Assessment of four biodiesel production processes using HYSYS. Plant

被引:289
|
作者
West, Alex H. [1 ]
Posarac, Dusko [1 ]
Ellis, Naoko [1 ]
机构
[1] Univ British Columbia, Dept Biol & Chem Engn, Vancouver, BC V6T 1Z3, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
biodiesel; process design; process simulation; economic assessment;
D O I
10.1016/j.biortech.2007.11.046
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Four continuous biodiesel processes were designed and simulated in HYSYS. The first two employed traditional homogeneous alkali and acid catalysts. The third and fourth processes used a heterogeneous acid catalyst and a supercritical method to convert a waste vegetable oil feedstock into biodiesel. While all four processes were capable of producing biodiesel at high purity, the heterogeneous and supercritical processes were the least complex and had tile smallest number of unit operations. Material and energy flows, as well as sized unit operation blocks, were used to conduct an economic assessment of each process. Total capital investment, total manufacturing cost and after tax rate-of-return were calculated for each process. The heterogeneous acid catalyst process had the lowest total capital investment and manufacturing costs, and had the only positive after tax rate-of-return. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6587 / 6601
页数:15
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