DSC characterization of ZSM-5/MgO/Al2O3 catalysts

The physico-chemical characterization of magnesium-modified ZSM-5 zeolite catalysts has been performed by differential scanning calorimetry. Evidence has been found of the formation of magnesium oxide and the magnesium spinel phase in alumina-bonded ZSM-5 catalysts. DSC proved a suitable technique for characterization of these systems.

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Zusammenfassung Mg-modifizierte ZSM-5-Zeolithkatalysatoren wurden durch DSC charakterisiert. Es wurden Beweise für die Bildung von Magnesiumoxid und Magnesiumspinell in ZSM-5/Aluminiumoxid-Katalysatoren gefunden. DSC hat sich zur Characterisierung dieser Systeme als geeignet erwiesen.

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- 3CM-5, . - - . .

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This work was carried out within the Progetto finalizzato Energetica 2 of the National Research Council of Italy.     

Methyl radical addition to methyl ethyl ketone

From relative rates of acetone formation in the azomethane sensitized decomposition of methyl ethyl ketone at 290 °C, log₁₀(k/cm³mol^–1s^–1)=5.3±0.4 for the methyl radical addition to methyl ethyl ketone has been determined.

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290°C, , . lg₁₀(^{3 –1–1})=5,3±0,4.

     

X-ray spectral investigation by synchrotron radiation of supported Re/SiO2 and (Re+Pt)/SiO2 catalysts prepared via triethoxyrhenium

Using synchrotron radiation L_III absorption spectra of rhenium in Re/SiO₂ and (Re+Pt)/SiO₂ catalysts prepared via triethoxyrhenium have been studied. The conclusion has been drawn that reduced catalysts contain lowvalent rhenium ions and their composition is more uniform than that of the previously examined catalysts Re/Al₂O₃ and (Re+Pt)/Al₂O₃ prepared by a conventional impregnation technique.

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L_III- Re/SiO₂ (Re+Pt)/SiO₂, . , , Re/Al₂O₃ (Re+Pt)/Al₂O₃, .

     

X-ray and thermal studies on uranyl acetates of zinc,magnesium and nickel

Thermal decomposition of metal uranyl acetates is one of the best ways of preparation of uranates in crystalline form at low temperatures. Acetates of the type M(UO₂)₂(OAc)₆·7H₂O (M=Zn(II), Mg(II) and Ni(II) were prepared and characterised. Their X-ray powder diffraction analysis showed that they all belong to the orthorhombic crystal class.The thermal decomposition of acetates in air goes through the reduction of uranium(VI) to uranium(IV) during acetate decomposition followed by reoxidation by oxygen. Zinc uranylacetate gave on thermal decomposition ZnU₃O₁₀, the nickel salt gave NiU₃O₁₀ and the magnesium salt gave a mixture of MgUO₄ and MgU₃O₁₀. The thermal decomposition of acetates in helium led to reduction of uranium(VI) to uranium(IV) with the formation of UO₂. No lower valent uranates could be identified.

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Zusammenfassung Thermische Zersetzung von Metalluranylazetaten ist eine der geeignetsten Methoden zur Darstellung kristalliner Uranate bei niedrigen Temperaturen. Azetate des Types M(UO₂)₂(OAc)₆·7H₂O mitM=Zn(II), Mg(II) und Ni(II) wurden hergestellt und beschrieben. Eine Pulverdiffraktionsanalyse zeigte, daß alle der orthorhombischen Kristallklasse angehören. Der thermische Zerfall der Azetate in Luft vollzieht sich während des Azetatzerfalls über die Reduktion von Uran(VI) zu Uran(IV) bis zu einer anschließenden Reoxydation durch Sauerstoff. Bei der thermischen Zersetzung liefert Zinkuranylazetat ZnU₃O₁₀, das Nickelsalz liefert NiU₃O₁₀ und das Magnesiumsalz ein Gemisch aus MgUO₄ und MgU₃O₁₀. Der thermische Zerfall der Azetate in Helium führt zur Reduktion von Uran(VI) zu Uran(IV) unter Bildung von UO₃. Uranate mit niedrigerer Wertigkeit konnten nicht identifiziert werden.

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. M(UO₂)₂(OAc)₆ · 7H₂O, M = , . , . , . ZnU₃O₁₀, — NiU₃O₁₀, MgUO₄ MgU₃O₁₀. . .

