Chitinase biotechnology: Production,purification, and application

Chitin is one of the most abundant biopolymers and is present in many organisms in different forms. Its resistance to degradation has caused many problems in industry (waste decomposition) and agriculture (as protective structures in pests); this has led to increased interest in chitin‐hydrolyzing enzymes: chitinases. Chitinases are enzymes that break down the 1→4 β‐glycoside bond of N‐acetyl d ‐glucosamine in chitin to produce mono‐ and oligomers. The inducible nature of chitinases, low activity of synthesized enzymes, and inertia of the substrate are only a few of the problems that can be solved by biotechnology to meet industry demands for green, energy‐efficient, pollution‐free, and economically profitable chitin use. This review aims to present the pitfalls and successes in research and production of chitinolytic enzymes, as well as to promote the use of chitinases in everyday practice. The focus is on the biosynthesis of chitinases: inducers, type of fermentation, and media composition. Methods for purification and future perspectives are also discussed.     

Production and purification of urokinase: a comprehensive review

An increased emphasis on prevention of fatalities due to thrombovascular disorders is broadening opportunities for several cardiovascular agents, especially plasminogen activators, for preventing strokes and heart attacks. Hence, urokinase, as one of the most potent plasminogen activators is attracting a great deal of attention. Developments in cell lines and bioprocess technology have made it possible to produce urokinase from in vitro cell culture. Attempts are now underway to enhance urokinase production from cell culture through media manipulation, bioreactor cultivation, and innovative purification techniques. Downstream processing also poses an intricate problem due to the complexity of cell culture extracts, susceptibility of urokinase to autocatalytic and proteolytic degradation and due to the presence of plasminogen activator inhibitors in the culture media. Hence, enhancing cellular productivity and downstream product recovery continue to be major challenges as discussed in this review. Furthermore, an approach for integrated upstream and downstream processing is needed to develop an economically viable technology. In the present review the emerging trends in urokinase production and purification have been discussed in detail.     

Production, purification, characterization, and applications of lipases

Lipases (triacylglycerol acylhydrolases, EC 3.1.1.3) catalyze the hydrolysis and the synthesis of esters formed from glycerol and long-chain fatty acids. Lipases occur widely in nature, but only microbial lipases are commercially significant. The many applications of lipases include speciality organic syntheses, hydrolysis of fats and oils, modification of fats, flavor enhancement in food processing, resolution of racemic mixtures, and chemical analyses. This article discusses the production, recovery, and use of microbial lipases. Issues of enzyme kinetics, thermostability, and bioactivity are addressed. Production of recombinant lipases is detailed. Immobilized preparations of lipases are discussed. In view of the increasing understanding of lipases and their many applications in high-value syntheses and as bulk enzymes, these enzymes are having an increasing impact on bioprocessing.     

Production,purification and immobilization of glucose isomerase from Streptomyces olivochromogenes PTCC 1547

Production of glucose isomerase from Streptomyces olivochromogenes PTCC 1457 was followed by its purification and immobilization. Different immobilization methods including the use of a hydrophobic support were investigated.     

Production,purification and characterization of a thermostable laccase from a tropical white-rot fungus

A thermostable laccase was isolated from a tropical white-rot fungus Polyporus sp. which produced as high as 69,738 units of laccase l⁻¹ in an optimized medium containing 20 g of malt extract l⁻¹, 2 g of yeast extract l⁻¹, 1.5 mM CuSO₄. The laccase was purified to electrophoretic purity with a final purification of 44.70-fold and a recovery yield of 21.04%. The purified laccase was shown to be a monomeric enzyme with a molecular mass of 60 kDa. The optimum temperature and pH value of the laccase were 75°C and pH 4.0, respectively, for 2,2′-azino-bis (3-ethylbenzothiazoline-6-sulfonate) (ABTS). The Michaelis–Menten constant (K _m ) of the laccase was 18 μM for ABTS substrate. The laccase was stable at pH values between 5.5 and 7.5. About 80% of the initial enzyme activity was retained after incubation of the laccase at 70°C for 2 h, indicating that the laccase was intrinsically highly thermostable and with valuable potential applications. The laccase activity was promoted by 4.0 mM of Mg²⁺, Mn²⁺, Zn²⁺ and Ca²⁺, while inhibited by 4.0 mM of Co²⁺, Al³⁺, Cu²⁺, and Fe²⁺, showing different profiles of metal ion effects.     

