ThuliumV1, Pascal, Checkpoint, bibRecord, 001307

Reforming of Pd-lanthanide catalysts

Identifieur interne : 001307 ( Pascal/Checkpoint ); précédent : 001306; suivant : 001308

Reforming of Pd-lanthanide catalysts

Auteurs : N. Mahalakshmi Sita [Inde]

Source :

Indian journal of chemical technology [ 0971-457X ] ; 1997.

RBID : Pascal:97-0441293

Descripteurs français

Pascal (Inist)
- Reformage catalytique, Hydrocarbure, Cyclohexane, Heptane, Cyclopentane(méthyl), Catalyse hétérogène, Catalyseur sur support, Catalyseur mixte, Alumine, Palladium, Dysprosium, Holmium, Thulium, Activité catalytique, Site actif, Cinétique, Etude expérimentale.
Wicri :
- topic : Hydrocarbure.

English descriptors

KwdEn :
- Active site, Alumina, Catalyst activity, Catalytic reforming, Cyclohexane, Dysprosium, Experimental study, Heptane, Heterogeneous catalysis, Holmium, Hydrocarbon, Kinetics, Mixed catalyst, Palladium, Supported catalyst, Thulium.

Abstract

The reforming reactions of cyclohexane, methyl cyclopentane and n-heptane on the Pd/γ-Al₂O₃ and Pd-Ln/γ-Al₂O₃ (Ln=Dy, Ho, Tm) catalysts have been investigated. The results demonstrate that Pd-Ln/γ-Al₂O₃ catalysts evince high activity and stability compared to Pd/γ-Al₂O₃ catalysts. Owing to the different lanthanide content in the catalysts, the aromatisation and isomerization yields are different in the reforming reactions of n-heptane and cyclopentane. It is interesting to investigate the optimum content of lanthanides which gives the maximum aromatisation and isomerization yield.

Affiliations:

Inde

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

to stream Pascal, to step Corpus: 001358
to stream Pascal, to step Curation: 001358

