A TSP-based MILP Model for Medium-Term Planning of Single-Stage Continuous Multiproduct Plants

被引:47
作者
Liu, Songsong [1 ]
Pinto, Jose M. [2 ]
Papageorgiou, Lazaros G. [1 ]
机构
[1] UCL, Dept Chem Engn, Ctr Proc Syst Engn, London WC1E 7JE, England
[2] Polytech Univ, Othmer Jacobs Dept Chem & Biol Engn, Brooklyn, NY 11201 USA
关键词
D O I
10.1021/ie800646q
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this paper, we consider the problem of medium-term planning of single-stage continuous plants with a single processing unit that manufactures several products over a planning horizon of several weeks. Sequence-dependent changeover times and Costs Occur when switching from one type of product to another. To overcome the computational expensiveness of traditional slot-based models for large instances, a novel TSP-based (traveling salesman problem) mixed-integer linear programming (MILP) model is proposed that relies on a hybrid discrete/continuous time representation. The model is applied to an example of a real world polymer processing plant to illustrate its applicability. Finally, the proposed model is compared to recently published approaches through literature examples, and the results show that the Computational performance of the proposed model is superior.
引用
收藏
页码:7733 / 7743
页数:11
相关论文
共 22 条
[1]   A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants [J].
Alle, A ;
Papageorgiou, LG ;
Pinto, JM .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (1-2) :3-15
[2]   Mixed-integer programming models for the scheduling and operational optimization of multiproduct continuous plants [J].
Alle, A ;
Pinto, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (11) :2689-2704
[3]  
[Anonymous], 2007, ILOG CPLEX 11 0 USER
[4]   Perspectives on model based integration of process operations [J].
Bassett, MH ;
Dave, P ;
Doyle, FJ ;
Kudva, GK ;
Pekny, JF ;
Reklaitis, GV ;
Subrahmanyam, S ;
Miller, DL ;
Zentner, MG .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (6-7) :821-844
[5]   Decomposition techniques for the solution of large-scale scheduling problems [J].
Bassett, MH ;
Pekny, JF ;
Reklaitis, GV .
AICHE JOURNAL, 1996, 42 (12) :3373-3387
[6]  
Brooke A., 2008, GAMS: A User's Guide
[7]   Optimal scheduling of a lube oil and paraffin production plant [J].
Casas-Liza, J ;
Pinto, JM .
COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (06) :1329-1344
[8]   Simple continuous-time formulation for short-term scheduling of batch and continuous processes [J].
Castro, PM ;
Barbosa-Póvoa, AP ;
Matos, HA ;
Novais, AQ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (01) :105-118
[9]   Medium-term planning of single-stage single-unit multiproduct plants using a hybrid discrete/continuous-Time MILP model [J].
Chen, Peter ;
Papageorgiou, Lazaros G. ;
Pinto, Jose M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (06) :1925-1934
[10]   A decomposition method for the simultaneous planning and scheduling of single-stage continuous multiproduct plants [J].
Erdirik-Dogan, M ;
Grossmann, IE .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (01) :299-315