Optimization design of recuperator in a chemical heat pump system based on entransy dissipation theory

Based on the entransy dissipation theory, the multi-parameter optimization design of recuperator is conducted in an Isopropanol–Acetone–Hydrogen (IAH) chemical heat pump system. The performance of the heat pump system can be improved significantly through the multi-parameter optimization, when the main operation parameters of chemical heat pump remain unchanged. When the main operation parameters of chemical heat pump and the heat transfer area of recuperator remain unchanged, the heat transfer rate of recuperator, the high-temperature heat released from the exothermic reactor, and the coefficient of performance (COP) and exergy efficiency of IAH heat pump system greatly increase while the compressor power decreases remarkably as entransy dissipation number decreases. This is done only by optimizing the combination of design parameters of recuperator taking entransy dissipation number as the objective function under certain constraint conditions, and the cost is no more than the low-temperature waste heat having no practical value.

[1]  A. Bejan,et al.  Entropy Generation Through Heat and Fluid Flow , 1983 .

[2]  Mingtian Xu,et al.  Principle of equipartition of entransy dissipation for heat exchanger design , 2010 .

[3]  Antonio Casimiro Caputo,et al.  Heat exchanger design based on economic optimisation , 2008 .

[4]  Pornpote Piumsomboon,et al.  Dynamic Simulation and Control of an Isopropanol-Acetone-Hydrogen Chemical Heat Pump , 2004 .

[5]  Fang Yuan,et al.  Two energy conservation principles in convective heat transfer optimization , 2011 .

[6]  Mingtian Xu,et al.  Thermodynamic analysis of waste heat power generation system , 2010 .

[7]  Ning Pan,et al.  A new approach to analysis and optimization of evaporative cooling system I: Theory , 2010 .

[8]  Mehmet Yilmaz,et al.  Performance evaluation criteria for heat exchangers based on second law analysis , 2001 .

[9]  Wen-Quan Tao,et al.  Effectiveness–thermal resistance method for heat exchanger design and analysis , 2010 .

[10]  Morten Boje Blarke,et al.  Towards an intermittency-friendly energy system: Comparing electric boilers and heat pumps in distributed cogeneration , 2012 .

[11]  Mingtian Xu,et al.  The thermodynamic basis of entransy and entransy dissipation , 2011 .

[12]  Christopher R. Houck,et al.  A Genetic Algorithm for Function Optimization: A Matlab Implementation , 2001 .

[13]  Jiangfeng Guo,et al.  Viscous dissipation effect on entropy generation in curved square microchannels , 2011 .

[14]  Mingtian Xu,et al.  Entransy dissipation number and its application to heat exchanger performance evaluation , 2009 .

[15]  Alper Yilmaz,et al.  Minimum entropy generation for laminar flow at constant wall temperature in a circular duct for optimum design , 2009 .

[16]  Hasan Demir,et al.  A review on adsorption heat pump: Problems and solutions , 2008 .

[17]  Ning Pan,et al.  Optimization principles for convective heat transfer , 2009 .

[18]  Mingtian Xu,et al.  Multi-Objective Optimization of Heat Exchanger Design by Entropy Generation Minimization , 2010 .

[19]  A. Bejan,et al.  Optimal allocation of a heat-exchanger inventory in heat driven refrigerators , 1995 .

[20]  D. P. Sekulic,et al.  Fundamentals of Heat Exchanger Design , 2003 .

[21]  Fengrui Sun,et al.  “Volume-Point” heat conduction constructal optimization with entransy dissipation minimization objective based on rectangular element , 2008 .

[22]  Kuppan Thulukkanam Heat Exchanger Design Handbook , 2013 .

[23]  Mingtian Xu,et al.  The application of field synergy number in shell-and-tube heat exchanger optimization design , 2009 .

[24]  J. E. Hesselgreaves Rationalisation of second law analysis of heat exchangers , 2000 .

[25]  Mingtian Xu,et al.  Performance analysis of Isopropanol–Acetone–Hydrogen chemical heat pump , 2012 .

[26]  V. Bertola,et al.  A critical analysis of the minimum entropy production theorem and its application to heat and fluid flow , 2008 .

[27]  Peter Harriott,et al.  Unit Operations of Chemical Engineering , 2004 .

[28]  R. Ogulata,et al.  Irreversibility analysis of cross flow heat exchangers , 2000 .

[29]  Qun Chen,et al.  An entransy dissipation-based optimization principle for building central chilled water systems , 2012 .

[30]  Mingtian Xu,et al.  The Entropy Generation Minimisation based on the Revised Entropy Generation Number , 2010 .

[31]  Xinguang Cheng,et al.  Least dissipation principle of heat transport potential capacity and its application in heat conduction optimization , 2003 .

[32]  Wei Liu,et al.  Entransy expression of the second law of thermodynamics and its application to optimization in heat transfer process , 2011 .

[33]  Don W. Green,et al.  Perry's Chemical Engineers' Handbook , 2007 .

[34]  Ilya Prigogine,et al.  Introduction to Thermodynamics of Irreversible Processes , 1967 .

[35]  XinGang Liang,et al.  Entransy—A physical quantity describing heat transfer ability , 2007 .

[36]  Mingtian Xu,et al.  The Application of Entransy Dissipation Theory in Optimization Design of Heat Exchanger , 2012 .

[37]  Yeong-Koo Yeo,et al.  Optimal design of a chemical heat pump using the 2-propanol/acetone/hydrogen system , 1997 .