Production of N,N′-diacetylchitobiose from chitin using temperature-sensitive chitinolytic enzyme preparations of Aeromonas sp. GJ-18

Summary N,N′-diacetylchitobiose was produced from chitin as a major hydrolytic product by controlling the ratio of β-N-acetylglucosaminidase to N,N′-diacetylchitobiohydrolase activities in the crude enzyme preparation of Aeromonas sp. GJ-18. When the enzyme preparation was preincubated at 50 °C, β-N-acetylglucosaminidase was nearly inactivated, while the N,N′-diacetylchitobiohydrolase was still active. Thus, the composition of chitin oligosaccharides depended on the preincubation temperature of the crude enzyme preparations. Typically, after 7 days of incubation with the substrate chitin, 78.9 and 56.6% of N,N′-diacetylchitobiose yields were obtained from swollen α-chitin and powdered β-chitin, respectively, with enzyme preparations that had been pretreated at 50 °C for 60 min.     

Purification and characterization of enantioselective N-acetyl-β-Phe acylases from Burkholderia sp. AJ110349

For the production of enantiopure β-amino acids, enantioselective resolution of N-acyl β-amino acids using acylases, especially those recognizing N-acetyl-β-amino acids, is one of the most attractive methods. Burkholderia sp. AJ110349 had been reported to exhibit either (R)- or (S)-enantiomer selective N-acetyl-β-Phe amidohydrolyzing activity, and in this study, both (R)- and (S)-enantioselective N-acetyl-β-Phe acylases were purified to be electrophoretically pure and determined the sequences, respectively. They were quite different in terms of enantioselectivities and in their amino acids sequences and molecular weights. Although both the purified acylases were confirmed to catalyze N-acetyl hydrolyzing activities, neither of them show sequence similarities to the N-acetyl-α-amino acid acylases reported thus far. Both (R)- and (S)-enantioselective N-acetyl-β-Phe acylase were expressed in Escherichia coli. Using these recombinant strains, enantiomerically pure (R)-β-Phe (>99% ee) and (S)-β-Phe (>99% ee) were obtained from the racemic substrate.     

Structures of Conversion Products Formed from 18β-Glycyrrhetinic Acid by Streptomyces sp. G-20

Dynamic profiles of the rate of O₂ generation from press-injured and inoculated rice leaf slices, versus the time after inoculation, discriminated between the incompatible and compatible combination of blast fungus races with a cultivar. The application of sodium saccharin to rice seedlings via the root system for 6 days changed the compatible to incompatible profile. Even after press- injury and inoculation with the compatible conidia, the leaf application of sodium saccharin enhanced superoxide generation. The application of N-methylsaccharin in a similar manner, however, did not enhance the superoxide generation. Inoculation of press-injured leaves with incompatible conidia in the presence of an aqueous diffusate of the germinating compatible conidia changed the incompatible to compatible profile. The application to press-injured of concanavalin A or a lyophylized preparation from 5 m ammonia extracts of rice leaf homogenate prior to stimulating with a resistance-inducing factor (RIF) from the fungus also enhanced the superoxide generation. The RIF, either from the incompatible or compatible race, gave a quite similar profile of activation upon the generation of the superoxide anion.     

Production and properties of ∝-mannosidase from aspergillus sp.

Summary Aspergillus sp NCIM 508 produced 22 U/L of extracellular -mannosidase activity in a medium containing 8 % brewer's yeast cells. The optimum period and pH range for maximum production of the enzyme were 7 days and 4.0–6.0, respectively. The optimum pH and temperature for enzyme activity were 6.0 and 50°C, respectively. The enzyme was stable for 24 h at 28°C, in the pH range 6.0–7.0. The enzyme retained 100 and 65 % of its original activity after heating for 15 min at 45 and 55°C, respectively. The Km and V_max for p-nitrophenyl--D- mannoside (PNPM) were 71M and 7.5 × 10^–2 moles/min/mg, respectively. The enzyme was strongly inhibited by 1 mM Hg⁺⁺ and Cu⁺⁺ and partially by Co.⁺⁺ (NCL Communication No.; 5780)     

