Kinetics of Thermostable Alanine Racemase of Bacillus stearothermophilus

Unlabeled D- and L-alanine were racemized in deuterium oxide with an alanine racemase of Bacillus stearothermophilus at saturated concentration of substrate, and various p²H and temperature. Samples of the solution were taken at intervals, and all alanine isomers in the samples were transformed into a mixture of diastereomeric derivatives of methyl N-(–)-camphanylalaninate. Their ratio was measured on a GC-Mass, and the relative rate was calculated at the initial stage of the reaction. There was little difference in the decrease rate of the optical rotation between the enantiomers. Internal proton-transfer to the antipode was almost zero for either substrate. The α-hydrogen was abstracted 1.2–2.3 times faster from D-alanine than from L-alanine. D-Alanine gave an almost even mixture of deuterium labeled D- and L-alanine, while L-alanine gave a mixture of labeled D- and L-alanine at a ratio of 3:1. These results suggest the racemase builds two different bases in the active site. The base for D-alanine may be closer to the enzyme surface, and that for L-alanine inside.     

Practical Preparation of D-Galactosyl-β1→4-L-rhamnose Employing the Combined Action of Phosphorylases

D-Galactosyl-β1→4-L-rhamnose (GalRha) was produced enzymatically from 1.1 M sucrose and 1.0 M L-rhamnose by the concomitant actions of four enzymes (sucrose phosphorylase, UDP-glucose-hexose 1-phosphate uridylyltransferase, UDP-glucose 4-epimerase, and D-galactosyl-β1→4-L-rhamnose phosphorylase) in the presence of 1.0 mM UDP-glucose and 30 mM inorganic phosphate. The accumulation of GalRha in 1 liter of the reaction mixture reached 230 g (the reaction yield was 71% from L-rhamnose). Sucrose and fructose in the reaction mixture were removed by yeast treatment, but isolation of GalRha by crystallization after yeast treatment was unsuccessful. Finally, 49 g of GalRha was isolated from part of the reaction mixture with yeast treatment by gel-filtration chromatography.     

Mutant of Escherichia coli Tolerant to the Lysis Induced by Cephalexin

2,3-Diaminopropionate ammonia-lyase (DAPAL), which catalyzes α,β-elimination of 2,3-diaminopropionate regardless of its stereochemistry, was purified from Salmonella typhimurium. We cloned the Escherichia coli ygeX gene encoding a putative DAPAL and purified the gene product to homogeneity. The protein obtained contained pyridoxal 5′-phosphate and was composed of two identical subunits with a calculated molecular weight of 43,327. It catalyzed the α,β-elimination of both D- and L-2,3-diaminopropionate. The results confirmed that ygeX encoded DAPAL. The enzyme acted on D-serine, but its catalytic efficiency was only 0.5% that with D-2,3-diaminopropionate. The enzymologic properties of E. coli DAPAL resembled those of Salmonella DAPAL, except that L-serine, D- and L-β-Cl-alanine were inert as substrates of the enzyme from E. coli. DAPAL had significant sequence similarity with the catalytic domain of L-threonine dehydratase, which is a member of the fold-type II group of pyridoxal phosphate enzymes, together with D-serine dehydratase and mammalian serine racemase.     

Preparation of Optically Active Allothreonine by Separating from a Diastereoisomeric Mixture with Threonine

A simple procedure is described to obtain D- and L-allothreonine (D- and L-aThr). A mixture of N-acetyl-D-allothreonine (Ac-D-aThr) and N-acetyl-L-threonine (Ac-L-Thr) was converted to a mixture of their ammonium salts and then treated with ethanol to precipitate ammonium N-acetyl-L-threoninate (Ac-L-Thr·NH₃) as the less-soluble diastereoisomeric salt. After separating Ac-L-Thr·NH₃ by filtration, Ac-D-aThr obtained from the filtrate was hydrolyzed in hydrochloric acid to give D-aThr of 80% de, recrystallized from water to give D-aThr of >99% de. L-aThr was obtained from a mixture of the ammonium salts of Ac-L-aThr and Ac-D-Thr in a similar manner.     

