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Catalyst over-heating

The first set of reactions is the mainstay of the petrochemical industry 1 outstanding examples are the oxidation of propene to propenal (acrolein) catalysed by bismuth molybdate, and of ethene to oxirane (ethylene oxide) catalysed by silver. In general these processes work at high but not perfect selectivity, the catalysts having been fine-tuned by inclusion of promoters to secure optimum performance. An especially important reaction is the oxidation of ethene in the presence of acetic (ethanoic) acid to form vinyl acetate (ethenyl ethanoate) catalysed by supported palladium-gold catalysts this is treated in Section 8.4. Oxidation reactions are very exothermic, and special precautions have to be taken to avoid the catalyst over-heating. [Pg.217]

The N20 decomposition, CO oxidation, and H2 oxidation reactions are known to exhibit concentration oscillations over noble metal catalysts. Flytzani-Stephanopoulos et al. (47) have observed oscillations for the oxidation of NH3 over Pt. The effects are dramatic and lead to large temperature cycles for the catalyst wire. Heat and mass transfer effects are important. [Pg.18]

Magnesium hydride is obtained hy combining the elements at about 500°C. A convenient method of preparation involves passing hydrogen under pressure over heated magnesium powder in the presence of magnesium iodide as catalyst. [Pg.524]

Other reported syntheses include the Reimer-Tiemann reaction, in which carbon tetrachloride is condensed with phenol in the presence of potassium hydroxide. A mixture of the ortho- and para-isomers is obtained the para-isomer predominates. -Hydroxybenzoic acid can be synthesized from phenol, carbon monoxide, and an alkali carbonate (52). It can also be obtained by heating alkali salts of -cresol at high temperatures (260—270°C) over metallic oxides, eg, lead dioxide, manganese dioxide, iron oxide, or copper oxide, or with mixed alkali and a copper catalyst (53). Heating potassium salicylate at 240°C for 1—1.5 h results in a 70—80% yield of -hydroxybenzoic acid (54). When the dipotassium salt of salicylic acid is heated in an atmosphere of carbon dioxide, an almost complete conversion to -hydroxybenzoic acid results. They>-aminobenzoic acid can be converted to the diazo acid with nitrous acid followed by hydrolysis. Finally, the sulfo- and halogenobenzoic acids can be fused with alkali. [Pg.292]

It must be repeated that this argument depends upon the assumption that there is only one way in which the molecules of formic acid can be attached to the surface of the catalyst. There is, however, some evidence against this assumption. Constable finds that the two simultaneous reactions undergone by allyl alcohol when passed over heated copper are differently influenced by the physical state of the catalyst. This points to the conclusion that there are two independent centres of activity on the catalyst surface with two different modes of adsorption, or, at any rate, centres where the energy of adsorption is so different that different reactions are facilitated. Hoover and Rideal f find that the two alternative decompositions of ethyl alcohol by thoria show a different behaviour towards poisons, which points to the same conclusion. [Pg.240]

C. After purging out the gas-phase butene, the catalyst was heated to various temperatures indicated, and the desorbed species were purged out of the reactor by He. Then a pulse of oxygen (or NzO) was passed over the catalyst at various temperatures. After the pulse had completely left the reactor, thermal desorption was resumed, and the desorption products were collected and analyzed. [Pg.173]

If an inert material is initially adsorbed on the fixed bed comprising an appropriate adsorbent and a catalyst, the heat of adsorption—having the same order of magnitude as the latent heat of evaporation—will be released (Figure 15). Since no reaction takes place in this phase, moderate temperature excursions are acceptable, and recycle flows over external heat exchangers or injection of liquid adsorptives may serve as heat sinks. In the subsequent reaction phase, the heat liberated by an exothermic reaction on the catalyst is taken up by the desorption of the inert from the previously loaded neighboring adsorbent particles. As long as this desorption occurs, the heat of reaction will not lead to major temperature increases. Sooner or later, of course, the adsorbent will be depleted and the temperatures will drift upward, at which point the adsorption phase must be repeated. [Pg.407]

Ammonia is now made by the Badischo Auiliu nnd Sodafabrik, by passing nitrogen and hydrogen over heated platinum a.t a temperature of 80°, under a, pvessnre of about thirty atmospheres. Other catalysts used in the process are manganese, uranium and osmium. [Pg.101]

Irreversible transformations are those in which reactants do not reform from products upon cooling. Generally one of the reactants is in a metastable state, and only requires thermal agitation or the presence of a catalyst to initiate the transformation. Examples would be combustion of a fossil fuel or glass devitrification. Power-compensated DSC has a distinct advantage over heat-flux DSC in determining the kinetics of transformation from metastable phases. In these type of reactions,... [Pg.60]

Indicate reaction conditions and catalysts over and under the arrow in a smaller type size. The Greek capital letter delta indicates heat hv indicates light, where h is Planck s constant and the Greek letter nu is the photon frequency. [Pg.272]

Many desirable characteristics of honeycomb monolithic catalyst beds were illustrated by these two examples (1) catalyst loading lower than on pellets was adequate to maintain activity (2) the axial heat transfer rate resulted in rapid heat dissipation from the reaction zone (3) a vanation of void-to-caialysi-surface ratio with new turbulent interfaces at each interval introduced a convenient control over the extent of reaction. Two other variables that were investigated are loading of catalyst over bed length and type of catalyst used however, the comparative analyses have not been as systematically demonstrated for the particular operation described in these tests. [Pg.182]


See other pages where Catalyst over-heating is mentioned: [Pg.52]    [Pg.52]    [Pg.30]    [Pg.70]    [Pg.71]    [Pg.166]    [Pg.163]    [Pg.208]    [Pg.507]    [Pg.292]    [Pg.538]    [Pg.2210]    [Pg.742]    [Pg.991]    [Pg.273]    [Pg.276]    [Pg.381]    [Pg.91]    [Pg.184]    [Pg.227]    [Pg.535]    [Pg.51]    [Pg.153]    [Pg.253]    [Pg.429]    [Pg.431]    [Pg.239]    [Pg.184]    [Pg.37]    [Pg.16]    [Pg.70]    [Pg.33]    [Pg.289]    [Pg.315]    [Pg.60]    [Pg.19]    [Pg.1966]    [Pg.113]    [Pg.199]    [Pg.1119]    [Pg.274]   
See also in sourсe #XX -- [ Pg.101 , Pg.118 ]




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