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Catalyst improvements

The oxidation of methacrolein to methacrylic acid is most often performed over a phosphomolybdic acid-based catalyst, usually with copper, vanadium, and a heavy alkaU metal added. Arsenic and antimony are other common dopants. Conversions of methacrolein range from 85—95%, with selectivities to methacrylic acid of 85—95%. Although numerous catalyst improvements have been reported since the 1980s (120—123), the highest claimed yield of methacryhc acid (86%) is still that described in a 1981 patent to Air Products (124). [Pg.253]

Catalyst improvements allow methanol plants and plants using the Oxo process for aldehyde production to operate at lower pressures. The process also has a higher yield and produces a better quality product (Dale, 1987). [Pg.44]

Acid-treated clays were the first catalysts used in catalytic cracking processes, but have been replaced by synthetic amorphous silica-alumina, which is more active and stable. Incorporating zeolites (crystalline alumina-silica) with the silica/alumina catalyst improves selectivity towards aromatics. These catalysts have both Fewis and Bronsted acid sites that promote carbonium ion formation. An important structural feature of zeolites is the presence of holes in the crystal lattice, which are formed by the silica-alumina tetrahedra. Each tetrahedron is made of four oxygen anions with either an aluminum or a silicon cation in the center. Each oxygen anion with a -2 oxidation state is shared between either two silicon, two aluminum, or an aluminum and a silicon cation. [Pg.70]

Improve Chemical Engineering. Improvements in catalyst performance inevitably mean that the optimum plant operating condition will be different from that for the unimproved catalyst. Design changes may be needed to obtain the maximum benefit from improved performance. The cost of such changes must be taken into account when assessing the value of catalyst improvement. [Pg.242]

Promotion We use the term promotion, or classical promotion, to denote the action of one or more substances, the promoter or promoters, which when added in relatively small quantities to a catalyst, improves the activity, selectivity or useful lifetime of the catalyst. In general a promoter may either augment a desired reaction or suppress an undesired one. For example, K or K2O is a promoter of Fe for the synthesis of ammonia. A promoter is not, in general, consumed during a catalytic reaction. If it does get consumed, however, as is often the case in electrochemical promotion utilizing O2 conducting solid electrolytes, then we will refer to this substance as a sacrificial promoter. [Pg.9]

All mechanistic studies on activation by NHC complexes are of great interest (particularly when computations and experiments are combined) as they help rationalise catalytic behaviour, they allow catalyst improvement and nltimately they might allow rational catalyst design. [Pg.241]

In contrast to simple metalloporphyrins, or cofacial diporphyrins, the catalytic performance of these biomimetic catalysts improves at higher pH as a result, the smallest overpotential was observed at pH 8 (0.5 V) and at pH > 8 no partially reduced oxygen species could be detected at any potential. [Pg.680]

Entry 6 is an example of application of the chiral diazaborolidine enolate method (see p. 572). Entry 7 involves generation of the silyl ketene acetal by silylation after conjugate addition of the enolate of 3-methylbutanoyloxazolidinone to allyl 3,3,3-trifluoroprop-2-enoate. A palladium catalyst improved the yield in the rearrangement... [Pg.575]

The Pschorr reaction is a method of synthesis of phenanthrenes from diazotized Z-2-aminostilbenes. A traditional procedure involves heating with a copper catalyst. Improved yields are often observed, however, if the diazonium ion is treated with iodide ion. Suggest a mechanism for the iodide-catalyzed reaction. [Pg.1061]

Figure 2). However, the work clearly shows the need for catalyst improvement and leaves open the opportunity to identify other novel products. With these results in mind we can now turn to our preliminary work in this area. Figure 2). However, the work clearly shows the need for catalyst improvement and leaves open the opportunity to identify other novel products. With these results in mind we can now turn to our preliminary work in this area.
Historically, catalyst improvements take place continuously, at a rate of circa 25% increase in activity every four years, for established processes. However, the changes... [Pg.32]

The application of the hybrid catalysts improved the quality of the produced oil. This was noticed as an increase in the water content in the oil, implying that de-oxygenation over the hybrid catalysts was more intense than over the pure materials. [Pg.320]

As mentioned above one of the fundamental attributes ascribed to homogeneous catalysts is superior activity at low temperature. However, even within classes of such catalysts, improvements in catalyst activity can be made allowing operation at lower temperatures, thus reducing or avoiding completely this mode of catalyst decay. One such example can found in recent advances in palladium catalysed ethene carbonylation (Equation 1.1). [Pg.5]

Ronning, Holmen, and coworkers—Ce doping of Cu/Zn/Al catalysts improves stability. Ronning et al,339 explored the impact of ceria addition to Cu/ZnO catalysts. Catalysts were prepared by co-precipitation of Cu, Zn, and Al from their corresponding nitrates. Ceria was incorporated into the catalyst by impregnation of cerium nitrate either before or after calcination (6 hours at 350 °C or 400 °C). The chemical compositions of the resulting catalysts are reported in Table 62. [Pg.208]

It used to be that the iso-butyraldehyde had to be split out before the dimerization reaction, but catalyst improvements have permitted cogeneration of both C4 alcohols and 2-EH. [Pg.206]

The Sohio technology is based on a catalyst of bismuth an4 molybdenum oxides. Subsequent catalyst improvements came from the use of bismuth phosphomolybdate on a silica gel, and more recently, antimony-uranium oxides. Each change in catalyst was motivated Jby a higher conversion rate per pass to acrylonitrile. [Pg.276]

Coke formation during xylene isomerization has been studied using in situ infrared spectroscopy [78]. A study done on EB isomerization with a bifunctional catalyst containing EUO zeolite indicated that poor initial selectivity of the catalyst improves after a period of fast deactivation, during which micropores are blocked [79]. [Pg.495]

In this case RAMEB acts as a catalyst improving the transfer of pollutants from the solid phase to the aqueous phase of the soil. [Pg.218]

Upon the addition of Lewis (i.e. All ) and protonic non-compSexing. acids (i.e. HPF5) promoters to [Ru(00)3X3] catalysts, improvements in selectivity to valuable products (acetic acid + ethyl acetate) and in reaction rate are observed. This is believed to be due to an acceleration by acids of the alkyl migration-carbonyl insertion step of the process, as discussed in detail in a recent paper (10). [Pg.230]


See other pages where Catalyst improvements is mentioned: [Pg.416]    [Pg.135]    [Pg.508]    [Pg.155]    [Pg.73]    [Pg.422]    [Pg.232]    [Pg.278]    [Pg.191]    [Pg.473]    [Pg.229]    [Pg.172]    [Pg.292]    [Pg.526]    [Pg.558]    [Pg.115]    [Pg.431]    [Pg.418]    [Pg.61]    [Pg.245]    [Pg.998]    [Pg.3]    [Pg.114]    [Pg.341]    [Pg.308]    [Pg.320]    [Pg.64]    [Pg.313]    [Pg.430]    [Pg.346]   
See also in sourсe #XX -- [ Pg.576 ]




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