Globally optimal synthesis of heat exchanger networks. Part I: Minimal networks

被引:26
作者
Chang, Chenglin [1 ,2 ]
Peccini, Alice [3 ]
Wang, Yufei [1 ]
Costa, Andre L. H. [3 ]
Bagajewicz, Miguel J. [4 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing, Peoples R China
[2] Zhejiang Univ, Coll Chem & Biol Engn, Zhejiang Prov Key Lab Adv Chem Engn Manufacture T, Hangzhou, Peoples R China
[3] Rio de Janeiro State Univ UERJ, Inst Chem, Rio De Janeiro, Brazil
[4] Univ Oklahoma, Sch Chem Biol & Mat Engn, Norman, OK 73019 USA
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
enumeration algorithm; global optimality; heat exchanger networks; minimal structures; STAGE-WISE SUPERSTRUCTURE; MATCHES PROBLEM; OPTIMIZATION; NUMBER; DESIGN; UNITS; FORMULATION; HEURISTICS; ALGORITHM; STRATEGY;
D O I
10.1002/aic.16267
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This article introduces the concept of minimal structure (MSTR) and presents an enumeration algorithm for the synthesis of heat exchanger networks based on MSTR. Minimal Structures refer to a class of heat exchanger networks featuring acyclic heat transfer networks without energy loops. The enumerations used are either exhaustive or smart with a stopping criterion. Without loss of generality we use the isothermal mixing Synheat model, that is, the method applies identically to other superstructures, with likely variations in the optimization models associated to each step. A conjecture is used to state that the algorithm renders solutions that are globally optimal. Literature examples are used to demonstrate the capabilities of the enumeration algorithm. Most of our solutions compare favorably with the best reported ones in literature, with exceptions where the reported solution is not minimal.
引用
收藏
页数:15
相关论文
共 43 条
[1]   Heat exchanger network synthesis using genetic algorithm and differential evolution [J].
Aguitoni, Maria Claudia ;
Pavao, Leandro Vitor ;
Siqueira, Paulo Henrique ;
Jimenez, Laureano ;
da Silva Sa Ravagnani, Mauro Antonio .
COMPUTERS & CHEMICAL ENGINEERING, 2018, 117 :82-96
[2]   On the Minimum Number of Units in Heat Exchanger Networks [J].
Bagajewicz, Miguel ;
Valtinson, Gary .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (44) :16899-16904
[3]   New rigorous one-step MILP formulation for heat exchanger network synthesis [J].
Barbaro, A ;
Bagajewicz, MJ .
COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (09) :1945-1976
[4]   A Novel Approach for Linearization of a MINLP Stage-Wise Superstructure Formulation [J].
Beck, Anton ;
Hofmann, Rene .
COMPUTERS & CHEMICAL ENGINEERING, 2018, 112 :17-26
[5]   How to tighten a commonly used MINLP superstructure formulation for simultaneous heat exchanger network synthesis [J].
Beck, Anton ;
Hofmann, Rene .
COMPUTERS & CHEMICAL ENGINEERING, 2018, 112 :48-56
[6]   Global optimization of heat exchanger network synthesis problems with and without the isothermal mixing assumption [J].
Björk, KM ;
Westerlund, T .
COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (11) :1581-1593
[7]   An alternative strategy for global optimization of heat exchanger networks [J].
Bogataj, Milos ;
Kravanja, Zdravko .
APPLIED THERMAL ENGINEERING, 2012, 43 :75-90
[8]  
Brooke A., 2005, GAMS USERS GUIDE
[9]   COMMENTS ON IMPROVEMENTS ON A REPLACEMENT FOR THE LOGARITHMIC MEAN [J].
CHEN, JJJ .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (10) :2488-2489
[10]   110th Anniversary: On the Departure from Heuristics and Simplified Models toward Globally Optimal Design of Process Equipment [J].
Costa, Andre L. H. ;
Bagajewicz, Miguel J. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2019, 58 (40) :18684-18702