Biodiesel production from Jatropha oil using mesoporous molecular sieves supporting K2SiO3 as catalysts for transesterification

被引:49
作者
Wu, Haitang [1 ]
Zhang, Junhua [1 ]
Liu, Yanping [2 ]
Zheng, Jilu [1 ]
Wei, Qin [1 ]
机构
[1] Northwest A&F Univ, Coll Forestry, Yangling 712100, Peoples R China
[2] Northwest A&F Univ, Coll Sci, Yangling 712100, Peoples R China
关键词
Transesterification; Heterogeneous catalysis; Biodiesel; Solid base catalyst; Jatropha oil; HETEROGENEOUS BASE CATALYST; WASTE COOKING OIL; SOYBEAN OIL; SOLID CATALYST; SUNFLOWER OIL; OXIDE; OPTIMIZATION; SILICA; SBA-15; K2CO3;
D O I
10.1016/j.fuproc.2013.10.021
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A series of solid base catalysts based on potassium salts (K2CO3, K2SiO3 and KAc) supported on mesoporous silicas (SBA-15 and AISBA-15) were prepared by impregnation method and used to catalyze the transesterification of Jatropha oil with methanol. The prepared catalysts were characterized by several techniques such as X-ray diffraction (XRD), Brunauer-Emmet-Teller method (BET), transmission electron microscopy (TEM) and temperature-programmed desorption of CO2 (CO2-TPD). In addition, various parameters affecting catalytic activity and biodiesel yield were investigated. The results showed that Al element dopant in SBA-15 could protect the pore structure of supported catalyst. The basicity and catalytic activity of AISBA-15 silica were improved significantly after loading potassium compounds. The activity of K2SiO3 impregnated catalyst was superior to those of K2CO3 and KAc impregnated catalysts. A biodiesel yield of 95% was obtained (using the K2SiO3/AISBA-15 catalyst) with 30 wt.% of K2SiO3 loading on AISBA-15 support, methanol/Jatropha oil molar ratio 9, reaction temperature 60 degrees C, reaction time 150 min and catalyst/oil mass ratio 3%. Reuse of the catalyst indicated that the K2SiO3/AISBA-15 had steady catalytic activity compared with traditional KOH and K2CO3 catalysts. After being reused for 5 cycles, a modest decrease of its activity led to a reduction of about 6% in the biodiesel yield. This decrease of catalytic activity was mainly caused by the potassium leaching and the adsorption of organic deposits on the catalyst surface. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:114 / 120
页数:7
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