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dc.contributor.authorDinçer, Ali Rıza
dc.contributor.authorAral, İbrahim Feda
dc.date.accessioned2022-05-11T14:10:30Z
dc.date.available2022-05-11T14:10:30Z
dc.date.issued2021
dc.identifier.issn2083-4772
dc.identifier.issn2083-4810
dc.identifier.urihttps://doi.org/10.24425/aep.2021.136448
dc.identifier.urihttps://hdl.handle.net/20.500.11776/5421
dc.description.abstractThis study investigated the Octyl Phenol Ethoxylate (OPE) removal potentials of raw and treated industrial treatment sludges (ITS) at different pH. Experiments were conducted in a set of 500 ml Erlenmeyer flasks, into which OPE solutions of 300 ml with different initial concentrations (50-300 mu g/l) were added into. Adsorption of Octyl Phenol Ethoxylate from an aqueous solution into ITS105 (T=105 degrees C), ITS300 (T=300 degrees C), ITS600 (T=600 degrees C) and ITS450 (pyrolyzed, T=450 degrees C) was carried out at a room temperature. The OPE adsorption rate increase in the treatment sludge processed at 600 degrees C. As opposed to the sludge treated at 105 degrees C, the adsorption rate decreased as the concentration increased. The reason for this was that the porous structure was degraded at 600 degrees C, and the surface charge balance was disrupted. ITS300 had a lower adsorption capacity for Octyl Phenol Ethoxylate removal than ITS105, ITS600 and ITS450 (pyrolyzed). The treatment sludge pyrolyzed at 450 degrees C conformed with the Freundlich isotherm at pH 4 (R-2=0.94) and pH 7 (R-2=0.89). The treatment sludge heat-treated at 600 degrees C conformed with the Freundlich isotherm at pH 4 (R-2=0.97), pH 7 (R-2=0.98) and pH 10 (R-2=0.99). Additionally, for ITS600, the Brunauer, Emmett and Teller (BET) isotherm was valid at neutral pH. The OPE adsorption coefficient for ITS600 at pH 4 and pH 7 was calculated as 1.05 L/mu g and 1.083 L/mu g, respectively. According to the BET isotherm (for ITS600) the q m values at pH 4 and pH 7 were respectively 8.21 mu g/g and 2.92 mu g/g. The temperature of the adsorption value obtained with the Temkin isotherm showed that the interaction between the OPE and the adsorbent substances was not a chemical or ionic interaction but probably a physical interaction.en_US
dc.language.isoengen_US
dc.publisherPolska Akad Nauk, Polish Acad Sciences, Inst Environ Eng Pasen_US
dc.identifier.doi10.24425/aep.2021.136448
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectWaste Sludgeen_US
dc.subjectAdsorptionen_US
dc.subjectOctyl Phenol Ethoxylateen_US
dc.subjectPyrolyzed sludgeen_US
dc.subjectActivated-Sludgeen_US
dc.subjectBisphenol-Aen_US
dc.subjectAdsorptionen_US
dc.subjectBiocharen_US
dc.subjectWateren_US
dc.subjectAdsorbenten_US
dc.subjectIsothermen_US
dc.subjectBiosorptionen_US
dc.subjectProductsen_US
dc.subjectKineticsen_US
dc.titleRemoval of Octyl Phenol Ethoxylate (OPE) Using Processed and Unprocessed Industrial Biological Waste Sludgeen_US
dc.typearticleen_US
dc.relation.ispartofArchives of Environmental Protectionen_US
dc.departmentFakülteler, Çorlu Mühendislik Fakültesi, İnşaat Mühendisliği Bölümüen_US
dc.departmentFakülteler, Çorlu Mühendislik Fakültesi, Çevre Mühendisliği Bölümüen_US
dc.identifier.volume47en_US
dc.identifier.issue1en_US
dc.identifier.startpage53en_US
dc.identifier.endpage60en_US
dc.institutionauthorDinçer, Ali Rıza
dc.institutionauthorAral, İbrahim Feda
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.authorscopusid7004045635
dc.authorscopusid57212405947
dc.identifier.wosWOS:000627901100007en_US
dc.identifier.scopus2-s2.0-85102489498en_US


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