Redistribution kinetics of isotope molecules due to reversible bimolecular reactions with several atomic channels

Isotope kinetic equations for reversible bimolecular reactions describe the rearrangement of atoms in activated complexes. It has been established from the model reaction CH₄+HCH₃+H₂ that the isotopic homoexchange of methane via two atomic channels is given by one set of equations with different sets of parameters.

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- . CH₄+HCH₃+H₂ , .

     

On the mechanism of chlorobenzene hydrolysis over Cu promoted lanthanum phosphate

The reaction mechanism of chlorobenzene hydrolysis to produce phenol over Cu promoted lanthanum phosphate has been studied taking into account a parallel reaction through which benzene is formed. There is a competition for the adsorption sites between the reactants and the reaction products.

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, , , . .

     

Determination of hydrogen chemisorbed on supported nickel catalysts by dimethyl zinc

Nickel supported on various metal oxides was titrated with dimethyl zinc tetrahydrofuranate at 130°C. The amount of hydrogen chemisorbed on nickel was evaluated from the amount of methane evolved after subtraction of OH groups of the support. The fraction of hydrogen bonded to nickel varied between 24–83 % of the overall hydrogen measured in dependence of support and correlated with activity of catalysts in the reaction of diethylene glycol with ammonia.

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, , 130°C. , , OH . , , 24 83% .

     

Reaction of vinyl radicals with propylene in the gas phase

The reaction of vinyl radicals with propylene and propyl radicals was investigated in the gas phase. The radicals were produced by mercury sensitized decomposition of molecular hydrogen followed by addition of hydrogen atoms to propylene and acetylene. Vinyl radical adds to propylene effectively while hydrogen atom abstraction does not occur.

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. , , . , , .

     

Diffusion of hydrocarbons in mordenite and molecular-sieve selectivity of mordenite catalysts

The diffusion of n-octane and n-propylbenzene in mordenite and the molecularsieve selectivity in hydrocracking of octane-propylbenzene binary mixtures over a mordenite catalyst have been studied. The hydrocarbon diffusivities and molecular-sieve selectivity change are accounted for by diffusion through mordenite channel mouths poisoned with an easily adsorbable hydrocarbon.

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- , () -. , , .

     

Hydrocarbon conversion on promoted rhodium/Al2O3 catalysts

In (E+Rh)/Al₂O₃ catalysts (E=Sn, Pb, Mo and W) the catalytic properties of rhodium in benzene hydrogenation, propane hydrogenolysis and n-hexane conversion change drastically. For modified rhodium the decrease in the hydrogenolysis rate of C–C bonds in paraffins leads to an increased yield of the products of non-destructive conversion of n-hexane.

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(E+Rh)/Al₂O₃ (E:Sn, Pb, Mo, W) , , -. C–C -.

     

Stability of hyperbolic reactors

For the one-phase tubular reactor, a new mathematical model is suggested, viz. a hyperbolic system of first order partial differential equations instead of the usual second order parabolic ones. This physically better model is investigated from the point of view of stability via the second Lyapunov method.

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. .

     

Enhancement of H2- and retardation of O2-adsorption during O2?H2 titration cycles on Pt?Al2O3 catalyst surfaces

The title effects can be eliminated if the slow bleeding of H₂ from freshly reduced CuO-towers (often used as O₂-getters in purifying N₂ carrier gas) can be avoided, then H₂–O₂ titrations of Pt surfaces give consistent values from almost the first titration. Water injected at 25 °C also hardly affects the titer values.

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H₂ O₂ , H₂ CuO ( O₂ N₂ — -). H₂–O₂ Pt . , 25° C, .

     

PMR study of the lifetime of complexes with a strong hydrogen bond at low temperatures

The kinetics of formation and cleavage of hydrogen bonds in complexes of carboxylic acids with proton acceptors have been studied by PMR spectroscopy over the range –100 to 150°C. The activation parameters of the processes have been measured.

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¹H –100° ÷–155°C . .

     

X-ray diffraction studies of reforming platinum-alumina catalysts in a high-temperature chamber

X-ray diffraction studies of platinum-alumina catalysts in a high-temperature chamber indicate that in a stream of hydrogen starting from 550–600 K, platinum is practically completely reduced. In several cases at higher temperatures a platinum hydride is also formed.

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, , 550–600 ; .

     

Active state of copper in catalysts for low-temperature methanol synthesis

Copper-containing catalysts have been investigated in low-temperature methanol synthesis. It is shown that the active component of the catalyst is the copper ion and not the metallic copper as is supposed previously.

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, , , .

     

Evidence of blockage of PtH offretite channels by platinum crystallites

The introduction of platinum in a protonic offretite causes a decrease of its activity for m-xylene isomerization and an increase of its constraint index. This is due to the blockage of the offretite channels by small platinum crystallites (<8 Å), as confirmed by the study of m-xylene adsorption.

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- . (<8 Å), -.

     

Catalytic properties of phosphorus-containing rhenium complexes in the hydrogenation of hexene-1

Rhenium (V, VI) complexes with organophosphorus ligands proved to be catalytically active in hexene-1 hydrogenation. The kinetics of this process catalyzed by ReOCl₃(PPh₃)₂ has been examined. The organic ligand in the coordination sphere of rhenium complexes was found to affect selectivity to olefin bonds or nitro groups in the hydrogenation of hydrocarbons.

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(V, VI) -1. , ReOCl₃ (PPh₃)₂. , .

