Vapor-liquid equilibrium measurements for binary mixtures of R1234yf with R32, R125, and R134a
暂无分享,去创建一个
[1] Eric W. Lemmon,et al. A New Functional Form and New Fitting Techniques for Equations of State with Application to Pentafluoroethane (HFC-125) , 2005 .
[2] Eric W. Lemmon,et al. Thermodynamic Properties of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf): Vapor Pressure and p–ρ–T Measurements and an Equation of State , 2011 .
[3] Eric W. Lemmon,et al. Equations of State for Mixtures of R-32, R-125, R-134a, R-143a, and R-152a , 2004 .
[4] Katsuyuki Tanaka,et al. Thermodynamic properties of HFO-1234yf (2,3,3,3-tetrafluoropropene) , 2010 .
[5] R. Tillner-Roth,et al. An International Standard Equation of State for Difluoromethane (R-32) for Temperatures from the Triple Point at 136.34 K to 435 K and Pressures up to 70 MPa , 1997 .
[6] D. Peng,et al. A New Two-Constant Equation of State , 1976 .
[7] H. Baehr,et al. An International Standard Formulation for the Thermodynamic Properties of 1,1,1,2‐Tetrafluoroethane (HFC‐134a) for Temperatures from 170 K to 455 K and Pressures up to 70 MPa , 1994 .
[8] M. McLinden,et al. NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .