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1.
Magnesia aerogel activated by hydrogen spillover at 430 °C or at 200 °C becomes a catalyst for the hydrogenation of ethylene. This catalytic activity, observed already at 50 °C, is further enhanced by a treatment in oxygen at 430 °C.
, 430 200°C, . 50°C 430°C.
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2.
The thermogravimetry of mixtures of metallic copper and copper oxides was studied. The experiments were performed by heating the samples in air to 700–800° to transform all the components to copper(II) oxide, and continuing the heating in nitrogen to 1050–1100° when the dissociation of copper(II) oxide to copper(I) oxide is complete. The identification of the components and their quantitative determination were carried out by determining the shape, size, and ratio of the segments of the curves obtained during the heating. The method can be used for quantitative analysis of mixtures of copper and/or copper oxides.
Zusammenfassung Gemische von metallischem Kupfer und Kupferoxiden wurden thermogravimetrisch untersucht. Zur Überführung aller Komponenten in Kupfer(II)-oxid erhitzte man sie in Luft auf 700–800°, um daraufhin bis zur vollständigen Dissoziation des Kupfer-(II)-oxids zu Kupfer(I)-oxid unter Stickstoff die Temperatur bis auf 1050–1100° zu steigern. Die Identifizierung der Komponenten und ihre quantitative Bestimmung erfolgten durch die Form, Größe und die Verhältnisse der verschiedenen Abschnitte der erhaltenen Kurven. Diese Methode ist zur quantitativen Bestimmung von Gemischen aus Kupfer und Kupferoxid sowie von Kupferoxiden geeignet.

Résumé Étude thermogravimétrique de mélanges du cuivre métallique et d'oxydes de cuivre. Les échantillons sont d'abord chauffés dans l'air jusqu'à 700–800° jusqu'à ce que tous les constituants soient transformés en oxyde de cuivre(II); le chauffage est ensuite poursuivi dans l'azote jusqu'à 1010–1100°, où la dissociation de l'oxyde de cuivre(II) en oxyde de cuivre(I) est complète. Les constituants ont été identifiés et dosés en utilisant la forme, la dimension et les proportions des différentes parties des courbes pendant le chauffage. La méthode peut être utilisée pour l'analyse quantitative de mélanges de cuivre et ou d'oxydes de cuivre.

. 700–800: ( (), 1050–1100° [ () (I)]. , , . / .


The author wishes to acknowledge the financial assistance provided by the Technion — Israel Institute of Technology.The author wishes also to thank Dr. R. F. Tylecote (University of Newcastle Upon Tyne, England) for very helpful comments and useful discussions of this investigation and to Mrs. N. Leder for chemical analyses.  相似文献   

3.
A series of samples in the system Co1–xZnxFe2O4 (x=0.3, 0.4, 0.6, 0.8 and 1) were prepared by the usual ceramic technique. The D. C. electrical resistivity and thermoelectric power were measured in the temperature range from room temperature up to about 600 K. Transition from the ferrimagnetic region to the paramagnetic region is accompanied by an increase in the activation energy by an amountE, which varies in the range 0.052–0.090 eV. The large values ofE obtained may be due to the fairly strong B-B exchange interaction in Co-Zn ferrites.
Zusammenfassung Mittels üblicher Keramiktechniken wurden Proben des Systemes Co1xZnxFe2O4 unterschiedlicher Zusammensetzung (x=0,3, 0,4, 0,6, 0,8, 1,0) dargestellt. Im Temperaturbereich Raumtemperatur-600 K wurde der elektrische Widerstand gegenüber Gleichstrom sowie die Thermospannung dieser Proben ermittelt. Der Übergang von der ferrimagnetischen zur paramagnetischen Region wird von einem Anwachsen der Aktivierungsenergie um den BetragE=0,052–0,090 eV begleitet. Den so erhaltenen grossen E-Werten liegen wahrscheinlich die ziemlich starken B-B Austausch Wechselwirkungen in Co-Zn Ferriten zu Grunde.

1–xZnxFe24 =0,3;0,4;0,6;0,8 1, 600 . E, 0,052–0,090 . E - - .
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4.
    
