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Please use this identifier to cite or link to this item: https://doi.org/10.1080/01457631003603949
DC FieldValue
dc.titleAdsorption parameter and heat of adsorption of activated carbon/HFC-134a pair
dc.contributor.authorLoh, W.S.
dc.contributor.authorKumja, M.
dc.contributor.authorRahman, K.A.
dc.contributor.authorNg, K.C.
dc.contributor.authorSaha, B.B.
dc.contributor.authorKoyama, S.
dc.contributor.authorEl-Sharkawy, I.I.
dc.date.accessioned2014-06-17T06:10:49Z
dc.date.available2014-06-17T06:10:49Z
dc.date.issued2010-01
dc.identifier.citationLoh, W.S., Kumja, M., Rahman, K.A., Ng, K.C., Saha, B.B., Koyama, S., El-Sharkawy, I.I. (2010-01). Adsorption parameter and heat of adsorption of activated carbon/HFC-134a pair. Heat Transfer Engineering 31 (11) : 910-916. ScholarBank@NUS Repository. https://doi.org/10.1080/01457631003603949
dc.identifier.issn01457632
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/59385
dc.description.abstractThis article presents the adsorption isotherms of HFC-134a and activated carbon Maxsorb III measured using the constant-volume-variable-pressure method. The adsorption isotherms cover temperature ranges from 293 to 338 K and pressures up to 0.7 MPa. The trends of the experimental isotherms for activated carbon are found to be identical in all cases with previous studies except that the vapor uptake is slightly higher. The adsorption characteristic of the Dubinin-Ashtakov equation has been regressed from the experimental isotherms data and the maximum specific uptake is 2.15 kg of adsorbate adsorbed per kilogram of activated carbon. The heat of adsorption, which is concentration and temperature dependent, has also been extracted from the experiments. Copyright © Taylor and Francis Group, LLC 2010.
dc.description.urihttp://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1080/01457631003603949
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentMECHANICAL ENGINEERING
dc.contributor.departmentCIVIL ENGINEERING
dc.description.doi10.1080/01457631003603949
dc.description.sourcetitleHeat Transfer Engineering
dc.description.volume31
dc.description.issue11
dc.description.page910-916
dc.description.codenHTEND
dc.identifier.isiut000277485300002
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