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dc.contributor.authorGundogdu A.
dc.contributor.authorDuran C.
dc.contributor.authorSenturk H.B.
dc.contributor.authorSoylak M.
dc.contributor.authorOzdes D.
dc.contributor.authorSerencam H.
dc.contributor.authorImamoglu M.
dc.date.accessioned20.04.201910:49:12
dc.date.accessioned2019-04-20T21:44:36Z
dc.date.available20.04.201910:49:12
dc.date.available2019-04-20T21:44:36Z
dc.date.issued2012
dc.identifier.issn0021-9568
dc.identifier.urihttps://dx.doi.org/10.1021/je300597u
dc.identifier.urihttps://hdl.handle.net/20.500.12403/894
dc.description.abstractThe ability of activated carbon which was produced by chemical activation using zinc chloride from tea industry wastes (TIWAC) to adsorb phenol molecules from aqueous solution was tested by equilibrium, kinetic, and thermodynamic parameters. Phenol adsorption on TIWAC took place with a high yield at pH values in the range 4 to 8. The optimum contact period was observed as 4.0 h and from the adsorption graphs plotted as a function of time; it was established that phenol adsorption on TIWAC conformed more to a pseudosecond-order kinetic model. Additionally, it was determined that the adsorption rate is controlled by intraparticle diffusion as well as film diffusion. It was established that phenol adsorption on TIWAC can be better defined by the Langmuir adsorption model and its adsorption capacity was 142.9 mg·g-1 from the linear Langmuir equation. Temperature had an adverse effect on adsorption yield, and hence, the adsorption process was exothermic in our case. Moreover, increasing electrolyte concentration in the medium has a positive effect on adsorption yield. From the data obtained, it was concluded that the removal of phenol from aqueous solution by TIWAC produced from tea industry wastes with a very low cost took place with an extremely high performance. © 2012 American Chemical Society.en_US
dc.language.isoengen_US
dc.publisherAmerican Chemical Society
dc.relation.isversionof10.1021/je300597u
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectActivated carbon
dc.subjectChemical activation
dc.subjectChemicals removal (water treatment)
dc.subjectChlorine compounds
dc.subjectElectrolytes
dc.subjectKinetics
dc.subjectPhenols
dc.subjectSolutions
dc.subjectZinc chloride
dc.subjectAdsorption capacities
dc.subjectElectrolyte concentration
dc.subjectIntra-particle diffusion
dc.subjectLangmuir adsorption model
dc.subjectLow cost activated carbons
dc.subjectPseudo-second-order kinetic models
dc.subjectThermodynamic parameter
dc.subjectThermodynamic studies
dc.subjectAdsorption
dc.subjectActivated carbon
dc.subjectChemical activation
dc.subjectChemicals removal (water treatment)
dc.subjectChlorine compounds
dc.subjectElectrolytes
dc.subjectKinetics
dc.subjectPhenols
dc.subjectSolutions
dc.subjectZinc chloride
dc.subjectAdsorption capacities
dc.subjectElectrolyte concentration
dc.subjectIntra-particle diffusion
dc.subjectLangmuir adsorption model
dc.subjectLow cost activated carbons
dc.subjectPseudo-second-order kinetic models
dc.subjectThermodynamic parameter
dc.subjectThermodynamic studies
dc.subjectAdsorption
dc.titleAdsorption of phenol from aqueous solution on a low-cost activated carbon produced from tea industry waste: Equilibrium, kinetic, and thermodynamic studyen_US
dc.typearticleen_US
dc.relation.journalJournal of Chemical and Engineering Dataen_US
dc.contributor.departmentBayburt Universityen_US
dc.contributor.authorID16042269000
dc.contributor.authorID16042074800
dc.contributor.authorID16043586100
dc.contributor.authorID7006488616
dc.contributor.authorID25646623400
dc.contributor.authorID23100981600
dc.contributor.authorID55148345500
dc.identifier.volume57
dc.identifier.issue10
dc.identifier.startpage2733
dc.identifier.endpage2743
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US


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