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Mixed-integer optimization techniques for planning and scheduling of chemical processes.

机译:用于计划和调度化学过程的混合整数优化技术。

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摘要

This thesis explores the application of mixed integer optimization techniques to planning and scheduling problems of significant importance to the chemical process industries. The goal is to develop novel models for these problems, as well as effective algorithms for their solution.;The problem of selecting processes and capacity expansion policies for a chemical complex is addressed first. The objective is to maximize the net present value given predictions for prices and demands during a long range time horizon. This planning problem is modelled as a multiperiod mixed integer linear program (MILP), and a computational study is carried out to evaluate the performance of several solution strategies. Based on a variable disaggregation technique that exploits the presence of lot sizing substructures, an alternative formulation is also given. This includes more variables and constraints but exhibits a tighter linear programming relaxation, and it requires an order of magnitude less computational time than the original one.;We then propose a strategy for reformulating a large class of multiperiod MILP models for planning and scheduling. The strategy is illustrated with an MILP model that can handle a wide variety of scheduling problems in multiproduct/multipurpose batch chemical plants.;Subsequently, we consider the problem of multiproduct scheduling on continuous parallel production lines. A large-scale mixed integer nonlinear program (MINLP) is developed and solved by using the generalized Benders decomposition. The proposed technique is applied to a real world problem for a polymer production plant. The corresponding MINLP, which contains 780 binary variables, 23,000 continuous variables and 3,200 constraints, predicts annual savings of several million dollars.;Last, we address theoretical and computational issues related to generalized Benders decomposition. First, it is proved that an MINLP formulation with zero nonlinear programming relaxation gap requires only one Benders cut in order to converge. Second, by exploiting the Kuhn-Tucker optimality conditions for nonlinear problems, a methodology is developed which avoids the explicit solution of large nonlinear subproblems. Finally, a theoretical analysis shows that the application of generalized Benders decomposition to nonconvex problems does not always lead to the global optimum for these problems.
机译:本文探讨了混合整数优化技术在计划和调度问题上的应用,这些问题对化学过程工业具有重要意义。目的是为这些问题开发新颖的模型,并为它们解决问题提供有效的算法。首先解决化学复合物的选择工艺和容量扩展策略的问题。目标是在长期的时间范围内,根据给定的价格和需求预测,使净现值最大化。该规划问题被建模为多周期混合整数线性程序(MILP),并且进行了计算研究以评估几种解决方案策略的性能。基于利用批量大小子结构的存在的可变分解技术,还给出了一种替代公式。这包括更多的变量和约束条件,但线性规划松弛更紧密,并且与原始模型相比,所需的计算时间要少一个数量级。;然后,我们提出了一种重新规划大型多周期MILP模型以进行计划和调度的策略。通过MILP模型说明了该策略,该模型可以处理多产品/多用途批处理化工厂中的各种调度问题。随后,我们考虑了连续并行生产线上的多产品调度问题。通过使用广义Benders分解,开发并求解了大型混合整数非线性程序(MINLP)。所提出的技术被应用于聚合物生产厂的实际问题。相应的MINLP包含780个二进制变量,23,000个连续变量和3200个约束,预计每年将节省数百万美元。最后,我们解决与广义Benders分解有关的理论和计算问题。首先,证明了具有零非线性编程弛豫间隙的MINLP公式仅需切割一个Benders即可收敛。其次,通过利用Kuhn-Tucker最优性条件求解非线性问题,开发了一种避免大型非线性子问题显式求解的方法。最后,理论分析表明,将广义Benders分解应用于非凸问题并不总是导致这些问题的全局最优。

著录项

  • 作者

    Sahinidis, Nikolaos Vasili.;

  • 作者单位

    Carnegie Mellon University.;

  • 授予单位 Carnegie Mellon University.;
  • 学科 Chemical engineering.;Operations research.
  • 学位 Ph.D.
  • 年度 1990
  • 页码 302 p.
  • 总页数 302
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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