TY - JOUR
T1 - Transesterification kinetics of Camelina sativa oil on metal oxide catalysts under conventional and microwave heating conditions
AU - Patil, Prafulla
AU - Gude, Veera Gnaneswar
AU - Pinappu, Saireddy
AU - Deng, Shuguang
N1 - Funding Information: This project was partially supported by the New Mexico State University Office of Vice President for Research and the State of New Mexico through a New Mexico Technology Research Collaborative grant .
PY - 2011/4/15
Y1 - 2011/4/15
N2 - The reaction kinetics of transesterification of Camelina sativa oil using metal oxide catalysts under the conventional heating and the microwave-heating conditions were investigated. The transesterification reaction rates and the fatty acid methyl ester (FAME) conversion rates were determined using heterogeneous metal oxide catalysts, i.e., BaO, CaO, MgO and SrO and two different heating methods. It was observed during the kinetic studies in this work that the BaO and SrO catalysts generated higher FAME yields than the CaO and MgO catalysts. A comparison between the conventional heating and the microwave-assisted transesterification processes showed that the reaction rate constants obtained in the microwave-assisted transesterification process are of two orders of magnitude higher than those obtained with the conventional heating method. Therefore, it can be well concluded that the heating method and solid catalysts play vital roles in improving the reaction kinetics and optimizing the reactors for biomass conversion to biodiesel.
AB - The reaction kinetics of transesterification of Camelina sativa oil using metal oxide catalysts under the conventional heating and the microwave-heating conditions were investigated. The transesterification reaction rates and the fatty acid methyl ester (FAME) conversion rates were determined using heterogeneous metal oxide catalysts, i.e., BaO, CaO, MgO and SrO and two different heating methods. It was observed during the kinetic studies in this work that the BaO and SrO catalysts generated higher FAME yields than the CaO and MgO catalysts. A comparison between the conventional heating and the microwave-assisted transesterification processes showed that the reaction rate constants obtained in the microwave-assisted transesterification process are of two orders of magnitude higher than those obtained with the conventional heating method. Therefore, it can be well concluded that the heating method and solid catalysts play vital roles in improving the reaction kinetics and optimizing the reactors for biomass conversion to biodiesel.
KW - Biodiesel
KW - Camelina sativa oil
KW - Heterogeneous catalysts
KW - Microwave-heating
KW - Transesterification kinetics
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U2 - 10.1016/j.cej.2011.02.030
DO - 10.1016/j.cej.2011.02.030
M3 - Article
SN - 1385-8947
VL - 168
SP - 1296
EP - 1300
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
IS - 3
ER -