Patent Application
20180291410
The present invention relates to the method for sucrose phosphorylase mediated production of 2-O-α-D-glucopyranosyl-L-ascorbic acid.
2-O-α-D-glucopyranosyl-L-ascorbic acid (AA-2G) is a highly stable form of all the known L-ascorbic acid derivatives. Modification of the hydroxyl group in 2-position of L-ascorbic acid (responsible for its biological activity and stability) has improved the stability of L-ascorbic acid (L-AA) significantly. Glycosylation of the hydroxyl group in 2-position of L-ascorbic acid offers several advantages over other derivatives such as phosphate and sulphate derivatives. The other isoforms of
Glycosyl transferases (GTs) are the enzymes responsible for the synthesis of glycosides in nature whereas glycosyl hydrolases (GHs) have been evolved to degrade them. Both glycosyl transferases and glycosyl hydrolases have been successfully used for the production of a wide-variety of glycosides. These enzymes have also been used in enzymatic synthesis of AA-2G.
Rat intestinal and rice seed α-glucosidases, which belong to GHs, have produced AA-2G when maltose and
Cyclodextrin Glucanotransferase (CGTase), which belongs to GTs, is another well studied enzyme for the large scale production of AA-2G. EP0425066 discloses a process for producing AA-2G, which may be carried out in an industrial scale allowing a saccharide-transferring enzyme such as CGTase to act on a solution containing L-ascorbic acid and an α-glucosyl saccharide to form AA-2G and by-products. When CGTase is used along with cyclodextrin (the most preferred donor substrate) or starch as a donor substrate several AA-2-maltooligosaccharide by-products were inevitably formed because of the transfer of whole or part of linearized maltooligosaccharide to the
WO2004013344 discloses a process for producing AA-2G using α-isomaltosyl glucosaccharide forming enzyme (IMG) from Arthrobacter globiformis where AA-5G or AA-6G are not formed or formed in such a small amount that the formation of these cannot be detected (<0.1% wt/wt on dry solid basis). In this process the IMG was used as a transglycosylating enzyme along with CGTase and partial starch hydrolysate as donor substrate (to breakdown the starch into oligosaccharides). The combination of these two enzymes improved the yields and reduced the formation of AA-5G and AA-6G contents below 0.1%. However the formation of several by-products was not avoided. The by-products were further treated with glucoamylase to convert into AA-2G. Thus this system needed in total 3 enzymes to run the whole process efficiently.
The currently available enzymatic methods can produce AA-2G in large scale. The presence of several by-products and different isoforms at the end of the reaction are still bottlenecks in the whole process and are interfering in AA-2G isolation and purification. The by-products can be converted into AA-2G by glucoamylase treatment and the AA-2G can be easily separated from
Thus, there is still the need for an improved process for the production of AA-2G with high yields.
It is an objective of the present invention to provide an efficient one-step production process for large-scale manufacture of AA-2G.
The objective is solved by the subject of the present invention.
According to the invention there is provided a method for producing 2-O-α-D-glucopyranosyl-L-ascorbic acid (AA-2G) comprising the sequential steps of:
The present invention provides a novel and improved method for producing 2-O-α-D-glucopyranosyl-L-ascorbic acid comprising the sequential steps of:
Thus, it was an objective to find an enzyme which can use a simple and low cost disaccharide or monosaccharide as donor substrate and perform transglycosylation only at the 2-position of
Among the GT and GH classes, the glycoside phosphorylases (GPs) are special in several respects. GPs catalyze the phosphorolysis of α- and β-D-glycosides, mainly glucosides (Glc-OR) including disaccharides and oligo-or poly-saccharides of varying degree of polymerization. Glucosyl transfer to phosphate (Pi) is favored thermodynamically in vivo because phosphate is usually present in large excess over α-D-glucose-1-phosphate (Glc-1-P). However, thermodynamic equilibrium constants (Keq) of GP-catalyzed reactions fall between the Keq values for the reaction of GTs (Keq<<1) and GHs (Keq>>1). The relatively favorable Keq and the fact that phosphor-activated sugars are less expensive than nucleotide-activated ones, which are required by most GTs, make GPs interesting biocatalysts for the stereo- and regiospecific synthesis of glucosides.
