Continuous Chitosan Hydrolyzate Production by Immobilized Chitosanolytic Enzyme from Enterobacter sp. G-1

Chitosanolytic enzymes from Enterobacter sp. G-1 were immobilized on various carriers to continuously hydrolyze chitosan. Four different carriers were tested: FE-3901 (strong basic anion exchage resin, ionic binding), glutaraldehyde-treated FE-4612 (weak basic anion exchange resin, cross-linking), Chitopearl (chitosan beads), and alginate calcium. Glutaraldehyde-treated FE-4612 and Chitopearl immobilized more protein than the others. The enzyme immobilized on FE-3901 had the greatest activity. The activity of enzyme immobilized on FE-3901 decreased rapidly when exposed to a continuous flow of 1% chitosan. The enzyme immobilized with Chitopearl retained more than 50% of its original activity after 17 days, and the activity was fully restored by re-immobilization.     

Immobilization of levan fructotransferase for the production of di-fructose anhydride from levan

Levan fructotransferase (LFTase) from Arthrobacter ureafaciens K2032 was immobilized on various carriers of which Chitopearl BCW2501 beads showed the higher activity of 320 U g^–1 for the formation of di-fructose anhydride compounds. The immobilized enzyme retained about 60% of its initial activity after being used for 20 cycles.     

Continuous production of maltotetraose using a dual immobilized enzyme system of maltotetraose-forming amylase and pullulanase

In order to produce a product with a high content of maltotetraose, dual-enzyme systems composed of immobilized maltotetraose-forming amylase (G(4)-forming amylase) and pullulanase were studied. The thermostability of individually immobilized enzymes was examined in continuous operation; studies revealed that the enzyme immobilized on "Chitopearl" was much more stable than that immobilized on Diaion HP-50. The effects of operating conditions on the stability of G(4) forming amylase immobilized on "Chitopearl" were examined to confirm that the apparent half-life data could be arranged using the immobilized enzyme stability factor, f(s). As for the dual immobilized enzyme system, six methods of usage were considered, with five yielding a 7-10% (w/w) higher content of maltotetraose product than the single-enzyme system. The effects of operating conditions on the maltotetraose production reaction were examined to confirm that the maltotetraose content of the products could be analyzed using the specific space velocity,SSV. In dual immobilized enzyme systems, pullulanase immobilized on the same carrier as the G(4)-forming amylase was found to be more stable than pullulanase immobilized on separate carriers. The effectiveness of using immobilized pullulanase along with the G(4)-forming amylase was confirmed from constant-conversion operations in which the maltotetraose content in the product was kept at 50% (w/w) in laboratory-scale experimentation.     

Immobilization of glucose isomerase

The immobilization of glucose isomerase (D-xylose ketol isomerase, EC 5.3.1.5) by covalently bonding to various carriers and by adsorption to ion exchange resins was attempted in order to obtain a stable immobilized enzyme which can be used for continuous isomerization of glucose in a column. Of the covalent bonding methods, the colloidal silica-glutaraldehyde method showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Ludox HS-30 bound glucose isomerase column showed a half-life of 24 days and an enzyme usage of 0.07 units per gram of isomerized sugar (d.s, fructose 45%). Of the resins used, the macromolecular type or porous type strongly basic anion exchange resins showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Amberlite IRA-904 resine-bound glucose isomerase showed a half-life of 23 days and an enzyme usage of 0.06 units per gram of isomerized sugar (d.s., fructose 45%). Based on the ease of the immobilization process, the possibility of carrier reuse and the extensive use already achieved by ion exchange resins in the sugar industry, IRA-904 resin was selected as the candidate for commercialization.     

