Zinc rejection from leachate solutions of industrial solid waste — effects of pressure and concentration on nanofiltration membrane performance
The treatment by nanofiltration of real solutions of industrial solid waste leachate using the charged Nanomax-50 membrane, largely used in industrial water treatment, was investigated. The retention of zinc, present in coercive quantities, was studied according to the experimental parameters. The r...
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description | The treatment by nanofiltration of real solutions of industrial solid waste leachate using the charged Nanomax-50 membrane, largely used in industrial water treatment, was investigated. The retention of zinc, present in coercive quantities, was studied according to the experimental parameters. The results show that zinc retention varied from 96 to 99%, depending on the composition of solution and operating conditions. At work pH (pH = 5.0), zinc was at 99.99% in the form of Zn
2+ (Cheaqs v. L20.1, a program for calculating chemical equilibria in aquatic systems, RIVM, Bilthoven, The Netherlands,-2004); a better retention (99%) was obtained with low energy. Thus, the optimal transmembrane pressure was 5 bar in the case of a 75 ppm solution. At low concentration (3.99 ppm), the retention decreased when the pressure exceeded 8 bar. These results differ from the majority of those presented in previous works regarding metal ion nanofiltration. At
P = 5 bar and when the concentration increased (from 75 to 559 ppm), the repulsion phenomenon became less important due to a higher interaction between membrane and metal ions, and consequently the latter was retained less (98%). Duly noted here is the influence of ionic strength related to the solution concentration on zinc rejection, which was found weak. |
doi_str_mv | 10.1016/j.desal.2008.03.006 |
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2+ (Cheaqs v. L20.1, a program for calculating chemical equilibria in aquatic systems, RIVM, Bilthoven, The Netherlands,-2004); a better retention (99%) was obtained with low energy. Thus, the optimal transmembrane pressure was 5 bar in the case of a 75 ppm solution. At low concentration (3.99 ppm), the retention decreased when the pressure exceeded 8 bar. These results differ from the majority of those presented in previous works regarding metal ion nanofiltration. At
P = 5 bar and when the concentration increased (from 75 to 559 ppm), the repulsion phenomenon became less important due to a higher interaction between membrane and metal ions, and consequently the latter was retained less (98%). Duly noted here is the influence of ionic strength related to the solution concentration on zinc rejection, which was found weak.</description><identifier>ISSN: 0011-9164</identifier><identifier>EISSN: 1873-4464</identifier><identifier>DOI: 10.1016/j.desal.2008.03.006</identifier><identifier>CODEN: DSLNAH</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Charged membrane ; Chemical engineering ; Exact sciences and technology ; Industrial use water ; Medium composition ; Membrane separation (reverse osmosis, dialysis...) ; Nanofiltration ; Pollution ; Water treatment and pollution ; Zinc leachate solution</subject><ispartof>Desalination, 2009-04, Vol.239 (1), p.58-65</ispartof><rights>2008 Elsevier B.V.</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c395t-e92674ef70ca135fdc44708bfcbd200697a3c0c759f40ed4eb05407fd5b8a2ae3</citedby><cites>FETCH-LOGICAL-c395t-e92674ef70ca135fdc44708bfcbd200697a3c0c759f40ed4eb05407fd5b8a2ae3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0011916409000216$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21296509$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Belkhouche, Nasr-Eddine</creatorcontrib><creatorcontrib>Didi, Mohamed Amine</creatorcontrib><creatorcontrib>Taha, Samir</creatorcontrib><creatorcontrib>Farès, Naïma Ben</creatorcontrib><title>Zinc rejection from leachate solutions of industrial solid waste — effects of pressure and concentration on nanofiltration membrane performance</title><title>Desalination</title><description>The treatment by nanofiltration of real solutions of industrial solid waste leachate using the charged Nanomax-50 membrane, largely used in industrial water treatment, was investigated. The retention of zinc, present in coercive quantities, was studied according to the experimental parameters. The results show that zinc retention varied from 96 to 99%, depending on the composition of solution and operating conditions. At work pH (pH = 5.0), zinc was at 99.99% in the form of Zn
2+ (Cheaqs v. L20.1, a program for calculating chemical equilibria in aquatic systems, RIVM, Bilthoven, The Netherlands,-2004); a better retention (99%) was obtained with low energy. Thus, the optimal transmembrane pressure was 5 bar in the case of a 75 ppm solution. At low concentration (3.99 ppm), the retention decreased when the pressure exceeded 8 bar. These results differ from the majority of those presented in previous works regarding metal ion nanofiltration. At