Production, purification, and characterization of the debittering enzyme naringinase

This review discusses the debittering enzyme naringinase and its essential role in the commercial processing of citrus fruit juice. Applications of this enzyme in other areas are identified. Characterization of the enzyme is detailed and its immobilized preparations are discussed. Production of microbial naringinase by fermentation is described.     

Production, purification, and characterization of xylanase from a hyperxylanolytic mutant of Aspergillus ochraceus

Enhancement of the productivity of xylanase and beta-xy-losidase of Aspergillus ochraceus was investigated by multistep mutagenesis. The spores of the wild strain were subjected to UV and N-methyl-N-nitro-N-nitro-soguanidine (NTG). The hyperxylanolytic mutant (NG-13), which showed good clearing on the surface of the xylan-agar plate, secretes xylanase and beta-xylosidase at high levels during growth on commercial xylan and on agricultural wastes. Both liquid and solid state cultures were employed in the study for enzyme production. The xylanase from NG-13 was purified to homogeneity by ammonium sulfate precipitation and gel filtration. This purified enzyme showed a pH optimum of 6.0 and was stable in the range of pH 5 to 10. Prolonged stability of the enzyme was observed at 45 degrees C though its activity was maximal at 50 degrees C. The molecular weight of the enzyme was estimated to be 4.3 x 10(4) by SDS-polyacrylamide gel electrophoresis and 5 x 10(4) by gel filtration on Sephadex G-75. The kinetic data showed that the K(m) and V(max) values for xylan were 1 x 10(-3)M and 19.6 mumol/ min/mg protein, respectively. The enzyme was both more active and thermostable in the presence of K(+)and was inactivated by thiol reagents such as Hg(2+), p-hydroxymercuribenzoate (PHMB), 3', 5'-dithiobis (2'-nitrobenzoic acid) (DTNB), and N-ethylmaleimide (NEM).     

Human tumor necrosis factor. Production, purification, and characterization

Human tumor necrosis factor (TNF) was purified to homogeneity from serum-free tissue culture supernatants of the HL-60 promyelocytic leukemia cell line induced by 4 beta-phorbol 12-myristate 13-acetate. The purification scheme consisted of controlled-pore glass and DEAE-cellulose chromatography, Mono Q-fast-protein liquid chromatography, and reverse-phase high performance liquid chromatography. The purified protein was homogeneous by the criteria of sodium dodecyl sulfate-polyacrylamide gel electrophoresis and NH2-terminal sequence analysis. The specific activity of purified tumor necrosis factor is approximately 10(8) units/mg. The protein has a molecular weight of approximately 17,000, an isoelectric point of 5.3, and contains two cysteines involved in a disulfide bridge. Approximately 50% homology between TNF and another cytolytic lymphokine, lymphotoxin, exists when the NH2-terminal 34 residues of TNF and internal sequence generated by tryptic, Staphylococcus aureus V8 protease, and chymotryptic digests of TNF are aligned with the complete amino acid sequence of lymphotoxin.     

Production,optimization, purification,characterization, and anti-cancer application of extracellular L-glutaminase produced from the marine bacterial isolate

