Ca and Zn mixed oxide as a heterogeneous base catalyst for transesterification of palm kernel oil

被引:236
作者
Ngamcharussrivichai, Chawalit [1 ]
Totarat, Prangsinan [1 ]
Bunyakiat, Kunchana [1 ]
机构
[1] Chulalongkorn Univ, Fac Sci, Dept Chem Technol, Bangkok 10330, Thailand
关键词
biodiesel; transesterification; mixed metal oxide; heterogeneous catalyst;
D O I
10.1016/j.apcata.2008.02.020
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Transesterification of palm kernel oil with methanol over mixed oxides of Ca and Zn has been investigated batchwise at 60 degrees C and 1 atm. CaO center dot ZnO catalysts were prepared via a conventional co-precipitation of the corresponding mixed metal nitrate solution in the presence of a soluble carbonate salt at near neutral conditions. The catalysts were characterized by using techniques of X-ray diffraction (XRD), scanning electron microscope (SEM), and thermogravimetric analysis (TGA). The results indicated that the mixed oxides possess relatively small particle sizes and high surface areas, compared to pure CaO and ZnO. Moreover, the combination of Ca and Zn reduced the calcination temperature required for decomposition of metal carbonate precipitates to active oxides. Influences of Ca/Zn atomic ratio in the mixed oxide catalyst, catalyst amount, methanol/oil molar ratio, reaction time, and water amount on the methyl ester (ME) content were studied. Under the suitable transesterification conditions at 60 degrees C (catalyst amount = 10 wt.%, methanol/oil molar ratio = 30, reaction time = 1 h), the ME content of > 94% can be achieved over CaO center dot ZnO catalyst with the Ca/Zn ratio of 0.25. The mixed oxide can be also applied to transesterification of palm olein, soybean, and sunflower oils. Furthermore, the effects of different regeneration methods on the reusability of CaO center dot ZnO catalyst were investigated. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:77 / 85
页数:9
相关论文
共 36 条
[1]   Potassium leaching during triglyceride transesterification using K/γ-A12O3 catalysts [J].
Alonso, D. Martin ;
Mariscal, R. ;
Moreno-Tost, R. ;
Poves, M. D. Zafra ;
Granados, M. Lopez .
CATALYSIS COMMUNICATIONS, 2007, 8 (12) :2074-2080
[2]   New heterogeneous process for biodiesel production: A way to improve the quality and the value of the crude glycerin produced by biodiesel plants [J].
Bournay, L ;
Casanave, D ;
Delfort, B ;
Hillion, G ;
Chodorge, JA .
CATALYSIS TODAY, 2005, 106 (1-4) :190-192
[3]  
Boynton R.S., 1980, Chemistry and Technology of Lime and Limestone
[4]  
Contreras C, 2006, ADV TECHNOL MAT MAT, V8, P122, DOI [DOI 10.2240/AZ0J0M00220, 10.2240/azojomo0220]
[5]  
Costantino U, 1998, EUR J INORG CHEM, P1439
[6]  
Coteron A, 1997, RECENT RES DEV OIL C, V1, P109
[7]  
Cullity B., 1978, ELEMENTS XRAY DIFFRA
[8]   Biodiesel from sunflower oil in supercritical methanol with calcium oxide [J].
Demirbas, Ayhan .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (03) :937-941
[9]  
DUNN RO, 2001, J OLEO SCI, V50, P415, DOI DOI 10.5650/JOS.50.415
[10]   Selective transesterification of triolein with methanol to methyl oleate and glycerol using alumina loaded with alkali metal salt as a solid-base catalyst [J].
Ebiura, T ;
Echizen, T ;
Ishikawa, A ;
Murai, K ;
Baba, T .
APPLIED CATALYSIS A-GENERAL, 2005, 283 (1-2) :111-116