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Catalyst preparation and

Kiziing M B and Jaras S G 1996 A review of plasma techniques in catalyst preparation and catalytic reactions Appl. Catalysis A 147 1-21... [Pg.2813]

Fig. 2. LP Oxo gas recycle flow scheme A, feedstock pretreatment B, reactor C, catalyst preparation and treatment systems D, condenser E, separator F,... Fig. 2. LP Oxo gas recycle flow scheme A, feedstock pretreatment B, reactor C, catalyst preparation and treatment systems D, condenser E, separator F,...
Ethylene Oxide Catalysts. Of all the factors that influence the utihty of the direct oxidation process for ethylene oxide, the catalyst used is of the greatest importance. It is for this reason that catalyst preparation and research have been considerable since the reaction was discovered. There are four basic components in commercial ethylene oxide catalysts the active catalyst metal the bulk support catalyst promoters that increase selectivity and/or activity and improve catalyst life and inhibitors or anticatalysts that suppress the formation of carbon dioxide and water without appreciably reducing the rate of formation of ethylene oxide (105). [Pg.458]

We started the fundamental research on the direct synthesis of DME finm synthesis gas, including catalyst preparation and reactor and process development, since 1998. In 2002, we... [Pg.490]

The reactions were carried out in the steady state flow mode as described previously [11]. Differential kinetics were determined from plots of conversion vs. W/F. Three catalysts CoZSM-5, HZSM-5 and NaZSM-5 (Si/AI = 11) were studied in this work. The catalyst preparation and the standard pretreatment used prior to reaction have been described previously [11]. It involved dehydration in flowing dried 0 as the temperature was raised slowly to 500°C. The feed comprised CH4 (0.28%), NO (0.21 %) or NOj (0.21 %). and/or Oj (2.6%) in He. The flow rate was 75 ml/min and the gas hour space velocity (GHSV) was varied between 4,500 and 250,000 h by changing the weight of catalyst samples. [Pg.652]

In this paper we report (i) the catalytic activity for SCR of VOx/Zr02 samples prepared by various methods (adsorption from aqueous metavanadate solutions at different pH values, dry impregnation, and adsorption from VO(acetylacetonate)2 in toluene), (ii) sample characterization (nuclearity, dispersion and oxidation state) by means of XPS, ESR and FTIR and (iii) the nature and reactivity of the surface species observed in the presence of the reactant mixture. Catalytic results are here reported in full. Characterization data relevant to the discussion of the catalytic activity will be given, whereas details on the catalysts preparation and... [Pg.691]

Kim and Somorjai have associated the different tacticity of the polymer with the variation of adsorption sites for the two systems as titrated by mesitylene TPD experiments. As discussed above, the TiCl >,/Au system shows just one mesitylene desorption peak which was associated with desorption from low coordinated sites, while the TiCl c/MgClx exhibits two peaks assigned to regular and low coordinated sites, respectively [23]. Based on this coincidence, Kim and Somorjai claim that isotactic polymer is produced at the low-coordinated site while atactic polymer is produced at the regular surface site. One has to bear in mind, however, that a variety of assumptions enter this interpretation, which may or may not be vahd. Nonetheless it is an interesting and important observation which should be confirmed by further experiments, e.g., structural investigations of the activated catalyst. From these experiments it is clear that the degree of tacticity depends on catalyst preparation and most probably on the surface structure of the catalyst however, the atomistic correlation between structure and tacticity remains to be clarified. [Pg.143]

Yeong, K. K., Gavriilidis, A., Zape, R., Hessel, V., Catalyst preparation and deactivation issues for nitrobenzene hydrogenation in a microstructured falling film reactor, Catal. Today 81, 4 (2003) 641-651. [Pg.654]

AujC fVGC Reference Catalyst Preparation and Characterization... [Pg.258]

Table 40,1. Catalysts prepared, and value of specific surface area. Table 40,1. Catalysts prepared, and value of specific surface area.
In the most effective, chirally modified catalytic systems, Pt/cinchonidine and Raney-Ni/tartaric acid, the enantioselectivity was also sensitive to the method of catalyst preparation and on support properties (5, 6). [Pg.525]

