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Zeolites supported

Zeolite-supported Co catalyst was synthesized by solid-state ion exchange using the procedure described by Kucherov and Slinkin[16, 17], CoO... [Pg.15]

These N,N-chelating hgands were then covalently grafted on a modified Y-zeolite containing supermicropores . The selectivities observed were low (up to 11% ee) but led to similar values when comparing the imsupported and zeolite-supported Cu complexes. Interestingly, however, the zeolite catalysts could be recovered and reused several times with no loss of activity. [Pg.111]

Table 11 Effect of bis(oxazoline) on the aziridination of styrene with zeolite-supported ... Table 11 Effect of bis(oxazoline) on the aziridination of styrene with zeolite-supported ...
Examples of fluids confined In pores and spaces of molecular or nanometer dimensions abound In technological and natural products and processes. These Include wetting and lubrication, zeolite supported catalysis, silica gel based chromatrographlc separations, drying of paper... [Pg.257]

Crosswise SEM-EDX analyses show that the global Si/Al ratio (zeolite + support) varies in a very different way (Figure 5) according to the presence or absence of the y-Al203 toplayer in the support. [Pg.131]

Figure 7. N2 permeances at 30 C in the a-Al203 suppon alone (I, ), in the a-Al203 support plus the y-Al203 toplayer (2, ) and in the zeolite-support composite (3, A). Figure 7. N2 permeances at 30 C in the a-Al203 suppon alone (I, ), in the a-Al203 support plus the y-Al203 toplayer (2, ) and in the zeolite-support composite (3, A).
Oxide- and Zeolite-supported "Molecular" Metal Clusters Synthesis, Structure, Bonding, and Catalytic Properties... [Pg.211]

Abstract This review is a summary of supported metal clusters with nearly molecular properties. These clusters are formed hy adsorption or sirnface-mediated synthesis of metal carbonyl clusters, some of which may he decarhonylated with the metal frame essentially intact. The decarhonylated clusters are bonded to oxide or zeolite supports by metal-oxygen bonds, typically with distances of 2.1-2.2 A they are typically not free of ligands other than the support, and on oxide surfaces they are preferentially bonded at defect sites. The catalytic activities of supported metal clusters incorporating only a few atoms are distinct from those of larger particles that may approximate bulk metals. [Pg.211]

Oxide- and Zeolite-Supported Molecular Metal Clusters... [Pg.213]

Gates BC (2005) Oxide- and Zeolite-supported Molecular Metal Clusters Synthesis, Structure, Bonding, and Catalytic Properties. 16 211-231 Gibson SE (nee Thomas), Keen SP (1998) Cross-Metathesis. 1 155-181 Gisdakis P, see Rosch N (1999) 4 109-163 Gdrling A, see Rosch N (1999) 4 109-163... [Pg.283]

Fierro-Gonzalez, J.C., Kuba, S., Hao, Y. et al. (2006) Oxide- and zeolite-supported molecular metal complexes and clusters physical characterization and determination of structure, bonding, and metal oxidation state, J. Phys. Chem. B, 110, 13326. [Pg.138]

A N—N bond pre-exists in RNOx compound, which then decomposes, leading to N2. Over zeolite-supported Ag and Cu catalysts, the formation of nitrosonium and A-nitroso-A-alkylhydroxylamate intermediates have been assumed by Martens et al. [6], Brosius and Martens [8] and Kharas [7], respectively, to explain the N—N bonding before the release of molecular N2. [Pg.146]

The present model deals with a supported transition metal cation which is highly dispersed, at the molecular scale, on an oxide, or exchanged in a zeolite. In the case of zeolite-supported cations, the formation of different metal species in metal/zeolite catalysts (metal oxides, metal oxocations, besides cationic species) has been considered by different authors who have suggested these species to play key roles in SCR catalysis [14,15], This supported cation can also be considered as located at a metal oxide/support interface. [Pg.147]

As can be seen, the catalytic process over a zeolite-supported cation, or an oxide-supported cation, can be considered as a supported homogeneous catalysis, as far as adsorbed reactants and products behave like reactive ligands. The model developed for lean DcNO. catalysts over supported cations (function 3), as well as this supported homogeneous catalysis approach, is also suitable for stoichiometric mixture (TWC) comprising CO and H2 as reductants over supported transition metal cations [20-22],... [Pg.148]

Molybdenum allyl complexes react with surface OH groups to produce catalysts active for olefin metathesis.34 35 Using silica as a support for the heterog-enization of Ti and Zr complexes for the polymerization of ethylene did not give clear results.36 In these cases, HY zeolite appeared to be a more suitable support. The comparable productivity of the zeolite-supported catalyst with... [Pg.250]

On sulfided metallic phases the hydrotreatment reactions also takes place. Noble metal catalysts usually include a zeolitic support. They are particularly used for fulfilling two different objectives, in the case of a gasoline oriented HCK their cracking and isomerization activity is the most important (increasing high octane and conversion yield). In a diesel HCK unit, the noble metal catalyst is mainly oriented to aromatic saturation and cetane improvement. However, in this latter case, also sulfided metal catalysts are used, especially NiW. [Pg.43]

The microwave technique has also been found to be a potential method for the preparation of the catalysts containing highly dispersed metal compounds on high-porosity materials. The process is based on thermal dispersion of active species, facilitated by microwave energy, into the internal pore surface of a microporous support. Dealuminated Y zeolite-supported CuO and CuCl sorbents were prepared by this method and used for S02 removal and industrial gas separation, respectively [5], The results demonstrated the effective preparation of supported sorbents by micro-wave heating. The method was simple, fast, and energy-efficient, because the synthesis of both sorbents required a much lower temperature and much less time compared with conventional thermal dispersion. [Pg.348]

Schmitz, A.D., G. Bowers, and C. Song, Shape-selective hydrogenation of naphthalene over zeolite-supported Pt and Pd catalysts. Catal. Today, 31,45-56 (1996). [Pg.473]

After the catalytic runs no modification of mean particle size is observed for this last system. Conversly, Ru CO) deposited on silica-alumina is readily decomposed at 200°C to metallic particles of 1 nm mean size which are also catalysts for the F-T synthesis. The catalytic activity at 200°C is C i one tenth of the Y zeolite supported ones and methane is practically the only hydrocarbon formed. Electron microscopy examination of the catalyst after reaction reveals a drastic sintering of the... [Pg.199]

Yamamoto, Ichikawa, and coworkers—mesoporous material and zeolite supported Au and Pt catalysts—formate intermediates observed with Au/zeolites. [Pg.267]

Pt supported on an acidic support is a typical catalyst for the skeletal isomerization of light n-paraffins. The acidic supports can be acidic oxides, e.g., halogenated (Cl, F) alumina or sulfated zir-conia (Zr02/S04), or an appropriate zeolite, e.g., Mordenite. Pt-(C1, F)-alumina catalysts have a high performance at low temperatures and efficiently operate at temperatures between 115 and 150°C. Such low temperatures thermodynamically favor isomerization and thus, highly branched products are obtained. Zeolite supports are less active at lower temperatures and have to be operated at about... [Pg.115]


See other pages where Zeolites supported is mentioned: [Pg.17]    [Pg.168]    [Pg.314]    [Pg.107]    [Pg.114]    [Pg.132]    [Pg.219]    [Pg.220]    [Pg.223]    [Pg.38]    [Pg.89]    [Pg.279]    [Pg.349]    [Pg.81]    [Pg.310]    [Pg.305]    [Pg.45]    [Pg.495]   
See also in sourсe #XX -- [ Pg.39 , Pg.204 ]




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Support zeolites

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