Tryptophan Synthase and Production of l-Tryptophan in Regulatory Mutants

A 5-fluorotryptophan-resistant mutant of Brevibacterium flavum, No. 187, accumulated 2.6 g of indole 3-glycerol (InG) in addition to 8.0 g of l-tryptophan per liter in the culture medium. The addition of l-serine to the medium decreased the accumulation of InG and increased that of l-tryptophan up to a concentration of 10.3 g/liter, while the addition of l-tryptophan increased the InG accumulation, suggesting that InG was formed by hydrolysis of indole 3-glycerol phosphate (InGP), the substrate of tryptophan synthase (TS) which catalyzed the final step reaction of tryptophan biosynthesis. Then, in order to examine the mechanism of the InG accumulation, TS was purified from tryptophan auxotroph, TA-60. The reaction mechanism of TS was Ordered Bi Bi with Km’s of 0.63 and 0.038 mm for serine and InGP, respectively. Tryptophan, a product of the TS reaction, inhibited TS competitively with respect to serine and the Ki for tryptophan was estimated to be 2.0 mm. On the other hand, anthranilate synthase (AS), the first enzyme in the tryptophan biosynthetic pathway, was much less sensitive to the feedback inhibition by tryptophan in strain No. 187 than in the wild strain. The tryptophan concentration giving 50% inhibition of AS in strain No. 187 was estimated to be 2.4 mm, almost comparable to that of TS, 7.7 mm. From these results, it was concluded that the accumulation of InG in strain No. 187 would result from the product inhibition of TS by the tryptophan accumulated.     

Studies on the Utilization of Hydrocarbon by Microorganisms

An uracil-requiring mutant (KY7122) of Arthrobacter paraffineus KY4303 (ATCC15591) was found to accumulate orotic acid and orotidine on n-paraffine as a sole carbon source.

Both substances were definitely indentified as orotic acid and orotidine, from the results on column and paper chromatography, UV and IR absorption spectra, elementary analysis and analyses of hydrolysate.

Cultural conditions for orotic acid and orotidine fermentation were then investigated. As the carbon source n-paraffines from C₁₄ to C₁₆ were the most suitable for the fermentation, and sorbitol, fructose and mannitol were best utilized for the growth, and orotidine produced from them were twice as much as those from hydrocarbon. The addition of 200 mg of uracil and 2 g of C. S. L to 1 liter of medium was most optimal for orotic acid and orotidine fermentation.

Orotic acid and orotidine accumulations were enhanced by the addition of either l-tyrosine, l-leusine, l-threonine, gluconate or meat extract.     

Mechanism of l-Threonine and l-Lysine Production by Analog-resistant Mutants of Corynebactemum glutamicum

Homoserine dehydrogenases and aspartokinases in l-threonine- or l-threonine and l-lysine-producing mutants derived from Corynebacterium glutamicum KY 9159 (Met^?) were studied with respect to the sensitivity to the inhibition by end products, l-threonine and l-lysine. The activities of homoserine dehydrogenases in the mutants which produced l-threonine or l-threonine and l-lysine were slightly less susceptible to the inhibition by l-threonine than the activity in the parent strain, KY 9159. The aspartokinases in the threonine-producing mutants, KY 10484 and KY 10230, which were resistant to α-amino-β-hydroxylvaleric acid (AHV, a threonine analog) and more sensitive to thialysine (a lysine analog) than the parent, were sensitive to the concerted feedback inhibition by l-lysine and l-threonine by about the same degree as KY 9159. The aspartokinase in an AHV- and thialysine-resistant mutant, KY 10440, which was derived from KY 10484 and produced about 14 mg/ml of l-threonine in a medium containing 10% glucose was less susceptible to the concerted feedback inhibition than KY 10484 or KY 9159, although the activity was still under the feedback control. In the parent strain, l-threonine activated aspartokinase activity in the absence of ammonium sulfate, an activator of the enzyme, but partially inhibited the activity in the presence of the salt. On the other hand, the enzyme of KY 10440 was activated by l-threonine either in the presence or in the absence of the salt. In another AHV- and thialysine-resistant mutant, KY 10251, which was derived from KY 10230 and produced both 9 mg/ml of l-threonine and 5/5 mg/ml of l-lysine, l-threonine and l-lysine simultaneously added hardly inhibited the activity of aspartokinase.

