Crossflow filtration of iron(III), copper(II), and cadmium(II) aqueous solutions with alginic acid/cellulose composite membranes

The removal of Fe(III), Cu(II), and Cd(II) ions from aqueous solutions was investigated with a crossflow filtration technique. Alginic acid (AA)/cellulose composite membranes were used for retention. In the filtration of Fe(III) solutions, the effects of the crossflow velocity, applied pressure, AA...

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Veröffentlicht in:Journal of applied polymer science 2010-01, Vol.115 (1), p.616-623
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description The removal of Fe(III), Cu(II), and Cd(II) ions from aqueous solutions was investigated with a crossflow filtration technique. Alginic acid (AA)/cellulose composite membranes were used for retention. In the filtration of Fe(III) solutions, the effects of the crossflow velocity, applied pressure, AA content of the membranes, and pH on the retention percentage and the permeate flux were examined. The maximum retention percentage was found to be 89% for a 1 × 10−4M Fe(III) solution at the flow velocity of 100 mL/min and the pressure of 60 kPa with 0.50% (w/v) AA/cellulose composite membranes at pH 3. Aqueous solutions of Cu(II) and Cd(II) were filtered at the flow velocity of 100 mL/min and pressure of 10 kPa. The effects of the AA content of the membranes and pH of the waste medium on the retention percentage and the permeate flux were determined. For 1 × 10−4M Cu(II) and Cd(II) solutions, the maximum retention percentages were found to be 94 and 75%, respectively, at pH 7 with 0.50% (w/v) AA/cellulose composite membranes. When metal‐ion mixtures were used, the retention percentages of Fe(III), Cu(II), and Cd(II) were found to be 89, 48, and 10%, respectively, at pH 3 with 0.50% (w/v) AA/cellulose composite membranes. © 2009 Wiley Periodicals, Inc. J Appl Polym Sci, 2010
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Alginic acid (AA)/cellulose composite membranes were used for retention. In the filtration of Fe(III) solutions, the effects of the crossflow velocity, applied pressure, AA content of the membranes, and pH on the retention percentage and the permeate flux were examined. The maximum retention percentage was found to be 89% for a 1 × 10−4M Fe(III) solution at the flow velocity of 100 mL/min and the pressure of 60 kPa with 0.50% (w/v) AA/cellulose composite membranes at pH 3. Aqueous solutions of Cu(II) and Cd(II) were filtered at the flow velocity of 100 mL/min and pressure of 10 kPa. The effects of the AA content of the membranes and pH of the waste medium on the retention percentage and the permeate flux were determined. For 1 × 10−4M Cu(II) and Cd(II) solutions, the maximum retention percentages were found to be 94 and 75%, respectively, at pH 7 with 0.50% (w/v) AA/cellulose composite membranes. When metal‐ion mixtures were used, the retention percentages of Fe(III), Cu(II), and Cd(II) were found to be 89, 48, and 10%, respectively, at pH 3 with 0.50% (w/v) AA/cellulose composite membranes. © 2009 Wiley Periodicals, Inc. 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Appl. Polym. Sci</addtitle><description>The removal of Fe(III), Cu(II), and Cd(II) ions from aqueous solutions was investigated with a crossflow filtration technique. Alginic acid (AA)/cellulose composite membranes were used for retention. In the filtration of Fe(III) solutions, the effects of the crossflow velocity, applied pressure, AA content of the membranes, and pH on the retention percentage and the permeate flux were examined. The maximum retention percentage was found to be 89% for a 1 × 10−4M Fe(III) solution at the flow velocity of 100 mL/min and the pressure of 60 kPa with 0.50% (w/v) AA/cellulose composite membranes at pH 3. Aqueous solutions of Cu(II) and Cd(II) were filtered at the flow velocity of 100 mL/min and pressure of 10 kPa. The effects of the AA content of the membranes and pH of the waste medium on the retention percentage and the permeate flux were determined. For 1 × 10−4M Cu(II) and Cd(II) solutions, the maximum retention percentages were found to be 94 and 75%, respectively, at pH 7 with 0.50% (w/v) AA/cellulose composite membranes. When metal‐ion mixtures were used, the retention percentages of Fe(III), Cu(II), and Cd(II) were found to be 89, 48, and 10%, respectively, at pH 3 with 0.50% (w/v) AA/cellulose composite membranes. © 2009 Wiley Periodicals, Inc. J Appl Polym Sci, 2010</description><subject>Applied sciences</subject><subject>Aqueous solutions</subject><subject>Cellulose</subject><subject>composites</subject><subject>Exact sciences and technology</subject><subject>Exchange resins and membranes</subject><subject>Filtration</subject><subject>Flow