dc.contributor.author |
Pandey, D. |
|
dc.contributor.author |
Mondal, M.K. |
|
dc.date.accessioned |
2020-11-18T05:41:47Z |
|
dc.date.available |
2020-11-18T05:41:47Z |
|
dc.date.issued |
2020-11-01 |
|
dc.identifier.issn |
03783812 |
|
dc.identifier.uri |
http://localhost:8080/xmlui/handle/123456789/912 |
|
dc.description.abstract |
In the present study, equilibrium solubility of CO2 was studied in the aqueous blend of 2-(methylamino)ethanol (MAE) and aminoethylethanolamine (AEEA). Total concentration of blend solution, weight fraction of AEEA in aqueous (MAE+AEEA) blend, temperature, and partial pressure of CO2 was varied from 10 to 30 wt %, 0.10 to 0.30, 298.15 to 323.15 K, and 8.11 to 20.67 kPa, respectively. Maximum loading 0.944 mol CO2/mol amine was occurred at 298.15 K, 20.27 kPa of CO2 partial pressure, 10 wt % total concentration with 0.30 wt fraction AEEA. The Kent-Eisenberg thermodynamic model was modified by incorporating newly introduced correction factor (Fk) to predict CO2 solubility in the aqueous blend of MAE+AEEA. Experimental data and model predicted data was in good agreement with each other. In addition, heat of CO2 absorption was also calculated for this amine blend and reported as -73.43 kJ/mol. © 2020 Elsevier B.V. |
en_US |
dc.description.sponsorship |
Ministry of Human Resource Development |
en_US |
dc.language.iso |
en_US |
en_US |
dc.publisher |
Elsevier B.V. |
en_US |
dc.relation.ispartofseries |
Fluid Phase Equilibria;Vol. 522 |
|
dc.subject |
2-(methylamino)ethanol |
en_US |
dc.subject |
Aminoethylethanolamine |
en_US |
dc.subject |
Modified kent-eisenberg model |
en_US |
dc.subject |
CO2 solubility |
en_US |
dc.subject |
Heat of absorption |
en_US |
dc.title |
Equilibrium CO2 solubility in the aqueous mixture of MAE and AEEA: Experimental study and development of modified thermodynamic model |
en_US |
dc.type |
Article |
en_US |