In this work, the eSAFT-VR Mie EoS is applied to watermethanesalt and watercarbon dioxidesalt mixtures. Initially, the EoS parameters for non-electrolyte systems are fitted and temperature dependent waterion interaction parameters are introduced to improve the behavior of the model at high temperatures. Furthermore, a database of experimental methane and carbon dioxide solubility in single-salt aqueous solutions was compiled and is given in SI units as Supporting Information. Four different parameterization schemes regarding gasion dispersion energy have been pursued in this work, namely: (a) setting the gasion dispersion energy parameter to zero, (b) using the SAFT-VR Mie combining rules without any binary interaction parameters, (c) using the predictive Hudson -McCoubrey combining rules and last but not least (d) fitting to experimental solubility of gases in aqueous solutions of single salts. The fitting approach yields an average deviation from experimental data of about 10%, compared to more than 25% for the other approaches. However, despite the great overall deviations of the predictive methods, there are cases where they yield excellent results, such as methane solubility in aqueous NaCl solutions. The salting-out behavior predicted with the fitted parameters is excellent at room temperature but deviate from experimental data at higher temperatures. Finally, the model is applied to gas solubility in mixed salt solutions, without further adjustable parameters and the predictions are in excellent agreement with experiments. Overall, eSAFT-VR Mie shows great potential for gas solubility calculations under salinity.