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作 者:SHAO Li HAN Ji-tian SU Guo-ping PAN Ji-hong
机构地区:[1]School of Energy and Power Engineering, Shandong University, Jinan 250061, China [2]School of Vehicle and Energy, Yanshan University, Qinhuangdao 066004, China
出 处:《Journal of Hydrodynamics》2007年第6期677-682,共6页水动力学研究与进展B辑(英文版)
基 金:the National Natural Science Foundation of China (Grant No. 50376030).
摘 要:This article presents an experimental investigation on condensation heat transfer of R-134a in horizontal straight and helically coiled tube-in-tube heat exchangers. The experiments were carried out at three saturation temperatures(35 ℃ , 40 ℃ and 45 ℃ ) with the refrigerant mass flux varying from 100 kg/m2 s to 400 kg/m2 s and the vapor quality ranging from 0.1 to 0.8. The effects of vapor quality and mass flux of R-134a on the condensation heat transfer coefficient were investigated. The results indicate that the condensation heat transfer coefficients of the helical section are 4%-13.8% higher than that of the straight section. The experimental results were compared with the data available in literature for helical and straight pipes.This article presents an experimental investigation on condensation heat transfer of R-134a in horizontal straight and helically coiled tube-in-tube heat exchangers. The experiments were carried out at three saturation temperatures(35 ℃ , 40 ℃ and 45 ℃ ) with the refrigerant mass flux varying from 100 kg/m2 s to 400 kg/m2 s and the vapor quality ranging from 0.1 to 0.8. The effects of vapor quality and mass flux of R-134a on the condensation heat transfer coefficient were investigated. The results indicate that the condensation heat transfer coefficients of the helical section are 4%-13.8% higher than that of the straight section. The experimental results were compared with the data available in literature for helical and straight pipes.
关 键 词:R-134A helically coiled tube two-phase heat transfer
分 类 号:TK124[动力工程及工程热物理—工程热物理]
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