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.     

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.     

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.     

An Improved Synthesis of DL-Canavanine

Excellent l-proline producers were screened for among sulfaguanidine resistant mutants derived from three typical l-glutamic acid-producing bacteria: Brevibacterium flavum, B. lactofermentum, and C. glutamicum.

The best strain, No. 199, is a sulfaguanidine resistant mutant derived from an isoleucine auxotroph of B. flavum 2247 by nitrosoguanidine. Strain No. 199 produced 35 mg/ml of l-proline after 72 hr of cultivation with 10% glucose as a carbon source. The strain also accumulated purine bases such as adenine, guanine, and hypoxanthine, i.e., degradation products of purine nucleotides. In the mutant, 1.6 ~ 2.0 fold more intracellular ATP was found than that in the parent strain; it is a substrate of glutamate kinase relating to l-proline biosynthesis.

On the contrary, the levels of intracellular glutamic acid, a substrate of glutamate kinase, were similar among these strains.

It was confirmed that the increment of internal ATP, which was important in the l-proline production mechanism, was very effective in the improvement of l-proline producers.     

Micropolyamide Thin-layer Chromatography of Fluorescein-thiohydantoin-Amino Acids at Picomole Level

The formation of aromatic l-amino acid decarboxylase in bacteria was studied with intact cells in a reaction mixture containing the aromatic l-amino acids, 3,4-dihydroxy-l-phenyl-alanine, l-tyrosine, l-phenylalanine, l-tryptophan and 5-hydroxy-l-tryptophan. Activity was widely distributed in such genera as Achromobacter, Micrococcus, Staphylococcus and Sarcina. Bacterial strains belonging to the Micrococcaceae showed especially high decarboxylase activity toward l-tryptophan, 5-hydroxy-l-tryptophan and l-phenylalanine. M. percitreus AJ 1065 was selected as a promising source of aromatic l-amino acid decarboxylase. Results of experiments with this bacterium showed that the aromatic amine formed from l-tryptophan by the enzymatic method was identical with tryptamine. M. percitreus constitutively produced an enzyme which exhibited decarboxylase activity toward l-tryptophan. However, when large amounts of the aromatic l-amino acids listed above or the tryptamine formed from l-tryptophan were added, enzyme formation was repressed.

Cells with high enzyme activity were prepared by cultivating this bacterium at 30°C for 24 hr in a medium containing 0.5% glycerol, 0.5% yeast extract, 0.5% Polypepton, 3.0 vol % soybean protein hydrolyzate, 0.1% KH₂PO₄, 0.1% MgSO₄ · 7H₂O, 0.001% FeSO₄ · 7H₂O and 0.001% MnSO₄ · 5H₂O in tap water (pH 8.0).     

Optimal Conditions for the Enzymatic Production of l-Aromatic Amino Acids from the Corresponding 5-Substituted Hydantoins

The reaction conditions for the production of l-tryptophan from dl-5-indolyl- methylhydantoin by Flavobacterium sp. AJ-3940, and the cultural conditions for the formation of the enzyme involved by this bacterium were investigated. The optimal pH of this reaction was around 8.5 and the optimal temperature was between 45 to 55°C. The amount of l-tryptophan produced was remarkably increased by the addition of inosine, which formed a water insoluble adduct with l-tryptophan, to the reaction mixture because of the release of end-product inhibition by l-tryptophan. This enzyme was inducibly and intracellularly produced by Flavobacterium sp. AJ-3940 in proportion to the increase in cell growth. Cells showing high activity were obtained using a medium containing 5 g glucose, 5 g (NH₄)₂SO₄, 1 g KH₂PO₄, 3 g K₂HPO₄, 0.1 g MgSO₄ · 7H₂O, 0.01 g CaCl₂ · 2H₂O, 50 ml corn steep liquor and 3.5 g dl-5-indolylmethylhydantoin in a total volume of 1 liter (pH 7.0). Under the best conditions, 43 mg/ml of l-tryptophan was produced from 50 mg/ml of dl-5-indolylmethylhydantoin with a molar yield of 97% in the presence of cells of Flavobacterium sp. AJ-3940. In addition, other l-aromatic amino acids such as l-phenylalanine, l-tyrosine, l-DOPA and related l-amino acids were also produced from the corresponding 5-substituted hydantoins by this bacterium containing the l-tryptophan-producing enzyme induced by dl-5-indolylmethylhydantoin.     

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.     

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.     

Production of L-Isoleucine by AHV Resistant Mutants of Brevibacterium flavum

The growth of Brevibacterium flavum No. 2247A was inhibited by α-amino-β-hydroxy-valeric acid (AHV), and the inhibition was partially reversed by L-isoleucine.

AHV resistant strain ARI-129, which was isolated on a medium supplemented with 2 mg/ml of AHV, produced 11 g/liter of L-isoleucine.

No difference was observed in threonine dehydratase between No. 2247A and ARI–129. Homoserine dehydrogenase from ARI–129 was insensitive to the feedback inhibition by L-isoleucine and L-threonine.

O-Methyl-L-threonine resistant mutant, strain AORI–126, which was derived from ARI–129, produced 14.5 g/liter of L-isoleucine. Specific activity of threonine dehydratase from AORI–126 increased about two-fold higher than those from No. 2247A and ARI–129, whereas degree of inhibition of the enzyme by L-isoleucine was the same among three strains.

Among auxotrophic mutants derived from ARI–129, adenine and lysine auxotrophs produced more L-isoleucine than the parent did.

In the adenine auxotroph, L-isoleucine production was markedly reduced by the addition of excess adenine.     

Microbial Production of l-Threonine

The growth of Brevibacterium flavum No. 2247 was inhibited over 90% at a concentration above 1 mg/ml of α-amino-β-hydroxyvaleric acid, a threonine analogue, and the inhibition was reversed by the addition of l-threonine, and to lesser extent by l-leucine, l-isoleucine, l-valine and l-homoserine. l-Methionine stimulated the inhibition. Several mutants resistant to the analogue produced l-threonine in the growing cultures. The percentage of l-threonine producer in the resistant mutants depended on the concentration of the analogue, to which they were resistant. The best producer, strain B-183, was isolated from resistant strains selected on a medium containing 5 mg/ml of the analogue. Mutants resistant to 8 mg/ml of the analogue was derived from strain B-183 by the treatment with mutagen, N-methyl-N’-nitro-N-nitrosoguanidine. Among the mutants obtained, strain BB-82 produced 13.5 g/liter of l-threonine, 30% more than did the parental strain. Among the resistant mutants obtained from Corynebacterium acetoacidophilum No. 410, strain C-553 produced 6.1 g/liter of l-threonine. Several amino acids other than l-threonine were also accumulated, and these accumulations of amino acids were discussed from the view of regulation mechanism of l-threonine biosynthesis.     

L-Threonine Production by a Mutant of Arthrobactev paraffineus

An isoleucine leaky auxotroph of Arthrobacter paraffineus, which was isolated by Takayama et al.³⁾ as a mutant producing L-threonine and L-valine from n-paraffin, was subjected to further mutagenesis in an attempt to obtain better L-threonine producers. Some of the double auxotrophs derived from the isoleucine auxotroph and some of their revertants with respect to isoleucine requirement produced more L-threonine than the original isoleucine auxotroph. In contrast to the original isoleucine auxotroph, a revertant derived from a methionine plus isoleucine double auxotroph, KY7135, produced an increased amount of L-threonine and a decreased amount of L-valine. The optimum level of L-methionine for L-threonine production in KY7135 was much higher (1000 ~ 2000 μg/ml) with n-paraffin medium than with sorbitol or mannitol medium (10 ~ 50 μg/ml). L-Threonine production reached a maximum level (11.5 mg/ml) in 7 days incubation with the medium containing 10% n-paraffin (C₁₂ ~ C₁₄ rich). Several mutants which produce L-threonine more than 12 mg/ml were obtained from KY 7135 by monocolony isolation procedure.     

Screening of l-Isoleucine Producers among Ethionine Resistant Mutants of l-Threonine Producing Bacteria

Two types of l-isoleucine producing mutants were derived from l-threonine producers by the supplement of the resistance to ethionine.

Main control site in l-isoleucine biosynthetic pathway after threonine is threonine dehydratase. In case of Brevibacterium flavum No. 14083, l-isoleucine production was based on the insensitiveness of this key enzyme to feedback inhibition by l-isoleucine. As regards Brevibacterium flavum No. 168, it was based on the increase in the specific activity of this enzyme.

The former produced 11.3 g/liter of l-isoleucine and the latter produced 9.92 g/liter from glucose. The former showed a vigorous ability of acetic acid assimilation, but the latter did not.     

Biosynthetic Threonine Deaminase from Proteus morganii

Biosynthetic threonine deaminase was purified to an apparent homogeneous state from the cell extract of Proteus morganii, with an overall yield of 7.5%. The enzyme had a s⁰_20,w of 10.0 S, and the molecular weight was calculated to be approximately, 228,000. The molecular weight of a subunit of the enzyme was estimated to be 58,000 by sodium dodecyl sulfate gel electrophoresis. The enzyme seemed to have a tetrameric structure consisting of identical subunits. The enzyme had a marked yellow color with an absorption maximum at 415 nm and contained 2 mol of pyridoxal 5′-phosphate per mol. The threonine deaminase catalyzed the deamination of l-threonine, l-serine, l-cysteine and β-chloro-l-alanine. Km values for l-threonine and l-serine were 3.2 and 7.1 mm, respectively. The enzyme was not activated by AMP, ADP and ATP, but was inhibited by l-isoleucine. The Ki for l-isoleucine was 1.17 mm, and the inhibition was not recovered by l-valine. Treatment with mercuric chloride effectively protected the enzyme from inhibition by l-isoleucine.     

Regio- and stereoselective oxygenation of proline derivatives by using microbial 2-oxoglutarate-dependent dioxygenases

We evaluated the substrate specificities of four proline cis-selective hydroxylases toward the efficient synthesis of proline derivatives. In an initial evaluation, 15 proline-related compounds were investigated as substrates. In addition to l-proline and l-pipecolinic acid, we found that 3,4-dehydro-l-proline, l-azetidine-2-carboxylic acid, cis-3-hydroxy-l-proline, and l-thioproline were also oxygenated. Subsequently, the product structures were determined, revealing cis-3,4-epoxy-l-proline, cis-3-hydroxy-l-azetidine-2-carboxylic acid, and 2,3-cis-3,4-cis-3,4-dihydroxy-l-proline.     

