DocumentCode
3163012
Title
Simulation of the catalytic reactive distillation process for biodiesel production via transesterification
Author
Yang Xiao ; Haoyang Li ; Guomin Xiao ; Lijing Gao ; Xiaomei Pan
Author_Institution
Sch. of Chem. & Chem. Eng., Southeast Univ., Nanjing, China
Volume
1
fYear
2014
fDate
19-21 Aug. 2014
Firstpage
196
Lastpage
199
Abstract
In order to simulate catalytic reactive distillation process for biodiesel production via transesterification accurately, the Antoine parameters of biodiesel and NRTL binary interaction coefficients were regressed using Aspen Plus Data Regression function according to the data in literatures. Then vapor pressure of biodiesel under different temperature and phase equilibrium conditions could be described with these parameters. Catalytic reactive distillation process for biodiesel production via transesterification was simulated with Aspen Plus software successfully. Reaction and separation was integrated in one catalytic reactive distillation column. As a result, although methanol-to-oil ratio was only 4:1, high purity (99.8 wt %) of biodiesel with high yield (99.7%) was obtained. The catalytic reactive distillation process for biodiesel production via transesterification would be adequately good to have a potential industrial relevance.
Keywords
bioenergy conversion; catalysis; distillation; Antoine parameters; Aspen Plus data regression function; Aspen Plus software; NRTL binary interaction coefficients; biodiesel production; catalytic reactive distillation process; transesterification; Biofuels; Biological system modeling; Distillation equipment; Methanol; Production; Software; Solids; Aspen Plus; Biodiesel Production; Catalytic Reactive Distillation Process; Simulation; Transesterification;
fLanguage
English
Publisher
ieee
Conference_Titel
Materials for Renewable Energy and Environment (ICMREE), 2013 International Conference on
Conference_Location
Chengdu
Print_ISBN
978-1-4799-3335-8
Type
conf
DOI
10.1109/ICMREE.2013.6893646
Filename
6893646
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