Sucrose phosphorylase (SPase; EC 2.4.1.7), a glucosyl phosphorylase, catalyzes the conversion of sucrose and phosphate into D-fructose and α-D-glucose-1-phosphate (Glc 1-P). SPase has been isolated from a number of bacterial sources. Genes encoding SPase have been cloned from different bacteria and expressed heterologously (Kawasaki H et al., Biosci. Biotech. Biochem. (1996) 60:322-324; Kitao S and Nakano E, J. Ferment. Bioeng. (1992) 73:179-184; van den Broek LAM et al., Appl. Microbiol. Biotechnol. (2004) 65:219-227). According to the systematic sequence-based classification of glycosylhydrolases (GH) and glycosyltransferases (GT) SPase belongs to family GH13 (Clan GH-H), often referred to as the α-amylase family. The three-dimensional structure of SPase from Bifidobacterium adolescentis has been solved recently, revealing an (beta/alpha)8 barrel fold and a catalytic site in which two carboxylate groups probably fulfill the role of a nucleophile (Asp192) and a general acid/base (Glu232).
“Sucrose phosphorylase” as used herein refers not only to enzymes of the EC 2.4.1.7 class but also to molecules or functional equivalents thereof which exhibit the same properties in relation to its substrates and products. “Functional equivalents” or analogs of the enzyme are, within the scope of the present invention, various polypeptides thereof, which moreover possess the desired biological function or activity, e.g. enzyme activity.
One embodiment of the invention relates to a method for producing AA-2G, wherein the SPase is of metagenomic, microbial or bacterial origin. As used herein the term “metagenomics” refers to genetic material directly recovered from environmental samples.
A further embodiment of the invention relates to a method for producing AA-2G, wherein the SPase is of microbial or bacterial origin, preferably of bacterial origin.
Homodimeric enzyme refers to an enzyme complex formed by two identical molecules. Some of the SPase are capable of forming homodimers. Examples of homodimeric SPases are amongst others derived from Bifidobacterium adolescentis, Streptococcus mutans, or Bifidobacterium longum. Surprisingly, homodimeric SPases exhibit high site-selectivity in glycosylation of
As used herein, the term “by-product” refers to any undesired product, specifically refers to AA-3G, AA-5G or AA-6G. The term “substantially free of by-product”means that the content of the by-product is less than 25%, less than 20%, 15%, 10%, 5%, or less than 1% by weight.
One embodiment of the invention relates to the sucrose phosphorylase showing high stability at a pH below 7, preferably at a pH below 6, more preferred at a pH below 5 and most preferred at a pH below 4.
In particular embodiments, the sucrose phosphorylase of the invention has a residual sucrose phosphorylase activity after incubation for 48 hours at 60° C. and at pH selected from 2.0, 3.0, 4.0, 5.0, 6.0, and 7.0, of at least 50%, preferably at least 55%, 60%, 65%, 70%, 75%, 80%, 82%, 84%, 86%, 90%, 92%, or at least 94%, relative to the sucrose phosphorylase activity at 0 hours (before start of the incubation). In preferred embodiments, the incubation pH is 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 5.5, 6.0, 6.5 or 7.0. In even more preferred embodiments, the incubation pH is 5.2, and the residual activity is at least 50%, 55%, 60%, 65%, 70%, 75%, 80%, or at least 82%.
SPase activity was determined at 30° C. using a continuous coupled enzymatic assay, in which production of Glc 1-P from sucrose and inorganic phosphate is coupled to the reduction of NAD+ in the presence of phosphoglucomutase (PGM) and glucose 6-phosphate dehydrogenase (G6P-DH) as described in Example 2.
One embodiment of the invention relates to the sucrose phosphorylase recombinantly produced using genetic material directly obtained from environmental samples.
The advantage of using microbial sucrose phosphorylases is the simple production and isolation and stability of these enzymes. They can be obtained from microorganisms naturally or recombinantly expressing SPase.
One embodiment of the invention relates to sucrose phosphorylase obtained from Agrobacterium vitis, Bifidobacterium adolescentis, Bifidobacterium longum, Escherichia coli; preferably Escherichia coli 06, Lactobacillus acidophilus, Lactobacillus delbrueckii subsp. lactis, Leuconostoc mesenteroides, Listeria monocytogenes, Pseudomonas putrefaciens, Pseudomonas saccharophila, Rhodopirellula baltica, Shewanella baltica, Shewanella frigidimarina, Solibacter usitatus, Streptococcus mutans or Synechococcus sp.
