Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

High pressure phase behavior for the binary mixture of valeronitrile, capronitrile and lauronitrile in supercritical carbon dioxide at temperatures from 313.2 to 393.2 K and pressures from 3.9 to 25.7 MPa

Kim, S.-H.[Sung-Hyun], Jang, Y.-S.[Yoon-Seok], Yoon, S.-D.[Soon-Do], Byun, H.-S.[Hun-Soo]
Fluid Phase Equilib. 2011, 312, 93-100
ABSTRACT
High pressure phase equilibria for the (carbon dioxide + valeronitrile), (carbon dioxide + capronitrile) and (carbon dioxide + lauronitrile) systems are measured in static apparatus at five temperatures of 313.2, 333.2, 353.2, 373.2 and 393.2 K and pressures up to 25.7 MPa. The three carbon dioxide + nitrile systems have continuous critical mixture curves that exhibit maximums in pressure at temperatures between the critical temperatures of carbon dioxide and nitriles. The solubility of valeronitrile, capronitrile and lauronitrile for the (carbon dioxide + nitriles) systems increases as the temperature increases at a fixed pressure. The (carbon dioxide + valeronitrile), (carbon dioxide + capronitrile) and (carbon dioxide + lauronitrile) systems exhibit type-I phase behavior. The experimental results for the (carbon dioxide + valeronitrile), (carbon dioxide + capronitrile) and (carbon dioxide + lauronitrile) systems are correlated with Peng-Robinson equation of state using a mixing rule including one and two adjustable parameters.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C6H11N hexanenitrile
3 C12H23N n-dodecanenitrile
4 C5H9N pentanenitrile
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
  • 4
  • 1
  • Critical pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 3
  • POMD
  • 4
  • 1
  • Critical pressure, kPa ; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 3
  • POMD
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Mole fraction - 4; Gas
  • Gas
  • Liquid
  • Visual Observation in Variable Volume Cell
  • 6
  • POMD
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 51
  • POMD
  • 1
  • 2
  • Critical pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 2
  • POMD
  • 1
  • 2
  • Critical pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 2
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 55
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Mole fraction - 1; Gas
  • Gas
  • Liquid
  • Visual Observation in Variable Volume Cell
  • 8
  • POMD
  • 1
  • 3
  • Critical pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 2
  • POMD
  • 1
  • 3
  • Critical pressure, kPa ; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 2
  • POMD
  • 1
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Visual Observation in Variable Volume Cell
  • 58
  • POMD
  • 1
  • 3
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Mole fraction - 1; Gas
  • Gas
  • Liquid
  • Visual Observation in Variable Volume Cell
  • 10