Optimal Short-Term Scheduling of Large-Scale Multistage Batch Plants

被引:40
|
作者
Castro, Pedro M. [1 ,3 ]
Hariunkoski, Iiro [2 ]
Grossmann, Ignacio E. [3 ]
机构
[1] Inst Nacl Engn Tecnol & Inovacao, Dept Modelacao & Simulacao Proc, P-1649038 Lisbon, Portugal
[2] ABB Corp Res Ctr, D-68526 Ladenburg, Germany
[3] Carnegie Mellon Univ, Dept Chem Engn, Pittsburgh, PA 15213 USA
基金
美国安德鲁·梅隆基金会;
关键词
UNLIMITED INTERMEDIATE STORAGE; CONTINUOUS-TIME FORMULATION; PARALLEL UNITS; MIXED-INTEGER; MILP MODEL;
D O I
10.1021/ie900734x
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a new decomposition algorithm for the optimal scheduling of large-scale multiproduct plants containing a large number of orders, Rather than tackling highly complex, full-space problems that cannot be solved in reasonable time, the complete set of orders is scheduled sequentially by considering one, or a couple of them, at a time. As we proceed through the iterations, previously scheduled orders can be partly rescheduled to allow for some flexibility while keeping the combinatorial complexity at a manageable level. Once a complete schedule is obtained, the same concept is applied to improve the schedule locally. The user can choose to rely on either a unit-specific or a sequencing variable based continuous-time mixed-integer linear programming model. In addition, there are other parameters that affect how the decomposition is carried out, so the algorithm is highly versatile and adaptable to problems of varying sizes, The largest problem solved is a real-life, 50-order, 17-unit, 6-stage problem, for which a very good solution can be found in less than 1 min of computational time.
引用
收藏
页码:11002 / 11016
页数:15
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