The book focuses on three main themes catalyst preparation and activation, reaction mechanism, and process-related topics. A panel of expert contributors discusses synthesis of catalysts, carbon nanomaterials, nitric oxide calcinations, the influence of carbon, catalytic performance issues, chelating agents, and Cu and alkali promoters. They also explore Co/silica catalysts, thermodynamic control, the Two Alpha model, co-feeding experiments, internal diffusion limitations. Fe-LTFT selectivity, and the effect of co-fed water. Lastly, the book examines cross-flow filtration, kinetic studies, reduction of CO emissions, syncrude, and low-temperature water-gas shift. [Pg.407]

The majority of the presentations can be grouped into three subject areas catalyst preparation and activation, reaction mechanism, and process-related topics. [Pg.422]

The [S]cr value depends on the nature of the catalyst, its surface area per unit of weight, the ratio of the rates of hydroperoxide decomposition into free radicals and molecular products, hydrocarbon and dioxygen concentrations, the method of catalyst preparation, and the chemical treatment of the surface. [Pg.425]

Reetz, M.T. and Koch, M., Water-soluble colloidal Adams catalyst preparation and use in catalysis,... [Pg.92]

Note Products depend on reaction conditions and on catalyst preparation and treatment. References given as examples only. [Pg.143]

Figure 8.7 Structural changes of ReOx species in HZcvd catalyst preparation and the catalytic reaction conditions, and a proposed structure of active [Re6017] cluster in the ZSM-5 pore channel, where the [Re6013] cluster is bound to the pentagonal rings of the zeolite inner wall via three lattice oxygen atoms, and the oxygen atoms are tentatively arranged on the Re6 octahedron. Figure 8.7 Structural changes of ReOx species in HZcvd catalyst preparation and the catalytic reaction conditions, and a proposed structure of active [Re6017] cluster in the ZSM-5 pore channel, where the [Re6013] cluster is bound to the pentagonal rings of the zeolite inner wall via three lattice oxygen atoms, and the oxygen atoms are tentatively arranged on the Re6 octahedron.
In this brief overview, we will use selected examples to illustrate how nanotechnology impacts catalyst preparation and ways that catalytic reactions can be conducted. We will also discuss the impact of catalysis on nanotechnology using examples where catalysts are used to facilitate preparation of nanostructures and nanomaterials, and to produce motion in nanomachines. [Pg.5]

A number of recenf reviews of DMFC technology are available. See those by McNicol, Rand, and Williams for earlier developments of catalysts for DMFC, Thomas ef al. for cafhode catalyst development at LANL, and Liu et al. for a summary of anode catalyst preparation and support development. ... [Pg.47]

Jao, R.-M., Leu, L.-J., and Chang, J.-R. (1996) Effects of catalyst preparation and pretreatment on light naphtha isomerization over mordenite-supported Pt catalysts. Appl Catal A., 135, 301-315. [Pg.501]

Attention to catalyst preparation and reaction conditions is of crucial importance for the success of an Ir-catalyzed allylic substitution, because many ligands are altered by C—H activation at aryl (see above) or CH3 groups. For most reactions, tetrahydrofuran (THF) is the preferred solvent it is important that dry THF (<35gg H20mr THF, Karl Fischer titration) is used for catalyst preparation because this step is very sensitive to water. The following procedures have been appHed. [Pg.217]

With an available diesel emergency generator supplying power to critical pumps, the control room operators initiated shutdown procedures for the two reactor areas. An uninterruptible power supply (UPS) kept power to the DCS screens and instruments however, the DCS system was designed close all catalyst preparation and reactor feed valves on loss of power. Outside operators were sent to manually block in reactor feeds. [Pg.370]

Conduct a thorough Process Hazards Analysis (PHA) for the following areas raw material storage, raw material feed systems, catalyst preparation, and catalyst storage. The PHA leader must he on the approved corporate list. Ensure the following scenarios are considered ... [Pg.377]


See other pages where Catalyst preparation and is mentioned: [Pg.342]    [Pg.195]    [Pg.231]    [Pg.214]    [Pg.117]    [Pg.71]    [Pg.112]    [Pg.475]    [Pg.542]    [Pg.156]    [Pg.315]    [Pg.14]    [Pg.319]    [Pg.24]    [Pg.113]    [Pg.293]    [Pg.207]    [Pg.381]    [Pg.375]    [Pg.61]    [Pg.422]    [Pg.154]    [Pg.242]    [Pg.243]    [Pg.245]    [Pg.247]    [Pg.249]   


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