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Comparison of Activated Carbon and Iron Impregnated Activated Carbon Derived From Golbasi Lignite To Remove Cyanide From Water

dc.authorid Depci, Tolga/0000-0001-9562-8068
dc.authorscopusid 23767083500
dc.authorwosid Depci, Tolga/A-2867-2016
dc.contributor.author Depci, Tolga
dc.date.accessioned 2025-05-10T16:46:25Z
dc.date.available 2025-05-10T16:46:25Z
dc.date.issued 2012
dc.department T.C. Van Yüzüncü Yıl Üniversitesi en_US
dc.department-temp Yuzuncu Yil Univ, Fac Engn Architecture, Dept Min Engn, TR-65080 Van, Turkey en_US
dc.description Depci, Tolga/0000-0001-9562-8068 en_US
dc.description.abstract The ability of lignite-activated carbon (LAC) and iron-impregnated activated carbon (FeAC) obtained from Golbasi lignite to remove cyanide ions from aqueous solution by adsorption was researched and compared with each other. The same process was applied also with commercial activated carbons which are in both granular (CAC-1) and powder forms (CAC-2). The morphologies, structures and properties of the activated carbons were determined by BET, XRD, XRF, SEM, zeta meter and magnetometer, respectively. The effects of various experimental parameters, such as initial cyanide concentration, pH, adsorbent type and particle size were researched in a batch adsorption technique at a temperature of 25 degrees C. BET surface area of LAC is determined as 921 m(2)/g. The obtained magnetic activated carbon has high surface area of 667 m(2)/g with 19 wt.% Fe3O4 coated and perfect magnetic separation performance. Langmuir model was found to be the best representative for cyanide-adsorption. The maximum monolayer adsorption capacities of LAC and FeAC are 60.18 mg/g and 67.82 mg/g at pH values of 7-7.5 and 64.10 mg/g and 68.02 mg/g at pH values of 10-10.5, respectively. Kinetic evaluation indicated that the cyanide adsorption onto the obtained activated carbons followed the pseudo-second order rate reaction. The diffusion-controlled kinetic models on the cyanide-adsorbent system showed that the removal rate was controlled not only by intraparticle diffusion but also by film diffusion. All experimental results point out that the LAC and FeAC are viable candidates for the removal of cyanide from water and wastewater. (C) 2011 Elsevier B.V. All rights reserved. en_US
dc.description.woscitationindex Science Citation Index Expanded
dc.identifier.doi 10.1016/j.cej.2011.12.003
dc.identifier.endpage 478 en_US
dc.identifier.issn 1385-8947
dc.identifier.issn 1873-3212
dc.identifier.scopus 2-s2.0-84856348188
dc.identifier.scopusquality Q1
dc.identifier.startpage 467 en_US
dc.identifier.uri https://doi.org/10.1016/j.cej.2011.12.003
dc.identifier.uri https://hdl.handle.net/20.500.14720/1142
dc.identifier.volume 181 en_US
dc.identifier.wos WOS:000301087000051
dc.identifier.wosquality Q1
dc.institutionauthor Depci, Tolga
dc.language.iso en en_US
dc.publisher Elsevier Science Sa en_US
dc.relation.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject Cyanide en_US
dc.subject Magnetic Activated Carbon en_US
dc.subject Non-Linear Regression en_US
dc.subject Turkish Lignite en_US
dc.title Comparison of Activated Carbon and Iron Impregnated Activated Carbon Derived From Golbasi Lignite To Remove Cyanide From Water en_US
dc.type Article en_US

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