A rigorous MINLP model for the optimal synthesis and operation of utility plants

被引:136
作者
Bruno, JC
Fernandez, F
Castells, F
Grossmann, LE [1 ]
机构
[1] Carnegie Mellon Univ, Dept Chem Engn, Pittsburgh, PA 15213 USA
[2] Univ Rovira & Virgili, Dept Engn Quim, Tarragona, Spain
关键词
process integration; utility systems; mixed-integer optimization;
D O I
10.1205/026387698524901
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a mixed-integer nonlinear programming (MINLP) model for performing structural and parameter optimization of utility plants that satisfy given electrical, mechanical and heating demands of industrial processes. In this model, nonlinear equations are extensively used for the cost of equipment and for the plant performance in terms of enthalpies, entropies and efficiencies. The proposed approach allows for the simultaneous optimization of the configuration, and selection of flowrates, enthalpies and steam turbine efficiencies. All major conventional utility plant equipment are included in the superstructure for the MINLP model. The proposed approach is not only useful for synthesis, but also for analysing different design alternatives. The model has been implemented in the computer package STEAM, and several applications are reported to illustrate the program capabilities, including a comparison with a simplified MILP model.
引用
收藏
页码:246 / 258
页数:13
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