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

Solubility Measurement and Thermodynamic Properties Calculation for Several CO2 + Ether Absorbent Systems

Li, Yun, You, Yanhong, Huang, Weijia, Yang, Jie
J. Chem. Eng. Data 2019, 64, 3, 1020-1028
ABSTRACT
Six physical absorbents with the ether groups were selected for CO2 absorption: tetraethylene glycol dimethyl ether (TEGDME), diethylene glycol monohexyl ether, 2-butoxyethyl ether, triethylene glycol monobutyl ether, ethylene glycol dibutyl ether, and dipropylene glycol dimethyl ether (DPGDME). CO2 solubilities in these absorbents were measured at 273.15 K and 283.15 K, and 0 {1.2 MPa. Henry!|s constants of these CO2 + ether absorbent systems were calculated and analyzed at 273.15 K. The ether group is found more powerful than the methylene group, and the ethyl group is more effective than the hydroxyl group to improve the absorption ability of the absorbents. A lower temperature tends to facilitate the absorption process by increasing the absorption ability. Henry!|s constants and mass solubilities of the ether absorbents were compared with those of the ionic liquids, common solvents, and other absorbents. TEGDME and DPGDME are potential absorbents according to the evaluation in both mole and mass fraction. The thermodynamic properties, such as entropy, enthalpy, and Gibbs free energy of solution, for CO2 + the ether absorbent systems were calculated and discussed for potential development of corresponding CO2 capture processes.
Compounds
# Formula Name
1 C10H22O5 2,5,8,11,14-pentaoxapentadecane
2 CO2 carbon dioxide
3 C10H22O3 2-(2-hexyloxyethoxy)ethanol
4 C12H26O3 5,8,11-trioxapentadecane
5 C10H22O4 triethylene glycol monobutyl ether
6 C8H18O3 2-methoxy-1-(2-methoxy-1-methylethoxy)propane
7 C10H22O2 5,8-dioxadodecane
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
  • 7
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 2
  • POMD
  • 1
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16
  • POMD
  • 3
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16
  • POMD
  • 4
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16
  • POMD
  • 5
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16
  • POMD
  • 7
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16
  • POMD
  • 6
  • 2
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 16