Transesterification of soybean oil using a novel heterogeneous base catalyst: Synthesis and characterization of Na-pumice catalyst, optimization of transesterification conditions, studies on reaction kinetics and catalyst reusability

被引:22
作者
de Luna, Mark Daniel G. [1 ,2 ]
Cuasay, Jodel L. [2 ]
Tolosa, Nolan C. [3 ]
Chung, Tsair-Wang [4 ]
机构
[1] Univ Philippines Diliman, Dept Chem Engn, Quezon City 1101, Philippines
[2] Univ Philippines Diliman, Natl Grad Sch Engn, Energy Engn Program, Quezon City 1101, Philippines
[3] Malayan Coll Laguna, Off Res Promot & Coordinat, Cabuyao 4025, Laguna, Philippines
[4] Chung Yuan Christian Univ, Dept Chem Engn, Taoyuan 32023, Taiwan
关键词
Biodiesel; Catalyst regeneration; Catalyst synthesis; Kinetics; Optimization; Transesterification; RESPONSE-SURFACE METHODOLOGY; JATROPHA-CURCAS OIL; BIODIESEL PRODUCTION; SODIUM-SILICATE; FRYING OIL; PALM OIL; CAO; OPPORTUNITIES; SUPPORT; FUEL;
D O I
10.1016/j.fuel.2017.07.086
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
The transesterification of soybean oil using sodium-loaded pumice (Na-pumice) catalyst synthesized through wet impregnation was investigated in this study. X-ray diffraction (XRD) spectroscopy, scanning electron microscopy with energy dispersive X-ray (SEM-EDX) spectroscopy, and Brunauer-Emmett-Teller (BET) surface analysis were used to characterize the prepared Na-pumice catalysts. Response surface methodology (RSM) based on the three-factor, three-level Box-Behnken Design was employed to optimize the transesterification reaction at constant temperature of 60 degrees C. The process variables were reaction time, methanol-to-oil molar ratio, and catalyst dosage while the fatty acid methyl ester (FAME) yield was the main response variable. The optimum reaction conditions were X-1 (reaction time, h) = 2.75, X-2 (amount of catalyst, wt%) = 12.86, and X-3 (methanol/oil molar ratio) = 24: 1, with an actual FAME yield of> 99%. The kinetics of the transesterification process and the reusability of the catalyst were also investigated. Results showed that reaction kinetics at optimum conditions conformed to the pseudo-first order model with coefficient of determination and k values of 0.9862 and 0.0277 min(-1), respectively. More importantly, the washed catalyst maintained> 99% methyl ester yield even after three successive usage.
引用
收藏
页码:246 / 253
页数:8
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