Mechanism of Asymmetric Production of d-Amino Acids from the Corresponding Hydantoins by Pseudomonas sp.

The mechanism of asymmetric production of d-amino acids from the corresponding hydantoins by Pseudomonas sp. AJ-11220 was examined by investigating the properties of the enzymes involved in the hydrolysis of dl-5-substituted hydantoins. The enzymatic production of d-amino acids from the corresponding hydantoins by Pseudomonas sp. AJ-11220 involved the following two successive reactions; the d-isomer specific hydrolysis, i.e., the ring opening of d-5-substituted hydantoins to d-form N-carbamyl amino acids by an enzyme, d-hydantoin hydrolase (d-HYD hydrolase), followed by the d-isomer specific hydrolysis, i.e., the cleavage of N-carbamyl-d-amino acids to d-amino acids by an enzyme, N-carbamyl-d-amino acid hydrolase (d-NCA hydrolase).

l-5-Substituted hydantoins not hydrolyzed by d-HYD hydrolase were converted to d-form 5- substituted hydantoins through spontaneous racemization under the enzymatic reaction conditions.

It was proposed that almost all of the dl-5-substituted hydantoins were stoichiometrically and directly converted to the corresponding d-amino acids through the successive reactions of d-HYD hydrolase and d-NCA hydrolase in parrallel with the spontaneous racemization of l-5-substituted hydantoins to those of dl-form.     

The Production of Xylitol,l-Arabinitol and Ribitol by Yeasts

The polyalcohol production from the pentoses such as d-xylose, l-arabinose and d-ribose by various genera and species of yeasts was examined. Candida polymorpha dissimilated aerobically these three pentoses and produced xylitol from d-xylose, l-arabinitol from l-arabinose and ribitol from d-ribose at good yield of 30~40% of sugar consumed. The result suggests that these polyalcohols would be major products from pentoses by yeasts, but some unidentified minor polyalcohols were also produced.     

Fermentative Production of l-Arginine

Most of the bacteria, which were examined for the sensitivity to l-arginine analogs (l-canavanine, l-homoarginine, d-arginine and arginine hydroxamate), were insensitive to the analogs at a concentration of 8 mg/ml. Corynebacterium glutamicum DSS-8 isolated as d-serine-sensitive mutant from an isoleucine auxotroph KY 10150, was found to be sensitive to d-arginine and arginine hydroxamate. Furthermore, DSS-8 produced l-arginine in a cultural medium. l-Arginine analog-resistant mutants were derived from DSS-8 by N-methyl-N′-nitro-N-nitrosoguanidine (NTG) treatment. Most of them were found to produce a large amount of l-arginine. An isoleucine revertant from one of these mutants produced 19.6 mg/ml of l-arginine in the medium containing 15% (as sugar) of molasses.

The mechanism of the sensitivity to l-arginine analogs and that of the production of l-arginine in the d-serine-sensitive mutant, DSS-8, were investigated. DSS-8 seems to be a mutant having increased permeability to d- and l-arginine.     

Biological Activities of Sex Hormone Produced by Tremella mesenteriea

d-Aminoacylase was found to be produced not only by S. olivaceus 62–3 isolated from soil but also by three strains of type culture of Streptomyces species. All four of these strains produced d-aminoacylase intracellularly only when an inducer was added to the culture medium. d-Amino acids or N-acetyl-d-amino acids were effective as inducers.

As S. tuirus showed the highest d-aminoacylase activity, the enzyme extract of this strain was subjected to further investigation to determine the optimal conditions for optical resolution of N-acetyl-dl-phenylglycine. Almost all contaminating l-aminoacylase in the enzyme extract could be eliminated by DEAE-Sephadex adsorption. d-Phenylglycine of 99.9% optical purity was obtained after complete hydrolysis of d-isomer with the use of d-aminoacylase solution.     

Effects of Glycine and d-Amino Acids on Growth of Various Microorganisms

Growth of various microorganisms in media containing high concentrations of glycine or d-amino acids was examined. Susceptibilities to glycine or d-amino acids differed among microorganisms, and the differences in susceptibility have no direct relation with Gram staining, morphological forms, and aerobic or anaerobic nature of the organisms. Certain glycine-resistant bacteria tested, which included Bacillus cereus, Staphylococcus aureus and Serratia marcescens, exhibited relatively high oxidative activities towards glycine. The inhibition of the growth of Escherichia coli by either glycine or d-amino acids, which included d-threonine, d-alanine and d-lysine, was reversed by l-alanine, partialy by l-serine, and not by l-lysine or l-threonine. These results suggest that the growth inhibition of microorganisms by d-amino acids was similar to that by glycine. The incorporation of l-alanine into E. coli cells which were preincubated with glycine was less than those of preincubated without glycine. Particularly, the incorporation into the cell wall fraction was most susceptible to glycine. An additive effect of penicillin and glycine was observed in the inhibition of cell wall biosynthesis as determined by the intracellular accumulation of N-acetylamino sugar compounds.     