Production of ��-poly-l-lysine using a novel two-stage pH control strategy by Streptomyces sp. M-Z18 from glycerol

The production of ε-poly-l-lysine (ε-PL) by Streptomyces sp. M-Z18 from glycerol was investigated in a 5-L jar-fermenter. Batch fermentations by Streptomyces sp. M-Z18 at various pH values ranging from 3.5 to 4.5 were studied. Based on the analysis of the time course of specific cell growth rate and specific ε-PL formation rate, a novel two-stage pH control strategy was developed to improve ε-PL production by shifting the culture pH from 3.5 to 3.8 after 36 h of cultivation. By applying the strategy, the maximal ε-PL concentration and productivity had a significant improvement and reached 9.13 g L⁻¹ and 4.76 g L⁻¹ day⁻¹, respectively, compared with those in one-stage pH control process where the pH value is controlled at 3.5 (7.83 g L⁻¹ and 3.13 g L⁻¹ day⁻¹). Fed-batch fermentation with two-stage pH control strategy was also applied to produce ε-PL; final ε-PL concentration of 30.11 g L⁻¹ was obtained, being 3.3-fold greater than that of batch fermentation. To our knowledge, it is the first report on production of ε-PL from glycerol in fermenter scale and achievement of high ε-PL production with two-stage pH control strategy.     

The release of oligosaccharides from glycoproteins by endo-β-N-acetylglucosaminidase of Flavobacterium sp.

Endo-β-N-acetylglucosaminidase, purified to homogenicity from the cultural filtrate of Flavobacterium sp., liberated oligosaccharides from various glycoproteins. The enzyme could liberate the carbohydrate chain from native ovalbumin. The release of oligosaccharides from ribonuclease B, yeast carboxypeptidase and a Ricinus lectin was also observed. These glycoproteins contain neutral oligosaccharides that are attached to the protein through glycosyl asparagine bonds. The treatment of glycoprotein with SDS and boiling was more effective for removal of oligosaccharides by the enzyme. The enzyme hydrolyzed all five heterogeneous ovalbumin glycopeptides, although the rate of hydrolysis decreased as the size of the sugar moiety increased. Removal of the neutral oligosaccharides did not appear to effect the enzymatic properties of the hemagglutination ability of these glycoproteins.     

β-N-Acetylglucosaminidase MthNAG from Myceliophthora thermophila C1, a thermostable enzyme for production of N-acetylglucosamine from chitin

Applied Microbiology and Biotechnology - Thermostable enzymes are a promising alternative for chemical catalysts currently used for the production of N-acetylglucosamine (GlcNAc) from chitin. In...     

Production of yeast chitin–glucan complex from biodiesel industry byproduct

Crude glycerol from the biodiesel industry was used as carbon source for high cell density fed-batch cultivation of Pichia pastoris aiming at producing a chitin–glucan complex (CGC). More than 100 g L^?1 biomass was obtained in less than 48 h. The yield of biomass on a glycerol basis was 0.55 g g^?1 during the batch phase and 0.63 g g^?1 during the fed-batch phase. The chitin–glucan complex was recovered from the yeast cell wall by hot alkaline extraction. CGC content in the cell wall was found to be relatively constant throughout the cultivation (18–26%) with a volumetric productivity of 1.28 g L^?1 h^?1 at the end of the fed-batch phase. The molar ratio of chitin:β-glucan in the extracted biopolymer was 16:84, close to other CGC extracted from Aspergillus biomass. The extracted polymer was characterized by Differential Scanning Calorimetry (DCS) and solid-state Nuclear Magnetic Resonance (NMR) spectroscopy and compared with commercial biopolymers, namely, crab shell chitin and/or chitosan, algal β-glucan (laminarin) and fungal chitin–glucan complex (kiOsmetine).     

The Production of α-Ketoglutaric Acid from Salicylic Acid by Pseudomonas sp.†

Metabolites from salicylic acid by microorganisms were investigated. About eighty strains of bacteria which were able to utilize salicylic acid as a sole source of carbon were isolated from soil and other natural sources.