Amberlite IRA 900 versus calcium alginate in immobilization of a novel,engineered β-fructofuranosidase for short-chain fructooligosaccharide synthesis from sucrose

The immobilization of β-fructofuranosidase for short-chain fructooligosaccharide (scFOS) synthesis holds the potential for a more efficient use of the biocatalyst. However, the choice of carrier and immobilization technique is a key to achieving that efficiency. In this study, calcium alginate (CA), Amberlite IRA 900 (AI900) and Dowex Marathon MSA (DMM) were tested as supports for immobilizing a novel engineered β-fructofuranosidase from Aspergillus japonicus for scFOS synthesis. Several immobilization parameters were estimated to ascertain the effectiveness of the carriers in immobilizing the enzyme. The performance of the immobilized biocatalysts are compared in terms of the yield of scFOS produced and reusability. The selection of carriers and reagents was motivated by the need to ensure safety of application in the production of food-grade products. The CA and AI900 both recorded impressive immobilization yields of 82 and 62%, respectively, while the DMM recorded 47%. Enzyme immobilizations on CA, AI900 and DMM showed activity recoveries of 23, 27, and 17%, respectively. The CA, AI900 immobilized and the free enzymes recorded their highest scFOS yields of 59, 53, and 61%, respectively. The AI900 immobilized enzyme produced a consistent scFOS yield and composition for 12 batch cycles but for the CA immobilized enzyme, only 6 batch cycles gave a consistent scFOS yield. In its first record of application in scFOS production, the AI900 anion exchange resin exhibited potential as an adequate carrier for industrial application with possible savings on cost of immobilization and reduced technical difficulty.     

Preparation of d-sorbose from d-tagatose by immobilized d-tagatose 3-epimerase

d-Tagatose 3-epimerase (d-TE) from Pseudomonas sp. ST-24 was immobilized on various types of Chitopearl beads. The highest activity was found in d-TE immobilized on Chitopearl beads of BCW 2503, the yield being about 80% of free enzyme applied. Maximum activity of the immobilized enzyme was obtained at pH 7–9 and around 60°C. The enzyme was stable in a pH range of 7–10, and below 60°C. In a high concentration (30%) of substrate, the reaction progressed without substrate inhibition. Two grams of d-sorbose crystals could be obtained from 3 g d-tagatose. Furthermore, in a batch reaction repeated five times, about 70% of d-tagatose was converted to d-sorbose each time.     

无花果蛋白酶在阴离子交换树脂上的固定化

无花果蛋白酶通过８％戊二醛活化载体,共价结合到聚苯乙烯阴离子交换树脂ＧＭ２０１上,固定化作用在ｐＨ７．７,酶浓度０．８ｍｇ／ｇ树脂,４℃下进行６ｈ。得到的固定化酶表观Ｋ_ｍ值（酪蛋白,１．１１×１０~（－４）ｍｏｌ／Ｌ）小于溶液酶Ｋ_ｍ值（１．９６×１０~（－４）ｍｏｌ／Ｌ）;固定化酶活性在ｐＨ６～８保持稳定,溶液酶最适ｐＨ为７．２;固定化酶最适温度由溶液酶的５０～６０℃移至３７℃;固定化酶２５℃保持７ｄ,重复水解酪蛋白７次后,保留８３．３％活性。固定化酶对酪蛋白水解度达４７．５％,对大豆球蛋白达１１．６％。     

Immobilization of proteases to porous chitosan beads and their catalysis for ester and peptide synthesis in organic solvents.

alpha-Chymotrypsin (CT), subtilisin BPN' (STB), and subtilisin Carlsberg (STC) were immobilized by adsorption to porous chitosan beads (Chitopearl, CP). The immobilized enzymes showed higher catalytic activities than free enzymes for amino acid esterification in many hydrophilic organic solvents except for methanol and DMF. In ethanol, the initial rate of the esterification increased with water content, whereas in ethyl acetate, the maximum rate was obtained at 2%-3% water. CP-immobilized CT also catalysed transesterification of Ac-Tyr-OMe in ethanol and peptide synthesis in acetonitrile from Ac-Tyr-OH or its ethyl ester and amino acid amides. The immobilized enzymes are highly stable in organic solutions, and can easily be separated from the reaction solutions. Repeated esterifications of Ac-Tyr-OH in acetonitrile by a CP-immobilized CT gave almost constant yields of the ester for more than 3 weeks.     

