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Dissertations / Theses on the topic 'Platinum supported alumina catalysts'

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Published: 3 June 2025

Last updated: 31 July 2025

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1

Dawson, Richard James. "Electrochemical recovery of platinum and palladium from alumina supported catalysts." Thesis, Imperial College London, 2006. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.440527.

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The process dissolves Pt and Pd selectively from catalysts in a leach reactor, using an oxidant (I3-) and complement (I-), the reduced form of the oxidant. The precious metals are then electrodeposited on the cathode of an electrochemical reactor, incorporating a cation-permeable membrane, to enable the oxidant to be regenerated simultaneously at the anode without its subsequent reduction at the cathode. The iodide system was identified as being able to dissolve Pt and Pd, using tri-iodide as oxidant, at neutral pH to minimise alumina dissolution rates. The reaction kinetics were determined us

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2

Bansode, Vijaya Anil. "Partial oxidation of propane on ceria-and alumina-supported platinum catalysts." Morgantown, W. Va. : [West Virginia University Libraries], 2006. https://eidr.wvu.edu/etd/documentdata.eTD?documentid=4462.

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Thesis (M.S.)--West Virginia University, 2006.<br>Title from document title page. Document formatted into pages; contains xi, 80 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 68-71).

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3

Fialho, Batista Ana Teresa. "Atomic scale insight into platinum based catalysts supported on chlorinated gamma-alumina." Thesis, Lyon, 2019. http://www.theses.fr/2019LYSEN062.

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Plusieurs procédés industriels utilisent des catalyseurs hétérogènes bifonctionnels avec des sites actif métalliques et acides. L’influence de la distance entre les deux types de site actif sur l’activité et la sélectivité du catalyseur a souvent été décrite par un « critère d’intimité » dans la littérature. Les travaux reportés dans la présente thèse revisitent ce critère en étudiant des catalyseurs constitués de nanoparticules de platine supportées sur alumine gamma chlorée, utilisés en reformage catalytique des coupes pétrolières de type naphtas. Plusieurs techniques, dont la microscopie HR

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4

Soames, Mark. "Sol-gel routes to platinum, platinum-tin and platinum-potassium reforming catalysts." Thesis, Brunel University, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.311280.

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5

Gopalan, Usha. "Hydrodenitrogenation of pyridine over alumina supported platinum catalyst." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0001/MQ32537.pdf.

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6

Telford, David Alexander. "Temperature programmed studies of alumina-supported platinum catalysts : experimental and numerical modelling studies." Thesis, University of Cambridge, 2002. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.620259.

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7

Riley, C. C. A. "Effect of pretreatment of the state and reactivity of alumina-supported platinum-iridium catalysts." Thesis, Imperial College London, 1987. http://hdl.handle.net/10044/1/46303.

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8

Bahloul, Djamila. "Influence des conditions d'activation sur les proprietes catalytiques du platine depose sur alumine." Poitiers, 1987. http://www.theses.fr/1987POIT2258.

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9

Martinez, Hugo. "Influence des proprietes acido-basiques du couple support-reactif lors du cokage des catalyseurs metalliques supportes." Poitiers, 1988. http://www.theses.fr/1988POIT2320.

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Comparaison des depots de colce obtenus a partir de l'anthracene et du phenanthrene sur des catalyseurs d'acidites variables. Augmentation de la quantite de colce en presence du platine. L'effet de l'addition de chlore a l'alumine depend de la temperature

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10

Bircumshaw, Lucy Deborah. "Î±-alumina supported catalysts for pollution control." Thesis, University College London (University of London), 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.395526.

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11

Aslam, Toseef. "Reforming of hydrocarbons on supported platinum and platinum-tin catalysts." Thesis, University of Reading, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.405472.

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12

Romeo, Michelangelo. "Proprietes des catalyseurs intermetalliques platine-uranium, platine sur oxyde d'uranium et platine-cobalt-oxyde d'uranium sur alumine pour les reactions de rearrangement de squelette des hydrocarbures." Université Louis Pasteur (Strasbourg) (1971-2008), 1987. http://www.theses.fr/1987STR13098.

