Kinetics of Zinc Recovery from Spent Pickling Effluents

This work has focused on the study of the kinetics of zinc removal from spent pickling effluents by means of membrane-assisted solvent extraction (NDSX), as the main step in the valorization process of the metal. Tributyl phosphate (TBP) and service water were used as extraction (EX) and back-extrac...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Industrial & engineering chemistry research 2007-01, Vol.46 (3), p.907-912
Hauptverfasser: Samaniego, H, San Román, M. F, Ortiz, I
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 912
container_issue 3
container_start_page 907
container_title Industrial & engineering chemistry research
container_volume 46
creator Samaniego, H
San Román, M. F
Ortiz, I
description This work has focused on the study of the kinetics of zinc removal from spent pickling effluents by means of membrane-assisted solvent extraction (NDSX), as the main step in the valorization process of the metal. Tributyl phosphate (TBP) and service water were used as extraction (EX) and back-extraction (BEX) agents, respectively. Working with hollow fiber membrane contactors, kinetic experiments were performed in order to analyze the influence of operation variables on the rate of zinc separation. A mathematical model that considers diffusion through the organic membrane as the main kinetic resistance was developed, and the membrane mass transport coefficient was estimated by means of the parameter estimation tool gEST (from gPROMS) to obtain a value of K m = 3.89 × 10-4 m/h. Simulated results agreed satisfactorily with experimental data, thus confirming the validity of the kinetic model and parameters.
doi_str_mv 10.1021/ie060836w
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_754546692</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>754546692</sourcerecordid><originalsourceid>FETCH-LOGICAL-a396t-3e4317a47b922a1172bf465aee7e3ad2580927f1680044d5b831b4e1db90031c3</originalsourceid><addsrcrecordid>eNptkMtKAzEUhoMoWC8L32A2Ii5GT-6ZpRRbxarFKoibkEkTSZ3O1GTq5e0dqbQbVwfO-f7_wIfQEYYzDASfBwcCFBWfW6iHOYGcA-PbqAdKqZwrxXfRXkozAOCcsR6SN6F2bbApa3z2EmqbPTjbfLj4nfnYzLPJwtVtNg72rQr1a3bpfbXsNukA7XhTJXf4N_fR0-DysX-Vj-6H1_2LUW5oIdqcOkaxNEyWBSEGY0lKzwQ3zklHzZRwBQWRHgsFwNiUl4rikjk8LQsAii3dRyer3kVs3pcutXoeknVVZWrXLJOWnHEmREE68nRF2tikFJ3XixjmJn5rDPrXjV676djjv1aTrKl8NLUNaRNQTBZAacflKy6k1n2t7ya-aSGp5PpxPNHsbth_HtwONNn0Gpv0rFnGunPzz_8f2698vg</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>754546692</pqid></control><display><type>article</type><title>Kinetics of Zinc Recovery from Spent Pickling Effluents</title><source>American Chemical Society Journals</source><creator>Samaniego, H ; San Román, M. F ; Ortiz, I</creator><creatorcontrib>Samaniego, H ; San Román, M. F ; Ortiz, I</creatorcontrib><description>This work has focused on the study of the kinetics of zinc removal from spent pickling effluents by means of membrane-assisted solvent extraction (NDSX), as the main step in the valorization process of the metal. Tributyl phosphate (TBP) and service water were used as extraction (EX) and back-extraction (BEX) agents, respectively. Working with hollow fiber membrane contactors, kinetic experiments were performed in order to analyze the influence of operation variables on the rate of zinc separation. A mathematical model that considers diffusion through the organic membrane as the main kinetic resistance was developed, and the membrane mass transport coefficient was estimated by means of the parameter estimation tool gEST (from gPROMS) to obtain a value of K m = 3.89 × 10-4 m/h. Simulated results agreed satisfactorily with experimental data, thus confirming the validity of the kinetic model and parameters.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie060836w</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Chemical engineering ; Exact sciences and technology</subject><ispartof>Industrial &amp; engineering chemistry research, 2007-01, Vol.46 (3), p.907-912</ispartof><rights>Copyright © 2007 American Chemical Society</rights><rights>2007 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a396t-3e4317a47b922a1172bf465aee7e3ad2580927f1680044d5b831b4e1db90031c3</citedby><cites>FETCH-LOGICAL-a396t-3e4317a47b922a1172bf465aee7e3ad2580927f1680044d5b831b4e1db90031c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie060836w$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie060836w$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=18479033$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Samaniego, H</creatorcontrib><creatorcontrib>San Román, M. F</creatorcontrib><creatorcontrib>Ortiz, I</creatorcontrib><title>Kinetics of Zinc Recovery from Spent Pickling