Serveur d'exploration sur le cobalt au Maghreb

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In-situ Mössbauer spectroscopic study of iron site evolution in iron and cobalt molybdates catalysts in propene oxidation reaction conditions

Identifieur interne : 000349 ( PascalFrancis/Curation ); précédent : 000348; suivant : 000350

In-situ Mössbauer spectroscopic study of iron site evolution in iron and cobalt molybdates catalysts in propene oxidation reaction conditions

Auteurs : B. Benaichouba [Algérie] ; P. Bussiere [France] ; J. C. Vedrine [France]

Source :

RBID : Pascal:95-0549176

Descripteurs français

English descriptors

Abstract

In-situ Mössbauer spectroscopy was used to study Fexco1-xMoO4 molybdates and their mixtures with Bi2(MoO4)3 in the 360-415°C range under a flow of a mixture C3H6/02/NS=100/100/560 Torr. Ferrous molybdate FeMo04 was progressively oxidized to ferric molybdate and ferric oxide. Mixed cobalt and iron molybdates Fexco1-xMoO4 exhibited the following behaviour : (1) for all iron contents, the α phase spectrum diminished to the benefit of the β phase. The Fe3+ sites of the solid solution underwent reduction. At high iron content, the Fe3+ in Fe2(MoO4)3 was detected and diminished by half under catalytic conditions ; (2) when Bi2(MoO4)3 was added to FexCo1-xMoO4, there was no reduction of Fe3+ sites in the solid solution. The α → β phase transition was not observed in the case of the low and medium iron contents. In the high iron content samples the α-phase spectrum decreased to the expense of the β phase but did not disappear totally after catalytic reaction. It is concluded that cobalt stabilizes Fe2+ sites in the solid solution while Bi2(MoO4) stabilizes Fe3+ in the solid solution. It is proposed that Fe2+-Fe3+ pairs take an important place in the mechanism of propene mild oxidation.
pA  
A01 01  1    @0 0926-860X
A03   1    @0 Appl. catal., A Gen.
A05       @2 130
A06       @2 1
A08 01  1  ENG  @1 In-situ Mössbauer spectroscopic study of iron site evolution in iron and cobalt molybdates catalysts in propene oxidation reaction conditions
A11 01  1    @1 BENAICHOUBA (B.)
A11 02  1    @1 BUSSIERE (P.)
A11 03  1    @1 VEDRINE (J. C.)
A14 01      @1 Ecole normale supérieure Mostaganem, lab. spectroscopie matériaux @2 27000 Mostaganem @3 DZA @Z 1 aut.
A14 02      @1 CNRS Univ. Claude Bernard, inst. rech. catalyse @2 69626 Villeurbanne @3 FRA @Z 2 aut. @Z 3 aut.
A20       @1 31-45
A21       @1 1995
A23 01      @0 ENG
A43 01      @1 INIST @2 18840A @5 354000050026060040
A44       @0 0000
A45       @0 21 ref.
A47 01  1    @0 95-0549176
A60       @1 P
A61       @0 A
A64 01  1    @0 Applied catalysis. A, General
A66 01      @0 NLD
C01 01    ENG  @0 In-situ Mössbauer spectroscopy was used to study Fexco1-xMoO4 molybdates and their mixtures with Bi2(MoO4)3 in the 360-415°C range under a flow of a mixture C3H6/02/NS=100/100/560 Torr. Ferrous molybdate FeMo04 was progressively oxidized to ferric molybdate and ferric oxide. Mixed cobalt and iron molybdates Fexco1-xMoO4 exhibited the following behaviour : (1) for all iron contents, the α phase spectrum diminished to the benefit of the β phase. The Fe3+ sites of the solid solution underwent reduction. At high iron content, the Fe3+ in Fe2(MoO4)3 was detected and diminished by half