Biosynthesis of polymalic acid in fermentation: advances and prospects for industrial application

Some microorganisms naturally produce β-poly(l-malic acid) (PMA), which has excellent water solubility, biodegradability, and biocompatibility properties. PMA has broad prospective applications as novel biopolymeric materials and carriers in the drug, food, and biomedical fields. Malic acid, a four-carbon dicarboxylic acid, is widely used in foods and pharmaceuticals, as a platform chemical. Currently, malic acid produced through chemical synthesis and is available as a racemic mixture of l- and d-forms. The d-form malic acid exhibits safety concerns for human consumption. There is extensive interest to develop economical bioprocesses for l-malic acid and PMA production from renewable biomass feedstocks. In this review, we focus on PMA biosynthesis by Aureobasidium pullulans, a black yeast with a large genome containing genes encoding many hydrolases capable of degrading various plant materials. The metabolic and regulatory pathways for PMA biosynthesis, metabolic engineering strategies for strain development, process factors affecting fermentation kinetics and PMA production, and downstream processing for PMA recovery and purification are discussed. Prospects of microbial PMA and malic acid production are also considered.     

Studies on Sugar-isomerizing Enzyme

A glucose isomerase which reversibly catalyzes the reaction between d-glucose and d-fructose was demonstrated in the cell-free extracts of a strain of Streptomyces sp. isolated from soil. The enzyme was produced when the strain was grown in the medium containing xylan or xylan-containing material such as wheat bran. A medium which consists of 3% of wheat bran, 2% of corn steep liquor and 0.024% of CoCl₂·6H₂O is recommendabie for the production of the glucose isomerase enzyme with the strain. With the enzyme, some conditions for the conversion of d-glucose to d-fructose were also studied. The method is very useful for the production of invert sugar from d-glucose and is now on the way to be applied to the practical use.     

l-Isoleucine Production by Analog-resistant Mutants Derived from Threonine-producing Strain of Corynebacterium glutamicum

A thiaisoleucine-resistant mutant, ASAT–372, derived from a threonine producer of Corynebacterium glutamicum, KY 10501, produced 5 mg/ml each of l-isoleucine and l-threonine. l-Isoleucine productivity of ASAT–372 was improved stepwise, with concurrent decrease in threonine production, by successively endowing it with resistivity to such substances as ethionine, 4-azaleucine and α-aminobutyric acid. The mutant strain finally selected, RAM–83, produced 9.7 mg/ml of l-isoleucine with a medium containing 10% (as sugar) molasses.

l-Isoleucine production was significantly affected by the concentration of ammonium sulfate in the fermentation medium. At 4% ammonium sulfate l-isoleucine production was enhanced whereas l-threonine production was suppressed. At 2% ammonium sulfate l-threonine production was stimulated while l-isoleucine production decreased.     

2-Keto-l-Gulonic Acid Fermentation

Fractionation of sorbitol metabolites in the culture liquid of Gluconobacter melanogenus IFO 3292 was examined by column chromatographic techniques. Ion exchange column chromatography of the culture supernatant allowed to divide the components of the metabolites into Fractions I, II, III and IV. Paperelectrophoretic and paperchromatographic analyses of these fractions revealed that Fractions I, II, III and IV contained neutral sugar, hexonic acids, 5-ketohexonic acid and 2-ketohexonic acids, respectively.

The neutral sugar in Fraction I, the 5-ketohexonic acid in Fraction III and the 2-ketohexonic acids in Fraction IV were isolated and determined to be l-sorbose, 5-keto-d- mannonic, 2-keto-d-gluconic and 2-keto-l-gulonic acids, respectively, from their physical properties. In Fraction II were contained two different hexonic acids, one of which was identified to be l-idonic acid by the aid of substrate specificity of a hexonic acid dehydrogenase of Pseudomonas aeruginosa, and the other was determined to be d-mannonic acid as the phenylhydrazide derivative.     

