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 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.     

Starch-hydrolyzing Enzymes in Germinating Kidney Bean

Enzymatic production of D-Glu was investigated by the succesive reactions of a glutamate racemase (EC 5.1.1.3) and a glutamate decarboxylase (EC 4.1.1.15) on L-Glu.Lactobacillus brevis ATCC8287 was chosen as a source of glutamate racemase. This strain produced a glutamate decarboxylase simultaneously. The glutamate racemase activity in the cell free extracts was 0.035 units/mg protein. The enzyme kept its activity even at 500 Mm of L-Glu (74g/liter). The optimum pHs of the racemase and the decarboxylase were at around 8.5 and below 4.0, respectively. Both enzymes had no activity at the optimum pH for the other enzyme. L-Glu was racemized first by the glutamate racemase at pH 8.5, then the pH was shifted to 4.0 at which L-Glu was decarboxylated by the glutamate decarboxylase. Starting from 100 g/liter of L-Glu, 50 g/liter of D-Glu was produced and no L-Glu remained in the reaction mixture.     

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.     

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.     

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.     

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.     

Synthesis of l-Tyrosine or 3,4-Dihydroxyphenyl-l-alanine from Pyruvic Acid,Ammonia and Phenol or Pyrocatechol

The synthesis of l-tyrosine or 3,4-dihydroxyphenyl-l-alanine (l-dopa) from pyruvate, ammonia and phenol or pyrocatechol was studied with intact cells of Erwinia herbicola ATCC 21434 containing high tyrosine phenol lyase activity. By elemental analyses and determination of optical activity, the tyrosine or dopa synthesized was confirmed to be entirely of l-form. Maximum amount of l-tyrosine (60.5 g/liter) or l-dopa (58.5 g/liter) was formed using this enzymatic method by feeding sodium pyruvate and phenol or pyrocatechol. However, large amounts of by-products were formed in the l-dopa synthetic reaction mixture. By-products were proved to be formed from l-dopa and pyruvate by a nonenzymic reaction. pH and the temperature of reaction had intensive effects on the formation of by-products. A simple method using a boric acid-pyrocatechol complex was devised, as the feeding procedure of substrates was complicated.     

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.     

Characterization of and Ethanol Hyper-production by Clostridium thermocellum I-1-B

An ethanol hyper-producing clostridial strain, I-1-B, was isolated from Shibi hot spring, Kagoshima prefecture and identified as Clostridium thermocellum based on morphological and physiological proper­ ties. The carbohydrates used as energy sources were glucose, fructose, cellobiose, cellulose and esculin. Fermentation products were ethanol, lactate, acetate, formate, carbon dioxide, and hydrogen. The optimum, maximum, and minimum temperature for growth are about 60, 70, and 47°C, respectively. Optimum pH for growth is about 7.5, and growth occurs at starting pH between 6.0 and 9.0. I-1-B strain has strong tolerance for ethanol and hyper ethanol-productivity. Ethanol concentrations causing 50%. decrease of growth yield are 27 and 16g/liter for I-1-B and ATCC27405 of C. thermocellum, respectively. The organism was cultured on a medium containing 80 g/liter cellulose at 60°C for 156 h. The culture was fed with a vitamin mixture containing vitamin B₁₂ and mineral salts solution at intervals. In this culture the organism produced 23.6 g/liter (512mM) ethanol, 8.5 g/liter (94mM) lactate, 2.9 g/liter (48mM) acetate, and 0.9 g/liter (20mM) formate. The molar ratio of ethanol to total acidic products was 3.2. The ethanol productivity of the strain I-1-B is superior to any of the wild and mutant strains of C. thermocellum so far reported.     

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.     

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.     

Purification and Crystallization of d-Arabinose (l-Fucose) Isomerase from Aerobacter aerogenes by Polyethylene Glycol

d-Arabinose(l-fucose) isomerase (d-arabinose ketol-isomerase, EC 5.3.1.3) was purified from the extracts of d-arabinose-grown cells of Aerobacter aerogenes, strain M-7 by the procedure of repeated fractional precipitation with polyethylene glycol 6000 and isolating the crystalline state. The crystalline enzyme was homogeneous in ultracentrifugal analysis and polyacrylamide gel electrophoresis. Sedimentation constant obtained was 15.4s and the molecular weight was estimated as being approximately 2.5 × 10⁵ by gel filtration on Sephadex G-200.

Optimum pH for isomerization of d-arabinose and of l-fucose was identical at pH 9.3, and the Michaelis constants were 51 mm for l-fucose and 160 mm for d-arabinose. Both of these activities decreased at the same rate with thermal inactivation at 45 and 50°C. All four pentitols inhibited two pentose isomerase activities competitively with same Ki values: 1.3–1.5 mm for d-arabitol, 2.2–2.7 mm for ribitol, 2.9–3.2 mm for l-arabitol, and 10–10.5 mm for xylitol. It is confirmed that the single enzyme is responsible for the isomerization of d-arabinose and l-fucose.     

