甘孟瑜, 潘登, 马利, 等. The Kinetics of the Esterification of Free Fatty Acids in Waste Cooking Oil Using Fe2(SO4)3/C Catalyst[J]. 中国化学工程学报(英文版), 2009,17(1):83-87. DOI: 10.1016/S1004-9541(09)60037-9.
(SO
甘孟瑜, 潘登, 马利, 等. The Kinetics of the Esterification of Free Fatty Acids in Waste Cooking Oil Using Fe2(SO4)3/C Catalyst[J]. 中国化学工程学报(英文版), 2009,17(1):83-87. DOI: 10.1016/S1004-9541(09)60037-9.DOI:
The esterification of free fatty acids(FFA) in waste cooking oil with methanol in the presence of Fe
2
(SO
4
)
3
/C(ferric sulfate/active carbon) catalyst was studied.The effects of different temperature
methanol/FFA mole ratio and amount of catalyst on the conversion of FFA were investigated.The results demonstrated that under optimal esterification conditions the final acid value of the resultant system can be reduced to ~1(mg KOH)·g
-1
which met fu
lly the requirements in post-treatment for efficient separation of glycerin and biodiesel.The kinetics of the esterification were also investigated under different temperatures.The results indicated that the rate-control step could be attributed to the surface reaction and the esterification processes can be well-depicted by the as-calculated kinetic formula in the range of the experimental conditions.
Abstract
The esterification of free fatty acids(FFA) in waste cooking oil with methanol in the presence of Fe
2
(SO
4
)
3
/C(ferric sulfate/active carbon) catalyst was studied.The effects of different temperature
methanol/FFA mole ratio and amount of catalyst on the conversion of FFA were investigated.The results demonstrated that under optimal esterification conditions the final acid value of the resultant system can be reduced to ~1(mg KOH)·g
-1
which met fully the requirements in post-treatment for efficient separation of glycerin and biodiesel.The kinetics of the esterification were also investigated under different temperatures.The results indicated that the rate-control step could be attributed to the surface reaction and the esterification processes can be well-depicted by the as-calculated kinetic formula in the range of the experimental conditions.
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Complete kinetic model for esterification reaction of lauric acid with glycerol to synthesize glycerol monolaurate
Esterification of acetic acid with isobutanol catalyzed by ionic liquid n-sulfopropyl-3-methylpyridinium trifluoromethanesulfonate: Experimental and kinetic study
Liquid-phase esterification of methacrylic acid with methanol catalyzed by cation-exchange resin in a fixed bed reactor: Experimental and kinetic studies
Construction of a Brönsted-Lewis solid acid catalyst La-PW-SiO2/SWCNTs based on electron withdrawing effect of La(III) on π bond of SWCNTs for biodiesel synthesis from esterification of oleic acid and methanol
Polymeric ionic liquids (PILs) with high acid density: Tunable catalytic performance for biodiesel production
相关作者
Han-Qiao Hu
Yue Zhang
Ming Fan
Yong Cai
Guang-Wen Chu
Liang-Liang Zhang
Meng Shi
Kelei Huang
相关机构
Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology
Petrochemical Research Institute, China National Petroleum Corporation
State Key Laboratory of Organic-Inorganic Composites, Beijing University of Chemical Technology
Guangxi Key Laboratory of Petrochemical Resource Processing and Process Intensification Technology, School of Chemistry and Chemical Engineering, Guangxi University
School of Chemical Sciences, University of Chinese Academy of Sciences