A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water system. The modified Redlich-Kwong equation of state with a new correlated cross-interaction parameter was used to calculate fugacity coefficients for the vapor phase. The dissolved oxygen followed Henry's law. A new expression was correlated from the experimental data to calculate Henry's constant of oxygen. The calculated results of equilibrium composition were compared with the available experimental data and those calculated by other models with different parameters. The comparison revealed that the new model is suitable for calculating both liquid and vapor compositions while the empirical method is only suitable for estimating the liquid com...
Oxygen gas is widely used as oxidant in a variety of industrial processes, such as hydrometallurgy, ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...
An unsymmetric thermodynamic model for the liquid-vapour equilibria in the H2O-CO2-NaCl and H2O-H2S-...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen–water syste...
An algorithm based on a modified Redlich-Kwong-Soaave equation of state is presented for solving the...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The UNIQUAC activity coefficient model and fugacity coefficient model of modified Redlich-Kwong pred...
The pure water phase equilibrium is calculated over a wide temperature range using the Gibbs ensembl...
Supercritical water oxidation (SCWO) is a new process of waste treatment. The use of water and oxyg...
This article is a part of the Sir John S. Rowlinson FestschriftInternational audience(P, x) vapor-li...
Oxygen gas is widely used as oxidant in a variety of industrial processes, such as hydrometallurgy, ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...
An unsymmetric thermodynamic model for the liquid-vapour equilibria in the H2O-CO2-NaCl and H2O-H2S-...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen-water syste...
A new thermodynamic model was presented to calculate the phase equilibria for the oxygen–water syste...
An algorithm based on a modified Redlich-Kwong-Soaave equation of state is presented for solving the...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The solubility of oxygen in pure liquid water was measured at a total pressure of about 100 kPa and ...
The UNIQUAC activity coefficient model and fugacity coefficient model of modified Redlich-Kwong pred...
The pure water phase equilibrium is calculated over a wide temperature range using the Gibbs ensembl...
Supercritical water oxidation (SCWO) is a new process of waste treatment. The use of water and oxyg...
This article is a part of the Sir John S. Rowlinson FestschriftInternational audience(P, x) vapor-li...
Oxygen gas is widely used as oxidant in a variety of industrial processes, such as hydrometallurgy, ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...
An unsymmetric thermodynamic model for the liquid-vapour equilibria in the H2O-CO2-NaCl and H2O-H2S-...