Links to Exploration step

Pascal:97-0441293

Le document en format XML

<record><TEI><teiHeader><fileDesc><titleStmt><title xml:lang="en" level="a">Reforming of Pd-lanthanide catalysts</title>
<author><name sortKey="Mahalakshmi Sita, N" sort="Mahalakshmi Sita, N" uniqKey="Mahalakshmi Sita N" first="N." last="Mahalakshmi Sita">N. Mahalakshmi Sita</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Inorganic and Analytical Chemistry Division, Regional Research Laboratory</s1>
<s2>Trivandrum 695 019</s2>
<s3>IND</s3>
<sZ>1 aut.</sZ>
</inist:fA14>
<country>Inde</country>
<wicri:noRegion>Trivandrum 695 019</wicri:noRegion>
</affiliation>
</author>
</titleStmt>
<publicationStmt><idno type="wicri:source">INIST</idno>
<idno type="inist">97-0441293</idno>
<date when="1997">1997</date>
<idno type="stanalyst">PASCAL 97-0441293 INIST</idno>
<idno type="RBID">Pascal:97-0441293</idno>
<idno type="wicri:Area/Pascal/Corpus">001358</idno>
<idno type="wicri:Area/Pascal/Curation">001358</idno>
<idno type="wicri:Area/Pascal/Checkpoint">001307</idno>
<idno type="wicri:explorRef" wicri:stream="Pascal" wicri:step="Checkpoint">001307</idno>
</publicationStmt>
<sourceDesc><biblStruct><analytic><title xml:lang="en" level="a">Reforming of Pd-lanthanide catalysts</title>
<author><name sortKey="Mahalakshmi Sita, N" sort="Mahalakshmi Sita, N" uniqKey="Mahalakshmi Sita N" first="N." last="Mahalakshmi Sita">N. Mahalakshmi Sita</name>
<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Inorganic and Analytical Chemistry Division, Regional Research Laboratory</s1>
<s2>Trivandrum 695 019</s2>
<s3>IND</s3>
<sZ>1 aut.</sZ>
</inist:fA14>
<country>Inde</country>
<wicri:noRegion>Trivandrum 695 019</wicri:noRegion>
</affiliation>
</author>
</analytic>
<series><title level="j" type="main">Indian journal of chemical technology</title>
<idno type="ISSN">0971-457X</idno>
<imprint><date when="1997">1997</date>
</imprint>
</series>
</biblStruct>
</sourceDesc>
<seriesStmt><title level="j" type="main">Indian journal of chemical technology</title>
<idno type="ISSN">0971-457X</idno>
</seriesStmt>
</fileDesc>
<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Active site</term>
<term>Alumina</term>
<term>Catalyst activity</term>
<term>Catalytic reforming</term>
<term>Cyclohexane</term>
<term>Dysprosium</term>
<term>Experimental study</term>
<term>Heptane</term>
<term>Heterogeneous catalysis</term>
<term>Holmium</term>
<term>Hydrocarbon</term>
<term>Kinetics</term>
<term>Mixed catalyst</term>
<term>Palladium</term>
<term>Supported catalyst</term>
<term>Thulium</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Reformage catalytique</term>
<term>Hydrocarbure</term>
<term>Cyclohexane</term>
<term>Heptane</term>
<term>Cyclopentane(méthyl)</term>
<term>Catalyse hétérogène</term>
<term>Catalyseur sur support</term>
<term>Catalyseur mixte</term>
<term>Alumine</term>
<term>Palladium</term>
<term>Dysprosium</term>
<term>Holmium</term>
<term>Thulium</term>
<term>Activité catalytique</term>
<term>Site actif</term>
<term>Cinétique</term>
<term>Etude expérimentale</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Hydrocarbure</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">The reforming reactions of cyclohexane, methyl cyclopentane and n-heptane on the Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 and Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 (Ln=Dy, Ho, Tm) catalysts have been investigated. The results demonstrate that Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts evince high activity and stability compared to Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts. Owing to the different lanthanide content in the catalysts, the aromatisation and isomerization yields are different in the reforming reactions of n-heptane and cyclopentane. It is interesting to investigate the optimum content of lanthanides which gives the maximum aromatisation and isomerization yield.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="2"><s0>0971-457X</s0>
</fA01>
<fA05><s2>4</s2>
</fA05>
<fA06><s2>3</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Reforming of Pd-lanthanide catalysts</s1>
</fA08>
<fA11 i1="01" i2="1"><s1>MAHALAKSHMI SITA (N.)</s1>
</fA11>
<fA14 i1="01"><s1>Inorganic and Analytical Chemistry Division, Regional Research Laboratory</s1>
<s2>Trivandrum 695 019</s2>
<s3>IND</s3>
<sZ>1 aut.</sZ>
</fA14>
<fA20><s1>155-156</s1>
</fA20>
<fA21><s1>1997</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>2364D1</s2>
<s5>354000067758610080</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 1997 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>8 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>97-0441293</s0>
</fA47>
<fA60><s1>P</s1>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="2"><s0>Indian journal of chemical technology</s0>
</fA64>
<fA66 i1="01"><s0>IND</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>The reforming reactions of cyclohexane, methyl cyclopentane and n-heptane on the Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 and Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 (Ln=Dy, Ho, Tm) catalysts have been investigated. The results demonstrate that Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts evince high activity and stability compared to Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts. Owing to the different lanthanide content in the catalysts, the aromatisation and isomerization yields are different in the reforming reactions of n-heptane and cyclopentane. It is interesting to investigate the optimum content of lanthanides which gives the maximum aromatisation and isomerization yield.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001C01A03B</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Reformage catalytique</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Catalytic reforming</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Reformación catalítica</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="GER"><s0>Kohlenwasserstoff</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Cyclohexane</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Cyclohexane</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Ciclohexano</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Heptane</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Heptane</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Heptano</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Cyclopentane(méthyl)</s0>
<s1>ENT</s1>
<s2>NK</s2>
