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Pd/Al2O3 catalysts

This work has recently been extended, again with a single Pd/Al2O3 catalyst pellet 69). The image time was reduced to 34 s by introduction of manganese ions into the... [Pg.35]

Recently, Sederman and co-workers (755) used the DEPT MRI pulse sequence described in Section V.A.2 to investigate 1-octene hydrogenation occurring over a l-wt.% Pd/Al2O3 catalyst in a trickle-bed reactor. The reactor was of inner diameter... [Pg.69]

In the case of Pd/Al2O3 catalysts the morphology of the metal particles is also important because it determines the hydrogenation and isomerization selectivity. On flat metal surfaces isomerization is prefened whereas rough surfaces are more active... [Pg.1014]

Aromatization of the Methylcyclohexane Fraction of Krasnodar Naphtha on a PD-AL2O3 Catalyst 12)... [Pg.797]

CHSV= 10 Ncm g h heating/cooling rate, 15 C min catalyst, 10%Pd/La2O3(5%)-Al2O3. [Pg.377]

The CO + NO reaction on various kinds of Pd catalysts was investigated by Rainer et al (112). Kinetics data for Pd/A Os and planar model Pcl/Al2O3/Ta(110) catalysts were compared with those for CO ) NO on Pd(lll), (100), and (110) surfaces. Figure 20 is a comparison of the Arrhenius plots measured at partial pressures of about 1 mbar in each reactant tor the model catalysts and at a CO pressure of 5.9 and a NO pressure of 6.8 mbar (in a helium carrier) for the Pd/A Os powder catalyst. [Pg.305]


See other pages where Pd/Al2O3 catalysts is mentioned: [Pg.255]    [Pg.270]    [Pg.994]    [Pg.196]    [Pg.255]    [Pg.270]    [Pg.994]    [Pg.196]    [Pg.257]    [Pg.275]    [Pg.27]    [Pg.32]    [Pg.34]    [Pg.66]    [Pg.466]    [Pg.184]    [Pg.240]    [Pg.189]    [Pg.141]    [Pg.51]    [Pg.268]    [Pg.197]    [Pg.65]    [Pg.204]    [Pg.437]    [Pg.46]   


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