velocity</subject><subject>Flux</subject><subject>Forms of application and semi-finished materials</subject><subject>Membranes</subject><subject>Polymer industry, paints, wood</subject><subject>Reproduction</subject><subject>Technology of polymers</subject><subject>waste</subject><subject>Wastes</subject><issn>0021-8995</issn><issn>1097-4628</issn><issn>1097-4628</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNp9kU9vFCEYxomxiWvrwW_AxbhNnC7_YY7tRtttGu1B45FQFhRlhinMZO3Njy7TbXurFyDwe573fXgBeIvRCUaIrMwwnFCMhHgBFhi1smGCqJdgUd9wo9qWvwKvS_mFEMYciQX4u86pFB_TDvoQx2zGkHqYPAw59cvNZnP8Ado0DC4v78-m30Jrtl2YuvkCmtvJpanAkuI0SwvchfEnNPFH6IOFxobtyroYp5iKq07dkEoYHexcd5NN78oROPAmFvfmYT8E3z59_Lq-aK6-nG_Wp1eNZYiIpsW8pc47KSxRkihOhVVcUoKRIlR64RhRhNeVSCW8sYTVgPyGMSXVljB6CN7vfYecas9l1F0oc2e1iRpAq1YQygmayeV_SSwkJrU0EhU93qN2_sXsvB5y6Ey-0xjpeR66zkPfz6Oy7x5sTbEm-prehvIkIARTzgWq3GrP7UJ0d88b6tPr60fnZq8IZXR_nhQm_9ZCUsn198_numWXZ_KMrTWi_wDgP6Yu</recordid><startdate>20100105</startdate><enddate>20100105</enddate><creator>CIFCI, Cemal</creator><creator>SANH, Oya</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>20100105</creationdate><title>Crossflow filtration of iron(III), copper(II), and cadmium(II) aqueous solutions with alginic acid/cellulose composite membranes</title><author>CIFCI, Cemal ; SANH, Oya</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4026-91593efe76c28728536c85732108237f6e42825e422786fac241505b44878d243</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Applied sciences</topic><topic>Aqueous solutions</topic><topic>Cellulose</topic><topic>composites</topic><topic>Exact sciences and technology</topic><topic>Exchange resins and membranes</topic><topic>Filtration</topic><topic>Flow velocity</topic><topic>Flux</topic><topic>Forms of application and semi-finished materials</topic><topic>Membranes</topic><topic>Polymer industry, paints, wood</topic><topic>Reproduction</topic><topic>Technology of polymers</topic><topic>waste</topic><topic>Wastes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>CIFCI, Cemal</creatorcontrib><creatorcontrib>SANH, Oya</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Journal of applied polymer science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>CIFCI, Cemal</au><au>SANH, Oya</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Crossflow filtration of iron(III), copper(II), and cadmium(II) aqueous solutions with alginic acid/cellulose composite membranes</atitle><jtitle>Journal of applied polymer science</jtitle><addtitle>J. Appl. Polym. Sci</addtitle><date>2010-01-05</date><risdate>2010</risdate><volume>115</volume><issue>1</issue><spage>616</spage><epage>623</epage><pages>616-623</pages><issn>0021-8995</issn><issn>1097-4628</issn><eissn>1097-4628</eissn><coden>JAPNAB</coden><abstract>The removal of Fe(III), Cu(II), and Cd(II) ions from aqueous solutions was investigated with a crossflow filtration technique. Alginic acid (AA)/cellulose composite membranes were used for retention. In the filtration of Fe(III) solutions, the effects of the crossflow velocity, applied pressure, AA content of the membranes, and pH on the retention percentage and the permeate flux were examined. The maximum retention percentage was found to be 89% for a 1 × 10−4M Fe(III) solution at the flow velocity of 100 mL/min and the pressure of 60 kPa with 0.50% (w/v) AA/cellulose composite membranes at pH 3. Aqueous solutions of Cu(II) and Cd(II) were filtered at the flow velocity of 100 mL/min and pressure of 10 kPa. The effects of the AA content of the membranes and pH of the waste medium on the retention percentage and the permeate flux were determined. For 1 × 10−4M Cu(II) and Cd(II) solutions, the maximum retention percentages were found to be 94 and 75%, respectively, at pH 7 with 0.50% (w/v) AA/cellulose composite membranes. When metal‐ion mixtures were used, the retention percentages of Fe(III), Cu(II), and Cd(II) were found to be 89, 48, and 10%, respectively, at pH 3 with 0.50% (w/v) AA/cellulose composite membranes. © 2009 Wiley Periodicals, Inc. J Appl Polym Sci, 2010</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><doi>10.1002/app.31066</doi><tpages>8</tpages></addata></record>
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source Wiley Online Library Journals Frontfile Complete
subjects Applied sciences
Aqueous solutions
Cellulose
composites
Exact sciences and technology
Exchange resins and membranes
Filtration
Flow velocity
Flux
Forms of application and semi-finished materials
Membranes
Polymer industry, paints, wood
Reproduction
Technology of polymers
waste
Wastes
title Crossflow filtration of iron(III), copper(II), and cadmium(II) aqueous solutions with alginic acid/cellulose composite membranes
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