KINETIC MODEL OF ALGAL BIODIESEL PRODUCTION UNDER SUPERCRITICAL METHANOLYSIS

A model for the supercritical trans-esterification reaction of algae is developed to study the effect of the operating parameters on the process kinetics. A well-mixed batch reactor equation was used to express the lab scale reactor. The model is based on experimental data described in a previous st...

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Veröffentlicht in:ARPN journal of engineering and applied sciences 2015-01, Vol.10 (1), p.274-278
Hauptverfasser: Amin, Ashraf, Aboel-Enin, S A, Diwani, G El, Hawash, S
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Sprache:eng
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