IndiumV3, Main, Repository, bibRecord, 001B57

Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NOx-SCR with CH4

Identifieur interne : 001B57 ( Main/Repository ); précédent : 001B56; suivant : 001B58

Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NOx-SCR with CH4

Auteurs : RBID : Pascal:12-0414522

Descripteurs français

Pascal (Inist)
- Catalyseur, Réduction chimique, Méthane, Spectrométrie IR, Oxyde d'azote, Synergie, Microscopie électronique transmission, Matériau poreux, Réaction catalytique, Mordénite, Activité catalytique, Palladium, Platinoïde, Solide, Site adsorption, Indium, Particule, Agglomération, Spectrométrie photoélectron, Rayon X, Catalyse hétérogène.
Wicri :
- concept : Agglomération.

English descriptors

KwdEn :
- Adsorption site, Agglomeration, Catalyst, Catalyst activity, Catalytic reaction, Chemical reduction, Heterogeneous catalysis, Indium, Infrared spectrometry, Methane, Mordenite, Nitrogen oxide, Palladium, Particle, Photoelectron spectrometry, Platinoid, Porous material, Solid, Synergism, Transmission electron microscopy, X ray.

Abstract

The addition of Pd improves the catalytic performance of InH mordenite for the SCR of NO with methane, but this effect depends on the In/Al ratio. We studied two PdlnMordenite samples, one with In/Al = 1/3 (PdInHM(1/3)) and the other with In/Al = 1/6 (PdInHM(1/6)). While in the former the presence of Pd in the InHM(1/3) catalyst increased the activity, in the sample with lower In content this effect was not observed. In order to explain these observations, the catalysts were characterized with several techniques. TPR results showed that the presence of palladium shifted the reduction peak of the solid PdInHM(1/3) towards higher temperatures, while on solid PdInHM(1/6), the shift was negligible. This effect could be ascribed to a higher Pd-In interaction in the PdInHM(1/3) catalyst. FTIR of CO adsorbed showed the presence of Pd²⁺, Pd⁺ and Pd⁰ adsorption sites in the calcined PdInHM(1/3). However, in the case of PdInHM(1/6), there was no evidence of Pd²⁺ species. The TEM images of used PdInHM(1/3) catalysts suggested the mobilization of indium to inner positions into the matrix, thus increasing the interactions with Pd. In the fresh PdInHM(1/6) the indium particles could not be detected but after reaction some agglomeration of particles could be observed, which is in agreement with CO-FTIR and XPS results. In brief, the results indicate that in the PdInHM(1/3) catalyst, Pd and In interact closely, giving place to a promotional effect of Pd, which prevents the agglomeration of In species.

Links toward previous steps (curation, corpus...)

