Production of tannase by the immobilized cells of Bacillus licheniformis KBR6 in Ca-alginate beads

AIMS: The present study was aimed at finding the optimal conditions for immobilization of Bacillus licheniformis KBR6 cells in calcium-alginate (Ca-alginate) beads and determining the operational stability during the production of tannin-acyl-hydrolase (tannase) under semicontinous cultivation. METHODS AND RESULTS: The active cells of B. licheniformis KBR6 were immobilized in Ca-alginate and used for the production of tannase. The influence of alginate concentration (5, 10, 20 and 30 g l(-1)) and initial cell loading on enzyme production were studied. The production of tannase increased significantly with increasing alginate concentration and reached a maximum enzyme yield of 0.56 +/- 0.03 U ml(-1) at 20 g l(-1). This was about 1.70-fold higher than that obtained by free cells. The immobilized cells produced tannase consistently over 13 repeated cycles and reached a maximum level at the third cycle. Scanning electron microscope study indicated that the cells in Ca-alginate beads remain in normal shape. CONCLUSIONS: The Ca-alginate entrapment is a promising immobilization method of B. licheniformis KBR6 for repeated tannase production. Tannase production by immobilized cells is superior to that of free cells because it leads to higher volumetric activities within the same period of fermentation. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first report of tannase production from immobilized bacterial cells. The bacterium under study can produce higher amounts of tannase with respect to other fungal strains within a short cultivation period.     

Immobilization of Aspergillus oryzae tannase and properties of the immobilized enzyme

Tannase enzyme from Aspergillus oryzae was immobilized on various carriers by different methods. The immobilized enzyme on chitosan with a bifunctional agent (glutaraldehyde) had the highest activity. The catalytic properties and stability of the immobilized tannase were compared with the corresponding free enzyme. The bound enzyme retained 20·3% of the original specific activity exhibited by the free enzyme. The optimum pH of the immobilized enzyme was shifted to a more acidic range compared with the free enzyme. The optimum temperature of the reaction was determined to be 40 °C for the free enzyme and 55 °C for the immobilized form. The stability at low pH, as well as thermal stability, were significantly improved by the immobilization process. The immobilized enzyme exhibited mass transfer limitation as reflected by a higher apparent K_m value and a lower energy of activation. The immobilized enzyme retained about 85% of the initial catalytic activity, even after being used 17 times.     

Covalent linking of alkaline protease on trichlorotriazine activated nylon

Alkaline protease was covalently attached to nylon using trichlorotriazine. Enzymatic activity was determined at different trichlorotriazine activation temperature and time. It was observed that, the optimum temperature and pH of the immobilized alkaline protease was comparable to that of the free enzyme. Immobilization improved the thermal stability and pH stability of the enzyme.     

Characteristics of yeast invertase immobilized on porous cellulose beads.

Invertase from Candida utilis was immobilized on porous cellulose beads by an ionic-quanidino bond. The immobilized invertase showed optimum activity between pH 4.0 and 5.4, while the free enzyme had a sharp optimum at pH 4.1. Both temperature profiles were fairly similar up to 55 degrees C. However, above this temperature the immobilized enzyme was more stable than the free enzyme. From the temperature data, the activation energies were found to be 7,322 and 4,052 cal/g mol for the free and the immobilized enzyme, respectively. Candida invertase shows characteristics of substrate inhibition. Both the Km and Ki for the free and the immobilized enzymes were determined. The apparent Ki for the immobilized invertase was much higher than the Ki of the free enzyme, suggesting a diffusion effect. Immobilized invertase molecules deep in the pores only see sucrose concentrations much less than the bulk concentrations. Immobilization, thus, offers certain processing advantages in this regard.     

Immobilization of tyrosinase on chitosan-clay composite beads

Tyrosinase was immobilized on glutaraldehyde crosslinked chitosan-clay composite beads and used for phenol removal. Immobilization yield, loading efficiency and activity of tyrosinase immobilized beads were found as 67%, 25% and 1400 U/g beads respectively. Optimum pH of the free and immobilized enzyme was found as pH 7.0. Optimum temperature of the free and immobilized enzyme was determined as 25-30 °C and 25 °C respectively. The kinetic parameters of free and immobilized tyrosinase were calculated using l-catechol as a substrate and K(m) value for free and immobilized tyrosinase were found as 0.93 mM and 1.7 mM respectively. After seven times of repeated tests, each over 150 min, the efficiency of phenol removal using same immobilized tyrosinase beads were decreased to 43%.     