under catalytic conditions ; (2) when Bi2(MoO4)3 was added to FexCo1-xMoO4, there was no reduction of Fe3+ sites in the solid solution. The α → β phase transition was not observed in the case of the low and medium iron contents. In the high iron content samples the α-phase spectrum decreased to the expense of the β phase but did not disappear totally after catalytic reaction. It is concluded that cobalt stabilizes Fe2+ sites in the solid solution while Bi2(MoO4) stabilizes Fe3+ in the solid solution. It is proposed that Fe2+-Fe3+ pairs take an important place in the mechanism of propene mild oxidation.
C02 01  1    @0 001C01A03A
C03 01  X  FRE  @0 Etude expérimentale @5 01
C03 01  X  ENG  @0 Experimental study @5 01
C03 01  X  GER  @0 Experimentelle Untersuchung @5 01
C03 01  X  SPA  @0 Estudio experimental @5 01
C03 02  X  FRE  @0 Spectrométrie Mössbauer @5 03
C03 02  X  ENG  @0 Moessbauer spectrometry @5 03
C03 02  X  GER  @0 Moessbauer Spektrometrie @5 03
C03 02  X  SPA  @0 Espectrometría Mössbauer @5 03
C03 03  X  FRE  @0 Catalyseur @5 05
C03 03  X  ENG  @0 Catalyst @5 05
C03 03  X  GER  @0 Katalysator @5 05
C03 03  X  SPA  @0 Catalizador @5 05
C03 04  X  FRE  @0 Fer Oxyde @1 ACT @2 NC @2 NA @5 07
C03 04  X  ENG  @0 Iron Oxides @1 ACT @2 NC @2 NA @5 07
C03 04  X  SPA  @0 Hierro Óxido @1 ACT @2 NC @2 NA @5 07
C03 05  X  FRE  @0 Cobalt Oxyde @1 ACT @2 NC @2 NA @5 08
C03 05  X  ENG  @0 Cobalt Oxides @1 ACT @2 NC @2 NA @5 08
C03 05  X  SPA  @0 Cobalto Óxido @1 ACT @2 NC @2 NA @5 08
C03 06  X  FRE  @0 Molybdène Oxyde @1 ACT @2 NC @2 FX @2 NA @5 09
C03 06  X  ENG  @0 Molybdenum Oxides @1 ACT @2 NC @2 FX @2 NA @5 09
C03 06  X  SPA  @0 Molibdeno Óxido @1 ACT @2 NC @2 FX @2 NA @5 09
C03 07  X  FRE  @0 Bismuth Oxyde @1 ACT @2 NC @2 NA @5 10
C03 07  X  ENG  @0 Bismuth Oxides @1 ACT @2 NC @2 NA @5 10
C03 07  X  SPA  @0 Bismuto Óxido @1 ACT @2 NC @2 NA @5 10
C03 08  X  FRE  @0 Réaction catalytique @5 12
C03 08  X  ENG  @0 Catalytic reaction @5 12
C03 08  X  SPA  @0 Reacción catalítica @5 12
C03 09  X  FRE  @0 Oxydation @5 13
C03 09  X  ENG  @0 Oxidation @5 13
C03 09  X  GER  @0 Oxidation @5 13
C03 09  X  SPA  @0 Oxidación @5 13
C03 10  X  FRE  @0 Hydrocarbure @2 FX @5 14
C03 10  X  ENG  @0 Hydrocarbon @2 FX @5 14
C03 10  X  GER  @0 Kohlenwasserstoff @2 FX @5 14
C03 10  X  SPA  @0 Hidrocarburo @2 FX @5 14
C03 11  X  FRE  @0 Composé éthylénique @5 15
C03 11  X  ENG  @0 Ethylenic compound @5 15
C03 11  X  SPA  @0 Compuesto etilénico @5 15
C03 12  X  FRE  @0 Propène @1 ENT @2 NK @5 16
C03 12  X  ENG  @0 Propene @1 ENT @2 NK @5 16
C03 12  X  SPA  @0 Propeno @1 ENT @2 NK @5 16
C03 13  X  FRE  @0 Acroléine @1 FIN @2 NK @2 FX @5 18
C03 13  X  ENG  @0 Acrolein @1 FIN @2 NK @2 FX @5 18
C03 13  X  SPA  @0 Acroleína @1 FIN @2 NK @2 FX @5 18
C03 14  X  FRE  @0 Catalyse hétérogène @5 19
C03 14  X  ENG  @0 Heterogeneous catalysis @5 19
C03 14  X  SPA  @0 Catálisis heterogénea @5 19
C03 15  X  FRE  @0 FexCo1-xMoO4 @4 INC @5 32
C03 16  X  FRE  @0 Co Fe Mo O @4 INC @5 33
C03 17  X  FRE  @0 Composé quaternaire @4 CD @5 96
C03 17  X  ENG  @0 Quaternary compound @4 CD @5 96
C07 01  X  FRE  @0 Métal transition Composé @2 NC @2 NA @5 06
C07 01  X  ENG  @0 Transition metal Compounds @2 NC @2 NA @5 06
C07 01  X  SPA  @0 Metal transición Compuesto @2 NC @2 NA @5 06
N21       @1 317

