Biodiesel production from Jatropha curcas Oil

被引:125
作者
Jain, Siddharth [1 ]
Sharma, M. P. [1 ]
机构
[1] Indian Inst Technol Roorkee, Alternate Hydro Energy Ctr, Roorkee 247667, Uttarakhand, India
关键词
Jatropha curcas oil (JCO) kinetics; Transesterification; Methyl ester (ME); Fatty acid methyl ester (FAME); WASTE COOKING OIL; METHYL-ESTERS; RAPESEED OIL; FUEL PRODUCTION; VEGETABLE-OILS; TRANSESTERIFICATION; OPTIMIZATION; KINETICS; ACID; TRIGLYCERIDES;
D O I
10.1016/j.rser.2010.07.047
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In view of the fast depletion of fossil fuel, the search for alternative fuels has become inevitable, looking at huge demand of diesel for transportation sector, captive power generation and agricultural sector, the biodiesel is being viewed a substitute of diesel. The vegetable oils, fats, grease are the source of feedstocks for the production of biodiesel. Significant work has been reported on the kinetics of transesterification of edible vegetable oils but little work is reported on non-edible oils. Out of various non-edible oil resources, Jatropha curcas oil (JCO) is considered as future feedstocks for biodiesel production in India and limited work is reported on the kinetics of transesterification of high FFA containing oil. The present study reports a review of kinetics of biodiesel production. The paper also reveals the results of kinetics study of two-step acid-base catalyzed transesterification process carried out at pre-determined optimum temperature of 65 and 50 degrees C for esterification and transesterification process, respectively, under the optimum condition of methanol to oil ratio of 3:7 (v/v), catalyst concentration 1% (w/w) for H2SO4 and NaOH and 400 rpm of stirring. The yield of methyl ester (ME) has been used to study the effect of different parameters. The maximum yield of 21.2% of ME during esterification and 90.1% from transesterification of pretreated JCO has been obtained. This is the first study of its kind dealing with simplified kinetics of two-step acid-base catalyzed transesterification process carried at optimum temperature of both the steps which took about 6 h for complete conversion of TG to ME. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3140 / 3147
页数:8
相关论文
共 69 条
[1]   A LOW-WASTE PROCESS FOR THE PRODUCTION OF BIODIESEL [J].
AHN, E ;
KONCAR, M ;
MITTELBACH, M ;
MARR, R .
SEPARATION SCIENCE AND TECHNOLOGY, 1995, 30 (7-9) :2021-2033
[2]   Experimental evaluation of the transesterification of waste palm oil into biodiesel [J].
Al-Widyan, MI ;
Al-Shyoukh, AO .
BIORESOURCE TECHNOLOGY, 2002, 85 (03) :253-256
[3]  
[Anonymous], 2003, 14103 DIN EN
[4]   Optimisation of biodiesel production by sunflower oil transesterification [J].
Antolín, G ;
Tinaut, FV ;
Briceño, Y ;
Castaño, V ;
Pérez, C ;
Ramírez, AI .
BIORESOURCE TECHNOLOGY, 2002, 83 (02) :111-114
[5]   Acid-catalyzed homogeneous esterification reaction for biodiesel production from palm fatty acids [J].
Aranda, Donato A. G. ;
Santos, Rafael T. P. ;
Tapanes, Neyda C. O. ;
Ramos, Andre Luis Dantas ;
Antunes, Octavio Auqusto C. .
CATALYSIS LETTERS, 2008, 122 (1-2) :20-25
[6]   Theoretical study of the transesterification of triglycerides to biodiesel fuel [J].
Asakuma, Yusuke ;
Maeda, Kouji ;
Kuramochi, Hidetoshi ;
Fukui, Keisuke .
FUEL, 2009, 88 (05) :786-791
[7]   Prospects of biodiesel production from vegetables oils in India [J].
Barnwal, BK ;
Sharma, MP .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2005, 9 (04) :363-378
[8]  
Bhatnagar AK, 2003, ALL IND SEM NAT POL
[9]  
Boocock DGB, 1998, J AM OIL CHEM SOC, V75, P1167, DOI 10.1007/s11746-998-0130-8
[10]   Fast one-phase oil-rich processes for the preparation of vegetable oil methyl esters [J].
Boocock, DGB ;
Konar, SK ;
Mao, V ;
Sidi, H .
BIOMASS & BIOENERGY, 1996, 11 (01) :43-50