Nonlinear and mixed-integer optimization in chemical process network systems

C. Adjiman, C. Schweiger, C. Floudas
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引用次数: 9

Abstract

The use of networks allows the representation of a variety of important engineering problems. The treatment of a particular class of network applications, the Process Synthesis problem, is exposed in this paper. Process Synthesis seeks to develop systematically process owsheets that convert raw materials into desired products. In recent years, the optimization approach to process synthesis has shown promise in tackling this challenge. It requires the development of a network of interconnected units, the process superstructure, that represents the alternative process owsheets. The mathematical model-ing of the superstructure has a mixed set of binary and continuous variables and results in a mixed-integer optimization model. Due to the nonlinearity of chemical models, these problems are generally classiied as Mixed-Integer Nonlinear Programming (MINLP) problems. A number of local optimization algorithms for MINLP problems are outlined in this paper: Generalized Benders Decomposition (GBD), Outer Approximation (OA), Generalized Cross Decomposition (GCD), Extended Cutting Plane (ECP), Branch and Bound (BB), and Feasibility Approach (FA), with particular emphasis on the Generalized Benders Decomposition. Recent developments for the global optimization of nonconvex MINLPs are then introduced. In particular, two branch-and-bound approaches are discussed: the Special structure Mixed Integer Nonlinear BB (SMIN-BB), where the binary variables should participate linearly or in mixed-bilinear terms, and the General structure Mixed Integer Nonlinear BB (GMIN-BB), where the continuous relaxation of the binary variables must lead to a twice-diierentiable problem. Both algorithms are based on the BB global optimization algorithm for nonconvex continuous problems. Once some of the theoretical issues behind local and global optimization algorithms for MINLPs have been exposed, attention is directed to their practical use. The algorithmic framework MINOPT is discussed as a computational tool for the solution of process synthesis problems. It is an implementation of a number of local optimization algorithms for the solution of MINLPs. The synthesis problem for a heat exchanger network is then presented to demonstrate the application of some local MINLP algorithms and the global optimization SMIN-BB algorithm.
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化工过程网络系统的非线性和混合整数优化
网络的使用可以表示各种重要的工程问题。本文提出了处理一类特殊的网络应用——过程综合问题的方法。工艺综合旨在系统地开发将原材料转化为所需产品的工艺表。近年来,工艺合成的优化方法在解决这一挑战方面显示出了希望。它需要发展一个相互连接的单元网络,即过程上层建筑,它代表了可选择的过程表。上部结构的数学模型具有二元和连续变量的混合集,并得到混合整数优化模型。由于化学模型的非线性,这些问题通常被归类为混合整数非线性规划问题。本文概述了求解MINLP问题的几种局部优化算法:广义Benders分解(GBD)、外逼近(OA)、广义交叉分解(GCD)、扩展切割平面(ECP)、分支定界(BB)和可行性方法(FA),重点介绍了广义Benders分解。然后介绍了非凸minlp全局优化的最新进展。特别讨论了两种分支定界方法:特殊结构混合整数非线性BB (smmin -BB),其中二元变量必须线性参与或以混合双线性项参与;一般结构混合整数非线性BB (gmmin -BB),其中二元变量的连续松弛必须导致二次可微问题。这两种算法都是基于非凸连续问题的BB全局优化算法。一旦minlp的局部和全局优化算法背后的一些理论问题被暴露出来,人们就会关注它们的实际应用。讨论了算法框架MINOPT作为求解过程综合问题的计算工具。它是求解minlp问题的若干局部优化算法的实现。最后以换热器网络的综合问题为例,说明了局部MINLP算法和全局优化smi - bb算法的应用。
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