Redefining the minimal substrate tolerance of mandelate racemase. Racemization of trifluorolactate

Mandelate racemase (EC 5.1.2.2) from Pseudomonas putida catalyzes the interconversion of the enantiomers of mandelic acid and a variety of aryl- and heteroaryl-substituted mandelate derivatives, suggesting that β,γ-unsaturation is a requisite feature of substrates for the enzyme. We show that β,γ-unsaturation is not an absolute requirement for catalysis and that mandelate racemase can bind and catalyze the racemization of (S)-trifluorolactate (k(cat) = 2.5 ± 0.3 s(-1), K(m) = 1.74 ± 0.08 mM) and (R)-trifluorolactate (k(cat) = 2.0 ± 0.2 s(-1), K(m) = 1.2 ± 0.2 mM). The enzyme was shown to catalyze hydrogen-deuterium exchange at the α-postion of trifluorolactate using (1)H NMR spectrocsopy. β-Elimination of fluoride was not detected using (19)F NMR spectroscopy. Although mandelate racemase bound trifluorolactate with an affinity similar to that exhibited for mandelate, the turnover numbers (k(cat)) were markedly reduced by ～318-fold, resulting in catalytic efficiencies (k(cat)/K(m)) that were ~400-fold lower than those observed for mandelate. These observations suggested that chemical steps on the enzyme were likely rate-determining, which was confirmed by demonstrating that the rates of mandelate racemase-catalyzed racemization of (S)-trifluorolactate were not dependent upon the solvent microviscosity. Circular dichroism spectroscopy was used to measure the rates of nonenzymatic racemization of (S)-trifluorolactate at elevated temperatures. The values of ΔH(?) and ΔS(?) for the nonenzymatic racemization reaction were determined to be 28.0 (±0.7) kcal/mol and -15.7 (±1.7) cal K(-1) mol(-1), respectively, corresponding to a free energy of activation equal to 33 (±4) kcal/mol at 25 °C. Hence, mandelate racemase stabilizes the altered trifluorolactate in the transition state (ΔG(tx)) by at least 20 kcal/mol.     

南海深海微生物酯酶EST12-7在制备(R)-2-氯丙酸乙酯中的应用研究

利用来源南海深海的微生物酯酶EST12-7不对称水解反应拆分制备（R）-2-氯丙酸乙酯。并探寻了温度、pH、底物浓度、有机溶剂和反应时间等因素对酯酶EST12-7催化制备（R）-2-氯丙酸乙酯的影响。结果表明,深海微生物酯酶EST12-7催化制备（R）-2-氯丙酸乙酯的最佳反应条件为：13.8 μg/ml酯酶EST12-7,50 mmol/L（±）-2-氯丙酸乙酯,2%正癸醇,pH8.5,30℃,0.05mol/L Tris-HCl,反应60 min。在最佳反应条件下,（±）-2-氯丙酸乙酯的转化率可达49%,所制备的（R）-2-氯丙酸乙酯的光学纯度为98%。通过对酯酶EST12-7拆分制备（R）-2-氯丙酸甲酯和（R）-2-氯丙酸乙酯进行比较,2-氯丙酸酯中的链长对酯酶EST12-7拆分反应有极大的影响。     

Purification and characterization of a feruloyl esterase from the intestinal bacterium Lactobacillus acidophilus

Dietary ferulic acid (FA), a significant antioxidant substance, is currently the subject of extensive research. FA in cereals exists mainly as feruloylated sugar ester. To release FA from food matrices, it is necessary to cleave ester cross-linking by feruloyl esterase (FAE) (hydroxycinnamoyl esterase; EC 3.1.1.73). In the present study, the FAE from a human typical intestinal bacterium, Lactobacillus acidophilus, was isolated, purified, and characterized for the first time. The enzyme was purified in successive steps including hydrophobic interaction chromatography and anion-exchange chromatography. The purified FAE appeared as a single band in sodium dodecyl sulfate-polyacrylamide gel electrophoresis, with an apparent molecular mass of 36 kDa. It has optimum pH and temperature characteristics (5.6 and 37 degrees C, respectively). The metal ions Cu(2+) and Fe(3+) (at a concentration of 5 mmol liter(-1)) inhibited FAE activity by 97.25 and 94.80%, respectively. Under optimum pH and temperature with 5-O-feruloyl-L-arabinofuranose (FAA) as a substrate, the enzyme exhibited a K(m) of 0.0953 mmol liter(-1) and a V(max) of 86.27 mmol liter(-1) min(-1) mg(-1) of protein. Furthermore, the N-terminal amino acid sequence of the purified FAE was found to be A R V E K P R K V I L V G D G A V G S T. The FAE released FA from O-(5-O-feruloyl-alpha-L-arabinofuranosyl)-(1-->3)-O-beta-D-xylopyranosyl-(1-->4)-D-xylopyranose (FAXX) and FAA obtained from refined corn bran. Moreover, it released two times more FA from FAXX in the presence of added xylanase.     

