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R22在水平双侧强化管外的凝结换热

Condensation heat transfer of R22 outside horizontal doubly-enhanced tubes

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【作者】 张定才刘启斌陶文铨何雅玲

【Author】 ZHANG Dingcai,LIU Qibin, TAO Wenquan, HE Yaling (State Key Laboratory of Multiphase Flow in Power Engineering , Xi’an Jiaotong University, Xi’an 710049 ,Shaanxi,China)

【机构】 西安交通大学动力工程多相流国家重点实验室西安交通大学动力工程多相流国家重点实验室 陕西西安710049陕西西安710049陕西西安710049

【Abstract】 An experimental study on R22 film condensation on single horizontal tubes(one smooth tube and two doubly enhanced ones) was conducted at the saturation temperatures of 32℃, 35℃ and 38℃ respectively. A modified Wi lson plot was used to obtain the water-side and vapor-side heat transfer coeff icients. The results indicated that the experimental condensation heat transfer coefficients agreed with the Nusselt theory with ±10%. The water side heat tr ansfer coefficients of tube No.1 and tube No.2 were 2.78 and 2.99 times of t hat of smooth tube, respectively. At the same heat flux the condensation heat t ransfer coefficients of tube No.1 and tube No.2 were 8.2—18.0 times and 8. 1—12.4 times of the smooth tube, respectively. Thermal resistance analysis sh owed that the relative percentage of vapor-side thermal resistance increased wi th water velocity. When the thermal resistance values of the two sides were equ al, the water velocity of tube No.1 was 1.25 m·s-1(Re=2.41×104) and that of No.2 was 0.82 m·s-1(Re=1.54×104).For all cases, th e wall thermal resistance was less than 4 percentage. The reasons accounting fo r the superiority of tube No.1 were analyzed.

【基金】 国家重点基础研究基金项目(G2000026303);国家自然科学基金项目(50323001).~~
  • 【文献出处】 化工学报 ,Journal of Chemical Industry and Engineering(China) , 编辑部邮箱 ,2005年10期
  • 【分类号】TK124;
  • 【被引频次】37
  • 【下载频次】363
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