Energy Optimization for a Multistage Crude Oil Distillation Process

被引:31
|
作者
Gu, Wugen [1 ]
Wang, Kan [1 ]
Huang, Yuqing [1 ]
Zhang, Bingjian [1 ]
Chen, Qinglin [1 ]
Hui, Chi-Wai [2 ]
机构
[1] Sun Yat Sen Univ, Sch Chem & Chem Engn, Key Lab Low Carbon Chem & Energy Conservat Guangd, Guangzhou 510275, Guangdong, Peoples R China
[2] Hong Kong Univ Sci & Technol, Chem & Biomol Engn Dept, Hong Kong, Hong Kong, Peoples R China
基金
中国国家自然科学基金;
关键词
Crude oil distillation; Energy optimization; Exergy analysis; Mathematical model; DESIGN OPTIMIZATION; FRACTIONATION UNITS; PART I;
D O I
10.1002/ceat.201400130
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Energy optimization is a hot research topic for design and operation of crude oil distillation plants. Optimum energy utilization in a multistage crude oil distillation process is achieved by optimizing the distillation load of each distillation column as well as the yield of the sidestreams of distillation columns. A generalized multistage distillation energy consumption model is proposed, and the optimal distillation load distribution is accomplished by minimizing the total energy consumption. Based on the optimal distillation loads, a nonlinear programming model is then formulated to determine the yields of sidestreams by maximizing the thermal exergy recovery for the crude oil plant. Finally, a four-stage crude oil distillation plant is investigated to demonstrate the performance of the proposed approach. The results show a decrease in energy consumption and an increase in heat recovery.
引用
收藏
页码:1243 / 1253
页数:11
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