Studies on the Behaviors of Impurities on the Crystallization of l-Glutamic Acid

The behaviors of impurities on the crystallizations of the free acid and the hydrochloride, monosodium, zinc, calcium and barium salts of l-glutamic acid were examined, and a tendency was recognized that coexisting impurities were apt to be taken into the crystals when the crystallization proceeded from the zwitterion, i.e., Glu.^± or The adsorption of l-tyro-sine was compared when l, d and dl-glutamic acid were crystallized with coexistence of l-tyrosine, and an effect of more or less extent of steric configuration on its behavior could be recognized.     

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.     

Cultural Conditions for l-Leucine Production by Strain No. 218, a Mutant of Brevibacterium lactofermentum 2256

The excellent l-leucine producing mutant No. 218, derived from a biotin requiring glutamic acid producing strain, is methionine and isoleucine auxotrophic. A suboptimum growth condition made by adding a limiting amount of isoleucine was necessary for the maximum production of l-leucine. On the other hand, methionine was indifferent to the productivity if sufficiently supplied for growth.

Biotin of more than 50 μg/liter caused the accumulation of l-leucine; less than 50 μg/liter, however, gave a drastic change in accumulation pattern from l-leucine to l-glutamic acid. Strain No. 218 produced 28 mg/ml of l-leucine after 72 hr cultivation when 13 % glucose was supplied as a carbon source, thus giving the yield of 21.6%.

Effects on l-leucine production of concentrations of inorganic salts, pH, temperature and aeration were also investigated.     

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.     

Metabolism of l-Theanine,d-Theanine and the Related Compounds in Bacteria

Some strains of Pseudomonas was found capable of utilizing l-theanine or d-theanine as a sole nitrogen and carbon source. The cell-free extract catalyzes the hydrolysis of the amide group of the compounds and the hydrolase activity was influenced remarkably by the nitrogen source in the medium. l-Theanine and d-theanine were hydrolyzed to yield stoichiometrically l-glutamic acid and d-glutamic acid, respectively, and ethylamine, which were isolated from the reaction mixture and identified.

The theanine hydrolase of Pseudomonas aeruginosa was purified approximately 200-fold. It was shown that the activities of l-theanine hydrolase, d-theanine hydrolase and the heat-stable l-glutamine hydrolase and d-glutamine hydrolase are ascribed to a single enzyme, which may be regarded as a γ-glutamyltransferase from the point of view of the substrate specificity and the properties. This theanine hydrolase catalyzed the transfer of γ-glutamyl moiety of the substrates and glutathione to hydroxylamine. l-Glutamine and d-glutamine were hydrolyzed by the theanine hydrolase and also by the heat-labile enzyme of the same strain of Pseudomonas aeruginosa, whose properties resembled the common glutaminase.     

Induction of Antibiotic Formation in Streptomyces sp. No. 362 by the Change of Cellular Fatty Acid Spectrum

Microorganisms which require oleic acid for the formation of antibiotics were screened. Streptomyces sp. No. 362, one of the selected organisms, produced antimicrobial substances only when oleic acid, palmitic acid or the high concentration of l-glutamic acid (or l-glutamine) was supplemented to the medium. The cellular fatty acid composition was changed by the supplement of these fatty acids, but not by l-glutamic acid (or l-glutamine). Antibiotic-producing cells had about 4 to 10 times larger amino acid pools, especially l-glutamic acid pool, and hexosamine pools. The ability for l-glutamate uptake of cells grown in the oleic or palmitic acid supplemented medium was markedly enhanced and the efflux of the accumulated l-glutamate was reduced. The antibiotic produced by this strain was identified as one of the streptothricin-group antibiotics and the role of these additives in the antibiotic formation is discussed.     

Studies on the Polymorphism of l-Glutamic Acid

The effects on the polymorphic crystallization of l-glutamic acid were examined of many substances including amino acids, inorganic salts, surface active agents, and sodium salt or hydrochloride of l-glutamic acid, when contained in the mother liquor.

The co-existence of amino acids, especially of l-aspartic acid, l-phenylalanine, l-tyrosine, l-lcucine and l-cystine contributed to the crystallization of l-glutamic acid in α-form, and these amino acid showed an inhibitory action on the transition of α-crystals as the solid phase in the aqueous solution, to β-crystals.