New Polar Constituents in the Pupae of the Silkworm Bombyx mori L. (II): Developmental Changes of the Constituents

A correlation between the quantitative changes in L-methionine analogs, the ratio of D-serine/L-serine during the pupal stage, and metamorphosis was observed. The glycoside appearing at low blood sugar values during the pupal stage was isolated and characterized as D-glucosyl-L-tyrosine. ¹H-NMR indicated the appearance and increase of this glycoside, and Mirrorcle Ray CV4 equipment was used to take X-ray pictures of the pupal bodies. The results indicate that γ-cyclic di-L-glutamate and L-methionine sulfone might be concerned with ammonia assimilation in the pupae, and that D-glucosyl-L-tyrosine served as a switch for the fatty acid (pupal oil) dissimilation hybrid system.     

Structure of Rugulovasine A,B and their Derivatives

Culture conditions for the preparation of cells containing high tyrosine phenol lyase activity were studied with Erwinia herbicola ATCC 21434. Adding pyridoxine to the medium enhanced enzyme formation, suggesting that it was utilized as a precursor of the coenzyme, pyridoxal phosphate. Glycerol plus succinic acid; amino acids, such as, DL-methionine, DL-alanine and glycine; and metallic ion, ferrous ion promoted enzyme formation as well as cell growth. Adding L-tyrosine, as inducer, to the culture medium was essential for enzyme formation. However, when large amounts of L-tyrosine were added, the enzyme formation was repressed by the phenol liberated from L-tyrosine. In fact, formation of the enzyme was enhanced by removing phenol during cultivation. L(D)-Phenylalanine or phenylpyruvic acid had a synergistic effect on the induction of enzyme by L-tyrosine.

Cells with high enzyme activity were prepared by growing cells at 28°C for 28 hr in a medium containing 0.2% L-tyrosine, 0.2% KH₂PO₄, 0.1% MgSO₄7H₂O, 0.001% FeSO_4·7H₂O, 0.01% pyridoxine-HC1, 0.6% glycerol, 0.5% succinic acid, 0.1% DL-methionine, 0.2% DL-alanine, 0.05% glycine, 0.1% L-phenylalanine and 120 ml/liter hydrolyzed soybean protein in tap water with the pH controlled at 7.5 throughout cultivation.     

Enzymatic Quantification of L-Tartrate in Wines and Grapes by Using the Secondary Activity of D-Malate Dehydrogenase

L-Tartrate in wines and grapes was enzymatically quantified by using the secondary activity of D-malate dehydrogenase (D-MDH). NADH formed by the D-MDH reaction was monitored spectrophotometrically. Under the optimal conditions, L-tartrate (a 1.0 mM sample solution) was fully oxidized by D-MDH in 30 min. A linear relationship was obtained between the absorbance difference and the L-tartrate concentration in the range of a 0.02-1.0 mM sample solution with a correlation coefficient of 0.9991. The relative standard deviation from ten measurements was 1.71% at the 1.0 mM sample solution level. The proposed method was compared with HPLC, and the values determined by both methods were in good agreement.     

Acceptor Specificity of Cyclodextrin Glycosyltransferase from Bacillus stearothermophilus and Synthesis of α-D-Glucosyl O-β-D-galactosyl-(1→4)-β-D-glucoside

Bacillus stearothermophilus CGTase had a wider acceptor specificity than Bacillus macerans CGTase did and produced large amounts of transfer products of various acceptors such as D-galactose, D-mannose, D-fructose, D- and L-arabinose, d- and L-fucose, L-rhamnose, D-glucosamine, and lactose, which were inefficient acceptors for B. macerans CGTase. The main component of the smallest transfer products of lactose was assumed to be α-D-glucosyl O-β-D-galactosyl-(l→4)-β-D-glucoside.     

Effects of Acetylation with Acetic Anhydricle

1. L-Asparaginase (EC 3.5.1.1) from Escherichia coli A–l–3 was acetylated using acetic anhydride as a modifying chemical. The fully acetylated L-asparaginase retained 60% of the activity of the unmodified L-asparaginase.

2. The acetylated L-asparaginase hydrolyzed D-asparagine and L-glutamine as well as L-asparagine in the same ratio as the unmodified L-asparaginase did.

3. However, the effects of pH on the activity of the acetylated L-asparaginase showed very interesting differences from that of L-asparaginase. On the other hand, both L-asparaginase and the acetylated L-asparaginase exhibited similar pH activity curves on L-glutamine hydrolysis.