     

Effect of the medium in hexacyanoferrate (III)-iodide and peroxodisulfate-iodide reaction

The kinetics of the two reactions hexacyanoferrate (III)-iodide and peroxodisulfate-iodide in several isodielectric water-cosolvent mixtures have been studied. The results can be rationalized as a consequence of the cosolventwater interaction.

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(III) -. -.

     

Thermometrische und Enthalpimetrische Titrationsmethoden

Zusammenfassung Ausgehend von der allgemeinsten Form der Wärmeleistungsbilanzgleichung für thermometrische und enthalpiemetrische Titrationsmethoden werden die Möglichkeiten dieser Methoden in der analytischen Chemie und im Bereich der Stoffdatenbestimmung aufgezeigt und kritisch gewürdigt. Der Bedarf an zuverlässigen Stoffdaten erschließt den thermometrischen und enthalpiemetrischen Titrationsmethoden im Bereich der Thermo chemie der Lösungen neue Anwendungsgebiete.

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Starting from the most general form of the balance equation of thermal performance for thermometric and enthalpimetric methods of titration, the possibilities of these methods in analytical chemistry and in the field of determining data on materials are demonstrated and critically appreciated. The demand for reliable data on materials opens new fields of application of thermometric and enthalpimetric titration methods in the sphere of the thermal chemistry of solutions.

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Résumé A partir de la forme la plus générale de l'équation du bilan de puissance calorifique pour les méthodes de titrages thermométriques et enthalpimétriques, on montre les possibilités de ces méthodes en chimie analytique et dans le domaine de la détermination des données des substances et on en donne une appréciation critique. Les exigences sur les données sûres relatives aux constituants ouvrent aux méthodes de titrations thermpmétriques et enthalpimétriques de nouveaux domaines d'application dans le domaine de la thermochimie en solution.

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, , . .

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Vorgetragen anläßlich des II. Seminars Thermometrische Analyse (II. Thermometriás Szeminárium) Budapest, 2–7 September 1980.

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Teile dieser Arbeit sind Ergebnisse, die im Rahmen eines vom Bundesministerium für Forschung und Technologie gef6rderten Forschungsprogramms der DECHEMA (F91-J) am Lehrstuhl für Chemie VI der Universität Regensburg erhalten wurden. Herrn Prof. Dr. R. Wachter, Universität Regensburg, danke ich für Diskussionen und Hinweise.     

Non quasi-stationary state pyrolysis. Induction period of neopentane pyrolysis

The principle of an apparatus using an isothermal continuous flow stirred tank reactor to study homogeneous gas phase reactions at space times of the order of 1 sec is given. With this apparatus, the induction period of neopentane pyrolysis (as an example) has been clearly shown.

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, , 1 . , , .

     

Periodic thermal instability during the differential thermal analysis of pyrite

The cause of oscillations in high resolution DTA curves was investigated using simultaneous TG supported by microscopic and XRD examination of quenched samples. The latter techniques showed the instability resulted from the sequential ignition of individual or small groups of particles. This behaviour was different to that observed in our earlier isothermal tests where the oscillations were caused by periodic cracking of the oxide film.

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Zusammenfassung Die Ursache von Oscillationen in hochaufgelösten DTA-Kurven wurde durch TG und gleichzeitige Ausführung von mikroskopischen und XRD-Untersuchungen von abgeschreckten Proben erforscht. Die zuletzt genannten Techniken lassen eine Instabilität erkennen, die auf eine regelmässig aufeinanderfolgende Verbrennung von individuellen oder kleinen Gruppen von Partikeln zurückzuführen ist. Dieses Verhalten unterscheidet sich von dem, das in unseren früheren isothermen Testversuchen beobachtet wurde, bei denen die Oscillationen durch periodisches Zerreissen des Oxidfilms verursacht wurden.

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- . , . , .

     

La and Zn promotion of Ru Fischer-Tropsch catalysts

An investigation of the use of La- and Zn-promoters for Ru/SiO₂ F-T catalysts has been carried out. It was found that, while the use of a La-promoter did not result in any improvement over the use of a K one, Zn-promotion resulted in much higher yields of olefins. The CH₄ and olefin selectivities of the Zn-promoted Ru/SiO₂ were essentially insensitive to temperature over the range 250–320 °C. The Zn-promoted catalyst was found to have many of the same catalytic properties previously found for Ru/ZnO, but was much more active. Thus, it is possible to achieve certain interesting catalytic properties for Ru by the use of Zn-promotion without having to make use of the low surface area support ZnO.

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La Zn- Ru/SiO₂ F-T. , , La- - , Zn- . CH₄ Zn- Ru/SiO₂ , -, 250–320°C. Zn- , Ru/ZnO, . Ru, Zn- ZnO .

     

Experimental study of the bifurcation diagram in the Belousov-Zhabotinskii reaction

In the citric acid-Mn²⁺–H₂SO₄–KBrO₃ system a hysteresis phenomenon in the switching on and off of the oscillations has been observed. The possible bifurcation diagrams of the system are discussed.

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-Mn⁺²–H₂SO₄–KBrO₃ . .

     

Oxidation of hydrocarbon mixtures over a complex vanadium catalyst

Vapor-phase oxidation of hydrocarbon mixtures over vanadium oxide (promoted by potassium sulfate)-silica catalyst has been studied. It is shown that the inhibition of the rates of formation of individual products depends on the ability of the added hydrocarbons to similar specific interaction with the catalyst.

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. , , .