Among these bacteria, several strains produced a large amount of keto acids in the culture fluid during the cultivation. The acid was isolated from the culture fluid of strain K 102 in crystalline form. The crystal was identified as α-ketoglutaric acid by physicochemical methods. From the taxonomical studies, the isolated bacterial strains K 102 and K 362 were assumed to be Pseudomonas sp.     

Production of fructooligosaccharides by crude enzyme preparations of β-fructofuranosidase from <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis>

Fructooligosaccharides (FOS) were produced from sucrose by using crude enzyme preparations of β-fructofuranosidases (FFases) obtained from sucrose-cultured cells of Aureobasidium pullulans DSM 2404. When the preparation mainly consisted of FFase I, that has high transfructosylating activity, the FOS yield was 62%. When the reaction was carried out with additional commercial glucose isomerase (GI) at an activity ratio of FFase and GI of 1:2, the maximum FOS yield reached 69%. This value was higher than those obtained previously using other Aureobasidium spp. (53–59%).     

Production of β-mannosidase and β-mannanase by an alkalophilic Bacillus sp.

Summary An alkalophilic bacterium producing high amounts of the cell-associated -mannosidase and extracellular -mannanase was isolated from soil. The isolate (AM-001) that grew well in alkaline pH media was identified as a strain of Bacillus sp. The optimal cultivation temperature for enzyme production was 31° C for -mannosidase and 37° C for -mannanase with the optimum production medium composed of 1% konjac powder, 0.2% yeast extract, 2% Polypepton, 0.1% K₂HPO₄, 0.02% MgSO₄ · 7H₂O and 0.5% Na₂CO₃. Optimum pH and temperature for -mannosidase were 7.0 and 55° C, and for -mannanase were 9.0 and 65° C.     

Production of β-galactosidase from thermophilic fungus Rhizomucor sp

A thermostable β-galactosidase was produced extracellularly by a thermophilic Rhizomucor sp, with maximum enzyme activity (0.21 U mg⁻¹) after 4 days under submerged fermentation condition (SmF). Solid state fermentation (SSF) resulted in a nine-fold increase in enzyme activity (2.04 U mg⁻¹). The temperature range for production of the enzyme was 38–55°C with maximum activity at 45°C. The optimum pH and temperature for the partially purified enzyme was 4.5 and 60°C, respectively. The enzyme retained its original activity on incubation at 60°C up to 1 h. Divalent cations like Co²⁺, Mn²⁺, Fe²⁺ and Zn²⁺ had strong inhibitory effects on the enzyme activity. The K _m and V _max for p-nitrophenyl-β- _D-galactopyranoside and o-nitrophenyl-β - _D-galactopyranoside were 0.39 mM, 0.785 mM and 232.1 mmol min⁻¹ mg⁻¹ respectively. The K _m and V _max for the natural substrate lactose were 66.66 μM and 0.20 μ mol min⁻¹ mg⁻¹. Received 10 March 1997/ Accepted in revised form 17 July 1997     

Production of thermostable α-galactosidase from thermophilic fungusHumicola sp

The thermophilic fungus,Humicola sp isolated from soil, secreted extracellular -galactosidase in a medium cotaining wheat bran extract and yeast extract. Maximum enzyme production was found in a medium containing 5% wheat bran extract as a carbon source and 0.5% beef extract as a carbon and nitrogen source. Enzyme secretion was strongly inhibited by the presence of Cu²⁺, Ni²⁺ and Hg²⁺ (1mM) in the fermentation medium. Production of enzyme under stationary conditions resulted in 10-fold higher activity than under shaking conditions. The temperature range for production of the enzyme was 37° C to 55°C, with maximum activity (5.54 U ml^–1) at 45°C. Optimum pH and temperature for enzyme activity were 5.0 and 60° C respectively. One hundred per cent of the original activity was retained after heating the enzyme at 60°C for 1 h. At 5mM Hg²⁺ strongly inhibited enzyme activity. TheK _m andV _max forp-nitrophenyl--d-galactopyranoside were 60M and 33.6 mol min^–1 mg^–1, respectively, while for raffinose those values were 10.52 mM and 1.8 mol min^–1 mg^–1, respectively.     

