Homogenous densities in the liquid phase and VLE data were measured for the monoethanolamine and carbon dioxide system. The density data were obtained on five isotherms in a temperature range between 313.15 K and 353.15 K at atmospheric pressure and for two different loadings. VLE data were acquired on the isotherms 333.15 K, 353.15 K, and 373.15 K. These new data enabled the adjustment of an e-NRTL Gibbs excess model in combination with a cubic equation of state for CO2 to describe the gas phase. The model represents the partial pressure of CO2 above carbon dioxide loaded pure monoethanolamine well.publishedVersio
The p-T phase diagrams of two ternary systems (CO2 + Ar + N2 and CO2 + Ar + H2) have been measured a...
Vapor-liquid equilibria (VLE) data of the ternary mixture of CO2 + N2 + CH4 were measured at the iso...
AbstractWithin the fight against global warming and the reduction of greenhouse-gases emission, rese...
Homogenous densities in the liquid phase and VLE data were measured for the monoethanolamine and car...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
Precise knowledge of vapor–liquid equilibrium (VLE) data of (CO2 + diluent) mixtures is crucial in t...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
Vapor-liquid equilibrium measurements for the binary system CO2 + CO are reported at 253, 273, 283 a...
Vapor-liquid equilibrium measurements for the binary system CO2 + CO are reported at 253, 273, 283 a...
Acknowledgements This work was part of an ongoing Joint Industrial Project (JIP) conducted jointly a...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
The p-T phase diagrams of two ternary systems (CO2 + Ar + N2 and CO2 + Ar + H2) have been measured a...
Vapor-liquid equilibria (VLE) data of the ternary mixture of CO2 + N2 + CH4 were measured at the iso...
AbstractWithin the fight against global warming and the reduction of greenhouse-gases emission, rese...
Homogenous densities in the liquid phase and VLE data were measured for the monoethanolamine and car...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
Precise knowledge of vapor–liquid equilibrium (VLE) data of (CO2 + diluent) mixtures is crucial in t...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
Vapor-liquid equilibrium measurements for the binary system CO2 + CO are reported at 253, 273, 283 a...
Vapor-liquid equilibrium measurements for the binary system CO2 + CO are reported at 253, 273, 283 a...
Acknowledgements This work was part of an ongoing Joint Industrial Project (JIP) conducted jointly a...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
The p-T phase diagrams of two ternary systems (CO2 + Ar + N2 and CO2 + Ar + H2) have been measured a...
Vapor-liquid equilibria (VLE) data of the ternary mixture of CO2 + N2 + CH4 were measured at the iso...
AbstractWithin the fight against global warming and the reduction of greenhouse-gases emission, rese...