The Production of Xylitol and d-Xylonic Acid by Yeast

Pichia quercibus Phaff et Knapp produced xylitol and d-xylonic acid by aerobic dissimilation of d-xylose at good yield of 40% of sugar consumed. The products were isolated from the fermented broth and identified. It would be interesting that both of xylitol, a reduction product of d-xylose, and d-xylonic acid, an oxidation product, are accumulated in the fermented broth.     

2-Keto-l-gulonic Acid Fermentation

A number of bacterial strains from type culture collections and natural sources were examined in their metabolic characteristics toward sorbitol and l-sorbose.

Paper chromatographic analyses of sorbitol and l-sorbose metabolites obtained from the cultures of various bacteria revealed that the organisms producing 2-keto-l-gulonic acid from sorbitol were merely found in the genera Acetobacter, Gluconobacter and Pseudomonas, whereas those producing the acid from l-sorbose were distributed in the twelve genera of bacteria: Acetobacter, Alcaligenes, Aerobacter, Azotobacter, Bacillus, Escherichia, Gluconobacter, Klebsiella, Micrococcus, Pseudomonas, Serratia and Xanthomonas.

G. melanogenus, which was characterized by excellent production of 2-keto-l-gulonic acid from sorbitol, also formed several other sugars and sugar acids as the sorbitol metabolites. These compounds were identified to be d-fructose, l-sorbose, d-mannonic acid, L-idonic acid, 2-keto-d-gluconic acid and 5-keto-d-mannonic acid, respectively, by means of two-dimensional paper chromatography.

Bacteria producing 2-keto-l-gulonic acid from sorbitol were usually isolated from fruits but not from soil.     

The Determination of d-Glutamic Acid and d-Aspartic Acid by Means of a New Oxidase

The fractional determination of d-glutamic and d-aspartic acids using the enzyme preparation of Aspergillus ustus strain f. was studied. In the first part of this paper, the procedure of enzyme preparation, the effect of sodium chloride on enzyme activity, and a new device for the fractional determination of d-glutamic and d-aspartic acids are described. In the latter part, the contents of d-glutamic and d-aspartic acids of cancer and normal tissues are estimated. However, it was found that the cancer tissues are not characterized by the presence of d-glutamic acid in opposition to Kögl’s claim.     

Biochemical Aspects of 2-Keto-l-gulonate Accumulation from 2,5-Diketo-d-gluconate by Corynebacterium sp. and Its Mutants

Corynebacterium sp. SHS 0007 accumulated 2-keto-l-gulonate and 2-keto-d-gluconate simultaneously with 2,5-diketo-d-gluconate utilization. This strain, however, possibly metabolized 2,5- diketo-d-gluconate through two pathways leading to d-gluconate as a common intermediate: via 2- keto-d-gluconate, and via 2-keto-l-gulonate, l-idonate and 5-keto-d-gluconate. A polysaccharide- negative, 2-keto-l-gulonate-negative and 5-keto-d-gluconate-negative mutant produced only calcium 2-keto-l-gulonate from calcium 2,5-diketo-d-gluconate, in a 90.5 mol% yield. The addition of a hydrogen donor such as d-glucose was essential for its production. This mutant possessed the direct oxidation route of d-glucose to d-gluconate, the pentose cycle pathway and a possible Embden-Meyerhof-Parnas pathway, indicating that d-glucose was metabolized through these three pathways and provided NADPH for the reduction of 2,5-diketo-d-gluconate.     

Production of d-lactate using a pyruvate-producing Escherichia coli strain

To generate an organism capable of producing d-lactate, NAD⁺-dependent d-lactate dehydrogenase was expressed in our pyruvate-producing strain, Escherichia coli strain LAFCPCPt-accBC-aceE. After determining the optimal culture conditions for d-lactate production, 18.4 mM d-lactate was produced from biomass-based medium without supplemental mineral or nitrogen sources. Our results show that d-lactate can be produced in simple batch fermentation processes.     

