Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Effect of impurities in captured CO2 on liquid-vapor equilibrium

Ahmad, M.[Mohammad], Gernert, J.[Johannes], Wilbers, E.[Erwin]
Fluid Phase Equilib. 2014, 363, 149-155
ABSTRACT
The capture of large amounts of CO2from power plants and other large CO2 point sources has become relevant within the concept to mitigate CO2 emissions via carbon capture and storage. The objective of this study was to investigate the impact of some major impurities found in the CO2 stream captured frompower plants and other large point sources on the liquid vapor phase change compared to pure CO2. The study contributes to a better understanding of how and within which boundary conditions transmissionof impure CO2 from an emission and capture point to a storage location can be realized. A set up was constructed to provide the experimental data needed to trace the phase diagrams of the CO2-impurities mixtures. The data show an expansion of the liquid-vapor phase envelope and a start ofboiling (in liquid) or condensation (in vapor) at relatively higher pressures. The experimental data were later used to assess the capabilities of three mixture models: the Soave- Redlich-Kwong cubic equationof state, the GERG-2008 model, and the EOS-CG model.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 N2 nitrogen
3 O2 oxygen
4 Ar argon
5 CH4 methane
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
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 2; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Closed cell (Static) method
  • 10
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 10
  • POMD
  • 1
  • 3
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 3; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Closed cell (Static) method
  • 11
  • POMD
  • 1
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 11
  • POMD
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 4; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Closed cell (Static) method
  • 10
  • POMD
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 11
  • POMD
  • 5
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 1; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Closed cell (Static) method
  • 11
  • POMD
  • 5
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 11