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CFC_S替代工质R134a、R142b在水平管外池沸腾传热与强化 被引量:2

Nucleate Pool Boiling Heat Transfer and Enhancement of R134a and R142b on Horizontal Tube
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摘要 研究了R134a、R142b在光滑管和机械加工表面多孔管水平管外的池沸腾换热性能,分析了工质在水平管外的沸腾传热机理,实验的对比压力P/Pc=0.20。实验结果表明,光滑管外沸腾实验结果与取平均表面粗糙度为2μm的Gorenflo公式预测结果吻合较好,与光滑管相比,机械加工表面多孔管能显著地强化沸腾传热,且随着热流密度的增加,强化倍率减小。通过数据拟合,得到了沸腾换热系数的经验关系式。 An experimental investigation on nucleate pool boiling heat transfer of refrigerants outside horizontal plain and E tube has been carried out and the heat transfer mechanism was discussed.The refrigerants are R134a and R142b at normalized saturation pressure P/P c =0 20.For the plain tube,the present data of R134a and R142b are coincided well with Gorenflo correlation for surface roughness 2μm.Compared with plain tube,the machime processed porous tube shows considerable enhancement effect.And the enhancement rate decreases with increasing heat flux.The correlations of boiling heat transfer coefficients are obtained.
出处 《制冷学报》 CAS CSCD 北大核心 1997年第3期6-11,共6页 Journal of Refrigeration
基金 广东省自然科学基金
关键词 池沸腾 传热系数 CFCc 替代物 制冷剂 Pool boiling Heat transfer coefficient CFC S Alternatives,Refrigerants.
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同被引文献28

  • 1刘文毅,李妩,陶文铨.R123水平强化单管外池沸腾换热实验研究[J].制冷学报,2005,26(4):30-34. 被引量:10
  • 2刘启斌,何雅玲,张定才,陶文铨.R123在水平双侧强化管外池沸腾换热[J].化工学报,2006,57(2):251-257. 被引量:15
  • 3PIORO I L, ROHSENOW W, DOERFFER S S. Nucleate pool boiling heat transfer(Ⅰ): Review of parametric effects of boiling surface [J]. International Journal of Heat and Mass Transfer, 2004, 47(23): 5033-5044. DOI:10.1016/j.ijheatmasstransfer.2004.06.019.
  • 4ZHANG B J, KIM K J. Nucleate pool boiling heat transfer augmentation on hydrophobic self-assembly mono-layered alumina nano-porous surfaces [J]. International Journal of Heat and Mass Transfer, 2014, 73: 551-561. DOI: 10.1016/j.ijheatmasstransfer. 2014.02.032.
  • 5JO H J, AHN H S, KANG S H, et al. A study of nucleate boiling heat transfer on hydrophilic, hydrophobic and heterogeneous wetting surfaces [J]. International Journal of Heat and Mass Transfer, 2011, 54(25): 5643-5652. DOI: 10.1016/j.ijheatmasstransfer.2011.06.001.
  • 6LEE Y, GYU D, KIM J H, JUNG D. Nucleate boiling heat transfer coefficients of HFO1234yf on various enhanced surfaces [J]. International Journal of Refrigeration, 2014, 38:198-205. DOI: 10.1016/j.ijrefrig.2013.09.014.
  • 7SUN Z H, GONG M Q, LI Z J, et al. Nucleate pool boiling heat transfer coefficients of pure HFC134a, HC290, HC600a and their binary and ternary mixtures [J]. International Journal of Heat and Mass Transfer, 2007, 50(1): 94-104. DOI: 10.1016/j. ijheatmasstransfer.2006.06.041.
  • 8NAE H K, EUL J L, HO W B. Pool boiling of R-134a/oil mixtures on enhanced tubes having different pore and gap sizes [J]. International Journal of Heat and Mass Transfer,2013, 66: 118-127. DOI: 10.1016/j.ijheatmasstransfer.2013.07.016.
  • 9EVRAAM G, STEVEN E. Local heat transfer coefficient for pool boiling of R-134a and R-123 on smooth and enhanced tubes [J]. International Journal of Heat and Mass Transfer, 2012, 55(11): 3021-3028. DOI: 10.1016/j.ijheatmasstransfer.2012.02.012.
  • 10JUNG D, LEEB H, BAE D, et al. Nucleate boiling heat transfer coefficients of flammable refrigerants on various enhanced tubes [J]. International Journal of Refrigeration, 2005, 28(3): 451-455. DOI: 10.1016/j.ijrefrig.2004.07.024.

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