Immobilization of the recombinant invertase INVB from <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> on Nylon-6

The recombinant invertase INVB (re-INVB) from Zymomonas mobilis was immobilized on microbeads of Nylon-6, by means of covalent bonding. The enzyme was strongly and successfully bound to the support. The activity of the free and immobilized enzyme was determined, using 10% (w/v) sucrose, at a temperature ranging between 15 and 60 °C and a pH ranging between 3.5 and 7. The optimal pH and temperature for the immobilized enzyme were 5.5 and 25 °C, respectively. Immobilization of re-INVB on Nylon-6 showed no significant change in the optimal pH, but a difference in the optimal temperature was evident, as that for the free enzyme was shown to be 40 °C. The values for kinetic parameters were determined as: 984 and 98 mM for of immobilized and free re-INVB, respectively. values for immobilized and free enzymes were 6.1 × 10² and 1.2 × 10⁴ s⁻¹, respectively, and immobilized re-INVB showed of 158.73 μmol h min⁻¹ mg⁻¹. Immobilization of re-INVB on Nylon-6 enhanced the thermostability of the enzyme by 50% at 30 °C and 70% at 40 °C, when compared to the free enzyme. The immobilization system reported here may have future biotechnological applications, owing to the simplicity of the immobilization technique, the strong binding of re-INVB to the support and the effective thermostability of the enzyme.     

Immobilization of polygalacturonase from Aspergillus niger onto activated polyethylene and its application in apple juice clarification

The present work is focused on efficient immobilization of polygalacturonase on polyethylene matrix, followed by its application in apple juice clarification. Immobilization of polygalacturonase on activated polyethylene and its use in apple juice clarification was not reported so far. Aspergillus niger Van Tieghem (MTCC 3323) produced polygalacturonase when grown in modified Riviere's medium containing pectin as single carbon source by fed-batch culture. The enzyme was precipitated with ethanol and purified by gel filtration chromatography (Sephacryl S-100) and immobilized onto glutaraldehyde-activated polyethylene. The method is very simple and time saving for enzyme immobilization. Various characteristics of immobilized enzyme such as optimum reaction temperature and pH, temperature and pH stability, binding kinetics, efficiency of binding, reusability and metal ion effect on immobilized enzymes were evaluated in comparison to the free enzyme. Both the free and immobilized enzyme showed maximum activity at a temperature of 45 degrees C and pH 4.8. Maximum binding efficiency was 38%. The immobilized enzyme was reusable for 3 cycles with 50% loss of activity after the third cycle. Twenty-four U of immobilized enzyme at 45 degrees C and 1 h incubation time increased the transmittance of the apple juice by about 55% at 650 nm. The immobilized enzyme can be of industrial advantage in terms of sturdiness, availability, inertness, low price, reusability and temperature stability.     

Enhanced stabilization of mungbean thiol protease immobilized on glutaraldehyde-activated chitosan beads

A thiol protease purified from mungbean seedlings was immobilized on chitosan beads cross-linked with glutaraldehyde. The yield of the immobilized enzyme was maximum (～99%) at 1% concentration each of chitosan and glutaraldehyde. The immobilized enzyme showed reusability for 15 batch reactions. Immobilization shifted the optimum pH of the enzyme to a more acidic range and enhanced its stability both at acidic as well as alkaline pH values compared to the free enzyme. The stability of the enzyme to temperature and in aqueous non-conventional medium (ethanol and DMSO) was significantly improved by the immobilization process. The immobilized enzyme exhibited mass transfer limitation reflected by a higher apparent K_m value. This study produced an immobilized biocatalyst having improved characteristics and better operational stability than the soluble enzyme. The increase in stability in the presence of high concentrations of ethanol and DMSO may make it useful for catalyzing organic reactions such as trans-esterification and trans-amidation similar to other cysteine proteinases.     

