Thermodynamics Research Center / ThermoML | International Journal of Thermophysics

Measurement of the (p, rho, T) Properties for Pure Hydrocarbons at Temperatures up to 600 K and Pressures up to 200 MPa

Ito, T.[Takayoshi], Nagata, Y.[Yoshikazu], Miyamoto, H.[Hiroyuki]
Int. J. Thermophys. 2014, 35, 9-10, 1636-1646
ABSTRACT
The data available for the thermodynamic properties of propane, n -butane, and isobutane at temperatures above 440 K are outdated and show significant discrepancies with each other. The ambiguity associated with these data could be limiting to the development of any understanding related to the effects of mixing of these substances with other materials such as CO 2 , ammonia, and non-flammable or lower-flammable HFC refrigerants. In this study, the (p, ? , T) properties of propane, n -butane, and isobutane were measured at temperatures ranging from (360 to 600) K and pressures ranging from (50 to 200) MPa. Precise measurements were carried out using a metal-bellows variable volumometer with a thermostatted air bath. The expanded uncertainties (k=2) in the temperature, pressure, and density measurements were estimated to be less than 5 mK, 0.02 MPa, and 0.88 kg * m -3 ( T=423 K, pless than100 MPa), 0.76 kg * m -3 ( T=423 K, p=100 MPa), 0.76 kg * m -3 ( Tgreater than423 K, pless than100 MPa), and 2.94 kg * m -3 ( Tgreater than423 K, p=100 MPa), respectively. The data obtained throughout this study were systematically compared with the calculated values derived from the available equations of state. These models agree well with the measured data at higher temperatures up to 600 K, demonstrating their suitability for an effective and precise examination of the mixing effects of potential alternative mixtures.
Compounds
# Formula Name
1 C4H10 butane
2 C4H10 2-methylpropane
3 C3H8 propane
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
  • 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)
  • Bellows volumetry
  • 66
  • POMD
  • 2
  • 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)
  • Bellows volumetry
  • 66
  • POMD
  • 3
  • 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)
  • Bellows volumetry
  • 66