Effect of several factors on soluble lipase-mediated biodiesel preparation in the biphasic aqueous-oil systems

被引:40
作者
Chen, Xin [1 ]
Du, Wei [1 ]
Liu, Dehua [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
soluble lipase; oleic acid; esterification; biodiesel;
D O I
10.1007/s11274-008-9714-6
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Biodiesel is increasingly perceived as an important component of solutions to the important current issues of fossil fuel shortages and environmental pollution. Utilization of soluble lipase offers an alternative approach to lipase-catalyzed biodiesel production using immobilized enzyme or whole-cell catalysis. Soluble lipase NS81020, produced by submerged fermentation of genetically modified Aspergillus oryzae microorganism, was first proposed here as the catalyst of biodiesel preparation with oleic acid in the biphasic aqueous-oil systems. The effect factors such as enzyme concentration, water content, temperature, molar ratio of methanol to oil, stirring rate and pH of buffer solution on the esterification rate were investigated systematically. The reaction time could be shortened with the increasing of enzyme concentration as long as the maximum enzyme absorptive capacity on the interface in the biphasic aqueous-oil systems was not achieved. The optimal water content in the biphasic aqueous-oil systems was 10 wt% by oleic acid weight. The reaction rate was enhanced with the increasing molar ratio of methanol to oil, the increasing stirring rate or the decreasing temperature. Although soluble lipase NS81020 had lower activity at pH 10.55, hydroxyl ion conduced to restrain hydrolysis of methyl ester and facilitated the reaction toward the methyl ester formation.
引用
收藏
页码:2097 / 2102
页数:6
相关论文
共 26 条
[1]   Proposed kinetic mechanism of the production of biodiesel from palm oil using lipase [J].
Al-Zuhair, Sulaiman ;
Ling, Fan Wei ;
Jun, Lim Song .
PROCESS BIOCHEMISTRY, 2007, 42 (06) :951-960
[2]   A numerical investigation into the anomalous slight NOx increase when burning biodiesel; A new (old) theory [J].
Ban-Weiss, George A. ;
Chen, J. Y. ;
Buchholz, Bruce A. ;
Dibble, Robert W. .
FUEL PROCESSING TECHNOLOGY, 2007, 88 (07) :659-667
[3]  
CAO SG, 2002, PHARM BIOTECHNOL, V9, P281
[4]  
DING F, 2004, CHEM IND ENG, V21, P361
[5]   Continuous enzymatic transesterification of high oleic sunflower oil in a packed bed reactor: influence of the glycerol production [J].
Dossat, V ;
Combes, D ;
Marty, A .
ENZYME AND MICROBIAL TECHNOLOGY, 1999, 25 (3-5) :194-200
[6]   Study on acyl migration in immobilized lipozyme TL-catalyzed transesterification of soybean oil for biodiesel production [J].
Du, W ;
Xu, YY ;
Liu, DH ;
Li, ZB .
JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2005, 37 (1-6) :68-71
[7]   Comparative study on lipase-catalyzed transformation of soybean oil for biodiesel production with different acyl acceptors [J].
Du, W ;
Xu, YY ;
Liu, DH ;
Zeng, J .
JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2004, 30 (3-4) :125-129
[9]   Production of biodiesel fuel from triglycerides and alcohol using immobilized lipase [J].
Iso, M ;
Chen, BX ;
Eguchi, M ;
Kudo, T ;
Shrestha, S .
JOURNAL OF MOLECULAR CATALYSIS B-ENZYMATIC, 2001, 16 (01) :53-58
[10]   Biodiesel fuel production from plant oil catalyzed by Rhizopus oryzae lipase in a water-containing system without an organic solvent [J].
Kaieda, M ;
Samukawa, T ;
Matsumoto, T ;
Ban, K ;
Kondo, A ;
Shimada, Y ;
Noda, H ;
Nomoto, F ;
Ohtsuka, K ;
Izumoto, E ;
Fukuda, H .
JOURNAL OF BIOSCIENCE AND BIOENGINEERING, 1999, 88 (06) :627-631