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Catalysis optimized

Wijngaarden R.J, Kronberg A and Westerterp K.R (1998) Industrial Catalysis - Optimizing Catalysts and Processes, Wiley-VCH. [Pg.140]

Wijngaarden, Ruud Industrial Catalysis - Optimizing Catalysts and Processes / R. J. Wijngaarden A. Kronberg K. R. Westerterp. - Weinheim New York Chichester Brisbane Singapore Toronto WILEY-VCH, 1998 ISBN 3-527-28581-4... [Pg.275]

An improved procedure has been developed for the preparation of vinylphos-phonate-linked dinucleotide analogues such as 226. The method involves the coupling of an H-phosphonate diester at 0-3 of the top nucleoside with a p-bromovinyl derivative of thymidine, using palladium catalysis. Optimization studies were carried out, and under the best conditions, yields were high. ... [Pg.280]

Considering the featmes of G as one atom thick surface combining the possibility to imprint the active site or support the metal NPs, the use of G could lead in a few years to a drastic change in the panorama of catalysis optimizing the use of noble and critical metals and reducing the dependency of catalysis on these inorganic elements. [Pg.115]

Wijngaarden RJ, Kronberg A, Westerterp KR. Industrial Catalysis Optimizing Catalysts and Processes. Weinheim Wiley-VCH 1998. [Pg.77]

A kinetic method for the determination of 2,4-dinitrophenol is proposed. The method is based on the inhibiting effect of 2,4-dinib ophenol on the Mn(II) catalysis of the oxidation of malachite green with potassium periodate. The reaction was followed spectrophotometrically at 615 nm. The optimal experimental conditions for the determination of 2,4-dinitrophenol were established under the optimal reaction conditions ... [Pg.136]

In comparison to heterogeneous catalyzed reactions, homogeneous catalysis offers several important advantages. The catalyst complex is usually well defined and can be rationally optimized by ligand modification. Every metal center can be active in the reaction. The reaction conditions are usually much milder (T usually < 200 °C), and selectivities are often much higher than with heterogeneous catalysts. [Pg.218]

Control of emissions of CO, VOC, and NOj, is high on the agenda. Heterogeneous catalysis plays a key role and in most cases structured reactors, in particular monoliths, outperform packed beds because of (i) low pressure drop, (ii) flexibility in design for fast reactions, that is, thin catalytic layers with large geometric surface area are optimal, and (iii) attrition resistance [17]. For power plants the large flow... [Pg.191]

Figure 8.23. The solid and monotonically declining line to the right represents the equilibrium curve. The four curves represent lines with constant rates in the same plot. Since we want to operate at points where of maximum ammonia concentration, the optimal operation line is defined as the line running parallel to the equilibrium curve, passing through all the maxima. [Adapted from I. Dybkjaer, in Ammonia Catalysis and Manufacture (1995) Ed. A. Nielsen. Springer-Verlag, Berlin/Heidelberg, p. 199.]... Figure 8.23. The solid and monotonically declining line to the right represents the equilibrium curve. The four curves represent lines with constant rates in the same plot. Since we want to operate at points where of maximum ammonia concentration, the optimal operation line is defined as the line running parallel to the equilibrium curve, passing through all the maxima. [Adapted from I. Dybkjaer, in Ammonia Catalysis and Manufacture (1995) Ed. A. Nielsen. Springer-Verlag, Berlin/Heidelberg, p. 199.]...

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See also in sourсe #XX -- [ Pg.7 ]




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