One embodiment of the invention relates to recombinantly produced sucrose phosphorylase, preferably as a full-length protein or a catalytically active fragment thereof or a fusion protein. Methods for the recombinant production of enzymes are known to the person skilled in the art (e.g. Sambrook J. et al. Molecular cloning: a laboratory manual. ISBN 0-87969-309-6).
As used herein, “full-length protein” refers to sucrose phosphorylase protein encoded by a gene derived from an organism as, for instance, listed above. Said naturally occurring gene, in particular the sucrose phosphorylase encoding region of said gene, is directly employed for the recombinant production of SPase.
“A catalytically active fragment” of a sucrose phosphorylase refers to protein fragments of sucrose phosphorylase which have the same or substantially the same activity and substrate specificity as native SPase. The length of the fragments is not crucial provided that the fragments will have the same or similar substrate specificity and catalyze the formation of the same products as native sucrose phosphorylase.
The term “fusion protein” refers to sucrose phosphorylase or catalytically active fragments thereof recombinantly fused to at least one further protein, polypeptide or peptide. Said at least one further protein, polypeptide or peptide may be of any kind (e.g. enzyme).
It is noted that within the scope of the invention also functional variants (i.e. mutations including deletions, substitutions and insertions) of sucrose phosphorylase are encompassed, provided that these functional variants have the same or substantially the same activity as the native sucrose phosphorylase.
However, it is of course also possible to use sucrose phosphorylase directly obtained from the organism which naturally produces said sucrose phosphorylase.
The SPase may be employed in the incubation step as either a cell-free enzyme, which may but need not be partially purified, a whole-cell system pre-treated physically or chemically for improved permeability of the cell membrane (permeabilization) and mechanical stability, encapsulated catalyst in which said free enzyme or whole-cell system are entrapped, preferably in gel-like structures, or immobilized on a carrier. Advantageously the SPase is immobilized on a carrier which preferably is a solid support. The carrier is preferably a chromatography resin, preferably selected from the group consisting of anion exchange chromatography resin, cation exchange chromatography resin, affinity chromatography resin (e.g. comprising immobilized SPase specific antibodies) and hydrophobic interaction chromatography resin.
The SPase of the present invention may be immobilized (temporarily or covalently) on any carrier, preferably particles (e.g. beads), in particular chromatography resin, provided that the enzymatic activity of the enzyme is not affected in a way to change its substrate specificity or to reduce its activity to low conversion rates.
In a further embodiment of the invention the sucrose phosphorylase is used in the form of whole-cell, cell free extract, crude, purified or immobilized form.
The reaction of SPase proceeds with net retention of the anomeric configuration and occurs through a double displacement mechanism involving two configurationally inverting steps: cleavage of the carbon-oxygen bond of the glucosyl donor and formation of a covalent β-glucosyl-enzyme (β-Glc-E) intermediate; and reaction of the intermediate with phosphate to yield Glc 1-P. In a side reaction, the β-Glc-E intermediate may be intercepted by water, leading to hydrolysis. Hydrolytic conversion of sucrose is irreversible but proceeds nearly two orders of magnitude slower than the phosphorolytic reaction. SPase also catalyzes transglucosylation reactions which occur in competition with hydrolysis and whereby the β-Glc-E intermediate is attacked by external nucleophiles and new α-D-glucosides are produced.
Biochemical studies have shown that SPase is strictly specific for transferring a glucosyl moiety and does not tolerate structural modifications on the glucopyranosyl ring including epimerization and deoxygenation.
The glucosyl donor to be employed in the method of the present invention can be any one which serves as substrate for the transglycosylation reaction catalyzed by the SPase.
The list of known glucosyl donors for SPase is short: sucrose, Glc 1-P and α-D-glucose 1-fluoride. Among the three known glycosyl donors sucrose is a cheap and highly stable high-energy glucosyl donor and weakly hydrolyzed by SPase.
However, the glucosyl donor may also be selected from the group consisting of sucrose and analogues of sucrose in which the fructosyl moiety has been modified or substituted by another ketosyl residue, or further stable, activated glucosyl donors such as α-D-glucose-1-azide, and/or mixtures thereof.
One embodiment of the invention relates to a method for producing AA-2G, wherein the glucosyl donor is sucrose, Glc 1-P or α-D-glucose 1-fluoride, preferably the glucosyl donor is sucrose or Glc 1-P, more preferred sucrose.
