Optimization study of binary metal oxides catalyzed transesterification system for biodiesel production

被引:34
作者
Lee, H. V. [1 ]
Taufiq-Yap, Y. H. [2 ]
机构
[1] Univ Malaya, Inst Postgrad Studies, Nanotechnol & Catalysis Res Ctr NanoCat, Kuala Lumpur 50603, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Ctr Excellence Catalysis Sci & Technol, Upm Serdang 43400, Selangor, Malaysia
关键词
Jatropha curcas oil; Response surface methodology; Catalyst; Optimization; Fuel properties; Transesterification; Mixed metal oxides; Statistical analysis; RESPONSE-SURFACE METHODOLOGY; OIL; SCIENCE;
D O I
10.1016/j.psep.2014.10.001
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The focus of this study is to produce biodiesel using non-edible feedstock (Jatropha curcas oil) via heterogeneous base catalyzed transesterification reaction. The solid base catalysts, binary metal oxide (CaO-ZnO and CaO-La2O3) were selected for the transesterification of high acid jatropha oil. Furthermore, the design of experiments was performed using 5-level-4 factor central composite design coupled with response surface methodology (RSM) in order to optimize the transesterification conditions. Four process factors were evaluated: (1) reaction time (1-5 h), (2) methanol/oil molar ratio (15:1-30:1), (3) reaction temperature (40-200 degrees C) and (4) catalyst loading (1-5 wt.%). Based on the quadratic model generated from RSM, reaction temperature rendered the most significant effect for both CaO-ZnO and CaO-La2O3 catalyzed reactions, followed by catalyst loading and reaction time. Besides, both reaction models showed that interaction between reaction temperature with reaction time and catalyst loading has positively influenced the biodiesel yield. The highest conversion predicted for CaO-ZnO and CaO-La2O3 catalyzed reactions was 97.03% and 96.27%, respectively, with reasonable predictability and sufficient accuracy data (small error: 0.33-0.34%). Furthermore, the physicochemical characteristics of produced biodiesel were tested with compliance to ASTM D7851 and EN 14124. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:430 / 440
页数:11
相关论文
共 35 条
[1]   Optimization of biodiesel production by alkali-catalyzed transesterification of used frying oil [J].
Atapour, Mehdi ;
Kariminia, Hamid-Reza ;
Moslehabadi, Parivash Moslehi .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2014, 92 (02) :179-185
[2]   Response surface methodology (RSM) as a tool for optimization in analytical chemistry [J].
Bezerra, Marcos Almeida ;
Santelli, Ricardo Erthal ;
Oliveira, Eliane Padua ;
Villar, Leonardo Silveira ;
Escaleira, Luciane Amlia .
TALANTA, 2008, 76 (05) :965-977
[3]   Biodiesel production using chemical and biological methods - A review of process, catalyst, acyl acceptor, source and process variables [J].
Bharathiraja, B. ;
Chakravarthy, M. ;
Kumar, R. Ranjith ;
Yuvaraj, D. ;
Jayamuthunagai, J. ;
Kumar, R. Praveen ;
Palani, S. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2014, 38 :368-382
[4]   Biodiesel production from various feedstocks and their effects on the fuel properties [J].
Canakci, M. ;
Sanli, H. .
JOURNAL OF INDUSTRIAL MICROBIOLOGY & BIOTECHNOLOGY, 2008, 35 (05) :431-441
[5]   Rice husk ash as a catalyst precursor for biodiesel production [J].
Chen, Kung-Tung ;
Wang, Jian-Xun ;
Dai, Yong-Ming ;
Wang, Po-Hsiang ;
Liou, Cyong-Ying ;
Nien, Chia-Wei ;
Wu, Jhong-Syuan ;
Chen, Chiing-Chang .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2013, 44 (04) :622-629
[6]   Process Optimization for Biodiesel Production from Waste Cooking Palm Oil (Elaeis guineensis) Using Response Surface Methodology [J].
Chin, L. H. ;
Hameed, B. H. ;
Ahmad, A. L. .
ENERGY & FUELS, 2009, 23 (1-2) :1040-1044
[7]   Chemicals from biomass: Synthesis of glycerol carbonate by transesterification and carbonylation with urea with hydrotalcite catalysts. The role of acid-base pairs [J].
Climent, Maria J. ;
Corma, Avelino ;
De Frutos, Pilar ;
Iborra, Sara ;
Noy, Maria ;
Velty, Alexandra ;
Concepcion, Patricia .
JOURNAL OF CATALYSIS, 2010, 269 (01) :140-149
[8]  
Diya'uddeen BH, 2012, PROCESS SAF ENVIRON, V90, P164, DOI [10.1016/j.psep.2012.02.005, 10.1016/j.psep.2012.04.002]
[9]  
Elsheikh Y. A., 2014, PROCESS SAF IN PRESS
[10]   Optimization of the transesterification reaction in biodiesel production [J].
Ferella, F. ;
Di Celso, G. Mazziotti ;
De Michelis, I. ;
Stanisci, V. ;
Veglio, F. .
FUEL, 2010, 89 (01) :36-42