THE USE OF DYNAMIC-PROGRAMMING WITH PARALLEL COMPUTERS FOR PROCESS SYNTHESIS

被引:7
作者
FRAGA, ES [1 ]
MCKINNON, KIM [1 ]
机构
[1] UNIV EDINBURGH,DEPT MATH & STAT,EDINBURGH EH9 3JZ,MIDLOTHIAN,SCOTLAND
关键词
D O I
10.1016/0098-1354(94)85019-4
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The generation of optimal heat integrated separation sequences is an important and basic task in chemical process design. The efficient generation of these sequences is crucial because design packages must generate many such sequences. We describe the use of parallel computers to reduce the time required to determine the optimal sequences. In this paper, we concentrate on the use of discrete programming techniques, with particular emphasis on the use of dynamic programming, as implemented on distributed memory multi-computers. We show that, although dynamic programming was superseded for some problems by the use of combined methods including branch and bound for serial machines, a parallel implementation of dynamic programming for process synthesis can be superior.
引用
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页码:1 / 13
页数:13
相关论文
共 17 条
[1]   SYNTHESIS OF HEAT INTEGRATED NONSHARP DISTILLATION SEQUENCES [J].
AGGARWAL, A ;
FLOUDAS, CA .
COMPUTERS & CHEMICAL ENGINEERING, 1992, 16 (02) :89-108
[2]   RADICALLY DIFFERENT FORMULATION AND SOLUTION OF THE SINGLE-STAGE FLASH PROBLEM [J].
BOSTON, JF ;
BRITT, HI .
COMPUTERS & CHEMICAL ENGINEERING, 1978, 2 (2-3) :109-122
[3]  
Coulson JM, 1983, CHEM ENG, V6
[4]  
DHALLU NS, 1988, I CHEM E S SER, V109
[5]  
DHALLU NS, 1988, THESIS S BANK POLYTE
[6]   Fractionation of straight-run Pennsylvania gasoline [J].
Fenske, MR .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1932, 24 :482-485
[7]   A MIXED-INTEGER NONLINEAR-PROGRAMMING FORMULATION FOR THE SYNTHESIS OF HEAT-INTEGRATED DISTILLATION SEQUENCES [J].
FLOUDAS, CA ;
PAULES, GE .
COMPUTERS & CHEMICAL ENGINEERING, 1988, 12 (06) :531-546
[8]  
FRAGA ES, 1991, COMPUTER ORIENTED PR, P235
[9]   Multicomponent rectification - Estimation of the number of theoretical plates as a function of the reflux ratio [J].
Gilliland, ER .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 :1220-1223
[10]   THE SYNTHESIS OF COST OPTIMAL HEAT-EXCHANGER NETWORKS - AN INDUSTRIAL REVIEW OF THE STATE OF THE ART [J].
GUNDERSEN, T ;
NAESS, L .
COMPUTERS & CHEMICAL ENGINEERING, 1988, 12 (06) :503-530