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1.
Template-free synthetic, boron-containing pentasil type zeolites exhibit structural and catalytic properties similar to those of SABO zeolites made in the presence of n-propylamine.
, , , SABO, -.
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2.
The liquid-phase catalytic hydrogenation of various organic compounds was carried out using new rhodium catalysts supported on AlPO4–SiO2 (2080 wt. %) system, in methanol as solvent, under low hydrogen pressure (0.55 MPa) and at 293 K. Neither alkene isomerization nor hydrogenolysis products were detected in any of the cases.
AlPO4–SiO2 (2080 . %), , , (0,55 MPa) 293 . , .
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3.
Effect of silylation with hexamethyldisilazane on adsorption and catalytic properties of porous glass-supported platinum catalysts has been studied. Catalytic activity decreases markedly with an increase in surface coverage by trimethylsilyl groups for all the following reactions examined: hydrogenation of benzene, dehydrogenation of cyclohexane and dehydrocyclization of n-hexane.
, . , : , -.
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4.
    
According to the suggested equations to describe the distribution of cotelomerization products, relative constants for chain propagation and transfer characterizing elementary steps of the process, and the character of the depencence between the product formation rate and the reactant concentrations have been established.
, . , . .
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5.
The activating effect of nickel on MoS2 impregnated with an aqueous solution of Ni(CH3COO)2 and sulfided has been established to be proportional to the amount of active nickel incorporated as Ni2+ cations in the MoS2 lattice. MoS2 capacity for active nickel is limited and determined by the preparation method of the parent MoS2.
MoS2 ( Ni(CH3COO)2, ) Ni2+, . MoS2 «» .
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6.
The monooxygenation of aniline by hemin, with oxygen activation by direct electron transfer from a cathode to the catalytically active center and direct participation of the reduced oxygen species in the reaction has been carried out.
.
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7.
    
Syngas reactions have been performed under pressure (6 MPa) on Co–Y and Co–Cu–Y catalysts with the intent to obtain good conversions and high C2–C5 alcohol selectivities. The addition of MoOx promotes the alcohol production and stabilizes the catalysts. TPR experiments indicate clearly the strong interaction between Co, Cu and Mo and XRD data show that MoOx prevents structural damage during the ageing.
Co–Y Co–Cu–Y 6 MPa C2–C5. MoOx . Co, Cu Mo, , MoOx .
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8.
Studies of the liquid-phase oxidation of dibenzyl ether in the presence of 12 acetylacetonates of 3d metals and a comparative analysis of the dependence of the catalytic activity and selectivity of chelates on the atomic number and valence state have been carried out.
12 3d . .
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9.
A kinetic equation for cyclohexane dehydrogenation at PO=1.0 MPa has been obtained.
1,0 .
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10.
A static method is described for measurement of the equilibrium values of temperature, pressure and composition of the solid phase, and determination of the number of degrees of freedom in heterogeneous systems containing a gaseous phase, including water vapour. With this method, it has been found that in the system formed in the thermal dehydration of CaC2O4·H2O a solid solution of monohydrate and anhydride coexists in equilibrium with water vapour. The composition of the solid solution changes with the temperature and the pressure of water vapour. The dehydration enthalpy of the solid solution referred to 1 mol H2O does not depend on its composition. It was found to be H deh=(69+-3) kJ·mol–1.
Zusammenfassung Eine isotherme Methode zur Messung von Temperatur, Druck und Zusammensetzung der festen Phase im Gleichgewicht und zur Bestimmung der Anzahl der Freiheitsgrade in heterogen Systemen mit einer Gasphase (z.B. Wasserdampf) wird beschrieben. Mit dieser Methode wurde nachgewiesen, dass bei der thermischen Entwässerung von CaC2O4·H2O eine feste Lösung von Monohydrat und Anhydrid im Gleichgewicht mit Wasserdampf existiert. Die Zusammensetzung dieser festen Lösung ändert sich mit der Temperatur und dem Wasserdampfdruck, ihre Dehydratationsenthalpie (pro 1 mol Wasser) hängt nicht von der Zusammensetzung ab und wurde zu H deh=(69±3) kJ mol–1 bestimmt.

, , , , . , , 24·2 . . , 1 , H .=69±3 .–1.
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11.
The activity of vanadia/titania catalysts in CO oxidation has been tested and found to be of the same order as that observed for unsupported vanadia; the simultaneous presence of vanadium-sodium compounds cancels the activity, probably because of the elimination of labile V=0 species at surface defects.
V2O5/TiO2 CO, V2O5; - , , V=0 .
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12.
The decompositions of the clathrate compounds [M(NCS)2(4-MePy)4]·nG (whereM=Mn, Co, Ni or Cd;G=4-methylpyridine (4-MePy), benzene or xylenes) were studied on a Q-derivatograph under quasi-equilibrium conditions and with linear heating. These clathrates can be divided into two groups, in which the loss of guest is either (I) accompanied by destruction of the host complex, or (II) occurs before decomposition of the host complex. Kinetic parameters were obtained.
Zusammenfassung Die Zersetzung von Clathrat-Verbindungen der Zusammensetzung [M(NCS)2(4-MePy)4]·nG (M=Mn, Co, Ni, Cd;G=4-Methylpyridin (4-MePy), Benzen, o-,m, p-Xylen) wurde mittels Q-Derivatograph unter Quasi-Gleichgewichtsbedingungen und bei linearer Aufheizung untersucht.Die studierten Clathrate lassen sich in zwei Gruppen einteilen, je nachdem ob die Abgabe des Gastmoleküls G entweder vor oder unter Gleichzeitiger Zerstörung des Wirtskomplexes erfolgt. Kinetische Parameter wurden ermittelt.

