n-Pentane isomerization in a continuous-flow reactor on Pt/Al2O3 catalysts modified by adsorbed bismuth and palladium

Isomerization of n-pentane has been studied in a continuous-flow reactor at atmospheric pressure on Pt/Al₂O₃ catalysts modified by adsorbed bismuth and palladium. Lower activity and higher selectivity have been obtained on a catalyst modified by bismuth. Both activity and selectivity have decreased on a catalyst modified by palladium. After oxygen treatment the Pd–Pt/Al₂O₃ catalyst showed the most pronounced change in catalytic properties and its stability was lower than that of the unmodified Pt/Al₂O₃ catalyst.

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- , Pt/Al₂O₃, . , . , , . Pd–Pt/Al₂O₃ , Pt/Al₂O₃.

     

Effect of iron on the behavior of Fe2O3?MoO3/SiO2 ammoxidation catalysts

Catalytic ammoxidation of propylene was studied using Fe₂O₃–MoO₃/SiO₂ catalysts, which have been prepared following a special method. Interaction of ammonia with the catalysts was studied by means of IR spectroscopy and gravimetrically using a McBain balance. Introduction of iron into MoO₃/SiO₂ catalysts modifies acidic as well as redox properties.

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Fe₂O₃–MoO₃/SiO₂ . . - . MoO₃/SiO₂ , .

     

A new method for preparation of Mo/Al2O3 catalysts for olefin metathesis

A new method of preparation of highly active catalysts for metathesis of -olefins through the anchoring of [Mo₂O₄(C₂O₄)₂(H₂O)₂]^2– anion to the surface of -Al₂O₃ with further thermal activation in H₂ and CO is proposed.

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- [Mo₂O₄(C₂O₄)₂(H₂O₂]^2– -Al₂O₃ H₂ CO.

     

Modification effect of Cu upon Pt In Pt?Cu?Al2O3 catalysts

In Pt–Cu–Al₂O₃ catalysts Cu might display either Electronic Ligand Effect or Ensemble Effect, depending on the preparation method of catalysts. For catalysts with Pt added before Cu, the latter exhibits an Electronic Ligand Effect. However, for catalysts with Cu added before Pt or with co-added Pt and Cu, Cu mainly demonstrates an Ensemble Effect.

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Pt–Cu/Al₂O₃ , . Pt Cu, , .

     

Effect of iron on the properties of supported Rh?Fe catalysts. Rh?Fe/Al2O3 catalysts

The chemical state of metals in Rh–Fe/Al₂O₃ catalysts has been examined. Iron forms clusters with rhodium, whose size and composition depend on the metal ratio in the catalyst. The structure of active sites affects the amount and adsorption heat of hydrogen and carbon monoxide and the mechanism of their interaction.

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Rh–Fe/Al₂O₃ , , . , .

     

Coke deposits on Pt/Al2O3 catalysts of varying dispersities

Coke deposition during cyclopentane reaction was investigated on Pt/Al₂O₃ catalysts of varying dispersity. For all working pressures the higher the metallic accessibility, the higher the amount of coke deposited on the catalyst. Nevertheless, coke deposited on the less dispersed catalysts is more toxic for the metallic function. An increasing metal accessibility improves the graphitization of coke on the support and so, prevent the deactivation of the metal of a bifunctional catalyst.

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Pt/Al₂O₃ . , , , . , , , . , .

     

Hydrogenation of xylenes over supported Pt catalysts. Influence of different variables on their catalytic activity

In this work we studied and compared the catalytic activity of various supported Pt systems on the gas-phase hydrogenation of o-, m- and p-xylene. We analyzed the influence of different catalyst preparation variables (solvent, precursor, salt, support and catalyst reduction temperature used) on the catalytic activity and selectivity towards the corresponding cis-and trans-dimethylcyclohexanes.

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- o-, m- -. (, , ) - -.

     

Potentiometric titration of sorbed hydrogen on palladium carrier catalysts

A method of determination of adsorbed and absorbed hydrogen on palladium catalysts with carbon carriers is suggested and verified. The method allows H_ad and H_ab to be determined with an accuracy of about 10% using catalysts containing at least 5% Pd.

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- . . . 10% , , - , 5% Pd.

     

On the deactivation of Fe2O3?MoO3/SiO2 catalysts in the oxidation of methanol to formaldehyde

The deactivation behavior of Fe₂O₃–MoO₃/SiO₂ catalysts with different Fe₂O₃+MoO₃ content in the oxidation of methanol to formaldehyde is investigated. A simplified reaction-deactivation kinetic model is presented and used to compare and discuss the different behaviors.

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Fe₂O₃–MoO₃/SiO₂ Fe₂O₃+MoO₃ . : -.

     

Catalytic reduction of NO with H2 and CO over cobalt-alumina and chromium-alumina catalysts

The catalytic reduction of NO with H₂ and CO has been studied over Co/Al and Cr/Al catalysts prepared by coprecipitation. The data show a much larger difference in the activities of Cr/Al and Co/Al when reducing NO with CO than in the case of H₂. In both cases Cr/Al appears to be much more selective to N₂ formation than Co/Al. The dependence of the selectivity on temperature is different for the two reductants on the Co/Al catalyst. The results suggest that most of the N₂O desorbs from the surface of the Co/Al catalyst before N₂ is formed.

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NO H₂ CO Co/Al Cr/Al, . NO CO Cr/Al Co/Al, . Cr/Al N₂, Co/Al. , N₂O Co/Al N₂.

