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

dc.contributor.authorPandey, D.
dc.contributor.authorMondal, M.K.
dc.date.accessioned2020-11-18T05:41:47Z
dc.date.available2020-11-18T05:41:47Z
dc.date.issued2020-11-01
dc.description.abstractIn 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.sponsorshipMinistry of Human Resource Developmenten_US
dc.identifier.issn03783812
dc.identifier.urihttps://idr-sdlib.iitbhu.ac.in/handle/123456789/912
dc.language.isoen_USen_US
dc.publisherElsevier B.V.en_US
dc.relation.ispartofseriesFluid Phase Equilibria;Vol. 522
dc.subject2-(methylamino)ethanolen_US
dc.subjectAminoethylethanolamineen_US
dc.subjectModified kent-eisenberg modelen_US
dc.subjectCO2 solubilityen_US
dc.subjectHeat of absorptionen_US
dc.titleEquilibrium CO2 solubility in the aqueous mixture of MAE and AEEA: Experimental study and development of modified thermodynamic modelen_US
dc.typeArticleen_US

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