By contrast, the specificity of SPase for glucosyl acceptors is comparably relaxed.
One embodiment of the invention relates to a method for producing AA-2G, wherein the glucosyl acceptor is ascorbic acid or functional variant thereof.
Stereochemically pure glucosylglycerol was obtained in high yields of ≥90% donor substrate converted and the concentration was close to 1 M (250 g/L) when the glycerol acceptor was typically ≤2.5-fold molar excess over sucrose (Goedl et al., Angew Chem Int Ed Engl. 2008; 47(52):10086-9). The acceptor promiscuity of different SPase enzymes determined by different research groups has been excellently reviewed by Goedl et al. (Biocatal Biotrans. 2010; 28(1):10-21). The optimum pH for glycosyl transfer reactions using SPase was from 6.5 to 7.5. Interestingly the optimum pH of 6.5 of sucrose phosphorylase (from Streptococcus mutans) for glucosylation of phosphate and hydroquinone was shifted to below 5.0 pH when acetic acid was used as glucosyl acceptor which indicates the requirement of protonated form of interacting group of acceptor for effective transfer of glucosyl unit.
Kwon et al. (Biotechnol Lett. 2007 April; 29(4):611-615) disclosed the possibility of producing AA-2G in one step from L-AA and sucrose using recombinantly produced Bifidobacterium longum sucrose phosphorylase. The concentrations of
In objective of the present invention was the glycosylation of
A further embodiment of the invention relates to the method of producing AA-2G, wherein the incubation step is carried out at a pH range of 4.0 to 7.0, or in a range of 4.0 to 6.5, or in a range of 4.5 to 6.5, or in a range of 4.8 to 6.2, or in a range of 5.0 to 5.5. Surprisingly, the site selectivity is strongly improved by working at a pH in the range of about 4.0 to 7.0, or at a pH in the range of about 4.5 to 6.0, or at a pH in the range of about 4.8 to 5.5, or at a pH of about 5.2. The reaction at an unsuitable pH would lead to poor site-selectivity. In a further embodiment of the invention the incubation step is carried out at a pH of about 5.2.
The pH of the reaction medium can be adjusted using simple organic and inorganic materials or using different types of buffer mixtures. The pH can be adjusted before initiating the reaction by enzyme addition. The pH can be also adjusted during the reaction to maintain the desired pH. The pH can be adjusted manually or in automatic way.
A further embodiment of the invention relates to the method of producing AA-2G, wherein the incubation step is carried out at a temperature range of about 30 to 70° C., or in a range of about 35 to 65° C., or in a range of about 40 to 60° C., or in a range of about 40 to 50° C. In a further embodiment of the incubation step is carried out at a temperature of about 40° C.
A further embodiment of the invention relates to the method of producing AA-2G, wherein the incubation step is performed for at least 24 h, preferably for at least 48 h, more preferred for at least 72 h.
A further embodiment of the invention relates to the method of producing AA-2G, wherein the glucosyl acceptor is used in 0.3 to 3 fold molar excess to glucosyl donor. In a further embodiment of the invention the glucosyl acceptor is used in 0.5 to 2.5 fold molar excess to glucosyl donor, or in 1.0 to 2 fold molar excess. In a further embodiment of the invention the glucosyl acceptor is used in 1.5 fold molar excess to glucosyl donor. In a further embodiment of the invention the glucosyl acceptor is ascorbic acid and the glucosyl donor is sucrose.
A further embodiment of the invention relates to a method of producing AA-2G, wherein the amount of sucrose phosphorylase in the reaction mixture is in the range of 1 U/mL to 10,000 U/mL, or in the range of 5 U/mL to 100 U/mL, or in the range of 10 U/mL to 50 U/mL, or in the range of 20 U/mL to 40 U/mL. In a further embodiment of the invention the sucrose phosphorylase is used in an amount of about 30 U/mL.
A further embodiment of the invention relates to a method of producing AA-2G, wherein additional sucrose phosphorylase and sucrose are added to the reaction mixture during incubation to maintain sucrose phosphorylase in the range of 1 U/mL to 10,000 U/mL, or in the range of 5 U/mL to 100 U/mL, or in the range of 10 U/mL to 50 U/mL, or in the range of 20 U/mL to 40 U/mL, or at about 30 U/mL and sucrose in the range of 100 to 2,000 mM, or in the range of 250 mM to 1,000 mM or about 800 mM.
