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R22替代工质蒸发器的性能研究 被引量:1

Numerical Study of Heat Transfer and Flow Characteristics in R22 Refrigerant Replacement Evaporators
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摘要 基于湿球温度效率法,建立了蒸发器的稳态分布参数模型。分别以R22及其3种替代产品(R407C,R410A,R134A)为工质,运用该模型详细比较了在流量变化及风量变化两种情况下2排管蒸发器的换热和流动特性。结果表明:当迎风面风速不变时,随着管内冷媒流量的增大,各种工质蒸发器总换热量、显热换热量、潜热换热量均增大,但潜热换热量增大得更快。压降亦随着管内流量的增大而增大。当管内冷媒流量不变时,随着蒸发器迎风面风速的增大,各种工质蒸发器总换热量、显热换热量均增加,潜热换热量下降,同时压降亦下降,但下降的趋势随着风速的增大而最终趋于平缓。四种工质中,R134A性能较好,但其压降也最大,R410其次,压降最小,但其蒸发压力比R22高出60%左右。R407C与R22在换热量及压降方面最为接近,是其理想的替代产品。 Based on the ε_c-BF, a steady state distributed parameters model is put forward in the numerical simulation of refrigerant circuitry in evaporators in this paper. Applying this model, the heat transfers and flow characteristics of two-rows counter-flow evaporators which used the refrigerant replacement of R22 (R407C, R410A, R134A) are studied. When the frontal velocity is constant, with the refrigerant mass velocity increasing, the total capacity, sensible capacity , and the latent capacity of all evaporators which apply different refrigerants increase, the pressure drop in tubes decrease. When the refrigerant mass velocity is constant, with the frontal velocity increasing, the total capacity, sensible capacity of all evaporators which apply different refrigerants increase and the latent capacity, pressure drop in tubes decrease. Among the characteristic comparison of four refrigerants evaporators, the heat transfer rate of R134A evaporators is better than the other refrigerants evaporators, but its pressure drop is the highest. The heat transfer rate of R410A evaporators is better than R22 evaporator, but the evaporate pressure much higher than that of R22; both of the two refrigerant replacement are not the perfect replacements. The heat transfer rate of R407C evaporators is 3%~5% higher than R22 evaporators and the pressure drop of R407C evaporators is 5%~10% lower than R22. R407C is the ideal refrigerant replacement of R22.
出处 《低温与特气》 CAS 2005年第2期15-19,共5页 Low Temperature and Specialty Gases
关键词 蒸发器 替代工质 流程布置 数值模拟 evaporators refrigerant replacement refrigerant circuitry numerical simulation
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参考文献7

  • 1曹锋,陈芝久,赵薰,黄培炫,李汉武.制冷系统中R407C替代R22技术研究综述[J].制冷与空调,2002,2(1):61-63. 被引量:18
  • 2陈斌,陈光明.R407C、R410A系统热力性能研究综述[J].制冷,2003,22(3):24-30. 被引量:14
  • 3薛殿华.空气调节[M].北京:中国建筑工业出版社,1985..
  • 4WANG C C,JANG J Y,CHIOU N F. A heat transfer and friction correlation for wavy fin-and-tube heat exchangers[J]. International Journal of Heat Mass Transfer,1999,42: 1919-1924.
  • 5TRAVISS D P,ROHSENOW W M,BARON A B. Forced-Convection Condensation Inside Tube: Heat Transfer Equation for Evapoator Design[J]. ASHRAE Trans,1973.
  • 6陈常青.低温换热器[M].北京:机械工业出版社,1986..
  • 7REFPROP7.1,National Institute of Standards and Technology,Gaithersburg,MD,2003.

二级参考文献30

  • 1Bivens D B , et al. Performance of R32/R125/R134a mixtures in systems with accumulators or flooded evaporators.ASHRAE Transaction, 1997( I ) : 777 - 780.
  • 2Hwang, Y, et al. Experiences with refrigerant mixtures.ASHRAE Transaction, 1997( I ) :765 - 776.
  • 3Cavallini, A , et al.Working fluids for mechanical refrigelation--invited paper presented at the 19th international congress of refrigeration,the Hague,August 1995.International Journal of Refrigeration. 1996(8), VOL. 19:485 - 496.
  • 4Aprea, C , et al. An experimental evaluation of the greenhouse effect in R- 22 substitution.Energy Conversion and Management, 1998(9), VOL.39:877 - 887.
  • 5Chin,L ,et al.Issues relating to the adoption of R-410A in air conditioning systems. Proceedings of the 20th International Congress of Refrigeration,Sydney ,1999, Vol. 2: (paper 179 ).
  • 6Piao, C C ,et al.A study of thermodynamic properties of HFC-32/125/134a ternary mixture.Proceedings of the 19th Intemational Congress of Refrigeration,The Hague,1995,Vol.4a: 488 - 495.
  • 7Heide, R. The staface tension of HFC refrigerants and mixtures. International Journal of Refrigeration, 1997(7), Vol.20:496 - 5O3.
  • 8Klein, S A , et al.Refrigeration syslem performance using Liquid- suction heat exchangers. International Journal of Refrigeration, 2000(8 ), Vol. 23,588 - 596.
  • 9Mei, V C, et al. Performance tests of R - 22 and R - 32/R -125/R- 134a mixture for baseline air conditioning and liquid over-feeding operations .ASHRAE Transaction,1995( II ):1072 - 1076.
  • 10Mei, V C, et al. Experimental study of an R- 407C drop -in test on an off- the - shelf air conditioner with a counter-cross- flow evaporator.ASHRAE Transaction, 1998( I ):833 - 837.

共引文献29

同被引文献20

  • 1刘建,魏文建,丁国良,王凯建.对具有复杂流路布置的翅片管换热器的性能仿真与分析[J].化工学报,2005,56(1):47-52. 被引量:24
  • 2郑钢.使用R407C冷媒的翅片管冷凝器的计算机模拟[J].建筑热能通风空调,2005,24(1):18-21. 被引量:1
  • 3Aganda A A,Coney J E R,Sheppard C G W.Airflow maldistribution and the performance of a packaged air conditioning unit evaporator.Applied Thermal Engineering,2000,20(6):515-528.
  • 4Amgad.Effect of airflow maldistribution on pressure drop and thermal performance of heat exchangers in residential heat pump systems.ASHRAE Transaction,2003,109(1):9-14.
  • 5Wang C C,Jiang J Y,Lai C C,et al.Effect of circuit arrangement on the performance of air cooled condensers.International Journal of Refrigeration,1999,22(6):275-282.
  • 6J H Lee,S W Bae,K H Bang,et al.Experimental and numerical research on condenser performance for R22 and R407C refrigerants.International Journal of Refrigeration,2002,25(3):372-382.
  • 7S D Goldstein.A mathematically complete analysis of plate fin heat exchangers.ASHRAE Transaction,1983,89(2A):447-470.
  • 8Y T Ge,R Cropper.Performance evaluations of air-cooled condensers using pure and mixture refrigerants by four-section lumped modeling methods.Applied Thermal Engineering,2005,25(10):1549-1564.
  • 9Ellison P R,Crewick F A,Fischer F K,et al.A computer model for air-cooled refrigerant condenser with specified refrigerant circuiting.ASHRAE Transaction,1981,87(1):1106-1124.
  • 10A A Aganda,J E R Coney,et al.A comparison of the predicted and experimental heat transfer performance of a finned tube evaporator.Applied Thermal Engineering,2000,20(6):499-513.

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