NickelMaghrebV1, PascalFrancis, Checkpoint, bibRecord, 000115

Steam reforming of methane to syngas over NiAl2O4 spinel catalysts

Identifieur interne : 000115 ( PascalFrancis/Checkpoint ); précédent : 000114; suivant : 000116

Steam reforming of methane to syngas over NiAl2O4 spinel catalysts

Auteurs : N. Salvi [Algérie] ; A. Boulahouache [Algérie] ; C. Petit [France] ; A. Kiennemann [France] ; C. Rabia [Algérie]

Source :

International journal of hydrogen energy [ 0360-3199 ] ; 2011.

RBID : Pascal:11-0412765

Descripteurs français

Pascal (Inist)
- Reformage vapeur, Méthane, Gaz synthèse, Spinelle, Catalyseur, Oxyde de nickel, Procédé sol gel, Diffractométrie RX, Microscopie électronique balayage, Microscopie électronique transmission, Aire superficielle, Structure cristalline, Nickel, Aluminium, Matériau cristallin, Frittage, Conversion catalytique, Haute performance, Stabilité, Hydrogène.
Wicri :
- topic : Nickel, Aluminium, Hydrogène.

English descriptors

KwdEn :
- Aluminium, Catalyst, Catalytic conversion, Crystalline material, Crystalline structure, High performance, Hydrogen, Methane, Nickel, Nickel oxide, Scanning electron microscopy, Sintering, Sol gel process, Spinel, Stability, Steam reforming, Surface area, Synthesis gas, Transmission electron microscopy, X ray diffractometry.

Abstract

A series of several mixed oxides close to NiAl₂O₄ (NiAl₂O₄, 5 wt% NiO/NiAl₂O₄, 10 wt% NiO/ NiAl₂O₄ and 15 wt% NiO/NiAl₂O₄) were prepared by a pseudo sol gel method using propionic acid then calcinated at 900 °C during 4 h. The catalysts were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), transmission electron microscopy (TEM), surface areas (BET) and temperature-programmed reduction (TPR). The nature of the crystalline structure, the surface area and the reduction temperature depend on the Ni/ Al ratio. For the stoichiometric ratio Ni/Al exactly equal to 0.5, homogeneous crystalline spinel phase was formed after temperature of calcination was equal or higher than 725 °C. The spinel structure being a non-tolerant structure for an excess of Ni, when Ni/Al is higher than 0.5, free NiO in strong interaction with the spinel was present and favoured the reduction of the nickel of the structure at lower temperature compared to the spinel. Till 700 °C, the spinel structure was well conserved even if it was partially reduced. For a temperature higher than 700 °C, the structure leads to Ni species formation on γ-Al₂O₃. Comparative steam reforming of methane was conducted to control the formation of Ni and its sintering. The stoichiometric spinel showed relevant catalytic performances: high CH₄ conversion, high selectivities of CO and H₂ and low carbon formation. The presence of nickel inside the spinel structure of NiAl₂O₄ catalyst confers a high stability and strong dispersion for the metallic particles. The low formation of carbon was due to the high dispersion and the limited growing of the Ni particles on γ-Al₂O₃. Over 5 wt% of NiO excess, a rough decrease of the CH₄ conversion, CO and H₂ selectivities were observed. The x wt% NiO/NiAl₂O₄ systems give an important carbon formation due to a large Ni particle formation after rapid sintering.

Affiliations:

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

to stream PascalFrancis, to step Corpus: 000120
to stream PascalFrancis, to step Curation: 000321

