, C12P7, C12P17