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含油R134a水平强化管外池沸腾换热实验研究 被引量:3

EXPERIMENTAL STUDY ON POOL BOILING HEAT TRANSFER OF R134A-OIL MIXTURE OUTSIDE SINGLE HORIZONTAL ENHANCED TUBES
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摘要 本文对含Solest-120冷冻油的R134a,在饱和温度为5℃和10℃工况下,在水平高效强化管(管E21.为C3型管,管E22为A1型管)管外池沸腾换热进行了实验研究。实验结果表明:与相同管径的光管的换热性能相比,强化管E21、E22的管内传热系数强化倍率分别为3.703和3.035。随着含油浓度的增加,管外池沸腾换热效果得到优化,含油率为1.0×10^(-4)时的管外传热系数比含油5.0×10^(-5)时更高,在实验研究的水流速范围内,在蒸发温度为5℃时增加了3.7%~7.2%,而在蒸发温度为10℃时增加了0.8%~10.9%。从含油R134a的黏度、表面张力等的角度,对含油率高时换热系数大的结论进行了必要的物理解释。研究对开发设计蒸发器有一定实际的指导意义。 Pool boiling heat transfer of R134a with Sloest-120 oil outside single horizontal enhanced tubes (E21 tube is C3 type, E22 tube is A1 type.) is experimentally measured at the saturation temperature of 5℃ and 10℃. The results show that heat transfer coefficients of E21 tube and E22 tube are 3.703 and 3.305 times of that of regular tubes respectively. The heat transfer increases with the oil density, the coefficient of 1.0 × 10^-4 oil is higher than that of 5.0× 10^-5 oil. Within the flow velocity range of water in experiment, the coefficient increases 3.7%-7.2% at 5℃, and 0.8%-10.9% at 10℃. The paper gives a theoretical analysis on the results based on the viscosity and surface tension of R134a-Oil mixtures. This research can provide instruction on designing and developing evaporators.
出处 《工程热物理学报》 EI CAS CSCD 北大核心 2011年第2期269-272,共4页 Journal of Engineering Thermophysics
基金 中国博士后科学基金(No.20060400997) 辽宁省自然科学基金(No.20072159)
关键词 强化管 R134a含油工质 池沸腾传热 测试 enhanced tubes R134a-oil mixtures pool boiling heat transfer testing
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参考文献7

  • 1丁睿,郑钢,宋吉.润滑油对管内沸腾换热影响研究综述[J].流体机械,2006,34(11):80-85. 被引量:7
  • 2Eckels S J, Doerr T M, Pate M B. Heat Transfer Coefficients and Pressure Drops for R2134a and an Ester Lubricant Mixture in a Smooth Tube and a Micro-Fin Tube [J]. ASHRAE Trans., 1998, 104:366-375.
  • 3Cawte H, Sanders D A, Poland GA. Effect of Lubricating oil Contamination on Evaporation in Refrigerants R12 and R22 [J]. Int. J. of Energy Research, 1996,20(8): 663 -679.
  • 4Zurcher O, Thome J R, Favrat D. Flow Boiling and Pressure Drop Measurements for R2134a/Oil Mixtures. Part 2. Evaporation in a Plain Tube [J]. HVAC&R Research, 1997, 3(1): 54-64.
  • 5Webb RL, Rudy TM, Kedzierski, MA. Prediction of the Condensation Coefficient on Horizontal Integral-Fin Tubes [J]. ASME Journal of Heat Transfer, 1985, 107(2): 369-376.
  • 6Gnielinski V. New Equations for Heat and Mass Transfer in Turbulent Pipe and Channel Flow [J]. Int. Chemical Engineering, 1976, 16(2): 359- 368.
  • 7CHENG B, TAG WQ. Experimental Study of R152a Film Condensation on Single Horizontal Smooch tube and Enhanced Tubes [J]. ASME J. Heat Transfer, 1994, 16(2): 266- 270.