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The authors thank Dr. D. D. Sood, Head, Fuel Chemistry Division, for his encouragement during the course of this work.     

Tracer study of complete oxidation complexes in the oxidative dehydrogenation of butylene

A tracer technique using divinyl-¹⁴C was used to determine the butylene and divinyl contents in the surface complexes of complete oxidation during the oxidative dehydrogenation of butylenes over Bi–Mo, Fe–Sb and Fe₂O₃ catalysts. The rate of decomposition of the surface complexes was found to be independent of their relative butylene and divinyl content.

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–C¹⁴ Bi–Mo, Fe–Sb Fe₂O₃ ., .

     

Collisional energy transfer in the decomposition of 2-methyloxetane and 3-methyloxetane, II. Gas/wall collisions

The variable encounter method has been applied for the study of gas/wall vibrational energy transfer in the thermal decomposition of 2-methyloxetane and 3-methyloxetane. The average probability of reaction per collision was deduced from the data and was compared with stochastic calculations based on gaussian and exponential energy transfer probability models. The gaussian model fits the experimental data best. Using this model, the average down step energies were 2600 and 2690 cm^–1 for 2-methyloxetane and 3-methyloxetane, respectively, at 750 K, and they decreased with increasing temperature.

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/ 2- 3-. , . . , 2600 2690 ^–1 750 K 2- 3-, . .

     

Transient phenomena in o-xylene oxidation in a fluidized bed reactor

The effect of stirring a vanadium-titanium-tellurium catalyst on the yield of the selective oxidation products for oxidation of o-xylene in fluidized bed reactors has been studied. It is shown that the stirring of catalyst pellets increases the yield of phthalic anhydride.

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-- - . , .

     

Kinetics of partly diffusion controlled reactions. X. Use of a high pressure cell in fluorescence quenching experiments

The increase of the pressure over a liquid results in an increase of its viscosity, which makes possible the study of the mechanism of diffusion-controlled, or not, fluorescence quenching processes. This technique has been applied to the quenching of the fluorescence of two substituted anthraquinones by N,N-dimethyl-p-toluidine in acetonitrile solution.

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. - . N,N--- .

     

Kinetics of the oxidation of some polycyclic aromatic hydrocarbons by lead tetraacetate in aqueous acetic acid and perchloric acid medium

The state of metal cations in CuCr₂O₄/-Al₂O₃ catalysts under its operation in catalytic heat generators has been examined. IR spectra of adsorbed CO indicate copper ion reduction in the catalyst to Cu⁺, whose surface concentration was determined. Diffuse reflectance spectra have revealed that the initial catalyst contains Cr(VI), disappearing after reaction.

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CuCr₂O₄/-Al₂O₃ (). - CO , Cu⁺. Cu⁺. , Cr(VI), .

     

Hydroisomerization and hydrocracking of 2-methylhexane on PtUSHY catalysis. Effect of platinum content

The stability and the ratio of the isomerization to cracking rates increase very much with platinum introduction and the isomer and cracking product distributions are significantly modified. This can be explained by the change from an acid to a bifunctional mechanism. However, platinum has practically no effect on the rate of 2-methylhexane transformation. This could be attributed to the fact that neither on USHY nor on PtUSHY is the formation of the carbenium ions with a 2-methylhexane skeleton the limiting step.

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, . . , 2-. , 2- USHY, PtUSHY.

     

Calculation of the mass transfer coefficient with a chemical reaction in a gas-liquid system

A solution of the problem of mass transfer in a turbulent boundary layer has been obtained with a first-order chemical reaction occurring in the liquid phase. The dependence of the enhancement factor for absorption and of the mass transfer coefficient on the model parameters can be used for building up a hierarchic model of the gas-liquid reactor.

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. .

     

Theory of differential thermal analysis taking into account heat exchange between the specimen and reference cells

A basic formula of differential thermal analysis is evolved for the case when the heat transfer coefficient between the specimen cell and the reference cell is not zero. The more general formula obtained differs from the classical formula by including the parameters of the reference cell and the heat transfer coefficient between the cells. It indicates that utilization of the classical formula is not correct if heat exchange occurs between the cells. To utilize the generalized formula, additional measurements of the temperature changes of the reference material are required. However, if the time constants of the two cells are identical, the formula can be changed to assume the form of the classical formula for DTA if a correction factor is introduced which takes into account the effect of heat exchange between the cells.

