Studies on the Mechanism of Strengthening Fish Gel by Basic Amino Acids

An electro-energizing fermentation (E-E F) method has been developed. In this method, a direct electrical current is applied to a microbial culture to accelerate the reductive metabolism of microorganisms or to impart profitable effects to microbial cells. This E-E F method was applied to l-glutamic acid fermentation by Brevibacterium flavum No. 2247. When glucose was used as a substrate, the addition of 0.01 mm neutral red (NR), redox dye (electron carrier), to the fermentation broth at the beginning of cultivation was effective for l-glutamate (l-Glu) production. A direct current of 200~300 μA/cm² at 1.5 V was applied through out the cultivation of this bacterium. This resulted in about a 10% increase in yield of l-Glu.     

Substrate Specificity of Alkaline Proteinases from Aspergillus sydowi and Aspergillus sulphureus

l-Fucose (l-galactose) dehydrogenase was isolated to homogeneity from a cell-free extract of Pseudomonas sp. No 1143 and purified about 380-fold with a yield of 23 %. The purification procedures were: treatment with polyethyleneimine, ammonium sulfate fractionation, chromatographies on phenyl-Sepharose and DEAE-Sephadex, preparative polyacrylamide gel electrophoresis, and gel filtration on Sephadex G-100. The enzyme had a molecular weight of about 34,000. The optimum pH was at 9 — 10.5 and the isoelectric point was at pH 5.1. l-Fucose and l-galactose were effective substrates for the enzyme reaction, but d-arabinose was not so much. The anomeric requirement of the enzyme to l-fucose was the β-pyranose form, and the reaction product from l-fucose was l-fucono- lactone. The hydrogen acceptor for the enzyme reaction wasNADP⁺, and NAD ⁺ could be substituted for it to a very small degree. Km values were 1.9mm, 19mm, 0.016mm, and 5.6mm for l-fucose, l- galactose, NADP⁺, and NAD⁺, respectively. The enzyme activity was strongly inhibited by Hg^{2 +}, Cd^{2 +}, and PCMB, but metal-chelating reagents had almost no effect. In a preliminary experiment, it was indicated that the enzyme may be usable for the measurement of l-fucose.     

Regulatory Properties of Chorismate Mutase from Corynebacterium glutamicum

Regulatory properties of chorismate mutase from Corynebacterium glutamicum were studied using the dialyzed cell-free extract. The enzyme activity was strongly feedback inhibited by l-phenylalanine (90% inhibition at 0.1~1 mm) and almost completely by a pair of l-tyrosine and l-phenylalanine (each at 0.1~1 mm). The enzyme from phenylalanine auxotrophs was scarcely inhibited by l-tyrosine alone but the enzyme from a wild-type strain or a tyrosine auxotroph was weakly inhibited by l-tyrosine alone (40~50% inhibition, l-tyrosine at 1 mm). The enzyme activity was stimulated by l-tryptophan and the inhibition by l-phenylalanine alone or in the simultaneous presence of l-tyrosine was reversed by l-tryptophan. The Km value of the reaction for chorismate was 2.9 } 10^?3 m. Formation of chorismate mutase was repressed by l-phenylalanine. A phenylalanine auxotrophic l-tyrosine producer, C. glutamicum 98–Tx–71, which is resistant to 3-amino-tyrosine, p-aminophenylanaine, p-fluorophenylalanine and tyrosine hydroxamate had chorismate mutase derepressed to two-fold level of the parent KY 10233. The enzyme in C. glutamicum seems to have two physiological roles; one is the control of the metabolic flow to l-phenylalanine and l-tyrosine biosynthesis and the other is the balanced partition of chorismate between l-phenylalanine-l-tyrosine biosynthesis and l-tryptophan biosynthesis.     

