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On palladium

Szanyi J, Kuhn W K and Goodman D W 1994 CO oxidation on palladium 2. A combined kinetic-infrared reflection absorption spectroscopic study of Pd(IOO) J. Phys. Chem. 98 2978... [Pg.955]

Figure Bl.26.1. Sorption isothemi for chemisorption of hydrogen on palladium film at 273 K (Stephens S J 19597. Phys. Chem.. 63 188-94). Figure Bl.26.1. Sorption isothemi for chemisorption of hydrogen on palladium film at 273 K (Stephens S J 19597. Phys. Chem.. 63 188-94).
Conrad FI, ErtI G and Latta E E 1974 Adsorption of hydrogen on palladium single crystal surfaces Surf. Sc/41 435-46... [Pg.1898]

CO Oxidation Catalyzed by Palladium. One of the best understood catalytic reactions occurring on a metal surface is the oxidation of carbon monoxide on palladium ... [Pg.176]

A -Pyrazolines are obtained by the reduction of pyrazoles with sodium and alcohol, by catalytic hydrogenation on palladium or by electrochemical means (B-76MI40402). In some cases the reduction proceeds further yielding pyrazolidines and open-chain compounds. [Pg.243]

Partial hydrogenation of the quaternary pyridinium salts in the presence of triethylamine on palladium in methanol has been used for the synthesis of a large number of alkaloids. The tetrahydropyridine derivatives thus formed undergo various cyclization reactions in acidic media (89). [Pg.303]

In a recent variation of this synthesis of the tetrahydro-j8-carboline system, hexahydro derivatives (65) of the salt 55 were cyclized to fully aromatic j8-carbohne derivatives (66a and 66b) on palladium dehydrogenation, presumably by way of an enamine intermediate. ... [Pg.98]

A variety of catalysts including copper, nickel, cobalt, and the platinum metals group have been used successfully in carbonyl reduction. Palladium, an excellent catalyst for hydrogenation of aromatic carbonyls is relatively ineffective for aliphatic carbonyls this latter group has a low strength of adsorption on palladium relative to other metals (72,91). Nonetheless, palladium can be used very well with aliphatic carbonyls with sufficient patience, as illustrated by the difficult-to-reduce vinylogous amide I to 2 (9). [Pg.66]

Ionic liquids have already been demonstrated to be effective membrane materials for gas separation when supported within a porous polymer support. However, supported ionic liquid membranes offer another versatile approach by which to perform two-phase catalysis. This technology combines some of the advantages of the ionic liquid as a catalyst solvent with the ruggedness of the ionic liquid-polymer gels. Transition metal complexes based on palladium or rhodium have been incorporated into gas-permeable polymer gels composed of [BMIM][PFg] and poly(vinyli-dene fluoride)-hexafluoropropylene copolymer and have been used to investigate the hydrogenation of propene [21]. [Pg.266]

In the presence of catalytic amounts of Pd(0), silicon-substituted vinyloxiranes can rearrange into the corresponding ot-silyl- 3,y-unsaturated aldehydes (Scheme 9.34) [151]. Treatment of 80 with Pd(OAc)2 and P(OPh)3 results in the formation of 7t-allylpalladium complex 81. Bond rotation to give 82, followed by migration of the silyl moiety, affords aldehyde 83, which is trapped in situ to provide the Felkin-Anh product 84. The reaction proceeds with retention of configuration and the ee of the starting material is retained in the product. The size of the silicon substituents is critical for the outcome of the reaction, as is the choice of ligands on palladium. [Pg.340]

The situation has now changed and currently an area of considerable research interest is in heterogenizing homogeneous catalysts. One such instance is to be found in the ethylene based manufacture of vinyl acetate (11). A homogeneous catalytic process based on palladium and copper salts was first devised, but corrosion problems were made much less serious in a heterogeneous system based on the same chemical principles. [Pg.231]

Catalytic Reactivity of Hydrogen on Palladium and Nickel Hydride Phases... [Pg.245]

