Effects of Acetylation with Acetic Anhydricle

1. L-Asparaginase (EC 3.5.1.1) from Escherichia coli A–l–3 was acetylated using acetic anhydride as a modifying chemical. The fully acetylated L-asparaginase retained 60% of the activity of the unmodified L-asparaginase.

2. The acetylated L-asparaginase hydrolyzed D-asparagine and L-glutamine as well as L-asparagine in the same ratio as the unmodified L-asparaginase did.

3. However, the effects of pH on the activity of the acetylated L-asparaginase showed very interesting differences from that of L-asparaginase. On the other hand, both L-asparaginase and the acetylated L-asparaginase exhibited similar pH activity curves on L-glutamine hydrolysis.

4. The acetylated L-asparaginase was found to become more stable against acid or heat in the presence of L-aspartate than in its absence in the same manner as L-asparaginase was.

     

l-Asparaginase from Escherichia coli

Crystalline l-asparaginase from Escherichia coli A-I-3 hydrolyzed d-asparagine, l- and d-glutamine but at much slower rates than the rate at which it hydrolyzed l-asparagine. Inhibitions by these substrates and related compounds were revealed to be competitive.

d-Asparagine showed the same affinity for the enzyme both in its hydrolysis and inhibition of l-asparagine hydrolysis. l-Aspartate, d-aspartate and α-N-ethylasparagine inhibited various hydrolysis reactions with the respective inhibitor constants. The enzyme was found to hydrolyze β-methylaspartate as well as β-aspartohydroxamate. These data strongly suggest that the hydrolysis occurred at the same active site of the enzyme molecule with relatively low specificity for the configuration of the substrate molecule and the kind of bonding which it hydrolyzes.     

Partial Purification and Some Properties of Extracellular Asparaginase from Candida utilis

Extracellular asparaginase from Candida utilis was partially purified by precipitation with acetone and by column chromatography on DEAE Sephadex A-50 and Sephadex G-200. The specific activity of the enzyme preparation was 3900 units per mg of protein. Candida asparaginase characteristically had deaminating activity for d-asparagine as well as for l-asparagine. But this enzyme was not able to hydrolyzed l- or d-glutamine. SH inhibitor, chelating agents and metal ions did not show any inhibition or activation of l-asparaginase activity. Optimum pH was about 6 for both l- and d-asparagine. This asparaginase was stable between pH 4 and pH 10 in heating for 10 min at 50°C.     

Therapeutic l-asparaginase: upstream,downstream and beyond

l-asparaginase (l-asparagine amino hydrolase, E.C.3.5.1.1) is an enzyme clinically accepted as an antitumor agent to treat acute lymphoblastic leukemia and lymphosarcoma. It catalyzes l-asparagine (Asn) hydrolysis to l-aspartate and ammonia, and Asn effective depletion results in cytotoxicity to leukemic cells. Microbial l-asparaginase (ASNase) production has attracted considerable attention owing to its cost effectiveness and eco-friendliness. The focus of this review is to provide a thorough review on microbial ASNase production, with special emphasis to microbial producers, conditions of enzyme production, protein engineering, downstream processes, biochemical characteristics, enzyme stability, bioavailability, toxicity and allergy potential. Some issues are also highlighted that will have to be addressed to achieve better therapeutic results and less side effects of ASNase use in cancer treatment: (a) search for new sources of this enzyme to increase its availability as a drug; (b) production of new ASNases with improved pharmacodynamics, pharmacokinetics and toxicological profiles, and (c) improvement of ASNase production by recombinant microorganisms. In this regard, rational protein engineering, directed mutagenesis, metabolic flux analysis and optimization of purification protocols are expected to play a paramount role in the near future.     

Effects of a Feedback-Resistant Aspartokinase III Gene on L-Isoleucine Production in Escherichia coli K-12

An L-isoleucine-overproducing recombinant strain of E. coli, TVD5, was also found to overproduce L-valine. The L-isoleucine productivity of TVD5 was markedly decreased by addition of L-lysine to the medium. Introduction of a gene encoding feedback-resistant aspartokinase III increased L-isoleucine productivity and decreased L-valine by-production. The resulting strain accumulated 12 g/l L-isoleucine from 40 g/l glucose, and suppression of L-isoleucine productivity by L-lysine was relieved.     

Protective Actions of l-Aspartate from Acid or Proteolytic Inactivation

1. l-Aspartate was found to replace l-asparagine in the protective action from acid inactivation of l-asparaginase (EC 3.5.1.1) produced by Escherichia coli A–1–3 and at the same time to inhibit the proteolytic inactivation by α-chymotrypsin.

2. l-Asparaginase changed in its chromatographic properties in the presence of l-aspartate and became to be absorbed on the CM Sephadex column.

3. The sedimentation patterns of l-asparaginase at pH 3.5 were identical either in the presence or absence of l-aspartate, showing partial dissociation. But the reversibility to the active state was observed only in the enzyme dissolved in the solution containing l-aspartate.

