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Simulation of biodiesel industrial production via solid base catalyst in a fixed-bed reactor
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作者 李浩扬 潘晓梅 +2 位作者 肖洋 肖国民 黄金金 《Journal of Southeast University(English Edition)》 EI CAS 2014年第3期380-386,共7页
Biodiesel industrial production based on a solid base catalyst in a fixed-bed was simulated. The lab and bench scale experiments were carded out effectively, in which the kinetic model is established and it can descri... Biodiesel industrial production based on a solid base catalyst in a fixed-bed was simulated. The lab and bench scale experiments were carded out effectively, in which the kinetic model is established and it can describe the transesterification reaction well. The Antoine equation of biodiesel is regressed with the vapor-liquid data cited of literature. The non-random two liquid (NRTL) model is applied to describe the system of fatty acid methyl ester (FAME), methanol and glycerol and parameters are obtained. The Ternary phase map is obtained from Aspen Plus via the liquid-liquid equilibrium (LLE) data. In order to describe the production in a fixed-bed performs in industrial scale after being magnified 1 000 times, the Aspen Plus simulation is employed, where two flowsheets are simulated to predict material and energy consumption. The simulation results prove that at least 350. 42 kW energy consumption can be reduced per hour to produce per ton biodiesel compared with data reported in previous references. 展开更多
关键词 solid base catalyst fixed-bed reactor aspen plus simulation biodiesel industrial production
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