In the designing stage for the unit operation of gas sweetening, the models to determine acid gases solubility are limited and highly complex. Therefore, the aim of this study is to analyse the reliability of a simpler model, the Modified Kent-Eisenberg (KE) Model to predict the solubility of hydrogen sulphide in methyldiethanolamine (MDEA) solution. In this work, Modified Kent-Eisenberg model is re-derived for a different ternary system. The system involved in this research work is a ternary system of H2S-MDEA-H2O system; hence, a different set of ionic dissociation equations of the species involved are used for the derivation of equations to further modify the KE model prior to its evaluation
The solubilities of CO2 and H2S mixtures in methyldiethanolamine aqueous solutions were investigated...
International audienceModelling of CO 2 solubility in aqueous solutions of potassium lysinate (LysK)...
Haloalkaliphilic biological desulfurization has been recognized as a promising technology due to its...
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...
In this work, 72 new experimental solubility data points for H(2)S and CO(2) mixtures in aqueous N-m...
Alkanolamine processes are used in the industry to remove acid gases, like CO2, H2S and other sulphu...
In gas sweetening, acid gases such as CO2 and/or H2S are usually removed by chemical absorption th...
The hydrogen sulfide (H2S) absorption capacity of a 70 wt% aqueous methyldiethanolamine (MDEA) solut...
International audienceAqueous amine solutions are widely used in the industry for acid gas removal. ...
Natural gas, synthesis gas, and flue gas typically contain a large number of impurities (e.g., acidi...
International audienceNatural gas always contains contaminants such as acid gases (CO2 and H2S), mer...
The solubilities of CO2 and H2S mixtures in methyldiethanolamine aqueous solutions were investigated...
International audienceModelling of CO 2 solubility in aqueous solutions of potassium lysinate (LysK)...
Haloalkaliphilic biological desulfurization has been recognized as a promising technology due to its...
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...
In this work, 72 new experimental solubility data points for H(2)S and CO(2) mixtures in aqueous N-m...
Alkanolamine processes are used in the industry to remove acid gases, like CO2, H2S and other sulphu...
In gas sweetening, acid gases such as CO2 and/or H2S are usually removed by chemical absorption th...
The hydrogen sulfide (H2S) absorption capacity of a 70 wt% aqueous methyldiethanolamine (MDEA) solut...
International audienceAqueous amine solutions are widely used in the industry for acid gas removal. ...
Natural gas, synthesis gas, and flue gas typically contain a large number of impurities (e.g., acidi...
International audienceNatural gas always contains contaminants such as acid gases (CO2 and H2S), mer...
The solubilities of CO2 and H2S mixtures in methyldiethanolamine aqueous solutions were investigated...
International audienceModelling of CO 2 solubility in aqueous solutions of potassium lysinate (LysK)...
Haloalkaliphilic biological desulfurization has been recognized as a promising technology due to its...