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<name sortKey="Bussiere, P" sort="Bussiere, P" uniqKey="Bussiere P" first="P." last="Bussiere">P. Bussiere</name>
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<title xml:lang="en" level="a">In-situ Mössbauer spectroscopic study of iron site evolution in iron and cobalt molybdates catalysts in propene oxidation reaction conditions</title>
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<sZ>2 aut.</sZ>
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</inist:fA14>
<country>France</country>
</affiliation>
</author>
<author>
<name sortKey="Vedrine, J C" sort="Vedrine, J C" uniqKey="Vedrine J" first="J. C." last="Vedrine">J. C. Vedrine</name>
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<title level="j" type="main">Applied catalysis. A, General</title>
<title level="j" type="abbreviated">Appl. catal., A Gen.</title>
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<title level="j" type="main">Applied catalysis. A, General</title>
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<idno type="ISSN">0926-860X</idno>
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<keywords scheme="KwdEn" xml:lang="en">
<term>Acrolein</term>
<term>Bismuth Oxides</term>
<term>Catalyst</term>
<term>Catalytic reaction</term>
<term>Cobalt Oxides</term>
<term>Ethylenic compound</term>
<term>Experimental study</term>
<term>Heterogeneous catalysis</term>
<term>Hydrocarbon</term>
<term>Iron Oxides</term>
<term>Moessbauer spectrometry</term>
<term>Molybdenum Oxides</term>
<term>Oxidation</term>
<term>Propene</term>
<term>Quaternary compound</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr">
<term>Etude expérimentale</term>
<term>Spectrométrie Mössbauer</term>
<term>Catalyseur</term>
<term>Fer Oxyde</term>
<term>Cobalt Oxyde</term>
<term>Molybdène Oxyde</term>
<term>Bismuth Oxyde</term>
<term>Réaction catalytique</term>
<term>Oxydation</term>
<term>Hydrocarbure</term>
<term>Composé éthylénique</term>
<term>Propène</term>
<term>Acroléine</term>
<term>Catalyse hétérogène</term>
<term>FexCo1-xMoO4</term>
<term>Co Fe Mo O</term>
<term>Composé quaternaire</term>
</keywords>
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<term>Hydrocarbure</term>
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<div type="abstract" xml:lang="en">In-situ Mössbauer spectroscopy was used to study Fe
<sub>x</sub>
co
<sub>1-x</sub>
MoO
<sub>4</sub>
molybdates and their mixtures with Bi
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
in the 360-415°C range under a flow of a mixture C
<sub>3</sub>
H
<sub>6</sub>
/0
<sub>2</sub>
/N
<sub>S</sub>
=100/100/560 Torr. Ferrous molybdate FeMo0
<sub>4</sub>
was progressively oxidized to ferric molybdate and ferric oxide. Mixed cobalt and iron molybdates Fe
<sub>x</sub>
co
<sub>1-x</sub>
MoO
<sub>4</sub>
exhibited the following behaviour : (1) for all iron contents, the α phase spectrum diminished to the benefit of the β phase. The Fe
<sup>3+</sup>
sites of the solid solution underwent reduction. At high iron content, the Fe
<sup>3+</sup>
in Fe
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
was detected and diminished by half under catalytic conditions ; (2) when Bi
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
was added to Fe
<sub>x</sub>
Co
<sub>1-x</sub>
MoO
<sub>4</sub>
, there was no reduction of Fe
<sup>3+</sup>
sites in the solid solution. The α → β phase transition was not observed in the case of the low and medium iron contents. In the high iron content samples the α-phase spectrum decreased to the expense of the β phase but did not disappear totally after catalytic reaction. It is concluded that cobalt stabilizes Fe
<sup>2+</sup>
sites in the solid solution while Bi
<sub>2</sub>
(MoO
<sub>4</sub>
) stabilizes Fe
<sup>3+</sup>
in the solid solution. It is proposed that Fe
<sup>2+</sup>
-Fe
<sup>3+</sup>
pairs take an important place in the mechanism of propene mild oxidation.</div>
</front>
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<fA05>
<s2>130</s2>
</fA05>
<fA06>
<s2>1</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG">