4. l-Aspartate did not prevent the enzyme either from the dissociation into subunits or from decrease in the activity by urea.

5. High concentration of l-aspartate was shown to inhibit the l-asparagine hydrolysis reaction.

6. l-Aspartate was suggested from ORD measurements to cause changes in the higher structure as well as the ionic properties or proteolytic inactivation.

     

Production of l-rhamnulose,a rare sugar,from l-rhamnose using commercial immobilized glucose isomerase

Abstract

A commercial immobilized d-glucose isomerase from Streptomyces murines (Sweetzyme) was used to produce l-rhamnulose from l-rhamnose in a packed-bed reactor. The optimal conditions for l-rhamnulose production from l-rhamnose were determined as pH 8.0, 60?°C, 300?g L^?1 l-rhamnose as a substrate, and 0.6?h^?1 dilution rate. The half-life of the immobilized enzyme at 60?°C was 809?h. Under the optimal conditions, the immobilized enzyme produced an average of 135?g L^?1 l-rhamnulose from 300?g L^?1 l-rhamnose after 16 days at pH 8.0, 60?°C, and 0.6?h^?1 dilution rate, with a productivity of 81?g/L/h and a conversion yield of 45% in a packed-bed reactor.     

Membrane-Integrated Fermentation System for Improving the Optical Purity of D-Lactic Acid Produced during Continuous Fermentation

This report describes the production of highly optically pure D-lactic acid by the continuous fermentation of Sporolactobacillus laevolacticus and S. inulinus, using a membrane-integrated fermentation (MFR) system. The optical purity of D-lactic acid produced by the continuous fermentation system was greater than that produced by batch fermentation; the maximum value for the optical purity of D-lactic acid reached 99.8% enantiomeric excess by continuous fermentation when S. leavolacticus was used. The volumetric productivity of the optically pure D-lactic acid was about 12 g/L/h, this being approximately 11-fold higher than that obtained by batch fermentation. An enzymatic analysis indicated that both S. laevolacticus and S. inulinus could convert L-lactic acid to D-lactic acid by isomerization after the late-log phase. These results provide evidence for an effective bio-process to produce D-lactic acid of greater optical purity than has conventionally been achieved to date.     

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.     

Enzymatic activity of L-amino acid oxidase from snake venom Crotalus adamanteus in supercritical CO2

L-amino acid oxidase (L-AAO) from snake venom Crotalus adamanteus was successfully tested as a catalyst in supercritical CO₂ (SC-CO₂). The enzyme activity was measured before and after exposure to supercritical conditions (40°C, 110 bar). It was found that L-AAO activity slightly increased after SC-CO₂ exposure by up to 15%. L-AAO was more stable in supercritical CO₂ than in phosphate buffer under atmospheric pressure, as well as in the enzyme membrane reactor (EMR) experiment. 3,4-Dihydroxyphenyl-L-alanine (L-DOPA) oxidation was performed in a batch reactor made of stainless steel that could withstand the pressures of SC-CO₂, in which L-amino acid oxidase from C. adamanteus was able to catalyze the reaction of oxidative deamination of L-DOPA in SC-CO₂. For the comparison L-DOPA oxidation was performed in the EMR at 40°C and pressure of 2.5 bar. Productivity expressed as mmol-s of converted L-DOPA after 3?h per change of enzyme activity after 3?h was the highest in SC-CO₂ (1.474?mmol?U^?1), where catalase was present, and the lowest in the EMR (0.457?mmol?U^?1).     

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.     

Production of 3,4-Dihydroxyphenyl-L-alanine (L-DOPA) and Its Derivatives by Vibrio tyrosinaticus

Six strains of bacteria belonging to Vibrio and Pseudomonas were selected as good producers of L-DOPA from L-tyrosine out of various bacteria. The condition for the formation of L-DOPA by Vibrio tyrosinaticus ATCC 19378 was examined and the following results were obtained. (1) Intermittent addition of L-tyrosine in small portions gave higher titer of L-DOPA than single addition of L-tyrosine. (2) Higher amount of L-DOPA was produced in stationary phase of growth than in logarithmic phase. (3) Addition of antioxidant, chelating agent or reductant such as L-ascorbic acid, araboascorbic acid, hydrazine, citric acid and 5-ketofructose increased the amount of L-DOPA formed. (4) L-Tyrosine derivatives such as N-acetyl-L-tyrosine amide, N-acetyl-L-tyrosine, L-tyrosine amide, L-tyrosine methyl ester and L-tyrosine benzyl ester were converted to the corresponding L-DOPA derivatives.

In the selected condition about 4 mg/ml of L-DOPA was produced from 4.3 mg/ml of L-tyrosine.     