to stream Main, to step Corpus: 001687

Links to Exploration step

Pascal:12-0414522

Le document en format XML

<record><TEI><teiHeader><fileDesc><titleStmt><title xml:lang="en" level="a">Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NO<sub>x</sub>
-SCR with CH<sub>4</sub>
</title>
<author><name sortKey="Gutierrez, Laura" uniqKey="Gutierrez L">Laura Gutierrez</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Instituto de Investigaciones en Catálisis y Petroquímica, INCAPE (FIQ, UNL - CONICET), Santiago del Estero 2829</s1>
<s2>3000, Santa Fe</s2>
<s3>ARG</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>6 aut.</sZ>
</inist:fA14>
<country>Argentine</country>
<wicri:noRegion>3000, Santa Fe</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Boix, Alicia" uniqKey="Boix A">Alicia Boix</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Instituto de Investigaciones en Catálisis y Petroquímica, INCAPE (FIQ, UNL - CONICET), Santiago del Estero 2829</s1>
<s2>3000, Santa Fe</s2>
<s3>ARG</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>6 aut.</sZ>
</inist:fA14>
<country>Argentine</country>
<wicri:noRegion>3000, Santa Fe</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Decolatti, Hernan" uniqKey="Decolatti H">Hernan Decolatti</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Instituto de Investigaciones en Catálisis y Petroquímica, INCAPE (FIQ, UNL - CONICET), Santiago del Estero 2829</s1>
<s2>3000, Santa Fe</s2>
<s3>ARG</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>6 aut.</sZ>
</inist:fA14>
<country>Argentine</country>
<wicri:noRegion>3000, Santa Fe</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Solt, Hanna" uniqKey="Solt H">Hanna Solt</name>
<affiliation wicri:level="1"><inist:fA14 i1="02"><s1>Institute of Nanochemistry and Catalysis, Chemical Research Center, Hungarian Academy of Sciences, Pusztaszeri ut. 59-67</s1>
<s2>1025 Budapest</s2>
<s3>HUN</s3>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Hongrie</country>
<placeName><settlement type="city">Budapest</settlement>
<region nuts="2">Hongrie centrale</region>
</placeName>
</affiliation>
</author>
<author><name sortKey="Lonyi, Ferenc" uniqKey="Lonyi F">Ferenc Lonyi</name>
<affiliation wicri:level="1"><inist:fA14 i1="02"><s1>Institute of Nanochemistry and Catalysis, Chemical Research Center, Hungarian Academy of Sciences, Pusztaszeri ut. 59-67</s1>
<s2>1025 Budapest</s2>
<s3>HUN</s3>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Hongrie</country>
<placeName><settlement type="city">Budapest</settlement>
<region nuts="2">Hongrie centrale</region>
</placeName>
</affiliation>
</author>
<author><name sortKey="Miro, Eduardo" uniqKey="Miro E">Eduardo Miro</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Instituto de Investigaciones en Catálisis y Petroquímica, INCAPE (FIQ, UNL - CONICET), Santiago del Estero 2829</s1>
<s2>3000, Santa Fe</s2>
<s3>ARG</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>6 aut.</sZ>
</inist:fA14>
<country>Argentine</country>
<wicri:noRegion>3000, Santa Fe</wicri:noRegion>
</affiliation>
</author>
</titleStmt>
<publicationStmt><idno type="inist">12-0414522</idno>
<date when="2012">2012</date>
<idno type="stanalyst">PASCAL 12-0414522 INIST</idno>
<idno type="RBID">Pascal:12-0414522</idno>
<idno type="wicri:Area/Main/Corpus">001687</idno>
<idno type="wicri:Area/Main/Repository">001B57</idno>
</publicationStmt>
<seriesStmt><idno type="ISSN">1387-1811</idno>
<title level="j" type="abbreviated">Microporous mesoporous mater.</title>
<title level="j" type="main">Microporous and mesoporous materials</title>
</seriesStmt>
</fileDesc>
<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Adsorption site</term>
<term>Agglomeration</term>
<term>Catalyst</term>
<term>Catalyst activity</term>
<term>Catalytic reaction</term>
<term>Chemical reduction</term>
<term>Heterogeneous catalysis</term>
<term>Indium</term>
<term>Infrared spectrometry</term>
<term>Methane</term>
<term>Mordenite</term>
<term>Nitrogen oxide</term>
<term>Palladium</term>
<term>Particle</term>
<term>Photoelectron spectrometry</term>
<term>Platinoid</term>
<term>Porous material</term>
<term>Solid</term>
<term>Synergism</term>
<term>Transmission electron microscopy</term>
<term>X ray</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Catalyseur</term>
<term>Réduction chimique</term>
<term>Méthane</term>
<term>Spectrométrie IR</term>
<term>Oxyde d'azote</term>
<term>Synergie</term>
<term>Microscopie électronique transmission</term>
<term>Matériau poreux</term>
<term>Réaction catalytique</term>
<term>Mordénite</term>
<term>Activité catalytique</term>
<term>Palladium</term>
<term>Platinoïde</term>
<term>Solide</term>
<term>Site adsorption</term>
<term>Indium</term>
<term>Particule</term>
<term>Agglomération</term>
<term>Spectrométrie photoélectron</term>
<term>Rayon X</term>
<term>Catalyse hétérogène</term>
</keywords>
<keywords scheme="Wicri" type="concept" xml:lang="fr"><term>Agglomération</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">The addition of Pd improves the catalytic performance of InH mordenite for the SCR of NO with methane, but this effect depends on the In/Al ratio. We studied two PdlnMordenite samples, one with In/Al = 1/3 (PdInHM(1/3)) and the other with In/Al = 1/6 (PdInHM(1/6)). While in the former the presence of Pd in the InHM(1/3) catalyst increased the activity, in the sample with lower In content this effect was not observed. In order to explain these observations, the catalysts were characterized with several techniques. TPR results showed that the presence of palladium shifted the reduction peak of the solid PdInHM(1/3) towards higher temperatures, while on solid PdInHM(1/6), the shift was negligible. This effect could be ascribed to a higher Pd-In interaction in the PdInHM(1/3) catalyst. FTIR of CO adsorbed showed the presence of Pd<sup>2+</sup>