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.     

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.     

Branched Chain Amino Acid Aminotransferase of Pseudomonas sp

Branched chain amino acid aminotransferase was partially purified from Pseudomonas sp. by ammonium sulfate fractionation, aminohexyl-agarose and Bio-Gel A-0.5 m column chromatography.

This enzyme showed different substrate specificity from those of other origins, namely lower reactivity for l-isoleucine and higher reactivity for l-methionine.

Km values at pH 8.0 were calculated to be 0.3 mm for l-leucine, 0.3 mm for α-ketoglutarate, 1.1 mm for α-ketoisocaproate and 3.2 mm for l-glutamate.

This enzyme was activated with β-mercaptoethanol, and this activated enzyme had different kinetic properties from unactivated enzyme, namely, Km values at pH 8.0 were calculated to be 1.2 mm for l-leucine, 0.3 mm for α-ketoglutarate.

Isocaproic acid which is the substrate analog of l-leucine was competitive inhibitor for pyridoxal form of unactivated and activated enzymes, and inhibitor constants were estimated to be 6 mm and 14 mm, respectively.     

Production of L-Tryptophan by 5-Fluorotryptophan Resistant Mutants of Bacillus subtilis

The growth of Bacillus subtilis TR–44, a prototrophic transductant from one of inosine producers, was completely inhibited by 200 µg/ml of 5-fiuorotryptophan, a tryptophan analogue, and the inhibition was reversed by the addition of L-tryptophan.

Several mutants resistant to 5FT* produced L-tryptophan in the growing cultures. The best producer, strain FT–39, which was selected on a medium containing 1500 µg/ml of 5FT, produced 2 g/liter of L-tryptophan, when cultured in a medium containing 8% of glucose but without any tryptophan precursors. In this mutant, anthranilate synthetase, a key enzyme of the tryptophan biosynthesis, had increased over 280-fold, presumably owing to a genetic derepression. From FT–39, mutants resistant to 7000 µg/ml of 5FT were derived. Among them, strain FF–25 produced 4 g/liter of L-tryptophan, twice as much as did the parental strain. Since this strain produced large amount of L-phenylalanine as well as L-tryptophan, the genetic alteration seemed to be involved in some metabolic regulation of common part of the aromatic amino acid biosynthetic pathway.

Further, some auxotrophs derived from these 5FT resistant mutants produced more L-tryptophan than did the parental strains.

Relationships between the accumulation of L-tryptophan and the regulation mechanisms of the L-tryptophan biosynthesis were discussed.     

Antibacterial Activity of l-Lysine α-Oxidase against rec+ and rec− Strains of Bacillus subtilis

2-Deoxyribose 5-phosphate production through coupling of the alcoholic fermentation system of baker’s yeast and deoxyriboaldolase-expressing Escherichia coli was investigated. In this process, baker’s yeast generates fructose 1,6-diphosphate from glucose and inorganic phosphate, and then the E. coli convert the fructose 1,6-diphosphate into 2-deoxyribose 5-phosphate via D-glyceraldehyde 3-phosphate. Under the optimized conditions with toluene-treated yeast cells, 356 mM (121 g/l) fructose 1,6-diphosphate was produced from 1,111 mM glucose and 750 mM potassium phosphate buffer (pH 6.4) with a catalytic amount of AMP, and the reaction supernatant containing the fructose 1,6-diphosphate was used directly as substrate for 2-deoxyribose 5-phosphate production with the E. coli cells. With 178 mM enzymatically prepared fructose 1,6-diphosphate and 400 mM acetaldehyde as substrates, 246 mM (52.6 g/l) 2-deoxyribose 5-phosphate was produced. The molar yield of 2-deoxyribose 5-phosphate as to glucose through the total two step reaction was 22.1%. The 2-deoxyribose 5-phosphate produced was converted to 2-deoxyribose with a molar yield of 85% through endogenous or exogenous phosphatase activity.     

Microbial Conversion of DL-5-Substituted Hydantoins to the Corresponding L-Amino Acids by Pseudomonas sp. Strain NS671

A bacterial strain, NS671, which converts DL-5-(2-methylthioethyl)hydantoin stereospecifically to L-methionine, was isolated from soil and was classified into the genus Pseudomonas. With growing cells of Pseudomonas sp. strain NS671, DL-5-(2-methylthioethyl)hydantoin was effectively converted to L-methionine. Under adequate conditions, 34g of L-methionine per liter was produced with a molar yield of 93% from DL-5-(2-methylthioethyl)hydantoin added successively. In addition to L-methionine, other amino acids such as L-valine, L-leucine, L-isoleucine, and L-phenylalanine were also produced from the corresponding 5- substituted hydantoins, but these L-amino acids produced were partially consumed by strain NS671. The hydantoinase, by which 5-substituted hydantoin rings are opened, was ATP-dependent. The N-carbamylamino acid amidohydrolase was found to be strictly L-specific, and its activity was inhibited by high concentration of ATP.     

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.