Publication:
Removal of Lead (II) from Aqueous Solution by Batch Adsorption on Various Inexpensive Adsorbents Using Experimental Design

dc.authorscopusid56366528300
dc.authorscopusid57090524600
dc.authorscopusid17436339900
dc.authorscopusid55360859700
dc.contributor.authorSalman, T.
dc.contributor.authorAydın Temel, F.
dc.contributor.authorTuran, N.G.
dc.contributor.authorOrhan Ardali, Y.
dc.date.accessioned2020-06-21T13:41:39Z
dc.date.available2020-06-21T13:41:39Z
dc.date.issued2015
dc.departmentOndokuz Mayıs Üniversitesien_US
dc.department-temp[Salman] Taylan, Department of Environmental Engineering, Ondokuz Mayis Üniversitesi, Samsun, Turkey; [Aydın Temel] Fulya, Department of Environmental Engineering, Ondokuz Mayis Üniversitesi, Samsun, Turkey; [Turan] Nurdan Gamze, Department of Environmental Engineering, Ondokuz Mayis Üniversitesi, Samsun, Turkey; [Orhan Ardali] Yuksel-Yuksel-Yueksel, Department of Environmental Engineering, Ondokuz Mayis Üniversitesi, Samsun, Turkeyen_US
dc.description.abstractThis study focuses on adsorption of lead (II) using various inexpensive adsorbents, such as dried activated sludge, diatomite, and sepiolite, through the batch process. The data were evaluated using three types of isotherm models to determine the design parameters. Additionally, the adsorption kinetics was analyzed using first- and second-order kinetics. The regression coefficient (R2) quantitatively evaluates the correlation between the experimental data and the predicted responses. The Box–Behnken design of three factors at three levels was used to determine the important parameters affecting the adsorption of lead (II) by different adsorbents and the results showed that pH, initial concentration, and type of adsorbent in these experiments are the important factors. The Freundlich isotherm model fits for all adsorbents, as indicated by the R2 values of 0.992, 0.997, and 0.997 for Pb2+ adsorption onto dried activated sludge, diatomite, and sepiolite at pH 3, respectively. The adsorption capacity was found as 19.85, 25.24, and 33.37 (mg g−1) for dried activated carbon, diatomite, and sepiolite, respectively. The pseudo-second-order model fits the experimental data very well. For kinetic studies, the R2 values for Pb2+ are 0.989, 0.992, and 0.997 for dried activated sludge, diatomite, and sepiolite, respectively. The obtained R2 values suggest good adjustments to the experimental results since these values indicate that 99.72% of the variability in the response could be explained by the models. © 2014 Balaban Desalination Publications. All rights reserved.en_US
dc.identifier.doi10.1080/19443994.2014.951073
dc.identifier.endpage1575en_US
dc.identifier.issn1944-3994
dc.identifier.issn1944-3986
dc.identifier.issue6en_US
dc.identifier.scopus2-s2.0-84944276855
dc.identifier.scopusqualityQ3
dc.identifier.startpage1566en_US
dc.identifier.urihttps://doi.org/10.1080/19443994.2014.951073
dc.identifier.volume56en_US
dc.identifier.wosWOS:000362832300016
dc.identifier.wosqualityQ4
dc.language.isoenen_US
dc.publisherBellwether Publishing, Ltd.en_US
dc.relation.ispartofDesalination and Water Treatmenten_US
dc.relation.journalDesalination and Water Treatmenten_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectAdsorption Kineticsen_US
dc.subjectExperimental Designen_US
dc.subjectInexpensive Adsorbentsen_US
dc.subjectIsothermsen_US
dc.titleRemoval of Lead (II) from Aqueous Solution by Batch Adsorption on Various Inexpensive Adsorbents Using Experimental Designen_US
dc.typeArticleen_US
dspace.entity.typePublication

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