欢迎登录材料期刊网

材料期刊网

高级检索

目前国际上已商业化使用或提出的潜在的环保工质,大多数为氢氟烃(HFC)混合物,利用状态方程描述混合工质热力性质时,交互作用系数是重要参数之一.本文应用Peng-Robinson状态方程对多种HFC二元混合物的气液相平衡(vapor-liquid equilibrium,VLE)实验数据进行了回归,得到了相应混合物的交互作用系数.提出了交互作用系数新关联式,结果表明所得到的交互作用系数能很好的应用于描述HFC混合物气液相平衡性质,计算精度可以满足工程应用的需要.

参考文献

[1] Chueh P L;Prausnitz J M .Vapor-Liquid Equilibria at High Pressures, Vapor-Phase Fugacity Coefficients in Nonpolar and Quantum-Gas Mixtures[J].Industrial and Engineering Chemistry Research,1967,6(04):492-498.
[2] 童景山.流体的热物理性质[M].北京:中国石化出版社,1996
[3] Peng D Y;Robinsion D B .A New Two-Constant Equation of State[J].Industrial and Engineering Chemistry Research,1976,15(01):59-64.
[4] MCLINDEN M O;Lemmon E W;Jacobsen R T .Thermodynamic Properties for the Alternative Refrigerants[J].International Journal of Refrigeration-Revue Internationale du Froid,1998,21(04):322-338.
[5] 段远源,王忠伟.氢氟烃混合物气液相平衡研究进展[J].流体机械,2004(02):28-30,23.
[6] Lee M J;Sun H C .Thermodynamic Property Predictions for Refrigerant Mixtures[J].Industrial and Engineering Chemistry Research,1992,31(04):12121216.
[7] Sand J R;Fischer S K;Jones J A .Carnahan-Starling-DeSantis and Lee-Kesler-Plocker Interaction Coefficients for Several Binary Mixtures of Ozone-Safe Refrigerants[J].International Journal of Refrigeration-Revue Internationale du Froid,1994,17(02):123-129.
[8] Weber L A;Silva A M .Design of a High-Pressure Ebulliometer, with Vapor-Liquid Equilibrium Results for the Systems CHF2CI+CF3-CH3 and CF3-CH2F+CH2F2[J].International Journal of Theoretical Physics,1996,17(04):873-888.
[9] Strom K H U;Gren U B .A Study of Vapour-Liquid Equilibria for the Binary Mixtures HCFC22/CFC114,HCFC22/HCFC142b and HCFC22/152a[J].Canadian Journal of Chemical Engineering,1993,71(06):940-947.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%