Serveur d'exploration sur le cobalt au Maghreb

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Phenol electrooxidation on Fe-Co3O4 thin film electrodes in alkaline medium

Identifieur interne : 000251 ( PascalFrancis/Curation ); précédent : 000250; suivant : 000252

Phenol electrooxidation on Fe-Co3O4 thin film electrodes in alkaline medium

Auteurs : M. A. M. Cartaxo [Portugal] ; K. Ablad [Maroc] ; J. Douch [Maroc] ; Y. Berghoute [Maroc] ; M. Hamdani [Maroc] ; M. H. Mendonca [Portugal] ; J. M. F. Nogueira [Portugal] ; M. I. S. Pereira [Portugal]

Source :

RBID : Pascal:12-0407166

Descripteurs français

English descriptors

Abstract

Fe-CO3O4 thin film with different amounts of Fe have been used for the electro-oxidation of phenol in alkaline medium at room temperature. The electrodes were prepared by coating stainless steel supports with successive layers of the oxides, obtained by thermal decomposition at 673 K. The electrolysis was carried out at constant potential and the phenol disappearance, during the electrolysis, was monitored by UV-Vis absorbance measurements between 250 and 500 nm. After 3 h of electrolysis, the intermediates were identified by comparing the HPLC data and UV-Vis spectra to those from pure standards. The results indicate that the same oxidation products are formed on the different prepared electrodes, namely the decomposition products of phenol such as benzoquinone, hydroquinone and cathecol in basic medium. Simulated results show clearly the decrease of the amount of phenolic species with the electrolysis time. An enhancement of the phenol removal is observed with the presence of iron in the oxide. Under the operating conditions, around 30% of the initial phenol has been removed at ca. 3 h and the complete degradation is obtained after 54 h of electrolysis, when Fe-Co3O4 thin film with 10% of Fe is used as anode.
pA  
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A03   1    @0 Chemosphere : (Oxf.)
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A06       @2 4
A08 01  1  ENG  @1 Phenol electrooxidation on Fe-Co3O4 thin film electrodes in alkaline medium
A11 01  1    @1 CARTAXO (M. A. M.)
A11 02  1    @1 ABLAD (K.)
A11 03  1    @1 DOUCH (J.)
A11 04  1    @1 BERGHOUTE (Y.)
A11 05  1    @1 HAMDANI (M.)
A11 06  1    @1 MENDONCA (M. H.)
A11 07  1    @1 NOGUEIRA (J. M. F.)
A11 08  1    @1 PEREIRA (M. I. S.)
A14 01      @1 Deportamento de Engenharia Química e do Ambiente, Escola Superior de Tecnologia do Instituto Politécnico de Tomar, Estrada do Serra @2 2300-313 Tomar @3 PRT @Z 1 aut.
A14 02      @1 Loboratoire de Chimie Physique, Faculté des Sciences, Université Ibn Zohr, B.P. 8106/S Cité Dakhla @2 Agadir @3 MAR @Z 2 aut. @Z 3 aut. @Z 4 aut. @Z 5 aut.
A14 03      @1 Centro de Ciências Moleculares e Materials, Faculdade de Ciencias da Universidade de Lisboa @3 PRT @Z 1 aut. @Z 6 aut. @Z 8 aut.
A14 04      @1 Centro de Química e Bioquímica, Faculdade de Ciências da Universidade de Lisboa @3 PRT @Z 7 aut.
A20       @1 341-347
A21       @1 2012
A23 01      @0 ENG