Regulatory Properties of Prephenate Dehydrogenase and Prephenate Dehydratase from Corynebacterium glutamicum

Regulatory properties of the enzymes in l-tyrosine and l-phenyalanine terminal pathway in Corynebacterium glutamicum were investigated. Prephenate dehydrogenase was partially feedback inhibited by l-tyrosine. Prephenate dehydratase was strongly inhibited by l-phenylalanine and l-tryptophan and 100% inhibition was attained at the concentrations of 5 × 10^?2mm and 10^?1mm, respectively. l-Tyrosine stimulated prephenate dehydratase activity (6-fold stimulation at 1 mm) and restored the enzyme activity inhibited by l-phenylalanine or l-tryptophan. These regulations seem to give the balanced synthesis of l-tyrosine and l-phenyl-alanine. Prephenate dehydratase from C. glutamicum was stimulated by l-methionine and l-leucine similarly to the enzyme in Bacillus subtilis and moreover by l-isoleucine and l-histidine. C. glutamicum mutant No. 66, an l-phenylalanine producer resistant to p-fluorophenyl-alanine, had a prephenate dehydratase completely resistant to the inhibition by l-phenylalanine and l-tryptophan.     

Crystallization and Characterization of Polyamine Oxidase from Aspergillus terreus

A thin-layer flow cell system for the determination of l-ascorbic acid by an ascorbate electrode was constructed and several components of this system were investigated. The most preferable conditions for optimum operation of the system were as follows: injection volume 150 μ1, delay coil length 60 cm, flow rate 1 ml/min, temperature 20°C, cell spacer thickness 0.2 mm. The linear response region was 0.2-3.0 mm and 0.02-0.5 mm (original l-ascorbic acid concentration) in the cases of pure oxygen and atmospheric oxygen bubbling, respectively. The relative standard variation at 1.5 mm l-ascorbic acid was 3.1 % for 20 successive assays. The measuring time was 2–3 min for each of these assays.     

Inhibition of l-Alanine Adding Enzyme by Glycine

l-Alanine adding enzymes from Bacillus subtilis and Bacillus cereus which catalyzed l-alanine incorporation into UDPMurNAc were partially purified and the properties of the enzymes were examined. The enzyme from B. subtilis was markedly stimulated by reducing agents including 2-mercaptoethanol, dithiothreitol, glutathione and cysteine. Mn²⁺ and Mg²⁺ activated l-alanine adding activity and their optimal concentrations were 2 to 5 mm and 10 mm, respectively. The optimum pH was 9.5 and the Km for l-alanine was 1.8×10^?4m. l-Alanine adding reaction was strongly inhibited by p-chloromercuribenzoate and N-ethyl-maleimide. Among glycine, l- and d-amino acids and glycine derivatives, glycine was the most effective inhibitor of the l-alanine adding reaction. The enzyme from B. cereus was more resistant to glycine than that from B. subtilis. Glycine was incorporated into UDPMurNAc in place of l-alanine, and the Ki for glycine was 4.2×l0^?3m with the enzyme from B. subtilis. From these data, the growth inhibition of bacteria by glycine is discussed.     

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.     

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-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.     

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.     

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.     

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.     

Distribution of 7-Keto-8-aminopelargonic Acid Synthetase in Bacteria and the Control Mechanism of the Enzyme Activity

The 7-keto-8-aminopelargonic acid (KAPA) synthetase activities of cell-free extracts from various bacteria were investigated. The experiments on the substrate specificity of KAPA synthetase, using crude cell-free extracts from bacteria having high enzyme activity, showed that l-serine and pyruvic acid could replace l-alanine, but that, when the enzyme was partially purified, these compounds were not effective. Many kinds of amino acids such as l-cysteine, l-serine, d-alanine, glycine, d-histidine, and l-histidine, inhibited the enzyme activity. This inhibition was found to be competitive with l-alanine. Pyridoxal 5′-phosphate, which is a cofactor of the enzyme, also inhibited the enzyme activity at high concentrations. The repression of KAPA synthetase by biotin occurred in Bacillus subtilis and B. sphaericus but not in Micrococcus roseus and Pseudomonas fluorescens, even at a concentration of 1000 mµg per ml of biotin.     

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.     

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.     

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.     

Structure of Colletochlorin from Colletotrichum nicotianae

Pseudomonas melanogenum ATCC 17806 required methionine, cysteine, cystine, cystathionine, homocysteine or homocystine for growth. However, the addition of these amino acids decreased remarkably l-DOPA (3,4-dihydroxyphenyl-l-alanine) production by the bacterium. l-DOPA production by the bacterium was further affected by the amount of the substrate, the method of its addition and by the addition of antioxidants, as was the case with Vibrio tyrosinaticus.

Under suitable conditions about 8 mg/ml of l-DOPA were produced from 8.6 mg/ml of l-tyrosine.     

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.     

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.     

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.