Immobilization of functionally unstable catechol-2,3-dioxygenase greatly improves operational stability

Thermophilic catechol 2,3-dioxygenase (EC 1.13.11.2) from Bacillus stearothermophilus has been immobilized on highly activated glyoxyl agarose beads. The enzyme could be fully immobilized at 4 degrees C and pH 10.05 with a high retention of activity (around 80%). Enzyme immobilized under these conditions showed little increase in thermostability compared with the soluble enzyme, but further incubation of immobilized enzyme at 25 degrees C and pH 10.05 for 3 h before borohydride reduction resulted in conjugates exhibiting a 100-fold increase in stability (c.f. the free enzyme). The stability of catechol 2,3-dioxygenase immobilized under these conditions was essentially independent of protein concentration whereas free enzyme was rapidly inactivated at low protein concentrations. An apparent stabilization factor of over 700-fold was recorded in the comparison of free and immobilized catechol 2,3-dioxygenases at protein concentrations of 10 μg/ml. Immobilization increased the 'optimum temperature' for activity by 20 degrees C, retained activity at substrate concentrations where the soluble enzyme was fully inactivated and enhanced the resistance to inactivation during catalysis. These results suggest that the immobilization of the enzyme under controlled conditions with the generation of multiple covalent links between the enzyme and matrix both stabilized the quaternary structure of the protein and increased the rigidity of the subunit structures.     

利用固定化黑曲霉单宁酶制备没食子酸的研究

用海藻酸钙载体包埋单宁酶,制备出转化五倍子单宁成没食子酸能力较好的固定化酶。研究了固定化条件和固定化单宁酶的部分性质,结果表明：最佳固定化条件为海藻酸钠90mg包埋单宁酶546u(3mL,182u/Ml),在1%～2%CaCl₂中作硬化处理;固定化单宁酶的最适温度为45℃,在10～50℃范围内稳定;其最适Ph值为6.5,在Ph5～7之间基本稳定;在此基础上,进行了没食子酸实验室克量级酶法制备实验,3次实验没食子酸产品的平均产率达到61%。和目前所用工业生产没食子酸的硫酸水解法相当,具有潜在的工业开发价值。     

Tannase enzyme production by entrapped cells of Aspergillus niger FETL FT3 in submerged culture system

The ability of immobilized cell cultures of Aspergillus niger FETL FT3 to produce extracellular tannase was investigated. The production of enzyme was increased by entrapping the fungus in scouring mesh cubes compared to free cells. Using optimized parameters of six scouring mesh cubes and inoculum size of 1 × 10⁶ spores/mL, the tannase production of 3.98 U/mL was obtained from the immobilized cells compared to free cells (2.81 U/mL). It was about 41.64% increment. The immobilized cultures exhibited significant tannase production stability of two repeated runs.     

Protease produced by Pseudomonas aeruginosa K-187 and its application in the deproteinization of shrimp and crab shell wastes

In addition to chitinase/lysozyme, Pseudomonas aeruginosa K-187 also produced a protease useful for the deproteinization of shrimp and crab shell wastes. The optimal culture conditions for P. aeruginosa K-187 to attain the highest protease activity were investigated and discussed. The highest protease activity was as high as 21.2 U/ml, 10-fold that (2.2 U/ml) obtained prior to optimization. The protease of P. aeruginosa K-187, produced under the optimal culture conditions, was tested for crustacean waste deproteinization. The percent of protein removal for shrimp and crab shell powder (SCSP) after 7-day incubation was 72%, while that of natural shrimp shell (NSS) and acid-treated SCSP was 78% and 45%, respectively. In contrast, with the protease produced under pre-optimization conditions, the percent of protein removal for SCSP, NSS, and acid-treated SCSP was 48%, 55%, and 40%, respectively. For comparison, three other protease-producing microbes were tested for crustacean waste deproteinization. However, they were shown to be less efficient in deproteinization than P. aeruginosa K-187. The crude protease produced by P. aeruginosa K-187 can be covalently immobilized on a reversibly soluble polymeric support (hydroxypropyl methycellulose acetate succinate). The immobilized enzyme was soluble above pH 5.5 but insoluble below pH 4.5. Immobilization efficiency was 82%. The immobilized enzyme was stable between pH 6 and 9 and at temperatures below 60 degrees C. The optimum pH and temperature for the immobilized enzyme was pH 8 and 50 degrees C. The half-life of the immobilized enzyme was 12 days, longer than that of free protease (8 days). The utilization of the immobilized enzyme for the deproteinization of SCSP has resulted in a 67% protein removal. By contrast, SCSP protein removal by using free enzymes was 72%. The protease was further purified and characterized. The purification steps included ammonium sulfate precipitation, DEAE-Sepharose CL-6B ion-exchange chromatography, and Sephacryl S-200 gel-permeation chromatography. The enzyme had a molecular weight estimated to be 58.8 kDa by using sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The purified enzyme was active from pH 7 to 9 and its optimal pH was 8.     

