Solvent systems with liquid–liquid phase split
are potentially
interesting for designing advanced CO2 absorption processes.
However, physico-chemical data for assessing the benefits of such
processes are scarce in the literature. Therefore, a comprehensive
study on thermodynamic properties of such a system (N,N-diethyl-propylamine-triacetonediamine (EvA25)
+ H2O + CO2) was carried out in the present
work. More than 750 experimental data points of different physico-chemical
properties of that system were taken at temperatures between 20 and
120 °C, pressures of up to 75 bar, and CO2 loadings
of up to 3 mol/mol. They comprise data for liquid–liquid equilibrium,
CO2 solubility, liquidus temperature, chemical speciation,
heat capacity, density, viscosity, and vapor pressure. The liquid–liquid
phase split occurs at elevated temperatures and reduces the solubility
of CO2 in the solvent. The organic liquid phase contains
only little CO2, so that only the aqueous phase has to
be regenerated. Based on the new data, options for using the liquid–liquid
phase split in the design of CO2 absorption processes are
discussed.