二级参考文献13

  • 1Cho Keumnam, Tae Sang-Jin. Evaporation Heat transfer for R-22 and R-407C refrigerant-oil mixture in a microfin tube with a U-bend[J]. International Journal of Refrigeratioga-Revue Intemationale du Froid, 20(10, 23 ( 3 ) : 219-231.
  • 2Ha S, Bergles A E. Influence of oil on local evaporation heat la-ansfer inside a horizontal microfin tube [ J ].ASHRAE Transactions, 1993,99( ptl ) : 1244-1258.
  • 3Hambraeus Katarina. Heat transfer coefficient during twophase flow boiling of HFC-134a[J]. International Journal of Refrigeration-Revue Internationale du Froid, 1991, 14(6) : 357-362.
  • 4Hambraeus K, M Sc. Heat transfer coefficient, two-phase flow boiling of HFC134a [ A ]. International refrigeration conference at Purdue[C]. 1992, : 205-214.
  • 5Hambraeus K. Heat transfer of oil-contaminated HFC134a in a horizontal evaporator[ J]. International Journal of Refrigeration-Revue Intemationale du Froid, 1995, 18 (2):87-99.
  • 6Manwell S P, Bergles A E. Gas-liquid flow patterns in refrigerant-oil mixtures [ J]. ASHRAE Transactions, 1994,100(pt 2):456-464.
  • 7Nidegger Eric, Thome John R, Favrat Daniel. Flow boiling and pressure drop measurements for R-134a/oil mixtures Part 1: evaporation in a microfin tube [ J ].ASHRAE Transactions, 1997,103 (pt 2) : 334.
  • 8Schlager L M, Pate M B, Bergles A E. Heat transfer and pressure drop performance of smooth and internally finned tubes with oil and refrigerant 22 mixtures[J].ASHRAE.Trans,1988,95(pt 2): 160-169.
  • 9Yoshida Suguru, Matsunaga Takashi, Hong Hai-qing, et al. Experimental investigation of oil influence on heat transfer to a refrigerant inside horizontal evaporator tubes[J]. Heat Transfer - Japanese Research, 1991,20(2) :113-129.
  • 10Yoshida Suguru, Matsunaga Takashi. Influence of oil on heat transfer to refrigerant flowing in a horizontal spirally grooved evaporator tube[ A]. Proc 3 ASME JSME Therm Eng Jt Conf[C]. Publ by ASME, New York, NY, USA.1993. 327-332.

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同被引文献40

  • 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
  • 3Ribatski G,Jacobi A M. Falling-film evaporation onhorizontal tubes-A critical review[J]. Refrigeration,2005,28(5):635-653.
  • 4Armbruster R,Mitrovic J. Heat transfer in falling filmon a horizontal tube[C]//Proceedings of the NationalHeat Transfer Conference. Portland,1995:13-21.
  • 5Hu X,Jacobi A M. The intertube falling film(part 2):Mode effects on sensible heat transfer to a falling liquidfilm[J]. Heat Transfer,1996,118(3):626-633.
  • 6Zeng X,Chyu M C,Ayub Z H. Evaporation heat transferperformance of nozzle-sprayed ammonia on a horizontaltube[J]. ASHRAE Transactions,1995,101:136-149.
  • 7Ganic E N,Roppo M N. An experimental study of fallingliquid film breakdown on a horizontal cylinder duringheat transfer[J]. Heat Transfer,1980,102(2):342-346.
  • 8Roques J F. Falling Film Evaporation on a Single Tubeand on a Tube Bundle[D]. Switzerland:Department ofMechanical Engineering,école Polytechnique Fédéralede Lausanne,2004.
  • 9Hu X,Jacobi A M. The intertube falling film(part 1):Flow characteristics,mode transitions and hysteresis[J].Journal of Heat Transfer,1996,118(3):616-625.
  • 10Mohamed A M I. Flow behavior of liquid falling film ona horizontal rotating tube [J]. Experimental Thermal andFluid Science,2007,31(4):325-332.

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