Application of electrodeionization (EDI) for removal of boron and silica from reverse osmosis (RU) permeate of geothermal water
dc.contributor.author | Arar, Ozgur | |
dc.contributor.author | Yuksel, Umran | |
dc.contributor.author | Kabay, Nalan | |
dc.contributor.author | Yuksel, Mithat | |
dc.date.accessioned | 2019-10-27T21:41:50Z | |
dc.date.available | 2019-10-27T21:41:50Z | |
dc.date.issued | 2013 | |
dc.department | Ege Üniversitesi | en_US |
dc.description.abstract | In this study, a hybrid process coupling reverse osmosis (RO) with electrodeionization (EDI) was investigated to remove boron and silica from geothermal water. The effect of applied voltage, feed flow rate, Na2SO4 concentration in the electrode compartments, membrane type and ion exchange resin bed configuration on the removal of boron and silica has been investigated. Geothermal water was obtained from the discharge lines in the geothermal plant of Izmir Geothermal Co. The RO system contained two parallel mounted brackish reverse osmosis membranes (BW-30-2540, Dow FilmTech). The RO permeate was collected using a single membrane configuration of operation by applying a 12 bar of pressure. The concentration of boron remaining in the permeate was 5.9 mg/L It was obtained that the concentration of boron decreased from 5.9 mg/L to 0.4 mg/L and silica from 03 mg Si/L to 0.1 mg Si/L with a layered bed configuration of EDI system when a 40 V of voltage was applied to the EDI system. The feed flow rate did not have any significant effect on the removal of boron and silica from the RO permeate of geothermal water by EDI. On the other hand, the transport of boron to the anode compartment of EDI system enhanced with increasing the feed flow rate. In a mixed bed EDI system, when the applied potential was 40 V. boron and silica concentrations in the product water were 1.60 mg B/L and 02 mg Si/L, respectively. The type of the membrane was found to be another important parameter on the removal of boron and silica from the RO permeate. (C) 2012 Elsevier B.V. All rights reserved. | en_US |
dc.description.sponsorship | Ege University Scientific Research ProjectEge University [EU-2009 FEN 081] | en_US |
dc.description.sponsorship | This study has been partially supported by Ege University Scientific Research Project (EU-2009 FEN 081). We would like to acknowledge Izmir Geothermal Co. for the support to perform RO tests in the geothermal field. The authors thank E. Yavuz for his support during RO tests in the field. We are especially grateful to Asahi Glass Co. (Japan), and Astom Co. (Japan) for sending us ion exchange membranes and Purolite Int Co. for ion exchange resins. | en_US |
dc.identifier.doi | 10.1016/j.desal.2012.10.001 | |
dc.identifier.endpage | 33 | en_US |
dc.identifier.issn | 0011-9164 | |
dc.identifier.issn | 1873-4464 | |
dc.identifier.issn | 0011-9164 | en_US |
dc.identifier.issn | 1873-4464 | en_US |
dc.identifier.startpage | 25 | en_US |
dc.identifier.uri | https://doi.org/10.1016/j.desal.2012.10.001 | |
dc.identifier.uri | https://hdl.handle.net/11454/46759 | |
dc.identifier.volume | 310 | en_US |
dc.identifier.wos | WOS:000316040000005 | en_US |
dc.identifier.wosquality | Q1 | en_US |
dc.indekslendigikaynak | Web of Science | en_US |
dc.language.iso | en | en_US |
dc.publisher | Elsevier | 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 | Electrodeionization | en_US |
dc.subject | Geothermal water | en_US |
dc.subject | Ion exchange membrane | en_US |
dc.subject | Reverse osmosis | en_US |
dc.subject | Silica | en_US |
dc.title | Application of electrodeionization (EDI) for removal of boron and silica from reverse osmosis (RU) permeate of geothermal water | en_US |
dc.type | Article | en_US |