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1.
A solid solution of vanadium in MoO3 with a solubility limit of about 3 mol.% V2O5 is shown to be formed. Its catalytic properties are discussed.
MoO3 3 . % V2O5 .
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2.
    
, 1.2·1018/2 3.6·1018/2, . , .
The endothermic stage of desctruction of Al2O3 crystal lattice begins with the adsorption of a monolayer of chloride and hydrogen ions (1.2×1018 m–2 and 3.6×1018 m–2, respectively). The abrupt change in the Al content of the solution is attributed to the release of low-coordinate aluminium ions from the environment of the cationic vacancies of the oxide lattice.
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3.
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.
(V, VI) -1. , ReOCl3 (PPh3)2. , .
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4.
The contents of three forms of molybdenum oxide compounds in molybdena-alumina catalysts have been determined by their solubility in water and ammonia. The form which is readily soluble in water and reducible to Mo(IV) at 400°C and PH2=105 Pa is active in cyclohexane dehydration, and the forms soluble in water and ammonia are active in thiophene hydrogenolysis.
. , 400°C PH 2=I Mo(IV); — .
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5.
Catalytic properties of Pd black-oxide systems have been studied in hydrogenation of crotonaldehyde. It has been revealed that the additions of basic and amphoteric oxides (MgO, Fe2O3 and ZnO) increase the hydrogenation rate of the ethylenic bond in crotonaldehyde.
Pd-- . , (MgO, Fe2O3, ZnO) .
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6.
A rate increase of SiH3Br formation in SiH4 photobromination under irradiation by a cw CO2 laser is reported. At low SiH4 pressures (1–2 Pa) the radiation effect is shown to be isotope-selective.
SiH3Br CO2 SiH4. , SiH4 (1–2 ) .
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7.
It has been shown that in the interaction of zinc oxide and phosgene, the most active are the samples having oxygen vacancies. A mechanism for this process is suggested.
, , . .
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8.
The dual role of catalysts in the interaction between an inorganic molecule AB and adsorbed oxygen ZO, as an electron donor (in the oxidative addition of AB) and as an electron acceptor (in subsequent ZO reduction), permits to interpret the orders of activities of various optimal catalysts and their dependence on the AB structure.
AB ZO — ( AB) ( ZO). AB.
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9.
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.
(), , , , -. Pt , .
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10.
A method has been proposed for the study of the stability of typical catalysts for complete oxidation with respect to poisoning by sulfur dioxide in CO oxidation.
CO.
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11.
    
23° - , (–1)/(2+1) 1/, ET . , (–1)/(2+1), — ET .
The correlation between the rate of gamma-initiated isosafrole oxidation and the rate of radiation-chemical initiation has been studied together with the dependence of the oxidation rate on (–1)/(2+1) and 1/ as well as on ET of the solvent at 23°C. It has been shown that the logarithm of the rate of free-radical oxidation is a linear function of (–1)/(2+1) and that of the ionic process depends linearly on ET of the solvent.
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12.
A new metal reactor with two chambers in which complete mixing of gases is achieved has been developed for use in the diaphragm method. This apparatus is suitable for the determination of the effective diffusion coefficient and its temperature dependence. It can also be used to determine the type of transport, the gas permeability coefficient and to investigate the macrokinetics of catalytic processes.
. : ; ; .
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13.
The stoichiometry of thermal decomposition was studied for the following compounds: Ni(pyNO)Cl2H2O (I), (pyNO=pyridine N-oxide), Ni(2-MepyNO)Cl2·2H2O (II), Ni(3-MepyNo)Cl2·2H2O (III) and Ni(4-MepyNO)2Cl2·C2H5OH (IV). The heating of the compounds led first to the release of H2O molecules (or C2H5OH molecules), with the formation of Ni(pyNO)Cl2 (V), Ni(2-MepyNO)Cl2(VI), Ni(3-MepyNO)Cl2 (VII) and Ni(4-MepyNO)2Cl2 (VIII). In the next stage, decomposition of the heterocyclic liugands set in. The compositions and spectral and magnetic properties of these complexes indicate their dimeric (II, III, IV, VIII) of polymeric (I, V, VI, VII) structure with coordinated molecules of H2O (or C2H5OH).
Zusammenfassung Die Stöchiometrie der thermischen Zersetzung folgender Verbindungen wurde untersucht: Ni(pyNO)Cl2·H2O (I), (pyNO=Pyridin-N-oxid), Ni(2-MepyNO)Cl2·2H2O (II), Ni(3-MepyNO)Cl2·2H2O (III) und Ni(4-MepyNO)2Cl2·C2H2OH (IV). Beim Erhitzen erfolgt zunächst die Abspaltung von Wasser bzw. C2H5OH unter Bildung von Ni(pyNO)Cl2 (V), Ni(2-MepyNO)Cl2 (VI), Ni(3-MepyNO)Cl2 (VII) und Ni(4-MepyNo)2Cl2 (VIII). Im nächsten Schritt setzt die Zersetzung der heterozyklischen Liganden ein. Aus den Zersetzungsreaktionen und den spektralen und magnetischen Eigenschaften dieser Komplexe folgt deren dimere (II, III, IV, VIII) oder polymere (I, V, VI, VII) Struktur mit koordinierten Wasser- bzw. C2H5OH-Molekülen.