Chemically surface modified gel (CSMG): an excellent enzyme-immobilization matrix for industrial processes

Invertase from S. cerevisiae has been immobilized on porous silica matrix, formed using sol-gel chemistry, with surface area of approximately 650 m(2)/g. The co-condensation of silica sol with 3-aminopropyl(triethoxy)silane produced an amino-chemically surface modified silica gel (N-CSMG) with a very high ligand loading of 3.6 mmol/g SiO(2); significantly higher than commercially available matrices. Surface amine groups were activated with glutaraldehyde to produce GA-N-CSMG, and invertase covalently attached by the aldehyde. Invertase was used as a model enzyme to measure the immobilizing character of the GA-N-CSMG material. Using an optimized immobilization protocol, a very high loading of 723 mg invertase per gram GA-N-CSMG is obtained; 3-200-fold higher than values published in literature. The reproducible, immobilized activity of 246,000 U/g GA-N-CSMG is also greater than any other in literature. Immobilized invertase showed almost 99% retention of free enzyme activity and no loss in catalytic efficiency. The apparent kinetic parameters K(M) and V(M) were determined using the Michealis-Menten kinetic model. K(M) of the free invertase was 1.5 times greater than that of the immobilized invertase--indicating a higher substrate affinity of the immobilized invertase. These findings show considerable promise for this material as an immobilization matrix in industrial processes.     

Cross-linked enzyme aggregates of β-glucosidase from Prunus domestica seeds

Cross-linked enzyme aggregates (CLEAs) of β-glucosidase were prepared and characterized. Under the optimum conditions, the activity recovery of CLEAs reached 84?%. The reduction by NaBH(4) resulted in slightly lower activities of CLEAs, while their thermostability was enhanced. CLEAs were more thermally stable than free enzyme (half lives, 973 vs. 518?min at 50?°C), while less stable than seed meal (half life, 1,090?min). In 90?% (v/v) t-butanol, the half lives of CLEAs and free enzyme were 53 and 6.7?h, respectively. Besides, the catalytic efficiency (V (max)/K (m)) of CLEAs was comparable to free enzyme (0.42 vs. 0.47?min(-1) mg(-1)). This carrier-free immobilized enzyme had a network structure with multiple layers. The productivity of salidroside using CLEAs reached 150?g/l?g catalyst, while being 6.3?g/l?g with seed meal.     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

The comparison of the estimation of enzyme kinetic parameters by fitting reaction curve to the integrated Michaelis-Menten rate equations of different predictor variables

The estimation of enzyme kinetic parameters by nonlinear fitting reaction curve to the integrated Michaelis-Menten rate equation ln(S(0)/S)+(S(0)-S)/K(m)=(V(m)/K(m))xt was investigated and compared to that by fitting to (S(0)-S)/t=V(m)-K(m)x[ln(S(0)/S)/t] (Atkins GL, Nimmo IA. The reliability of Michaelis-Menten constants and maximum velocities estimated by using the integrated Michaelis-Menten equation. Biochem J 1973;135:779-84) with uricase as the model. Uricase reaction curve was simulated with random absorbance error of 0.001 at 0.075 mmol/l uric acid. Experimental reaction curve was monitored by absorbance at 293 nm. For both CV and deviation <20% by simulation, K(m) from 5 to 100 micromol/l was estimated with Eq. (1) while K(m) from 5 to 50 micromol/l was estimated with Eq. (2). The background absorbance and the error in the lag time of steady-state reaction resulted in negative K(m) with Eq. (2), but did not affect K(m) estimated with Eq. (1). Both equations gave better estimation of V(m). The computation time and the goodness of fit with Eq. (1) were 40-fold greater than those with Eq. (2). By experimentation, Eq. (1) yielded K(m) consistent with the Lineweaver-Burk plot analysis, but Eq. (2) gave many negative parameters. Apparent K(m) by Eq. (1) linearly increased, while V(m) were constant, vs. xanthine concentrations, and the inhibition constant was consistent with the Lineweaver-Burk plot analysis. These results suggested that the integrated rate equation that uses the predictor variable of reaction time was reliable for the estimation of enzyme kinetic parameters and applicable for the characterization of enzyme inhibitors.     

