Optimization of a heat exchanger network superstructure using nonlinear programming

被引:4
作者
Morton, W [1 ]
机构
[1] Univ Edinburgh, Sch Chem Engn, Edinburgh EH9 3JL, Midlothian, Scotland
关键词
heat exchanger modelling; heat exchanger network design; nonlinear programming; successive quadratic programming;
D O I
10.1243/095440802760075797
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
A heat exchanger network design for a particular set of hot and cold stream duties requires multiple stream splits for minimum energy use. A modern NLP solver, FilterSQP, is applied to minimize a total cost function that takes account of capital and energy costs. The best solution contains fewer exchangers than the initial network. There are multiple local optima at various cost levels. They contain different subsets of exchangers of the initial design, which constitutes a partial superstructure for the problem. Several optimization alternatives are examined: for the model formulation, leading to problems with different optimum costs, for the way the objective is written, which affects the formal degree of nonlinearity in the equations or objective, and for the way the solver operates. For each combination of options, tests were run using widely different initial values for the Trust Region size, a parameter in the solver. FilterSQP solved the network with impressive reliability and efficiency from several starting guesses, some of which were highly arbitrary. From even the most unpromising initial guesses, the solver converged to a local optimum in nearly all cases.
引用
收藏
页码:89 / 104
页数:16
相关论文
共 16 条
[1]   Heat exchanger network retrofit via constraint logic programming [J].
Abbas, HA ;
Wiggins, GA ;
Lakshmanan, R ;
Morton, W .
COMPUTERS & CHEMICAL ENGINEERING, 1999, 23 :S129-S132
[2]   Initialising distillation column models [J].
Fletcher, R ;
Morton, W .
COMPUTERS & CHEMICAL ENGINEERING, 2000, 23 (11-12) :1811-1824
[3]  
Fletcher R., 1993, Annals of Operations Research, V46-47, P307, DOI 10.1007/BF02023102
[4]  
FLETCHER R, 1997, UNPUB MATH PROGRAMMI
[5]  
FLETCHER R, 1987, PRACTICAL OPTIMIZATI
[6]   A visual representation of process heat exchange as a basis for user interaction and stochastic optimization [J].
Fraga, ES ;
Patel, R ;
Rowe, GWA .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A7) :765-776
[7]  
Hohmann EC, 1971, THESIS U SO CALIFORN
[8]   THE PINCH DESIGN METHOD FOR HEAT-EXCHANGER NETWORKS [J].
LINNHOFF, B ;
HINDMARSH, E .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (05) :745-763
[9]  
LOCKE MH, 1983, AICHE J, V29, P5
[10]  
MCCABE WL, 1993, UNIT OPERATIONS CHEM, P315