Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Catalyst Section

Hydrocinnamic acid may also be prepared by the reduction of cinnamic acid with sodium and alcohol or with sodium amalgam or with hydrogen in the presence of Adams platinum oxide catalyst (Section 111,150) ... [Pg.753]

Lindlar catalyst (Section 9 9) A catalyst for the hydrogenation of alkynes to as alkenes It is composed of palladium which has been poisoned with lead(II) acetate and quino line supported on calcium carbonate... [Pg.1288]

The ylides 276 derived from compound 2 undergo ring opening on thermolysis to give 2-pyridylcyanamides (Section IV.F), and react with acetylenic esters to give pyrazolopyridines (Scheme 12) (86H(24)2563). In the addition of DMAD some intermediate dihydro derivative is obtained and dehydrogenated with chlo-ranll. An ylide of system 3 is used as a catalyst (Section IV.J)... [Pg.51]

I Aryl ketones are prepared by Friedel-Crafts acylation of an aromatic ring with an acid chloride in the presence of AICI3 catalyst (Section 16.3). [Pg.700]

I Methyl ketones are prepared by hydration of terminal alkvnes in the presence of Hg2+ catalyst (Section 8.4). [Pg.700]

Adams catalyst (Section 7.7) The Pt02 catalyst used for hydrogenations. [Pg.1234]

Lindlar catalyst (Section 8.5) A hydrogenation catalyst used to convert alkynes to cis alkenes. [Pg.1245]

Ziegler-Natta catalyst (Section 31.2) A catalyst of an alkylaluminum and a litanium compound used for preparing alkene polymers. [Pg.1253]

Catalyst Section. The design criteria for the HYGAS plant methanation section were developed in the late 1960 s (10). At that time, three commercially available nickel methanation catalysts and one ruthenium... [Pg.139]

In this paper we attempt a preliminary investigation on the feasibility of catalytic combustion of CO/ H2 mixtures over mixed oxide catalysts and a comparison in this respect of perovskite and hexaaluminate type catalysts The catalysts have been characterized and tested in the combustion of CO, H2 and CH4 (as reference fuel). The catalytic tests have been carried out on powder materials and the results have been scaled up by means of a mathematical model of the catalyst section of the Hybrid Combustor. [Pg.474]

Campbell S. 2006. Ballard Power System. Development of transition metal/chalcogen based cathode catalysts for PEM fuel cells. DOE Hydrogen Program Review, May 16-19, Washington, DC. Available at http //www.hydrogen.energy.gov/annual review06 fuelcells.html (click on catalysts section). [Pg.368]

Much effort has been expanded in drawing mechanistic inferences from the observation that cofacial bismetalloporphyrins containing a non-redox-active metal ion are fairly selective catalysts (e.g., (DPA)CoM, where M = Lu, Sc, Al, Ag, Pd, 2H, i.e., monometallic porphyrins Fig. 18.15). At least two hypotheses have been proposed (i) polarization of the 0-0 bond in catalytic intermediates by the second ion (on an N-H moiety) acting as a Lewis acid [CoUman et al., 1987, 1994] and (ii) spatial positioning of H+ donors especially favorable for proton transfer to the terminal O atoms of coordinated O2 [Ni et al., 1987 Rosenthal and Nocera, 2007]. To the best of my knowledge, neither hypothesis has yet been convincingly proven nor resulted in improved ORR catalysts. When seeking stereoelectronic rational of the observed av values, it is useful to be mindful that a fair number of simple Co porphyrins are also relatively selective ORR catalysts (Section 18.4.2). [Pg.671]

Figure 1 Fluidized bed reactor set-up, where (1) is the pyrolysis section and (2) the catalyst section. Figure 1 Fluidized bed reactor set-up, where (1) is the pyrolysis section and (2) the catalyst section.
The regeneration of coked catalysts (Section 8.6.5) can be represented by coke burning with air ... [Pg.552]

The catalytic site is chiral and analogous to that proposed for the isospedfic heterogeneous catalysts (Section 3.2), but, unlike the heterogeneous model site, interconversion between enantiomeric complexes is assumed to be possible, after each insertion step, when the metal atom is pentacoordinated.147,149 The analysis of the nonbonded interactions at the catalytic site showed that a si chain favors the formation of the A complex, which in turn favors the re coordination and insertion of the successive monomer unit, thus assuring the syndiospedfic propagation of the chain. [Pg.53]

Asymmetric induction using catalytic amounts of quininium or A-methyl-ephedrinium salts for the Darzen s reaction of aldehydes and ketones with phenacyl halides and chloromethylsulphones produces oxiranes of low optical purity [3, 24, 25]. The chiral catalyst appears to have little more effect than non-chiral catalysts (Section 12.1). Similarly, the catalysed reaction of sodium cyanide with a-bromo-ketones produces epoxynitriles of only low optical purity [3]. The claimed 67% ee for the phenyloxirane derived from the reaction of benzaldehyde with trimethylsul-phonium iodide under basic conditions [26] in the presence of A,A-dimethyle-phedrinium chloride was later retracted [27] the product was contaminated with the 2-methyl-3-phenyloxirane from the degradation of the catalyst. [Pg.539]

GT operation, a lifetime of the catalyst section of >8000 h must be guaranteed, corresponding to yearly replacement during scheduled inspection of hot combustor parts. Catalyst stability against poisoning by air- and fuel-borne contaminants must therefore also be considered. [Pg.366]

Different design concepts have been proposed to match the severe requirements of catalytic combustors. A main classification criterion is based on fuel/air stoichiometry in the catalyst section, which has a dominant effect on the selection of catalytic materials and on the operating characteristics of the combustor. In this section, only configurations based on lean catalytic combustion will be described. The peculiar characteristics of rich catalytic combustion will be described in a separate section. [Pg.366]

The first design concept tried to exploit fully the potential of catalytic combustion by completing the process in a single catalyst section. In such a configuration, a... [Pg.366]

No risk of flash back in the catalyst section thanks to O2 depletion in the fuel-rich stream and absence of fuel in backside cooling air. [Pg.371]

H and 13C NMR have also been widely used to study the binding of alkylammonium cations to crown ethers. The shift in substrate proton resonances can give detailed information of the preferred structure of the complex. This is particularly important in the study of chiral recognition by asymmetric receptors (79CSR85) (Section 5.21.3.2.2) and also the development of bioorganic models and catalysts (Section 5.21.5.1.1). [Pg.739]


See other pages where Catalyst Section is mentioned: [Pg.566]    [Pg.889]    [Pg.285]    [Pg.217]    [Pg.473]    [Pg.479]    [Pg.479]    [Pg.566]    [Pg.889]    [Pg.659]    [Pg.242]    [Pg.425]    [Pg.379]    [Pg.84]    [Pg.167]    [Pg.173]    [Pg.428]    [Pg.478]    [Pg.336]    [Pg.328]    [Pg.367]    [Pg.367]    [Pg.367]    [Pg.369]    [Pg.370]    [Pg.870]    [Pg.121]   


SEARCH



© 2024 chempedia.info