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Relationships between Catalyst Production and Performance

Catalyst design and production are the judicious application of available knowledge of the effect of production variables on catalyst structure and of the relationship between catalyst structure and performance. The usefulness of a catalyst is governed by certain performance requirements. The chief requirement is selectivity, the capability to accelerate reaction rates of desired reactions. Selectivity also includes the ability to minimize side reactions that are particularly deleterious, for example, those that lead to deactivating coke formation. Second, catalysts must be sufficiently active at reasonable temperatures for commercial application. [Pg.88]

Kinetic analysis of asymmetric autocatalysis was performed to study the reaction mechanism of asymmetric autocatalysis. The relationship between the reaction time and the yields of the product was investigated [67]. The i-P Zn addition to pyrimidine-5-carbaldehyde 11 was performed in the presence of enantiomerically pure autocatalyst, the reaction being monitored by HPLC using naphthalene as an internal standard. The plots shown in Fig. 4(a) constitute S-shaped curves that are characteristic of an autocatalytic reaction. The relationship between time, yield and enantiomeric excess was also measured in the asymmetric autocatalysis with amplification of ee using high to low ee of pyrimidyl alkanol as the catalyst (Fig. 4b) [68]. Portions of the reaction mixture were quenched periodically and analyzed by chiral HPLC. When pyrimidyl alkanols with high to good ee are used as the asymmetric autocatalyst, the observed values of yield and ee were well matched to our simulated... [Pg.10]

A similar lack of clarity pervades other areas concerning the relationship between the catalytic performance and fundamental properties of the catalysts. Wakabayashl et al. (10) reported that the optimized conversion of propylene to acrolein (>7%) over alumina-supported tin-antimony oxide (3 1) was dependent on the sintering temperature of the catalyst and was maximized after heating at 10(X)°C for 3 hr. Further work (22) showed that both electrical conductivity and surface area were maximized in the material containing 3% antimony and a close association between acrolein production and solid solution formation was suggested. [Pg.117]

The performance of the catalyst critically depends on the distribution of Co through the alumina carrier, as well as of Co particle size and distribution, degree of reduction, and pore structure of the alumina. The relationship between these parameters is not trivial, e.g. a high dispersion catalyst is not necessarily a good catalyst in terms of activity, selectivity and stability. Another aspect is the influence of impurities in raw materials, and during catalyst production and... [Pg.335]

Sabatier and Balandin had predicted a relationship between catal)dic activity and heat of adsorption. If a solid adsorbs the reactants only weakly, it will be a poor catalyst, but if it holds reactants, intermediates or products too strongly, it wiU again perform poorly. The ideal catalyst for a given reaction was predicted to be a compromise between too weak and too strong chemisorption. Balandin transformed this concept to a semiquantitative theory by predicting that a plot of the reaction rate of a catal)Tic reaction as a function of the heat of adsorption of the reactant should have a sharp maximum. He called these plots volcano-shaped curvesl This prediction was confirmed by Fahrenfort et al." An example of their volcano-shaped curve is reproduced in Fig. 9.1. They chose the catalytic decomposition of formic acid... [Pg.141]

The use of secondary modifiers, e. g. quinoline, and the choice of solvent also play important roles in directing semi-hydrogenation selectivity. For example, in the hydrogenation of 1-octyne over a series of Pd/Nylon-66 catalysts metal loading had no effect on selectivity when the reaction was performed in n-heptane as solvent. When the same experiment was conducted in n-propanol, however, an inverse relationship between selectivity and catalyst metal loading was observed [56], This effect has been interpreted as a polar solvent-induced modification of the Pd active sites, which alters the relative adsorption behavior of the alkyne and alkene species [57], Modification by addition of quinoline is reported to benefit the selective production of a cij-vitamin D precursor from the related disubstituted alkyne [58] ... [Pg.357]


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Catalyst performance

Catalyst performance relationships

Catalyst productivity

Catalysts production

Performance relationships

Product performance

Production performance

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