Enzymatic Production of l-Citrulline by Pseudomonas putida

To develop an efficient method for the production of l-citrulline, optimum conditions for the conversion of l-arginine to l-citrulline by microbial l-arginine deiminase and for production of the enzyme were studied. A number of micro-organisms were screened to test their ability to form and accumulate l-citrulline from l-arginine. Pseudomonas putida was selected as the best organism. With this organism, enzyme activity as high as 9.20 units per ml could be produced by a shaking culture at 30 C in a medium containing glucose, ammonium phosphate, l-arginine hydrochloride, yeast extract, peptone, and inorganic salts. Appropriate addition of a surface active agent to the reaction mixture was found to shorten the time required for the conversion. A large amount of l-arginine hydrochloride was converted stoichiometrically to l-citrulline in 62 hr at 37 C. Accumulated l-citrulline was readily isolated in pure form by ordinary procedures with ion-exchange resins. Yields of isolated l-citrulline of over 90.5% from l-arginine hydrochloride were easily attainable.     

Immobilization of Escherichia coli Cells Containing Aspartase Activity with Polyurethane and Its Application for l-Aspartic Acid Production

Whole cells of Escherichia coli containing aspartase activity were immobilized by mixing a cell suspension with a liquid isocyanate-capped polyurethane prepolymer (Hypol). The immobilized cell preparation was used to convert ammonium fumarate to l-aspartic acid. Properties of the immobilized E. coli cells containing aspartase were investigated with a batch reactor. A 1.67-fold increase in the l-aspartic acid production rate was observed at 37 degrees C as compared to 25 degrees C operating temperature. The pH optimum was broad, ranging from 8.5 to 9.2. Increasing the concentration of ammonium fumarate to 1.5 M from 1.0 M negatively affected the reaction rate. l-Aspartic acid was produced at an average rate of 2.18 x 10 mol/min per g (wet weight) of immobilized E. coli cells with a 37 degrees C substrate solution consisting of 1.0 M ammonium fumarate with 1 mM Mg (pH 9.0).     

Enzymatic Production of Urocanic Acid by Achromobacter liquidum

To develop an efficient method for the production of urocanic acid, optimal conditions for the production of microbial L-histidine ammonia lyase and for the conversion of L-histidine to urocanic acid by this enzyme were studied. A number of microorganisms were screened to test their ability to form and accumulate urocanic acid from L-histidine. Achromobacter liquidum was selected as the best organism. With this organism, enzyme activity as high as 2.0 units/ml could be produced by a shaking culture at 30 C in a medium containing glucose, urea, potassium phosphate, L-histidine, yeast extract, peptone, and inorganic salts. Appropriate addition of a surface-active agent to the reaction mixture shortened the time required for the conversion. A large amount of L-histidine was converted stoichiometrically to urocanic acid in 48 h at 40 C. Accumulated urocanic acid was readily isolated in pure form by ordinary procedures with isoelectric precipitation. Yields of isolated urocanic acid of over 92% from L-histidine were easily attainable. When the culture of Achromobacter liquidum was added to DL-histidine, D-histidine and urocanic acid were simultaneously obtained in high yields.     

Protease from Sporosarcina sp. RRLJ 1

Protease was isolated from Sporosarcina RRLJ1 which was collected from acid tea (Camellia sinensis) plantations. It showed potential for production of the enzyme for commercial purposes. The study revealed that optimum pH for growth of the organism was 6.5-7 and supplement of casein (1%) in the medium was required for production of protease. Enzyme production and enzyme activity was maximum in 72 hr old broth culture. Maximum activity of the enzyme was found at pH 6.5.     

Production of L-proline by Kurthia catenaforma

A number of organisms were screened for their ability to produce l-proline. Kurthia catenaforma, which we recently isolated, was selected. A serine-requiring mutant, strain 45, produced about 1.5 times the amount of this amino acid that the parent strain did. In investigations of various media, it was found that approximately 30 ml of l-proline per ml was produced in shaken culture at 30 C in a medium containing glucose, urea, corn steep liquor, casein hydrolysate, l-aspartic acid, and inorganic salts. To study the effect of l-aspartic acid on the production of l-proline, various amino or organic acids were substituted for l-aspartic acid, and the changes during fermentation were investigated. l-Aspartic acid was not replaced by the compounds tested, and this acid appeared to increase growth during the later stages of fermentation with a concurrent increase in the production of l-proline.     

