OPTIMUM DESIGN OF MULTIPURPOSE CHEMICAL-PLANTS

被引：188

作者：

GROSSMANN, IE ^{[1
]}

SARGENT, RWH ^{[1
]}

机构：

[1] UNIV LONDON IMPERIAL COLL SCI & TECHNOL,DEPT CHEM ENGN,LONDON SW7 2AZ,ENGLAND

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1979年 / 18卷 / 02期

关键词：

D O I：

10.1021/i260070a031

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The optimum design of chemical plants that are used in different ways at different times is considered. The subset of plants with piecewise constant operating conditions is formulated as a nonlinear program. The design of a multicrude pipeline and the design of sequential multiproduct batch plants are given as examples. The latter implies the solution of a mixed-integer problem for which an efficient method for obtaining good suboptimal solutions is proposed. The results show that with the approach developed in the paper, it is possible to design chemical plants that have a specified flexibility and that are economically optimum. © 1979, American Chemical Society. All rights reserved.

引用

页码：343 / 348

页数：6

共 6 条

[1]

Duffin R.J., 1967, GEOMETRIC PROGRAMMIN

[2] OPTIMUM DESIGN OF CHEMICAL-PLANTS WITH UNCERTAIN PARAMETERS [J].

GROSSMANN, IE ;

SARGENT, RWH .

AICHE JOURNAL, 1978, 24 (06) :1021-1028

[3] APPROACH TO OPTIMAL DESIGN OF NETWORKS [J].

MURTAGH, BA .

CHEMICAL ENGINEERING SCIENCE, 1972, 27 (05) :1131-&

[4]

PETERSON EL, 1973, OPTIMIZATION DESIGN, P228

[5] CHOICE OF EQUIPMENT SIZES FOR MULTIPRODUCT BATCH PLANTS - HEURISTICS VS BRANCH AND BOUND [J].

SPARROW, RE ;

FORDER, GJ ;

RIPPIN, DWT .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :197-203

[6]

[No title captured]

← 1 →