<s1>In-situ Mössbauer spectroscopic study of iron site evolution in iron and cobalt molybdates catalysts in propene oxidation reaction conditions</s1>
</fA08>
<fA11 i1="01" i2="1">
<s1>BENAICHOUBA (B.)</s1>
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<s1>BUSSIERE (P.)</s1>
</fA11>
<fA11 i1="03" i2="1">
<s1>VEDRINE (J. C.)</s1>
</fA11>
<fA14 i1="01">
<s1>Ecole normale supérieure Mostaganem, lab. spectroscopie matériaux</s1>
<s2>27000 Mostaganem</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
</fA14>
<fA14 i1="02">
<s1>CNRS Univ. Claude Bernard, inst. rech. catalyse</s1>
<s2>69626 Villeurbanne</s2>
<s3>FRA</s3>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
</fA14>
<fA20>
<s1>31-45</s1>
</fA20>
<fA21>
<s1>1995</s1>
</fA21>
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<s5>354000050026060040</s5>
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<s0>A</s0>
</fA61>
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</fA64>
<fA66 i1="01">
<s0>NLD</s0>
</fA66>
<fC01 i1="01" l="ENG">
<s0>In-situ Mössbauer spectroscopy was used to study Fe
<sub>x</sub>
co
<sub>1-x</sub>
MoO
<sub>4</sub>
molybdates and their mixtures with Bi
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
in the 360-415°C range under a flow of a mixture C
<sub>3</sub>
H
<sub>6</sub>
/0
<sub>2</sub>
/N
<sub>S</sub>
=100/100/560 Torr. Ferrous molybdate FeMo0
<sub>4</sub>
was progressively oxidized to ferric molybdate and ferric oxide. Mixed cobalt and iron molybdates Fe
<sub>x</sub>
co
<sub>1-x</sub>
MoO
<sub>4</sub>
exhibited the following behaviour : (1) for all iron contents, the α phase spectrum diminished to the benefit of the β phase. The Fe
<sup>3+</sup>
sites of the solid solution underwent reduction. At high iron content, the Fe
<sup>3+</sup>
in Fe
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
was detected and diminished by half under catalytic conditions ; (2) when Bi
<sub>2</sub>
(MoO
<sub>4</sub>
)
<sub>3</sub>
was added to Fe
<sub>x</sub>
Co
<sub>1-x</sub>
MoO
<sub>4</sub>
, there was no reduction of Fe
<sup>3+</sup>
sites in the solid solution. The α → β phase transition was not observed in the case of the low and medium iron contents. In the high iron content samples the α-phase spectrum decreased to the expense of the β phase but did not disappear totally after catalytic reaction. It is concluded that cobalt stabilizes Fe
<sup>2+</sup>
sites in the solid solution while Bi
<sub>2</sub>
(MoO
<sub>4</sub>
) stabilizes Fe
<sup>3+</sup>
in the solid solution. It is proposed that Fe
<sup>2+</sup>
-Fe
<sup>3+</sup>
pairs take an important place in the mechanism of propene mild oxidation.</s0>
</fC01>
<fC02 i1="01" i2="1">
<s0>001C01A03A</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE">
<s0>Etude expérimentale</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG">
<s0>Experimental study</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="GER">
<s0>Experimentelle Untersuchung</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA">
<s0>Estudio experimental</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE">
<s0>Spectrométrie Mössbauer</s0>
<s5>03</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG">
<s0>Moessbauer spectrometry</s0>
<s5>03</s5>
</fC03>
<fC03 i1="02" i2="X" l="GER">
<s0>Moessbauer Spektrometrie</s0>
<s5>03</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA">
<s0>Espectrometría Mössbauer</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE">
<s0>Catalyseur</s0>
<s5>05</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG">
<s0>Catalyst</s0>
<s5>05</s5>
</fC03>
<fC03 i1="03" i2="X" l="GER">
<s0>Katalysator</s0>
<s5>05</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA">
<s0>Catalizador</s0>
<s5>05</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE">
<s0>Fer Oxyde</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>07</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG">
<s0>Iron Oxides</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>07</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA">
<s0>Hierro Óxido</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>07</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE">