4. The acetylated L-asparaginase was found to become more stable against acid or heat in the presence of L-aspartate than in its absence in the same manner as L-asparaginase was.

     

Structures and Properties of a Diastereoisomeric Molecular Compound of (2S,3S)- and (2R,3S)-N-Acetyl-2-amino-3-methylpentanoic Acids

An X-ray crystal structural analysis revealed that (2S,3S)-N-acetyl-2-amino-3-methylpentanoic acid (N-acetyl-L-isoleucine; Ac-L-Ile) and (2R,3S)-N-acetyl-2-amino-3-methylpentanoic acid (N-acetyl-D-alloisoleucine; Ac-D-aIle) formed a molecular compound containing one Ac-L-Ile molecule and one Ac-D-aIle molecule as an unsymmetrical unit. This molecular compound is packed with strong hydrogen bonds forming homogeneous chains consisting of Ac-L-Ile molecules or Ac-D-aIle molecules and weak hydrogen bonds connecting these homogeneous chains in a fashion similar to that observed for Ac-L-Ile and Ac-D-aIle. Recrystallization of an approximately 1:1 mixture of Ac-L-Ile and Ac-D-aIle from water gave an equimolar molecular compound due to its lower solubility than that of Ac-D-aIle or especially Ac-L-Ile. The results suggest that the equimolar mixture of Ac-L-Ile and Ac-D-aIle could be obtained from an Ac-L-Ile-excess mixture by recystallization from water.     

Culture Conditions for the Production of l-Glutamic Acid from n-Paraffins by Glycerol Auxotroph GL-21

A novel process for the microbial production of l-glutamic acid on an industrial scale was successfully established by using a glycerol auxotroph.

The most suitable carbon source for producing L-glutamic acid was n-paraffins (C₁₃–C₁₅). The production of L-glutamic acid was not affected by a large amount of biotin or oleic acid in the absence of penicillin, and occurred maximally at the glycerol concentration of 0.02% at pH 6.6. The most effective temperature was 28°C.

Under optimal conditions in a 200 liter fermentor, the mutant produced 72 g/liter of L-glutamic acid. On the other hand, the parent produced 53 g/liter of L-glutamic acid in the presence of penicillin.

It is believed that the low productivity of L-glutamic acid by the parent strain was mainly due to the occurrence of the marked decrease in the viable cell counts at the later phase of the fermentation caused by the action of penicillin added.     

Efficient Production and Purification of Extracellular 1,2-α-L-Fucosidase of Bacillus sp. K40T

When Bacillus sp. K40T was cultured in the presence of L-fucose, 1,2-α-L-fucosidase was found to be produced specifically in the culture fluid. The enzyme was purified to homogeneity from a culture containing only L-fucose by chromatography on hydroxylapatite and chromatofocusing. The molecular weight of the enzyme was estimated to be 200,000 by gel filtration on Sephadex G-200. The enzyme was optimal at pH 5.5–7.0 and was stable at pH 6.0–9.0. The enzyme hydrolyzed the α(1 → 2)-L-fucosidic linkages in various oligosaccharides and glycoproteins such as lacto-N-fucopentaose (LNF)-I 〈O-α-L-fucose-(1 → 2)-O-β-D-galactose-(1 → 3)-N-acetyl-O-β-D-glucosamine-(1 → 3)-O-β-D-galactose-(1 → 4)-D-glucose〉, porcine gastric mucin, and porcine submaxillary mucin. The enzyme also acted on human erythrocytes, which was confirmed by the hemagglutination test using Ulex anti-H lectin. The enzyme did not hydrolyze α(1 → 3)-, α-(1 → 4)- and α-(1 → 6)-L-fucosidic linkages in LNF-III 〈O-β-D-galactose-(1 → 4)[O-α-L-fucose-(1 → 3)-]-N-acetyl-O-β-D-glucosamine-(1 → 3)-O-β-D-galactose-(1 → 4)-D-glucose〉, LNF-II 〈O-β-D-galactose-(1 → 3)[O-α-L-fucose-(1 → 4)-]-N-acetyl-O-β-D-galactose-(1 → 3)-O-β-D-galactose-(1 → 4)-D-glucose〉 or 6-O-α-L-fucopyranosyl-N-acetylglucosamine.     

