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Bonding, catalyst characterization

The book has been written as an introductory text, not as an exhaustive review. It is meant for students at the start of their Ph.D. projects and for anyone else who needs a concise introduction to catalyst characterization. Each chapter describes the physical background and principles of a technique, a few recent applications to illustrate the type of information that can be obtained, and an evaluation of possibilities and limitations. A chapter on case studies highlights a few important catalyst systems and illustrates how powerful combinations of techniques are. The appendix on the surface theory of metals and on chemical bonding at surfaces is included to provide better insight in the results of photoemission, vibrational spectroscopy and thermal desorption. [Pg.10]

Measurements of supported catalysts in diffuse reflection and transmission mode are in practice limited to frequencies above those where the support absorbs (below about 1250 cm-1). Infrared Emission Spectroscopy (IRES) offers an alternative in this case. When a material is heated to about 100 °C or higher, it emits a spectrum of infrared radiation in which all the characteristic vibrations appear as clearly recognizable peaks. Although measuring in this mode offers the attractive advantage that low frequencies such as those of metal-oxygen or sulfur-sulfur bonds are easily accessible, the technique has hardly been explored for the purpose of catalyst characterization. An in situ cell for IRES measurements and some experiments on Mo-O-S clusters of interest for hydrodesulfurization catalysts have been described by Weber etal. [11],... [Pg.224]

C.J. Wright (1985). In Catalysis. A Specialist Periodical Report, (Ed.) G.C. Bond G. Webb, pp. 46-74. Vol. 7. The Royal Society of Chemistry, London. Catalysts characterization with neutron techniques. [Pg.359]

A review is given of the use of spectroscopic techniques to investigate the MTG process. Examples are quoted of catalyst characterization, investigation of the first carbon-carbon bond formation, alkene oligomerization and catalyst deactivation through coke formation. [Pg.157]

Adhesion and Adhesives Adsorption Auger Electron Spectroscopy Bonding and Structure IN Solids Catalysis, Industrial Catalyst Characterization Chemical Thermodynamics Crystallography Photochemistry, Molecular Photoelectron Spectroscopy Solid-State Electrochemistry Tribology... [Pg.354]

Ratheesh Kumar, V. K. and K. R. Gopidas. Palladium nanoparticle-cored Gl-dendrimer stabilized by carbon-Pd bonds Synthesis, characterization and use as chemoselective, room temperature hydrogenation catalyst. Tetrahedron Lett. 52, 2011 3102-3105. [Pg.214]

Catalysis in a single fluid phase (liquid, gas or supercritical fluid) is called homogeneous catalysis because the phase in which it occurs is relatively unifonn or homogeneous. The catalyst may be molecular or ionic. Catalysis at an interface (usually a solid surface) is called heterogeneous catalysis, an implication of this tenn is that more than one phase is present in the reactor, and the reactants are usually concentrated in a fluid phase in contact with the catalyst, e.g., a gas in contact with a solid. Most catalysts used in the largest teclmological processes are solids. The tenn catalytic site (or active site) describes the groups on the surface to which reactants bond for catalysis to occur the identities of the catalytic sites are often unknown because most solid surfaces are nonunifonn in stmcture and composition and difficult to characterize well, and the active sites often constitute a small minority of the surface sites. [Pg.2697]

Rhodacarborane catalysts have been immobilized by attachment to polystyrene beads with appreciable retention of catalytic activity (227). A 13-vertex /oj iJ-hydridorhodacarborane has also been synthesized and demonstrated to possess catalytic activity similar to that of the icosahedral species (228). Ak-oxidation of closo- >(2- P((Z [) 2 - i- > l[l-Bih(Z, results in a brilliant purple dimer. This compound contains two formal Rh " centers linked by a sigma bond and a pak of Rh—H—B bridge bonds. A number of similar dimer complexes have been characterized and the mechanism of dimer formation in these rhodacarborane clusters have been studied in detail (229). [Pg.249]

The typical industrial catalyst has both microscopic and macroscopic regions with different compositions and stmctures the surfaces of industrial catalysts are much more complex than those of the single crystals of metal investigated in ultrahigh vacuum experiments. Because surfaces of industrial catalysts are very difficult to characterize precisely and catalytic properties are sensitive to small stmctural details, it is usually not possible to identify the specific combinations of atoms on a surface, called catalytic sites or active sites, that are responsible for catalysis. Experiments with catalyst poisons, substances that bond strongly with catalyst surfaces and deactivate them, have shown that the catalytic sites are usually a small fraction of the catalyst surface. Most models of catalytic sites rest on rather shaky foundations. [Pg.171]

Unfortunately, at present the information characterizing the properties of the active bond in polymerization catalysts is very scant. The analogy between the features of the active bonds in the propagation centers and those of the transition metal-carbon bond in individual organometallic compounds is sure to exist, but as in the initial form the latter do not show catalytic activity in olefin polymerization this analogy is restricted to its limits. [Pg.208]

The goal of this work was to prepare and characterize PtRu/MgO catalysts from cluster A which contained Pt-Ru bonds and compare with that prepared from a mixed solution of Pt(acac)2 and Ru(acac)3. The characterization methods included IR and EXAFS spectroscopy. Ethylene hydrogenation was used to test the catalytic activity of both PtRu/MgO catalysts. [Pg.209]

The addition of acetic acid (0.5 equiv. to the substrate) to the catalyst system led to increased activity (doubling of yield) by maintaining the selectivity with 1.2 equiv. H2O2 as terminal oxidant. Advantageously, the system is characterized by a certain tolerance towards functional groups such as amides, esters, ethers, and carbonates. An improvement in conversions and selectivities by a slow addition protocol was shown recently [102]. For the first time, a nonheme iron catalyst system is able to oxidize tertiary C-H bonds in a synthetic applicable and selective manner and therefore should allow for synthetic applications [103]. [Pg.96]


See other pages where Bonding, catalyst characterization is mentioned: [Pg.281]    [Pg.438]    [Pg.48]    [Pg.254]    [Pg.19]    [Pg.657]    [Pg.90]    [Pg.38]    [Pg.478]    [Pg.50]    [Pg.53]    [Pg.1046]    [Pg.217]    [Pg.769]    [Pg.504]    [Pg.91]    [Pg.2698]    [Pg.4]    [Pg.29]    [Pg.227]    [Pg.212]    [Pg.368]    [Pg.291]    [Pg.109]    [Pg.209]    [Pg.96]    [Pg.240]    [Pg.158]    [Pg.80]    [Pg.576]    [Pg.22]   
See also in sourсe #XX -- [ Pg.354 ]




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