     

Mechanism of methane photooxidation on V/SiO2 catalyst

CH₄ photooxidation on V/SiO₂ catalyst in the presence of gaseous oxygen has been studied by the mass-spectometric method. It has been established that CO₂ forms due to the interaction of CH₄ with surface oxygen anions bonded to vanadium ions. Photodecomposition of V⁴⁺O ₂ ^– species formed in O₂ adsorption on reduced vanadium ions leads to the reoxidation of the latter.

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- CH₄ V/SiO₂ . , CO₂ CH₄ , . V⁴⁺O ₂ ^– O₂ , .

     

Coked reforming catalysts: Self-regeneration by residual hydrogen

The deactivation and subsequent self-regeneration of several Pt/–Al₂O₃/honeycomb reforming catalysts have been investigated. Catalytic activity in the dehydrogenation of methylcyclohexane (MCH), taken as reaction model, has been evaluated at 400 °C in a continuous flow microreactor. The determining role of surface chlorine during the H₂ self-regeneration of catalysts is discussed. A catalyst with ca. 0.5% C1 shows complete self-regeneration. A regeneration mechanism, involving the spillover of residual hydrogen, is proposed.

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Pt/–Al₂O₃ . , , 400°C . . . 0.5% Cl . , .

     

Quantitative thermal analysis,I Mathematical problems of quantitative differential thermal analysis

A highly simplified method for calculating heat of phase transitions from DTA data is presented. Two DTA curves are needed to calculate the heat of transition and the specific heat of the sample: one is for the original sample and one is for a sample prepared by mixing the original sample with some unreactive diluent the specific heat of which is known. The data of the DTA curves used in the calculations are the peak area, the rate of heating and the deviation of the DTA curve from the base line.

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Zusammenfassung Eine einfache Methode zur Errechnung der Werte der Phasenübergangswärme aus den DTA Daten wird besprochen. Die Kenntnis der spezifischen Wärme der betreffenden Substanz und zwei Thermogramme sind hierzu nötig, jenes der Originalprobe und jenes einer Mischung der zu prüfenden Substanz mit einem indifferenten Stoff von bekannter spezifischer Wärme. Die notwendigen DTA Daten sind die Spitzenflächen, die Erhitzungsgeschwindigkeit und die Abweichung der DTA Kurve von der Nullinie.

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Résumé On décrit une méthode simple pour caIculer les chaleurs des transitions de phase à l'aide des données d'analyse thermique différentielle. Il est nécessaire de connaître la chaleur spécifique et les thermogrammes de l'échantillon pur et en mélange avec une substance indifférente, de chaleur spécific connue. Pour les calculs, on se sert des données suivantes: surface des pics d'A. T. D., vitesse de chauffage et déviation de la courbe d'A. T. D. par rapport à la ligne de base.

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(). () , . : , () .

     

Low-pressure decomposition of ammonia on rhodium

Kinetics of ammonia decomposition and adsorption of reactants on a polycrystalline rhodium wire have been studied by thermal desorption and mass-spectrometric methods. Qualitive discussion of the mechanism of ammonia interaction with rhodium is presented.

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- . .

     

Formation of O2? ion-radicals on reduced anatase. Influence of adsorbed CO on the stabilization of O2?

ESR studies of O₂ adsorption on reduced anatase have been performed. The amount of O ₂ ^– species is determined by adsorbed surface oxygen and their parameters are changed by CO adsorption.

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O₂ . , O ₂ ^– , CO.

     

Thermal decomposition of azoisopropane

The gas phase pyrolysis of azoisopropane has been investigated in a static system in the temperature range 494–546 K. On the basis of gas chromatographic analysis a mechanism is proposed to account for the experimental results.The rate constant of azoisopropane decomposition can be given by the expression {ie383-1}

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494–546^o . - . , : {ie383-2}

     

Effect of rhenium and chlorine on catalytic activity of L-zeolite Pt-catalysts

Interaction of components of L-zeolite Pt-Re catalyst and their effect on the dehydrocyclization of n-hexane has been examined.

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- L n -.

     

Temperature programmed reduction and oxidation of Ir/Al2O3 catalysts

3 % Ir/Al₂O₃ catalysts have been studied by means of temperature programmed reduction and oxidation. With growing degree of metal oxidation (higher T_ox) reducibility of the catalysts at low temperatures decreases.

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3% Ir/Al₂O₃ . ( ) .

     

Preparation of a Ru/Al2O3 catalyst from Ru3(CO)12 infrared and XPS study

A supported ruthenium catalyst on alumina prepared from Ru₃(CO)₁₂ has been studied by infrared and X-ray photoelectron spectroscopy (XPS). The triatomic cluster is retained on the support but breaks down at 150°C. Complete elimination of the carbonyl groups requires heating at 350°C under vacuum. XPS studies show that the decomposed catalyst does not change on further reduction in H₂ at 400°C. The ruthenium atoms remain trapped within the pores of the support.

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Al₂O₃, Ru₃(CO)₁₂, (XPS). , 150°C . 350°C . XPS , H₂ 400°C . .

     

Magnetic susceptibility measurement with a Dupont's thermogravimetric analyser

The adaptation of a Du Pont Thermogravimetric Analyser for the measurement of magnetic susceptibility as a function of temperature in the range – 80 °C to 300 °C is described.

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Zusammenfassung Die Adaptation des Du Pont's Thermogravimetric Analyzer zur Messung der magnetischen Suszeptibilität in Abhängigkeit von der Temperatur im Bereich von – 80° bis 300 °C wird mitgeteilt.

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–80°–300 °.