Simultaneous design and scheduling of a semicontinuous/batch plant for ethanol and derivatives production

被引:11
作者
Fumero, Yanina [1 ]
Montagna, Jorge M. [1 ,2 ]
Corsano, Gabriela [1 ]
机构
[1] INGAR Inst Desarrollo & Diseno CONICET UTN, Santa Fe, Argentina
[2] Univ Tecnol Nacl, Fac Reg Santa Fe, CIDISI, Santa Fe, Argentina
关键词
Batch/semicontinuous plant design; Scheduling; Ethanol and yeast productions; Mixed integer linear programming; MULTIPRODUCT BATCH PLANTS; NONCONTINUOUS PLANTS; OPTIMIZATION METHODS; PROTEIN-PRODUCTION; CONTINUOUS-TIME; PROCESS SYSTEMS; ASSIGNMENT; MULTISTAGE; RETROFIT; INDUSTRY;
D O I
10.1016/j.compchemeng.2011.08.004
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The interest on renewable fuels has greatly increased in the last years. Particularly, ethanol production arises as a good solution to many current economic-environmental problems. Yeast production from the ethanol residuals constitutes a sustainable alternative. Usually, this kind of plants is designed using single product campaigns. However, since yeast degradation is fast and a continuous supply must be assured, the mixed product campaign policy is the most appropriate. Besides, a stable context can be assumed to justify this approach that takes advantage of the special structure of the plant. Therefore, in this paper, a mixed integer linear programming model is formulated for simultaneous design and scheduling of a semicontinuous/batch plant for ethanol and derivatives production. The optimal plant configuration, unit sizes, number of batches of each product in the campaign and its sequencing is obtained in order to fulfill the ethanol and yeast demands minimizing the investment cost. (C) 2011 Elsevier Ltd. All rights reserved.
引用
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页码:342 / 357
页数:16
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