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

Measurement and Modeling of Enthalpy of Solution of Carbon Dioxide in Aqueous Solutions of Diethanolamine at Temperatures of (322.5 and 372.9) K and Pressures up to 3 MPa

Arcis, H.[Hugues], Ballerat-Busserolles, K.[Karine], Rodier, L.[Laurence], Coxam, J. -Y.[Jean-Yves]
J. Chem. Eng. Data 2012, 57, 3, 840-855
ABSTRACT
The enthalpies of solution (?solH) of carbon dioxide (CO2) in two aqueous solutions (w = 0.1500 and w = 0.3000) of diethanolamine (DEA) have been measured at two temperatures ((322.5 and 372.9) K) and pressures up to 3 MPa. Measurements were carried out by a flow calorimetric technique using a custom-made flow-mixing unit combined with a SETARAM C-80 isothermal differential heat-flux calorimeter. Enthalpies of solution of CO2 (?solH) have been obtained as function of loading, ? (moles CO2/mol amine). Influences of temperature, pressure, and absorbent composition have been discussed. Solubility data of the gas into the different absorbent (s) were derived from the enthalpic data. The experimental enthalpies of solution (?solH) of carbon dioxide (CO2) in the two aqueous solutions of diethanolamine have been compared with data derived from a rigorous thermodynamic model of phase equilibria based on a ? approach. Interaction parameters were chosen to be adjustable parameters in this model and were fitted to vapor liquid equilibrium data. Several formulations for the amine protonation and carbamate formation equilibrium constants have been tested. The different contributions to the enthalpy of solution of CO2 in aqueous solutions of DEA have been analyzed.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C4H11NO2 diethanolamine
3 H2O water
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
  • 2
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 2; Liquid
  • Liquid
  • Vibrating tube method
  • 12
  • POMD
  • 2
  • 1
  • 3
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Liquid
  • Flow calorimetry
  • 141
  • POMD
  • 2
  • 1
  • 3
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Liquid
  • Flow calorimetry
  • 124