Kinetics of palm oil transesterification in a batch reactor |
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Authors: | D Darnoko Munir Cheryan |
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Affiliation: | (1) Present address: Indonesian Oil Palm Research Institute, Jl. Brigjen Katamso 51, 20001 Medan, Indonesia;(2) Department of Food Science and Human Nutrition, Agricultural Bioprocess Laboratory, University of Illinois, 1302 W. Pennsylvania Ave., 61801 Urbana, IL |
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Abstract: | Methyl esters were produced by transesterification of palm oil with methanol in the presence of a catalyst (KOH). The rate
of transesterification in a batch reactor increased with temperature up to 60°C. Higher temperatures did not reduce the time
to reach maximal conversion. The conversion of triglycerides (TG), diglycerides (DG), and monoglycerides (MG) appeared to
be second order up to 30 min of reaction time. Reaction rate constants for TG, DG, and MG hydrolysis reactions were 0.018–0.191
(wt%·min)−1, and were higher at higher temperatures and higher for the MG reaction than for TG hydrolysis. Activation energies were 14.7,
14.2, and 6.4 kcal/mol for the TG, DG, and MG hydrolysis reactions, respectively. The optimal catalyst concentration was 1%
KOH. |
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Keywords: | Biodiesel kinetics methyl esters palm oil transesterification |
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