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一种改进的顺序型多目的间歇工厂生产调度的MILP模型 被引量:11

Modified MILP model for scheduling of sequential multipurpose batch plants
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摘要 分析了顺序型多目的工厂间歇生产的特点,建立了一种新的混合整数线性规划(MILP)模型.该模型以操作活动序列作为建模的依据,将整个间歇生产过程分解成若干个子系统.在对各子系统建模的基础上,实现了顺序型多目的工厂间歇调度的全局性优化.并通过算例验证了该模型求解结果的正确性和可行性.然后将新模型运用到更大规模的调度问题上,均求解出了有效的调度方案. Sequential multipurpose batch processes are common in many fine chemical manufacturing plants, such as traditional paint, food, pharmaceuticals, and specialty chemicals plants. The investigation in this paper includes analyzing the operational features of sequential multipurpose batch plants, decomposing the overall batch process spatially into several sub-systems, and presenting a modified MILP formulation for the scheduling of sequential multipurpose batch plants with continuous-time approaches. As the bi-index binary variables are substituted for the tri-index binary variables in the MILP model, the number of discrete variables decreases substantially. The new model is effective in solving large scale scheduling problems. In case studies, the proposed model was compared with the previous model presented by Voudouris and Grossmann. Moreover, several large scale scheduling problems were solved successfully with the proposed modeling approaches. These case studies prove the validity of the model and the practicability of the proposed approaches.
出处 《化工学报》 EI CAS CSCD 北大核心 2006年第4期861-866,共6页 CIESC Journal
基金 国家自然科学基金项目(20225620 20376025 20536020) 广东省科技计划项目(2004B50101002).~~
关键词 间歇过程 调度 顺序型多目的工厂 混合整数线性规划 batch process scheduling sequential multipurpose batch plants MILP
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参考文献15

  • 1Wang Baoguo(王保国),Xu Xi'en(许锡恩).Design and optimization of batch processing(间歇过程设计与优化).Beijing:China Petrochemical Press,1998
  • 2Wang Ju(王举).Study on the optimization algorithm and production scheduling for batch chemical processing[D].Tianjin:Tianjin University,2000
  • 3吴建昱,何小荣,陈丙珍,邱彤.新的多产品间歇生产调度的MILP模型[J].化工学报,2003,54(9):1251-1256. 被引量:8
  • 4Voudouris V T,Grossman I E.MILP model for scheduling and design of a special class of multipurpose batch plants.Computer & Chemical Engineering,1996,20(11):1335-1360
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二级参考文献16

  • 1Pinto Jose M, Grossmann Ignacio E. Continuous Time Mixed Integer Linear Programming Model for Short Term Scheduling of Multistage Batch Plants. Industrial & Engineering Chemistry Research, 1995, 34(9): 3037-3051.
  • 2Pinto Jose M, Grossmann Ignacio E. Alternate MILP Model for Short-term Scheduling of Batch Plants with Preordering Constraints. Industrial & Engineering Chemistry Research,1996, 35(1) : 338-342.
  • 3Pinto Jose M, Tiirkay A, Bolio B, Grossmann I E. STBS: A Continuous-time MILP Optimization for Short-term Scheduling of Batch Plants. Computers & Chemical Engineering, 1998, 22(9) : 1297-1308.
  • 4Cerda Jaime, Henning Gabriela P, Grossmann Ignacio E. Mixedinteger Linear Programming Model for Short-term Scheduling of Single-stage Multiproduct Batch Plants with Parallel Lines.Industrial & Engineering Chemistry Research, 1997, 36 (5):1695-1707.
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  • 6Schilling G, Pantelides C C. Simple Continuous-time Process Scheduling Formulation and a Novel Solution Algorithm. Computers & Chemical Engineering, 1996, 20 (Suppl):S1221-S1226.
  • 7Ierapetritou M G, Floudas C A. Effective Continuous-time Formulation for Short-term Scheduling · 1 · Multipurpose Batch Processes. Industrial & Engineering Chemistry Research,1998, 37(11): 4341-4359.
  • 8Ierapetritou M G, Floudas C A. Effective Continuous-time Formulation for Short-term Scheduling · 3· Multiple Intermediate Due Dates. Industrial & Engineering Chemistry Research,1999, 38(9): 3446-3461.
  • 9Orcun S, Altinel I K, Hortacsu O. General Continuous time Modds for Production Planning and Scheduling of Batch Processing Plants: Mixed Integer Linear Program Formulationsand Computational Issues. Computers & Chemical Engineering,2001, 25(2-3) : 371-389.
  • 10Lin X, Floudas C A. Design Synthesis and Scheduling of Multipurpose Batch Plants Via an Effective Continuous-time Formulation. Computers & Chemical Engineering, 2001, 25(4-6) : 665-674.

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