Links to Exploration step

Pascal:11-0412765

Le document en format XML

<record><TEI><teiHeader><fileDesc><titleStmt><title xml:lang="en" level="a">Steam reforming of methane to syngas over NiAl2O4 spinel catalysts</title>
<author><name sortKey="Salvi, N" sort="Salvi, N" uniqKey="Salvi N" first="N." last="Salvi">N. Salvi</name>
<affiliation wicri:level="3"><inist:fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB 109, El-Alia Bab Ezzouar</s1>
<s2>Alger</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<placeName><settlement type="city">Alger</settlement>
<region nuts="2">Wilaya d'Alger</region>
</placeName>
</affiliation>
</author>
<author><name sortKey="Boulahouache, A" sort="Boulahouache, A" uniqKey="Boulahouache A" first="A." last="Boulahouache">A. Boulahouache</name>
<affiliation wicri:level="1"><inist:fA14 i1="02"><s1>Laboratoire LCPMM, département de chimie, Faculté ses sciences, U. Blida, route de soumaa, BP</s1>
<s2>Blida</s2>
<s3>DZA</s3>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Blida</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Petit, C" sort="Petit, C" uniqKey="Petit C" first="C." last="Petit">C. Petit</name>
<affiliation wicri:level="3"><inist:fA14 i1="03"><s1>Ecole de Chimie, Polymères et Matériaux - Laboratoire Matériaux, Surface, Procédés pour la Catalyse (LMSPC), UMR CNRS 7515 - 25, rue Becquerel</s1>
<s2>67087 Strasbourg</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</inist:fA14>
<country>France</country>
<placeName><region type="region" nuts="2">Grand Est</region>
<region type="old region" nuts="2">Alsace (région administrative)</region>
<settlement type="city">Strasbourg</settlement>
</placeName>
</affiliation>
</author>
<author><name sortKey="Kiennemann, A" sort="Kiennemann, A" uniqKey="Kiennemann A" first="A." last="Kiennemann">A. Kiennemann</name>
<affiliation wicri:level="3"><inist:fA14 i1="03"><s1>Ecole de Chimie, Polymères et Matériaux - Laboratoire Matériaux, Surface, Procédés pour la Catalyse (LMSPC), UMR CNRS 7515 - 25, rue Becquerel</s1>
<s2>67087 Strasbourg</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</inist:fA14>
<country>France</country>
<placeName><region type="region" nuts="2">Grand Est</region>
<region type="old region" nuts="2">Alsace (région administrative)</region>
<settlement type="city">Strasbourg</settlement>
</placeName>
</affiliation>
</author>
<author><name sortKey="Rabia, C" sort="Rabia, C" uniqKey="Rabia C" first="C." last="Rabia">C. Rabia</name>
<affiliation wicri:level="3"><inist:fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB 109, El-Alia Bab Ezzouar</s1>
<s2>Alger</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<placeName><settlement type="city">Alger</settlement>
<region nuts="2">Wilaya d'Alger</region>
</placeName>
</affiliation>
</author>
</titleStmt>
<publicationStmt><idno type="wicri:source">INIST</idno>
<idno type="inist">11-0412765</idno>
<date when="2011">2011</date>
<idno type="stanalyst">PASCAL 11-0412765 INIST</idno>
<idno type="RBID">Pascal:11-0412765</idno>
<idno type="wicri:Area/PascalFrancis/Corpus">000120</idno>
<idno type="wicri:Area/PascalFrancis/Curation">000321</idno>
<idno type="wicri:Area/PascalFrancis/Checkpoint">000115</idno>
<idno type="wicri:explorRef" wicri:stream="PascalFrancis" wicri:step="Checkpoint">000115</idno>
</publicationStmt>
<sourceDesc><biblStruct><analytic><title xml:lang="en" level="a">Steam reforming of methane to syngas over NiAl2O4 spinel catalysts</title>
<author><name sortKey="Salvi, N" sort="Salvi, N" uniqKey="Salvi N" first="N." last="Salvi">N. Salvi</name>
<affiliation wicri:level="3"><inist:fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB 109, El-Alia Bab Ezzouar</s1>
<s2>Alger</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<placeName><settlement type="city">Alger</settlement>
<region nuts="2">Wilaya d'Alger</region>
</placeName>
</affiliation>
</author>
<author><name sortKey="Boulahouache, A" sort="Boulahouache, A" uniqKey="Boulahouache A" first="A." last="Boulahouache">A. Boulahouache</name>
<affiliation wicri:level="1"><inist:fA14 i1="02"><s1>Laboratoire LCPMM, département de chimie, Faculté ses sciences, U. Blida, route de soumaa, BP</s1>
<s2>Blida</s2>
<s3>DZA</s3>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Blida</wicri:noRegion>
</affiliation>
</author>
<author><name sortKey="Petit, C" sort="Petit, C" uniqKey="Petit C" first="C." last="Petit">C. Petit</name>
<affiliation wicri:level="3"><inist:fA14 i1="03"><s1>Ecole de Chimie, Polymères et Matériaux - Laboratoire Matériaux, Surface, Procédés pour la Catalyse (LMSPC), UMR CNRS 7515 - 25, rue Becquerel</s1>
<s2>67087 Strasbourg</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</inist:fA14>
<country>France</country>
<placeName><region type="region" nuts="2">Grand Est</region>
<region type="old region" nuts="2">Alsace (région administrative)</region>
<settlement type="city">Strasbourg</settlement>
</placeName>
</affiliation>
</author>
<author><name sortKey="Kiennemann, A" sort="Kiennemann, A" uniqKey="Kiennemann A" first="A." last="Kiennemann">A. Kiennemann</name>
<affiliation wicri:level="3"><inist:fA14 i1="03"><s1>Ecole de Chimie, Polymères et Matériaux - Laboratoire Matériaux, Surface, Procédés pour la Catalyse (LMSPC), UMR CNRS 7515 - 25, rue Becquerel</s1>