一种不对称水解（R,S）-2,6-二甲基苯基氨基丙酸甲酯的新酯酶基因的克隆表达和酶学性质研究

本文将来自反硝化无色杆菌Achromobacterdenitrificans1104的酯酶基因EHest,转化大肠杆菌中,成功表达了具有不对称水解农药甲霜灵的中间体(R,S)-2,6-二甲基苯基氨基丙酸甲酯( MAP )活性的酯酶EHesterase。用重组酯酶EHesterase催化MAP 的水解,底物浓度50 g/L,反应1h的转化率29.5%,产物( R-酸)的eep 是85.1%。该酶的最适反应pH和温度分别为9.0和50℃,在50℃以下和pH5~9之间具有较好的稳定性。该酶水解MAP 的米氏动力学参数Vm、Km 分别是0.733 g/(L·min)和7.49 g/L。加入10%DMSO对酶EHesterase的立体选择性和催化速度有一定的促进作用。 Cu2+、Fe3+对酶活有明显抑制作用。该酶水解MAP 的活性与水解p-对硝基苯乙酸酯的活性数量级相当,是水解橄榄油活性的333倍。     

Selection and characterization of a mutant of the cloned gene for mandelate racemase that confers resistance to an affinity label by greatly enhanced production of enzyme

The plasmid pSCR1 containing the gene for mandelate racemase (EC 5.1.2.2) from Pseudomonas putida (ATCC 12633) allows Pseudomonas aeruginosa (ATCC 15692) to grow on (R)-mandelate as its sole carbon source [Ransom, S. C., Gerlt, J. A., Powers, V. M., & Kenyon, G. L. (1988) Biochemistry 27, 540]; the chromosome of the P. aeruginosa host apparently does not contain the gene for mandelate racemase but does contain genes for the remaining enzymes in the mandelate pathway and enables growth on (S)-mandelate as carbon source. However, in the presence of alpha-phenylglycidate, an active-site-directed irreversible inhibitor (affinity label) of mandelate racemase, P. aeruginosa transformed with pSCR1 can utilize (S)-mandelate but not (R)-mandelate as carbon source. This inhibition of growth on (R)-mandelate provides a metabolic selection for mutants that are resistant to alpha-phenylglycidate. When (R)-mandelate is used as carbon source and alpha-phenylglycidate is present, a few colonies of P. aeruginosa transformed with pSCR1 grow slowly and appear on plates after several days. The plasmid isolated from these cells confers resistance to alpha-phenylglycidate on newly transformed cells of P. aeruginosa. This resistance to the affinity label is not due to a mutation within the primary structure of the enzyme. A single base change (C----A) located 87 bp upstream of the initiation codon for the gene for mandelate racemase was detected in three independent isolates of alpha-phenylglycidate-resistant colonies and appears responsible for a 30-fold increase in the amount of mandelate racemase encoded by the gene contained in the plasmid.(ABSTRACT TRUNCATED AT 250 WORDS)     

Racemization of undesired enantiomers: Immobilization of mandelate racemase and application in a fixed bed reactor

Production of optically pure products can be based on simple unselective synthesis of racemic mixtures combined with a subsequent separation of the enantiomers; however, this approach suffers from a 50% yield limitation which can be overcome by racemization of the undesired enantiomer and recycling. Application of biocatalyst for the racemization steps offers an attractive option for high‐yield manufacturing of commercially valuable compounds. Our work focuses on exploiting the potential of racemization with immobilized mandelate racemase. Immobilization of crude mandelate racemase via covalent attachment was optimized for two supports: Eupergit^® CM and CNBr‐activated Sepharose 4 Fast Flow. To allow coupling of enzymatic reaction with enantioselective chromatography, a mobile phase composition compatible with both processes was used in enzymatic reactor. Kinetic parameters obtained analyzing experiments carried out in a batch reactor could be successfully used to predict fixed‐bed reactor performance. The applicability of the immobilized enzyme and the determined kinetic parameters were validated in transient experiments recording responses to pulse injections of R‐mandelic acid. The approach investigated can be used for futher design and optimization of high yield combined resolution processes. The characterized fixed‐bed enzymatic reactor can be integrated e.g. with chromatographic single‐ or multicolumn steps in various configurations.     

