Equilibrium CO2 solubility in the aqueous mixture of MAE and AEEA: Experimental study and development of modified thermodynamic model

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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


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