<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>1870-249X</journal-id>
<journal-title><![CDATA[Journal of the Mexican Chemical Society]]></journal-title>
<abbrev-journal-title><![CDATA[J. Mex. Chem. Soc]]></abbrev-journal-title>
<issn>1870-249X</issn>
<publisher>
<publisher-name><![CDATA[Sociedad Química de México A.C.]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1870-249X2007000300001</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Preparation, Characterization and Salt Rejection of Negatively Charged Polyamide Nanofiltration Membranes]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Lin]]></surname>
<given-names><![CDATA[Shui Wai]]></given-names>
</name>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pérez Sicairos]]></surname>
<given-names><![CDATA[Sergio]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Félix Navarro]]></surname>
<given-names><![CDATA[Rosa María]]></given-names>
</name>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Instituto Tecnológico de Tijuana Centro de Graduados ]]></institution>
<addr-line><![CDATA[Tijuana Baja California]]></addr-line>
<country>México</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>09</month>
<year>2007</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>09</month>
<year>2007</year>
</pub-date>
<volume>51</volume>
<numero>3</numero>
<fpage>129</fpage>
<lpage>135</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_arttext&amp;pid=S1870-249X2007000300001&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_abstract&amp;pid=S1870-249X2007000300001&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.mx/scielo.php?script=sci_pdf&amp;pid=S1870-249X2007000300001&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Four thin-film composite (TFC) polyamide negatively charged nanofiltration (NF) membranes (NF-PS-1, NF-PS-2, NF-PS-3 and NF-PS-4) were prepared via interfacial polymerization technique which involved the formation of a polyamide thin film at the interfacial polysulfone (PS) microporous substrate between two immiscible liquid phases; an aqueous phase containing piperazine and an organic phase containing trimesoyl chloride (TMC = 0.25, 0.50, 1.00 and 2.00 wt%). Correlations of the intrinsic properties of these four NF filtration membranes, in regarding to the physical structures, surface negative charge density, pure water flux, pore size and the NF filtration performances, on the composition of the weight-% of TMC in the organic phase were investigated. Experimental results clearly demonstrated that NF membrane prepared from using 1.0 wt-% of TMC in hexane phase (i.e., NF-PS-3) gave a much higher salt rejections on salt containing negative divalent salts like Na2SO4 and MgSO4; the maximum rejection of Na2SO4 and MgSO4 were both to be 99.6 % for NF-PS-3 (TMC = 1.0 wt-%) while the rejections of Na2SO4 and MgSO4 for the rest of the three NF membranes were in the order of NF-PS-2 (TMC = 0.50 wt-%) > NF-PS-1 (TMC = 0.25 wt-%) > NF-PS-4 (TMC = 2.00 wt-%). Effects of the pH of the feed and the applied filtration pressure on the MgSO4 rejection were also investigated for this series of nanofiltration membranes.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Se prepararon cuatro membranas de nanofiltración (NF-PS-1, NF-PS-2, NF-PS-3, NF-PS-4) de película delgada (TFC) de poliamida cargadas negativamente, mediante la técnica de polimerización interfacial, la cual implica la formación de una película delgada en la interfase de un sustrato microporoso de polisulfona (PS) entre dos fases líquidas inmiscibles; una fase acuosa que contiene piperazina y una fase orgánica que contiene tricloruro de mesoilo (TMC) a diferentes concentraciones (0.25, 0.50. 