Accelerating transesterification reaction with biodiesel as co-solvent: A case study for solid acid sulfated tin oxide catalyst

被引:55
作者
Lam, Man Kee [1 ]
Lee, Keat Teong [1 ]
机构
[1] Univ Sains Malaysia, Sch Chem Engn, Nibong Tebal 14300, Pulau Pinang, Malaysia
关键词
Heterogeneous acid catalyst; Waste cooking oil; Free fatty acid; Biofuel; WASTE COOKING OIL; SOYBEAN OIL; SEED OIL; BASE; FUEL;
D O I
10.1016/j.fuel.2010.07.005
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Solid acid catalysts are normally used to catalyze the transesterification of oil with high free fatty acid (FFA) to biodiesel. However, the immiscible phases of methanol-oil-catalyst in the initial reaction mixture usually lead to slow reaction rate and long reaction time. One possible way to overcome this limitation is by using co-solvent that has high solubility in oil and methanol. Therefore, in the present study, the use of biodiesel as co-solvent for transesterification reaction catalyzed by SO(4)(2-)/SnO(2)-SiO(2) (solid acid catalyst) was investigated. It was found that with the use of biodiesel as co-solvent, a high FAME yield of 88.2% (almost 30% higher than without using co-solvent) can be obtained in a shorter reaction time (1.5 h) using the following reaction conditions; reaction temperature of 150 degrees C, methanol to oil ratio of 15 and catalyst loading of 6 wt.% (weight of oil). (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3866 / 3870
页数:5
相关论文
共 31 条
[1]   Parametric sensitivity in transesterification of waste cooking oil for biodiesel production-A review [J].
Banerjee, A. ;
Chakraborty, R. .
RESOURCES CONSERVATION AND RECYCLING, 2009, 53 (09) :490-497
[2]   Review: examining the use of different feedstock for the production of biodiesel [J].
Behzadi, S. ;
Farid, M. M. .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2007, 2 (05) :480-486
[3]  
Canakci M, 2003, T ASAE, V46, P945
[4]   Biodiesel from Low-Grade Animal Fat: Production Process Assessment and Biodiesel Properties Characterization [J].
Canoira, Laureano ;
Rodriguez-Gamero, Miguel ;
Querol, Enrique ;
Alcantara, Ramon ;
Lapuerta, Magin ;
Oliva, Fermin .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (21) :7997-8004
[5]   Transesterification reaction of vegetable oils, using superacid sulfated TiO2-base catalysts [J].
de Almeida, Rusiene M. ;
Noda, Lucia K. ;
Goncalves, Norberto S. ;
Meneghetti, Simoni M. P. ;
Meneghetti, Mario R. .
APPLIED CATALYSIS A-GENERAL, 2008, 347 (01) :100-105
[6]   Progress and recent trends in biodiesel fuels [J].
Demirbas, Ayhan .
ENERGY CONVERSION AND MANAGEMENT, 2009, 50 (01) :14-34
[7]   Synthesis of sulfated silica-doped tin oxides and their high activities in transesterification [J].
Du, Yunchen ;
Liu, Sen ;
Ji, Yanyan ;
Zhang, Yonglai ;
Wei, Shu ;
Liu, Fujian ;
Xiao, Feng-Shou .
CATALYSIS LETTERS, 2008, 124 (1-2) :133-138
[8]   Technical aspects of production and analysis of biodiesel from used cooking oil-A review [J].
Enweremadu, C. C. ;
Mbarawa, M. M. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2009, 13 (09) :2205-2224
[9]   Monoglyceride synthesis by glycerolysis of methyl oleate on solid acid-base catalysts [J].
Ferretti, Cristian A. ;
Soldano, Agostina ;
Apesteguia, Carlos R. ;
Isabel Di Cosimo, J. .
CHEMICAL ENGINEERING JOURNAL, 2010, 161 (03) :346-354
[10]   Biodiesel fuel production with solid superacid catalysis in fixed bed reactor under atmospheric pressure [J].
Furuta, S ;
Matsuhashi, H ;
Arata, K .
CATALYSIS COMMUNICATIONS, 2004, 5 (12) :721-723