In the presence of a large amount of l-glutamate or the hydrochloride at the time of nucleation of l-glutamic acid, mostly β-crystals appeared even in the presence of the amino acids named above.     

Isolation and Identification of O-Acetyl and 12-Hydroxyradiclonic Acids

An N-acetylglutamate-acetylornithine acetyltransferase-deficient arginine-requiring mutant AA–1, was derived from an l-arginine producer of Corynebacterium glutamicum. It accumulated a large amount (30 mg per ml) of l-glutamic acid and a small amount (1.2 mg per ml) of N^α-acetylornithine, an intermediate of arginine biosynthesis, in the culture medium.

The production of N^α-acetylornithine by AA–1 was not affected by the concentration of l-arginine in the medium, whereas that of l-glutamic acid was inhibited by a high concentration of l-arginine in the medium containing excess biotin.     

Production of l-Valine by 2-Thiazolealanine Resistant Mutants Derived from Glutamic Acid Producing Bacteria

Potent l-valine producers were screened among 2-thiazolealanine resistant mutants derived from three typical l-glutamic acid producing bacteria: Brevibacterium lactofermentum, Corynebacterium acetoacidophilum, Arthrobacter citreus. By strain No. 487, the best producer derived from Brevibacterium, 31 mg/ml of l-valine was produced after 72 hr when 10% glucose was supplied as a carbon source, thus giving the yield of 31% from glucose. Accumulation of the other amino acids was negligible. The addition of l-isoleucine and l-leucine in the culture medium did not reduce the l-valine production, indicating that the l-valine biosynthesis is insensitive to these end products in the l-valine producer.     

Conversion of the Extracellular Dextransucrase Isoenzymes from Leuconostoc mesenteroides NRRL B-1299

Effect of oxygen tension on l-lysine, l-threonine and l-isoleucine accumulation was investigated. Sufficient supply of oxygen to satisfy the cell’s oxygen demand was essential for the maximum production in each fermentation. The dissolved oxygen level must be controlled at greater than 0.01 atm in every fermentation, and the optimum redox potentials of culture media were above ?170 mV in l-lysine and l-threonine and above ?180 mV in l-isoleucine fermentations. The maximum concentrations of the products were 45.5 mg/ml for l-lysine, 10.3 mg/ml for l-threonine and 15.1 mg/ml for l-isoleucine. The degree of the inhibition due to oxygen limitation was slight in the fermentative production of l-lysine, l-threonine and l-isoleucine, whose biosynthesis is initiated with l-aspartic acid, in contrast to the accumulation of l-proline, l-glutamine and l-arginine, which is biosynthesized by way of l-glutamic acid.     

Studies on the Metabolism of d-Amino Acid in Microorganisms

It is confirmed by a new method for the determination of d-glutamic acid, that Aerobacter strain A rapidly metabolizes d-glutamic acid, while it only shows feeble metabolic activity towards l-glutamic acid when it is grown on a dl-glutamate-K₂HPO₄ medium. A specific d-glutamic oxidase is demonstrated in the cell-free extracts of Aerobacter strain A. This enzyme seems to be different from d-glutamic-aspartic oxidase obtained from Aspergillus ustus by the authors, since the former has no activity towards d-aspartic acid.     

Studies on the Synthesis of l-Amino Acids

l-Homoserine was prepared by the reduction of l-aspartic acid β-methyl ester with sodium borohydride in water solution without any racemization. The yield of l-homoserine was about 25% of the theoretical amount, and no product other than l-homoserine, l-aspartic acid and l-aspartic acid β-methyl ester was present in the reaction mixture. The low yield of l-homoserine was ascribed to the hydrolysis of the ester.

l-Azetidine-2-carboxylic acid could not be detected in the reaction mixture. In contrast with the reduction of l-glutamic acid γ-esters, the reduction of l-aspartic acid β-ester was not accompanied by the cyclization.     