1.00 y 2.00 % peso). Se investigaron las correlaciones entre las propiedades intrínsecas de las cuatro membranas de NF y la composición de la fase orgánica (% peso de TMC). Las propiedades estudiadas fueron; estructura física, densidad de carga superficial negativa, flujo a través de la membrana de agua pura, tamaño de poro y capacidad de filtración de las membranas. Los resultados experimentales demostraron claramente que la membrana de NF preparada con la solución que contiene 1.0 % de TMC (NF-PS-3) presenta mayor remoción de sales cuando tienen iones divalentes como el Na2SO4 y MgSO4; la máxima remoción de Na2SO4 y MgSO4 fue de 99.6 % para ambas sales, mientras que para las tres membranas restantes, el orden de remoción de las sales fue NF-PS-2 (TMC = 0.50 % peso) > NF-PS-1 (TMC = 0.25 % peso) > NF-PS-4 (TMC = 2.00 % peso). También se investigaron los efectos del pH de la solución alimentada al sistema y de la presión de filtración aplicada sobre la remoción de MgSO4 para esta serie de membranas de nanofiltración.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[Polyamide NF membrane]]></kwd>
<kwd lng="en"><![CDATA[preparation]]></kwd>
<kwd lng="en"><![CDATA[characterization]]></kwd>
<kwd lng="en"><![CDATA[NF performances]]></kwd>
<kwd lng="es"><![CDATA[Membrana de NF de poliamida]]></kwd>
<kwd lng="es"><![CDATA[preparación]]></kwd>
<kwd lng="es"><![CDATA[caracterización]]></kwd>
<kwd lng="es"><![CDATA[desempeño de NF]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[  	    <p align="justify"><font face="verdana" size="4">Article</font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="center"><font face="verdana" size="4"><b>Preparation, Characterization and Salt Rejection of Negatively Charged Polyamide Nanofiltration Membranes</b></font></p>  	    <p align="center"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="center"><font face="verdana" size="2"><b>Shui Wai Lin,* Sergio P&eacute;rez Sicairos and Rosa Mar&iacute;a F&eacute;lix Navarro</b></font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><i>Centro de Graduados, Instituto Tecnol&oacute;gico de Tijuana. Tijuana, Baja California, M&eacute;xico Fax: (858) 581 1211</i>, e&#45;mail: <a href="mailto:SL388@AOL.COM">SL388@AOL.COM</a></font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2">Recibido el 2 de marzo de 2007    ]]></body>
<body><![CDATA[<br> 	Aceptado el 6 de julio de 2007</font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Abstract</b></font></p>  	    <p align="justify"><font face="verdana" size="2">Four thin&#45;film composite (TFC) polyamide negatively charged nanofiltration (NF) membranes (NF&#45;PS&#45;1, NF&#45;PS&#45;2, NF&#45;PS&#45;3 and NF&#45;PS&#45;4) were prepared via interfacial polymerization technique which involved the formation of a polyamide thin film at the interfacial polysulfone (PS) microporous substrate between two immiscible liquid phases; an aqueous phase containing piperazine and an organic phase containing trimesoyl chloride (TMC = 0.25, 0.50, 1.00 and 2.00 wt%). Correlations of the intrinsic properties of these four NF filtration membranes, in regarding to the physical structures, surface negative charge density, pure water flux, pore size and the NF filtration performances, on the composition of the weight&#45;% of TMC in the organic phase were investigated. Experimental results clearly demonstrated that NF membrane prepared from using 1.0 wt&#45;% of TMC in hexane phase (i.e., NF&#45;PS&#45;3) gave a much higher salt rejections on salt containing negative divalent salts like Na<sub>2</sub>SO<sub>4</sub> and MgSO<sub>4</sub>; the maximum rejection of Na<sub>2</sub>SO<sub>4</sub> and MgSO<sub>4</sub> were both to be 99.6 % for NF&#45;PS&#45;3 (TMC = 1.0 wt&#45;%) while the rejections of Na<sub>2</sub>SO<sub>4</sub> and MgSO<sub>4</sub> for the rest of the three NF membranes were in the order of NF&#45;PS&#45;2 (TMC = 0.50 wt&#45;%) &gt; NF&#45;PS&#45;1 (TMC = 0.25 wt&#45;%) &gt; NF&#45;PS&#45;4 (TMC = 2.00 wt&#45;%). Effects of the pH of the feed and the applied filtration pressure on the MgSO<sub>4</sub> rejection were also investigated for this series of nanofiltration membranes.