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13

Lear, Tim. "Structure/activity correlations in alumina supported palladium catalysts." Thesis, University of Glasgow, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.275617.

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14

Sivalingam, Juvarajan. "Hydrogenolysis and reforming properties of platinum and platinum-tin supported catalysts." Thesis, Brunel University, 1992. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.303969.

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15

Thomson, Steven J. "Hydrosilylation of alkenes using polymer-supported platinum catalysts." Thesis, University of Strathclyde, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.400285.

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16

Cairns, Graham R. "Hydrogenation catalysts from supported palladium complexes." Thesis, University of Glasgow, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.360177.

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17

Messou, Davina Gnamien-Bla. "Valorisation de polyols en phase aqueuse sur catalyseurs bimétalliques supportés pour la production d'hydrocarbures." Thesis, Poitiers, 2016. http://www.theses.fr/2016POIT2316/document.

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La biomasse végétale (source de carbone renouvelable) peut être utilisée pour fabriquer des carburants liquides et produits de base pour la chimie. Ainsi depuis environ une dizaine d'années, se développe le procédé APHDO (Aqueous Phase HydroDeOxygenation) de transformation directe en phase aqueuse de polyols d'origine lignocellulosique (comme le sorbitol) en alcanes valorisables (C5-C6). Ce procédé repose sur une catalyse hétérogène bifonctionnelle métal/acide et fait intervenir des ruptures compétitives de liaisons C-C et C-O. L'objectif de la thèse est de mettre au point des systèmes bimétal

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18

Evans, Julia Margaret. "Active sites for hydrocarbon reforming over supported platinum catalysts." Thesis, University of Reading, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.262643.

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19

Wells, Peter Philip. "Controlled surface modification of supported platinum group metal catalysts." Thesis, University of Southampton, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.438652.

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20

Royker, Mariam. "Platinum promotion in supported gold catalysts for glycerol oxidation." Master's thesis, University of Cape Town, 2012. http://hdl.handle.net/11427/11987.

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Includes synopsis.<br>Includes bibliographical references.<br>There has been recently a drive toward cleaner fuels, with biodiesel proving to be a viable option. It is obtained by the transesterification of triglycerides, with glycerol as the main coproduct. Approximately 100kg of glycerol is formed per ton of biodiesel produced.

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21

Wright, M. A. P. "'1H NMR studies of hydrogen chemisorption on supported platinum and supported copper catalysts." Thesis, University of Nottingham, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.336858.

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22

McMillan, Scott Tomlinson. "The gas-phase hydrogenation of butyronitrile over supported platinum catalysts." Diss., Georgia Institute of Technology, 1985. http://hdl.handle.net/1853/11912.

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23

Havil, Patrick. "Influence du vieillissement thermique sur les proprietes physico-chimiques et la reactivite des catalyseurs mono et bimetalliques a base de platine et/ou rhodium sur alumine ou sur cerine." Paris 6, 1988. http://www.theses.fr/1988PA066291.

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Une etude systematique de la stabilite des catalyseurs de post-combustion mono et bimetalliques, platine-rhodium, supportes sur alumine et cerine a ete realisee pour un vieillissement thermique a des temperatures variant de 600 a 1100**(o)c. Les catalyseurs ont ete ensuite testes avec un melange de gaz synthetique simulant les conditions reelles. Le vieillissement a lieu principalement en milieu oxydant. Il est du soit au frittage de la phase metallique par grossissement des particules de 1 a 30 nm soit a l'encapsulation ou a la migration des ions platine et rhodium dans le support

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24

Hicks, Tanya Temaca. "Preparation, Characterization, and Activity of Mono-Dispersed Supported Catalysts." Thesis, Georgia Institute of Technology, 2004. http://hdl.handle.net/1853/4765.

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Mono-dispersed supported Ni catalysts were synthesized using the water-CTAB-hexanol reverse micellar system. The core of the reverse micelles contained an aqueous solution of NiCl2. Dynamic light scattering measurements showed that microemulsions having a water-to-surfactant molar ratio, Wo, of 10 lead to reverse micelles with lowest polydispersity, longest stability, and size range of interest. At an oil-to-aqueous phase ratio of 2, the diameter of the reverse micelles was found to increase with Wo in a linear fashion. At higher values of Wo (i.e. 25-30), the polydispersity was found to i

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25

Ozturk, Zafer. "Carbon Supported Platinum-palladium Catalysts For Methanol And Ethanol Oxidation Reactions." Master's thesis, METU, 2011. http://etd.lib.metu.edu.tr/upload/12613008/index.pdf.

