Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/1498
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dc.contributor.authorKundu, Madhusree-
dc.contributor.authorBandyopadhyay, S S-
dc.date.accessioned2011-07-13T04:58:06Z-
dc.date.available2011-07-13T04:58:06Z-
dc.date.issued2007-
dc.identifier.citationChem. Eng. Comm., 194:1138–1159, 2007en
dc.identifier.urihttp://doi.dx.org/10.1080/00986440701244341-
dc.identifier.urihttp://hdl.handle.net/2080/1498-
dc.descriptionCopyright for this article belongs to Taylor & Francisen
dc.description.abstractDesign of gas treating processes requires the knowledge of vapour-liquid equilibrium behaviour of (acid gas + aqueous alkanolamine) system. Present study is focused on thermodynamics and associated non-ideal behaviour of binary MEA + H2O, DEA + H2O, and MDEA + H2O systems, which is required to predict the vapour-liquid equilibrium of acid gases such as CO2, H2S over aqueous alkanolamine solutions. Determination of binary interaction parameters, analytical prediction of infinite dilution activity coefficient, heats of solution at infinite dilution, the excess Gibbs free energy and excess enthalpy for non-ideal alkanolamine-water systems are the objectives of this study.en
dc.format.extent648869 bytes-
dc.format.mimetypeapplication/pdf-
dc.language.isoen-
dc.publisherTaylor & Francisen
dc.subjectActivity coefficienten
dc.subjectAlkanolamineen
dc.subjectCO2en
dc.subjectInfinite dilutionen
dc.subjectMEDAen
dc.titleThermodynamics of Alkanolamine + Water Systemen
dc.typeArticleen
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