Hydrophobic nature of the active site of mandelate racemase

Mandelate racemase (EC 5.1.2.2) from Pseudomonas putida catalyzes the interconversion of the two enantiomers of mandelic acid with remarkable proficiency, stabilizing the altered substrate in the transition state by approximately 26 kcal/mol. We have used a series of substrate analogues (glycolates) and intermediate analogues (hydroxamates) to evaluate the contribution of the hydrophobic cavity within the enzyme's active site to ligand binding. Free energy changes accompanying binding of glycolate derivatives correlated well with the hydrophobic substituent constant pi and the van der Waals surface areas of the ligands. The observed dependence of the apparent binding free energy on surface area of the ligand was -30 +/- 5 cal mol(-1) A(-2) at 25 degrees C. Free energy changes accompanying binding of hydroxamate derivatives also correlated well with pi values and the van der Waals surface areas of the ligands, giving a slightly greater free energy dependence equal to -41 +/- 3 cal mol(-1) A(-2) at 25 degrees C. Surprisingly, mandelate racemase exhibited a binding affinity for the intermediate analogue benzohydroxamate that was 2 orders of magnitude greater than that predicted solely on the basis of hydrophobic interactions. This suggests that there are additional specific interactions that stabilize the altered substrate in the transition state. Mandelate racemase was competitively inhibited by (R,S)-1-naphthylglycolate (apparent K(i) = 1.9 +/- 0.1 mM) and (R,S)-2-naphthylglycolate (apparent K(i) = 0.52 +/- 0.03 mM), demonstrating the plasticity of the hydrophobic pocket. Both (R)- (K(m) = 0.46 +/- 0.06 mM, k(cat) = 33 +/- 1 s(-1)) and (S)-2-naphthylglycolate (K(m) = 0.41 +/- 0.03 mM, k(cat) = 25 +/- 1 s(-1)) were shown to be alternative substrates for mandelate racemase. These kinetic results demonstrate that no major steric restrictions are imposed on the binding of this bulkier substrate in the ground state but that steric factors appear to impair transition state/intermediate stabilization. 2-Naphthohydroxamate was identified as a competitive inhibitor of mandelate racemase, binding with an affinity (K(i) = 57 +/- 18 microM) that was reduced relative to that observed for benzohydroxamate and that was in accord with the approximately 10-fold reduction in the value of k(cat)/K(m) for the racemization of 2-naphthylglycolate. These findings indicate that, for mandelate racemase, steric constraints within the hydrophobic cavity of the enzyme-intermediate complex are more stringent than those in the enzyme-substrate complex.     

Optimizing Immobilization and Stabilization of Feruloyl Esterase from Humicola Insolens and its Application for the Feruloylation of Oligosaccharides

Feruloyl esterase (FAE)-catalyzed esterification reaction is as a potential route for the biosynthesis of feruloylated oligosaccharides as functional ingredients. Immobilization of FAE from Humicola insolens on metal chelate-epoxy supports was investigated. The study of effects of immobilization parameters using response surface methodology revealed the significance of enzyme/support ratio (3.25-29.25 mg/g support), immobilization time (14-38 h), buffer molarity (0.27-1.25 M) and pH (4.0-8.0). The interactions between enzyme-to-support ratio/buffer molarity and enzyme-to-support ratio/pH were found to be critical for the modulation of the immobilization activity yield and the retention of specific activity, respectively. Optimum conditions for FAE-immobilization on metal chelate Sepabeads® EC-EP R were identified to be 22.75 mg FAE/g support, pH of 5.0, 27.7 h and buffer molarity of 0.86 M. At these conditions, an activity yield of 82.4%, a specific activity retention of 143.4%, and an enzyme activity of 395.4 μmol/min. g support were achieved. Further incubation of the immobilized FAE at pH 10.0 improved its thermostability. Increasing the pore size of the epoxy support improved the retention of FAE hydrolytic activity and the esterifying efficiency of the immobilized biocatalyst. Optimally immobilized and stabilized FAE on metal chelate-epoxy support retained up to 92.9% of the free enzyme feruloylation efficiency to xylooligosaccharides..     