Q- [M(NCS)2(4-MePy)2]·nG, M , , , G — 4- , . , . .
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13.
From the analysis of the detailed reaction mechanism and taking into account vanadium complex formation processes, a steady state kinetic equation has been derived to describe experimental data in a wide range of reaction conditions.
, .
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14.
Liquid (aqueous) phase catalytic hydrogenation of compounds containing two oxo-groups in -position (biacetyl, glyoxal, alloxan) was studied in the presence of tungsten carbide catalyst. It has been shown that only one of the oxo-groups is affected in the course of the process and is transformed into a >CH–OH group. Comparative studies carried out in the presence of platinum catalyst attest the selective behaviour of tungsten carbide.
- - (, , ). , >C=O >CH–OH, . .
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15.
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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16.
The effect of various inorganic polymers on the catalytic activity and selectivity of platinum in the hydrogenation of 4-chloronitrobenzene and dinitrotoluene has been studied. Platinized iron-containing polycyanogens are less active but more selective catalysts for the hydrogenation of 4-chloronitrobenzene than Pt/C or Pt/BaSO4.
4- . , , , 4-, Pt/C Pt/BaSO4.
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17.
Infrared studies of the interaction of NO with CuY–A zelites have been made over the temperature range from –100°C to 400°C. Several forms of NO adsorption have been found, in particular, a stable cis-dimer at low temperatures.
- (–100+400°C) NO CuY–A . NO, ë - .
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18.
The catalytic acetoxylation of ethylene and propylene occurs under the action of oxygen in the presence of Pd(II)+HPA-6, where HPA-6 is the heteropolyacid H9PMo6V6O40. In addition to the products of acetoxylation (alkenyl and allyl acetates), oxidation products (acetaldehyde and acetone) are also formed. The selectivity of acetoxylation increases upon the addition of NaOAc.
— — Pd(II)+-6, -6 H9PMo6V6O40. (- ) — . NaOAc.
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19.
Thermal characteristics of the composites of poly(methyl methacrylate) and copper are reported, including the order of reaction and activation energy of the major second stage of pyrolysis. The randomly-distributed metal particles in the polymer matrix can form paths for heat transfer which determine the mechanism of thermal degradation.
Zusammenfassung Die thermischen Charakteristika der Verbindungen von Polymethylmethacrylat mit Kupfer werden zusammen mit der Reaktionsordnung und der Aktivierungsenergie der grösseren zweiten Stufe der Pyrolyse beschrieben. Die zufallsbestimmt verteilten Metallpartikel in der Polymermatrix können Wege des Wärmetransfers formen, welche den Mechanismus der thermischen Zersetzung bestimmen.

Résumé On décrit les caractéristiques thermiques de composites du polyméthylméthacrylate avec le cuivre, parmi lesquelles l'ordre de réaction et l'énergie d'activation de la seconde étape de la pyrolyse qui est la principale. Les particules du métal distribuées au hasard dans la matrice du polymère peuvent constituer des voies pour le transfert de chaleur qui déterminent le mécanisme de la dégradation thermique.

, . , .
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20.
Résumé On a modifié la méthode différentielle pour le calcul des paramètres cinétiques des réactions de décomposition thermique du type: A(s) B(s) + C(g), en utilisant les données de l'analyse thermodifférentielle. En effectuant le calcul des paramètres cinétiques des réactions de déshydratation de l'oxalate de calcium monohydraté et de décomposition du carbonate de calcium on obtient des résultats qui concordent d'une manière satisfaisante avec ceux obtenus par d'autres méthodes.
A modification of the differential method is presented in order to evaluate the kinetic parameters of thermal decomposition reactions of the type A s B s + +Cg, using differential thermal analysis (DTA) data. The kinetic parameters calculated for the dehydration and decomposition of calcium oxalate and carbonate agree satisfactorily with those mentioned in the literature.

Zusammenfassung Es wird über eine Abänderung der Differentialmethode zur Errechnung der kinetischen Parameter von thermischen Zersetzungsreaktionen des Typs A(s) B(s) + C(g) mit Hilfe von differentialthermoanalytischen Daten berichtet. Die am Beispiel der Dehydratation des Calciumoxalat-Monohydrats und der Zersetzung des Calciumcarbonats erhaltenen Ergebnisse der auf angegebene Weise durchgeführten kinetischen Berechnungen stimmen gut mit den nach anderen Methoden erhaltenen Resultaten überein.

A(s) (s) + C(g), (). , , , .
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