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液体酶催化生物柴油生产中关键参数的识别

Identification of critical parameters in liquid enzyme-catalyzed biodiesel production.

作者信息

Nordblad Mathias, Silva Vanessa T L, Nielsen Per Munk, Woodley John M

机构信息

Department of Chemical and Biochemical Engineering, Technical University of Denmark, DK-2800, Kgs. Lyngby, Denmark.

出版信息

Biotechnol Bioeng. 2014 Dec;111(12):2446-53. doi: 10.1002/bit.25305. Epub 2014 Aug 5.

Abstract

Callera™ Trans L, a liquid formulation of Thermomyces lanuginosus lipase, has recently shown great promise as a cost-efficient catalyst for methanolysis of triglyceride substrates, specifically in the BioFAME process. However, identifying the right combination of temperature and concentrations of catalyst, water and methanol to realize the full potential of the reaction system has remained a challenge. This study presents an investigation of the impact of temperature, enzyme and water concentration on the reaction, as well as the effect of methanol feed rate for the conversion of rapeseed oil in a fed-batch reaction system. It was observed that the reaction can be divided into two distinct parts. The first part of the reaction, during which primarily tri- and diglycerides are converted, proceeded at a high rate and thus required a high rate of methanol supply. The second part of the reaction, where the remaining di- and monoglycerides are converted, proceeded at a much lower rate. Consequently, it is necessary to reduce the methanol feed rate during the latter part of the reaction to avoid inhibition or even inactivation of the enzyme. Since the second part of the reaction occupied most of the 24-h reaction time, it was concluded that this is the part of the process where further development efforts should be targeted. This point was demonstrated by partially substituting the catalyst with a lipase with a different specificity, which enhanced the performance during the second phase of the reaction.

摘要

Callera™ Trans L是一种嗜热栖热菌脂肪酶的液体制剂,最近作为甘油三酯底物甲醇解的经济高效催化剂显示出巨大潜力,特别是在生物脂肪酸甲酯(BioFAME)工艺中。然而,确定温度与催化剂、水和甲醇浓度的正确组合以充分发挥反应系统的潜力仍然是一个挑战。本研究考察了温度、酶和水浓度对反应的影响,以及在补料分批反应系统中甲醇进料速率对菜籽油转化的影响。观察到该反应可分为两个不同的部分。反应的第一部分主要是甘油三酯和甘油二酯的转化,进行速度很快,因此需要高甲醇供应速率。反应的第二部分是剩余甘油二酯和甘油单酯的转化,进行速度要低得多。因此,有必要在反应后期降低甲醇进料速率,以避免酶的抑制甚至失活。由于反应的第二部分占了24小时反应时间的大部分,因此得出结论,这是该工艺中应进一步开展研发工作的部分。用具有不同特异性的脂肪酶部分替代催化剂证明了这一点,这提高了反应第二阶段的性能。

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