In this work the electrolyte equation of state as developed previously for the system MDEA-H2O-CO2-CH4 was further developed for the system MDEA-H2O-H2S-CH4. With this thermodynamic equilibrium model the total solubility of hydrogen sulfide and the speciation in aqueous solutions of N-methyldiethanolamine can be described quantitatively. The model results were compared to experimental H2S solubility data in aqueous MDEA in absence and presence of methane respectively. The application of equation of state models for this kind of acid gas – amine systems is a rather new development in the literature. An accurate description is difficult for this kind of complex systems with significant amount of both molecular and ionic species present in the...
In the designing stage for the unit operation of gas sweetening, the models to determine acid gases ...
In gas sweetening, acid gases such as CO2 and/or H2S are usually removed by "chemical" absorption th...
International audienceNatural gas always contains contaminants such as acid gases (CO2 and H2S), mer...
In this work the electrolyte equation of state as developed previously for the system MDEA-H2O-CO2-C...
In this work, 72 new experimental solubility data points for H2S and CO2 mixtures in aqueous N-methy...
Alkanolamine processes are used in the industry to remove acid gases, like CO2, H2S and other sulphu...
In this work, 72 new experimental solubility data points for H(2)S and CO(2) mixtures in aqueous N-m...
In this study the electrolyte equation of state as proposed by Solbraa [E. Solbraa, Equilibrium and ...
The hydrogen sulfide (H2S) absorption capacity of a 70 wt% aqueous methyldiethanolamine (MDEA) solut...
Absorption data for COS and N2O in aqueous solutions of N-methyldiethanolamine (MDEA), ethylene glyc...
International audienceAqueous amine solutions are widely used in the industry for acid gas removal. ...
In the designing stage for the unit operation of gas sweetening, the models to determine acid gases ...
In gas sweetening, acid gases such as CO2 and/or H2S are usually removed by "chemical" absorption th...
International audienceNatural gas always contains contaminants such as acid gases (CO2 and H2S), mer...
In this work the electrolyte equation of state as developed previously for the system MDEA-H2O-CO2-C...
In this work, 72 new experimental solubility data points for H2S and CO2 mixtures in aqueous N-methy...
Alkanolamine processes are used in the industry to remove acid gases, like CO2, H2S and other sulphu...
In this work, 72 new experimental solubility data points for H(2)S and CO(2) mixtures in aqueous N-m...
In this study the electrolyte equation of state as proposed by Solbraa [E. Solbraa, Equilibrium and ...
The hydrogen sulfide (H2S) absorption capacity of a 70 wt% aqueous methyldiethanolamine (MDEA) solut...
Absorption data for COS and N2O in aqueous solutions of N-methyldiethanolamine (MDEA), ethylene glyc...
International audienceAqueous amine solutions are widely used in the industry for acid gas removal. ...
In the designing stage for the unit operation of gas sweetening, the models to determine acid gases ...
In gas sweetening, acid gases such as CO2 and/or H2S are usually removed by "chemical" absorption th...
International audienceNatural gas always contains contaminants such as acid gases (CO2 and H2S), mer...