A C-NMR study on the influxes into the tricarboxylic acid cycle of a renal epithelial cell line, LLC-PK1/Cl4: the metabolism of [2-C]glycine, l-[3-C]alanine and l-[3-C]aspartic acid in renal epithelial cells

Perchloric acid extracts of LLC-PK₁/Cl₄ cells, a renal epithelial cell line, incubated with either [2-¹³C]glycine l-[3-¹³C]alanine, or d,l-[3-¹³C]aspartic acid were investigated by ¹³C-NMR spectroscopy. All amino acids, except labelled glycine, gave rise to glycolytic products and tricarboxylic acid cycle (TCA) intermediates. For the first time we also observed activity of γ-glutamyltransferase activity and glutathione synthetase activity in LLC-PK₁ cells, as is evident from enrichment of reduced glutathione. Time courseS showed that only 6% of the labelled glycine was utilized in 30 min, whereas 31% of l-alanine and 60% of l-aspartic acid was utilized during the same period. ¹³C-NMR was also shown to be a useful tool for the determination of amino acid uptake in LLC-PK₁ cells. These uptake experiments indicated that glycine alanine and aspartic acid are transported into Cl₄ cells via a sodium-dependent process. From the relative enrichment of the glutamate carbons, we calculated the activity of pyruvate dehydrogenase to be about 61% of when labelled l-alanine was the only carbon source for LLC-PK₁/Cl₄ cells. Experiments with labelled d,l-aspartic, however, showed that about 40% of C-3-enriched oxaloacetate (arising from a de-amination of aspartic acid) reached the pyruvate pool.     

Characteristics of levan fructotransferase from Arthrobacter ureafaciens K2032 and difructose anhydride IV formation from levan

A microorganism producing levan fructotransferase was isolated from sugar-disclosed soil and it was identified as Arthrobacter ureafaciens. The major product from levan by enzyme reaction was identified as di-D-fructofuranose 2,6':6,2' dianhydride by mass spectrometry, nuclear magnetic resonance, and chemical analyses. Small amounts of several oligosaccharides and free fructose were also formed by enzyme reaction. An extracellular enzyme that produces di-D-fructofuranose 2,6':6,2' dianhydride from levan was purified from the culture broth of A. ureafaciens K2032. The enzyme had optimum activity around pH 5.8 and 45 degrees C and had a dimeric form in solution. The N-terminal amino acid residues of the purified enzyme were SAPGSLRAVYHMTPPSGXLXDPQ. The enzyme has narrow substrate range and converts the levan to di-D-fructofuranose 2,6':6,2' dianhydride with around 62.5% conversion yield.     

Production of Coenzyme A by Sarcina lutea

To develop an efficient method for the production of coenzyme A (CoA), optimal conditions for its formation from pantothenic acid, cysteine, and adenine were studied. A number of microorganisms were screened for production of CoA. Strains belonging to the genera Sarcina, Bacillus, Microbacterium, Micrococcus, and Serratia accumulated CoA. Among these, Sarcina lutea was selected as the best organism, and the culture conditions for the production of CoA were investigated with this organism. Under optimal conditions, 600 mug of CoA per ml was accumulated in the culture broth. CoA was readily isolated in high purity by the use of charcoal, diethylaminoethyl-cellulose, Sephadex G-25, and Dowex-50. Yields of isolated CoA were over 33% from culture broth.     

