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The role of Pd-In interactions on the performance of PdIn-Hmordenite in the SCR of NOx with CH4

Identifieur interne : 002287 ( Main/Repository ); précédent : 002286; suivant : 002288

The role of Pd-In interactions on the performance of PdIn-Hmordenite in the SCR of NOx with CH4

Auteurs : RBID : Pascal:11-0458784

Descripteurs français

English descriptors

Abstract

The aims of this work were to use several techniques to characterize the generated species when indium and palladium were successively exchanged in H-mordenite and to investigate the effect of the Pd/In ratio on the said species as well as to correlate the activity of the prepared solids with the formed moieties. We studied the activity of In-Hmordenite catalysts obtained by reductive solid-state ion exchange and the effect of the addition of Pd. There was a clear correlation between the maximum catalytic activity of each catalyst and its ability to form NO2 in the temperature-programmed desorption of NO (NO-TPD) experiments performed after NO adsorption. PdInHM(1/3) was the catalyst that showed the best results in activity and, after the first catalytic test, it was further activated. The temperature-programmed reduction (TPR) and NO-TPD results of this solid suggest that the amount of active species increased after the reaction and that there would be some kind of Pd-In interaction. The characterization of the fresh and used samples by CO adsorption and FTIR shows the differences between PdInHM(1/3) and PdInHM(1/6) catalysts in terms of how Pd was present on the support, and justifies the different catalytic behavior of both catalysts.

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Pascal:11-0458784

Le document en format XML

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<div type="abstract" xml:lang="en">The aims of this work were to use several techniques to characterize the generated species when indium and palladium were successively exchanged in H-mordenite and to investigate the effect of the Pd/In ratio on the said species as well as to correlate the activity of the prepared solids with the formed moieties. We studied the activity of In-Hmordenite catalysts obtained by reductive solid-state ion exchange and the effect of the addition of Pd. There was a clear correlation between the maximum catalytic activity of each catalyst and its ability to form NO
<sub>2</sub>
in the temperature-programmed desorption of NO (NO-TPD) experiments performed after NO adsorption. PdInHM(1/3) was the catalyst that showed the best results in activity and, after the first catalytic test, it was further activated. The temperature-programmed reduction (TPR) and NO-TPD results of this solid suggest that the amount of active species increased after the reaction and that there would be some kind of Pd-In interaction. The characterization of the fresh and used samples by CO adsorption and FTIR shows the differences between PdInHM(1/3) and PdInHM(1/6) catalysts in terms of how Pd was present on the support, and justifies the different catalytic behavior of both catalysts.</div>
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<sub>2</sub>
in the temperature-programmed desorption of NO (NO-TPD) experiments performed after NO adsorption. PdInHM(1/3) was the catalyst that showed the best results in activity and, after the first catalytic test, it was further activated. The temperature-programmed reduction (TPR) and NO-TPD results of this solid suggest that the amount of active species increased after the reaction and that there would be some kind of Pd-In interaction. The characterization of the fresh and used samples by CO adsorption and FTIR shows the differences between PdInHM(1/3) and PdInHM(1/6) catalysts in terms of how Pd was present on the support, and justifies the different catalytic behavior of both catalysts.</s0>
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<s5>03</s5>
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<s5>03</s5>
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<s5>05</s5>
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<s0>Adsorption</s0>
<s5>05</s5>
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<s5>07</s5>
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<s2>NC</s2>
<s5>08</s5>
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<s0>Palladium</s0>
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<s5>08</s5>
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<s2>NC</s2>
<s5>08</s5>
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<s0>Platinoïde</s0>
<s2>NC</s2>
<s5>09</s5>
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<s2>NC</s2>
<s5>09</s5>
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<s0>Platinoide</s0>
<s2>NC</s2>
<s5>09</s5>
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<s0>Mordénite</s0>
<s5>10</s5>
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<s0>Mordenite</s0>
<s5>10</s5>
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<s0>Mordenita</s0>
<s5>10</s5>
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<s0>Solide</s0>
<s5>11</s5>
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<s0>Solid</s0>
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<s5>13</s5>
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<s5>13</s5>
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<s0>Echange ion</s0>
<s5>14</s5>
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<fC03 i1="14" i2="X" l="ENG">
<s0>Ion exchange</s0>
<s5>14</s5>
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<s0>Cambio iónico</s0>
<s5>14</s5>
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<s0>Corrélation</s0>
<s5>15</s5>
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<s5>15</s5>
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<s5>15</s5>
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<s0>Réaction catalytique</s0>
<s5>16</s5>
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<s5>16</s5>
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<s5>16</s5>
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<s5>17</s5>
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<s0>Thermodesorption</s0>
<s5>17</s5>
</fC03>
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<s0>Desabsorción térmica</s0>
<s5>17</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE">
<s0>Caractérisation</s0>
<s5>18</s5>
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<fC03 i1="18" i2="X" l="ENG">
<s0>Characterization</s0>
<s5>18</s5>
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<fC03 i1="18" i2="X" l="SPA">
<s0>Caracterización</s0>
<s5>18</s5>
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<fC03 i1="19" i2="X" l="FRE">
<s0>Support</s0>
<s5>19</s5>
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<fC03 i1="19" i2="X" l="ENG">
<s0>Support</s0>
<s5>19</s5>
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<s0>Soporte</s0>
<s5>19</s5>
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<s2>NC</s2>
<s5>20</s5>
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<s0>Transition metal</s0>
<s2>NC</s2>
<s5>20</s5>
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<s0>Metal transición</s0>
<s2>NC</s2>
<s5>20</s5>
</fC07>
<fC07 i1="02" i2="X" l="FRE">
<s0>Zéolite</s0>
<s5>21</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG">
<s0>Zeolite</s0>
<s5>21</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA">
<s0>Zeolita</s0>
<s5>21</s5>
</fC07>
<fC07 i1="03" i2="X" l="FRE">
<s0>Tamis moléculaire</s0>
<s5>22</s5>
</fC07>
<fC07 i1="03" i2="X" l="ENG">
<s0>Molecular sieve</s0>
<s5>22</s5>
</fC07>
<fC07 i1="03" i2="X" l="SPA">
<s0>Tamiz molecular</s0>
<s5>22</s5>
</fC07>
<fN21>
<s1>319</s1>
</fN21>
<fN44 i1="01">
<s1>OTO</s1>
</fN44>
<fN82>
<s1>OTO</s1>
</fN82>
</pA>
<pR>
<fA30 i1="01" i2="1" l="ENG">
<s1>SICAT Iberoamerican Congress on Catalysis</s1>
<s2>22</s2>
<s3>Cón-Cón, Viña del Mar CHL</s3>
<s4>2010-09-05</s4>
</fA30>
</pR>
</standard>
</inist>
</record>

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