: Ni(pyNO)Cl2-H2O (I), (pyNO=H- ), Ni(2-MepyNO)Cl2·22 (II), Ni(3-MepyNO)Cl2-2H2O (III) Ni(4-MepyNO)2Cl2-C2H5OH (IV). ( ) Ni(pyNO)Cl2 (V), Ni(2-MepyNO)Cl2 (VI), Ni(3-MepyNO)Cl2 (VII) Ni(4-MepyNO)2Cl2 (VIII). . , (II, III, IV, VIII) (I, V, VI, VII) .
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14.
At small concentrations of CO, palladium initiates a radical-chain process. At high CO concentrations CO oxidation occurs only on the surface of the heterogeneous catalyst and the effect of palladium is mainly due to the specific activation of carbon monoxide on the palladium surface.
CO . CO .
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15.
Pt(alizarine)2 complex adsorbed on the surface of titanium dioxide has been found to cause spectral sensitization of the photocatalytic activity of TiO2. Adsorption of the complex provides simultaneously sensitization of the photoprocess and catalysis of dark steps of dihydrogen formation.
, Pt()2 TiO2. , , .
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16.
Variations in the electronic state of silver catalysts for methanol oxidation under the effect of the reaction medium have been studied, using diffuse reflectance spectroscopy. The nature of active centers-Ag+ cations, Ag n + complexes and clusters of various sizes for bulk and supported catalysts are shown to be identical.
. - Ag+, Ag n + .
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17.
The photocatalytic properties of some cyanogen-and thiocyanogen-based inorganic polymers, such as paracyanogens containing different metals (Hg, Ag, Cu), polythiocyanogens of different iodine contents, polycyanogen and poly (cyanogenthiocyanate), have been tested in two systems. Cu-containing paracyanogen and the iodine-poor polythiocyanogens catalyze the photoreduction of methylviologen under visible light, furthermore the Cu-containing paracyanogen catalyzes the photoreduction of water to hydrogen under UV irradiation.
, , , , (Hg, Ag, Cu), , (), . , , , , , , -.
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18.
Kinetic data show that in the presence of K2WO4/Al2O3, methanethiol is largely produced by the reaction of H2S with metanol and partly with dimethyl ether. Dimethyl sulfide is formed during the interaction of methanethiol with methanol, of H2S with dimethyl ether and as a result of methanethiol disproportionation. Methane and carbon oxides are the decomposition products of methanethiol and dimethyl sulfide and of methanol and dimethyl ether, respectively.
, K2WO4/Al2O3 H2S — . , H2S . , — .
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19.
    
The synthesis and physicochemical properties of new metallic systems obtained by supporting Pd on colloidal AlPO4, AlPO4–SiO2 and AlPO4--Al2O3 to be used as reduction catalysts are reported. The catalytic activity of the above systems in the transfer reduction of nitrobenzene using cyclohexene as hydrogen donor has been measured.
, Pd AlPO4, AlPO4SiO2 AlPO4-Al2O3 . , .
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20.
The effect of hydrogen pressure on the selectivity of hydrogenation of 2-butene-1-al at the carbonyl group in the presence of Ru and Ru–ZnO catalysts indicates that the selectivity on the modified ruthenium catalyst in the pressure range of 0.51–8.08 MPa is a maximum at .
-2--І Ru Ru–ZnO-. , 0,51–8,08 , .
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