Abstract

L-glutaminase from bacterial sources has been proven to be effective and economical agents in cancer therapy, food industry and high-value chemicals like threonine. In the present study, a newly isolated bacterial strain was potentially producing extracellular L-glutaminase, it identified as Bacillus subtilis OHEM11 (MK389501) using the 16S rRNA gene. L-glutaminase production optimized and the optimum factors for production under submerged fermentation were at pH 6.5–7.0 and 35?°C after 28?hr using rhamnose and glutamine as carbon and nitrogen sources, respectively, while bagasse was the best inducer for the production under solid-state fermentation. Ethanol precipitation and ion-exchange chromatography using QFF are the purification steps. L-glutaminase was purified to 2-fold with specific activity 89.78?U/mg and its molecular weight about 54.8?kDa with the alkaline property of the enzyme makes it clear having carcinostatic property; maximum enzyme activity at pH 8.2 and 40?°C and retained about 90% activity for 1?hr. The cytotoxicity effect of L-glutaminase indicated a significant safety on Vero cells with high anticancer activity against NFS-60, HepG-2, and MCF-7 cancer cell lines. The outcomes demonstrated that L-glutaminase could be applied in many biotechnological applications such as pharmaceutical and food processing.     

Production of lipase in a fermentor using a mutant strain of Corynebacterium species: its partial purification and immobilization

Extracellular Corynebacterium lipase was produced using a 2.5 L Chemap fermentor using 1300 ml fermentation medium at temperature 33 degrees C, agitator speed 50 rpm, aeration rate 1 VVM having KLa 16.21 hr(-1). Crude lipase was purified by salting out method followed by dialysis and immobilized using calcium alginate gel matrix followed by glutaraldehyde cross linking Purification process increased specific activity of enzyme from 2.76 to 114.7 IU/mg. Activity of immobilized enzyme was 107.31 IU/mg. Optimum temperature for purified and immobilized enzyme activity were 65 degrees and 50 degrees C respectively. Optimum pH was 8.0 in both the cases, Km and Vmax value for purified lipase were 111.1 micromol/min and 14.7% respectively. Ca2+ (5 mM) was found to be stimulator for enzyme activity. Immobilized lipase retained 68.18% of the original activity when stored for 40 days.     

Production, purification, and characterization of alpha-amylase from Thermomonospora curvata.

Thermomonospora curvata produces an extracellular alpha-amylase. Maximal amylase production by cultures in a starch-mineral salts medium occurred at pH 7.5 and 53 degrees C. The crude enzyme was unstable to heating (65 degrees C) at pH 4 to 6, and was activated when heated at pH 8. The enzyme was purified 66-fold with a 9% yield and appeared homogeneous on discontinuous gel electrophoresis. The pH and temperature optima for activity of the purified enzyme were 5.5 to 6.0 and 65 degrees C. The molecular weight was calculated to be 62,000. The Km for starch was 0.39 mg/ml. The amylolytic pattern consisted of a mixture of maltotetraose and maltopentaose.     

Production, purification, and characterization of alpha-amylase from Thermomonospora curvata.

Thermomonospora curvata produces an extracellular alpha-amylase. Maximal amylase production by cultures in a starch-mineral salts medium occurred at pH 7.5 and 53 degrees C. The crude enzyme was unstable to heating (65 degrees C) at pH 4 to 6, and was activated when heated at pH 8. The enzyme was purified 66-fold with a 9% yield and appeared homogeneous on discontinuous gel electrophoresis. The pH and temperature optima for activity of the purified enzyme were 5.5 to 6.0 and 65 degrees C. The molecular weight was calculated to be 62,000. The Km for starch was 0.39 mg/ml. The amylolytic pattern consisted of a mixture of maltotetraose and maltopentaose.     

Production,purification and characterization of pectinase from a Bacillus sp. DT7

A soil isolate, Bacillus sp. DT7 has been found to produce significant amounts of an extracellular pectinase subsequently characterized as pectin lyase (EC 4.2.2.10). By optimizing growth conditions, Bacillus sp. DT7 produced higher amount of pectin lyase (53 units/ml) than that has been reported in the literature. Using gel filtration and ion exchange chromatography, this enzyme was purified and found to have a molecular mass of 106 kDa. The purified enzyme exhibited maximal activity at a temperature of 60 C and pH 8.0. The presence of 100 mM concentrations of CaCl₂ and mercaptoethanol significantly enhanced pectinase activity of the purified enzyme. This pectinase has tremendous applications in textile industry, plant tissue maceration and fruit juice wastewater treatments.     

