An Extended Formulation for the Flexible Short-Term Scheduling of Multiproduct Semicontinuous Plants

被引:7
作者
Capon-Garcia, Elisabet [1 ]
Ferrer-Nadal, Sergio [1 ]
Graells, Moises [1 ]
Puigjaner, Luis [1 ]
机构
[1] Univ Politecn Cataluna, ETSEIB, Chem Engn Dept CEPIMA, E-08028 Barcelona, Spain
关键词
CONTINUOUS-TIME FORMULATION; BATCH; FACILITIES; MODEL;
D O I
10.1021/ie800539f
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Chemical plants are moving toward more-flexible environments, to adapt faster to market changes. For the sake of this flexibility, batch and continuous units might be integrated and operated along the same processing route in a semicontinuous mode, featured by production campaigns of finite duration. Constant production rates for the entire operation have been usually considered. Thus, production adjustments were achieved through storage resources, production line stops, and multiple product campaigns. The objective of this work is to improve the production schedules by developing a new concept for flexible manufacturing, which allows one to program production rate profiles within each semicontinuous operation campaign. Hence, the extended formulation presented allows to address the tradeoff between the opportunities that may arise when adjusting processing rates and the storage needs and opportunities. Finally, several case studies show that the proposed adjustment of the processing rates leads to less storage utilization and more-efficient production performance.
引用
收藏
页码:2009 / 2019
页数:11
相关论文
共 10 条
[1]   Simple continuous-time formulation for short-term scheduling of batch and continuous processes [J].
Castro, PM ;
Barbosa-Póvoa, AP ;
Matos, HA ;
Novais, AQ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (01) :105-118
[2]   A novel event-driven formulation for short-term scheduling of multipurpose continuous processes [J].
Giannelos, NF ;
Georgiadis, MC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (10) :2431-2439
[3]   Effective continuous-time formulation for short-term scheduling. 2. Continuous and semicontinuous processes [J].
Ierapetritou, MG ;
Floudas, CA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (11) :4360-4374
[4]   An efficient MILP continuous-time formulation for short-term scheduling of multiproduct continuous facilities [J].
Méndez, CA ;
Cerdá, J .
COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (4-5) :687-695
[5]   Continuous time representation approach to batch and continuous process scheduling. 1. MINLP formulation [J].
Mockus, L ;
Reklaitis, GV .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) :197-203
[6]   Optimal campaign planning scheduling of multipurpose batch semicontinuous plants .1. Mathematical formulation [J].
Papageorgiou, LG ;
Pantelides, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (02) :488-509
[7]   OPTIMAL CYCLIC SCHEDULING OF MULTISTAGE CONTINUOUS MULTIPRODUCT PLANTS [J].
PINTO, JM ;
GROSSMANN, IE .
COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 (09) :797-816
[8]   MINLP MODEL FOR CYCLIC MULTIPRODUCT SCHEDULING ON CONTINUOUS PARALLEL LINES [J].
SAHINIDIS, NV ;
GROSSMANN, IE .
COMPUTERS & CHEMICAL ENGINEERING, 1991, 15 (02) :85-103
[9]   Improved unit-specific event-based continuous-time model for short-term scheduling of continuous processes: Rigorous treatment of storage requirements [J].
Shaik, Munawar A. ;
Floudas, Christodoulos A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (06) :1764-1779
[10]   The optimal operation of mixed production facilities - A general formulation and some approaches for the solution [J].
Zhang, X ;
Sargent, RWH .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (6-7) :897-904