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MEMBRANE IMMOBILIZED GLUCOSE ISOMERASE.

机译:膜固定化葡萄糖异构酶。

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High molecular weight copolymers of acrylonitrile with m-aminostyrene, p-aminostyrene of 4-vinylpyridine were synthesized by slurry polymerization so as to contain about 5 mole percent of amine or pyridine monomer. The monomer content was determined by ultraviolet absorption and non-aqueous titration of the acid copolymer salt in dimethylformamide. Unsupported ultrafiltration membranes were cast with an average pore radius of 40 to 80 nm. (alpha)-Chymotrypsin (CT), glucose isomerase (GI) or lactate dehydrogenase were immobilized to the membranes after appropriate chemical activation. The most frequently used activation methods were: trichloro-s-triazine on the aryl amine membrane for the coupling of CT; diazotization of the aryl amine membrane for the coupling of GI. The weight loading for CT was 6 to 12 percent with 40 to 65 percent retention of enzymatic specific activity. A purified GI from Streptomyces albus was covalently immobilized with 10 percent weight loading and 50 to 70 percent retention of enzymatic specific activity. Activity of membrane-bound GI was assayed at 70(DEGREES)C in pH 6.8 maleate buffer containing 0.3 M glucose, 7 mM MgSO(,4), and 3 mM CoSO(,4). Fructose formation was determined via cysteine-carbazole assay. A GI reactor containing a single 47 mm diameter membrane disk was operated in a single pass flow mode at a flow rate of 0.5 ml/min and resulted in 10% conversion; up to 20% conversion was observed with higher flow rates. A Co('+2) concentration of 0.4 and 3.0 mM was necessary for optimal thermal stability of soluble and immobilized GI, respectively. The GI-membrane reactor had a half-life of about 150 hours. The K(,m) and the V(,max) for the immobilized GI were 0.25 M and 15 (mu)mole/min-mg, respectively; these are slightly lower than and comparable to, respectively, those for soluble GI. When the flow rate was increased, a maximum level of activity was observed, at which diffusion control of the rate of reaction no longer existed. Diffusional limitations were shown to be insignificant at flow rates greater than or equal to 3 ml/min with a substrate concentration of 0.3 M glucose.
机译:通过淤浆聚合合成丙烯腈与4-乙烯基吡啶的间氨基苯乙烯,对氨基苯乙烯的高分子量共聚物,使其含有约5摩尔%的胺或吡啶单体。通过紫外线吸收和二甲基甲酰胺中的酸共聚物盐的非水滴定来确定单体含量。浇铸无孔超滤膜,平均孔径为40至80 nm。在适当的化学活化后,将α-胰凝乳蛋白酶(CT),葡萄糖异构酶(GI)或乳酸脱氢酶固定在膜上。最常用的活化方法是:芳基胺膜上的三氯-s-三嗪用于CT偶联;芳胺膜的重氮化,用于偶联GI。 CT的重量负荷为6%至12%,保留了40%至65%的酶比活性。将来自白色链霉菌(Streptomyces albus)的纯化GI共价固定,其负载量为10%,保留了酶比活性的50%至70%。在70(DEGREES)C在pH 6.8马来酸盐缓冲液中测定膜结合GI的活性,该缓冲液含有0.3 M葡萄糖,7 mM MgSO(,4)和3 mM CoSO(,4)。通过半胱氨酸-咔唑测定法确定果糖的形成。包含单个47 mm直径膜盘的GI反应器以单次通过模式以0.5 ml / min的流速运行,转化率为10%;在较高的流速下,观察到高达20%的转化率。分别需要0.4和3.0 mM的Co('+ 2)浓度才能分别实现可溶性和固定GI的最佳热稳定性。 GI膜反应器的半衰期约为150小时。固定的GI的K(,m)和V(,max)分别为0.25 M和15μmol/ min-mg;它们分别比可溶性GI的那些低一些并与之相当。当流速增加时,观察到最大的活性水平,在该水平上反应速率的扩散控制不再存在。在底物浓度为0.3 M的葡萄糖下,流速大于或等于3 ml / min时,扩散限制显示为微不足道。

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