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混合工质R134a/R23焓-浓度图的绘制 被引量:5

Enthalpy-composition Diagram Plotting for R134a/R23
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摘要 使用PR(Peng-Robinson)方程对混合工质R134a/R23进行了气液相平衡的预测和焓、熵的计算。针对PR方程液相精度比较差的问题,对PR方程引入了修正系数,重新推导了逸度系数、余函数等表达式,并将计算结果与实验数据进行了比较。根据计算得到的R134a/R23热物性数据,绘制了工程上广泛使用的二元混合工质的焓-浓度图,为基于该混合工质的循环计算,提供了重要的基础数据。 R134a/R23 is a new refrigerant mixture and friendly to environment. In this research, the vapor-liquid equilibrium, enthalpy, and entropy of this mixture were calculated based on Peng-Robinson(PR)equation of state(EOS). To make PR equation more accurate, a correction factor was correlated and the fugacity coefficient and complementary function were recalculated. According to the result from this calculation, an enthalpy-composition diagram was plotted, which supplies important data for thermophysical properties and cycle analysis of R134a/R23.
作者 王雁 杜垲
出处 《制冷学报》 CAS CSCD 北大核心 2005年第2期51-56,共6页 Journal of Refrigeration
基金 国家自然科学基金资助项目(50476045)
关键词 R134A 浓度图 绘制 二元混合工质 PR方程 气液相平衡 热物性数据 修正系数 逸度系数 实验数据 计算结果 循环计算 基础数据 表达式 余函数 Pyrology enthalpy-composition diagram modified PR equation,mixed-refrigerant R134a/R23
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  • 1王怀信.R152a/R22新型混合工质状态工程:博士学位论文[M].天津:天津大学图书馆,1992..
  • 2John T. McMullan. Refrigeration and the environment- issues and strategies for the future.Int. J. Refrig,2002,25(1) :89~ 99.
  • 3M. O. McLinden, E.W.Lemmon,R. T. Jacobsen.Thermodynamic properties for the alternative refrigerants. Int. J. Refrig,1998,21(4) :322 ~ 338.
  • 4M. Nagel, K. Bier. Vapor - liquid equilibrium of ternary mixtures of the refrigerants R32, R125 and R134a. Int. J. Refrig,1995,18(8) :534 - 543.
  • 5D.R.Defibaugh, G. Morrison. Interaction coefficients for 15 mixtures of flammable and non - flammable components. Int. J. Refrig. 1995,18(8) :518 - 523.
  • 6Y. Higashi. Vapor - Liquid equilibrium, Coexistence curve, and critical locus for binary HFC - 32/HFC - 134a mixture. Int. J. of Thermophysics, 1995.16(5) ; 1175 - 1184.
  • 7J. V Widiatmo, etc. Liquid densities of altemative refrigerants blended with difluoromethane,Pentafluorothane,and 1,1,1,2-Tetrafluoroethane. J. Chem. Eng. Data. 1997,42(2) :270 - 277.
  • 8J. V. Widiamo,etc. Bubble- point pressures and saturated-liquid densities of binary HFC - 32 + HFC - 125 system. High temperature - High pressures, 1993,25(2) :677 - 683.
  • 9J. R. Sand, etc. Carnahan - Starling - DeSantis and Lee -Kesler- PI/ǒ .ckex interaction coefficients for several binary mixtures of ozone- safe refrigerants. Int. J.Refrig, 1994,17(2) : 123- 129.
  • 10R. Tillner- Roth. An experimental study of the thermodynamic properties of the refrigerant mixture: { 1,1,1,2- tetrafluoroethane(R134a) + 1, 1 - difluoroethane(R152a)}, J. Chem.Thermodynamics.1993,25:1419-1441.

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