Study on the Interaction Coefficients in PR Equation with vdW Mixing Rules for HFC and HC Binary Mixtures
暂无分享,去创建一个
Peng Hu | Zeshao Chen | P. Hu | Zeshao Chen | Jian-Xin Chen | Jian-Xin Chen
[1] Youngil Kim,et al. Vapor–liquid equilibria for pentafluoroethane + propane and difluoromethane + propane systems over a temperature range from 253.15 to 323.15 K , 2003 .
[2] G. Morrison,et al. Interaction coefficients for 15 mixtures of flammable and non-flammable components , 1995 .
[3] B. Lee,et al. Vapor–Liquid Equilibria of CFC Alternative Refrigerant Mixtures: Trifluoromethane (HFC-23)+Difluoromethane (HFC-32), Trifluoromethane (HFC-23)+Pentafluoroethane (HFC-125), and Pentafluoroethane (HFC-125)+1,1-Difluoroethane (HFC-152a) , 2000 .
[4] D. Richon,et al. Vapor–liquid equilibrium data for the CO2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa , 2002 .
[6] R. Stryjek,et al. Vapor-liquid equilibria for difluoromethane (R32) + and pentafluoroethane (R125) + 1,1,1,3,3,3-hexafluoropropane (R236fa) at 303.2 and 323.3 K , 1999 .
[7] B. Lee,et al. Phase Equilibria of CFC Alternative Refrigerant Mixtures: 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea)+Difluoromethane (HFC-32), +1,1,1,2-Tetrafluoroethane (HFC-134a), and +1,1-Difluoroethane (HFC-152a) , 2001 .
[8] B. Lee,et al. Measurement of Vapor−Liquid Equilibria for the Binary Mixture of Propane (R-290) + Isobutane (R-600a) , 2004 .
[9] B. Lee,et al. Phase equilibria of hfc mixtures : Binary mixtures of trifluoromethane + 1,1-difluoroethane and trifluoromethane + 1,1,1-trifluoroethane at 283.15 and 293.15 K , 2002 .
[10] Min Young Jung,et al. Vapor−Liquid Equilibria for the Difluoromethane (HFC-32) + Pentafluoroethane (HFC-125) System , 2001 .
[11] Yukihiro Higashi,et al. Vapor−Liquid Equilibrium (VLE) Properties for the Binary Systems Propane (1) + n-Butane (2) and Propane (1) + Isobutane (3) , 2005 .
[12] Jong Sung Lim,et al. Phase Equilibria of CFC Alternative Refrigerant Mixtures: Binary Systems of Isobutane + 1,1,1,2-Tetrafluoroethane, + 1,1-Difluoroethane, and + Difluoromethane , 1999 .
[13] Chang Nyeon Kim,et al. Vapor−Liquid Equilibria for the Difluoromethane (HFC-32) + 1,1,1,2-Tetrafluoroethane (HFC-134a) System , 1997 .
[14] L. Fedele,et al. Vapor+Liquid Equilibrium Measurements and Correlation of the Binary Refrigerant Mixtures Difluoromethane (HFC-32)+1,1,1,2,3,3-Hexafluoropropane (HFC-236ea) and Pentafluoroethane (HFC-125)+1,1,1,2,3,3-Hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K , 2000 .
[15] Ki Hyun Park,et al. Phase Equilibria of CFC Alternative Refrigerant Mixtures. Binary Systems of Trifluoromethane (HFC-23) + 1,1,1,2-Tetrafluoroethane (HFC-134a) and Trifluoromethane (HFC-23) + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) at 283.15 and 293.15 K , 2001 .
[16] Jong Sung Lim,et al. Phase Equilibria of Chlorofluorocarbon Alternative Refrigerant Mixtures , 1999 .
[17] M. Kleiber. Vapor-liquid equilibria of binary refrigerant mixtures containing propylene or R134a , 1994 .
[18] D. Peng,et al. A New Two-Constant Equation of State , 1976 .
[19] Y. Higashi. Vapor−Liquid Equilibrium, Coexistence Curve, and Critical Locus for Pentafluoroethane + 1,1,1-Trifluoroethane (R125/R143a) , 1999 .
[20] C.-N. Kim,et al. Vapor–Liquid Equilibrium of HFC-32/134a And HFC-125/134a Systems , 1999 .
[21] Hwayong Kim,et al. Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Systems , 2005 .
[22] B. Lee,et al. Vapor–Liquid Equilibrium Measurements for Binary Mixtures Containing 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea)1 , 2000 .
[23] L. Fedele,et al. Isothermal VLE measurements for the binary mixtures HFC-134a + HFC-245fa and HC-600a + HFC-245fa , 2001 .