化工进展2012，Vol.31Issue(5)：1165-1168,1172,5.
基于双塔精馏的甲醇-碳酸二甲酯分离工艺
Separation technology for methanol-dimethyl carbonate system by double column distillation
杨德明 1王杨 1廖巧 1张雪杰1
作者信息
- 1. 常州大学石油化工学院,江苏常州213164
- 折叠
摘要
Abstract
Two kinds of double-column distillation process, double effect heat integration distillation and separate heat pump distillation, for separation of methanol-dimethyl carbonate system were simulated based on the methanol-dimethyl carbonate system azeotropic character. The binary interaction parameters of Wilson equation were fitted against the reported experimental data of methanol-dimethyl carbonate system. Based on the minimum annual total cost, simulations for the two kinds of double-column distillation process were performed by Aspen Plus software to achieve the optimal condition. The simulation results showed that the two kinds of double-column distillation need lower energy consumption and less annual total fee. Compared with double effect heat integration distillation, separate heat pump distillation can save total capital fee by 2.69% and annual total fee by 17.33%.关键词
甲醇-碳酸二甲酯/双效热集成精馏/分割式热泵精馏/年运行总费用Key words
methanol-dimethyl carbonate/double effect heat integration distillation/separate heatpump distillation/annual total fee分类
化学化工引用本文复制引用
杨德明,王杨,廖巧,张雪杰..基于双塔精馏的甲醇-碳酸二甲酯分离工艺[J].化工进展,2012,31(5):1165-1168,1172,5.