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Zusammenfassung Für den Fall, dass der Übertragungskoeffizient zwischen der Proben- und der Referenzzelle nicht Zero ist, wurde eine Grundformel der Differentialthermoanalyse entwickelt. Die entstandene Formel, die vielmehr allgemein ist, weicht von der klassischen dadurch ab, dass sie auch die Parameter der Referenzzelle, und den Wärmeübertragungskoeffizient zwischen den Zellen enthält. Sie deutet darauf hin, dass die Anwendung der klassischen Formel in dem Fall nicht einwandfrei ist, wenn ein Wärmeaustausch zwischen den Zellen zustande kommt. Zur Anwendung der verallgemeinerten Formel sind weitere Messungen des Temperaturaustausches vom Referenzmaterial erforderlich. Sind aber die Zeitkonstanten der zwei Zellen identisch, kann die Formel so geändert werden, dass sie die Gestalt der klassischen DTA-Formel annimt, wenn ein, mit der Wirkung des Wärmeaustausches zwischen den Zellen rechnender Korrektionsfaktor eingeführt wird.

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, . , , . . , , , , .

     

Displacement of hydrogen from rhodium surface by carbon monoxide under conditions of pulsed-gas chromatography

Interaction of carbon monoxide with hydrogen on the surface of rhodium catalysts has been investigated under conditions of pulsed-gas chromatography within the temperature range of –80 to 500 °C. At temperatures up to about 180 °C adsorbed hydrogen was found to be displaced to the gaseous phase as a result of carbon oxide adsorption. At higher temperatures conversion of carbon monoxide and hydrogen to methane takes place.

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–80 500 °C. 180 °C . .

     

Combination and disproportionation of methyl and 2-propyl radicals with 1,1,2-trimethylallyl radicals

The combinations and disproportionations of the CH₃ and 2-propyl (iP) radicals with the 1,1,2-trimethylallyl (TMA) radical have been studied in the gas phase in the temperature interval of 389–451 K and 490–540 K, respectively. For the ratios of the terminal (t) and non-terminal (n) combinations of the CH₃ and iP radicals with the TMA radical, values of 1.9±0.1 and 2.84±±0.10 were obtained, respectively. The ratios of the tt and tn and nn to tn combinations of the TMA radical were 1.59 and 0.46, respectively. The disproportionation-combination rations were (CH₃ , TMA)=0.022±±0.012 and (iP, TMA)=0.026±0.011.

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CH ₃ 2- (iP) 1,1,2- (TMA) : 389–451 K 490–540 K. (t) (n) TMA 1,9±0,1 2,84±0,10, . tt tn nn tn TMA 1,59 0,46, . (CH ₃ , TMA)=0,022±0,012 (iP, TMA)=0,026±0,011.

     

Study of hydroisomerization of n-hexane on natural mordenite catalyst

A mordenite-containing rock sample from the Tokaj Mountains (Hungary) and its various forms modified by chemical treatment have been tested for catalytic properties during isomerization of n-hexane. Addition of Pt to the catalyst leads to a sharp decrease in the rate of cracking and in the rate of deactivation and this results in a catalyst of high selectivity for hexane isomers.

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(), , , , -. Pt , .

     

Zersetzungsmechanismus von Mg(OH)2 und Mg(OD)2

Zusammenfassung Man untersucht, unter welchen Bedingungen das Proton einer ionischen OH^–-Gruppe die Elektronenwolke des O^2–Ions verlassen kann, um mit einer benachbarten OH^–-Gruppe ein H₂O-Molekül zu bilden. Voraussetzung zum Tunneln ist in der benachbarten OH^–-Gruppe ein freies Akzeptorniveau auf gleicher Höhe. Wenn die beiden betrachteten OH^–-Gruppen kristallographisch äquivalent sind, ist die letztgenannte Bedingung nicht erfüllt, da das Akzeptorniveau höher liegt als das Donatorniveau. Durch Koplung mit den gegenphasigen OH-Knickschwingungen wird eine Verbreiterung der Niveaus und schließlich — ab einer kritischen Amplitude — eine Überlappung herbeigeführt, die das Tunneln ermöglicht. Die Protonenumlagerung beginnt an der Oberfläche, weil an einer freien Oberfläche die Amplituden der wirksamen OH-Knickschwingungen bei gleicher Temperatur größer sind als im Innern des Kristalls.

