<?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>0872-1904</journal-id>
<journal-title><![CDATA[Portugaliae Electrochimica Acta]]></journal-title>
<abbrev-journal-title><![CDATA[Port. Electrochim. Acta]]></abbrev-journal-title>
<issn>0872-1904</issn>
<publisher>
<publisher-name><![CDATA[Sociedade Portuguesa de Electroquímica]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0872-19042008000100002</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Brillas]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Garrido]]></surname>
<given-names><![CDATA[J.A.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rodríguez]]></surname>
<given-names><![CDATA[R.M.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Arias]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Cabot]]></surname>
<given-names><![CDATA[P.L.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Centellas]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Universitat de Barcelona Facultat de Química Departament de Química Física]]></institution>
<addr-line><![CDATA[Barcelona ]]></addr-line>
<country>Spain</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2008</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2008</year>
</pub-date>
<volume>26</volume>
<numero>1</numero>
<fpage>15</fpage>
<lpage>46</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_arttext&amp;pid=S0872-19042008000100002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_abstract&amp;pid=S0872-19042008000100002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_pdf&amp;pid=S0872-19042008000100002&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[This paper reports the mineralization of an aromatic pharmaceutical as clofibric acid and the dye indigo carmine in 0.05 M Na2SO4 of pH 3.0 by electrochemical advanced oxidation processes such as anodic oxidation without and with electrogenerated H2O2, electro-Fenton and photoelectro-Fenton using a boron-doped diamond (BDD) anode. These procedures produce the strong oxidant hydroxyl radical in the form of BDD(·OH) from water oxidation at BDD and/or ·OH from Fenton’s reaction between added Fe2+ and H2O2 generated at the cathode by two-electron O2 reduction. Comparative degradation of both compounds is performed with an undivided electrolytic cell of 100 mL with an O2-diffusion cathode. The effect of current density and pollutant concentration on the degradation rate and current efficiency of the different methods is discussed. The decay kinetics of clofibric acid and indigo carmine and the evolution of their aromatic by-products and final carboxylic acids like oxalic and/or oxamic are described to clarify their reaction sequences. Anodic oxidation is able to completely mineralize both compounds mainly with BDD(·OH). Aromatic pollutants are more rapidly destroyed in electro-Fenton due to their faster reaction with ·OH, but final Fe(III)-oxalate and Fe(III)-oxamate can only be oxidized with BDD(·OH). The most efficient method is photoelectro-Fenton due to the parallel photolysis of Fe(III)-oxalate complexes with UVA light, although Fe(III)-oxamate complexes are not photodecomposed. Under these conditions, the degradation rate can be enhanced using Cu2+ as co-catalyst because Cu(II)-oxalate and Cu(II)-oxamate complexes are quickly destroyed by ·OH. Results on the fast mineralization of 2.5 L of cresols solutions of pH 3.0 by solar photoelectro-Fenton using a flow plant coupled to a solar photoreactor are also reported. The high efficiency and very low operational cost found for this procedure make it useful for the treatment of industrial wastewaters]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[clofibric acid]]></kwd>
<kwd lng="en"><![CDATA[indigo carmine]]></kwd>
<kwd lng="en"><![CDATA[cresols]]></kwd>
<kwd lng="en"><![CDATA[anodic oxidation]]></kwd>
<kwd lng="en"><![CDATA[electro-Fenton]]></kwd>
<kwd lng="en"><![CDATA[photoelectro-Fenton]]></kwd>
<kwd lng="en"><![CDATA[solar photoelectro-Fenton]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="center"><b>Wastewaters by Electrochemical Advanced Oxidation Processes    Using a BDD Anode and Electrogenerated H<sub>2</sub>O<sub>2</sub> with Fe(II)    and UVA Light as Catalysts</b></p>     <p align="center">&nbsp;</p>     <p align="center">&nbsp;</p> <h3 align="center"><b>E. Brillas,<a href="#1">*</a><a name="top1"></a> J.A. Garrido,    R.M. Rodríguez, C. Arias, P.L. Cabot, F. Centellas </b></h3>     <p align="center">&nbsp;</p>     <p align="center"><i>Laboratori d’Electroquímica dels Materials i del Medi Ambient,    Departament de Química Física, Facultat de Química, Universitat de Barcelona,    Martí i Franquès 1-11, 08028 Barcelona, Spain</i></p>     <p align="center">&nbsp;</p>      <p align="center">Received 18<sup>th</sup> July 2007</p>      <p>&nbsp;</p>      <p>&nbsp;</p>      <p><b>Abstract</b></p>      ]]></body>
<body><![CDATA[<p>This paper reports the mineralization of an aromatic pharmaceutical as clofibric acid and the dye indigo carmine in 0.05 M Na<sub>2</sub>SO<sub>4</sub> of pH 3.0 by electrochemical advanced oxidation processes such as anodic oxidation without and with electrogenerated H<sub>2</sub>O<sub>2</sub>, electro-Fenton and photoelectro-Fenton using a boron-doped diamond (BDD) anode. These procedures produce the strong oxidant hydroxyl radical in the form of BDD(<sup>·</sup>OH) from water oxidation at BDD and/or <sup>·</sup>OH from Fenton’s reaction between added Fe<sup>2+</sup> and H<sub>2</sub>O<sub>2</sub> generated at the cathode by two-electron O<sub>2</sub> reduction. Comparative degradation of both compounds is performed with an undivided electrolytic cell of 100 mL with an O<sub>2</sub>-diffusion cathode. The effect of current density and pollutant concentration on the degradation rate and current efficiency of the different methods is discussed. The decay kinetics of clofibric acid and indigo carmine and the evolution of their aromatic by-products and final carboxylic acids like oxalic and/or oxamic are described to clarify their reaction sequences. Anodic oxidation is able to completely mineralize both compounds mainly with BDD(<sup>·</sup>OH). Aromatic pollutants are more rapidly destroyed in electro-Fenton due to their faster reaction with <sup>·</sup>OH, but final Fe(III)-oxalate and Fe(III)-oxamate can only be oxidized with BDD(<sup>·</sup>OH). The most efficient method is photoelectro-Fenton due to the parallel photolysis of Fe(III)-oxalate complexes with UVA light, although Fe(III)-oxamate complexes are not photodecomposed.  Under  these conditions, the degradation rate can be enhanced using Cu<sup>2+</sup> as co-catalyst because Cu(II)-oxalate and Cu(II)-oxamate complexes are quickly destroyed by <sup>·</sup>OH. Results on the fast mineralization of 2.5 L of cresols solutions of pH 3.0 by solar photoelectro-Fenton using a flow plant coupled to a solar photoreactor are also reported. The high efficiency and very low operational cost found for this procedure make it useful for the treatment of industrial wastewaters</p>      <p><b><i>Keywords</i></b>: clofibric acid, indigo carmine, cresols, anodic oxidation,    electro-Fenton, photoelectro-Fenton, solar photoelectro-Fenton.</p>      <p>&nbsp;</p>      <p>&nbsp;</p>      <p>Texto disponível em PDF</p>      <p>Full text only in PDF format</p>      <p>&nbsp;</p>        <p>&nbsp;</p>      <p><b>References</b></p>     <p>&nbsp;</p>      ]]></body>
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