- 1962 . .
The kinetics of reduction of a low-temperature CO shift catalyst (1962, GDR) by hydrogen at 150°C has been studied by the static circulation method. An empirical equation has been obtained for the range of maximum reaction rates.
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5.
Electron microscopy and Mössbauer spectroscopy studies of nickel-based Raney catalysts have revealed that the catalysts are formed through the successive aggregation of their structural elements. Catalyst particles are covered by a thin layer of nickel oxide.
. , . .
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6.
The conditions and premises of the kinetic evaluation of thermoanalytical curves on the basis of chemical kinetics are demonstrated, and the limits of their availability are pointed out. For reactions with an unclear structural and chemical course, some appropriate definitions of terms are proposed.The possibilities of the use of the inflection points of the reaction rate versus time curve are presented. New methods of determination of kinetic parameters are described, including the ratio of the degrees of reactionx, the ratio of the reaction ratesx and the ratio of the tangent slopesx at these points.
Zusammenfassung Bedingungen und Voraussetzungen der kinetischen Auswertung thermoanalytischer Meßkurven auf der Basis der chemischen Kinetik werden dargestellt, gleichzeitig wird auf die Grenzen ihrer Gültigkeit hingewiesen. Für Reaktionen mit unklarem chemischem oder strukturellem Ablauf werden geeignete neue Bezeichnungen definiert.Die Möglichkeit zur Verwendung der Wendepunkte der Kurve Reaktionsgeschwindigkeit gegen Zeit vorgestellt. Neue Methoden werden beschrieben, die zur Bestimmung kinetischer Parameter das Verhältnis der Umsätzex 1 x 2, das Verhältnis der Reaktionsgeschwindigkeitenx 1/x 2, und das Verhältnis der Tangentensteigungenx 1/x 2 an den Wendepunkten verwenden.

. . . — . , (x), () () .
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7.
The effect of support content and composition of supported metal phase on the crystallite size, phase composition and catalytic properties of supported Ni and Cu–Ni catalysts has been investigated. It has been established that with increasing metal content, crystallite sizes and enantioselectivity increase. Copper added to Ni catalysts decreases metal phase dispersity and enantioselectivity.
, , - . , . є .
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8.
Thermal desorption spectra of oxygen desorbed from rhodium have been analyzed in terms of models accounting for the effect of lateral interactions between adsorbed particles and of their diffusion into the bulk of metal on the desorption kinetics of O2. Complex configuration of these spectra is ascribed to the processes of formation/decomposition of surface Rh oxides and the diffusion of particles into the near-surface layers of metal and back to the surface.
- , O2 . - O2 Rh - .
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9.
m-Xylene conversion was studied over dealuminated Y type zeolites in hydrogen forms, SiO2 to Al2O3 ratios were varied from 4.86 to 12.95.
- . SiO2/Al2O3 4,86 12,95.
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10.
Studies of water vapor adsorption on polycrystalline Rh at T>315 K and P=(2–4)×10–2 Pa indicate that water is adsorbed dissociatively to Oads and Oads through a molecularly adsorbed species. Desorption activation energy is 46 and 69 kJ/mol for molecular and dissociative species, respectively.
Rh (2–4)·10–2 . , O OH - . 46 /, -69 /.
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11.
Some peculiarities of reduction of one-electron oxidants, Ru(bpy) 3 3+ and Ru(bpy)2(py) 2 3+ , in the absence of catalysts (when oxidation of the oxidant's ligands occurs) and in their presence (when also oxidation of water to dioxygen occurs) are discussed. Both oxidation reactions are thought to have a common intermediate.
Ru(bpy) 3 3+ Ru(bpy)2(py) 2 3+ ( -) ( ). , .
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12.
    
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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13.
The strength of protonic sites and the concentration of acid centers in V2O5/Al2O3 catalysts have been estimated according to pyridine and ammonium adsorption.
V2O5/Al2O3.
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14.
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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15.
The character of the effect of initial reaction mixture and temperature on the selectivity of catalytic reduction of sulfur dioxide by methane in the presence of oxygen has been studied.
.
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16.
The effect of treatment conditions of high-silica zeolites on their oxidation-reduction properties in benzene adsorption has been studied.
- - .
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17.
    
Thekinetic (inhibiting) effect of added alkenes on the pyrolysis of 2,2-dimethylbutane was described in a previous letter. We now investigate thechemical effect of two alkenes (2-methyl-2-butene and isobutene) on this pyrolysis, more precisely the formation of new primary products and the changes in product distribution. The observed effects are interpreted by the addition of a free H· atom to the double bond of the alkene molecule and the subsequent reactions of the free radicals formed in this addition step.
() 2,2- . (2--2- ) , . H· , .
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18.
    
A higher activity of Na–X than Na–Y in CH3SH+SO2 reaction at 343 was observed. The increase of the copper content in the samples causes an increase of their activity. Water, sulfur, dimethyl disulfide, dimethyl trisulfide and sometimes dimethyl sulfide are registered as reaction products. (CH3)2S3 is formed as a result of the reaction between sulfur and (CH3)2S2.
, Na–X , Na–Y CH3SH+SO2 343 . . , , , , . (CH3)2S2 (CH3)2S3.
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19.
The hydrogenation of benzene, styrene and isoprene over magnesia doped with sodium and potassium vapors has been studied. Neither system displays a catalytic activity towards benzene hydrogenation. The initial rate, turnover number and time of halfdecay for styrene and isoprene hydrogenation have been determined.
, . . , .
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20.
Supported Ni-Pd/SiO2 catalysts of different Ni and Pd composition were studied in n-butane hydrogenolysis. The reaction rate, selectivity towards methane, ethane and propane were determined. On the basis of these data the relationship between the size and composition of the active center and the possibility of surface segregation of one of the components is discussed.
Ni-Pd/SiO2 Ni Pd -. , . .
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