<s2>67087 Strasbourg</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</inist:fA14>
<country>France</country>
<placeName><region type="region" nuts="2">Grand Est</region>
<region type="old region" nuts="2">Alsace (région administrative)</region>
<settlement type="city">Strasbourg</settlement>
</placeName>
</affiliation>
</author>
<author><name sortKey="Rabia, C" sort="Rabia, C" uniqKey="Rabia C" first="C." last="Rabia">C. Rabia</name>
<affiliation wicri:level="3"><inist:fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB 109, El-Alia Bab Ezzouar</s1>
<s2>Alger</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>5 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<placeName><settlement type="city">Alger</settlement>
<region nuts="2">Wilaya d'Alger</region>
</placeName>
</affiliation>
</author>
</analytic>
<series><title level="j" type="main">International journal of hydrogen energy</title>
<title level="j" type="abbreviated">Int. j. hydrogen energy</title>
<idno type="ISSN">0360-3199</idno>
<imprint><date when="2011">2011</date>
</imprint>
</series>
</biblStruct>
</sourceDesc>
<seriesStmt><title level="j" type="main">International journal of hydrogen energy</title>
<title level="j" type="abbreviated">Int. j. hydrogen energy</title>
<idno type="ISSN">0360-3199</idno>
</seriesStmt>
</fileDesc>
<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Aluminium</term>
<term>Catalyst</term>
<term>Catalytic conversion</term>
<term>Crystalline material</term>
<term>Crystalline structure</term>
<term>High performance</term>
<term>Hydrogen</term>
<term>Methane</term>
<term>Nickel</term>
<term>Nickel oxide</term>
<term>Scanning electron microscopy</term>
<term>Sintering</term>
<term>Sol gel process</term>
<term>Spinel</term>
<term>Stability</term>
<term>Steam reforming</term>
<term>Surface area</term>
<term>Synthesis gas</term>
<term>Transmission electron microscopy</term>
<term>X ray diffractometry</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Reformage vapeur</term>
<term>Méthane</term>
<term>Gaz synthèse</term>
<term>Spinelle</term>
<term>Catalyseur</term>
<term>Oxyde de nickel</term>
<term>Procédé sol gel</term>
<term>Diffractométrie RX</term>
<term>Microscopie électronique balayage</term>
<term>Microscopie électronique transmission</term>
<term>Aire superficielle</term>
<term>Structure cristalline</term>
<term>Nickel</term>
<term>Aluminium</term>
<term>Matériau cristallin</term>
<term>Frittage</term>
<term>Conversion catalytique</term>
<term>Haute performance</term>
<term>Stabilité</term>
<term>Hydrogène</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Nickel</term>
<term>Aluminium</term>
<term>Hydrogène</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">A series of several mixed oxides close to NiAl<sub>2</sub>
O<sub>4</sub>
 (NiAl<sub>2</sub>
O<sub>4</sub>
, 5 wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
, 10 wt% NiO/ NiAl<sub>2</sub>
O<sub>4</sub>
 and 15 wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
) were prepared by a pseudo sol gel method using propionic acid then calcinated at 900 °C during 4 h. The catalysts were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), transmission electron microscopy (TEM), surface areas (BET) and temperature-programmed reduction (TPR). The nature of the crystalline structure, the surface area and the reduction temperature depend on the Ni/ Al ratio. For the stoichiometric ratio Ni/Al exactly equal to 0.5, homogeneous crystalline spinel phase was formed after temperature of calcination was equal or higher than 725 °C. The spinel structure being a non-tolerant structure for an excess of Ni, when Ni/Al is higher than 0.5, free NiO in strong interaction with the spinel was present and favoured the reduction of the nickel of the structure at lower temperature compared to the spinel. Till 700 °C, the spinel structure was well conserved even if it was partially reduced. For a temperature higher than 700 °C, the structure leads to Ni species formation on γ-Al<sub>2</sub>
O<sub>3</sub>
. Comparative steam reforming of methane was conducted to control the formation of Ni and its sintering. The stoichiometric spinel showed relevant catalytic performances: high CH<sub>4</sub>
 conversion, high selectivities of CO and H<sub>2</sub>
 and low carbon formation. The presence of nickel inside the spinel structure of NiAl<sub>2</sub>
O<sub>4</sub>
 catalyst confers a high stability and strong dispersion for the metallic particles. The low formation of carbon was due to the high dispersion and the limited growing of the Ni particles on γ-Al<sub>2</sub>
O<sub>3</sub>
. Over 5 wt% of NiO excess, a rough decrease of the CH<sub>4</sub>
 conversion, CO and H<sub>2</sub>
 selectivities were observed. The x wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
 systems give an important carbon formation due to a large Ni particle formation after rapid sintering.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>0360-3199</s0>
</fA01>
<fA02 i1="01"><s0>IJHEDX</s0>
</fA02>
<fA03 i2="1"><s0>Int. j. hydrogen energy</s0>
</fA03>
<fA05><s2>36</s2>
</fA05>