Modulation of Mucor miehei lipase properties via directed immobilization on different hetero-functional epoxy resins: Hydrolytic resolution of (R,S)-2-butyroyl-2-phenylacetic acid

Purified lipase from Mucor miehei (MML) has been covalently immobilized on different epoxy resins (standard hydrophobic epoxy resins, epoxy-ethylenediamine, epoxy-iminodiacetic acid, epoxy-copper chelates) and adsorbed via interfacial activation on octadecyl-Sepabeads support (fully coated with very hydrophobic octadecyl groups). These immobilized enzyme preparations were used under slightly different conditions (temperature ranging from 4 to 25 °C and pH values from 5 to 7) in the hydrolytic resolution of (R,S)-2-butyroyl-2-phenylacetic acid.

Different catalytic properties (activity, specificity, enantioselectivity) were found depending on the particular support used. For example, the epoxy-iminodiacetic acid-Sepabeads gave the most active preparation at pH 7 while, at pH 5, the ethylenediamine-Sepabeads was superior.

More interestingly, the enantiomeric ratio (E) also depends strongly on the immobilized preparation and the conditions employed. Thus, the octadecyl-MML preparation was the only immobilized enzyme derivative which exhibited enantioselectivity towards R isomer (with E values ranging from 5 at 4 °C and pH 7 to 1.2 at pH 5 and 25 °C).

The other immobilized preparations, in contrast, were S selective. Immobilization on iminodiacetic acid-Sepabeads afforded the catalyst with the highest enantioselectivity (E=59 under optimum conditions).     

Optimization of culture conditions and properties of immobilized sulfide oxidase from Arthrobacter species

Arthrobacter species strain FR-3, isolated from sediments of a swamp, produced a novel serine-type sulfide oxidase. The production of sulfide oxidase was maximal at pH 7.5 and 30 degrees C. Among various carbon and nitrogen sources tested, glucose and yeast extract were found to be the most effective substrates for the secretion of sulfide oxidase. The sulfide oxidase was purified to homogeneity and the molecular weight of the purified enzyme was 43 kDa when estimated by sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The purified sulfide oxidase can be effectively immobilized in DEAE (diethylaminoethyl)-cellulose matrix with a yield of 66%. The purified free and immobilized enzyme had optimum activity at pH 7.5 and 6.0, respectively. Immobilization increases the stability of the enzyme with respect to temperature. The half-life of the immobilized enzyme was 30 min at 45 degrees C, longer than that of the free enzyme (10 min). The purified free sulfide oxidase activity was completely inhibited by 1 mM Co2+ and Zn2+ and sulfhydryl group reagents (para-chloromercuribenzoic acid and iodoacetic acid). Catalytic activity was not affected by 1 mM Ca2+, Mg2+, Na+ and metal-chelating agent (EDTA).     

Influence of pH and ionic strength on the adsorption, leaching and activity of myoglobin immobilized onto ordered mesoporous silicates

Myoglobin has been immobilized onto different ordered mesoporous silicates. The effect of the pH on the adsorption, leaching and activity was studied. The results showed that the maximum amount of protein was adsorbed at a pH 6.5, just below the protein isoelectric point (7–7.3). There was no effect of increasing ionic strength on the adsorption profile at different pH values. The adsorption is rationalized in terms of local electrostatic forces acting between the enzyme and the silica surface as well as hydrophobic interactions close to the protein isoelectric point, whereas at low pH the global charges give rise to protein–protein repulsion and at high pH enzyme–silica repulsion. Higher amounts of immobilized myoglobin were leached at a pH 4, while lower amounts were leached at pH 6.5. The catalytic activity of myoglobin immobilized onto SBA-15 showed optimal activity at a pH 6.5 in comparison to a pH of 5 for the free form.     

