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BIOCATALYTIC APPROACH FOR THE PRODUCTION OF VALUE-ADDED COMPOUNDS AND COFACTOR REGENERATION USING THE MEMBRANE REACTOR

机译:使用膜反应器生产增值化合物和辅助因子再生的生物催化方法

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The possibilities of developing biobased products as well as viable and biorefinary applications havebeen expanding. S. cerevisiae may be used as a raw material for enzyme production. Using the latter biomassfeedstock, alcohol dehydrogenase (ADH) among other enzymes may be obtained. This work focused on thestereoselective reduction of ketones to form chiral alcohols using ADH, a NAD(H)-dependent oxidoreductase. Therequired coenzymes were regenerated during the catalysis. Evaluations were made in a discontinuous process: thekinetic constants for ADH in reference to acetophenone (K_M=1.04 mM and V_(MAX)= 1.47 U) and 2-hexanone(K_M=1.38 mM and V_(MAX)= 1.05×10~(-1) U); the effect of the temperature on the enzyme′s activity was also evaluatedwithin the range from 25°C up to 50°C. The continuous bioconversion consisted of either oxidative or reductivereaction under the following condition: phosphate buffer (10 mM; pH 7.0 or 6.0), 1-phenylethanol or 2-hexanol (10mM) and acetophenone or 2-hexanone (10 mM); β-NAD or β-NADH (1mM) and ADH (150 U). The reactor was fedcontinuously under a specific feeding rate of 2 mL.h~(-1). The average of the formation of 1-phenylethanol was 3.1 mMwhereas for 2-hexanol, it was 3.6 mM. ADH responded accordingly to a substrate-coupled procedure using themembrane reactor.
机译:开发生物基产品以及可行和生物精制应用的可能性 不断扩大。酿酒酵母可以用作酶生产的原料。使用后一种生物质 作为原料,可以得到除其他酶外的醇脱氢酶(ADH)。这项工作的重点是 使用NAD(H)依赖性氧化还原酶ADH立体选择性还原酮以形成手性醇。这 催化过程中再生了所需的辅酶。评估是在不连续的过程中进行的: 苯乙酮(K_M = 1.04 mM和V_(MAX)= 1.47 U)和2-己酮的ADH动力学常数 (K_M = 1.38mM和V_(MAX)= 1.05×10〜(-1)U);还评估了温度对酶活性的影响 温度范围为25°C至50°C。连续的生物转化包括氧化或还原 在以下条件下进行反应:磷酸盐缓冲液(10 mM; pH 7.0或6.0),1-苯乙醇或2-己醇(10 mM)和苯乙酮或2-己酮(10 mM); β-NAD或β-NADH(1mM)和ADH(150 U)。给反应器加料 在2 mL.h〜(-1)的特定进料速率下连续进行。 1-苯基乙醇的平均形成量为3.1 mM 而对于2-己醇,为3.6 mM。因此,ADH使用 膜反应器。

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