Effect of alanine, leucine and fructose on lysyl-transfer ribonucleic acid ligase activity in a mutant of Escherichia coli K-12

A mutant of Escherichia coli K-12 was examined which has growth medium-dependent lysyl-transfer ribonucleic acid (tRNA) ligase activity. In minimal medium or 0.5% yeast extract, the activity of the enzyme in the mutant strain was 5 to 10% of wild type. However, when the mutant was grown in a highly enriched medium, such as AC broth (Difco), the activity of the mutant ligase increased 10- to 20-fold. We found that the supplementation of 0.5% yeast extract by l-alanine plus d-fructose replaces the need for the highly enriched medium. Fructose plus l-leucine and fructose plus l-alpha-amino-n-butyric acid were also stimulatory, but not as effective as fructose and alanine. With minimal medium, a combination of carbohydrate (fructose or glucose) plus alanine and leucine was required to replace the enriched medium. The most effective combination was fructose, glucose, alanine, and leucine. Lysyl-tRNA ligase was stimulated 1.5 to 2-fold in the wild-type strain or Hfr H (Hayes) by fructose plus alanine when these strains were cultured in 0.5% yeast extract. Experiments employing the combined technique of density labeling with D(2)O and isopycnic centrifugation in cesium chloride indicated that the increased activity of lysyl-tRNA ligase observed in AC broth or in the presence of fructose, glucose, alanine, and leucine is due to the synthesis of new enzyme.     

Characterization of a Heat-Stable Protease of Pseudomonas fluorescens P26

A heat-stable, extracellular proteolytic enzyme was isolated from Pseudomonas fluorescens P26. Brain heart infusion broth (Fisher Scientific Co.), pH 7.5, and incubation at 21 C provided the optimal conditions for bacterial growth for enzyme production. The organism had a D value of 2.6 min at 62.8 C (145 F). The enzyme, however, was quite heat-stable, requiring 15 hr at 62.8 C, 8 hr at 71.4 C, and 9 min at 121 C for complete inactivation. Milk, whey, and casein each had a protective effect on the enzyme against heat inactivation. Purification was accomplished by growth of organisms in broth, centrifugation, sterilization by filtration, ammonium sulfate precipitation (55% saturation), dialysis (against six changes of water), and protein separation by passage through a Sephadex G-100 column. Ultracentrifugation revealed a single band with a sedimentation coefficient of 1.51 which suggested a molecular weight of approximately 23,000. As little as 0.2 unit of the purified enzyme caused detectable flavor defects during 30 days of storage at 4 C, and the Hull test for liberation of tyrosine compared favorably in sensitivity with the sensory method in milk.     

Phosphatase Activity Among Candida Species and Other Yeasts Isolated from Clinical Material

A group of 277 yeasts isolated from burned children and 14 reference strains were tested for phosphatase activity by using phenolphthalein phosphate substrates. Phosphatase activity was widely distributed among various species and strains representing seven genera. Candida albicans, which was the most common yeast isolated from clinical material, was notably absent in producing the enzyme, whereas Candida tropicalis was the most consistent, strong, and rapidly active phosphatase-producing organism. The characteristic enzyme activity of a selected isolate of C. tropicalis was demonstrated in the presence of concentrations of inorganic phosphate which inhibited enzyme activity of other species. The greater enzyme activity of C. tropicalis was not related to more rapid or greater cell growth or decrease in the pH of culture media. Extracellular constitutive heat-labile acid phosphatase was found in broth filtrates of C. tropicalis, C. krusei, and a strain of Staphylococcus aureus.     

Enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by Flavobacterium sp.

An enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by the action of hydantoinase and carbamoylase has been investigated. A strain identified as (Flavobacterium) sp. I-3 isolated from soil was found to form l-tryptophan from dl-5-indolylmethylhydantoin. Cultural conditions for the formation of the l-tryptophan-forming activity were investigated, and the highest activity of 0.81 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth (hydantoinase, 3.6 μmol min⁻¹of N-carbamoyl-l-tryptophan formed per 1 ml of culture broth; carbamoylase, 0.92 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth) was obtained. These activities were found to be inducible and intracellular. Optimization of the parameters of the conversion reaction resulted in accumulation of 50 mg of l-tryptophan per 1 ml of cultural broth per day. The conversion yield from dl-5-indolylmethylhydantoin was about 100%. Accumulated l-tryptophan was readily isolated in pure form by ordinary procedures.     

l-Alanine as a precursor of ethylamine in Camellia sinensis

After absorption of ammonium nitrogen, nitrogen-deficient Camellia sinensis synthesized theanine following synthesis of glutamic acid and alanine. The rate of incorporation of ¹⁴C from l-alanine U-¹⁴C into theanine was faster than from acetaldehyde 1–2¹⁴4C. Incorporation of ¹⁴C from l-alanine U-¹⁴C into the ethylamide of theanine was prevented by adding an excess of ethylamine to the culture solution. Green seedlings converted alanine to ethylamine more rapidly than did etiolated seedlings.     