<fA06><s2>17</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Steam reforming of methane to syngas over NiAl2O4 spinel catalysts</s1>
</fA08>
<fA11 i1="01" i2="1"><s1>SALVI (N.)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>BOULAHOUACHE (A.)</s1>
</fA11>
<fA11 i1="03" i2="1"><s1>PETIT (C.)</s1>
</fA11>
<fA11 i1="04" i2="1"><s1>KIENNEMANN (A.)</s1>
</fA11>
<fA11 i1="05" i2="1"><s1>RABIA (C.)</s1>
</fA11>
<fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB 109, El-Alia Bab Ezzouar</s1>
<s2>Alger</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>5 aut.</sZ>
</fA14>
<fA14 i1="02"><s1>Laboratoire LCPMM, département de chimie, Faculté ses sciences, U. Blida, route de soumaa, BP</s1>
<s2>Blida</s2>
<s3>DZA</s3>
<sZ>2 aut.</sZ>
</fA14>
<fA14 i1="03"><s1>Ecole de Chimie, Polymères et Matériaux - Laboratoire Matériaux, Surface, Procédés pour la Catalyse (LMSPC), UMR CNRS 7515 - 25, rue Becquerel</s1>
<s2>67087 Strasbourg</s2>
<s3>FRA</s3>
<sZ>3 aut.</sZ>
<sZ>4 aut.</sZ>
</fA14>
<fA20><s1>11433-11439</s1>
</fA20>
<fA21><s1>2011</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>17522</s2>
<s5>354000508987181080</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2011 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>30 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>11-0412765</s0>
</fA47>
<fA60><s1>P</s1>
<s2>C</s2>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="1"><s0>International journal of hydrogen energy</s0>
</fA64>
<fA66 i1="01"><s0>GBR</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>A series of several mixed oxides close to NiAl<sub>2</sub>
O<sub>4</sub>
 (NiAl<sub>2</sub>
O<sub>4</sub>
, 5 wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
, 10 wt% NiO/ NiAl<sub>2</sub>
O<sub>4</sub>
 and 15 wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
) were prepared by a pseudo sol gel method using propionic acid then calcinated at 900 °C during 4 h. The catalysts were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), transmission electron microscopy (TEM), surface areas (BET) and temperature-programmed reduction (TPR). The nature of the crystalline structure, the surface area and the reduction temperature depend on the Ni/ Al ratio. For the stoichiometric ratio Ni/Al exactly equal to 0.5, homogeneous crystalline spinel phase was formed after temperature of calcination was equal or higher than 725 °C. The spinel structure being a non-tolerant structure for an excess of Ni, when Ni/Al is higher than 0.5, free NiO in strong interaction with the spinel was present and favoured the reduction of the nickel of the structure at lower temperature compared to the spinel. Till 700 °C, the spinel structure was well conserved even if it was partially reduced. For a temperature higher than 700 °C, the structure leads to Ni species formation on γ-Al<sub>2</sub>
O<sub>3</sub>
. Comparative steam reforming of methane was conducted to control the formation of Ni and its sintering. The stoichiometric spinel showed relevant catalytic performances: high CH<sub>4</sub>
 conversion, high selectivities of CO and H<sub>2</sub>
 and low carbon formation. The presence of nickel inside the spinel structure of NiAl<sub>2</sub>
O<sub>4</sub>
 catalyst confers a high stability and strong dispersion for the metallic particles. The low formation of carbon was due to the high dispersion and the limited growing of the Ni particles on γ-Al<sub>2</sub>
O<sub>3</sub>
. Over 5 wt% of NiO excess, a rough decrease of the CH<sub>4</sub>
 conversion, CO and H<sub>2</sub>
 selectivities were observed. The x wt% NiO/NiAl<sub>2</sub>
O<sub>4</sub>
 systems give an important carbon formation due to a large Ni particle formation after rapid sintering.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001D06B06B</s0>
</fC02>
<fC02 i1="02" i2="X"><s0>230</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Reformage vapeur</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Steam reforming</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Reformación vapor</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Méthane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Methane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Metano</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Gaz synthèse</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Synthesis gas</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Gas síntesis</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Spinelle</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Spinel</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Espinela</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Catalyseur</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Catalyst</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Catalizador</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Oxyde de nickel</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Nickel oxide</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Níquel óxido</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Procédé sol gel</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Sol gel process</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Procedimiento sol