Immobilization of laccase onto spacer-arm attached non-porous poly(GMA/EGDMA) beads: application for textile dye degradation

Non-porous poly(glycidyl methacrylate/ethyleneglycol dimetacrylate) (poly(GMA/EGDMA)) beads were prepared by suspension polymerization. The enzyme (i.e. laccase) was covalently immobilized onto plain and spacer-arm attached poly(GMA/EGDMA) beads. The amount of immobilized enzyme on the plain and spacer-arm attached beads was determined as 5.6 and 4.9 mg/g, respectively. The maximum activity (V(max)) and Michaelis constant (K(m)) of laccase immobilized on the spacer-arm attached beads, were found to be 77.6 U/min and 0.47 mM, respectively. Finally, the immobilized laccase was operated in a batch system, and textile dye Reactive Red 120 was successfully decolorized in the enzyme reactor.     

Comparative biosorption of mercuric ions from aquatic systems by immobilized live and heat-inactivated Trametes versicolor and Pleurotus sajur-caju

Trametes versicolor and Pleurotus sajur-caju mycelia immobilized in Ca-alginate beads were used for the removal of mercuric ions from aqueous solutions. The sorption of Hg(II) ions by alginate beads and both immobilized live and heat-killed fungal mycelia of T. versicolor and P. sajur-caju was studied in the concentration range of 0.150-3.00 mmol dm(-3). The biosorption of Hg(II) increased as the initial concentration of Hg(II) ions increased in the medium. Maximum biosorption capacities for plain alginate beads were 0.144+/-0.005 mmol Hg(II)/g; for immobilized live and heat-killed fungal mycelia of T. versicolor were 0.171+/-0.007 mmol Hg(II)/g and 0.383+/-0.012 mmol Hg(II)/g respectively; whereas for live and heat-killed P. sajur-caju, the values were 0.450+/-0.014 mmol Hg(II)/g and 0.660+/-0.019 mmol Hg(II)/g respectively. Biosorption equilibrium was established in about 1 h and the equilibrium adsorption was well described by Langmuir and Freundlich adsorption isotherms. Between 15 and 45 degrees C the biosorption capacity was not affected and maximum adsorption was observed between pH 4.0 and 6.0. The alginate-fungus beads could be regenerated using 10 mmol dm(-3) HCl solution, with up to 97% recovery. The biosorbents were reused in five biosorption-desorption cycles without a significant loss in biosorption capacity. Heat-killed T. versicolor and P. sajur-caju removed 73% and 81% of the Hg(II) ions, respectively, from synthetic wastewater samples.     

Enhanced activity and enantioselectivity of Candida rugosa lipase immobilized on macroporous adsorptive resins for ibuprofen resolution

The lipase from Candida rugosa was immobilized on three commercially available macroporous adsorptive resins for kinetic resolution of ibuprofen. One resin, CRB02, increased the enzyme activity by 50% to 0.027 g g(-1) min(-1). The deactivation constant (0.19 h(-1)) of the immobilized enzyme was half of that of the native enzyme and the enantioselectivity (E = 29.2) of the immobilized lipase was 2.2 times as much as that of the native lipase for the kinetic resolution of ibuprofen with 1-propanol in isooctane at 30 degrees C.     

Human CYP1A1 variants lead to differential eicosapentaenoic acid metabolite patterns

To answer the question whether the most common allelic variants of human CYP1A1, namely CYP1A1.1 (wild type), CYP1A1.2 (Ile462Val), and CYP1A1.4 (Thr461Asn), differ in their catalytic activity towards eicosapentaenoic acid (EPA), in vitro enzymatic assays were performed in reconstituted CYP1A1 systems. All CYP1A1 variants catalyzed EPA epoxygenation and hydroxylation to 17(R),18(S)-epoxyeicosatetraenoic acid (17(R),18(S)-EETeTr) and 19-OH-EPA, yet with varying catalytic efficiency and distinct regiospecificity. CYP1A1.1 and CYP1A1.4 formed 17(R),18(S)-EETeTr as main product (K(m)=53 and 50 microM; V(max)=0.60 and 0.50 pmol/min/pmol; V(max)/K(m)=0.11 and 0.10 microM(-1)min(-1), respectively), followed by 19-OH-EPA (K(m)=76 and 93 microM; V(max)=0.37 and 0.37 pmol/min/pmol; V(max)/K(m)=0.005 and 0.004 microM(-1)min(-1), respectively). The variant CYP1A1.2 produced almost equal amounts of both metabolites, but its catalytic efficiency for hydroxylation was five times higher (K(m)=66 microM; V(max)=1.7 pmol/min/pmol; V(max)/K(m)=0.026 microM(-1)min(-1)) and that for epoxygenation was twice higher (K(m)=66 microM; V(max)=1.5 pmol/min/pmol; V(max)/K(m)=0.023 microM(-1)min(-1)) than those of the wild-type enzyme. Thus, the Ile462Val polymorphism in human CYP1A1 affects EPA metabolism and may contribute to interindividual variance in the local production of physiologically active fatty acid metabolites in the cardiovascular system and other extrahepatic tissues, where CYP1A1 is expressed or induced by polycyclic aromatic hydrocarbons and other xenobiotics.     

