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
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceThe enthalpies of solution (Dsol H) of carbon dioxide (CO2) in two aqueous sol...
Homogenous densities in the liquid phase and VLE data were measured for the monoethanolamine and car...
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...
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...
High pressure vapor-liquid phase equilibrium data (P-T-x-y) for the binary mixtures of organic solve...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
Vapor–liquid equilibrium (VLE) data for the ternary system of carbon dioxide, ethanol and ethyl acet...
Often, power plants and industrial production plants \u2013 large point sources of CO2 - are situate...
Often, power plants and industrial production plants – large point sources of CO2 - are situated at ...
International audienceThe enthalpies of solution (Dsol H) of carbon dioxide (CO2) in two aqueous sol...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceThe enthalpies of solution (Dsol H) of carbon dioxide (CO2) in two aqueous sol...
Homogenous densities in the liquid phase and VLE data were measured for the monoethanolamine and car...
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...
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...
High pressure vapor-liquid phase equilibrium data (P-T-x-y) for the binary mixtures of organic solve...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
Vapor–liquid equilibrium (VLE) data for the ternary system of carbon dioxide, ethanol and ethyl acet...
Often, power plants and industrial production plants \u2013 large point sources of CO2 - are situate...
Often, power plants and industrial production plants – large point sources of CO2 - are situated at ...
International audienceThe enthalpies of solution (Dsol H) of carbon dioxide (CO2) in two aqueous sol...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceThe enthalpies of solution (Dsol H) of carbon dioxide (CO2) in two aqueous sol...