Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

High pressure vapor-liquid equilibria for binary carbon dioxide and protic ionic liquid based on ethanolamines + butanoic acid

Alcantara, Murilo L., Carvalho, Marlon L. de, Alvarez, Victor H., Ferreira, Pedro I.S., Paredes, Marcio L.L., Cardozo-Filho, Lucio, Silva, Andressa K., Liao, Luciano M., Pires, Carlos A.M., Mattedi, Silvana
Fluid Phase Equilib. 2018, 460, 162-174
ABSTRACT
High pressure phase equilibria data were measured for 3 protic ionic liquids and CO2. The studied ILs were based on ethanolamine cations and butanoate anions: 2-hydroxyethylammonium butanoate [2HEA][Bu]; N-methyl-2-hydroxyethylammonium butanoate [m-2HEA][Bu] and N-ethyl-2- hydroxyethylammonium butanoate [e 2HEA][Bu]. This ILs were chosen in order to study the effect of the alkyl growth, from central amine, on CO2 solubility. Water content, FT-IR, 1H and 13C NMR analysis were performed on samples. Charge profiles were also estimated by the geometrical and energetic optimization of ILs structures. The data were correlated with three models: Carvalho and Coutinho predictive empirical correlation; Peng-Robinson EoS; Peng-Robinson EoS coupled with Wong-Sandler/ NRTL or two parameters mixing rules; Predictive ternary PC-SAFT model. The results showed that the increase of the carbon chain length, bonded to the amine group, promotes higher CO2 solubility at medium-high pressures but lower CO2 solubility at low pressures. Henry's law constants were also compared to other ILs ones.
Compounds
# Formula Name
1 C6H15NO3 2-hydroxy ethylammonium butanoate
2 C7H17NO3 N-methyl-2-hydroxyethylammonium butanoate
3 C8H19NO3 N-ethyl-2-hydroxyethylammonium butanoate
4 CO2 carbon dioxide
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
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 24
  • POMD
  • 4
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 25
  • POMD
  • 4
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 20