Production of L-Threonine by Mutants Resistant to Both α-Amino-β-hydroxyvaleric Acid and S-(2-Aminoethyl)-L-cysteine Derived from Brevibacterium flavum

Growth of Brevibacterium flavum FA-1-30 and FA-3-115, L-lysine producers derived from Br. flavum No. 2247 as S-(2-aminoethyl)-L-cysteine (AEC) resistant mutants, was inhibited by α-amino-β-hydroxyvaleric acid (AHV), and this inhibition was reversed by L-threonine. All the tested AHV resistant mutants derived from FA-1-30 accumulated more than 4 g/liter of L-threonine in media containing 10% glucose, and the best producer, FAB-44, selected on a medium containing 5 mg/ml of AHV produced about 15 g/liter of L-threonine. Many of AHV resistant mutants selected on a medium containing 2 mg/ml of AHV accumulated L-lysine as well as L-threonine, AHV resistant mutants derived from FA-3-115 produced 10.7 g/liter of L-threonine maximally. AEC resistant mutants derived from strains BB–82 and BB–69, which were L-threonine producers derived from Br. flavum No. 2247 as AHV resistant mutants, did not produce L-threonine more than the parental strains, and moreover, many of them did not accumulate L-threonine but L-lysine. Homoserine dehydrogenases of crude extracts from L-threonine producing AHV resistant mutants derived from FA–1–30 and FA–3–115 were insensitive to the inhibition by L-threonine, and those of L-threonine and L-lysine producing AHV resistant mutants from FA–1–30 were partially sensitive.

Correlation between L-threonine or L-lysine production and regulations of enzymatic activities of the mutants was discussed.     

Selective,High Conversion of D-Glucose to 5-Keto-D-gluoconate by Gluconobacter suboxydans

Selective, high-yield production of 5-keto-D-gluconate (5KGA) from D-glucose by Gluconobacter was achieved without genetic modification. 5KGA production by Gluconobacter suffers byproduct formation of 2-keto-D-gluconate (2KGA). By controlling the medium pH strictly in a range of pH 3.5–4.0, 5KGA was accumulated with 87% conversion yield from D-glucose. The pH dependency of 5KGA formation appeared to be related to that of gluconate oxidizing activity.     

Isolation and Characterization of Thermotolerant Gluconobacter Strains Catalyzing Oxidative Fermentation at Higher Temperatures

Thermotolerant acetic acid bacteria belonging to the genus Gluconobacter were isolated from various kinds of fruits and flowers from Thailand and Japan. The screening strategy was built up to exclude Acetobacter strains by adding gluconic acid to a culture medium in the presence of 1% D-sorbitol or 1% D-mannitol. Eight strains of thermotolerant Gluconobacter were isolated and screened for D-fructose and L-sorbose production. They grew at wide range of temperatures from 10°C to 37°C and had average optimum growth temperature between 30-33°C. All strains were able to produce L-sorbose and D-fructose at higher temperatures such as 37°C. The 16S rRNA sequences analysis showed that the isolated strains were almost identical to G. frateurii with scores of 99.36-99.79%. Among these eight strains, especially strains CHM16 and CHM54 had high oxidase activity for D-mannitol and D-sorbitol, converting it to D-fructose and L-sorbose at 37°C, respectively. Sugar alcohols oxidation proceeded without a lag time, but Gluconobacter frateurii IFO 3264^T was unable to do such fermentation at 37°C. Fermentation efficiency and fermentation rate of the strains CHM16 and CHM54 were quite high and they rapidly oxidized D-mannitol and D-sorbitol to D-fructose and L-sorbose at almost 100% within 24 h at 30°C. Even oxidative fermentation of D-fructose done at 37°C, the strain CHM16 still accumulated D-fructose at 80% within 24 h. The efficiency of L-sorbose fermentation by the strain CHM54 at 37°C was superior to that observed at 30°C. Thus, the eight strains were finally classified as thermotolerant members of G. frateurii.     