Production, purification and characterization of a 50-kDa extracellular metalloprotease from Serratia marcescens

The extracellular metalloprotease (SMP 6.1) produced by a soil isolate of Serratia marcescens NRRL B-23112 was purified and characterized. SMP 6.1 was purified from the culture supernatant by ammonium sulfate precipitation, acetone fractional precipitation, and preparative isoelectric focusing. SMP 6.1 has a molecular mass of approximately 50 900 Da by sodium dodecyl sulfate/polyacrylamide gel electrophoresis (SDS-PAGE). The following substrates were hydrolyzed: casein, bovine serum albumin, and hide powder. SMP 6.1 has the characteristics of a metalloprotease, a pH optimum of 10.0, and a temperature optimum of 42° C. The isoelectric point of the protease is 6.1. Restoration of proteolytic activity by in-gel renaturation after SDS-PAGE indicates a single polypeptide chain. SMP 6.1 is inhibited by EDTA (9 μg/ml) and not inhibited by antipain dihydrochloride (120 μg/ml), aprotinin (4 μg/ml), bestatin (80 μg/ml), chymostatin (50 μg/ml), E-64 (20 μg/ml), leupeptin (4 μg/ml), Pefabloc SC (2000 μg/ml), pepstatin (4 μg/ml), phosphoramidon (660 μg/ml), or phenylmethylsulfonyl fluoride (400 μg/ml). SMP 6.1 retains full activity in the presence of SDS (1% w/v), Tween-20 (1% w/v), Triton X-100 (1% w/v), ethanol (5% v/v), and 2-mercaptoethanol (0.5% v/v). The extracellular metalloprotease SMP 6.1 differs from the serratiopeptidase (Sigma) produced by S. marcescens ATCC 27117 in the following characteristics: isoelectric point, peptide mapping and nematolytic properties. Received: 22 November 1996 / Received revision: 27 February 1997 / Accepted: 7 March 1997     

铜绿假单胞菌外毒素A的生产,分离纯化和鉴定

通过对培养基组成、种子活化、接种量和培养条件进行优化,使铜绿假单胞菌外毒素Ａ（ＰＥ）产量达到每毫升５－１０μｇ和１９２小鼠ＬＤ５０,不低于国外报道水平。经二步纯化,ＰＥ蛋白回收率为３３．３３％（ＰＥ）和１６．６７％（ＬＤ５０）,提纯系数为４３８．５（ＰＥ）或２１８．５（ＬＤ５０）,ＳＤＳ－ＰＡＧＥ呈现一条带,相对分子质量为６６０００,琼脂糖扩散鉴定与兔抗ＰＥ产生一条沉淀线,小鼠半数致死量为０．１５     

Production, purification and characterization of intracellular alanylaminopeptidase ofPseudomonas sp.

The soil bacteriumPseudomonas sp. was found to synthesize an aminopeptidase that prefers Ala-β-naphtylamide as substrate. The enzyme was purified 660-fold by ammonium sulfate fractionation, preparative electrophoresis, ion exchange chromatography on Protein-Pak Q 8 HR and molecular sieving chromatography on Zorbax SE-250. When purified to homogeneity, the enzyme was shown to be a monomeric protein with a molar mass of 65 kDa; it showed a maximum activity at pH 7.5 and 45°C.     

Yeast-derived recombinant human insulin-like growth factor I: Production, purification, and structural characterization

Recombinant human insulin-like growth factor I (IGF-I) is efficiently expressed and secreted fromSaccharomyces cerevisiae using a yeast -factor leader to direct secretion. However, approximately 10–20% of the IGF-I was in a monomeric form, the remaining materials being disulfide-linked aggregates. When the purified material was subjected to reverse-phase high-performance liquid chromatography (rp-HPLC), it gave two doublet peaks, I and II. Upon reduction, doublet peaks I and II converged to one doublet peak. This suggests that peaks I and II result from different disulfide structures, and the doublet feature of each peak results from other causes. Different disulfide structures between peaks I and II were also suggested from the near UV circular dichroism of these proteins. Only the peak II was biologically active, indicating that peak II has the correct disulfide structure. Concanavalin A affinity chromatography of the purified peak II doublet showed binding of the subpeak with an earlier rp-HPLC retention time, indicating that it was glycosylated. Sequence analysis of tryptic peptides suggested that Thr²⁹ was the site of glycosylation. Site-directed mutagenesis was used to convert Thr²⁹ to Asn²⁹. This substitution reduced, but did not eliminate IGF-I glycosylation, suggesting additional glycosylation sites. The site of carbohydrate addition was consistent with the model that O-glycosylations occur on hydroxyl amino acids near proline residues in -turns.     