Purification and properties of cytosolic alanine aminotransferase from the liver of two freshwater fish, Clarias batrachus and Labeo rohita

Cytosolic alanine aminotransferase (c-AAT) was purified up to 203- and 120-fold, from the liver of two freshwater teleosts Clarias batrachus (air-breathing, carnivorous) and Labeo rohita (water-breathing, herbivorous), respectively. The enzyme from both fish showed similar elution profiles on a DEAE-Sephacel ion exchange column. SDS-PAGE of purified enzymes revealed two subunits of 54 and 56 kDa, in both fish. The apparent Km values for l-alanine were 18.5+/-0.48 and 23.55+/-0.60 mM, whereas for 2-oxoglutarate the Km values were observed to be 0.29+/-0.023 and 0.33+/-0.028 mM for the enzyme from C. batrachus and L. rohita, respectively. With l-alanine as substrate, aminooxyacetic acid was found to act as a competitive inhibitor with KI values of 6.4 x 10(-4) and 3.4 x 10(-4) mM with c-AAT of C. batrachus and L. rohita, respectively. However, when 2-oxoglutarate was used as substrate, aminooxyacetic acid showed uncompetitive inhibition with similar KI values for purified c-AAT from both fish. Temperature and pH profiles of the enzyme did not show any marked differences between the two fish examined. These results suggest that liver c-AAT, isolated from these two fish species adapted to different modes of life, remain unaltered structurally. However, at the kinetic level, liver c-AAT from C. batrachus exhibits significantly higher affinity for the substrate l-alanine and decreased affinity for its metabolic inhibitor, in comparison to that of the enzyme purified from L. rohita. Such functional changes seem to be of physiological significance and also provide preliminary evidence for subtle changes in the enzyme as a mark of metabolic adaptation in the fish to different physiological demands.     

Expression of alr gene from Corynebacterium glutamicum ATCC 13032 in Escherichia coli and molecular characterization of the recombinant alanine racemase

We constructed the high-expression system of the alr gene from Corynebacterium glutamicum ATCC 13032 in Escherichia coli BL 21 (DE3) to characterize the enzymological and structural properties of the gene product, Alr. The Alr was expressed in the soluble fractions of the cell extract of the E. coli clone and showed alanine racemase activity. The purified Alr was a dimer with a molecular mass of 78 kDa. The Alr required pyridoxal 5'-phosphate (PLP) as a coenzyme and contained 2 mol of PLP per mol of the enzyme. The holoenzyme showed maximum absorption at 420 nm, while the reduced form of the enzyme showed it at 310 nm. The Alr was specific for alanine, and the optimum pH was observed at about nine. The Alr was relatively thermostable, and its half-life time at 60 degrees C was estimated to be 26 min. The K(m) and V(max) values were determined as follows: l-alanine to d-alanine, K(m) (l-alanine) 5.01 mM and V(max) 306 U/mg; d-alanine to l-alanine, K(m) (d-alanine) 5.24 mM and V(max) 345 U/mg. The K(eq) value was calculated to be 1.07 and showed good agreement with the theoretical value for the racemization reaction. The high substrate specificity of the Alr from C. glutamicum ATCC 13032 is expected to be a biocatalyst for d-alanine production from the l-counter part.     

Production of a fibrinolytic enzyme by thermophilic Streptomyces species

A strong fibrin-specific fibrinolytic enzyme was purified from the cell-free spent culture broth of a thermophilic organism, Streptomyces megasporus SD5. The strain could produce 150 mg crude protein per litre of spent broth, with a specific activity of 80 IU (Plough units) per milligram, within 18 h of incubation at 55 °C in glucose yeast/extract/peptone (GYP) medium, pH 8.0. For production of the enzyme, the strain could utilize different carbon and nitrogen sources with a C:N ratio of ∼ 1:2. The enzyme was stable at a broad range of pH ranging from 5 to 9, and highly thermostable with 50% activity after storage at 60 °C for 6 months. The enzyme belonged to the serine endopeptidase group. In vitro clot lysis revealed that the enzyme was active at 37 °C. This revised version was published online in July 2006 with corrections to the Cover Date.     