Batch and fed-batch bioreactor studies for the enhanced production of glutaminase-free L-asparaginase from Pectobacterium carotovorum MTCC 1428

The effect of dissolved oxygen (DO) level and pH (controlled/uncontrolled) was first studied to enhance the production of novel glutaminase-free L-asparaginase by Pectobacterium carotovorum MTCC 1428 in a batch bioreactor. The optimum level of DO was found to be 20%. The production of L-asparaginase was found to be maximum when pH of the medium was maintained at 8.5 after 12?h of fermentation. Under these conditions, P. carotovorum produced 17.97?U/mL of L-asparaginase corresponding to the productivity of 1497.50?U/L/h. The production of L-asparaginase was studied in fed-batch bioreactor by feeding L-asparagine (essential substrate for production) and/or glucose (carbon source for growth) at the end of the reaction period of 12?h. The initial medium containing both L-asparagine and glucose in the batch mode and L-asparagine in the feeding stream was found to be the best combination for enhanced production of glutaminase-free L-asparaginase. Under this condition, the L-asparaginase production was increased to 38.8?U/mL, which corresponded to a productivity of 1615.8?U/L/h. The production and productivity were increased by 115.8% and 7.9%, respectively, both of which are higher than those obtained in the batch bioreactor experiments.     

Synthesis of L-Tyrosine or 3,4-Dihydroxyphenyl-L-alanine from DL-Serine and Phenol or Pyrocathechol

Reaction conditions for the synthesis of L-tyrosine or L-dopa from DL-serine and phenol or pyrocatechol were studied with intact cells of Erwinia herbicola (ATCC 21434) containing high tyrosine phenol lyase activity. The optimum pH for this reaction was around 8.0, and the optimum temperature range was between 37~40°C for the synthesis of L-tyrosine and between 15~25°C for that of L-dopa. Sodium sulfite and EDTA were added to protect the synthesized L-dopa from decomposition. As high concentrations of phenol or pyrocatechol denatured the enzyme, each substrate was fed to maintain the optimum concentration during incubation.

The reaction mixture (100 ml) containing 4.0 g of DL-serine, 1.0 g of phenol or 0.7 g of pyrocatechol, 0.5 g of ammonium acetate and the cells, was incubated. During incubation, phenol or pyrocatechol was fed at intervals to maintain the substrate at the initial concentration. 5.35 g of L-tyrosine or 5.10 g of L-dopa was synthesized in 100 ml of the reaction mixture.     

Structure-Based Modification of D-Alanine-D-Alanine Ligase from Thermotoga maritima ATCC 43589 for Depsipeptide Synthesis

Depsipeptides are peptide-like polymers consisting of amino acids and hydroxy acids, and are expected to be new functional materials for drug-delivery systems and polymer science. In our previous study, D-alanyl-D-lactate, a type of depsipeptide, was enzymatically synthesized using D-alanine-D-alanine ligase from Thermotoga maritima ATCC 43589 (TmDdl) by Y207F substitution. Thereafter, in this study, further mutagenesis was introduced, based on structural comparison between TmDdl and a well-characterized D-alanine-D-alanine ligase from Escherichia coli. The S137A/Y207F mutant showed higher D-alanyl-D-lactate and lower D-alanyl-D-alanine synthesizing activity than the Y207F mutant. This suggests that substitution at the S137 residue contributes to product selectivity. Saturated mutagenesis on S137 revealed that the S137G/Y207F mutant showed the highest D-alanyl-D-lactate synthesizing activity. Moreover, the mutant showed broad substrate specificity toward D-amino acid and recognized D-lactate and D,L-isoserine as substrates. On the basis of these characteristics, various depsipeptides can be produced using S137G/Y207F-replaced TmDdl.     

Stereoselective Incorporation of Isoleucine into Cypridina Luciferin in Cypridina hilgendorfii (Vargula hilgendorfii)

The emission of light in the marine ostracod Cypridina hilgendorfii (presently Vargula hilgendorfii) is produced by the Cypridina luciferin-luciferase reaction in the presence of molecular oxygen. Cypridina luciferin has an asymmetric carbon derived from isoleucine, and the absolute configuration is identical to the C-3 position in L-isoleucine or D-alloisoleucine. To determine the stereoselective incorporation of the isoleucine isomers (L-isoleucine, D-isoleucine, L-alloisoleucine, and D-alloisoleucine), we synthesized four ²H-labeled isoleucine isomers and examined their incorporation into Cypridina luciferin by feeding experiments. Judging by these results, L-isoleucine is predominantly incorporated into Cypridina luciferin. This suggests that the isoleucine unit of Cypridina luciferin is derived from L-isoleucine, but not from D-alloisoleucine.