dc.contributor.author |
Katsou, E |
en |
dc.contributor.author |
Malamis, S |
en |
dc.contributor.author |
Tzanoudaki, M |
en |
dc.contributor.author |
Haralambous, KJ |
en |
dc.contributor.author |
Loizidou, M |
en |
dc.date.accessioned |
2014-03-01T01:36:42Z |
|
dc.date.available |
2014-03-01T01:36:42Z |
|
dc.date.issued |
2011 |
en |
dc.identifier.issn |
0304-3894 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/21403 |
|
dc.subject |
Adsorption |
en |
dc.subject |
Desorption |
en |
dc.subject |
Lead |
en |
dc.subject |
Regeneration |
en |
dc.subject |
Zeolite |
en |
dc.subject |
Zinc |
en |
dc.subject.classification |
Engineering, Environmental |
en |
dc.subject.classification |
Engineering, Civil |
en |
dc.subject.classification |
Environmental Sciences |
en |
dc.subject.other |
4-cycle |
en |
dc.subject.other |
Adsorption process |
en |
dc.subject.other |
Aqueous solutions |
en |
dc.subject.other |
Desorption efficiency |
en |
dc.subject.other |
Desorption process |
en |
dc.subject.other |
Diffusion process |
en |
dc.subject.other |
Liquid medium |
en |
dc.subject.other |
Natural zeolites |
en |
dc.subject.other |
Regeneration |
en |
dc.subject.other |
Regeneration cycles |
en |
dc.subject.other |
Secondary effluent |
en |
dc.subject.other |
Treated wastewater |
en |
dc.subject.other |
Two stage |
en |
dc.subject.other |
Wastewater treatment system |
en |
dc.subject.other |
Adsorption |
en |
dc.subject.other |
Desorption |
en |
dc.subject.other |
Effluent treatment |
en |
dc.subject.other |
Effluents |
en |
dc.subject.other |
Lead |
en |
dc.subject.other |
Metal ions |
en |
dc.subject.other |
Wastewater |
en |
dc.subject.other |
Wastewater treatment |
en |
dc.subject.other |
Zinc |
en |
dc.subject.other |
Zinc compounds |
en |
dc.subject.other |
Lead removal (water treatment) |
en |
dc.subject.other |
lead |
en |
dc.subject.other |
metal ion |
en |
dc.subject.other |
potassium chloride |
en |
dc.subject.other |
zeolite |
en |
dc.subject.other |
zinc |
en |
dc.subject.other |
adsorption |
en |
dc.subject.other |
aqueous solution |
en |
dc.subject.other |
desorption |
en |
dc.subject.other |
lead |
en |
dc.subject.other |
reaction kinetics |
en |
dc.subject.other |
waste treatment |
en |
dc.subject.other |
wastewater |
en |
dc.subject.other |
zeolite |
en |
dc.subject.other |
zinc |
en |
dc.subject.other |
adsorption |
en |
dc.subject.other |
article |
en |
dc.subject.other |
controlled study |
en |
dc.subject.other |
desorption |
en |
dc.subject.other |
kinetics |
en |
dc.subject.other |
liquid culture |
en |
dc.subject.other |
regeneration |
en |
dc.subject.other |
waste water management |
en |
dc.subject.other |
waste water treatment plant |
en |
dc.subject.other |
water contamination |
en |
dc.subject.other |
Adsorption |
en |
dc.subject.other |
Diffusion |
en |
dc.subject.other |
Kinetics |
en |
dc.subject.other |
Lead |
en |
dc.subject.other |
Metals |
en |
dc.subject.other |
Models, Statistical |
en |
dc.subject.other |
Potassium Chloride |
en |
dc.subject.other |
Reproducibility of Results |
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.subject.other |
Zeolites |
en |
dc.subject.other |
Zinc |
en |
dc.title |
Regeneration of natural zeolite polluted by lead and zinc in wastewater treatment systems |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/j.jhazmat.2010.12.061 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/j.jhazmat.2010.12.061 |
en |
heal.language |
English |
en |
heal.publicationDate |
2011 |
en |
heal.abstract |
The aim of this work was to investigate the potential regeneration of natural zeolite which had been contaminated with lead and zinc contained in aqueous solutions, treated secondary effluent and primary treated wastewater. Several desorbing solutions were examined for the removal of Pb(II) and Zn(II) from zeolite and the highest desorption efficiency was obtained for 3 M KCl and 1 M KCl, respectively. The desorption process depended on the type and concentration of the desorbing solution, the metal being desorbed, the mineral selectivity towards the metal and the composition of the liquid medium where the adsorption process had taken place. Successive regeneration cycles resulted in the reduction of desorption efficiency by more than 50% after 9 and 4 cycles for lead and zinc, respectively. Kinetics examination showed that desorption was slower than adsorption, while metal ions which had been easily adsorbed were difficult to be desorbed. Adsorption was characterized by a three-stage diffusion process, while desorption followed a two-stage diffusion process. (C) 2010 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.2010.12.061 |
en |
dc.identifier.isi |
ISI:000291912200020 |
en |
dc.identifier.volume |
189 |
en |
dc.identifier.issue |
3 |
en |
dc.identifier.spage |
773 |
en |
dc.identifier.epage |
786 |
en |