Fig. 5. Arrhenius plots for para-hydrogen conversion on palladium wire catalysts. O, Phj = 1-2 mm Hg A, Ph. = 6.1 mm Hg , after the exposure of a wire to atomic hydrogen produced in rf discharges. Compiled after Couper and Eley (29). Fig. 5. Arrhenius plots for para-hydrogen conversion on palladium wire catalysts. O, Phj = 1-2 mm Hg A, Ph. = 6.1 mm Hg , after the exposure of a wire to atomic hydrogen produced in rf discharges. Compiled after Couper and Eley (29).
Table III lists the kinetic equations for the reactions studied by Scholten and Konvalinka when the hydride was the catalyst involved. Uncracked samples of the hydride exhibit far greater activation energy than does the a-phase, i.e. 12.5 kcal/mole, in good accord with 11 kcal/mole obtained by Couper and Eley for a wire preexposed to the atomic hydrogen. The exponent of the power at p amounts to 0.64 no matter which one of the reactions was studied and under what conditions of p and T the kinetic experiments were carried out. According to Scholten and Konvalinka this is a unique quantitative factor common to the reactions studied on palladium hydride as catalyst. It constitutes a point of departure for the authors proposal for the mechanism of the para-hydrogen conversion reaction catalyzed by the hydride phase. Table III lists the kinetic equations for the reactions studied by Scholten and Konvalinka when the hydride was the catalyst involved. Uncracked samples of the hydride exhibit far greater activation energy than does the a-phase, i.e. 12.5 kcal/mole, in good accord with 11 kcal/mole obtained by Couper and Eley for a wire preexposed to the atomic hydrogen. The exponent of the power at p amounts to 0.64 no matter which one of the reactions was studied and under what conditions of p and T the kinetic experiments were carried out. According to Scholten and Konvalinka this is a unique quantitative factor common to the reactions studied on palladium hydride as catalyst. It constitutes a point of departure for the authors proposal for the mechanism of the para-hydrogen conversion reaction catalyzed by the hydride phase.
Fig. 8. Arrhenius plots for the formic acid decomposition on palladium foil (1) and small pieces of this foil (2) at a higher temperature range, when hydrogen evolving as a product of the reaction was absorbed by Pd and transformed into the /3-Pd-H hydride phase. At the lower temperature range the reaction proceeds on the a-Pd-H phase, with a higher activation energy when the foil was hydrogen pretreated (2a), and a lower activation energy for a degassed Pd foil (3a). After Brill and Watson (57). Fig. 8. Arrhenius plots for the formic acid decomposition on palladium foil (1) and small pieces of this foil (2) at a higher temperature range, when hydrogen evolving as a product of the reaction was absorbed by Pd and transformed into the /3-Pd-H hydride phase. At the lower temperature range the reaction proceeds on the a-Pd-H phase, with a higher activation energy when the foil was hydrogen pretreated (2a), and a lower activation energy for a degassed Pd foil (3a). After Brill and Watson (57).
The catalytic system studied by Rennard and Kokes was in fact very complex. It can be expected that the satisfactory prolongation of the reaction should, however, result in a deviation from the formulated kinetics. Unfortunately no investigation comparable to that of Scholten and Kon-valinka has been done in the case of olefin hydrogenation. Such a study of the catalytic activity of the pure /3-phase of palladium hydride in comparison with the a- or (a + /3)-phases would supplement our knowledge concerning catalytic hydrogenation on palladium. [Pg.265]

E.M. Stuve, and R.J. Madix, Bonding and dehydrogenation of ethylene on palladium metal. Vibrational spectra and temperature-programmed reaction studies on Pd(100), J. Phys. Chem. 89, 105-112 (1985). [Pg.88]

A large amount of the work on palladium isocyanide complexes has been mentioned earlier, in discussions on insertion reactions 30,74,108,169,170) and on addition reactions of coordinated isocyanides 25, 33, 34, 49) the reactions of [Pd(CNBu )2] with oxygen 107) and with various olefins 29, 110) were noted. [Pg.74]