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In this work, two groups of carbon supported Pt-Pd catalysts have been prepared in order to investigate the effect of Pd, as a second metal, and surfactants on the catalytic activity towards methanol and ethanol oxidation reactions used in the direct methanol and ethanol fuel cells. In the first group (group a), 1- hexanethiol was used as a stabilizing agent while in the second group (group b), 1,1 dimethyl hexanethiol was utilized. Cyclic voltammetry (CV), chronoamperometry (CA), X-ray diffraction (XRD), transmission electron microscopy (TEM), energy dispersive X-ray spectroscopy (EDS) and X-

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26

Dias, F. E. "Studies in synthesis-structure-function relationships in oxide-supported platinum catalysts." Thesis, University of Cambridge, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.598526.

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This work has involved the synthesis, and the physical and chemical characterisation, and reactor studies of oxide-supported platinum catalysts. Eight nominally identical catalysts with different preparation histories and hence different structure are the main subjects of these studies. Platinum-silica catalysts have been prepared using different types of silica, and the silicas have been exposed to different pre-treatments. Furthermore, different solvents and different platinum containing compounds have been used to deposit the metal on the silica. The aims of this work have been twofold. One

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27

Theodoulou, Louise. "Supported platinum and iridium catalysts for the selective hydrogenation of cinnamaldehyde." Thesis, University of Reading, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.343323.

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28

Nikulshina, Kulikova Maria. "(Ni)MoWS alumina supported hydrotreating catalysts prepared from mixed H4SiMonW12-nO40 heteropolyacids." Thesis, Lille 1, 2018. http://www.theses.fr/2018LIL1R015/document.

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Le développement de catalyseurs HDS plus efficaces est un enjeu majeur pour répondre aux exigences environnementales concernant la teneur en soufre dans les carburants. L'une des approches pour améliorer l'activité catalytique est le développement de catalyseurs ternaires NiMoW. Cette étude se concentre sur la synthèse et la caractérisation de catalyseurs (Ni)MoW préparés à partir hétéropolyacides (HPA) mixtes SiMo1W11 et SiMo3W9 de structure de Keggin. Les catalyseurs basés sur les HPAs monométalliques SiMo12 et SiW12 et leurs mélanges ont été préparés et étudiés. Les solides ont été caractér

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29

Nikulshina, Kulikova Maria. "(Ni)MoWS alumina supported hydrotreating catalysts prepared from mixed H4SiMonW12-nO40 heteropolyacids." Electronic Thesis or Diss., Université de Lille (2018-2021), 2018. http://www.theses.fr/2018LILUR015.

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Le développement de catalyseurs HDS plus efficaces est un enjeu majeur pour répondre aux exigences environnementales concernant la teneur en soufre dans les carburants. L'une des approches pour améliorer l'activité catalytique est le développement de catalyseurs ternaires NiMoW. Cette étude se concentre sur la synthèse et la caractérisation de catalyseurs (Ni)MoW préparés à partir hétéropolyacides (HPA) mixtes SiMo1W11 et SiMo3W9 de structure de Keggin. Les catalyseurs basés sur les HPAs monométalliques SiMo12 et SiW12 et leurs mélanges ont été préparés et étudiés. Les solides ont été caractér

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30

Swaminathan, Sneha. "Metal Oxide Nanofibers as Filters, Catalyst and Catalyst Support Structures." University of Akron / OhioLINK, 2010. http://rave.ohiolink.edu/etdc/view?acc_num=akron1279564885.

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31

Kushch, S. D., N. S. Kuyunko, A. A. Arbuzov, N. N. Dremova, and V. E. Muradyan. "Pt supported on reduced graphite oxide catalysts for H2 activation." Thesis, Sumy State University, 2013. http://essuir.sumdu.edu.ua/handle/123456789/35570.

