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1.
Studies of the phase composition and catalytic properties of several complex oxide catalysts for oxidative ammonolysis of propane indicate that the active phases of these catalysts are antimonates of the respective metals. Phosphorus and tungsten additives to the catalysts promote the formation of such phase compositions, i.e. the formation of antimonates and the binding of excess antimony oxide.
. , ; , .
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2.
Hydrogenolysis of ethane, n-hexane and cyclohexane has been studied on nickel-kieselguhr catalysts modified by organic and inorganic compounds of tin. Tin additives decrease nickel reactivity with respect to C–C dissociation, which is ascribed to the formation of surface intermetallides on the catalyst.
, - - , . . C–C .
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3.
Platinum dispersity and catalytic activity of L-zeolite-metal catalysts at 773 K have been studied depending on the nature of a modifying agent. The mean size of Pt particles is shown to decrease by a factor of 1.5–2 upon adding Re or W. No relation between Pt dispersity and activity in n-hexane dehydrocyclization has been revealed.
773 L . 1, 5–2 Re W. -.
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4.
Data are reported on variations of the gas phase volume and product accumulation in ethylene oxidation by lithium nitrate in acetic acid solutions, catalyzed by palladium acetate. An assumption is made on the routes of nitrate ion reduction.
, , . -.
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5.
The kinetics of methylcyclopentane hydrogenolysis on a Pt/Al2O3 catalyst (10% Pt) has been studied at 230°C. The selectivity to 2-methyl- and methylpentane formation depends on the partial pressures of the starting reactants (methylcyclopentane and hydrogen); the surface coverage by these reactants must be taken into account in selectivity studies.
Pt/Al2O3 (10% Pt) 230°C. 2-- 3- ( ). .
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6.
Studies of 1-ethyl-(-14C)-indane dehydroisomerization over a Pt/Al2O3 catalyst (AP-64) have revealed that 34.5% or 16.5% of the initial tracer label migrates into the -position of the expanded methylnaphthalene ring when the catalyst is pretreated at 763 K in Ar or H2, respectively. The reaction mechanism is discussed.
1--(14C)- -64. , 763 - 34,5% , —16,5%. .
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7.
The deactivation of a silver catalyst was investigated after six years of industrial production of ethylene oxide. Temperature-programmed reduction was used to characterize the chemical nature of the silver and its reactivity towards oxygen. The fresh and some aged catalysts were examined, also after different thermal treatments.During the industrial run, the surface species were modified and some oxygen diffused into the bulk of the metal. Aging caused permanent changes in the characteristics of the silver, resulting in a different interaction with oxygen. The TPR spectra exhibited a trend along the reactor axis, suggesting a correlation with the degree of deactivation of the catalyst.
Zusammenfassung Die Desaktivierung eines Silberkatalysators wurde nach 6-jährigem Einsatz zur industriellen Produktion untersucht. Temperaturprogrammierte Reduktion wurde angewandt, um die chemische Natur des Silbers und dessen Reaktivität gegenüber Sauerstoff zu charakterisieren. Frische und einige gealterte Katalysatoren wurden nach verschiedenen thermischen Vorbehandlungen untersucht. Die Alterung verursachte bleibende Veränderungen in charakteristischen Eigenschaften des Silbers, was in der unterschiedlichen Wechselwirkung mit Sauerstoff zum Ausdruck kommt. Die TPR-Resultate zeigen einen Trend entlang der Reaktorachse, was auf eine Korrelation mit dem Grad der Desaktivierung des Katalysators hindeutet.

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The experimental contributions by F. Genoni and G. Valassina are gratefully acknowledged.  相似文献   

8.
Reactivity and rate constants in reactions between peroxyl radicals of ethylene glycol diacetate and aromatic nitrons have been investigated.
.
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9.
Pt/sol and Pt/support catalysts with 6–15 Å Pt particles have been established to be low active in the hydrogenation of propargyl alcohol, butyn-l-ol-3 and dimethylethynylcarbinol. The specific catalytic activity significantly rises with increasing dPt above 15 Å and after the thermal treatment of highly dispersed catalysts in a hydrogen flow.
, -30 -- 6–15 Å , -1, -3 . dPt>15 Å .
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10.
    
H2PtCl6 H2PdCl4 -Al2O3 HCl. Pt Pd . -Al2O3.
The adsorption of H2PtCl6 and H2PdCl4 on -Al2O3 from aqueous HCl solutions has been studied. A correlation has been found between the optimum metal concentration and the dispersity of Pt or Pd, and the coverage of chemisorption sites on Al2O3 by ions of the supported compounds.
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