Standard catalyst

Many catalysts have been used but the standard catalysts are generally mixtures of silica and alumina or natural or synthetic aluminium silicate zeolites. 

Coke Factor is coke-forming characteristics of the equilibrium catalyst relative to coke-forming characteristics of a standard catalyst at the same conversion. 

Copper ore containing a deposit of aurlchalclte was obtained from Wards Natural Science Establishment. The mineral aurlchalclte crystallites were gently scraped from the ore and rinsed In ethanol prior to use. The synthetic precursor was prepared by copreclpltatlon from a mixture of IM Cu and IM Zn nitrate solutions, such that a Cu/Zn mole ratio of 30/70 was prepared, by dropwlse addition of IM Na2C03 at 90 C until the pH Increased from approximately 3 to 7. Calcination and reduction of the mineral were performed as In standard catalyst preparation procedures, which have been described In detail earlier (jL). ... 

The aurlchalclte mineral was calcined In air at 350°C for 4 hours according to the standard catalyst preparation procedure used earlier for the precipitated precursor (1 ). XRD showed that aurlchalclte and... 

In summary, large (>lpm) single crystal platelets of aurichalcite produced highly dispersed Cu and ZnO particles with dimensions on the order of 5 nm, as a result of standard catalyst preparation procedures used in the treatment of the precipitate precursors. The overall platelet dimensions were maintained throughout the preparation treatments, but the platelets became porous and polycrystalline to accommodate the changing chemical structure and density of the Cu and Zn components. The morphology of ZnO and Cu in the reduced catalysts appear to be completely determined by the crystallography of aurichalcite. 

In contrast, substituting the ort/to-methyl groups of SIMes with ortho-fluoride atoms profoundly alters the catalytic metathesis performance. In 2006, Grubbs and co-workers reported the synthesis of the fluorinated NHC-Ru catalysts 25 and 26 [41] (Fig. 3.8). Catalytic tests in the RCM of 1 to form 2 showed that the phosphine-free catalyst 26 was slower than the standard catalyst 16, which was consistent with theoretical investigations suggesting the electron-withdrawing fluoride atoms would lead to a decrease in catalyst activity [42]. However, in contrast to the computational... 

The outstanding performances of five-membered NHC ligands in organometallic chemistry and catalysis prompted Grubbs and co-workers to develop a novel stable four-membered NHC [64]. Following their interest in developing new ruthenium olefin metathesis catalysts, they synthesised and fully characterised complex 51 to study the impact of the architecturally unique NHC ligand on the activity of the Ru-based catalyst [65] (Fig. 3.20). In the RCM of 1 at 40°C in CH Cl with 51 (5 mol% catalyst), the reaction reached completion within 20 min, whereas less than 10 min are required for standard catalysts 14 and 16. It should be noted that catalysts 14 and 16 are able to complete the RCM of 1 with only 1 mol% catalyst at 30°C. 

Reaction temperatures of 60-120 °C are routinely used with standard catalysts and conventional heating sources [16]. Attempts to reduce reaction times by the use of higher temperatures are seldom effective, because the catalytic systems are often sensitive to heat [17]. As a consequence, access to new methods that enable fast coupling reactions has been highly desirable. 

This is also a reversible, exothermic reaction. Some reactors used for this reaction are similar to those used for ammonia synthesis see Figure 11.6. The standard catalyst is Cu/Zn0/Al203. 

The ruthenium compounds described above show a distinctly lower metathetic activity than the molybdenum alkenylidene complex 24 developed by Schrock et al. (Fig. 4, see also the chapter by R.R. Schrock, this volume) [18], which is another standard catalyst for any type of olefin metathesis reaction. However, they... 

This survey focuses on recent developments in catalysts for phosphoric acid fuel cells (PAFC), proton-exchange membrane fuel cells (PEMFC), and the direct methanol fuel cell (DMFC). In PAFC, operating at 160-220°C, orthophosphoric acid is used as the electrolyte, the anode catalyst is Pt and the cathode can be a bimetallic system like Pt/Cr/Co. For this purpose, a bimetallic colloidal precursor of the composition Pt50Co30Cr20 (size 3.8 nm) was prepared by the co-reduction of the corresponding metal salts [184-186], From XRD analysis, the bimetallic particles were found alloyed in an ordered fct-structure. The elecbocatalytic performance in a standard half-cell was compared with an industrial standard catalyst (bimetallic crystallites of 5.7 nm size) manufactured by co-precipitation and subsequent annealing to 900°C. The advantage of the bimetallic colloid catalysts lies in its improved durability, which is essential for PAFC applicabons. After 22 h it was found that the potential had decayed by less than 10 mV [187],... 

The utility of a palladium catalyst in the synthesis of substituted aryl acetylenes is well established.(7,8,9,10) The end-capping agent I was produced by using a standard catalyst system, dichlorobls(triphenylphosphlne)palladlum (II)/copper (I) iodide/triphenylphosphlne mixture, which has been employed in previously developed ethynylation procedures.(10) The copper (I) iodide is believed to act as a cocatalyst, reducing the palladium (II) complex to the active palladium (0) catalyst. The scheme is shown in Figure 3 (diethylamine is the solvent).(11)... 

Catalytic activity the ratio of the space velocity of the catalyst under test to the space velocity required for the standard catalyst to give the same conversion as the catalyst being tested usually multiplied by 100 before being reported. 

Wilkinson s catalyst [RhCl(PPh3)3], a standard catalyst for this reaction, is reported to give lower yields with less regioselectivity in these reactions. Conjugated dienes gave mixtures of 1,4- and 1,2-addition products in the presence of rhodium-NHC systems, whereas [RhCl(PPh3)3] leads to selective 1,4-addition. 

Industrial heterogeneous catalysts and laboratory-scale model catalysts are commonly prepared by first impregnating a support with simple transition metal complexes. Catalytically active metal nanoparticles (NPs) are subsequently prepared through a series of high temperature calcination and / or reduction steps. These methods are relatively inexpensive and can be readily applied to numerous metals and supports however, the NPs are prepared in-situ on the support via processes that are not necessarily well understood. These inherent problems with standard catalyst preparation techniques are considerable drawbacks to studying and understanding complex organic reaction mechanisms over supported catalysts. (4)... 

The addition of ethanol to diphenylketene (59a) shows that a standard catalyst like pyridine (50) may be incorporated into a concave structure and that... 

The composite and its isolated carbon network tested as a catalyst support on Fischer-Tropsch process shows big differences respect to the performance of a standard catalyst support. 

Derivatives of commercially available alkaloids, e.g. 8 and 13, have usually been used as the phase-transfer catalyst. Besides these classic standard catalysts, however, efforts have been also made to design novel organocatalysts with new proper-... 

The Accelrys implementation of pharmacophore fingerprint descriptors is called 3D Keys. This application is based on standard Catalyst feature definitions and is a part of the Cerius2 software package [7]. 

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