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精馏过程多工况优化设计的能量流结构理论
引用本文:尹清华,江山,陈清林,银奇英,华贲,钱宇. 精馏过程多工况优化设计的能量流结构理论[J]. 化工学报, 2003, 54(6): 775-782
作者姓名:尹清华  江山  陈清林  银奇英  华贲  钱宇
作者单位:华南理工大学传热强化与过程节能教育部重点实验室
基金项目:国家重点基础研究发展规划项目 (No G2 0 0 0 0 2 63 0 8),广东省自然科学基金项目 (No 0 0 0 474)~~
摘    要:以“三环节”能量流结构理论为基础建立了精馏过程多工况优化设计的火用经济数学模型,提出了精馏过程的多工况优化设计策略方法:将其分解为单个塔的多工况优化设计和塔间热集成的优化两个层次,有效输出火用价cU和待回收火用价cO为协调变量来解决多工况优化设计问题.并给出了应用实例.

关 键 词:精馏塔  多工况  优化  能量流结构理论  
文章编号:0438-1157(2003)06-0775-08
收稿时间:2001-09-17
修稿时间:2001-09-17

OPTIMIZATION OF DISTILLATION PROCESS UNDER MULTIPLE PERIOD OPERATION BASED ON ENERGY FLOW STRUCTURE THEORY
YIN Qinghua,JIANG Shan,CHEN Qinglin,YIN Qiying,HUA Ben,QIAN Yu. OPTIMIZATION OF DISTILLATION PROCESS UNDER MULTIPLE PERIOD OPERATION BASED ON ENERGY FLOW STRUCTURE THEORY[J]. Journal of Chemical Industry and Engineering(China), 2003, 54(6): 775-782
Authors:YIN Qinghua  JIANG Shan  CHEN Qinglin  YIN Qiying  HUA Ben  QIAN Yu
Abstract:Based on the three link energy flow structure theory,an optimization strategy for the distillation process under multiple period operation is presented.The highlights of the strategy are as follows:the problem solution is divided into two levels of single column and column system,and transformed exergy price c U and to be recovered exergy price c O are used as the coordination variables.Exergoeconomic models for the optimization of the whole distillation process (including single column and heat integration between columns) are established.The strategy and the model are applied successfully to the optimal design for the column system of a gas separation unit in a refinery under 3 period operation.The optimal scheme proposed is 29.4% less in energy consumption and 21.9% lower in the total cost compared to the exist traditional design.
Keywords:distillation column  multiple period operation  optimization  flow structure theory  
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