Production, purification, and characterization of a highly glucose-tolerant novel beta-glucosidase from Candida peltata.

Candida peltata (NRRL Y-6888) produced beta-glucosidase when grown in liquid culture on various substrates (glucose, xylose, L-arabinose, cellobiose, sucrose, and maltose). An extracellular beta-glucosidase was purified 1,800-fold to homogeneity from the culture supernatant of the yeast grown on glucose by salting out with ammonium sulfate, ion-exchange chromatography with DEAE Bio-Gel A agarose, Bio-Gel A-0.5m gel filtration, and cellobiose-Sepharose affinity chromatography. The enzyme was a monomeric protein with an apparent molecular weight of 43,000 as determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and gel filtration. It was optimally active at pH 5.0 and 50 degrees C and had a specific activity of 108 mumol.min-1.mg of protein-1 against p-nitrophenyl-beta-D-glucoside (pNP beta G). The purified beta-glucosidase readily hydrolyzed pNP beta G, cellobiose, cellotriose, cellotetraose, cellopentaose, and cellohexaose, with Km values of 2.3, 66, 39, 35, 21, and 18 mM, respectively. The enzyme was highly tolerant to glucose inhibition, with a Ki of 1.4 M (252 mg/ml). Substrate inhibition was not observed with 40 mM pNP beta G or 15% cellobiose. The enzyme did not require divalent cations for activity, and its activity was not affected by p-chloromercuribenzoate (0.2 mM), EDTA (10 mM), or dithiothreitol (10 mM). Ethanol at an optimal concentration (0.75%, vol/vol) stimulated the initial enzyme activity by only 11%. Cellobiose (10%, wt/vol) was almost completely hydrolyzed to glucose by the purified beta-glucosidase (1.5 U/ml) in both the absence and presence of glucose (6%). Glucose production was enhanced by 8.3% when microcrystalline cellulose (2%, wt/vol) was treated for 24 h with a commercial cellulase preparation (cellulase, 5 U/ml; beta-glucosidase, 0.45 U/ml) that was supplemented with purified beta-glucosidase (0.4 U/ml).     

Production, purification, and characterization of an extracellular chitosanase from Streptomyces.

The synthesis by Streptomyces sp. no. 6 of an extracellular chitosanase was induced by glucosamine. The enzyme was purified to homogeneity by Sephadex G-100, carboxymethyl-cellulose, and diethylaminoethyl-cellulose chromatography. The purified enzyme hydrolyzed chitosan (the beta-1,4-linked polymer of glucosamine) but not chitin nor carboxymethyl-cellulose. The only products of the hydrolysis detectable by paper chromatography were di- and triglucosamine. Sephadex G-100 chromatography and sodium dodecyl sulfate-polyacrylamide gel electrophoresis indicated that the molecular weight of the enzyme was between 29,000 and 26,000. Acid hydrolysates of the enzyme contained no cysteic acid or glucosamine or other carbohydrate. At 25 C, maximum activity was obtained between pH 4.5 and 6.5. The enzymatic hydrolysis of chitosan occurred over a wide range of temperatures and was maximal at 60 C. The rate of the reaction was inhibited by concentrations of soluble chitosan higher than 0.5 g/liter. The apparent Km calculated from a Lineweaver-Burke plot was 0.688 g/liter at pH 5.5. The enzyme prevented spore germination and caused a significant decrease in the turbidity of germinated spore suspensions of the Mucor strains tested. Such a decrease was the result of a partial lysis of the cell wall.