, Pd<sup>+</sup>
 and Pd<sup>0</sup>
 adsorption sites in the calcined PdInHM(1/3). However, in the case of PdInHM(1/6), there was no evidence of Pd<sup>2+</sup>
 species. The TEM images of used PdInHM(1/3) catalysts suggested the mobilization of indium to inner positions into the matrix, thus increasing the interactions with Pd. In the fresh PdInHM(1/6) the indium particles could not be detected but after reaction some agglomeration of particles could be observed, which is in agreement with CO-FTIR and XPS results. In brief, the results indicate that in the PdInHM(1/3) catalyst, Pd and In interact closely, giving place to a promotional effect of Pd, which prevents the agglomeration of In species.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>1387-1811</s0>
</fA01>
<fA03 i2="1"><s0>Microporous mesoporous mater.</s0>
</fA03>
<fA05><s2>163</s2>
</fA05>
<fA08 i1="01" i2="1" l="ENG"><s1>Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NO<sub>x</sub>
-SCR with CH<sub>4</sub>
</s1>
</fA08>
<fA11 i1="01" i2="1"><s1>GUTIERREZ (Laura)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>BOIX (Alicia)</s1>
</fA11>
<fA11 i1="03" i2="1"><s1>DECOLATTI (Hernan)</s1>
</fA11>
<fA11 i1="04" i2="1"><s1>SOLT (Hanna)</s1>
</fA11>
<fA11 i1="05" i2="1"><s1>LONYI (Ferenc)</s1>
</fA11>
<fA11 i1="06" i2="1"><s1>MIRO (Eduardo)</s1>
</fA11>
<fA14 i1="01"><s1>Instituto de Investigaciones en Catálisis y Petroquímica, INCAPE (FIQ, UNL - CONICET), Santiago del Estero 2829</s1>
<s2>3000, Santa Fe</s2>
<s3>ARG</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>6 aut.</sZ>
</fA14>
<fA14 i1="02"><s1>Institute of Nanochemistry and Catalysis, Chemical Research Center, Hungarian Academy of Sciences, Pusztaszeri ut. 59-67</s1>
<s2>1025 Budapest</s2>
<s3>HUN</s3>
<sZ>4 aut.</sZ>
<sZ>5 aut.</sZ>
</fA14>
<fA20><s1>307-320</s1>
</fA20>
<fA21><s1>2012</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>19627</s2>
<s5>354000508396620390</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2012 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>42 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>12-0414522</s0>
</fA47>
<fA60><s1>P</s1>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="1"><s0>Microporous and mesoporous materials</s0>
</fA64>
<fA66 i1="01"><s0>USA</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>The addition of Pd improves the catalytic performance of InH mordenite for the SCR of NO with methane, but this effect depends on the In/Al ratio. We studied two PdlnMordenite samples, one with In/Al = 1/3 (PdInHM(1/3)) and the other with In/Al = 1/6 (PdInHM(1/6)). While in the former the presence of Pd in the InHM(1/3) catalyst increased the activity, in the sample with lower In content this effect was not observed. In order to explain these observations, the catalysts were characterized with several techniques. TPR results showed that the presence of palladium shifted the reduction peak of the solid PdInHM(1/3) towards higher temperatures, while on solid PdInHM(1/6), the shift was negligible. This effect could be ascribed to a higher Pd-In interaction in the PdInHM(1/3) catalyst. FTIR of CO adsorbed showed the presence of Pd<sup>2+</sup>
, Pd<sup>+</sup>
 and Pd<sup>0</sup>
 adsorption sites in the calcined PdInHM(1/3). However, in the case of PdInHM(1/6), there was no evidence of Pd<sup>2+</sup>
 species. The TEM images of used PdInHM(1/3) catalysts suggested the mobilization of indium to inner positions into the matrix, thus increasing the interactions with Pd. In the fresh PdInHM(1/6) the indium particles could not be detected but after reaction some agglomeration of particles could be observed, which is in agreement with CO-FTIR and XPS results. In brief, the results indicate that in the PdInHM(1/3) catalyst, Pd and In interact closely, giving place to a promotional effect of Pd, which prevents the agglomeration of In species.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001C01J08</s0>
</fC02>
<fC02 i1="02" i2="X"><s0>001C01A03</s0>
</fC02>
<fC02 i1="03" i2="X"><s0>001C01I05A</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Catalyseur</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Catalyst</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Catalizador</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Réduction chimique</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Chemical reduction</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Reducción química</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Méthane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Methane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Metano</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Spectrométrie IR</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Infrared spectrometry</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Espectrometría IR</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Oxyde d'azote</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Nitrogen oxide</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Nitrógeno