D301树脂固定化假丝酵母脂肪酶

本研究选择7种吸附和离子交换树脂进行了假丝酵母脂肪酶(Candida sp.lipase)的固定化试验,通过测定固定化后各脂肪酶的酶活,筛选出固定化效果较好的弱碱性阴离子交换树脂D301;并通过扫描电镜将D301与脂肪酶Novozym 435的表面形貌做比较,进一步选定D301树脂作为载体,并对其采用戊二醛交联固定化,研究并优化了其固定化条件。结果表明,5%戊二醛溶液的加入量为8mL,处理时间为5h,酶液浓度为1.0g/L,磷酸缓冲盐溶液pH6.0,固定化处理10h效果最好,获得的固定化酶活力可达35U/mg,酶的固定化效率约为3.5U/(mg·h)。     

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.     

Immobilization of cycloisomaltooligosaccharide glucanotransferase for the production of cycloisomaltooligosaccharides from dextran

Immobilization of cycloisomaltooligosaccharide glucanotransferase (CITase) and its application in the production of cycloisomaltooligosaccharides (CIs) from dextran were studied. Among various carrier materials examined, the enzyme adsorbed physically on Chitopearl BCW-3505 showed the highest activity (1.75 U/ml carrier). The activity remaining was 35%. The maximum CI yield in batch reactions at 0.2, 2 and 10% dextran was 28, 24 and 12%, respectively. The maximum CI yield at 2% dextran (24%) was slightly less than that with the free enzyme under the same conditions (26%). The concentration of linear oligosaccharides, the byproducts in the reaction mixture, was greater with the immobilized CITase than the free enzyme. The immobilized CITase was less thermostable than the free enzyme by about 10 degrees C. The pattern of influence of Ca(2+) concentration on the thermostability differed between the free and immobilized CITase. A Ca(2+) concentration of 50-100 mM was optimum for the thermostability of the immobilized CITase, 10-50 mM for the free enzyme. CIs were produced continuously by a column system packed with the immobilized enzyme at 40 degrees C with a space velocity (SV) of 6 h(-1). The three quarters life time was 4 weeks. We think that relatively long life time at fast SV was accomplished and CI production cost by this method should be lower than the batch reaction. This is the first report on immobilization of CITase.     

On the Activities of Glucoamylase Chemically Fixed to Cyanogen Bromide-activated Cellulose

N-Carbamyl-D-amino acid amidohydrolase (DCase), produced with recombinant Escherichia coli cells using a cloned gene from Agrobacterium sp. strain KNK712, has been immobilized for use in the production of D-amino acids. The porous polymers, Duolite A-568 and Chitopearl 3003, were much better than other resins for the activity and stability of the adsorbed enzyme. The activity of DCase expressed on Duolite A-568 and Chitopearl 3003 amounted to 96 units/g-wet-resin and 91 units/g-wet-resin, respectively. DCase immobilized on Duolite A-568 was found to be most stable at about pH 7, and it was further stabilized by reductants such as dithiothreitol, L-cysteine, cysteamine, and sodium hydrosulfite. The stability during the repeated batch reactions was greatly improved when dithiothreitol was in the reaction mixture, and the higher crosslinking degree with glutaraldehyde also stabilized the immobilized enzyme. After 14 times repeated reactions, the remaining activity of the immobilized enzyme cross-linked with 0.1% and 0.2% of glutaraldehyde, and 0.2% of glutaraldehyde with dithiothreitol in the reaction mixture was 12%, 18%, and 63%, respectively. DCase produced with Pseudomonas sp. strain KNK003A and Pseudomonas sp. strain KNK505, which are thermotolerant soil bacteria, and that with Agrobacterium sp. strain KNK712 were also immobilized on Duolite A-568. The stability of the enzymes of thermotolerant bacteria during reactions was superior to that of Agrobacterium sp. strain KNK712, though the activity was lower than that of strain KNK712.     