Effluents</title><title>Industrial &amp; engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>This work has focused on the study of the kinetics of zinc removal from spent pickling effluents by means of membrane-assisted solvent extraction (NDSX), as the main step in the valorization process of the metal. Tributyl phosphate (TBP) and service water were used as extraction (EX) and back-extraction (BEX) agents, respectively. Working with hollow fiber membrane contactors, kinetic experiments were performed in order to analyze the influence of operation variables on the rate of zinc separation. A mathematical model that considers diffusion through the organic membrane as the main kinetic resistance was developed, and the membrane mass transport coefficient was estimated by means of the parameter estimation tool gEST (from gPROMS) to obtain a value of K m = 3.89 × 10-4 m/h. Simulated results agreed satisfactorily with experimental data, thus confirming the validity of the kinetic model and parameters.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNptkMtKAzEUhoMoWC8L32A2Ii5GT-6ZpRRbxarFKoibkEkTSZ3O1GTq5e0dqbQbVwfO-f7_wIfQEYYzDASfBwcCFBWfW6iHOYGcA-PbqAdKqZwrxXfRXkozAOCcsR6SN6F2bbApa3z2EmqbPTjbfLj4nfnYzLPJwtVtNg72rQr1a3bpfbXsNukA7XhTJXf4N_fR0-DysX-Vj-6H1_2LUW5oIdqcOkaxNEyWBSEGY0lKzwQ3zklHzZRwBQWRHgsFwNiUl4rikjk8LQsAii3dRyer3kVs3pcutXoeknVVZWrXLJOWnHEmREE68nRF2tikFJ3XixjmJn5rDPrXjV676djjv1aTrKl8NLUNaRNQTBZAacflKy6k1n2t7ya-aSGp5PpxPNHsbth_HtwONNn0Gpv0rFnGunPzz_8f2698vg</recordid><startdate>20070131</startdate><enddate>20070131</enddate><creator>Samaniego, H</creator><creator>San Román, M. F</creator><creator>Ortiz, I</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope></search><sort><creationdate>20070131</creationdate><title>Kinetics of Zinc Recovery from Spent Pickling Effluents</title><author>Samaniego, H ; San Román, M. F ; Ortiz, I</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a396t-3e4317a47b922a1172bf465aee7e3ad2580927f1680044d5b831b4e1db90031c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Samaniego, H</creatorcontrib><creatorcontrib>San Román, M. F</creatorcontrib><creatorcontrib>Ortiz, I</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><jtitle>Industrial &amp; engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Samaniego, H</au><au>San Román, M. F</au><au>Ortiz, I</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetics of Zinc Recovery from Spent Pickling Effluents</atitle><jtitle>Industrial &amp; engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2007-01-31</date><risdate>2007</risdate><volume>46</volume><issue>3</issue><spage>907</spage><epage>912</epage><pages>907-912</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>This work has focused on the study of the kinetics of zinc removal from spent pickling effluents by means of membrane-assisted solvent extraction (NDSX), as the main step in the valorization process of the metal. Tributyl phosphate (TBP) and service water were used as extraction (EX) and back-extraction (BEX) agents, respectively. Working with hollow fiber membrane contactors, kinetic experiments were performed in order to analyze the influence of operation variables on the rate of zinc separation. A mathematical model that considers diffusion through the organic membrane as the main kinetic resistance was developed, and the membrane mass transport coefficient was estimated by means of the parameter estimation tool gEST (from gPROMS) to obtain a value of K m = 3.89 × 10-4 m/h. Simulated results agreed satisfactorily with experimental data, thus confirming the validity of the kinetic model and parameters.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie060836w</doi><tpages>6</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0888-5885
ispartof Industrial & engineering chemistry research, 2007-01, Vol.46 (3), p.907-912
issn 0888-5885
1520-5045
language eng
recordid cdi_proquest_miscellaneous_754546692
source American Chemical Society Journals
subjects Applied sciences
Chemical engineering
Exact sciences and technology
title Kinetics of Zinc Recovery from Spent Pickling Effluents
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-25T08%3A08%3A05IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Kinetics%20of%20Zinc%20Recovery%20from%20Spent%20Pickling%20Effluents&rft.jtitle=Industrial%20&%20engineering%20chemistry%20research&rft.au=Samaniego,%20H&rft.date=2007-01-31&rft.volume=46&rft.issue=3&rft.spage=907&rft.epage=912&rft.pages=907-912&rft.issn=0888-5885&rft.eissn=1520-5045&rft.coden=IECRED&rft_id=info:doi/10.1021/ie060836w&rft_dat=%3Cproquest_cross%3E754546692%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=754546692&rft_id=info:pmid/&rfr_iscdi=true