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

Phase Behavior, Densities and Isothermal Compressibility of CO2 + Pentane + Acetone Ternary System in Various Phase Regions

Chen, J., Wu, W.[Weize], Liu, Z.[Zhimin], Jiang, T.[Tao], Huang, Y.[Ying], Yang, G.[Guanying], Han, B.[Buxing]
J. Chem. Eng. Data 2004, 49, 3, 537-543
ABSTRACT
The phase behavior and critical parameters of the CO2 (1) + pentane (2) + acetone (3) ternary system with different compositions were determined experimentally, and their densities were measured in both the subcritical and supercritical (SC) regions. The isothermal compressibility (KT) at some typical conditions was calculated using the density data. It is demonstrated that the density is sensitive to pressure as the pressure approaches the critical point of the mixtures, i.e, KT is large and increases sharply. KT also increases significantly as pressure approaches the dew point or the bubble point at other compositions close to the critical composition. However, KT is very small and is not sensitive to pressure well above the dew point or the bubble point. When the composition is far from the critical composition, KT has small values, and the effect of pressure on KT is very small, even near the phase-separation point.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C5H12 pentane
3 C3H6O acetone
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
  • 3
  • 2
  • 1
  • Critical pressure, kPa ; Liquid
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • DIRECT:UFactor:32
  • 15
  • POMD
  • 3
  • 2
  • 1
  • Critical temperature, K ; Liquid
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • VISOBSU:UFactor:8
  • 15
  • POMD
  • 3
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 14
  • POMD
  • 3
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Gas
  • Mole fraction - 1; Gas
  • Gas
  • Liquid
  • Closed cell (Static) method
  • 6
  • POMD
  • 3
  • 2
  • 1
  • 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)
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • OTHPVT:UFactor:16
  • 278
  • POMD
  • 3
  • 2
  • 1
  • 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)
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • OTHPVT:UFactor:16
  • 379
  • POMD
  • 3
  • 2
  • 1
  • 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)
  • Solvent: Amount ratio of component to other component of binary solvent - 2; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • OTHPVT:UFactor:16
  • 306