Anionic exchange nylon laminated membranes for enzyme immobilization

Summary This work presents the optimization of the chemical steps involved in nylon modification with dimethyl sulphate, polyethyleneimine, glutaraldehyde and 2-diethyl aminoethylamine to obtain a weak basic anion exchange support. Activated nylon laminated membranes were utilized for aminoacylase immobilization, allowing an ionically adsorbed enzyme derivative with high activity (0.16 U/mg E·cm²) and low removed activity (<1%). Optimum immobilization conditions and kinetic parameters were also determined. This immobilized enzyme can be used in laminated enzyme membrane reactors.     

Immobilization of trypsin on chitosan gels: use of different activation protocols and comparison with other supports

Trypsin was immobilized on chitosan gels coagulated with 0.1 or 1 M NaOH and activated with glutaraldehyde or glycidol. The derivatives were characterized by their recovered activity, thermal (40, 55 and 70 degrees C) and alkaline (pH 11) stabilities, amount of enzyme immobilized on gels for several enzyme loads (8-14 mg(protein)/g(Gel)) and compared to agarose derivatives. Enzyme loads higher than 14 mg(protein)/g(Gel) can be immobilized on glutaraldehyde derivatives, which showed 100% immobilization yield and, for loads up to 8 mg(protein)/g(Gel), 100% recovered activity. Activation with glycidol led to lower immobilization yields than the ones obtained with glutaraldehyde, 61% for agarose-glyoxyl (AgGly) with low grade of activation and 16% for the chitosan-glyoxyl (ChGly), but allowed obtaining the most stable derivative (ChGly), that was 660-fold more stable than the soluble enzyme at 55 and 70 degrees C-approximately threefold more stable than AgGly. The ChGly derivative presented also the highest stability during incubation at pH 11. Analyses of lysine residue contents in soluble and immobilized trypsin indicated formation of multipoint bonds between enzyme and support, for glyoxyl derivatives.     

Immobilization of urease on nanostructured polymer membrane and preparation of urea amperometric biosensor

A new matrix for enzyme immobilization of urease was obtained by incorporating rhodium nanoparticles (5% on activated charcoal) and chemical bonding of chitosan with different concentration (0.15%; 0.3%; 0.5%; 1.0%; 1.5%) in previously chemically modified AN copolymer membrane. The basic characteristics of the chitosan modified membranes were investigated. The SEM analyses were shown essential morphology change in the different modified membranes. Both the amount of bound protein and relative activity of immobilized enzyme were measured. A higher activity (about 77.44%) was measured for urease bound to AN copolymer membrane coated with 1.0% chitosan and containing rhodium nanoparticles. The basic characteristics (pH(opt), T(opt), thermal, storage and operation stability) of immobilized enzyme on this optimized modified membrane were also determined. The prepared enzyme membrane was used for the construction of amperometric biosensor for urea detection. Its basic amperometric characteristics were investigated. A calibration plot was obtained for urea concentration ranging from 1.6 to 23 mM. A linear interval was detected along the calibration curve from 1.6 to 8.2mM. The sensitivity of the constructed biosensor was calculated to be 3.1927 μAmM(-1)cm(-2). The correlation coefficient for this concentration range was 0.998. The detection limit with regard to urea was calculated to be 0.5mM at a signal-to-noise ratio of 3. The biosensor was employed for 10 days while the maximum response to urea retained 86.8%.     

The simultaneous production of sorbitol from fructose and gluconic acid from glucose using an oxidoreductase of Zymomonas mobilis

Summary The production of sorbitol and gluconic acid by toluene-treated, permeabilized cells of Zymomonas mobilis has been evaluated. From a 60% total sugar solution (300 g/l glucose and 300 g/l fructose), a sorbitol concentration of 290 g/l and a gluconic acid concentration of 283 g/l were achieved after 15 h in a batch process using free toluene-treated cells. A continuous process with immobilized cells was developed and only a small loss of enzyme activity (less than 5%) was evident after 120 h. With a strongly basic anion exchange resin and an eluent of 0.11 M Na₂B₄O₇/0.11 M H₃BO₃, good separation of sorbitol and gluconic acid was achieved.     