The production of succinic acid by yeast Yarrowia lipolytica through a two-step process

The production of α-ketoglutaric acid by yeast Yarrowia lipolytica VKMY-2412 from ethanol and its subsequent chemical conversion to succinic acid (SA) were investigated. A highly effective and environmentally friendly process of α-ketoglutaric acid production was developed using a special pH-controlling strategy, in which the titration of the culture broth with KOH in the acid-formation phase was minimal, that allowed accumulation of only low amounts of inorganic wastes in the course of SA recovery. The culture broth filtrate containing α-ketoglutaric acid (88.7 g l^?1) was directly employed for SA production; the amount of SA produced comprised 71.7 g l^?1 with the yield of 70 % from ethanol consumed. SA was isolated from the culture broth filtrate in a crystalline form with the purity of 100 %. The yield of isolated SA was as high as 72 % of its amount in the culture broth filtrate. The antimicrobial and nematocidic effects of SA of microbial origin on pathogenic organisms that cause human and plant diseases were revealed for the first time.     

Production of an extracellular maltase by thermophilic Bacillus sp. KP 1035.

Production of extracellular maltase was studied with thermophilic Bacillus sp. KP 1035, which was selected as the organism producing the highest levels of maltase. The final enzyme yield was increased by maltose, peptone, and yeast extract but reduced by succinate and fumarate. Maximum enzyme production was achieved at 55 degrees C and at an initial pH of 6.2 to 7.0 on a medium containing 0.3% maltose, 1% peptone, 0.1% meat extract, 0.3% yeast extract, 0.3% KH2PO4, and 0.1% KH2PO4. Maltase was synthesized in cytoplasm and accumulated as a large pool during the logarithmic growth phase, which preceded sporulation. At the end of this phase, the enzyme appeared in the culture broth, and its accumulation increased in parallel with a rise in the extracellular protein level. Maltase was stable for 24 h at 60 degrees C over a pH range of 5.6 to 9.0 and retained 95% of the original activity after treatment for 20 min at 70 degrees C at pH 6.8.     

Production of an extracellular maltase by thermophilic Bacillus sp. KP 1035.

Production of extracellular maltase was studied with thermophilic Bacillus sp. KP 1035, which was selected as the organism producing the highest levels of maltase. The final enzyme yield was increased by maltose, peptone, and yeast extract but reduced by succinate and fumarate. Maximum enzyme production was achieved at 55 degrees C and at an initial pH of 6.2 to 7.0 on a medium containing 0.3% maltose, 1% peptone, 0.1% meat extract, 0.3% yeast extract, 0.3% KH2PO4, and 0.1% KH2PO4. Maltase was synthesized in cytoplasm and accumulated as a large pool during the logarithmic growth phase, which preceded sporulation. At the end of this phase, the enzyme appeared in the culture broth, and its accumulation increased in parallel with a rise in the extracellular protein level. Maltase was stable for 24 h at 60 degrees C over a pH range of 5.6 to 9.0 and retained 95% of the original activity after treatment for 20 min at 70 degrees C at pH 6.8.     

Production of l-Phenylalanine from trans-Cinnamic Acid with Rhodotorula glutinis Containing l-Phenylalanine Ammonia-Lyase Activity

An enzymatic method using l-phenylalanine ammonia-lyase (EC 4.3.1.5) for the rapid conversion of trans-cinnamic acid to l-phenylalanine has been investigated. With Rhodotorula glutinis, enzyme activity as high as 0.3 U/ml of culture broth was obtained. The enzyme activity was kept stable for a relatively long time during cultivation by the addition of l-isoleucine. Optimization of the parameters of the conversion reaction resulted in accumulation of 18 mg of l-phenylalanine per ml of reaction mixture. The conversion yield from trans-cinnamic acid was about 70%. The method may provide a rapid and practical way to produce l-phenylalanine useful as an essential amino acid.