<s0>Cobalt Oxyde</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>08</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG">
<s0>Cobalt Oxides</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>08</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA">
<s0>Cobalto Óxido</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>08</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE">
<s0>Molybdène Oxyde</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>FX</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG">
<s0>Molybdenum Oxides</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>FX</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA">
<s0>Molibdeno Óxido</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>FX</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE">
<s0>Bismuth Oxyde</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG">
<s0>Bismuth Oxides</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA">
<s0>Bismuto Óxido</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE">
<s0>Réaction catalytique</s0>
<s5>12</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG">
<s0>Catalytic reaction</s0>
<s5>12</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA">
<s0>Reacción catalítica</s0>
<s5>12</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE">
<s0>Oxydation</s0>
<s5>13</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG">
<s0>Oxidation</s0>
<s5>13</s5>
</fC03>
<fC03 i1="09" i2="X" l="GER">
<s0>Oxidation</s0>
<s5>13</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA">
<s0>Oxidación</s0>
<s5>13</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE">
<s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG">
<s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="10" i2="X" l="GER">
<s0>Kohlenwasserstoff</s0>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA">
<s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE">
<s0>Composé éthylénique</s0>
<s5>15</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG">
<s0>Ethylenic compound</s0>
<s5>15</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA">
<s0>Compuesto etilénico</s0>
<s5>15</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE">
<s0>Propène</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>16</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG">
<s0>Propene</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>16</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA">
<s0>Propeno</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>16</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE">
<s0>Acroléine</s0>
<s1>FIN</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>18</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG">
<s0>Acrolein</s0>
<s1>FIN</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>18</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA">
<s0>Acroleína</s0>
<s1>FIN</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>18</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE">
<s0>Catalyse hétérogène</s0>
<s5>19</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG">
<s0>Heterogeneous catalysis</s0>
<s5>19</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA">
<s0>Catálisis heterogénea</s0>
<s5>19</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE">
<s0>FexCo1-xMoO4</s0>
<s4>INC</s4>
<s5>32</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE">
<s0>Co Fe Mo O</s0>
<s4>INC</s4>
<s5>33</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE">
<s0>Composé quaternaire</s0>
<s4>CD</s4>
<s5>96</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG">
<s0>Quaternary compound</s0>
<s4>CD</s4>
<s5>96</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE">
<s0>Métal transition Composé</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>06</s5>
</fC07>
<fC07 i1="01" i2="X" l="ENG">
<s0>Transition metal Compounds</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>06</s5>
</fC07>
<fC07 i1="01" i2="X" l="SPA">
<s0>Metal transición Compuesto</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>06</s5>
</fC07>
<fN21>
<s1>317</s1>
</fN21>
</pA>
</standard>
</inist>
</record>

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