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Adsorption kinetics of phenol and 3-nitrophenol from aqueous solutions on conventional and novel carbons

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dc.contributor.author Ioannou, Z en
dc.contributor.author Simitzis, J en
dc.date.accessioned 2014-03-01T01:29:48Z
dc.date.available 2014-03-01T01:29:48Z
dc.date.issued 2009 en
dc.identifier.issn 0304-3894 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/19345
dc.subject 3-Nitrophenol en
dc.subject Adsorption en
dc.subject Carbons en
dc.subject Kinetics en
dc.subject Phenol en
dc.subject.classification Engineering, Environmental en
dc.subject.classification Engineering, Civil en
dc.subject.classification Environmental Sciences en
dc.subject.other 3-Nitrophenol en
dc.subject.other Adsorption kinetics en
dc.subject.other Adsorption of phenol en
dc.subject.other Aqueous solutions en
dc.subject.other Carbonaceous materials en
dc.subject.other Commercial activated carbons en
dc.subject.other Experimental data en
dc.subject.other Intra-particle diffusion en
dc.subject.other Intraparticle diffusion models en
dc.subject.other Kinetic models en
dc.subject.other Macro pores en
dc.subject.other Mercury porosimetry en
dc.subject.other Mesopore en
dc.subject.other Nitrophenols en
dc.subject.other Novolac resin en
dc.subject.other Olive stones en
dc.subject.other Per unit en
dc.subject.other Pore diffusion coefficients en
dc.subject.other Power functions en
dc.subject.other Power model en
dc.subject.other Pseudo second order en
dc.subject.other Pseudo-first-order en
dc.subject.other SEM-EDAX en
dc.subject.other Square roots en
dc.subject.other Activated carbon en
dc.subject.other Biomass en
dc.subject.other Carbonaceous adsorbents en
dc.subject.other Chemicals removal (water treatment) en
dc.subject.other Diffusion en
dc.subject.other Function evaluation en
dc.subject.other Mercury (metal) en
dc.subject.other Phenolic resins en
dc.subject.other Phenols en
dc.subject.other Resins en
dc.subject.other Solutions en
dc.subject.other Adsorption en
dc.subject.other 3 nitrophenol en
dc.subject.other activated carbon en
dc.subject.other adsorbent en
dc.subject.other carbon en
dc.subject.other mercury en
dc.subject.other phenol en
dc.subject.other resin en
dc.subject.other activated carbon en
dc.subject.other adsorption en
dc.subject.other aqueous solution en
dc.subject.other kinetics en
dc.subject.other phenol en
dc.subject.other adsorption kinetics en
dc.subject.other aqueous solution en
dc.subject.other article en
dc.subject.other biomass en
dc.subject.other controlled study en
dc.subject.other diffusion en
dc.subject.other energy dispersive X ray spectroscopy en
dc.subject.other scanning electron microscopy en
dc.subject.other spectroscopy en
dc.subject.other waste water management en
dc.subject.other Adsorption en
dc.subject.other Carbon en
dc.subject.other Diffusion en
dc.subject.other Kinetics en
dc.subject.other Microscopy, Electron, Scanning en
dc.subject.other Nitrophenols en
dc.subject.other Phenol en
dc.subject.other Solutions en
dc.subject.other Spectrophotometry, Ultraviolet en
dc.subject.other Time Factors en
dc.subject.other Waste Disposal, Fluid en
dc.subject.other Water Pollutants, Chemical en
dc.subject.other Water Purification en
dc.title Adsorption kinetics of phenol and 3-nitrophenol from aqueous solutions on conventional and novel carbons en
heal.type journalArticle en
heal.identifier.primary 10.1016/j.jhazmat.2009.06.098 en
heal.identifier.secondary http://dx.doi.org/10.1016/j.jhazmat.2009.06.098 en
heal.language English en
heal.publicationDate 2009 en
heal.abstract Carbonaceous adsorbents prepared from olive stones biomass and novolac resin, as well as a commercial activated carbon for comparison reasons, have been examined for the removal of phenol and 3-nitrophenol from aqueous solutions. All carbonaceous adsorbents; have been characterized by SEM-EDAX analysis and mercury porosimetry. The experimental data were examined according to the following kinetic models: pseudo first order, pseudo second order. Natarajan and Khalaf, Elovich, power function equations and intraparticle diffusion. By plotting the amount of adsorbate (phenol or 3-nitrophenol) adsorbed per unit mass of adsorbent b(t), versus the square root of time, four regions can be distinguished (A, B, C and D). By applying all the previously described models it is concluded that: (a) the intraparticle diffusion model is valid for the B and C region, whereas macropore diffusion and mesopore diffusion, respectively, take place. The pore diffusion coefficient, D for each carbonaceous material was calculated and indicated that the adsorption is controlled by diffusion, (b) the power model for the adsorption of phenol on each of the three carbonaceous materials is acceptable only for the C region and (c) the pseudo second order for the adsorption of 3-nitrophenol on each of the three carbonaceous materials is acceptable for the C region. (C) 2009 Elsevier B.V. All rights reserved. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName Journal of Hazardous Materials en
dc.identifier.doi 10.1016/j.jhazmat.2009.06.098 en
dc.identifier.isi ISI:000271165100130 en
dc.identifier.volume 171 en
dc.identifier.issue 1-3 en
dc.identifier.spage 954 en
dc.identifier.epage 964 en


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