SYNTHESIS OF OPTIMAL PROCESS SYSTEMS WITH UNCERTAINTY

被引：34
作者：
NISHIDA, N
ICHIKAWA, A
TAZAKI, E
机构：
[1] TOKYO INST TECHNOL,MEGURO,TOKYO,JAPAN
[2] SCI UNIV TOKYO,NODA,CHIBA,JAPAN
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1974年 / 13卷 / 03期
关键词：
D O I：
10.1021/i260051a003
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
引用
收藏
页码：209 / 214
页数：6
相关论文
共 14 条
[1]   CONSIDERATION OF SENSITIVITY AND PARAMETER UNCERTAINTY IN OPTIMAL PROCESS DESIGN [J].
CHEN, MSK ;
ERICKSON, LE ;
FAN, LT .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1970, 9 (04) :514-&
[2]   COMPUTATIONAL ALGORITHM FOR THE SEQUENTIAL UNCONSTRAINED MINIMIZATION TECHNIQUE FOR NONLINEAR-PROGRAMMING [J].
FIACCO, AV ;
MCCORMICK, GP .
MANAGEMENT SCIENCE, 1964, 10 (04) :601-617
[3]   OPTIMAL SYNTHESIS OF PROCESS SYSTEMS NECESSARY CONDITION FOR OPTIMAL SYSTEM AND ITS USE IN SYNTHESIS OF SYSTEMS [J].
ICHIKAWA, A ;
FAN, LT .
CHEMICAL ENGINEERING SCIENCE, 1973, 28 (02) :357-373
[4]  
ICHIKAWA A, 1969, 34 ANN M SOC CHEM EN
[5]  
ICHIKAWA A, TO BE PUBLISHED
[6]  
KITTRELL JR, 1966, CHEM ENG PROG, V62, P79
[7]  
Linsley J., 1971, Journal of Optimization Theory and Applications, V8, P271, DOI 10.1007/BF00931883
[8]   OPTIMAL DESIGN AND CONTROL IN A CLASS OF DISTRIBUTED PARAMETER SYSTEMS UNDER UNCERTAINTY - APPLICATION TO TUBULAR REACTOR WITH CATALYST DEACTIVATION [J].
NISHIDA, N ;
TAZAKI, E ;
ICHIKAWA, A .
AICHE JOURNAL, 1972, 18 (03) :561-&
[9]  
NISHIDA N, 1972, THESIS TOKYO I TECHN
[10]  
RUDD DF, 1969, AICHE J, V15, P10
12