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Platinum catalysts of H2 activation with average size ≤2.0 nm were prepared in a base of reduction conversion of graphene oxide. A low few-layered carbon nanomaterial was prepared by thermoexpansion and annealing of graphene oxide. The uniformly dispersed Pt nanoparticles were supported on two-dimension graphene flat material by the use of pyridine or polyethyleneimine in alkaline (pH10) media as chelating agent modificating both metal precursor H2PtCl6 and support. Vacancies in carbon material formed as a result of thermoexpansion and annealing of graphite oxide probablly serve as anchor gro

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32

丁小華 and Siu-wa Ting. "Catalytic hydrogen generation from formic acid on supported platinum-ruthenium-bismuth oxide." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2011. http://hdl.handle.net/10722/193061.

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33

McNamara, John Martin. "An evaluation of alumina suppoted platinum catalysts for the oxidative dehydrogenation of n butane." Thesis, University of Glasgow, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.289903.

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34

Regali, Francesco. "Hydroconversion of model Fischer‑Tropsch wax over noble metal/silica-alumina catalysts." Doctoral thesis, KTH, Kemisk teknologi, 2013. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-129968.

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Synthetic fuels produced using the Fischer-Tropsch technology will play an important role in the future of the transportation sector. The Fischer-Tropsch synthesis (FTS) allows converting synthesis gas (CO + H2) into fuels of outstanding quality. The synthesis gas can be obtained from different carbon sources: natural gas, coal and biomass. In order to maximize the yield of middle distillates, the process is carried out in two main steps: the FT-synthesis that produces long-chain hydrocarbons (waxes) and a hydrocracking step, to selectively convert the waxes into fuels. Diesel produced by this

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35

Ngo, Lien Thuy. "Sintering and reactivity of model oxide-supported catalysts : Pt/ZnO(000-1)-O and Pd/[alpha]-Al₂O₃(0001) /." Thesis, Connect to this title online; UW restricted, 2004. http://hdl.handle.net/1773/8543.

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36

Emery, Duncan Alexander. "Study of the mechanism of electrochemical promotion of platinum catalysts supported on Yttria : stabilised zirconia." Thesis, Imperial College London, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.263583.

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37

Kamiuchi, Naoto. "Studies on Nano-structures and Catalytic Activities of Oxide-supported Precious Metal Catalysts." 京都大学 (Kyoto University), 2010. http://hdl.handle.net/2433/120878.

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38

Keyvanloo, Kamyar. "Preparation of Active, Stable Supported Iron Catalysts and Deactivation by Carbon of Cobalt Catalysts for Fischer-Tropsch Synthesis." BYU ScholarsArchive, 2014. https://scholarsarchive.byu.edu/etd/5705.

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The first half of this dissertation reports the development of supported Fe FT catalysts including the effects of various, carefully chosen preparation methods on the performance of alumina-supported iron/copper/potassium (FeCuK/Al2O3); it was determined that non-aqueous slurry impregnation and co-impregnation yielded catalysts with activities as high as any reported in the literature. Furthermore, the effects of support properties including pore size, hydroxyl group concentration, and support stabilizer were investigated for FeCuK/Al2O3 catalysts containing 20 or 40% Fe. For the first time, w

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39

Ammor, Hassan. "Irradiation microonde des catalyseurs supportes PT, AL : :(2)O::(3) et étude des réactions catalytiques." Nancy 1, 1988. http://www.theses.fr/1988NAN10064.

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Hydrogenolyse du méthylcyclopentane, dans les réactions d'isomérisation des hydrocarbures en C::(6), on en constate que le taux de conversion est toujours plus élevé pour les expériences en microonde que pour les expériences faites en classique. Les distributions en isomères sont identiques dans les deux modes de chauffage, mais on constate la présence de benzène en grande quantité, parmi les produits en réaction

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40

Celik, Caglar. "Carbon Supported And Surfactant Stabilized Metal Nanoparticle Catalysts For Direct Methanol Fuel Cells." Master's thesis, METU, 2005. http://etd.lib.metu.edu.tr/upload/12606368/index.pdf.