<s4>INC</s4>
<s5>32</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Catalyse hétérogène</s0>
<s5>35</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Heterogeneous catalysis</s0>
<s5>35</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Catálisis heterogénea</s0>
<s5>35</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Catalyseur sur support</s0>
<s5>36</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Supported catalyst</s0>
<s5>36</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Catalizador sobre soporte</s0>
<s5>36</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Catalyseur mixte</s0>
<s5>37</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Mixed catalyst</s0>
<s5>37</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Catalizador mixto</s0>
<s5>37</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Alumine</s0>
<s1>SUB</s1>
<s2>NK</s2>
<s5>38</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Alumina</s0>
<s1>SUB</s1>
<s2>NK</s2>
<s5>38</s5>
</fC03>
<fC03 i1="09" i2="X" l="GER"><s0>Tonerde</s0>
<s1>SUB</s1>
<s2>NK</s2>
<s5>38</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Alúmina</s0>
<s1>SUB</s1>
<s2>NK</s2>
<s5>38</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Palladium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>42</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Palladium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>42</s5>
</fC03>
<fC03 i1="10" i2="X" l="GER"><s0>Palladium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>42</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Paladio</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>42</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Dysprosium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>43</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Dysprosium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>43</s5>
</fC03>
<fC03 i1="11" i2="X" l="GER"><s0>Dysprosium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>43</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Disprosio</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>43</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Holmium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>44</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Holmium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>44</s5>
</fC03>
<fC03 i1="12" i2="X" l="GER"><s0>Holmium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>44</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Holmio</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>44</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Thulium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>45</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Thulium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>45</s5>
</fC03>
<fC03 i1="13" i2="X" l="GER"><s0>Thulium</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>45</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Tulio</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s5>45</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Activité catalytique</s0>
<s5>62</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Catalyst activity</s0>
<s5>62</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Actividad catalítica</s0>
<s5>62</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Site actif</s0>
<s5>63</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Active site</s0>
<s5>63</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Lugar activo</s0>
<s5>63</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Cinétique</s0>
<s5>64</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Kinetics</s0>
<s5>64</s5>
</fC03>
<fC03 i1="16" i2="X" l="GER"><s0>Kinetik</s0>
<s5>64</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Cinética</s0>
<s5>64</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Etude expérimentale</s0>
<s5>65</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Experimental study</s0>
<s5>65</s5>
</fC03>
<fC03 i1="17" i2="X" l="GER"><s0>Experimentelle Untersuchung</s0>
<s5>65</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Estudio experimental</s0>
<s5>65</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE"><s0>Métal transition</s0>
<s2>NC</s2>
<s5>39</s5>
</fC07>
<fC07 i1="01" i2="X" l="ENG"><s0>Transition metal</s0>
<s2>NC</s2>
<s5>39</s5>
</fC07>
<fC07 i1="01" i2="X" l="GER"><s0>Uebergangsmetalle</s0>
<s2>NC</s2>
<s5>39</s5>
</fC07>
<fC07 i1="01" i2="X" l="SPA"><s0>Metal transición</s0>
<s2>NC</s2>
<s5>39</s5>
</fC07>
<fC07 i1="02" i2="X" l="FRE"><s0>Platinoïde</s0>
<s2>NC</s2>
<s5>40</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG"><s0>Platinoid</s0>
<s2>NC</s2>
<s5>40</s5>
</fC07>
<fC07 i1="02" i2="X" l="GER"><s0>Platinmetalle</s0>
<s2>NC</s2>
<s5>40</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA"><s0>Platinoide</s0>
<s2>NC</s2>
<s5>40</s5>
</fC07>
<fC07 i1="03" i2="X" l="FRE"><s0>Lanthanide</s0>
<s2>NC</s2>
<s5>41</s5>
</fC07>
<fC07 i1="03" i2="X" l="ENG"><s0>Lanthanide</s0>
<s2>NC</s2>
<s5>41</s5>
</fC07>
<fC07 i1="03" i2="X" l="GER"><s0>Lanthanide</s0>
<s2>NC</s2>
<s5>41</s5>
</fC07>
<fC07 i1="03" i2="X" l="SPA"><s0>Lantánido</s0>
<s2>NC</s2>
<s5>41</s5>
</fC07>
<fN21><s1>272</s1>
</fN21>
</pA>
</standard>
</inist>
<affiliations><list><country><li>Inde</li>
</country>
</list>
<tree><country name="Inde"><noRegion><name sortKey="Mahalakshmi Sita, N" sort="Mahalakshmi Sita, N" uniqKey="Mahalakshmi Sita N" first="N." last="Mahalakshmi Sita">N. Mahalakshmi Sita</name>
</noRegion>
</country>
</tree>
</affiliations>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=$WICRI_ROOT/Wicri/Terre/explor/ThuliumV1/Data/Pascal/Checkpoint

HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 001307 | SxmlIndent | more

HfdSelect -h $EXPLOR_AREA/Data/Pascal/Checkpoint/biblio.hfd -nk 001307 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=    Wicri/Terre
   |area=    ThuliumV1
   |flux=    Pascal
   |étape=   Checkpoint
   |type=    RBID
   |clé=     Pascal:97-0441293
   |texte=   Reforming of Pd-lanthanide catalysts
}}

This area was generated with Dilib version V0.6.21.
Data generation: Thu May 12 08:27:09 2016. Site generation: Thu Mar 7 22:33:44 2024

	Serveur d'exploration sur le thulium
	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 le thulium

Reforming of Pd-lanthanide catalysts

Reforming of Pd-lanthanide catalysts

Source :

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