Studies on Metabolism of Pyrrolidone Carboxylic Acid in Bacteria

The present investigation is concerned with l-glutamic acid production in the presence of pyrrolidone carboxylic acid and glucose in Bacillus megaterium st. 6126. This strain does not grow on dl-pyrrolidone carboxylic acid (dl-PCA)¹⁾ as the sole source of carbon and nitrogen. The optimal concentration of yeast extract required for the maximal production of l-glutamic acid was 0.005% under the conditions used. As the yeast extract concentration was increased, growth increased proportionally; but the l-glutamic acid production did not exceed the control’s to which glucose and ammonium chloride had been added. l-Glutamic acid produced by both growing cultures and resting cells was derived from glucose and ammonium salt of dl-PCA. Isotope experiments suggested that the l-glutamic acid produced was partially derived from ammonium salt of dl-PCA in the growing culture which had been supplemented with d-glucose-U-¹⁴C or dl-PCA-1-¹⁴C and that ammonium salt of dl-PCA was consumed as the source of nitrogen and carbon for l-glutamic acid.     

The Acceptor Specificity of Amylomaltase from Escherichia coli IFO 3806

The acceptor specificity of amylomaltase from Escherichia coli IFO 3806 was investigated using various sugars and sugar alcohols. d-Mannose, d-glucosamine, N-acetyl- d-glucosamine, d-xylose, d- allose, isomaltose, and cellobiose were efficient acceptors in the transglycosylation reaction of this enzyme. It was shown by chemical and enzymic methods that this enzyme could transfer glycosyl residues only to the C4-hydroxyl groups of d-mannose, iY-acetyl- d-glucosamine, d-allose, and d-xylose, producing oligosaccharides terminated by 4–0-α-d-glucopyranosyl-d-mannose, 4–0-α-d-glucopyranosyl-yV-acetyl-d-glucosamine, 4-O-α-d-glucopyranosyl-d-allose, and 4–0-α-d-gluco- pyranosyl-d-xylose at the reducing ends, respectively.     

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.     

Taurine Levels in Some Tissues of Yellowtail (Seriola quinqueradiata) and Mackerel (Scomber japonicus)

The mechanism of stereospecific production of l-amino acids from the corresponding 5-substituted hydantoins by Bacillus brevis AJ-12299 was studied. The enzymes involved in the reaction were partially purified by DEAE-Toyopearl 650M column chromatography and their properties were investigated. The conversion of dl-5-substituted hydantoins to the corresponding l-amino acids consisted of the following two successive reactions. The first step was the ring-opening hydrolysis to N-carbamoyl amino acids catalyzed by an ATP dependent l-5-substituted hydantoin hydrolase. This reaction was stereospecific and the N-carbamoyl amino acid produced was exclusively the l-form. N-Carbamoyl-l-amino acid was also produced from the d-form of 5-substituted hydantoin, which suggests that spontaneous racemization occurred in the reaction mixture. In the second step, N-carbamoyl-l-amino acid was hydrolyzed to l-amino acid by an N-carbamoyl-l-amino acid hydrolase, which was also an l-specific enzyme. The ATP dependency of the l-5-substituted hydantoin hydrolase was supposed to be the limiting factor in the production of l-amino acids from the corresponding 5-substituted hydantoins by this bacterium.     

Mechanisms of Browning Degradation of d-Fructose in Special Comparison with d-Glucose-Glycine Reaction

Degradation mechanisms of d-fructose by the interaction with amino acids or organic acids in aqueous solution at initial pH 5.5 heated at 100°C were investigated and a substantial difference in mechanisms between fructose degradation and glucose-glycine reaction was presented. d-Fructose browned more intensely than did d-glucose in lower concentration of glycine and/or in earier stage of reaction period. By catalytic action of carboxylate anions without any condensation with amino groups, d-fructose was decomposed to 3-deoxy-d-erythrohexosulose, 5-(hydroxymelhyl)-2-furaldehyde, and a less amount of pyruval-dehyde through caramelization. It was considered that the main path of fructose degradation was 1,2-enolization but 2,3-enolization would also occur to a little extent.     

Simultaneous determination of primary and secondary d- and l-amino acids by reversed-phase high-performance liquid chromatography using pre-column derivatization with two-step labelling method

This work describes a method for the simultaneous determination of primary d- and l-amino acids and secondary amino acids such as d- and l-proline. In order to remove interferences in the simultaneous determination of primary and secondary amines, the primary amines were derivatized with o-phthalaldehyde/N-acetyl-l-cysteine (OPA/NAC) and subsequently with 1-(9-fluorenyl)ethyl chloroformate (FLEC) for secondary amines, in a pre-column separation derivatization technique. These fluorescent diastereomers of the amino acids were obtained within 3 min at room temperature and determined simultaneously by changing wavelengths during analysis in a single eluting run in the high-performance liquid chromatography column. This method, referred to as the “two-step labelling method,” is effective for the simultaneous determination of d- and l-amino acids.