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Enzymatic hollow fiber membrane bioreactor for penicilin hydrolysis

机译:用于青霉素水解的酶促中空纤维膜生物反应器

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Continuous enzymatic reaction has been proven as an efficient technique for several industrial applications. In this study, a type of hollow fiber membrane bioreactor where penicillin acylase entrapped within membrane pores was applied to continuously hydrolyze Penicillin G. The influences of various operating conditions on immobilization and enzymatic reaction processes were assessed. A mathematical model of the reactor behaviour at steady state condition was also developed. The immobilization results show that penicillin acylase was entrapped more than 90% (100,000 u.a m~(-2)). Due to the much smaller size of 6-APA compared to the membrane pore, the solute diffuses freely through the membrane. However, the immobilized enzyme membrane retained around 35% of the solute. In addition, K_m of immobilized penicillin acylase (8.04 mM) was slightly higher than that of free penicillin acylase (7.75 mM). The theoretical results indicated that convective transport was the main mechanism of mass transport even in the case where flux was very low. Low flux rate is important to avoid gel formation or enzyme release from membrane pores and to maximize the degree of conversion.
机译:连续的酶促反应已被证明是用于多种工业应用的有效技术。在这项研究中,一种中空纤维膜生物反应器(其中截留在膜孔中的青霉素酰基转移酶)被用于连续水解青霉素G。评估了各种操作条件对固定化和酶促反应过程的影响。还建立了稳态条件下反应堆行为的数学模型。固定化结果表明,青霉素酰化酶的截留率超过90%(100,000 u.a m〜(-2))。由于与膜孔相比,6-APA的尺寸要小得多,因此溶质可自由扩散通过膜。但是,固定的酶膜保留了约35%的溶质。此外,固定化青霉素酰基转移酶的K_m(8.04 mM)略高于游离青霉素酰基转移酶的K_m(7.75 mM)。理论结果表明,即使在通量很低的情况下,对流输运也是传质的主要机理。低通量速率对于避免凝胶形成或酶从膜孔中释放以及最大程度地提高转化率很重要。

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