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C01 01    ENG  @0 Fe-CO3O4 thin film with different amounts of Fe have been used for the electro-oxidation of phenol in alkaline medium at room temperature. The electrodes were prepared by coating stainless steel supports with successive layers of the oxides, obtained by thermal decomposition at 673 K. The electrolysis was carried out at constant potential and the phenol disappearance, during the electrolysis, was monitored by UV-Vis absorbance measurements between 250 and 500 nm. After 3 h of electrolysis, the intermediates were identified by comparing the HPLC data and UV-Vis spectra to those from pure standards. The results indicate that the same oxidation products are formed on the different prepared electrodes, namely the decomposition products of phenol such as benzoquinone, hydroquinone and cathecol in basic medium. Simulated results show clearly the decrease of the amount of phenolic species with the electrolysis time. An enhancement of the phenol removal is observed with the presence of iron in the oxide. Under the operating conditions, around 30% of the initial phenol has been removed at ca. 3 h and the complete degradation is obtained after 54 h of electrolysis, when Fe-Co3O4 thin film with 10% of Fe is used as anode.
C02 01  X    @0 001D16A04F
C02 02  X    @0 001D16A05B
C03 01  X  FRE  @0 Phénols @2 FX @5 01
C03 01  X  ENG  @0 Phenols @2 FX @5 01
C03 01  X  SPA  @0 Fenoles @2 FX @5 01
C03 02  X  FRE  @0 Oxydation @5 02
C03 02  X  ENG  @0 Oxidation @5 02
C03 02  X  SPA  @0 Oxidación @5 02
C03 03  X  FRE  @0 Réaction électrochimique @5 03
C03 03  X  ENG  @0 Electrochemical reaction @5 03
C03 03  X  SPA  @0 Reacción electroquímica @5 03
C03 04  X  FRE  @0 Oxyde de cobalt @5 04
C03 04  X  ENG  @0 Cobalt oxide @5 04
C03 04  X  SPA  @0 Cobalto óxido @5 04
C03 05  X  FRE  @0 Fer @2 NC @5 05
C03 05  X  ENG  @0 Iron @2 NC @5 05
C03 05  X  SPA  @0 Hierro @2 NC @5 05
C03 06  X  FRE  @0 Pollution eau @5 06
C03 06  X  ENG  @0 Water pollution @5 06
C03 06  X  SPA  @0 Contaminación agua @5 06
C03 07  X  FRE  @0 Décontamination @5 07
C03 07  X  ENG  @0 Decontamination @5 07
C03 07  X  SPA  @0 Descontaminación @5 07
C03 08  X  FRE  @0 Eau usée industrielle @5 08
C03 08  X  ENG  @0 Industrial waste water @5 08
C03 08  X  SPA  @0 Agua servida industrial @5 08
C03 09  X  FRE  @0 Epuration eau usée @5 09
C03 09  X  ENG  @0 Waste water purification @5 09
C03 09  X  SPA  @0 Depuración aguas servidas @5 09
C03 10  X  FRE  @0 Epuration physicochimique @5 10
C03 10  X  ENG  @0 Physicochemical purification @5 10
C03 10  X  SPA  @0 Depuración fisicoquímica @5 10
C03 11  X  FRE  @0 Matériau électrode @5 11
C03 11  X  ENG  @0 Electrode material @5 11
C03 11  X  SPA  @0 Material electrodo @5 11
C03 12  X  FRE  @0 Electrode couche mince @5 13
C03 12  X  ENG  @0 Thin layer electrode @5 13
C03 12  X  SPA  @0 Electrodo capa fina @5 13
C03 13  X  FRE  @0 Electrolyse @5 14
C03 13  X  ENG  @0 Electrolysis @5 14
C03 13  X  SPA  @0 Electrólisis @5 14
C03 14  X  FRE  @0 Traitement électrochimique @5 35
C03 14  X  ENG  @0 Electrochemical treatment @5 35
C03 14  X  SPA  @0 Tratamiento electroquímico @5 35
C07 01  X  FRE  @0 Composé organique @2 NA @5 43
C07 01  X  ENG  @0 Organic compounds @2 NA @5 43
C07 01  X  SPA  @0 Compuesto orgánico @2 NA @5 43
N21       @1 317