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ABSTRACT CARBON SUPPORTED AND SURFACTANT STABILIZED METAL NANOPARTICLE CATALYSTS FOR DIRECT METHANOL FUEL CELLS &Ccedil<br>elik, &Ccedil<br>aglar M.S., Department of Chemistry Supervisor: Assoc. Prof. Dr. G&uuml<br>ls&uuml<br>n G&ouml<br>kaga&ccedil<br>August 2005, 72 pages Carbon supported surfactant, such as 1-decanethiol and octadecanethiol, stabilized platinum and platinum/ruthenium species have been prepared recently. In this thesis, for the first time, 1-hexanethiol has been used as an organic stabilizer for the preparation of carbon supported platinum and platinum/ruthenium na

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41

Santillan-Jimenez, Eduardo. "CARBON NANOTUBE SUPPORTED METAL CATALYSTS FOR NO_x REDUCTION USING HYDROCARBON REDUCTANTS." UKnowledge, 2008. http://uknowledge.uky.edu/gradschool_diss/672.

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Nitrogen oxides (NOx) are atmospheric pollutants that pose a serious threat to both the environment and human health. Although catalytic deNOx technologies for engines working under stoichiometric air-to-fuel ratios (i.e., most gasoline engines) are already available, their performance is unsatisfactory under excess air conditions like those under which diesel engines operate. The selective catalytic reduction of NOx with hydrocarbon reductants (HC-SCR) is a potential deNOxsolution for diesel engines, whose operating temperatures are 150-500 ºC. Given that is unlikely for a single catalyst to

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42

Norris, Elizabeth L. "Steam reforming of methane over alumina supported nickel catalysts : influence of calcination temperature, gold doping and sulfur addition." Thesis, Keele University, 2013. http://eprints.keele.ac.uk/3817/.

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Alumina supported nickel and gold-doped nickel catalysts have been investigated for their use as hydrocarbon steam reforming catalysts. The influence of calcination temperature during preparation has been investigated using a variety of techniques including X-ray powder diffraction (XRD), X-ray photoelectron spectroscopy (XPS), BET surface area analysis, scanning electron microscopy (SEM) and temperature-programmed reduction (TPR). It has been shown that the nickel phases present and their subsequent reducibility are strongly dependent upon the calcination temperature during preparation. As th

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43

Zhao, Wei. "Dehydrogenation mechanisms of methyl-cyclohexane on γ-alumina supported platinum subnanometric-clusters : DFT coupled with experimental kinetics and kinetic modelling". Thesis, Lyon, 2017. http://www.theses.fr/2017LYSEN052/document.

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Le reformage catalytique vise à transformer les naphtas en aromatiques à haut indice d'octane et à produire simultanément du dihydrogène. Le catalyseur utilisé est composé d’agrégats sub-nanométriques à base de platine hautement dispersées sur un support d’alumine-gamma dont le comportement en réaction pose de nombreuses questions. Nous étudions expérimentalement et théoriquement une réaction modèle qui sonde les sites métalliques, la déshydrogénation du methyl-cyclohexane en toluène. Une compréhension détaillée à l'échelle atomique des mécanismes impliqués et des paramètres cinétiques est néc

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44

Sen, Selda. "Activity Of Carbon Supported Platinum Nanoparticles Catalysts Toward Methanol Oxidation Reaction: Role Of Metal Precursor And A New Surfactant." Master's thesis, METU, 2008. http://etd.lib.metu.edu.tr/upload/3/12609273/index.pdf.

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In this thesis, carbon supported platinum nanoparticle catalysts were prepared using PtCl4 and H2PtCl6 as starting materials and 1-heptanethiol, tert-nonyl mercaptan, 1-hexadecanethiol, 1-octadecanethiol as surfactants. These new catalysts were employed for methanol oxidation reaction which are used for direct methanol fuel cells. Tert-nonyl mercaptane was used for the first time in this type of reaction and the other surfactants were used for comparison of the catalysts performance. Cyclic voltammetry (CV), X-ray photoelectron spectroscopy (XPS), X-ray diffraction (XRD) and transmission elec

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45

Hoyle, N. D. "The characterisation of the adsorptive and catalytic properties of supported platinum metal catalysts by methods including differential scanning calorimetry." Thesis, Brunel University, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.370135.

