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.     

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.     

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.     

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.     

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.     

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.     

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.     

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.     

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.     

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.     

Culture Conditions of l-Isoleucine Fermentation from Acetic Acid

Culture conditions were studied for l-isoleucine production from acetic acid. Acetate and ammonium concentration in culture liquid exerted a great influence on the fermentation, and optimum concentration was 2–5 g/liter and 2–3 g/liter respectively. To maintain these conditions throughout the culture, it was necessary to supply intermittently a small amount of feeding solution which consisted of ammonium acetate and acetic acid. Molecular ratio of the former to the latter was 0.175, and total concentration of acetic acid was 700 g/liter.

Carbon dioxide showed an inhibitory influence on l-isoleucine production and adequate ventilation was necessary for satisfactory result. Maximum amount of l-isoleucine was 33.5 g/liter after 77-hr cultivation at 28°C and at pH 7.7. Production yield of l-isoleucine was 10% by weight from acetic acid.     

Effect of Penicillin on Amino Acid Fermentation

The effect of penicillin G(k) was first investigated on l-homoserine production by Micrococcus glutamicus 534-Co 147 (a threonine requiring mutant). The addition of 4 u/ml of penicillin, 7 to 9 hours after inoculation, brought about the conversion of l-homoserine to l-glutamic acid production. Similar phenomena were observed in l-lysine and l-valine fermentations. In these cases, a homoserine requiring and a leucine requiring mutant of M. glutamicus were used respectively. A marked conversion from lysine and valine to glutamate accumulation occured by penicillin addition. However, in l-isoleucine fermentation with Brevibacterium ammoniagenes ATCC 6871, no glutamate accumulation took place and isoleucine yields were remarkably decreased.     

Formation of Threonine Aldolase by Bacteria and Yeasts

Threonine aldolase was found to be formed in various strains of bacteria and yeasts when they were grown in media containing l-threonine as a sole source of carbon. As the other sources of carbon, d, l-allothreonine, l-serine and glycine were effective but glucose and sucrose were inert for the formation of the enzyme.

The maximal formation of the enzyme was observed in the initial of stationary phase of growth and, thereafter, the enzyme disappeared with the consumption of l-threonine. It seems that the enzyme is adaptive in nature and that it is responsible for the growth in threonine as the carbon source.     

Fermentative Production of l-Proline with Auxotrophs of Corynebacterium glutamicum

Two auxotrophic mutants of Corynebacterium glutamicum were found to produce a large amount of l-proline in the culture medium. High concentration of MgSO₄ or MnSO₄ in the medium stimulated the l-proline production by an isoleucine auxotroph. Optimum concentration of l-isoleucine was 200 μg/ml, and the higher concentration of l-isoleucine reduced the l-proline production. The auxotroph produced 14.8 mg/ml of l-proline when cultured in a medium containing 12% glucose, 1.7% NH₄C1,0.6% MgSO₄·7H₂O, 0.06% MnSO₄·4H₂O and 200 μg/ml of l-isoleucine. The other mutant, whose growth responds to the bases of nucleic acids, produced 7 to 13 mg/ml of l-proline in a cane molasses (15%, as glucose concentration)-medium containing 2% of the acid-hydrolyzate of soybean meal. The l-proline production by this mutant increased to a level of 27 to 31 mg/ml when the growth was suppressed by the addition of 4% NH₄C1 to the medium, or by the addition of 2 mg/ml of polyoxyethylenestearylamine, a surfactant, to a culture at an appropriate stage of the fermentation.     

Studies on l-Threonine Fermentation

Fifteen strains of bacteria were treated with ultraviolet light or N-methyl-N′-nitro-N-nitrosoguanidine to derive auxotrophic mutants, which were screened for their ability to produce l-threonine. A number of auxotrophs were derived from each strain. Among them, those which produced a large amount of l-threonine were found in Aerobacter aerogenes, Serratia marcescens and Escherichia coli, the members of the family Enterobacteriaceae. Nutritional requirements of these threonine producers were proved to be methionine, lysine, or α, ε-diaminopimelic acid (DAP).

In A. aerogenes and E. coli, double and triple auxotrophs were derived with futher mutational treatment. As a, rule, imposition of additional block led to the increase of l-threonine production. In E. coli, many triple auxotrophs (DAP^?, Met^?, He^?) and their isoleucine revertants were screened for their ability to produce l-threonine. Enhancement of l-threonine production was achieved with these mutants.

One of the isoleucine revertants, KY8280, was used to investigate some cultural conditions. As a result, l-threonine accumulation reached to a level of 13.8 mg/ml with the medium containing 7.5% fructose.     

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.     

Studies on the the Isoleucine Fermentation

Accumulation of L-isoleucine and L-valine was studied on 14 genera, 47 species and 110 strains of aerobic bacteria using bacterial type cultures. A large amount of L-isoleucine and a small amount of L-valine accumulated when 1% of DL-α-aminobutyric acid was added to the culture medium. As a rule, facultative aerobes such as Aerobacter, Erwinia, Serratia and Bacillus showed good accumulation. In the absence of α-aminobutyric acid, powerful L-isoleucine accumulators produced a large amount of L-valine, although the accumulation of L- isoleucine was scarcely observed under that condition. In the presence of α-aminobutyric acid, the accumulation of L-valine was generally suppressed, but in several strains, on the contrary, the accumulation increased as well as that of L-isoleucine. When DL-threonine was used instead of α-aminobutyric acid, the amount of L-isoleucine accumulated was not as high as that with α-aminobutyric acid in almost all strains except Serratia marcescens. It was concluded that a distinct relationship between bacterial genera or species and accumulation of L-isoleucine did not exist, that is, powerful accumulators were limited to special strains, and that the addition of α-aminobutyric acid was necessary for the accumulation of a large amount of L-isoleucine.     

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.     

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.     

Purification,Crystallization and Properties of Tryptophanase from Proteus rettgeri

An inducible tryptophanase was crystallized from the cell extract of Proteus rettgeri grown in a medium containing l-tryptophan. The purification procedure included ammonium sulfate fractionation, heat treatment, DEAE-Sephadex and hydroxylapatite column chromatographies. Crystals were obtained from solutions of the purified enzyme by the addition of ammonium sulfate.

The crystalline enzyme preparation was homogeneous by the criteria of ultracentrifugation and zone electrophoresis. The molecular weight was determined to be approximately 210,000.

The crystalline enzyme catalyzed the degradation of l-tryptophan into indole, pyruvate and ammonia in the presence of added pyridoxal phosphate. The enzyme also catalyzed pyruvate formation from 5-hydroxy-l-tryptophan, 5-methyl-l-tryptophan, S-methyl-l-cysteine and l- cysteine. l-, d-Alanine, l-phenylalanine and indole inhibited pyruvate formation from these substrates.