gel</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Diffractométrie RX</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>X ray diffractometry</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Difractometría RX</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Microscopie électronique balayage</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Scanning electron microscopy</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Microscopía electrónica barrido</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Microscopie électronique transmission</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Transmission electron microscopy</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Microscopía electrónica transmisión</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Aire superficielle</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Surface area</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Area superficial</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Structure cristalline</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Crystalline structure</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Estructura cristalina</s0>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Niquel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Aluminium</s0>
<s2>NC</s2>
<s2>FR</s2>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Aluminium</s0>
<s2>NC</s2>
<s2>FR</s2>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Aluminio</s0>
<s2>NC</s2>
<s2>FR</s2>
<s2>FX</s2>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Matériau cristallin</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Crystalline material</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Material cristalino</s0>
<s5>15</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Frittage</s0>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Sintering</s0>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Sinterización</s0>
<s5>16</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Conversion catalytique</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Catalytic conversion</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Conversión catalítica</s0>
<s5>17</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Haute performance</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>High performance</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Alto rendimiento</s0>
<s5>18</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Stabilité</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Stability</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Estabilidad</s0>
<s5>19</s5>
</fC03>
<fC03 i1="20" i2="X" l="FRE"><s0>Hydrogène</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fC03 i1="20" i2="X" l="ENG"><s0>Hydrogen</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fC03 i1="20" i2="X" l="SPA"><s0>Hidrógeno</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fN21><s1>283</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
</fN44>
<fN82><s1>OTO</s1>
</fN82>
</pA>
<pR><fA30 i1="01" i2="1" l="ENG"><s1>International Conference on Hydrogen Production (ICH2P-2010)</s1>
<s2>2</s2>
<s3>Istanbul TUR</s3>
<s4>2010-06-16</s4>
</fA30>
</pR>
</standard>
</inist>
<affiliations><list><country><li>Algérie</li>
<li>France</li>
</country>
<region><li>Alsace (région administrative)</li>
<li>Grand Est</li>
<li>Wilaya d'Alger</li>
</region>
<settlement><li>Alger</li>
<li>Strasbourg</li>
</settlement>
</list>
<tree><country name="Algérie"><region name="Wilaya d'Alger"><name sortKey="Salvi, N" sort="Salvi, N" uniqKey="Salvi N" first="N." last="Salvi">N. Salvi</name>
</region>
<name sortKey="Boulahouache, A" sort="Boulahouache, A" uniqKey="Boulahouache A" first="A." last="Boulahouache">A. Boulahouache</name>
<name sortKey="Rabia, C" sort="Rabia, C" uniqKey="Rabia C" first="C." last="Rabia">C. Rabia</name>
</country>
<country name="France"><region name="Grand Est"><name sortKey="Petit, C" sort="Petit, C" uniqKey="Petit C" first="C." last="Petit">C. Petit</name>
</region>
<name sortKey="Kiennemann, A" sort="Kiennemann, A" uniqKey="Kiennemann A" first="A." last="Kiennemann">A. Kiennemann</name>
</country>
</tree>
</affiliations>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=$WICRI_ROOT/Wicri/Terre/explor/NickelMaghrebV1/Data/PascalFrancis/Checkpoint

HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 000115 | SxmlIndent | more

HfdSelect -h $EXPLOR_AREA/Data/PascalFrancis/Checkpoint/biblio.hfd -nk 000115 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=    Wicri/Terre
   |area=    NickelMaghrebV1
   |flux=    PascalFrancis
   |étape=   Checkpoint
   |type=    RBID
   |clé=     Pascal:11-0412765
   |texte=   Steam reforming of methane to syngas over NiAl2O4 spinel catalysts
}}

This area was generated with Dilib version V0.6.27.
Data generation: Fri Mar 24 23:14:20 2017. Site generation: Tue Mar 5 17:03:47 2024

	Serveur d'exploration sur le nickel au Maghreb
	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 nickel au Maghreb

Steam reforming of methane to syngas over NiAl2O4 spinel catalysts

Steam reforming of methane to syngas over NiAl2O4 spinel 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