Carbonylation of methanol to acetic acid is fully discussed in Chapter 9. Another carbonylation process using a phosphine ligand to control the course of the reaction is a highly atom efficient route to the widely used monomer methyl methacrylate (Scheme 4.19). In this process the catalyst is based on palladium acetate and the phosphine ligand, bisphenyl(6-methyl-2-pyridyl) phosphine. This catalyst is remarkably (>99.5%) selective for the 2-carbonylation of propyne under the relatively mild conditions of <100 °C and 60 bar pressure. [Pg.112]

The free HCl and Cl generated in the catalytic cycle produce environmentally harmful chlorinated by-products to the extent that more than 3 kg of HCl need to be added to the reactor per tonne of acetaldehyde produced to keep the catalytic cycle going. Modified catalysts such as ones based on palladium/ phosphomolybdovanadates have been suggested as a way of reducing byproduct formation to less than 1% of that of the conventional Wacker process. These catalysts have yet to make an impact on commercial acetic production, however. [Pg.263]

Reinhoudt and coworkers studied the synthesis of hyper-branched polymers composed of organopalladium complexes with an SCS pincer ligand [11]. Removal of acetonitrile ligands on palladium led to the self-assembly of dinu-clear palladium complex (9) to give hyper-branched polymer (10), which was... [Pg.44]

Figure 10.6. Approximate energy diagram of CO oxidation on palladium. Note the largest energy barrier is the CO + O recombination. [Adapted from T. Engel and G. Ertl.J, Chem. Rhys. 69 (1978) 1267.]... Figure 10.6. Approximate energy diagram of CO oxidation on palladium. Note the largest energy barrier is the CO + O recombination. [Adapted from T. Engel and G. Ertl.J, Chem. Rhys. 69 (1978) 1267.]...
Oxygen Interactions and Reactions on Palladium(lOO) Coadsorption Studies with C2H4, H2O, and CH3OH... [Pg.165]


See other pages where On palladium is mentioned: [Pg.11]    [Pg.358]    [Pg.32]    [Pg.113]    [Pg.136]    [Pg.12]    [Pg.334]    [Pg.12]    [Pg.30]    [Pg.72]    [Pg.91]    [Pg.257]    [Pg.259]    [Pg.261]    [Pg.263]    [Pg.266]    [Pg.266]    [Pg.267]    [Pg.270]    [Pg.442]    [Pg.186]    [Pg.330]    [Pg.433]    [Pg.556]    [Pg.157]    [Pg.75]    [Pg.138]   
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20% Palladium hydroxide on carbon

Adsorption of CO on Palladium

Adsorption on palladium

Carbon monoxide on palladium

Catalytic Synthesis of ()-Ethyl 3-(4-methoxyphenyl)acrylate Using Palladium Nanoparticles Supported on Agarose Hydrogel

Common Additives in Palladium-Catalyzed Cross-Coupling Reactions - Effect on (Pre)catalyst and Active Catalytic Species

Formic acid oxidation on Palladium

Hydrogen, on palladium

Hydrogenation Palladium on Carbon

Interstitial Hydrides, Focussing on Palladium Hydride

Metal catalysts palladium-on-alumina

Metal catalysts palladium-on-carbon

Oxidation of CO on Palladium

Oxidation of Methane on Supported Palladium Under Lean Conditions Kinetics, Structure and Properties

P. Beletskaya and Andrei V. Cheprakov 2 Palladium Catalysts Immobilized on Polymeric Supports

Palladium chloride on carbon

Palladium complexes effect of ligand size on coordination number

Palladium hydroxide on barium sulfate

Palladium hydroxide on calcium carbonate

Palladium hydroxide on charcoal

Palladium on activated carbon

Palladium on active charcoal

Palladium on alumina

Palladium on barium

Palladium on barium sulfate

Palladium on calcium carbonate

Palladium on charcoal catalyst

Palladium on graphite

Palladium on porous glass

Palladium on silica

Palladium oxide on charcoal

Palladium, 10% on carbon

Palladium, on barium carbonate

Palladium, on barium carbonate recovery from spent catalyst

Palladium, on carbon, catalyst

Palladium-on-charcoal

Palladium-on-charcoal catalyst, biphenyl

Sorption of Palladium Ion on Montmorillonite

Stoichiometric Studies on the Palladium 1,2-Migration

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