óxido</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Synergie</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Synergism</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Sinergia</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Microscopie électronique transmission</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Transmission electron microscopy</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Microscopía electrónica transmisión</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Matériau poreux</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Porous material</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Material poroso</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Réaction catalytique</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Catalytic reaction</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Reacción catalítica</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Mordénite</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Mordenite</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Mordenita</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Activité catalytique</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Catalyst activity</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Actividad catalítica</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Palladium</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Palladium</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Paladio</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Platinoïde</s0>
<s2>NC</s2>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Platinoid</s0>
<s2>NC</s2>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Platinoide</s0>
<s2>NC</s2>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Solide</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Solid</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Sólido</s0>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Site adsorption</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Adsorption site</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Sitio adsorción</s0>
<s5>15</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Indium</s0>
<s2>NC</s2>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Indium</s0>
<s2>NC</s2>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Indio</s0>
<s2>NC</s2>
<s5>16</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Particule</s0>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Particle</s0>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Partícula</s0>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Agglomération</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>Agglomeration</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Aglomeración</s0>
<s5>18</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Spectrométrie photoélectron</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Photoelectron spectrometry</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Espectrometría fotoelectrón</s0>
<s5>19</s5>
</fC03>
<fC03 i1="20" i2="X" l="FRE"><s0>Rayon X</s0>
<s5>20</s5>
</fC03>
<fC03 i1="20" i2="X" l="ENG"><s0>X ray</s0>
<s5>20</s5>
</fC03>
<fC03 i1="20" i2="X" l="SPA"><s0>Rayos X</s0>
<s5>20</s5>
</fC03>
<fC03 i1="21" i2="X" l="FRE"><s0>Catalyse hétérogène</s0>
<s5>24</s5>
</fC03>
<fC03 i1="21" i2="X" l="ENG"><s0>Heterogeneous catalysis</s0>
<s5>24</s5>
</fC03>
<fC03 i1="21" i2="X" l="SPA"><s0>Catálisis heterogénea</s0>
<s5>24</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE"><s0>Zéolite</s0>
<s5>21</s5>
</fC07>
<fC07 i1="01" i2="X" l="ENG"><s0>Zeolite</s0>
<s5>21</s5>
</fC07>
<fC07 i1="01" i2="X" l="SPA"><s0>Zeolita</s0>
<s5>21</s5>
</fC07>
<fC07 i1="02" i2="X" l="FRE"><s0>Métal transition</s0>
<s2>NC</s2>
<s5>22</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG"><s0>Transition metal</s0>
<s2>NC</s2>
<s5>22</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA"><s0>Metal transición</s0>
<s2>NC</s2>
<s5>22</s5>
</fC07>
<fC07 i1="03" i2="X" l="FRE"><s0>Tamis moléculaire</s0>
<s5>23</s5>
</fC07>
<fC07 i1="03" i2="X" l="ENG"><s0>Molecular sieve</s0>
<s5>23</s5>
</fC07>
<fC07 i1="03" i2="X" l="SPA"><s0>Tamiz molecular</s0>
<s5>23</s5>
</fC07>
<fN21><s1>324</s1>
</fN21>
</pA>
</standard>
</inist>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=IndiumV3/Data/Main/Repository

HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 001B57 | SxmlIndent | more

HfdSelect -h $EXPLOR_AREA/Data/Main/Repository/biblio.hfd -nk 001B57 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=   *** parameter Area/wikiCode missing *** 
   |area=    IndiumV3
   |flux=    Main
   |étape=   Repository
   |type=    RBID
   |clé=     Pascal:12-0414522
   |texte=   Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NOx-SCR with CH4
}}

This area was generated with Dilib version V0.5.77.
Data generation: Mon Jun 9 10:27:54 2014. Site generation: Thu Mar 7 16:19:59 2024

	Serveur d'exploration sur l'Indium
	Attention, ce site est en cours de développement ! Attention, site généré par des moyens informatiques à partir de corpus bruts. Les informations ne sont donc pas validées.

Serveur d'exploration sur l'Indium

Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NOx-SCR with CH4

Further insights on the physico-chemical aspects of PdIn-Hmordenite catalysts for the NOx-SCR with CH4

Descripteurs français

English descriptors

Abstract

Links toward previous steps (curation, corpus...)

Links to Exploration step

Le document en format XML

Pour manipuler ce document sous Unix (Dilib)

Pour mettre un lien sur cette page dans le réseau Wicri