Microbial Production of l-Threonine

l-Threonine production by strain BB-69, which was derived from Brevibacterium flavum No. 2247 as a α-amino-β-hydroxyvaleric acid resistant mutant and produced about 12 g/liter of l-threonine, was reduced by the addition of l-lysine or l-methionine in the culture medium. Many of lysine auxotrophs but not methionine auxotrophs derived from strain B–2, which produced about 7 g/liter of l-threonine, produced more l-threonine than the parental strain. Except only one methionine auxotroph (BBM–21), none of lysine and methionine auxotrophs derived from BB–69 produced more l-threonine than the parental strain. Homoserine dehydrogenase of crude extract from strain B–2 was inhibited by l-threonine more strongly than that from BB–69. Strain BBM–21, a methionine auxotroph derived from BB–69, produced about 18 g/liter of l-threonine, 50% more than BB–69, while accumulation of homoserine decreased remarkably as compared with BB–69. l-Threonine production by BBM–21 was increased by the addition of l-homoserine, a precursor of l-threonine, while that by BB–69 was not. No difference was found among BBM–21, BB–69 and No. 2247 in the degree of inhibition of homoserine kinase by l-threonine. l-Threonine production by revertants of BBM–21, that is, mutants which could grow without methionine, were all lower than that of BBM–21. Correlation between l-threonine production and methionine or lysine auxotrophy was discussed.     

l-Tryptophan Production by 5-Methyltryptophan-resistant Mutants of Glutamate-producing Bacteria

1. Some of 5-methyltrypotophan (5MT)-resistant mutants derived from glutamate-producing bacteria such as Brevibacterium flavum, Corynebacterium acetoglutamicum and Micrococcus glutamicus produced a small amount of l-tryptophan, while tyrosine and phenylalanine auxotrophs of B. flavum did not.

2. 5-MT-resistant mutant derived from the auxotroph for tyrosine and phenylalanine produced 390 mg/liter of l-tryptophan at most. A mutant resistant to a higher concentration of 5MT, which was derived from a tyrosine and phenylalanine auxotrophic mutant which was resistant to a low concentration of 5MT, produced 660 mg/liter of l-tryptophan. Using this mutant, the effects of the concentrations of components of the culture medium on the l-tryptophan production were examined. The high concentration of l-tyrosine, but not l-phenylalanine, inhibited the l-tryptophan production. Using the improved culture medium, this strain produced 1.9 g/liter of l-tryptophan.     

Microbial Production of l-Threonine

l-Threonine producing α-amino-β-hydroxyvaleric acid resistant mutants were derived from E. coli K-12 with 3 x 10^-5 frequency. One of mutants, strain β-101, accummulated maximum amount of l-threonine (1. 9 g/liter) in medium. Among isoleucine, methionine and lysine auxotrophs derived from E. coli K-12, only methionine auxotrophs produced l-threonine. In contrast, among isoleucine, methionine and lysine auxotrophs derived from β-101, l-threonine accumulation was generally enhanced in isoleucine auxotrophs. One of isoleucine auxotrophs, strain βI-67, produced maximum amount of l-threonine (4. 7 g/liter). Methionine auxotroph, βM-7, derived from β-101 produced 3.8 g/liter, and βIM-4, methionine auxotroph derived from β1-67, produced 6.1 g/liter, when it was cultured in 3% glucose medium supplemented with 100 μg/ml of l-isoleucine and l-methionine, respectively. These l-threonine productivities of E. coli mutants were discussed with respect to the regulatory mechanisms of threonine biosynthesis. A favourable fermentation medium for l-threonine production by E. coli mutants was established by using strain βM-4.     

Utilization of Hydrocarbons by Microorganisms

As already reported, strain S1OB1 was found to accumulate l-glutamic acid in a thiamine-deficient medium at the sole expense of hydrocarbon. In order to elucidate the biosynthetic pathway of l-glutamic acid, first of all, the incorporation of molecular oxygen into l-glutamic acid was examined. l-Glutamic acid accumulated under ¹⁸O-enriched atmosphere was separated, purified, identified and found to have been enriched with ¹⁸O. This results indicate the occurrence of oxygenase reaction involving addition of molecular oxygen. From a postulated biosynthetic pathway of l-glutamic acid, theoretical ¹⁸O content was calculated and compared with experimental one. ¹⁸O content of cells grown on n-alkane or glucose was also examined.     