Implications of these results are discussed in relation to l-threonine or l-lysine production, AHV or thialysine resistance and regulation of l-threonine biosynthesis in these mutants.     

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.     

Production of l-Lysine by Fluoropyruvate-sensitive Mutants of Brevibacterium lactofermentum

Better producers of l-lysine were obtained by derivation of fluoropyruvate(FP)-sensitive mutants from Brevibacterium lactofermentum AJ3990. The coexistence of FP and excess biotin synergistically stimulated l-lysine formation by washed cells. FP inhibited 50% of growth and pyruvate dehydrogenase (PDH) activity of AJ3990 at 0.04 mm and 1 mm, respectively. Therefore, the synergistic effect of FP and excess biotin seems to be due to the optimization of the PDH/pyruvate carboxylase activity ratio in l-lysine biosynthesis. This was confirmed by the derivation of FP-sensitive mutants which have the optimal level of PDH activity for l-lysine production. The best producer, AJ11204, had about 27% PDH activity as compared with the parental strain and accumulated 70 g of l-lysine per liter with a conversion yield of 50% from glucose in the presence of excess biotin.     

Production of l-Threonine by Analog-resistant Mutants

Mutants resistant to α-amino-β-hydroxyvaleri0c acid (AHV) were derived from various bacteria which belong to Corynebacterium, Brevibacterium, Arthrobacter, Microbacterium, or Bacillus by mutational treatment with N-methyl-N′-nitro-N-nitrosoguanidine(NTG), and screened for their ability to produce l-threonine. A number of l-threonine producers were obtained from each group of bacteria. Among them, the mutants derived from C. glutamicum KY9159(Met^?) were further mutagenized with NTG to derive thialysine(S-Lys)-resistant mutants. An AHV-resistant mutant, KY10484 was proved to be much more sensitive to the growth inhibition by thialysine than the parent strain, KY9159. From KY10484, a number of AHV- and thialysine-resistant mutants were derived. Approximately a half of these mutants were found to produce more l-threonine than KY10484. Among these mutants, KY10440 (Met^?, AHV^R, s-Lys^R) was used to investigate the cultural conditions for l-threonine production. The growth of KY10440 decreased largely with addition of l-homoserine, a threonine precursor. l-Asparagine, l-cystine, l-glutamine or l-arginine partially reversed the inhibitory effect of l-homoserine. Addition of these amino acids at low level led to increase l-threonine production. The amount of l-threonine accumulation reached to a level of 14mg/ml with a medium containing 10% glucose and to a level of 10 mg/ml with a medium containing 5% molasses (as glucose).

Another AHV- and thialysine-resistant mutant, KY10251 which was also derived from KY9159 was found to produce both 9 mg/ml of l-threonine and 5.5 mg/ml of l-lysine in a culture broth.     

Enzymatic Production of Ribavirin from Orotidine by Erwinia carotovora AJ 2992

Microorganisms that produce ribavirin (1-β-d-ribofuranosyl-1,2,4-triazole-3-carboxamide; virazole^®) directly from orotidine and 1,2,4-triazole-3-carboxamide (TCA) were screened from our stock cultures. Of the 425 strains, Erwinia carotovora AJ 2992 was found to possess potent ribavirin-producing ability, from orotidine and TCA. In the presence of intact cells of E. carotovora AJ 2992, 183 mm ribavirin was produced from 300 mm orotidine and 300 mm TCA on 48 hr reaction.     

