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Catalytic reactions using

The study of catalytic reactions using surface science teclmiques has been fniithil over the last 30 years. Great strides have been made towards understanding the fiindamentals of catalytic reactions, particularly by... [Pg.953]

S. Bebelis, M. Makri, A. Buekenhoudt, J. Luyten, S. Brosda, P. Petrolekas, C. Pliangos, and C.G. Vayenas, Electrochemical activation of catalytic reactions using anionic, cationic and mixed conductors, Solid State Ionics 129, 33-46 (2000). [Pg.185]

Some Other Catalytic Reactions Useful for Fine Chemical... [Pg.105]

In contrast to Fe(-f3)-ate complexes a variety of examples for catalytic reactions using Fe(+2)-ate complexes are known in literature. [Pg.183]

These are just a few examples of catalytic reactions used industrially. Catalyst research is one of the most active areas of chemistry and chemical engineering. Our Box describes one direction such research is taking. [Pg.1110]

Each enzyme has a working name, a specific name in relation to the enzyme action and a code of four numbers the first indicates the type of catalysed reaction the second and third, the sub- and sub-subclass of reaction and the fourth indentifies the enzyme [18]. In all relevant studies, it is necessary to state the source of the enzyme, the physical state of drying (lyophilized or air-dried), the purity and the catalytic activity. The main parameter, from an analytical viewpoint is the catalytic activity which is expressed in the enzyme Unit (U) or in katal. One U corresponds to the amount of enzyme that catalyzes the conversion of one micromole of substrate per minute whereas one katal (SI unit) is the amount of enzyme that converts 1 mole of substrate per second. The activity of the enzyme toward a specific reaction is evaluated by the rate of the catalytic reaction using the Michaelis-Menten equation V0 = Vmax[S]/([S] + kM) where V0 is the initial rate of the reaction, defined as the activity Vmax is the maximum rate, [S] the concentration of substrate and KM the Michaelis constant which give the relative enzyme-substrate affinity. [Pg.445]

The production of synthesis gas based on heterogeneous catalytic reactions using 02 (air) as an oxidant is referred to as catalytic POx (CPO). Although the process is potentially able to process a wide range of hydrocarbon feedstocks, including heavy hydrocarbons, most of the information in the literature relates to the CPO of methane (or NG). The CPO of methane can be presented by the following equation ... [Pg.51]

Catalysis is a special type of closed-sequence reaction mechanism (Chapter 7). In this sense, a catalyst is a species which is involved in steps in the reaction mechanism, but which is regenerated after product formation to participate in another catalytic cycle. The nature of the catalytic cycle is illustrated in Figure 8.1 for the catalytic reaction used commercially to make propene oxide (with Mo as the catalyst), cited above. [Pg.177]

Fig. 1 Graphical representation shows immobilized enzyme catalytic activity and their recovery after the completion of the catalytic reaction using a simple magnet. Fig. 1 Graphical representation shows immobilized enzyme catalytic activity and their recovery after the completion of the catalytic reaction using a simple magnet.
More recently spinning disc reactors have been used by Wilson et alP0) to carry out catalytic reactions using supported zinc triflate catalyst for the rearrangement of a-pinene oxide to yield campholenic aldehyde. The results of this study, presented in Table 20.1, suggest that by using a supported catalyst on a spinning disc reactor it is possible to... [Pg.1130]

The turnover reaction of hydrolysis of 2, 3 -CMP could be made negligibly slow at temperatures below -60°C at pH 3-6 in 70% methanol, and below -35°C at pH 2.1. The rate of the catalytic reaction using crystalline enzyme was found to be 50-fold slower than that of dissolved enzyme for cyclic phosphate hydrolysis, and 200-fold slower for dinucleotide hydrolysis (presumably the greater reduction for the larger substrate reflects increased diffusional hindrance by the small solvent chan-... [Pg.266]

The catalytically active species 31 was isolated and its structure definitively determined using X-ray analysis. The complex 31 was seen to be quite stable below 70 °C under an argon atmosphere at pH 2.0-6.0 and in the absence of any reducible carbonyl compounds [50]. When the reducing ability of isolated 31 in acidic media was examined, the catalytic reactions using cyclohexanone and acetophenone (31 ketones HCOOH = 1 200 1000) yielded the corresponding alcohols quantitatively in 2h at pH2.0 at 70°C (Scheme 5.17). [Pg.122]

Very few catalytic reactions using complexes with stable non-NHC carbenes have been reported yet. Nevertheless, taking advantage of the specific properties of non-NHC carbenes, several catalytic reactions have been described, especially using CAACs. [Pg.142]

Acetoxylation of naphthalene was achieved with stoichiometric amount of Pd(OAc)2 or in a catalytic reaction using the Cu2+ + 02 system for the reoxidation of Pd(0) 786... [Pg.495]

Here the evaluation of the surface concentration of charged particles during the reaction is important for investigating the conversion and selectivity in the heterogeneous catalytic reaction. Using a treatment similar to Hauffe s (II), the concentration of charged particles on the surface can be evaluated at equilibrium as ... [Pg.284]

Further acid site strength and concentration measurements were reported by Morita et al. (164), who related the acidity measurements to various catalytic reactions. Using Y zeolite (Linde SK-40, 90% H form) activated at 450°C, they observed no acid sites stronger than an H0 of -8.2, although the total acid site concentration was almost twice that of the former investigations (Fig. 21, curve 4). They also measured acid site concentration as a function of decomposition temperature for NH4Y, and found that n-butylamine titration values paralleled results obtained from pyridine adsorption studies (41,151). The maximum total acidity occurred... [Pg.145]

These observations show that the catalytic reactions using complexes of different diphosphine ligands are likely to involve different reaction mechanisms. Also, subtle variations in metal basicity and catalyst stereochemistry can affect significantly the rate and mechanism of reaction. Therefore it is highly risky to generalize a reaction mechanism to seemingly similar catalysts. Our current research is directed towards determining these mechanistic differences. [Pg.88]

The reductive elimination eventually releases the newly formed organic product in a concerted mechanism. In the course of this process, the electron count is reduced by two. Iron has a great tendency for coordinative saturation, which in general does not favor processes such as ligand dissociation and reductive elimination. This aspect represents a potential limiting factor for catalytic reactions using iron. [Pg.3]

In the N-sulfonyl imine-catalyzed sulfoxidation, aqueous hydrogen peroxide serves as the final oxidizing agent, which is clearly of practical advantage. In principle it can be assumed that either an oxaziridine (F, Scheme 10.17) or a hydroper-oxy hemiaminal (H, Scheme 10.17) can result as the active species from the reaction of the N-sulfonyl imine E with hydrogen peroxide (Scheme 10.17). For imine 79 the idea of an intermediate oxaziridine is supported by the experimental finding that oxidation by the isolated oxaziridine and in the catalytic reaction (using 79 and... [Pg.303]

Right- and left-handed helical silica, Fig. lc,d, has been successfully used as an auxiliary in a catalytic reaction used in absolute asymmetric synthesis [56]. [Pg.128]


See other pages where Catalytic reactions using is mentioned: [Pg.920]    [Pg.283]    [Pg.55]    [Pg.185]    [Pg.185]    [Pg.50]    [Pg.244]    [Pg.15]    [Pg.240]    [Pg.480]    [Pg.339]    [Pg.416]    [Pg.244]    [Pg.187]    [Pg.217]    [Pg.41]    [Pg.376]    [Pg.88]    [Pg.64]    [Pg.110]    [Pg.4]    [Pg.291]    [Pg.284]    [Pg.15]    [Pg.8]    [Pg.88]    [Pg.30]   


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