Substrate Specificity of α-Glucosidase II in Rice Seed

The substrate specificity of rice α-glucosidase II was studied. The enzyme was active especially on nigerose, phenyl-α-maltoside and maltooligosaccharides. The actions on isomaltose and phenyl-α-glucoside were weak, and on sucrose and methyl-α-glucoside, negligible. The α-glucans, such as soluble starch, amylopectin, β-limit dextrin, glycogen and amylose, were also hydrolyzed.

The ratio of the maximum velocities for hydrolyses of maltose (G₂), nigerose (N), kojibiose (K), isomaltose (I), phenyl-α-maltoside (?M) and soluble starch (SS) was estimated to be 100: 94.4: 14.2: 7.1: 89.5: 103.1 in this order, and that for hydrolyses of malto-triose (G₃), -tetraose (G₄), -pentaose (G₅), -hexaose (G₆), -heptaose (G₇), -octaose (G₈), and amyloses ( and ), 113: 113: 113: 106: 113: 100: 106: 106. The Km values for N, K, I, ?M and SS were 2.4 mm, 0.58 mm, 20 mm, 1.6 mm and 5.0 mg/ml, respectively; those for G₂, G₃, G₄, G₅, G₆, G₇, G₈, and , 2.4 mm, 2.2 mm, 2.1 mm, 1.5 mm, 1.0 mm, 1.1 mm, 0.95 mm, 1.5 mm and 1.1 mm.

Rice α-glucosidase II is considered an enzyme with a preferential activity on maltooligosaccharides.     

Change in Permeability to l-Glutamic Acid in the Glycerol Auxotroph GL-21

In this study, the mechanism of the extracellular accumulation of l-glutamic acid by the glycerol auxotroph was partially clarified. Whenever Corynebacterium alkanolyticum GL–21 (glycerol auxotroph) accumulated a large amount of l-glutamic acid in the fermentation broth, the content of its cellular phospholipids was not more than 50% of that of C. alkanolyticum No. 314 (prototroph).

Moreover, biotin, oleic acid or thiamine had no influence on the cellular phospholipid content of the auxotroph.

Under limited supply of glycerol, the efflux of l-glutamic acid in the auxotroph was extremely enhanced, but its enzyme activities participating in l-glutamic acid biosynthesis remained at the same level as those of the prototroph.

From the results, it is considered that the regulation of phospholipid content gave rise to the destruction of the permeability barrier to l-glutamic acid in the cell membrane.     

Studies on Metabolism of Pyrrolidone Carboxylic Acid in Bacteria

l-Glutamic acid was formed from d-, l-, and dl-PCA with cell-free extract of Pseudomonas alcaligenes ATCC-12815 grown in the medium containing dl-PCA as a sole source of carbon and nitrogen. The enzyme(s) involved in this conversion reaction was distributed in the soluble fraction within the cell and in 0.5 saturated fraction at the fractionation procedure with the saturation of ammonium sulfate. Optimum pH of this enzyme(s) lied at pH 8.5 and optimum temperature was 30°C. Cu (5 × 10^?3 m) inhibited the reaction considerably while Ca or Fe accelerated it. PALP (1×10^?3 m) also gave an enhanced activity to some extent. The enzyme preparation converted dextro-rotatory enan-thiomorph of PCA to its laevo-rotatory one which in turn was not converted to the opposite rotation direction by this enzyme. Furthermore, the preparation did not, if any, show d-glutamic acid racemase activity. Isotopic experiments with using dl-PCA-1-¹⁴C revealed that l-glutamic acid-1-¹⁴C was formed by the cleavage of –CO–NH– bond of pyrrolidone ring of PCA. It was concluded that dl-PCA when assimilated by the present bacterium is at first transformed to l-PCA by the optically isomerizing enzyme and subsequently is cleaved to l-glutamic acid probably by the PCA hydrolysing enzyme.     

Conformational Change of a Natto Mucin in Solution

The mucin obtained from a natto sample was found to be composed of 58 % of γ-polyglutamic acid and 40% of polysaccharide. The ratio of l- and d-glutamic acid was determined to be 58:42 using l-glutamic acid decarboxylase. The weight- and z-average molecular weight were 2.08 × 10⁵ and 2.22 × 10⁵, respectively. The distribution curve of the sedimentation coefficient showed a small heterogeneity. The mucin molecule was considered to be randomly coiled at pH 5.0 ~ 8.8 and to be a rod-like molecule in the lower pH region.