Technical and Economic Analysis of Conventional and Supercritical Transesterification for Biofuel Production

被引：16
作者：
Nguyen, Dinh Duc [1 ]
Habibi, Ali [2 ]
Ghadami, Azam [2 ]
Pirouzfar, Vahid [2 ]
Su, Chia-Hung [3 ]
机构：
[1] Duy Tan Univ, Inst Res & Dev, Da Nang 550000, Vietnam
[2] Islamic Azad Univ, Cent Tehran Branch, Dept Chem Engn, Tehran, Iran
[3] Ming Chi Univ Technol, Dept Chem Engn, New Taipei, Taiwan
来源：
CHEMICAL ENGINEERING & TECHNOLOGY | 2020年 / 43卷 / 10期
关键词：
Biodiesel; Biofuel production; Supercritical transesterification; BIODIESEL PRODUCTION; CASTOR-OIL; PALM OIL; OPTIMIZATION; WASTE;
D O I：
10.1002/ceat.202000058
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
The transesterification process with potassium hydroxide (KOH) catalyst and the methanol supercritical process were evaluated by Aspen HYSYS software. Castor oil and methanol were used as feed and alcohol. In order to accomplish verification, the simulation results were compared to a laboratory research. For economic analysis, these results were transferred to Aspen Economic Analyzer software. Piping and process equipment cost were calculated for the two processes. Additionally, direct and indirect costs of these processes were estimated.
引用
收藏
页码：1922 / 1929
页数：8
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