Synthesis and optimization of the recovery route for residual products under uncertain product demand

被引:9
作者
Duque, Joaquim
Barbosa-Povoa, Ana Paula F. D. [1 ]
Novais, Augusto Q.
机构
[1] IST, CEG, DEG, P-1049001 Lisbon, Portugal
[2] INETI, DMS, P-1649038 Lisbon, Portugal
关键词
residual products recovery; optimization; network synthesis; environmental impact; stochastic flexibility index;
D O I
10.1016/j.cor.2005.06.008
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The present work describes an optimization model for managing the recovery of residual products that originate at industrial plants. The framework for the proposed general network superstructure, where all possible process transformations, storage, transports and auxiliary operations are accounted for, is modeled using a maximal state task network representation. This framework is combined with the evaluation of a set of environmental impacts, quantified by metrics (for air, water pollution, etc.) through the minimum environment impact analysis methodology and is associated with waste generation at utility production and transportation levels. The final model is described as a mixed-integer linear programming model, which, once solved, is able to suggest the optimal processing and transport routes, while optimizing a given objective function and meeting design and environmental constraints. For each solution obtained, a stochastic flexibility index is computed, allowing for the drawing of trade-off curves for investment decision support. A motivating example is explored, based on the recovery of the sludge obtained from aluminum surface finishing plants. This example aims to maximize the quantity of recovered sludge and reflects the trade-off between the costs of disposal. processing, transport and storage, while accounting for the limits imposed on the associated environmental pollutants. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1463 / 1490
页数:28
相关论文
共 8 条
[1]   DETAILED DESIGN OF MULTIPURPOSE BATCH PLANTS [J].
BARBOSAPOVOA, AP ;
MACCHIETTO, S .
COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 (11-12) :1013-1042
[2]  
Douglas J. M., 1988, Conceptual design of chemical processes
[3]   A GENERAL ALGORITHM FOR SHORT-TERM SCHEDULING OF BATCH-OPERATIONS .1. MILP FORMULATION [J].
KONDILI, E ;
PANTELIDES, CC ;
SARGENT, RWH .
COMPUTERS & CHEMICAL ENGINEERING, 1993, 17 (02) :211-227
[4]  
LINNINGER AA, 1994, AICHE S SER, V90, P46
[5]   A branch and bound procedure for the design of multipurpose batch plants with uncertain demands [J].
Nicolas, G ;
Rotstein, GE ;
BarbosaPovoa, APFD ;
Macchietto, S .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 :S1179-S1184
[6]  
PISTIKOPOULOS EN, 1994, AICHE S SERIES, V90, P139
[7]   Synthesis of flexible and reliable short-term batch production plans [J].
Rotstein, GE ;
Lavie, R ;
Lewin, DR .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (02) :201-215
[8]  
Stefanis SK, 1997, COMPUT CHEM ENG, V21, P1073, DOI 10.1016/S0098-1354(96)00319-5