Removal and recovery of boron from geothermal wastewater by selective ion-exchange resins - II. Field tests
dc.contributor.author | Kabay N. | |
dc.contributor.author | Yilmaz I. | |
dc.contributor.author | Yamac S. | |
dc.contributor.author | Yuksel M. | |
dc.contributor.author | Yuksel U. | |
dc.contributor.author | Yildirim N. | |
dc.contributor.author | Aydogdu O. | |
dc.contributor.author | Iwanaga T. | |
dc.contributor.author | Hirowatari K. | |
dc.date.accessioned | 2019-10-27T00:13:52Z | |
dc.date.available | 2019-10-27T00:13:52Z | |
dc.date.issued | 2004 | |
dc.department | Ege Üniversitesi | en_US |
dc.description.abstract | Column-mode removal of boron from geothermal wastewaters of the Kizildere Geothermal Power Station, Denizli, was performed using Diaion CRB 02 N-glucamine-type chelating resins. The resin was tested for 10 sorption-washing-elution-washing-regeneration-washing cycles in the geothermal field. The boron on the resin was eluted with 5% H2SO4 solution and the resin was regenerated with 4% NaOH solution prior to sorption of the following cycle. A certain decrease was observed in the break-through capacity of the resin after the first cycle. The decrease in resin capacity between cycles 2 and 7 was small, and it reached a plateau between cycles 7-10. A column-mode study was performed for the recovery ofboron from acidic eluates. For this, a weak base ion-exchange resin, Diaion WA 30, was used for separating boron from H2SO4 solutions collected in the field. © 2004 Elsevier B.V. All rights reserved. | en_US |
dc.description.sponsorship | New Energy and Industrial Technology Development Organization | en_US |
dc.description.sponsorship | This study was supported by NEDO (New Energy Development Organization, Japan). -- | en_US |
dc.identifier.doi | 10.1016/j.desal.2004.06.158 | |
dc.identifier.endpage | 438 | en_US |
dc.identifier.issn | 0011-9164 | |
dc.identifier.issn | 0011-9164 | en_US |
dc.identifier.issue | 01.Mar | en_US |
dc.identifier.scopusquality | Q1 | en_US |
dc.identifier.startpage | 427 | en_US |
dc.identifier.uri | https://doi.org/10.1016/j.desal.2004.06.158 | |
dc.identifier.uri | https://hdl.handle.net/11454/22521 | |
dc.identifier.volume | 167 | en_US |
dc.indekslendigikaynak | Scopus | en_US |
dc.language.iso | en | en_US |
dc.relation.ispartof | Desalination | 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 | Boron | en_US |
dc.subject | Boron recovery | en_US |
dc.subject | Chelating resins | en_US |
dc.subject | Diaion CRB 02 | en_US |
dc.subject | Diaion WA 30 | en_US |
dc.subject | Geothermal wastewater | en_US |
dc.subject | Ion exchange | en_US |
dc.title | Removal and recovery of boron from geothermal wastewater by selective ion-exchange resins - II. Field tests | en_US |
dc.type | Article | en_US |