Immobilization of glucooligosaccharide oxidase of Acremonium strictum for oligosaccharic acid production

Summary The glucooligosaccharide oxidase was covalently immobilized to chitosan with polyethyleneimine and glutaraldehyde. Immobilization improved thermal stability. When used for conversion of starch hydrolysate to oligosaccharic acids, the immobilized enzyme maintained 75% initial activity after 60 days of continuous operation. Strong substrate inhibition was seen at high concentrations of cellobiose and lactose for free enzyme but not for immobilized enzyme.     

Immobilization of catalase into chemically crosslinked chitosan beads

Bovine liver catalase was immobilized into chitosan beads prepared in crosslinking solution. Various characteristics of immobilized catalase such as the pH–activity curve, the temperature–activity curve, thermal stability, operational stability, and storage stability were evaluated. Among them the pH optimum and temperature optimum of free and immobilized catalase were found to be pH 7.0 and 35 °C. The K_m value of immobilized catalase (77.5 mM) was higher than that of free enzyme (35 mM). Immobilization decreased in V_max value from 32,000 to 122 μmol (min mg protein)⁻¹. It was observed that operational, thermal and storage stabilities of the enzyme were increased with immobilization.     

Immobilization of Xylan-Degrading Enzymes from Scytalidium thermophilum on Eudragit L-100

Summary Xylanase from Scytalidium thermophilum was immobilized on Eudragit L-100, a pH sensitive copolymer of methacrylic acid and methyl methacrylate. The enzyme was non-covalently immobilized and the system expressed 70% xylanase activity. The immobilized preparation had broader optimum temperature of activity between 55 and 65 °C as compared to 65 °C in case of free enzyme and broader optimum pH between 6.0 and 7.0 as compared to 6.5 in case of free enzyme. Immobilization increased the t_1/2 of enzyme at 60 °C from 15 to 30 min with a stabilization factor of 2. The K_m and V_max values for the immobilized and free xylanase were 0.5% xylan and 0.89 μmol/ml/min and 0.35% xylan and 1.01 μmol/ml/min respectively. An Arrhenius plot showed an increased value of activation energy for immobilized xylanase (227 kcal/mol) as compared to free xylanase (210 kcal/mol) confirming the higher temperature stability of the free enzyme. Enzymatic saccharification of xylan was also improved by xylanase immobilization.     

Immobilization of polyphenol oxidase on chitosan–SiO<Subscript>2</Subscript> gel for removal of aqueous phenol

A partially purified potato polyphenol oxidase (PPO) was immobilized in a cross-linked chitosan–SiO₂ gel and used to treat phenol solutions. Under optimized conditions (formaldehyde 20 mg/ml, PPO 4 mg/ml and pH 7.0), the activity of immobilized PPO was 1370 U/g and its K _m value for catechol was 12 mm at 25°C. The highest activity of immobilized enzyme was at pH 7.4. Immobilization stabilized the enzyme with 73 and 58% retention of activity after 10 and 20 days, respectively, at 30°C whereas most of the free enzyme was inactive after 7 days. The efficiency of removing phenol (10 mg phenol/l) by the immobilized PPO was 86%, and about 60% removal efficiency was retained after five recycles. The immobilized PPO may thus be a useful for removing phenolic compounds from industrial waste-waters.     

Immobilized β-glucosidase on magnetic chitosan microspheres for hydrolysis of straw cellulose

β-Glucosidase immobilized on magnetic chitosan microspheres for potential recycling usage in hydrolysis of cellulosic biomass was investigated. The immobilized enzyme had an activity of 6.4 U/g support under optimized condition when using cellobiose as substrate. Immobilization resulted in less increase of the apparent K_m, low drift of the optimal pH, as well as improved stability relative to the free enzyme. The immobilized β-glucosidase was applied to enzymatic hydrolysis of corn straw to produce 60.2 g/l reducing sugar with a conversion rate of 78.2% over the course of a 32-h reaction. This conversion rate was maintained above 76.5% after recycling the enzyme for use in eight batches (total 256 h), showing favorable operational stability of the immobilized enzyme.