Cellulase immobilization on Fe3O4 and characterization

A successful procedure for attaching cellulase to 45 mum iron oxide particles with a high-molecular-weight (1000) ligand has been developed. Mass and activity balances were calculated for immobilized enzymes with different loadings. The highest specific activity of the immobilized enzyme was 5.9 mmol glucose/g bound protein/h. The efficacy of retaining enzymatic activity was 128%. The optimum pH was 5.5 compared to 4.0 of the free enzyme. The half-life of the IMC was extended to 272 h compared to 0.77 h of the free enzyme.     

葡萄糖氧化酶的有机相共价固定化

将葡萄糖氧化酶(GOD)在最适pH条件下冻干后,以戊二醛活化的壳聚糖为载体,分别在传统水相和1,4-二氧六环、乙醚、乙醇三种不同的有机相中进行共价固定化。通过比较水相固定化酶和有机相固定化酶的酶比活力、酶学性质及酶动力学参数,考察酶在有机相中的刚性特质对酶在共价固定化过程中保持酶活力的影响。结果表明,戊二醛浓度为0.1%、加酶量为80 mg/1 g载体、含水1.6%的1,4-二氧六环有机相固定化GOD与水相共价固定化GOD相比,酶比活力提高2.9倍,有效酶活回收率提高3倍;在连续使用7次后,1,4-二氧六环有机相固定化GOD的酶活力仍为相应水相固定化酶的3倍。在酶动力学参数方面,不论是表观米氏常数,最大反应速度还是转换数,1,4-二氧六环有机相固定化的GOD(Kmapp=5.63 mmol/L,Vmax=1.70μmol/(min.mgGOD),Kcat=0.304 s-1)都优于水相共价固定化GOD(Kmapp=7.33 mmol/L,Vmax=1.02μmol/(min.mg GOD),Kcat=0.221 s-1)。因此,相比于传统水相,GOD在合适的有机相中进行共价固定化可以获得具有更高酶活力和更优催化性质的固定化酶。该发现可能为酶蛋白在共价固定化时因构象改变而丢失生物活性的问题提供解决途径。     

游离及固定化果糖基转移酶部分酶学性质的比较研究

 从诱变、筛选的米曲霉GX0 0 10菌株所产生的果糖基转移酶 ,经过纯化和固定化操作分别制备游离酶和固定化酶 ,对两者的酶学性质进行了比较研究 .结果表明 ,两者在蔗糖转化为蔗果低聚糖的酶促反应中 ,最适pH为 5 5,在pH5 0～ 7 5之间酶活性相对稳定 .游离酶和固定化酶的适宜温度范围分别是 4 5～ 52℃和 4 0～ 55℃ .在 55℃保温 60min ,酶活性保存率分别是 61 6%和 87 5% .固定化酶的热稳定性提高 .0 1mmol LHg2 +和 1mmol LAg+能完全抑制游离酶的活性 ,但只能部分抑制固定化酶的活性 ,1mmol L的Ti2 +能完全抑制两者的活性 .以蔗糖为底物时 ,游离酶的米氏常数Km=2 15mmol L ,而固定化酶Km =386mmol L .游离酶只能使用一次 ,固定化酶反复使用 54次后 ,剩余活力为 55 2 % .用 55% (W V)蔗糖溶液与固定化酶在pH5 0 ,4 6℃下作用 12h ,可获得61 5% (总低聚糖 总糖 )产物 ,其中蔗果五糖含量达到 7 2 % .     

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.