Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Solubilities of CO2 capture absorbents methyl benzoate, ethyl hexanoate and methyl heptanoate

Li, Yun, Liu, Qing, Huang, Weijia, Yang, Jie
J. Chem. Thermodyn. 2018, 127, 25-32
ABSTRACT
Carbon capture, utilization and sequestration technology is effective for carbon emissions reduction. The development of new absorbent seems to be one of the core components of carbon capture technology. In this paper, three esters, methyl heptanoate, ethyl hexanoate and methyl benzoate, were selected to determine CO2 solubilities at different temperatures ranging from 293.15 to 333.15 K, and pressures up to 1.2 MPa, using the isothermal synthesis method. The results showed that the absorbent with the straight-chain alkyl group was more effective for improving CO2 absorption capacity than the benzene group. Ethyl hexanoate showed slightly higher CO2 solubilities than its isomer methyl heptanoate. In addition, Henry's constant and thermodynamic properties such as solution enthalpy, solution entropy, solution Gibbs energy and solution heat capacity, were determined based on the measured data since the above properties are essential for designing an absorption process. Ethyl hexanoate is superior to the other two selected absorbents, common solvents, commercial absorbents, some physical absorbents, some polymeric absorbents and some ionic liquids, which indicates that it has potential value for CO2 capture technology. However, further studies will be necessary to assess the reliability of its industrial application.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C8H8O2 methyl benzoate
3 C8H16O2 ethyl hexanoate
4 C8H16O2 methyl heptanoate
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
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • volumetric method
  • 40
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • volumetric method
  • 40
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • volumetric method
  • 40