Managing risk through a flexible recipe framework

被引:10
作者
Ferrer-Nadal, Sergio [1 ]
Puigjaner, Luis [1 ]
Guillen-Gosalbez, Gonzalo [2 ]
机构
[1] Univ Politecn Cataluna, CEPIMA, ETSEIB, Dept Chem Engn, E-08028 Barcelona, Spain
[2] Carnegie Mellon Univ, Dept Chem Engn, Pittsburgh, PA 15213 USA
关键词
risk management; demand uncertainty; flexible recipe; sample average algorithm;
D O I
10.1002/aic.11404
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel approach is proposed that exploits the use of a flexible recipe framework as a better way to handle the risk associated with the scheduling under uncertainty of batch chemical plants. The proposed solution strategy relies on a novel two-stage stochastic formulation that explicitly includes the trade-off between risk and profit at the decision-making level. The model uses a continuous-time domain representation and the generalized notion of precedence. Management of risk is explicitly addressed by including a control measure (i.e., the profit in the worst scenario), as an additional objective to be considered, thus, leading to a multiobjective optimization problem. To overcome the numerical difficulties associated with such mathematical formulation, a decomposition strategy based on the sample average approximation (SAA) is introduced. The main advantages of this approach are illustrated through a case study, in which a set of solutions appealing to decision makers with different attitudes toward risk are obtained. The potential benefits of the proposed flexible recipe framework as a way of managing the risk associated with the plant operation under demand uncertainty are highlighted through comparison with the conventional approach that considers nominal operating conditions. Numerical results corroborate the advantages of exploiting the capabilities of the proposed flexible recipe framework for risk management purposes. (c) 2008 American Institute of Chemical Engineers.
引用
收藏
页码:728 / 740
页数:13
相关论文
共 45 条
[1]   Robust process planning under uncertainty [J].
Ahmed, S ;
Sahinidis, NV .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (05) :1883-1892
[2]   An MILP Continuous-Time Framework for Short-Term Scheduling of Multipurpose Batch Processes Under Different Operation Strategies [J].
Alberto Mendez, Carlos ;
Cerda, Jaime .
OPTIMIZATION AND ENGINEERING, 2003, 4 (1-2) :7-22
[3]  
[Anonymous], 1991, INTEGRATED PROCESS C
[4]   Risk and uncertainty in managing chemical manufacturing supply chains [J].
Applequist, GE ;
Pekny, JF ;
Reklaitis, GV .
COMPUTERS & CHEMICAL ENGINEERING, 2000, 24 (9-10) :2211-2222
[5]   New measures and procedures to manage financial risk with applications to the planning of gas commercialization in Asia [J].
Aseeri, A ;
Bagajewicz, MJ .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (12) :2791-2821
[6]   Managing financial risk in planning under uncertainty [J].
Barbaro, A ;
Bagajewicz, MJ .
AICHE JOURNAL, 2004, 50 (05) :963-989
[7]  
Biegler L. T., 1997, SYSTEMATIC METHODS C
[8]   Risk management in the scheduling of batch plants under uncertain market demand [J].
Bonfill, A ;
Bagajewicz, M ;
Espuña, A ;
Puigjaner, L .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (03) :741-750
[9]  
Brooke A., 1998, GAMS USERS GUIDE
[10]  
Cohen M. A., 1989, Journal of Manufacturing and Operations Management, V2, P81