A further embodiment of the invention relates to a method of producing AA-2G, wherein sucrose phosphorylase and sucrose are added simultaneously or at different time points to the reaction mixture to maintain the required amounts as described above.
The present invention is further illustrated by the following figures and Examples without being restricted thereto.
The Examples which follow are set forth to aid in the understanding of the invention but are not intended to, and should not be construed to limit the scope of the invention in any way. The Examples do not include detailed descriptions of conventional methods, e.g., cloning, transfection, and basic aspects of methods for expressing proteins in microbial host cells. Such methods are well known to those of ordinary skill in the art.
The E. coli BL21 host strain carrying pC21E vector with an insert of SPase gene under his-tag was used for the production of SPase. The gene was cloned under tact promoter system and was induced with IPTG. Little amount of culture from the glycerol stock was scratched with micropipette tip and inoculated into 50 mL of LB medium containing ampicillin (120 μg/mL). The flask was incubated at 30° C. overnight on shaker at 120 rpm for about 12 h. The overnight culture was inoculated into 200 mL LB medium containing ampicillin (120 μg/mL) to generate the OD600 of 0.01. The flask was incubated at 37° C., 120 rpm for several hours until the OD600 reach to 0.8 to 1.0. IPTG was added to the flask to make the final concentration of 1 mM. The flask was incubated on shaker at 25° C., 120 rpm for nearly 20 h. The cells were harvested by centrifugation at 5,000 rpm for 15 min. The supernatant was decanted and the pellet was washed with 100 mM citrate buffer pH 5.2 (5 mL of buffer for each 1 g of wet cell weight was used). The 1 g of wet cells was resuspended in 5 mL of lysis buffer (100 mM citrate buffer pH 5.2 containing 50 mM NaCl+1 mM EDTA+0.5 mM DTT). The suspension was passed 2 times through French press. The resulting cell lysate was centrifuged at 8,000×g to separate the soluble fraction from unbroken cells and cell debris. The SPase enzyme activity in the supernatant was quantified, aliquoted and stored at −20° C. for future use.
SPase activity was determined at 30° C. using a continuous coupled enzymatic assay, in which production of Glc 1-P from sucrose and inorganic phosphate is coupled to the reduction of NAD+ in the presence of phosphoglucomutase (PGM) and glucose 6-phosphate dehydrogenase (G6P-DH). The standard assay was performed essentially as described elsewhere in 50 mM potassium phosphate buffer, pH 7.0, containing 10 mM EDTA, 10 mM MgCl2 and 10 μM α-D glucose 1,6-bisphosphate. The reaction mixture contained 250 mM sucrose, 2.5 mM NAD+, 3 U/mL PGM, 3.4 U/mL NAD+-dependent G6P-DH and the enzyme solution in appropriate dilution. The formation of NADH with time was monitored spectrophotometrically at 340 nm. 1 Unit of SPase activity corresponds to the amount of enzyme that caused the reduction of 1 micromol of NAD+ per minute under the conditions described above. Protein concentrations were determined using the BioRad dye-binding method with bovine serum albumin as standard.
The reaction mixture, containing 1,200 mM of
The reaction mixture, containing 1,200 mM of
4 additional sucrose phosphorylases, representing the sequence diversity within the protein family, from Bifidobacterium adolescentis, Streptococcus mutans, Lactobacillus acidopholus, Leuconostoc mesenteroides have been evaluated. Homodimeric sucrose phosphorylases exhibited high site-selectivity in glycosylation of L-ascorbic acid at 2-OH resulting in AA-2G formation compared to monomeric type where a mixture of AA-2G and AA-6G were formed. Monomeric sucrose phosphorylases released AA-6G in substantial proportion of total product, whereas, with homodimeric proteins no AA-6G formed above the detection limit. However, the AA-2G synthesis at pH 5.2, which is essentially lacking at pH 7.5, was an essential characteristic of all sucrose phosphorylases tested.
Streptococcus mutans (SmSPase)
Lactobacillus acidopholus (LaSPase)
Bifidobacterium longum (BISPase)
Leuconostoc mesenteroides (LmSPase)
Bifidobacterium adolescentis (BaSPase)
| Number | Date | Country | Kind |
|---|---|---|---|
| 15186888.2 | Sep 2015 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2016/072586 | 9/22/2016 | WO | 00 |