Production of poly-β-hydroxybutyrate by thermophilic cyanobacterium, Synechococcus sp. MA19, under phosphate-limited conditions

Synechococcus sp. MA19, grown autotrophically under phosphate-limited conditions at 50 °C, produced poly--hydroxybutyrate (PHB) when intracellular phosphate content was 0.043–0.076mmol per g of cellular components. In the culture for 260h using Ca₃(PO₄)₂ as a phosphate source, strain MA19 accumulated PHB at 55% (w/w) of the dry cells and the amount of PHB produced was 2.4gl^–1 which was almost twice that without Ca₃(PO₄)₂ addition.     

Production of aromatic d-amino acids from α-keto acids and ammonia by coupling of four enzyme reactions

A multi-enzyme system composed of glutamate racemase, thermostable d-amino acid aminotransferase, glutamate dehydrogenase and formate dehydrogenase was employed for the production of aromatic d-amino acids, d-phenylalanine and d-tyrosine, from the corresponding α-keto acids, phenylpyruvate and hydroxyphenylpyruvate, respectively. The optimal concentration of ammonium formate for the production of these d-amino acids was found in the range of 0.25–1.0 M. The optimal concentration of α-keto acid was determined to be 50 mM, above which the productivity greatly decreased. To keep the concentration of α-keto acid around this concentration, α-keto acid was intermittently fed into the multi-enzyme system during the production period. By running the multi-enzyme system for 35 h, 48 g l⁻¹ of d-phenylalanine and 60 g l⁻¹ of d-tyrosine were produced with 100% of optical purity from the equimolar amounts of phenylpyruvate and hydroxyphenylpyruvate, respectively. The production levels of both aromatic d-amino acids were demonstrated to be dependent on the stability of glutamate racemase.     

1,3-β-Glucanases fromStreptomyces sp.1228 lytic enzyme system

Summary Four 1,3--glucanases GI, GII, GIV and GVIII from a culture filtrate ofStreptomyces sp. 1228 were purified by anion exchange chromatography using DEAE-Sepharose Cl-6B or DEAE-Cellulose, gel filtration on Bio-Gel P-200 or Sephacryl S-200, Amicon ultrafiltration and preparative PAGE. The M_r of these enzymes were 19000, 74000, 78000 and 56000 respectively. The glucanase GVIII consisted of two subunits. The optimal catalytic activity of the purified preparations was at 50–55°C and pH 5.5–6.0. The enzymes were also most stable at this pH. Both glucanases GI and GVIII were characterized by high thermostability. The glucanases showed different affinities towards laminarin with Km values of 6.65 x 10^–5 mol/l for GI, 2.35 x 10^–4 mol/l for GII, 8.1 x 10^–5mol/l for GIV and 8.1 x 10^–4mol/l for GVIII. The presence of metal ions was not required for activity of these enzymes but thiol groups increased their activity. D-glucono--lactone did not inhibit the enzymes.     

Production of poly(β-hydroxybutyrate-β-hydroxyvalerate) copolymer from sugars by Azotobacter salinestris

Azotobacter salinestris, a sodium-dependent, microaerophilic N₂-fixing soil bacterium, formed polyhydroxyalkanoate copolymers comprised of β-hydroxybutyric acid and 9–12 mol% β-hydroxyvaleric acid (HV) during growth on sugars. Increased HV content was achieved by feeding valeric acid to the culture growing on glucose, but propionic acid could be directed to HV formation only when it served as the sole C source. Polymer production in nitrogen-fixing cells was increased at higher aeration, provided that a complex organic nitrogen source was also present, but there was no HV in the polymer. HV production was increased to 28 mol% in nitrogen-fixing cells when aeration was lower and acetate was provided with glucose in the medium. Enzymes leading to the production of polyhydroxyalkanoate copolymers were found to be similar in A. salinestris and Azotobacter vinelandii, but A. vinelandii is unable to form HV from propionate or from sugars without valeric acid addition. A biochemical scheme is proposed for the production of HV in A. salinestris, whereby the glyoxylate bypass assimilates acetate to generate succinate, which may be converted into propionyl-CoA for HV synthesis. The results suggest that it may be possible to control the molar yield of HV formed from sugars by A. salinestris. Received: 21 January 1997 / Received revision: 7 April 1997 / Accepted: 13 April 1997