Suppr超能文献

用于乳糖酶促水解的超高温工艺的开发。IV. 两种耐热β-糖苷酶的固定化及用于乳糖转化的填充床反应器的优化。

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable beta-glycosidases and optimization of a packed-bed reactor for lactose conversion.

作者信息

Petzelbauer Inge, Kuhn Bernhard, Splechtna Barbara, Kulbe Klaus D, Nidetzky Bernd

机构信息

Division of Biochemical Engineering, Institute of Food Technology, Universität für Bodenkultur Wien (BOKU), Muthgasse 18, A-1190 Vienna, Austria.

出版信息

Biotechnol Bioeng. 2002 Mar 20;77(6):619-31. doi: 10.1002/bit.10110.

Abstract

Recombinant hyperthermostable beta-glycosidases from the archaea Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) were covalently attached onto the insoluble carriers chitosan, controlled pore glass (CPG), and Eupergit C. For each enzyme/carrier pair, the protein-binding capacity, the immobilization yield, the pH profiles for activity and stability, the activity/temperature profile, and the kinetic constants for lactose hydrolysis at 70 degrees C were determined. Eupergit C was best among the carriers in regard to retention of native-like activity and stability of Ss beta Gly and CelB over the pH range 3.0-7.5. Its protein binding capacity of approximately 0.003 (on a mass basis) was one-third times that of CPG, while immobilization yields were typically 80% in each case. Activation energies for lactose conversion by the immobilized enzymes at pH 5.5 were in the range 50-60 kJ/mol. This is compared to values of approximately 75 kJ/mol for the free enzymes. Immobilization expands the useful pH range for CelB and Ss beta Gly by approximately 1.5 pH units toward pH 3.5 and pH 4.5, respectively. A packed-bed enzyme reactor was developed for the continuous conversion of lactose in different media, including whey and milk, and operated over extended reaction times of up to 14 days. The productivities of the Eupergit C-immobilized enzyme reactor were determined at dilution rates between 1 and 12 h(-1), and using 45 and 170 g/L initial lactose. Results of kinetic modeling for the same reactor, assuming plug flow and steady state, suggest the presence of mass-transfer limitation of the reaction rate under the conditions used. Formation of galacto-oligosaccharides in the continuous packed-bed reactor and in the batch reactor using free enzyme was closely similar in regard to yield and individual saccharide components produced.

摘要

来自古菌嗜热栖热菌(SsβGly)和激烈热球菌(CelB)的重组超嗜热β-糖苷酶被共价连接到不溶性载体壳聚糖、可控孔径玻璃(CPG)和Eupergit C上。对于每一对酶/载体,测定了蛋白质结合能力、固定化产率、活性和稳定性的pH曲线、活性/温度曲线以及70℃下乳糖水解的动力学常数。就SsβGly和CelB在3.0 - 7.5的pH范围内保持类似天然的活性和稳定性而言,Eupergit C是载体中表现最佳的。其蛋白质结合能力约为0.003(以质量计),是CPG的三分之一,而每种情况下的固定化产率通常为80%。固定化酶在pH 5.5时乳糖转化的活化能在50 - 60 kJ/mol范围内。相比之下,游离酶的值约为75 kJ/mol。固定化分别使CelB和SsβGly的有用pH范围向pH 3.5和pH 4.5扩展了约1.5个pH单位。开发了一种填充床酶反应器,用于在包括乳清和牛奶在内的不同介质中连续转化乳糖,并在长达14天的延长反应时间内运行。测定了Eupergit C固定化酶反应器在1至12 h⁻¹的稀释率下以及使用45和170 g/L初始乳糖时的生产率。假设为活塞流和稳态,对同一反应器进行动力学建模的结果表明,在所使用的条件下反应速率存在传质限制。在连续填充床反应器和使用游离酶的间歇反应器中,低聚半乳糖的形成在产率和产生的单个糖类成分方面非常相似。

文献AI研究员

20分钟写一篇综述,助力文献阅读效率提升50倍。

立即体验

用中文搜PubMed

大模型驱动的PubMed中文搜索引擎

马上搜索

文档翻译

学术文献翻译模型,支持多种主流文档格式。

立即体验