SIMULTANEOUS OVERDESIGN AND OPTIMIZATION OF CHEMICAL PROCESSES

被引：2

作者：

DOERING, FJ ^{[1
]}

GADDY, JL ^{[1
]}

机构：

[1] MONSANTO ENVIRO CHEM,ST LOUIS,MO

来源：

COMPUTERS & CHEMICAL ENGINEERING | 1979年 / 3卷 / 1-4期

关键词：

D O I：

10.1016/0098-1354(79)80077-0

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

This paper presents the results of simultaneous overdesign and optimization of the contact sulfuric acid process. A stochastic optimization procedure is developed as described. Significant improvements in the economics of the process are achieved by optimization, and these improvements clearly justify the cost of such studies. © 1979.

引用

页码：465 / 472

页数：8

共 15 条

[1] Powers, Mayer, Design of a catalytic reactor-separator system with uncertainty in catalyst activity and selectivity, Ind. Eng. Chem. Process Des. Develop., 14, (1975)
[2] Chen, Erickson, Fan, Consideration of sensitivity and parameter uncertainty in optimal process design, Ind. Eng. Chem. Process Des. Develop., 9, (1970)
[3] Wen, Chang, Optimal design of systems involving parameter uncertainty, Ind. Eng. Chem. Process Des. Develop., 7, (1968)
[4] Kittrell, Watson, Don't overdesign process equipment, Chem. Eng. Progr., 62, 4, (1966)
[5] Saletan, Caselli, Optimum design capacity of new plants, Chem. Eng. Progr., 59, 5, (1963)
[6] Wilde, Optimum Seeking Methods, (1964)
[7] Ahlgren, Stevens, Process optimization in the presence of error, Ind. Eng. Chem. Process Des. Develop., 5, (1966)
[8] Nishida, Ichikawa, Tazaki, Optimal design and control in a class of distributed parameter systems under uncertainty—application to tubular reactor with catalyst deactivation, AIChE Journal, 18, (1972)
[9] Weisman, Holzman, Optimal process system design under conditions of risk, Ind. Eng. Chem. Process Des. Develop., 11, (1972)
[10] Freeman, Gaddy, Quantitative overdesign of chemical processes, AIChE J., 21, (1975)

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