Optimal design and control of dynamic systems under uncertainty: A probabilistic approach

被引:50
|
作者
Ricardez-Sandoval, Luis A. [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
关键词
Process design; Process control; Monte Carlo sampling; Uncertainty; SENSITIVITY-ANALYSIS; INPUT VARIABLES; CHEMICAL-PLANTS; OPTIMIZATION; INTEGRATION; FLEXIBILITY; STABILITY;
D O I
10.1016/j.compchemeng.2012.03.015
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This paper presents a new methodology for the simultaneous design and control of systems under random realizations in the disturbances. The key idea in this work is to perform a distribution analysis on the worst-case variability. Normal distribution functions, which approximate the actual distribution of the worst-case variability, are used to estimate the largest variability expected for the process variables at a user-defined probability limit. The resulting estimates in the worst-case variability are used to evaluate the process constraints, the system's dynamic performance and the process economics. The methodology was applied to simultaneously design and control a Continuous Stirred Tank Reactor (CSTR) process. A study on the computational demands required by the present method is presented and compared with a dynamic optimization-based methodology. The results show that the present methodology is a computationally efficient and practical tool that can be used to propose attractive (economical) process designs under uncertainty. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:91 / 107
页数:17
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