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Received August 23, 2013
Accepted April 21, 2014
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Pork lard conversion to biodiesel using a microchannel reactor

Department of Chemical Engineering, Faculty of Engineering, Kasetsart University, Chatuchak, Bangkok 10900, Thailand 1Department of Agro-Industrial, Food and Envirnmental Technology, Faculty of Applied Science, King Mongkut’s University of Technology North Bangkok, Pracharat 1 Road, Wongsawang, Bangsue, Bangkok 10800, Thailand
fengasj@ku.ac.th
Korean Journal of Chemical Engineering, December 2014, 31(12), 2170-2176(7), 10.1007/s11814-014-0120-5
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Abstract

Biodiesel was synthesized from pork lard via transesterification using a microchannel reactor. To investigate the effects of operating parameters, including reaction temperature (55-65 ℃), residence time (5-20 s), methanol-to-oil molar ratio (4.5 : 1 to 9 : 1), and catalyst concentration (0.7-1.3 wt%), a series of full factorial experiments with a complete replicate were conducted. Results were statistically analyzed using MINITAB with the significance level of 0.05. A quadratic model was proposed for the prediction of %FAME from the specified operating conditions._x000D_ High %FAME was obtained at low residence time due to the small size of droplets in the microchannel reactor. Evidence of droplets supported the presence of mass transfer limitation in this system. The optimal operating conditions provided %FAME of 95.41% were as follows: methanol-to-oil ratio of 6 : 1, temperature of 65 ℃, residence time of 5 s, and KOH concentration of 1.3%w/w.

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