</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Key words:</b> Polyamide NF membrane, preparation, characterization, NF performances.</font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Resumen</b></font></p>  	    <p align="justify"><font face="verdana" size="2">Se prepararon cuatro membranas de nanofiltraci&oacute;n (NF&#45;PS&#45;1, NF&#45;PS&#45;2, NF&#45;PS&#45;3, NF&#45;PS&#45;4) de pel&iacute;cula delgada (TFC) de poliamida cargadas negativamente, mediante la t&eacute;cnica de polimerizaci&oacute;n interfacial, la cual implica la formaci&oacute;n de una pel&iacute;cula delgada en la interfase de un sustrato microporoso de polisulfona (PS) entre dos fases l&iacute;quidas inmiscibles; una fase acuosa que contiene piperazina y una fase org&aacute;nica que contiene tricloruro de mesoilo (TMC) a diferentes concentraciones (0.25, 0.50. 1.00 y 2.00 % peso). Se investigaron las correlaciones entre las propiedades intr&iacute;nsecas de las cuatro membranas de NF y la composici&oacute;n de la fase org&aacute;nica (% peso de TMC). Las propiedades estudiadas fueron; estructura f&iacute;sica, densidad de carga superficial negativa, flujo a trav&eacute;s de la membrana de agua pura, tama&ntilde;o de poro y capacidad de filtraci&oacute;n de las membranas. Los resultados experimentales demostraron claramente que la membrana de NF preparada con la soluci&oacute;n que contiene 1.0 % de TMC (NF&#45;PS&#45;3) presenta mayor remoci&oacute;n de sales cuando tienen iones divalentes como el Na<sub>2</sub>SO<sub>4</sub> y MgSO<sub>4</sub>; la m&aacute;xima remoci&oacute;n de Na<sub>2</sub>SO<sub>4</sub> y MgSO<sub>4</sub> fue de 99.6 % para ambas sales, mientras que para las tres membranas restantes, el orden de remoci&oacute;n de las sales fue NF&#45;PS&#45;2 (TMC = 0.50 % peso) &gt; NF&#45;PS&#45;1 (TMC = 0.25 % peso) &gt; NF&#45;PS&#45;4 (TMC = 2.00 % peso). Tambi&eacute;n se investigaron los efectos del pH de la soluci&oacute;n alimentada al sistema y de la presi&oacute;n de filtraci&oacute;n aplicada sobre la remoci&oacute;n de MgSO<sub>4</sub> para esta serie de membranas de nanofiltraci&oacute;n.</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Palabras clave:</b> Membrana de NF de poliamida, preparaci&oacute;n, caracterizaci&oacute;n, desempe&ntilde;o de NF.</font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    ]]></body>
<body><![CDATA[<p align="justify"><font face="verdana" size="2"><a href="/pdf/jmcs/v51n3/v51n3a1.pdf" target="_blank">DESCARGAR ART&Iacute;CULO EN FORMATO PDF</a></font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>Acknowledegment</b></font></p>  	    <p align="justify"><font face="verdana" size="2">The authors would like to thank Mr. Israel Gradilla and Dr. Leonel Cota Araiza for performing the SEM and Dr. Enrique Samano for AFM analysis (all from CCMC&#45;UNAM, Ensenada, Mexico). This project was financed by COSNET (Grant No. 645.01&#45;P).</font></p>  	    <p align="justify"><font face="verdana" size="2">&nbsp;</font></p>  	    <p align="justify"><font face="verdana" size="2"><b>References</b></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">1.&nbsp;Cadotte, J. E.; Peterson, R. J. "Thin&#45;Film Composite Reverse&#45;Osmosis Membranes: Origin, Development, and Recent Advances" in: <i>Synthetic Membranes,</i> Volume I <i>Desalination,</i> American Chemical Society, A.F. Turbak, Ed., Washington, D.C., 1981.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4927926&pid=S1870-249X200700030000100001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    <!-- ref --><p align="justify"><font face="verdana" size="2">2.&nbsp;Lee, S.; Cho, J.; Elimelech, M. <i>Desalination</i> <b>2004,</b> <i>160,</i> 1&#45;12.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=4927928&pid=S1870-249X200700030000100002&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></font></p>  	    ]]></body>
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<body><![CDATA[ ]]></body><back>
<ref-list>
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