CO_2跨临界循环热泵热水器用气冷器的优化设计Optimal Design of Gas Cooler Applied in CO_2 Transcritical Cycle Heat Pump Water Heater
张仙平,王凤坤,范晓伟,沈恒根
ZHANG Xian-ping1,2,WANG Feng-kun3,FAN Xiao-wei3
摘要(Abstract):
在设计工况下,建立了用于CO2跨临界循环热泵热水器的套管式气冷器的稳态分布参数模型,对其结构参数进行了敏感性分析,指出了它们的合理变化范围:管内套1根管时,内管外径应至少大于8.00mm,低于10.00mm,外管内径应在11.00mm以上,13.00mm以下;管内套多根管时,3根管性能最优。优化设计结果对CO2气冷器产品的开发具有一定的指导意义。
Under the design condition,a steady state distributed-parameter model of coaxial gas cooler applied in CO2 transcritical cycle heat pump water heater was established.Based on this model,sensitivity analysis of gas cooler performace to its configuration parameters was carried out.According to the simulation results,it is suggested that when one tube in a tube is designed,the outer diameter of inside tube should be at least greater than 8.00mm and lower than 10.00mm,the inner diameter of outside tube is between 11.00mm and 13.00mm.For more tubes in a tube,three tubes in a tube shows the best characteristics.The results of optimization design are expected to offer useful guidelines for gas cooler design and its development.
关键词(KeyWords):
CO2跨临界循环;热泵热水器;气冷器;优化设计
CO2transcritical cycle;heat pump water heater;gas cooler;optimal design
基金项目(Foundation): 河南省高校新世纪优秀人才支持计划项目;; 河南省科技攻关项目(0524440040)
作者(Author):
张仙平,王凤坤,范晓伟,沈恒根
ZHANG Xian-ping1,2,WANG Feng-kun3,FAN Xiao-wei3
参考文献(References):
- [1]丁国良,张春路.制冷空调装置仿真与优化[M].北京:科学出版社,2001.
- [2]Jian Min Yin,Clark W.Bullard,Predrag S.Hrnjak.R744 gas cooler model development and vadilation[J].Int.J.Refrigeration,2001,24(7):692-701.
- [3]Sarkar J.Souvik Bhattacharyya,M.Ram Gopal.Sim-ulation of a transcritical CO2heat pump cycle for sim-ultaneous cooling and heating applications[J].Int.J.Refrigeration,2006,29(5):735-743.
- [4]黄冬平,梁贞潜,丁国良,等.基于模型的二氧化碳微通道气体冷却器性能分析[J].化工学报,2002,53(8):832-836.
- [5]杨俊兰.CO2跨临界循环系统及换热理论分析与实验研究[D].天津:天津大学,2005.
- [6]时红臣.跨临界二氧化碳热泵热水器系统仿真与水回路实验研究[D].南京:南京理工大学,2006.
- [7]王伯春.二氧化碳制冷系统动态仿真和研究[D].南京:南京理工大学,2003.
- [8]VDI.VDI Wa rmeatlas:Berechnungsbla tter f櫣r denWa rme櫣bergang',7.Auflage,VDI Verlag,D櫣sseldorf,Germany,1994.
- [9]Pitla SS,Groll EA,Ramadhyani S.Newcorrelation topredict the heat transfer coefficient during in-tube cool-ing of turbulent supercritical carbon dioxide[J].Int.J.Refrigeration,2002,25(7):887-895.
- [10]Seok Ho Yoon,Ju Hyok Kim,Yun Wook Hwang etal.Heat transfer and pressure drop characteristicsduring the in-tube cooling process of carbon dioxidein the supercritical region[J].Int.J.Refrigeration,2003,26(8):857-864.
- [11]Ren Rieberer.CO2working fluid for heat pumps[D].Graz:University of Technology,Austria,1998.
- [12]Incropera FP,DeWitt DP.Introduction to heat trans-fer,3rd ed[M].New York:John Wiley&Sons,1996.
- [13]洪芳军.CO2跨临界循环水-水热泵的理论和实验研究[D].天津:天津大学,2001.