A fundamental equation of state for cis-1,3,3,3-tetrafluoropropene (R-1234ze(Z))

Abstract A fundamental equation of state is presented for cis-1,3,3,3-tetrafluoropropene (R-1234ze(Z)). The equation of state is expressed explicitly in the Helmholtz energy with independent variables of temperature and density. The equation of state is based on experimental data for the critical parameters, vapor pressures, densities of the liquid and vapor phases, and sound speeds in the vapor phase. All thermodynamic properties can be derived as derivatives of the Helmholtz energy. The equation is valid for temperatures from 273 K to 430 K and for pressures up to 6 MPa. The estimated uncertainties of properties calculated from the equation are 0.15% in vapor pressures, 0.4% in vapor densities, 0.2% in liquid densities, and 0.05% in the vapor phase sound speeds. The equation exhibits reasonable extrapolation behavior in regions away from the experimental data.

[1]  J. S. Brown,et al.  Measurements and Correlations of cis-1,3,3,3-Tetrafluoroprop-1-ene (R1234ze(Z)) Saturation Pressure , 2014 .

[2]  A. Cavallini,et al.  The fluorinated olefin R-1234ze(Z) as a high-temperature heat pumping refrigerant , 2009 .

[3]  K. Joback,et al.  ESTIMATION OF PURE-COMPONENT PROPERTIES FROM GROUP-CONTRIBUTIONS , 1987 .

[4]  Y. Higashi,et al.  Measurements of PvT properties, vapor pressures, and critical parameters for low GWP refrigerant R-1234ze(z). , 2013 .

[5]  Gabriele Raabe,et al.  Molecular modeling of fluoropropene refrigerants. , 2012, The journal of physical chemistry. B.

[6]  R. Akasaka,et al.  A fundamental equation of state for trifluoromethyl methyl ether (HFE-143m) and its application to refrigeration cycle analysis , 2012 .

[7]  Eric W. Lemmon,et al.  An International Standard Formulation for the Thermodynamic Properties of 1,1,1-Trifluoroethane (HFC-143a) for Temperatures From 161 to 450 K and Pressures to 50 MPa , 2000 .

[8]  Eric W. Lemmon,et al.  Thermodynamic Properties of trans-1,3,3,3-tetrafluoropropene [R1234ze(E)]: Measurements of Density and Vapor Pressure and a Comprehensive Equation of State , 2010 .

[9]  R. Akasaka New Fundamental Equations of State with a Common Functional Form for 2,3,3,3-Tetrafluoropropene (R-1234yf) and trans-1,3,3,3-Tetrafluoropropene (R-1234ze(E)) , 2011 .

[10]  W. Wagner,et al.  Equations of State for Technical Applications. III. Results for Polar Fluids , 2003 .

[11]  B. Taylor,et al.  CODATA recommended values of the fundamental physical constants: 2006 | NIST , 2007, 0801.0028.

[12]  Roland Span,et al.  Equations of State for Technical Applications. I. Simultaneously Optimized Functional Forms for Nonpolar and Polar Fluids , 2003 .

[13]  Roland Span,et al.  Short Fundamental Equations of State for 20 Industrial Fluids , 2006 .

[14]  Katsuyuki Tanaka,et al.  Critical Parameters and Saturated Densities in the Critical Region for trans-1,3,3,3-Tetrafluoropropene (HFO-1234ze(E)) , 2010 .

[15]  Eric W. Lemmon,et al.  Thermodynamic Properties of Propane. III. A Reference Equation of State for Temperatures from the Melting Line to 650 K and Pressures up to 1000 MPa , 2009 .

[16]  Roland Span,et al.  Multiparameter Equations of State: An Accurate Source of Thermodynamic Property Data , 2000 .

[17]  Ryo Akasaka,et al.  A Reliable and Useful Method to Determine the Saturation State from Helmholtz Energy Equations of State , 2008 .

[18]  W. Wagner,et al.  A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .

[19]  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 .