Production of l-Tryptophan by Azaserine-resistant Mutants of Brevibacterium flavum

Azaserine-resistant mutants derived from a 5-fluorotryptophan-resistant, l-tryptophan-producing mutant of Brevibacterium flavum, accumulated 10.3 g/liter of l-tryptophan at maximum. The production increased to 11.4 g/liter when l-serine was added. In the mutant, only anthranilate synthase among enzymes of the tryptophan-specific bio synthetic pathway increased in activity to a 2-fold higher level than that in the parent strain, No. 187. Sensitivity of anthranilate synthase to the feedback inhibition was not altered by the mutation. Activity of 3-deoxy-d-arabino-heptulosonate 7-phosphate synthase, the first common enzyme for aromatic amino acid biosynthesis, also increased 2.7-fold and was less sensitive to the feedback inhibition by phenylalanine and tyrosine. Tryptophan transport activity in strain A-100 was similar as that in the parent. Azaserine inhibited anthranilate synthase activity by 50% at 0.075 mm. The inhibition was of a mixed type with respect to both the two substrates. Anthranilate synthase of strain A-100 was inhibited in a similar manner to that of the parent.     

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.     

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.     

Theanine Formation by Tea Suspension Cells

The theanine (THE: γ-glutamylethylamide) content and the growth rate of cultured cells of tea (Camellia sinensis L.) were increased greatly to 22.3%, in dry wt. with a medium containing 60 mM nitrate and 25 mM ethylamine as a nitrogen source. The optimum concentrations of nitrate, Mg²⁺, and K⁺ for the growth and formation of THE in suspension cells were 40mM, 3mM, and 104mM, respectively. The yield of THE accumulated in the cultured cells with the medium modified for THE formation was increased greatly due to a great increase of the growth rate.     

Some Physicochemical Properties of Invertase of Candida utilis

This study examined the microbial transformation of carbazole (CZ) by an isolated bacterium that can use CZ as a sole carbon and nitrogen source. The strain identified as Pseudomonas stutzeri produced a large amount of anthranilic acid (AA) from CZ in the medium containing a nonionic surfactant. In dialysis culture using ion-exchange resin, 7.9 g/liter (58mm) of AA was accumulated from 15g/liter (90mm) of CZ and the molar yield of AA reached about 64%.     

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.     

Microbial Production of d-Arabitol by n-Alkane-grown Candida tropicalis

In the course of study on citric acid fermentation by Candida tropicalis KY6224, in which n-alkane mixture (C–12 to C–15) was used as the sole source of carbon, we found that a arabitollike substance was accumulated when the medium-pH was controlled at low level (3.0 to 4.0). This substance was isolated in crystalline forms and identified as d-arabitol.

d-Arabitol production was also observed with ethanol, acetic acid and glucose as the sole source of carbon. Important factors for efficient production of d-arabitol were keeping the medium-pH at low-level (3.0 to 4.0) and the concentration of NaCl or KCl at high level (1 to 5%). This strain produced 75 mg/ml of d-arabitol in 120 hr incubation under optimal culture conditions; this corresponds to 50 % of n-alkane consumed.     

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.     

Microbial Production of l-Phenylalanine from n-Alkanes

A tyrosine auxotroph derived from a hydrocarbon utilizing bacterium, Corynebacterium sp. KY 4309, was found to accumulate a large amount of l-phenylalanine in the broth. The cultural conditions for l-phenylalanine production were studied. The pH value during cultivations exhibited a remakable effect on l-phenylalanine production. The addition of l-tryptophan enhanced the l-phenylalanine accumulation. Shikimic acid and phenylpyruvic acid are possible precursors of phenylalanine biosynthesis in this bacterium. Production of l-phenylalanine attained to a level of 10 mg per ml for 68 hr under optimal conditions.     

N-Acetylornithine-δ-aminotransferase-deficient and N-Acetylglutamokinase-deficient Arginine Auxotrophs of Corynebacterium glutamicum

An N-acetylglutamokinase-deficient arginine-requiring mutant, KY9390 and an N-acetylornithine aminotransferase-deficient arginine-requiring mutant, AA-7 were derived from a wild-type strain and an l-arginine-producing mutant of Corynebacterium glutamicum, respectively. KY 9390 accumulated 7.5 mg per ml of N-acetylglutamic acid and AA-7 accumulated 2 mg per ml of N-acetylglutamate-γ-semialdehyde, intermediates of arginine biosynthesis, in a culture medium.