On the Mechanism of l-Prolyl Diketopiperazine Formation by Streptomyces

Since l-prolyl diketopiperazines, l-prolyl-l-valine anhydride and l-leucyl-l-proline anhydride, had been isolated from the culture filtrate of Streptomyces sp. S-580, the mechanism of l-prolyl diketopiperazine formation by Streptomyces has been studied. These two l-prolyl diketopiperazines were not formed from their constituent amino acids incubated with intact cell or cell free homogenate of this strain in buffered salt solution containing energy source. However, from milk casein, poly peptone or gelatin, the former two were components of the culture medium of this strain, hydrolyzed with the pure streptomyces-protease, these l-prolyl diketopiperazines were obtained (only from gelatin, glycyl-l-proline anhydride were obtained in addition to these two). Furthermore, in hydrolysis of some synthetic l-prolyl peptides with this enzyme, l-prolyl diketopiperazine formation were also studied, and as the result, glycyl-l-proline anhydride was obtained from glycyl-l-prolyl-l-leucine but no l-prolyl diketopiperazine was formed from l-prolyl-l-leucyl-glycine. From these evidences, the possible route of l-prolyl diketopiperazine formation by Streptomyces has been discussed.     

Growth of Yeasts on n-Alkanes: Inhibition by a Lactonic Sophorolipid Produced by

The effects of amino acids on IMP production were examined with a mutant strain, KY10895, derived from Corynebacterium ammoniagenes KY13374. l-Proline improved the productivity of IMP more than any other amino acid. The optimum concentration of l-proline for IMP production was 1–2% and the IMP productivity was about 70% more than that in the control medium. The effects of l-proline analogs on IMP production were also examined with the mutant KY10895. DL-3,4-Dehydroproline inhibited IMP production. Mutants resistant to growth inhibition by dl-3,4-dehydroproline were derived from strain KY10895. Among mutants thus obtained, strain H-7335 had the highest productivity. The intracellular concentrations of l-proline in strain H-7335 were higher than those of the parental strain, KY10895. These findings indicated that an increase in intracellular l-proline was linked with an increase of IMP productivity and strengthening the l-proline synthesis of a strain was an effective method for obtaining a hyper-producer of IMP.     

Essential Role of Aspartokinase in L-Threonine Production by Escherichia coli W Mutants

We previously constructed an l-threonine-producing strain of E. coli W, KY8280, which is an Ile⁺ revertant of KY8279 which requires l-methionine, a,£-diaminopimelic acid and l-isoleucine [H. Kase et al., Agric. Biol. Chem., 35, 2089 (1971)]. From KY8280, another l-threonine-hyperproducing strain, KY8366, was obtained as an α-amino-β-hydroxy valeric acid (AHV, a threonine analog)-resistant mutant. Enzymatic analysis revealed that KY8280 constitutively expressed 8-fold higher l-threonine-sensitive aspartokinase I activity than KY8279. In addition, KY8366 constitutively expressed 13-fold higher l-lysine-sensitive aspartokinase III activity than KY8280. Such elevated levels of aspartokinases may contribute to the hyperproduction of l-threonine by these mutant strains. KY8366 produced 28 mg/ml of l-threonine in a culture medium fed with 12% glucose.     

l-Threonine Production by Auxotrophs of E. coli

Methionine auxotrophs were derived by the treatment with ultraviolet ray or N-methylN′-nitro-N-nitrosoguanidine from five strains of Escherichia coli. One of the methionine auxotrophs of E. coli C-6, strain No. 15, produced maximum amount of l-threonine (4.3 mg/ml) with the medium containing 5 % cane-molasses (as sugars). Double auxotrophs were derived with further mutational treatment from strain No. 15. It was found that l-threonine production was greatly enhanced by cultivating methionine-valine auxotrophs in the presence of l-valine and methionine. o.ne of the methionine-valine auxotroph, strain No. 234, produced maximum amount of l-threonine (10.5 mg/ml) from cane-molasses.

The requirement of l-valine for the growth of the strain No. 234 was found to be leaky, and it was suggested that some enzymes relating to l-valine metabolism were mutationally altered to temperature-sensitive.     

Determination of L-Cysteine with L-Methionine γ-Lyase

A chemically defined medium was devised to examine the growth, production and biochemical pathway of tetrocarcin A. The production of tetrocarcin A was greatly stimulated by l-feucine and its corresponding keto acid, α-ketoisocaproate, suggesting that l-leucine is involved in the biosynthesis of tetrocarcin A. About 10–12 μg/ml of tetrocarcin A was produced in a chemically defined medium consisting of 20 g sucrose, 2.5 g KNO₃, 5 g MgSO₄·7H₂O, 5 g KH₂PO₄ and 1 g l-leucine per liter of water (pH 7.0).     

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.