Optimal scheduling of single stage batch plants with direct heat integration

被引:22
|
作者
Castro, Pedro M. [1 ]
Custodio, Bruno [2 ,3 ]
Matos, Henrique A. [3 ]
机构
[1] Univ Lisbon, Ctr Invest Operac, Fac Ciencias, P-1749016 Lisbon, Portugal
[2] Unilever Jeronimo Martins, P-2690361 Santa Iria De Azoia, Portugal
[3] Univ Lisbon, CERENA, Dept Engn Quim, Inst Super Tecn, P-1049001 Lisbon, Portugal
关键词
Energy efficiency; Heat exchanger networks; Short-term scheduling; Multi objective optimization; Mathematical modeling; Mixed-integer linear programming; OPTIMIZATION MODELS; NETWORK DESIGN; FRAMEWORK; ENERGY;
D O I
10.1016/j.compchemeng.2015.07.006
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This paper addresses the multi-objective optimization problem arising in the operation of heat integrated batch plants, where makespan and utility consumption are the two conflicting objectives. A new continuous-time MILP formulation with general precedence variables is proposed to simultaneously handle decisions related to timing, product sequencing, heat exchanger matches (selected from a two-stage superstructure) and their heat loads. It features a complex set of timing constraints to synchronize heating and cooling tasks, derived from Generalized Disjunctive Programming. Through the solution of an industrial case study from a vegetable oil refinery, we show that major savings in utilities can be achieved while generating the set of Pareto optimal solutions through the 6-constraint method. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:172 / 185
页数:14
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