Scheduling of Multistage Batch Processes under Utility Constraints

被引:34
作者
Sundaramoorthy, Arul [1 ]
Maravelias, Christos T. [1 ]
Prasad, Pradeep [1 ]
机构
[1] Univ Wisconsin, Dept Biol & Chem Engn, Madison, WI 53705 USA
关键词
CONTINUOUS-TIME FORMULATION; MILP MODEL; STORAGE; PLANTS; OPTIMIZATION; OPERATIONS; FRAMEWORK;
D O I
10.1021/ie801386m
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We present a novel discrete-time mixed-integer programming (MIP) formulation for the simultaneous hatching and scheduling in multiproduct multistage processes under utility constraints. In addition to processing units and storage vessels, we consider utilities such as cooling water, steam, and electricity that are available in limited quantities. Since different tasks often share the limited utilities at the same time, we use a common time-grid approach. Further, the proposed method handles the hatching decisions (the number and sizes of batches) seamlessly without the usage of explicit batch-selection variables. To preserve batch identity in storage vessels, we introduce a new class of inventory variables and constraints. Our approach is the first to address limited utilities for simultaneous hatching and scheduling in multistage processes.
引用
收藏
页码:6050 / 6058
页数:9
相关论文
共 33 条
[31]   Simultaneous batching and scheduling in multistage multiproduct processes [J].
Sundaramoorthy, Arul ;
Maravelias, Christos T. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (05) :1546-1555
[32]   MILP model for scheduling and design of a special class of multipurpose batch plants [J].
Voudouris, VT ;
Grossmann, IE .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (11) :1335-1360
[33]  
Wu JY, 2004, J CHIN INST CHEM ENG, V35, P381