Heat transfer intensification for retrofitting heat exchanger networks with considering exchanger detailed performances

被引:12
|
作者
Pan, Ming [1 ]
Bulatov, Igor [2 ]
Smith, Robin [2 ]
机构
[1] Sun Yat Sen Univ, Guangdong Engn Technol Res Ctr Petrochem Energy C, Sch Chem Engn & Technol, Guangzhou 510275, Guangdong, Peoples R China
[2] Univ Manchester, Sch Chem Engn & Analyt Sci, Ctr Proc Integrat, Manchester M13 9PL, Lancs, England
关键词
heat exchanger network (HEN); retrofit; optimization; mixed integer linear programming (MILP); iteration; PRESSURE-DROP; PINCH ANALYSIS; MULTIOBJECTIVE OPTIMIZATION; FOULING MITIGATION; GENETIC ALGORITHMS; RECOVERY; ENERGY; INTEGRATION; CONSTRAINT; DESIGN;
D O I
10.1002/aic.16075
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The challenging of this work is to present a thorough study of implementing heat transfer intensification in heat exchanger network (HEN) retrofitting, including all details of exchanger geometry, stream bypassing and splitting, temperature-variation of properties, LMTD and its correction, and pressure drops. This leads to very complex mixed integer nonlinear programming (MINLP) problems rarely reported before. By adopting the MILP-based iterative approach proposed in the earlier work (Pan et al., Chem Eng Sci. 2013;104:498-524.), temperature-variation of properties, LMTD and its correction are initialized to parameters at first, and the rest nonlinear terms are then linearized and expressed as first-order Taylor series expansions. Finally, two iteration loops are executed to find optimal solutions. A small-scale motivating problem and an industrial scale problem are presented to demonstrate the validity and efficiency of the proposed methods. (c) 2018 American Institute of Chemical Engineers AIChE J, 64: 2052-2077, 2018
引用
收藏
页码:2052 / 2077
页数:26
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