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R22及其替代工质饱和池沸腾传热研究 被引量:3

Investigation on Saturated Nucleate Pool Boiling Heat Transfer of R22 and Its Alternatives
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摘要 目前R22的主要替代工质有R134a、R410a、R407c等。利用机械加工表面多孔管可以显著提高R22替代工质满液式蒸发器的沸腾传热系数。本文通过试验研究了R134a、R410a、R407C等工质在机械加工表面多孔管蒸发器中沸腾的传热性能。试验结果表明:相同的热流密度下,R410a的总传热系数是R22的1.28~1.37倍;R407c是R22的0.80~0.81倍。R134a是R22的1.08~1.10倍。机械加工表面多孔管管束效应因制冷剂不同而不同。对R22,下排管沸腾换热系数高于上排管。而对R134a、R410a与R407c,上排管沸腾换热系数最大,中排管和下排管有所不同。 R134a,R410a and R407c were used to replace R22 as alternative refrigerants for central air-conditioning System.The experiment results show that the location of the tube makes a big difference to the boiling heat transfer coefficients of R22 and its alternative refrigerants on the surface of tube.In the same heat flux range,the boiling heat transfer coefficient of R134a outside tube bundles is 1.26~1.28 times to that of R22;for R410a,it is 2.62~3.14 times to that of R22;and for R407c,it is 0.62~0.63 times to that of R22.Heat transfer coefficients of different refrigerants show the similar regularity on the same mechanically processed tube with porous surface.In the analysis of evaporator performance,we find that in the same heat flux range,the total heat transfer coefficients of R407c in evaporator are 0.80~0.81 times to those of R22;for R134a,they are 1.08~1.10 times to those of R22;for R410a,which have the best performance in the evaporator,they are 1.28~1.37 times to those of R22.
出处 《流体机械》 CSCD 北大核心 2011年第3期63-67,共5页 Fluid Machinery
关键词 池核沸腾 换热系数 混合工质 机械加工表面多孔管 nucleate pool boiling heat transfer coefficient refrigerant mixtures mechanically processed tube with porous surface
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  • 1袁巍,周盛,陆亚钧.压气机间隙流与处理机匣作用的三维数值分析[J].北京航空航天大学学报,2004,30(9):885-888. 被引量:27
  • 2卢新根,楚武利,朱俊强,王如根.梯状间隙结构对轴流压气机影响的试验与数值模拟[J].工程热物理学报,2005,26(2):234-236. 被引量:9
  • 3Pete Dexter.R410A空调制冷剂的特点[J].暖通空调,2005,35(B11):7-7. 被引量:3
  • 4吴华根,束鹏程,邢子文.采用替代工质的空气源热泵性能试验研究[J].暖通空调,2006,36(1):60-62. 被引量:11
  • 5.新型制冷剂R410A与R22之物性比较[Z],三星空调有限公司资料[Z].,2003..
  • 6Takeshi Ebisu, Kunikazu Torikoshi. Heat Transfer Characteristics and Correlations for R410A Flowing Inside a Horizontal Smooth Tube[J]. ASHRAR Trans, 1998.556-561.
  • 7Yoshida S, etc. Heat trabsfer to non-azeotropic mixtures of refrigerants flowing in a horizontal evaporator tube [J].ASME/JSME Thermal Engineering Proceedings, 1991,2:295-300.
  • 8Yongchan Kim, Kookjeong Seo, Jin Taek Chung. Evaporation heat transfer characteristics of R410A in 7 and 9.52mm smooth/micro-fin tubes[J]. Int. J. of Refrig,2002,25:716-730.
  • 9Wijaya H, Spatz MW.Two-phase flow heat transfer and pressure drop characteristics of R22 and R32/125 [J].ASHRAE Trans, 1995,101:1020-1027.
  • 10Goto M, Inoue N, Ishiwatari N. Condensation and evaporation heat transfer of R410A inside internally grooved horizontal tubes[J]. Int. J. of Refrig, 2001,24: 628-638.

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