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Dynamic And Steady-state Analysis Of Oxidative Dehydrogenation Of EthaneKaramullaoglu, Gulsun 01 July 2005 (has links) (PDF)
In this research, oxidative dehydrogenation of ethane to ethylene was studied over Cr-O and Cr-V-O mixed oxide catalysts through steady-state and dynamic experiments. The catalysts were prepared by the complexation method. By XRD, presence of Cr2O3 phase in Cr-O / and the small Cr2O3 and V2O4 phases of Cr-V-O were revealed. In H2-TPR, both catalysts showed reduction behaviour. From XPS the likely presence of Cr+6 on fresh Cr-O was found. On Cr-V-O, the possible reduction of V+5 and Cr+6 forms of the fresh
sample to V+4, V+3 and Cr+3 states by TPR was discovered through XPS. With an O2/C2H6 feed ratio of 0.17, Cr-O exhibited the highest total conversion value of about 0.20 at 447° / C with an ethylene selectivity of 0.82. Maximum ethylene selectivity with Cr-O was obtained as 0.91 at 250° / C. An ethylene selectivity of 0.93 was reached with the Cr-V-O at 400° / C. In the experiments performed by using CO2 as the mild oxidant, a yield value of 0.15 was achieved at 449° / C on Cr-O catalyst. In dynamic experiments performed over Cr-O, with C2H6 pulses injected into O2-He flow, the possible occurrence of two reaction sites for the formation of CO2 and H2O was detected. By Gaussian fits to H2O curves, the presence of at least three production ways was thought to be probable.
Different from Cr-O, no CO2 formation was observed on Cr-V-O during pulsing C2H6 to O2-He flow. In the runs performed by O2 pulses into C2H6-He flow over Cr-V-O, formation of CO rather than C2H4 was favored.
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Destruction catalytique à basses températures des composés organiques volatils (COV) / Total abatement of volatile organic compounds (VOC) by catalytic oxidation at low temperatureOusmane, Mohamad 03 March 2010 (has links)
L’objectif de notre travail, était l’étude de deux classes de catalyseurs dans la réaction d’oxydation totale de COV. L’application visée étant la destruction à basse température de ces traces de polluants dans l’air. Des oxydes mixtes Co3O4-CeO2 ont été préparés par co-précipitation. Avec l’oxyde mixte (% atomique Co/Ce = 1), nous avons obtenu les meilleures performances catalytiques et montré que la réactivité étaient exaltée par une forte mobilité des oxygènes de coeur. Des catalyseurs à base d’or (2wt%) et de palladium (1wt%) ont été déposés sur des supports oxydes comme la cérine et le titane afin de favoriser une interaction métal support, ou sur un support alumine. Des solides à base d’alumine dopée au cérium, manganèse, fer et titane ont également été préparés. Pour l’or, l’évolution des performances catalytiques en fonction du support ont été les suivantes: Au2%/Al2O3 < Au2%/TiO2 < Au2%/CeO2, alors que pour le palladium nous avons obtenu les tendances suivantes : Pd1%/CeO2 < Pd1%/Al2O3 < Pd1%/TiO2. Pour l’Au, l’interaction métal support a permis d’expliquer les différences de réactivité alors que pour le palladium, l’activité est liée aux sites actifs de palladium Pd0/PdO présents à la surface. Avec les systèmes dopés, les résultats ont montré que les meilleurs catalyseurs étaient le Au2%/Ce5%/Al2O3 et le Pd1%/Ce5%/Al2O3. Cette exaltation a été attribuée à la grande mobilité des oxygènes en raison d’un défaut de structure induit par l’insertion des ions Al3+ au sein du réseau de la cérine et une forte interaction des particules très bien dispersées / The aim of the work was to study two classes of catalysts for the complete oxidation of volatile organic compounds. The target application for air pollution control is the total abatement of VOC at low temperature. Mixed oxide Co3O4-CeO2, were prepared by co-precipitation method. Among them, the mixed oxide corresponding to Co/Ce atomic ratio close to 1, was the best performing. The participation of surface oxygen species and high bulk mobile oxygen were the factors determining the high activity of Co30Ce in the total oxidation of propylene and toluene. Au (2wt%) and Pd (1wt%) catalysts were prepared over typical reducible oxides, such as CeO2 and TiO2. For comparison, catalysts over Al2O3, were also prepared. Moreover, the effect on the activity of Au and Pd supported over Al2O3 doped by cerium, manganese, iron and titanium was investigated. The so prepared Au and Pd catalysts were compared in the total oxidation of propylene. It was found that the activity of gold catalysts supported over un-doped oxides varied in the order: Au2%/Al2O3 < Au2%/TiO2 < Au2%/CeO2, while a different trend was observed for palladium catalysts: Pd1%/CeO2 < Pd1%/Al2O3 < Pd1%/TiO2. For Au catalysts, the nature of the support and the extent of interaction with the support are the key factors in determining the activity, whilst for the Pd supported ones, the activity seems to be governed by the nature of Pd species, Pd0/PdO, present in the catalyst. Au2%/Ce5%/Al2O3 and Pd1%/Ce5%/Al2O3 appear the best samples. The enhanced catalytic performances were attributed to high-oxygen mobility due to a defective ceria structure induced by the insertion of Al3+ ions into the lattice and also strong metal-support interaction between nanoparticles highly dispersed
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