Cloning,Expression, and Identification of Genes Involved in the Conversion of DL-2-Amino-Δ2-thiazoline-4-carboxylic Acid to L-Cysteine via S-Carbamyl-L-cysteine Pathway in Pseudomonas sp. TS1138

Two novel genes (tsB, tsC) involved in the conversion of DL-2-amino-Δ²-thiazoline-4-carboxylic acid (DL-ATC) to L-cysteine through S-carbamyl-L-cysteine (L-SCC) pathway were cloned from the genomic DNA library of Pseudomonas sp. TS1138. The recombinant proteins of these two genes were expressed in Escherichia coli BL21, and their enzymatic activity assays were performed in vitro. It was found that the tsB gene encoded an L-ATC hydrolase, which catalyzed the conversion of L-ATC to L-SCC, while the tsC gene encoded an L-SCC amidohydrolase, which showed the catalytic ability to convert L-SCC to L-cysteine. These results suggest that tsB and tsC play important roles in the L-SCC pathway and L-cysteine biosynthesis in Pseudomonas sp. TS1138, and that they have potential applications in the industrial production of L-cysteine.     

L-Tyrosine production by Polyauxotrophic Mutants of Corynebacterium glutamicum

Polyauxotrophic mutants of Corynebacterium glutamicum which have additional requirements to L-phenylalanine were derived from L-tyrosine producing strains of phenylalanine auxotrophs, C. glutamicum KY 9189 and C. glutamicum KY 10233, and screened for L-tyrosine production. The increase of L-tyrosine production was noted in many auxotrophic mutants derived from both strains. Especially some double auxotrophs which require phenylalanine and purine, phenylalanine and histidine, or phenylalanine and cysteine produced significantly higher amounts of L-tyrosine compared to the parents, A phenylalanine and purine double auxotrophic strain LM–96 produced L-tyrosine at a concentration of 15.1 mg per ml in the medium containing 20% sucrose. L-Tyrosine production by the strain decreased at high concentrations of L-phenylalanine.     

Breeding of a Cyclic Imide-Assimilating Bacterium,Pseudomonas putida s52, for High Efficiency Production of Pyruvate

A succinimide-assimilating bacterium, Pseudomonas putida s52, was found to be a potent producer of pyruvate from fumarate. Using washed cells from P. putida s52 as catalyst, 400 mM pyruvate was produced from 500 mM fumarate in a 36-h reaction. Bromopyruvate, a malic enzyme inhibitor, was used for the selection of mutants with higher pyruvate productivity. A bromopyruvate-resistant mutant, P. putida 15160, was found to be an effective catalyst for pyruvate production. Moreover, under batch bioreactor conditions, 767 mM of pyruvate was successfully produced from 1,000 mM fumarate in a 72-h reaction with washed cells from P. putida 15160 as catalyst.     

L-Tyrosine Production by Analog-resistant Mutants Derived from a Phenylalanine Auxotroph of Corynebacterium glutamicum

Mutants resistant to various phenylalanine- or tyrosine-analogs were isolated from a phenylalanine auxotroph of Corynebacterium glutamicum KY 10233 by treatment with N- methyl-N′-nitro-N-nitrose guanidine (NTG) and screened for L-tyrosine production. A mutant, 98–Tx–71, which is resistant to 3-aminotyrosine, p-aminophenylalanine, p-fluoro-phenylalanine, and tyrosine hydroxamate was found to produce L-tyrosine at a concentration of 13.5 mg/ml in the cane molasses medium containing 10% of sugar calculated as glucose. A tyrosine-sensitive mutant, pr–20 which was derived from 98–Tx–71 produced L-tyrosine at a concentration of 17.6 mg/ml. L-Tyrosine formation in the strain pr–20 was found to be still inhibited by L-phenylalanine though it was not inhibited by L-tyrosine. The L-tyrosine formation in the mutant was repressed neither by L-phenylalanine nor by L-tyrosine.     

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.     

Culture Conditions for the Production of l-Glutamic Acid from n-Paraffins by Glycerol Auxotroph GL-21

A novel process for the microbial production of l-glutamic acid on an industrial scale was successfully established by using a glycerol auxotroph.

The most suitable carbon source for producing L-glutamic acid was n-paraffins (C₁₃–C₁₅). The production of L-glutamic acid was not affected by a large amount of biotin or oleic acid in the absence of penicillin, and occurred maximally at the glycerol concentration of 0.02% at pH 6.6. The most effective temperature was 28°C.

Under optimal conditions in a 200 liter fermentor, the mutant produced 72 g/liter of L-glutamic acid. On the other hand, the parent produced 53 g/liter of L-glutamic acid in the presence of penicillin.

It is believed that the low productivity of L-glutamic acid by the parent strain was mainly due to the occurrence of the marked decrease in the viable cell counts at the later phase of the fermentation caused by the action of penicillin added.     

New Resolving Agents

Seven optical active 2-benzylamino alcohols were synthesized by reduction of N-benzoyl derivatives of L-alanine, L-valine, L-leucine, L-phenylalanine, L-aspartic acid, L-glutamic acid and L-lysine and applied for the resolution of (±)-trans-chrysanthemic acid. d-trans-Chrys-anthemic acid was obtained by resolution via the salts of 2-benzylamino alcohols derived from L-valine and L-leucine, while (?)-trans-chrysanthemic acid was prepared through the salts of the amino alcohols derived from L-alanine and L-phenylalanine.