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Developing the reaction kinetics for a biodiesel reactor

Slinn, Matthew and Kendall, Kevin (2009) Developing the reaction kinetics for a biodiesel reactor. Bioresource Technology, 100 (7). pp. 2324-2327. ISSN 0960-8524

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URL of Published Version: http://dx.doi.org/10.1016/j.biortech.2008.08.044

Identification Number/DOI: 10.1016/j.biortech.2008.08.044

The aim of this paper was to investigate the kinetics of the biodiesel reaction in order to find out how best to reach 96.5% methyl ester. The purity of the biodiesel product was examined using gas chromatography to the EN14214 FAME standard and real-time optical microscopy was used to observe the reaction. The problem was the reaction doesn’t reach completion and the mechanism is not understood. It was observed that droplet size had a major influence on reaction end point and that the reaction was mass-transfer limited. This observation was confirmed by developing a mass-transfer based reaction model using the data from the batch reactor which agreed with results from other researchers. The model predicted better conversion with more mixing intensity. The results show that significant improvements could be made to the conventional FAME process.

Type of Work:Article
Date:April 2009 (Publication)
School/Faculty:Schools (1998 to 2008) > School of Engineering
Department:Department of Chemical Engineering
Keywords:Biodiesel, reactor, reaction, transesterification, theory
Subjects:TP Chemical technology
Institution:University of Birmingham
Copyright Holders:Elsevier B.V.
ID Code:798
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