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

Accurate P-rho-T Data and Phase Boundary Determination for a Synthetic Residual Natural Gas Mixture

Cristancho, D. E.[Diego E.], Mantilla, I. D.[Ivan D.], Coy, L. A., Tibaduiza, A.[Andrea], Ortiz-Vega, D. O.[Diego O.], Hall, K. R.[Kenneth R.]
J. Chem. Eng. Data 2011, 56, 4, 826-832
ABSTRACT
This paper reports P-p-T data (P is pressure, p is mass density, T is temperature) for a ternary mixture that resembles a residual natural gas. The measurements utilized a high-pressure, single-sinker magnetic-suspension densimeter (MSD) from (200 to 450) K up to 170 MPa and an automated isochoric apparatus to determine densities and phase boundary data up to 20 MPa. The MSD technique yielded accurate data, with better than a 0.05 % estimated error at two standard deviations up to 200 MPa. The relative uncertainties for phase-boundary temperatures and pressures were 0.45 % and 0.04 %, respectively. The isochoric densities had essentially the same estimated error as the MSD data. The GERG-2004 and AGA8-DC92 equations of state compared well to the density data. A new method provided saturation densities from isochoric data with a relative uncertainty of 0.12 %, compensating the isochoric densities for cell and transfer-line volume changes and for mass interchange between the cell and the combination of the transfer line and pressure transducer.
Compounds
# Formula Name
1 CH4 methane
2 C2H6 ethane
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
  • 2
  • 3
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Mole fraction - 2; Gas
  • Mole fraction - 1; Gas
  • Gas
  • Liquid
  • ISOPVT
  • 7
  • POMD
  • 1
  • 2
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • ISOCHOR
  • 7
  • POMD
  • 1
  • 2
  • 3
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Mole fraction - 1; Fluid (supercritical or subcritical phases)
  • Mole fraction - 2; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Buoyancy - hydrostatic balance with magnetic suspension - one sinker
  • 40
  • POMD
  • 1
  • 2
  • 3
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Mole fraction - 1; Fluid (supercritical or subcritical phases)
  • Mole fraction - 2; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • ISOCHOR
  • 84