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46

Sen, Fatih. "The Preparation And Analysis Of New Carbon Supported Pt And Pt+second Metal Nanoparticles Catalysts For Direct Methanol Fuel Cells." Phd thesis, METU, 2012. http://etd.lib.metu.edu.tr/upload/12614728/index.pdf.

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In this thesis, firstly, carbon-supported platinum nanoparticle catalysts have been prepared by using PtCl4 and H2PtCl6 as starting materials and 1-hexanethiol, and tert-octanethiol, as surfactants for the first time. Secondly, these prepared catalysts were heated to 200 &deg<br>C, 300 &deg<br>C, and 400 &deg<br>C for 4 h under argon gas. Lastly, PtRu/C catalysts, which have different atomic percent ratios of Pt and Ru (Pt/Ru: 0.8, 2.1 and 3.5), were prepared using PtCl4 and RuCl3 as starting materials and tert-octanethiol as a surfactant. Each was characterized by X-ray diffraction, transmis

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47

Thinon, Olivier. "CO conversion over dual-site catalysts by the Water-Gas Shift Reaction for fuel cell applications : comparative mechanistic and kinetic study of gold and platinum supported catalysts." Thesis, Lyon 1, 2009. http://www.theses.fr/2009LYO10187.

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Les piles à combustible, alimentée par de l’hydrogène, représentent une solution prometteuse pour limiter la pollution. L’une des alternatives économiques envisagées à court et moyen terme est de produire l’hydrogène à partir d’un carburant tel que le méthane ou le bio-éthanol. Cette transformation a pour objectif d’obtenir un mélange de gaz riche en hydrogène avec une très faible teneur en CO, ce dernier étant un poison pour les piles de type PEM. La réaction de Water-Gas Shift (WGS) est une étape clé du procédé ; elle convertit CO en CO2 par réaction avec l’eau et fournit une quantité d’hydr

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48

Heponiemi, A. (Anne). "Catalytic wet air oxidation of industrial wastewaters:oxidation of bisphenol A over cerium supported metal catalysts." Doctoral thesis, Oulun yliopisto, 2015. http://urn.fi/urn:isbn:9789526208992.

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Abstract The large amounts of industrial wastewaters, contaminated by hazardous and toxic compounds together with ever tightening legislation, have challenged traditional wastewater treatment methods. Therefore, the development of discharge limits under, cost-effective and ecological wastewater treatment has become an essential concern. Catalytic water phase technologies are interesting alternatives for traditional wastewater treatment. Among them catalytic wet air oxidation (CWAO) has been used successfully in the management of various industrial effluents. However, the development of an acti

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49

Ertan, Salih. "Preparation And Characterization Of Carbon Supported Platinum Nanocatalysts With Different Surfactants For C1 To C3 Alcohol Oxidations." Master's thesis, METU, 2011. http://etd.lib.metu.edu.tr/upload/12613623/index.pdf.

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In this thesis, carbon supported platinum nanoparticles have been prepared by using PtCl4 as a starting material and 1-octanethiol, 1-decanethiol, 1-dodecanethiol and 1-hexadecanethiol as surfactants for methanol, ethanol and 2-propanol oxidation reactions. The structure, particle sizes and surface morphologies of the platinum were characterized by X-ray diffraction (XRD), atomic force microscopy (AFM) and transmission electron microscopy (TEM). XRD and TEM results indicate that all prepared catalysts have a face centered cubic structure and are homogeneously dispersed on the carbon support wi

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50

Dumeignil, Franck Payen Edmond Grimblot Jean. "Catalyse et environnement." Villeneuve d'Ascq : Université des sciences et technologies de Lille, 2007. https://iris.univ-lille1.fr/dspace/handle/1908/177.

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Reproduction de : Habilitation à diriger des recherches : Sciences physiques : Lille 1 : 2005.<br>Synthèse des travaux en français et curriculum vitae. Recueil de publications en anglais non reproduit dans la version électronique. N° d'ordre (Lille 1) : 501. Titre provenant de la page de titre du document numérisé. Bibliogr. 5 p. Liste des publications et des communications.

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