Continuous hydrolysis of oil by immobilized lipase in a countercurrent reactor

Lipase from Pseudomonas fluorescens biotype I was immobilized by adsorption of anion exchange resin using glutaraldehyde to enhance the adsorption. The activity yield of the immobilized lipase was very low (below 1%) when lipase activity was measured using emulsion substrate. The activity yield was 10-70% when lipase activity was measured using non-emulsion substrate. Countercurrent reactors for hydrolysis of oil using non-emulsion substrate were studied. A fluidized bed reactor was found to be superior to a fixed bed one since in a fixed bed reactor the separation rate of the two layers was slow and the flow rate of the reactor had to be slower than the separation rate. A fluidized bed reactor system equipped with settling compartments and stirring compartments was devised. Continuous lipolysis at 60 degrees C and continuous separation of oily product and water soluble product were performed. After continuous operation for more than 3 months, 70% of the initial activity of the immobilized lipase was observed at the end of the reaction.     

Adsorption of BSA on strongly basic chitosan: Equilibria

Equilibrium isotherms for adsorption of bovine serum albumin (BSA) on a new adsorbent, a strongly basic crosslinked chitosan (Chitopearl 2503), which is hard and is not compressed by pressure in a column, have been presented and compared with diethylaminoethyl (DEAE) Sepharose Fast Flow (hard gel). In Chitopearl 2503, when only buffer existed in the BSA solution, the isotherm was not affected by the initial concentration of BSA but it was affected by pH considerably. The isotherm was favorable when pH >/= pl ( congruent with 4.8). When NaCl existed in the BSA solution, the amount of BSA absorbed on the resin decreased with increasing concentration of NaCl. When the concentration of NaCl was 200 mol/m(3), the resin did not adsorb BSA at all. The equilibrium data were correlated by the Langmuir equation reasonably well. The BSA may be adsorbed mainly by electrostatic attraction between negatively charged BSA and positively charged quanternary ammonium groups at pH > pl and by protonation reaction of the primary ammonium groups by weak acid groups of BSA at pH = pl. These are confirmed by measuring the amount of inorganic ion exchanged for BSA. In DEAE Sepharose Fast Flow, the isotherm was favorable when pH > pl but unfavorable ar pH = pl. The saturation capacity of BSA on Chitopearl 2503 is about 1.3 to 2.2 times larger than that on DEAE Sepharose Fast Flow. (c) 1994 John Wiley & Sons, Inc.     

N-氨甲酰基-D-氨基酸酰胺水解酶的固定化工艺

以TJS环氧基树脂作为载体对N-氨甲酰基-D-氨基酸酰胺水解酶进行固定化,最佳工艺条件为：1g树脂载体大约对应133U酶液,蛋白质量浓度0.35mg/mL,固定时间15h,温度28℃,pH7.5,固定化酶活达到58.5U。蛋白固定率可达97.4%,酶活回收率达到49.3%,得到的固定化酶使用半衰期达到26批。     

Covalent immobilization of ω-transaminase from Vibrio fluvialis JS17 on chitosan beads

Chitosan beads were prepared by emulsion method and used for the immobilization of ω-transaminase of Vibrio fluvialis. The yield of enzyme immobilization (54.3%) and its residual activity (17.8%) were higher than those obtained with other commercial beads. ω-Transaminase was effectively immobilized on the chitosan beads at pH 6.0. The optimal pH of the immobilized enzyme was pH 9.0, which is the same as that of the free enzyme. The immobilized enzyme on chitosan beads retained ca. 77% of its conversion after five consecutive reactions with the 25 mM substrate, while the immobilized enzyme on Eupergit^® C retained 12%. Also, the immobilized ω-transaminase on chitosan bead retained 70% of initial activity when it's stored at 4 °C for 3.5 weeks. Addition of the co-factor, pyridoxal 5-phosphate (PLP), was needed to maintain the stability of the immobilized ω-transaminase.