Scheduling of a continuous plant with recycling of byproducts: A case study from a tissue paper mill

被引:29
作者
Castro, Pedro M. [1 ]
Westerlund, Joakim [2 ]
Forssell, Sebastian [3 ]
机构
[1] INETI, Dept Modelacao & Simulacao Proc, P-1649038 Lisbon, Portugal
[2] Abo Akad Univ, Proc Design Lab, FIN-20500 Turku, Finland
[3] Borealis Polymers Oy, BU Phenol, FIN-06101 Porvoo, Finland
关键词
Production planning; Mixed integer linear programming; Uniform time grid; Event points; Continuous plant; Intermediate storage; MULTIPURPOSE BATCH PLANTS; CONTINUOUS-TIME FORMULATIONS; DESIGN; DISCRETE; ALGORITHM; INDUSTRY;
D O I
10.1016/j.compchemeng.2008.10.004
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This paper considers an industrial scheduling problem. It involves profit maximization and the determination of the optimal cycle time, while meeting the minimum demands for the several products. Resource-Task Network-based formulations are employed and a detailed comparison between continuous- and discrete-time models is provided. Both have the improved capability of handling tasks with flexible proportions of input materials in order to consider the incorporation of different flowrates of byproducts that are recycled back to the first production stage. The continuous-time formulation is shown to be more efficient and the resulting mixed integer nonlinear program (MINLP) can be solved to optimality within reasonable computational time. A new recycling policy is proposed that achieves the double goal of making the process more profitable due to important savings oil the more expensive raw-materials and also more environmentally friendly, due to the reduction of waste disposal requirements. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:347 / 358
页数:12
相关论文
共 25 条
[1]   DETAILED DESIGN OF MULTIPURPOSE BATCH PLANTS [J].
BARBOSAPOVOA, AP ;
MACCHIETTO, S .
COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 (11-12) :1013-1042
[2]   Scheduling of a multi-product batch process in the chemical industry [J].
Blomer, F ;
Gunther, HO .
COMPUTERS IN INDUSTRY, 1998, 36 (03) :245-259
[3]   Two new continuous-time models for the scheduling of multistage batch plants with sequence dependent changeovers [J].
Castro, Pedro M. ;
Grossmann, Ignacio E. ;
Novais, Augusto Q. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (18) :6210-6226
[4]   Simultaneous design and scheduling of multipurpose plants using resource task network based continuous-time formulations [J].
Castro, PM ;
Barbosa-Póvoa, AP ;
Novais, AQ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (02) :343-357
[5]   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
[6]   Optimal periodic scheduling of batch plants using RTN-based discrete and continuous-time formulations:: A case study approach [J].
Castro, PM ;
Barbosa-Póvoa, AP ;
Matos, HA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (14) :3346-3360
[7]  
*EUR COMM IIPC, 2001, REF DOC BEST AV TECH
[8]   Continuous-time versus discrete-time approaches for scheduling of chemical processes: a review [J].
Floudas, CA ;
Lin, XX .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (11) :2109-2129
[9]  
*FOR BAS SECT TECH, 2006, STRAT RES AG INN COM
[10]   A novel event-driven formulation for short-term scheduling of multipurpose continuous processes [J].
Giannelos, NF ;
Georgiadis, MC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (10) :2431-2439