P = 5 bar and when the concentration increased (from 75 to 559 ppm), the repulsion phenomenon became less important due to a higher interaction between membrane and metal ions, and consequently the latter was retained less (98%). Duly noted here is the influence of ionic strength related to the solution concentration on zinc rejection, which was found weak.</description><subject>Applied sciences</subject><subject>Charged membrane</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>Industrial use water</subject><subject>Medium composition</subject><subject>Membrane separation (reverse osmosis, dialysis...)</subject><subject>Nanofiltration</subject><subject>Pollution</subject><subject>Water treatment and pollution</subject><subject>Zinc leachate solution</subject><issn>0011-9164</issn><issn>1873-4464</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNqFkc2KFDEUhYM4YDv6BG6y0V2VN5VUqmrhQgb_YMCNs5lNSCU3mCaVtEmV4s5XGPAJfRLT3aNLhUDI4Ts3l3MIecagZcDky31rsejQdgBjC7wFkA_Ijo0Db4SQ4iHZATDWTEyKR-RxKfv67CbOd-Tu1kdDM-7RrD5F6nJaaEBtPusVaUlhO8qFJkd9tFtZs9fhqHtLv-lSmV8_flJ0rvpP1CFjKVtGqqOlJkWDcc36NLueqGNyPvxRFlzmrCPSA2aX8qIr_oRcOB0KPr2_L8nN2zefrt431x_ffbh6fd0YPvVrg1MnB4FuAKMZ7501Qgwwzs7MtsYgp0FzA2boJycArcAZegGDs_086k4jvyQvznMPOX3ZsKxq8cVgCHWftBXVARcD78b_gkxAx6UUFeRn0ORUSkanDtkvOn9XDNSxJ7VXp57UsScFXNU9q-v5_XhdjA6u5mF8-WvtalGyh6lyr84c1lC-esyqGI81MOtzDV_Z5P_5z2-1GK7Z</recordid><startdate>20090401</startdate><enddate>20090401</enddate><creator>Belkhouche, Nasr-Eddine</creator><creator>Didi, Mohamed Amine</creator><creator>Taha, Samir</creator><creator>Farès, Naïma Ben</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7UA</scope></search><sort><creationdate>20090401</creationdate><title>Zinc rejection from leachate solutions of industrial solid waste — effects of pressure and concentration on nanofiltration membrane performance</title><author>Belkhouche, Nasr-Eddine ; Didi, Mohamed Amine ; Taha, Samir ; Farès, Naïma Ben</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c395t-e92674ef70ca135fdc44708bfcbd200697a3c0c759f40ed4eb05407fd5b8a2ae3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Applied sciences</topic><topic>Charged membrane</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>Industrial use water</topic><topic>Medium composition</topic><topic>Membrane separation (reverse osmosis, dialysis...)</topic><topic>Nanofiltration</topic><topic>Pollution</topic><topic>Water treatment and pollution</topic><topic>Zinc leachate solution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Belkhouche, Nasr-Eddine</creatorcontrib><creatorcontrib>Didi, Mohamed Amine</creatorcontrib><creatorcontrib>Taha, Samir</creatorcontrib><creatorcontrib>Farès, Naïma Ben</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Water Resources Abstracts</collection><jtitle>Desalination</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Belkhouche, Nasr-Eddine</au><au>Didi, Mohamed Amine</au><au>Taha, Samir</au><au>Farès, Naïma Ben</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Zinc rejection from leachate solutions of industrial solid waste — effects of pressure and concentration on nanofiltration membrane performance</atitle><jtitle>Desalination</jtitle><date>2009-04-01</date><risdate>2009</risdate><volume>239</volume><issue>1</issue><spage>58</spage><epage>65</epage><pages>58-65</pages><issn>0011-9164</issn><eissn>1873-4464</eissn><coden>DSLNAH</coden><abstract>The treatment by nanofiltration of real solutions of industrial solid waste leachate using the charged Nanomax-50 membrane, largely used in industrial water treatment, was investigated. The retention of zinc, present in coercive quantities, was studied according to the experimental parameters. The results show that zinc retention varied from 96 to 99%, depending on the composition of solution and operating conditions. At work pH (pH = 5.0), zinc was at 99.99% in the form of Zn
2+ (Cheaqs v. L20.1, a program for calculating chemical equilibria in aquatic systems, RIVM, Bilthoven, The Netherlands,-2004); a better retention (99%) was obtained with low energy. Thus, the optimal transmembrane pressure was 5 bar in the case of a 75 ppm solution. At low concentration (3.99 ppm), the retention decreased when the pressure exceeded 8 bar. These results differ from the majority of those presented in previous works regarding metal ion nanofiltration. At
P = 5 bar and when the concentration increased (from 75 to 559 ppm), the repulsion phenomenon became less important due to a higher interaction between membrane and metal ions, and consequently the latter was retained less (98%). Duly noted here is the influence of ionic strength related to the solution concentration on zinc rejection, which was found weak.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.desal.2008.03.006</doi><tpages>8</tpages></addata></record> |
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subjects | Applied sciences Charged membrane Chemical engineering Exact sciences and technology Industrial use water Medium composition Membrane separation (reverse osmosis, dialysis...) Nanofiltration Pollution Water treatment and pollution Zinc leachate solution |
title | Zinc rejection from leachate solutions of industrial solid waste — effects of pressure and concentration on nanofiltration membrane performance |
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