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作者机构:Univ London Imperial Coll Sci Technol & Med Dept Chem Engn Ctr Proc Syst Engn London SW7 2BY England
出 版 物:《JOURNAL OF PROCESS CONTROL》 (工艺过程控制杂志)
年 卷 期:2000年第10卷第2-3期
页 面:219-227页
核心收录:
学科分类:0711[理学-系统科学] 07[理学] 0817[工学-化学工程与技术] 08[工学] 070105[理学-运筹学与控制论] 081101[工学-控制理论与控制工程] 0811[工学-控制科学与工程] 0701[理学-数学] 071101[理学-系统理论]
基 金:IRC Engineering and Physical Sciences Research Council, EPSRC
主 题:dynamic modelling design process control optimization
摘 要:A general, rigorous dynamic model is described for studying the interactions of design and control in a double-effect distillation system. Two approaches are adopted. In the first, the steady-state process design and the control system are optimized sequentially;potential operability bottlenecks are identified and the economic advantage of double-effect systems over conventional single column systems is demonstrated. In the second approach, the process design and the control system are optimized simultaneously leading to a more economically beneficial system than that obtained using the sequential approach. (C) 2000 IFAC. Published by Elsevier Science Ltd. All rights reserved.