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The conditions have been studied under which the proton of an ionic OH^– group can leave the electron cloud of the O^2– ion to form a H₂O molecule with a neighbouring OH^– group. The condition of tunnelling is the presence of a free acceptor level of similar height in the neighbouring OH^– group. If the two OH^– groups are equivalent crystallographically, this condition is not fulfilled since the acceptor level lies higher than the donor level. Coupling with the opposite-phase OH bending vibrations leads to a broadening of the levels and finally to an overlap, which renders the tunnelling possible. The proton transfer starts at the surface as at any given temperature the amplitude of the effective OH bending vibrations is larger at the surface than inside the crystal.

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Résumé On recherche les conditions dans lesquelles le proton d'un groupe ionique OH^–peut quitter le nuage électronique de l'ion O^2– pour former une molécule d'eau avec un groupe OH^– voisin. La condition de l'effet tunnel est que le groupe OH^– voisin possède un même niveau libre accepteur. Cette condition n'est pas réalisée dans le cas de deux groupes OH^–voisins cristallographiquement équivalents puisque le niveau accepteur est plus haut que le niveau donneur. Le couplage des vibrations de déformation en opposition de phase des OH provoque un élargissement des niveaux et finalement — à partir d'une amplitude critique — un recouvrement qui permet l'effet tunnel. La transposition protonique commence en surface puisque pour une surface libre les amplitudes des vibrations de déformation actives des OH sont plus grandes qu'à l'intérieur du cristal.

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, , -, ²- [₂] -. -. , , , . -, , , . , , .

     

Reduction of benzylideneaniline over supported Pd catalysts

In this work we have carried out a study on the liquid phase hydrogenation of benzylideneaniline, using dihydrogen over various supported Pd catalysts. Benzyl-ideneaniline reduction can be classified as insensitive to the catalyst structure. On the other hand, no compensating effect has been observed in performing the reaction over different supported Pd catalysts.

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Pd , . . Pd , .

     

Temperature-programmed reduction. Metal-support interaction on supported monometallic Ru and Cu Catalysts

Ru and Cu samples supported on SiO₂, Al₂O₃ and MgO were studied by the temperature-programmed reduction (TPR) technique. Experiments were carried out both on unreduced impregnated salts and after oxidation of already reduced samples.The TPR profiles were found to be strongly dependent on the support used, indicating different degrees of interaction between the metal and the support, which can be ranked as MgOAl₂O₃>SiO₂. It is suggested that the interaction occurs through the formation of surface complexes difficult to reduce. The decrease in hydrogen consumption observed on the Ru samples with the number of TPR cycles is attributed to the difficulty in oxidizing large Ru particles.

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Zusammenfassung Auf SiO₂, Al₂O₃ und MgO aufgebrachte Ru- und Cu-Proben wurden mittels temperaturprogrammierter Reduktion (TPR) untersucht. Experimente wurden sowohl an unreduzierten Salzimprägnierungen als auch nach Oxydation von bereits reduzierten Proben ausgeführt. Die TPR-Profile sind stark vom benutzten Trägen abhängig, was auf unterschiedliche Grade der Wechselwirkung zwischen Metall und Träger hindeutet; die Reihenfolge ist MgOAl₂O₃>SiO₂. Es wird vermutet, daß das Wesen der Wechselwirkung in der Bildung von schwer reduzierbaren Oberflächenkomplexen zu suchen ist. Die bei Ru-Proben mit der Zahl der TPR-Zyklen beobachtete Verminderung des Wasserstoffverbrauchs wird mit der Schwierigkeit, große Ru-Partikel zu oxydieren, in Zusammenhang gebracht.

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- () SiO₂, l₂₃ MgO. , , , . , , MgO Al₂O₃>SiO₂. , , . , .

     

Beckmann rearrangement of cyclohexanone oxime p-toluenesulfonate on acidic catalysts

The Beckmann rearrangement of cyclohexanone oxime p-toluenesulfonate has been studied using several catalysts. The reaction is catalyzed by weakly acidic sites and seems to occur by way of O-(p-toluenesulfonyl)--caprolactim.

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- -, . - -(-)--.

     

The problem of identifying an adequate kinetic equation for a chemical transformation in thermal analysis

Additional criteria are suggested for the selection of an adequate functiong() describing the mechanism of a chemical transformation using the Satava method.

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Zusammenfassung Zusätzliche Kriterien werden zur Auswahl der geeigneten Funktion g() zur Beschreibung des Mechanismus der chemischen Umwandlung mit der Satava-Methode vorgeschlagen.

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g() .