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Pascal:12-0407166

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<term>Electrochemical treatment</term>
<term>Electrode material</term>
<term>Electrolysis</term>
<term>Industrial waste water</term>
<term>Iron</term>
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<term>Phénols</term>
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<term>Fer</term>
<term>Pollution eau</term>
<term>Décontamination</term>
<term>Eau usée industrielle</term>
<term>Epuration eau usée</term>
<term>Epuration physicochimique</term>
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<term>Electrode couche mince</term>
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<div type="abstract" xml:lang="en">Fe-CO3O4 thin film with different amounts of Fe have been used for the electro-oxidation of phenol in alkaline medium at room temperature. The electrodes were prepared by coating stainless steel supports with successive layers of the oxides, obtained by thermal decomposition at 673 K. The electrolysis was carried out at constant potential and the phenol disappearance, during the electrolysis, was monitored by UV-Vis absorbance measurements between 250 and 500 nm. After 3 h of electrolysis, the intermediates were identified by comparing the HPLC data and UV-Vis spectra to those from pure standards. The results indicate that the same oxidation products are formed on the different prepared electrodes, namely the decomposition products of phenol such as benzoquinone, hydroquinone and cathecol in basic medium. Simulated results show clearly the decrease of the amount of phenolic species with the electrolysis time. An enhancement of the phenol removal is observed with the presence of iron in the oxide. Under the operating conditions, around 30% of the initial phenol has been removed at ca. 3 h and the complete degradation is obtained after 54 h of electrolysis, when Fe-Co
<sub>3</sub>
O
<sub>4</sub>
thin film with 10% of Fe is used as anode.</div>
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<s1>Deportamento de Engenharia Química e do Ambiente, Escola Superior de Tecnologia do Instituto Politécnico de Tomar, Estrada do Serra</s1>
<s2>2300-313 Tomar</s2>
<s3>PRT</s3>
<sZ>1 aut.</sZ>
</fA14>
<fA14 i1="02">
<s1>Loboratoire de Chimie Physique, Faculté des Sciences, Université Ibn Zohr, B.P. 8106/S Cité Dakhla</s1>
<s2>Agadir</s2>
<s3>MAR</s3>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
</fA14>
<fA14 i1="03">
<s1>Centro de Ciências Moleculares e Materials, Faculdade de Ciencias da Universidade de Lisboa</s1>
<s3>PRT</s3>
<sZ>1 aut.</sZ>
<sZ>6 aut.</sZ>
<sZ>8 aut.</sZ>
</fA14>
<fA14 i1="04">
<s1>Centro de Química e Bioquímica, Faculdade de Ciências da Universidade de Lisboa</s1>
<s3>PRT</s3>
<sZ>7 aut.</sZ>
</fA14>
<fA20>
<s1>341-347</s1>
</fA20>
<fA21>
<s1>2012</s1>
</fA21>
<fA23 i1="01">
<s0>ENG</s0>
</fA23>
<fA43 i1="01">
<s1>INIST</s1>
<s2>15565</s2>
<s5>354000508852020040</s5>
</fA43>
<fA44>
<s0>0000</s0>
<s1>© 2012 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45>
<s0>3/4 p.</s0>
</fA45>
<fA47 i1="01" i2="1">
<s0>12-0407166</s0>
</fA47>
<fA60>
<s1>P</s1>
</fA60>
<fA61>
<s0>A</s0>
</fA61>
<fA64 i1="01" i2="1">
<s0>Chemosphere : (Oxford)</s0>
</fA64>
<fA66 i1="01">
<s0>GBR</s0>
</fA66>
<fC01 i1="01" l="ENG">
<s0>Fe-CO3O4 thin film with different amounts of Fe have been used for the electro-oxidation of phenol in alkaline medium at room temperature. The electrodes were prepared by coating stainless steel supports with successive layers of the oxides, obtained by thermal decomposition at 673 K. The electrolysis was carried out at constant potential and the phenol disappearance, during the electrolysis, was monitored by UV-Vis absorbance measurements between 250 and 500 nm. After 3 h of electrolysis, the intermediates were identified by comparing the HPLC data and UV-Vis spectra to those from pure standards. The results indicate that the same oxidation products are formed on the different prepared electrodes, namely the decomposition products of phenol such as benzoquinone, hydroquinone and cathecol in basic medium. Simulated results show clearly the decrease of the amount of phenolic species with the electrolysis time. An enhancement of the phenol removal is observed with the presence of iron in the oxide. Under the operating conditions, around 30% of the initial phenol has been removed at ca. 3 h and the complete degradation is obtained after 54 h of electrolysis, when Fe-Co
<sub>3</sub>
O
<sub>4</sub>
thin film with 10% of Fe is used as anode.</s0>
</fC01>
<fC02 i1="01" i2="X">
<s0>001D16A04F</s0>
</fC02>
<fC02 i1="02" i2="X">
<s0>001D16A05B</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE">
<s0>Phénols</s0>
<s2>FX</s2>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG">
<s0>Phenols</s0>
<s2>FX</s2>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA">
<s0>Fenoles</s0>
<s2>FX</s2>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE">
<s0>Oxydation</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG">
<s0>Oxidation</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA">
<s0>Oxidación</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE">
<s0>Réaction électrochimique</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG">
<s0>Electrochemical reaction</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA">
<s0>Reacción electroquímica</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE">
<s0>Oxyde de cobalt</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG">
<s0>Cobalt oxide</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA">
<s0>Cobalto óxido</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE">
<s0>Fer</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG">
<s0>Iron</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA">
<s0>Hierro</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE">
<s0>Pollution eau</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG">
<s0>Water pollution</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA">
<s0>Contaminación agua</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE">
<s0>Décontamination</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG">
<s0>Decontamination</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA">
<s0>Descontaminación</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE">
<s0>Eau usée industrielle</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG">
<s0>Industrial waste water</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA">
<s0>Agua servida industrial</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE">
<s0>Epuration eau usée</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG">
<s0>Waste water purification</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA">
<s0>Depuración aguas servidas</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE">
<s0>Epuration physicochimique</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG">
<s0>Physicochemical purification</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA">
<s0>Depuración fisicoquímica</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE">
<s0>Matériau électrode</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG">
<s0>Electrode material</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA">
<s0>Material electrodo</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE">
<s0>Electrode couche mince</s0>
<s5>13</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG">
<s0>Thin layer electrode</s0>
<s5>13</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA">
<s0>Electrodo capa fina</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE">
<s0>Electrolyse</s0>
<s5>14</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG">
<s0>Electrolysis</s0>
<s5>14</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA">
<s0>Electrólisis</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE">
<s0>Traitement électrochimique</s0>
<s5>35</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG">
<s0>Electrochemical treatment</s0>
<s5>35</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA">
<s0>Tratamiento electroquímico</s0>
<s5>35</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE">
<s0>Composé organique</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fC07 i1="01" i2="X" l="ENG">
<s0>Organic compounds</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fC07 i1="01" i2="X" l="SPA">
<s0>Compuesto orgánico</s0>
<s2>NA</s2>
<s5>43</s5>
</fC07>
<fN21>
<s1>317</s1>
</fN21>
</pA>
</standard>
</inist>
</record>

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