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固定化酶催化桐油酯交换反应的研究 被引量:12

A Study on Immobilized Lipase Catalyzed Transesterification Reaction of Tung Oil
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摘要 【目的】本文以桐油为原料,研究固定化脂肪酶催化桐油与甲醇酯交换反应的工艺条件。【方法】Novo435脂肪酶为催化剂,在无有机溶剂存在的情况下,利用响应面研究方法,对桐油酯交换反应的工艺条件进行研究和优化。【结果】得到了桐油酯交换反应的最佳工艺条件:醇油比2.2﹕1、温度43℃、脂肪酶用量14%(与油脂的质量比)、搅拌转速200 r/min,反应18 h后,桐油的酯交换率达到了67.5%(理论为73.3%)。脂肪酶经有机溶剂洗涤后连续使用120 h,桐油酯交换率减小了6%。理论甲醇量不能一次加入,分两批加入,共反应36 h后,桐油的酯交换率达到85%(理论为100%)。【结论】影响桐油酯交换反应的显著因素为醇油比、脂肪酶用量、反应温度和反应时间,各因素间有一定的交互作用。 [Objective] The transesterification reaction conditions of tung oil with methanol with immobilized lipase as catalyst was studied. [Method] Novo435 lipase was the catalyst, and a response surface methodology was used to optimize the transesterification reaction of tung oil in the non-solvent system. [Result] The optimized reaction condition was found: rotation rate was 200 r/min, the molar ratio of methanol to oil was 2.2:1, reaction temperature was 43℃, the catalyst was 14% (based on the weight of oil), and after reacting for 18 h, 67.5% of the oil was converted to its corresponding methyl esters (the academic conversion is 73.3%). The lipase was washed by organic solvents after each reaction and reused again, the esters conversion of tung oil was decreased by 6% after the lipase being reused for 120 h. The theoretical amount of methanol was added by two steps, 85% conversion was obtained after 36 h of reaction (theoretical conversion is 100%). [Conclusion]The molar ratio of methanol to oil, the catalyst amount, the reaction temperature and reaction time were all highly significant factors, and there was a relative significant interaction between every two factors.
出处 《中国农业科学》 CAS CSCD 北大核心 2006年第10期2089-2094,共6页 Scientia Agricultura Sinica
基金 河南省杰出人才创新基金项目资助(032001300)
关键词 无溶剂 酯交换 生物柴油 脂肪酶 桐油 Non-solvent Transesterification Biodiesel Lipase Tung oil
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参考文献12

  • 1闵恩泽,唐忠,杜泽学,吴巍.发展我国生物柴油产业的探讨[J].中国工程科学,2005,7(4):1-4. 被引量:88
  • 2冀星,郗小林,孔林河,李俊峰,李丽.生物柴油技术进展与产业前景[J].中国工程科学,2002,4(9):86-93. 被引量:94
  • 3隆金桥.桐油改性的研究[J].广西民族学院学报(自然科学版),2000,6(1):27-29. 被引量:4
  • 4Demirbas A.Biodesel fuels from vegetable oils via catalytic and non-catalytic supercritical alcohol transesterifications and other methods:a survey.Energy Conversion and Management,2003,44:2093-2109.
  • 5Watanabe Y,Shimada Y,Sugthara A,Tominaga Y.Conversion of degummed soybean oil to biodiesel fuel with immobilized Candida antarctica lipase.Journal of Molecular Catalysis B:Enzymatic,2002,17:151-155.
  • 6Shieh C J,Liao H F,Lee C C.Optimization of lipase-catalyzed biodiesel byresponse surface methodogy.Bioresource Technology,2003,88:103-106.
  • 7Du W,Xu Y Y,Liu D H,Zeng J.Comparative study on lipase-catalyzed transformation of soybean oil for biodiesel production with different acyl acceptors.Journal of Molecular Catalysis B:Enzymatic,2004,30:125-129.
  • 8Soumanou M M,Bornscheuer U T.Improvement in lipase-catalyzed synthesis of fatty acid methyl esters from sunflower oil.Enzyme and Microbial Technology,2003,33:97-103.
  • 9Xu Y Y,Du W,Liu D H,Zeng J.A novel enzymatic route for biodiesel production from renewable oils in a solvent-free medium.Biotechnology Letters,2003,25:1239-1241.
  • 10邓利,谭天伟,王芳.脂肪酶催化合成生物柴油的研究[J].生物工程学报,2003,19(1):97-101. 被引量:191

二级参考文献38

  • 1范航,张大年.生物柴油试制研究[J].化学世界,2000,41(S1):65-66. 被引量:21
  • 2中国油脂植物编写委员会.中国油脂植物[M].北京:科学出版社,1987.193-196.
  • 3Soumanou M M, Bornscheuer U T. Enzyme Microb Technol, 2003, 33(1): 97
  • 4Nelson L A, Foglia T A, Marmer W N. J Am Oil Chem Soc, 1996, 73(9): 1191
  • 5Fukuda H, Kondo A, Noda H. J Biosci Bioeng, 2001, 92(5): 405
  • 6K(o)se O, Tüter M, Aksoy H A. Bioresour Technol, 2002, 83(2): 125
  • 7Watanabe Y, Shimada Y, Sugihara A, Tominaga Y. J Am Oil Chem Soc, 2001, 78(7): 703
  • 8Shimada Y, Watanabe Y, Sugihara A, Tominaga Y. J Mol Catal B, 2002, 17(3-5): 133
  • 9Lara P V, Park E Y. Enzyme Microb Technol, 2004, 34(3-4): 270
  • 10Du W, Xu Y Y, Liu D H. Biotechnol Appl Biochem, 2003, 38(2): 103

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