Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Thermodynamic Properties of cis-1,1,1,4,4,4-Hexafluoro-2-butene (HFO-1336mzz(Z)): Measurements of the pT Property and Determinations of Vapor Pressures, Saturated Liquid and Vapor Densities, and Critical Parameters

Tanaka, K.[Katsuyuki], Akasaka, R.[Ryo], Sakaue, E.[Eiichi], Ishikawa, J.[Junichi], Kontomaris, K. K.[Konstantinos Kostas]
J. Chem. Eng. Data 2016, 61, 7, 2467-2473
ABSTRACT
In this work, comprehensive measurements of pT (pressure density temperature) properties of cis-1,1,1,4,4,4-hexafluoro-2-butene (HFO-1336mzz(Z)) were performed. Although this novel fluid has been proposed for various applications, including its use as a possible working fluid for organic Rankine cycle systems, reliable experimental data on its thermodynamic properties are scarcely available. In this work, the isochoric method was employed to obtain the properties of this fluid along 26 isochores for densities between 88 and 1295 kg*m 3, and 344 pT data points were obtained in the temperature range from 323 K (49.85 deg C) to 503 K (229.85 deg C) and at pressures up to 10 MPa. The data covered single-phase liquid and vapor regions, two-phase region, and supercritical region. The data in the critical region were correlated with a simple polynomial expression, which was used to determine the critical parameters analytically. The vapor pressures and the densities of the saturated liquid and vapor were obtained from an analysis of the single- and two-phase data. The experimental uncertainties in the measurements of temperatures, pressures, densities below 100 kg*m 3, and higher densities were estimated to be 0.028 K, 4 kPa, 0.6%, and 0.4%, respectively.
Compounds
# Formula Name
1 C4H2F6 (Z)-1,1,1,4,4,4-hexafluorobut-2-ene
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • Critical temperature, K ; Liquid
  • Liquid
  • Gas
  • Derived from PVT data
  • 1
  • POMD
  • 1
  • Critical pressure, kPa ; Liquid
  • Liquid
  • Gas
  • Derived from PVT data
  • 1
  • POMD
  • 1
  • Critical density, kg/m3 ; Liquid
  • Liquid
  • Gas
  • Derived from PVT data
  • 1
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 184
  • POMD
  • 1
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • ISOCHOR
  • 94
  • POMD
  • 1
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • ISOCHOR
  • 66