A comprehensive thermodynamic model based on electrolyte nonrandom two-liquid
(eNRTL) equation in conjunction with PC-SAFT equation-of-state has been developed for …

Carbon dioxide (CO2) solubility in aqueous electrolyte solutions is of special interest for
carbon capture and storage and for biochemical processes, particularly at moderate to high …

A thermodynamic model based on the electrolyte NRTL activity coefficient equation and PC-
SAFT equation-of-state is developed for CO2 solubility in aqueous solutions of NaCl and …

Determining the solubility of non-hydrocarbon gases such as carbon dioxide (CO2) and
nitrogen (N2) in water and brine is one of the most controversial challenges in the oil and …

A thermodynamic model developed for CO 2 and H 2 S solubilities in aqueous MDEA
solution is extended to cover CO 2 and H 2 S solubilities in aqueous DIPA solution, aqueous …

Abstract The electrolyte SAFT-HR (eSAFT-HR) equation of state (EoS) has been
successfully applied to model the solubility of CO 2 in aqueous N-methyldiethanolamine …

Constructing an accurate model with the capability to accurately forecast gas solubility in
electrolyte solutions across diverse temperature, pressure, and salt concentration ranges …

The electrolyte version of SRK plus association equation of state (eSRK-CPA EoS) was
employed to correlate CO 2 solubility in MDEA aqueous solutions. The applied model …

Solvent influence and salt influence on CO 2 solubility are essential factors toward the
development of processes involving CO 2 conversion. In this work, the equation of state …

In this work, the eSAFT-VR Mie equation of state (EoS) is applied to water–methane–salt
and water–carbon dioxide–salt mixtures. Initially, the EoS parameters for nonelectrolyte …