The production of N-acetylglutamate-γ-semialdehyde by AA-7 was not affected by the concentration of l-arginine in the medium, whereas that of N-acetylglutamic acid by KY 9390 was inhibited by the addition of l-arginine in the medium.     

Studies on the Enzymatic Production of l-Aspartic Acid from Maleic Acid

The enzymatic production of l-aspartic acid from maleic acid with cell suspensions of Alcaligenes faecalis 5-24, isolated from solid by the authors, was investigated.

The optimum conditions of this reaction and some cultural conditions which influenced on the ability of the cells to catalyze the above reaction were mainly studied.

The cells grown on maleic acid as a sole source of carbon showed exclusively the strong ability. The cells grown on a carbon source other than maleic acid showed no activity of this reaction.

It was concluded that an inducibles enzyme whose formation was stimulated by the presence of maleic acid might be involved in the reaction for the production of l-aspartic acid from maleic acid.

It was found that malonic acid was replaceable for maleic acid which played an inductive role for the formation of the enzyme system concerned with the reaction of l-aspartic acid production from maleic acid.

The cells grown in the medium containing malonic acid showed a stronger activity of the above reaction than the cells grown on maleic acid. The induction effect of malonic acid was remarkable when the organism was cultured in an acid medium. Whereas, consumption of C¹⁴-malonic acid in the medium by the organism was not observed at all in any pH milieu even where the formation of the enzyme system essential for the reaction was fully conducted. It indicated that malonic acid penetrated preferentially in acid milieu into the cells was a non-metabolic inducer like thiomethyl-β-d-galactoside in β-galactosidase system and that permeability barrier might exist in the organism.

The formation of cis-trans isomerase which catalyzed the conversion of maleic acid to fumaric acid was much stimulated by the addition of either malonic acid or maleic acid. From these results, it was concluded that l-aspartic acid was produced from maleic acid and ammonium ion by both actions of the inducible cis-trans isomerase and the constitutive aspartase.     

Continuous Production of l-Alanine with NADH Regeneration by a Nanofiltration Membrane Reactor

A conjugated enzyme system, alanine dehydrogenase (AIDH) for stereospecific reduction of pyruvate to l-alanine and glucose dehydrogenase (GDH) for regeneration of NADH, were coimmobilized in a nanofiltration membrane bioreactor (NFMBR) for the continuous production of l-alanine from pyruvate with NADH regeneration. Since pyruvate was proved to be unstable at neutral pH, it was kept under acidic conditions and supplied to NFMBR separately from the other substrates. As 0.2 m pyruvate in HCl solution (pH 4), 10 mm NAD, 0.2 m glucose, and 0.2 m NH₄Cl in 0.5 m Tris buffer (pH 8) were continuously supplied to NFMBR with immobilized AIDH (100 U/ml) and GDH (140 U/ml) at the retention time of 80 min, the maximum conversion, reactor productivity, and NAD regeneration number were 100%, 320 g/liter/d, and 20,000, respectively. To avoid the effect of pyruvate instability, a consecutive reaction system, lactate dehydrogenase (l-LDH) and AIDH, was also used. In this system, the l-LDH provides pyruvate, the substrate for the AIDH reaction, from l-lactate regenerating NADH simultaneously, so the pyruvate could be consumed as soon as it was produced. As 0.2 m l-lactate, 10 mm NAD, 0.2 m NH₄Cl in 0.5 m Tris buffer (pH 8) were continuously supplied to NFMBR with immobilized l-LDH (100 U/ml) and AIDH (100 U/ml) at the retention time of 160 min, the maximum conversion, reactor productivity, and the NAD regeneration number were 100%, 160 g/Iiter/d, and 20,000, respectively.     

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.