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1.
A quantum-chemical analysis of the models for geminal OH groups of Al2O3 and of the processes of their dehydroxylation with further dissociative chemisorption of hydrogen has been carried out. Calculations were performed by the SCF MO LCAO method using STO-3G basis set in terms of the cluster approach.
OH- Al2O3 . , STO-3G .
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2.
Two different mechanisms of tritium exchange between and CH3OH vapor in glass vessels have been found: (i) bimolecular exchange in the gas phase, (ii) pseudomonomolecular exchange between gaseous and CH3OH adsorbed on the surface. The total and partial orders, rate constants and activation energies are given.
, CH3OH , : 1) 2) CH3OH, . , .
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3.
[Cu(-C2H2)2]+, [Cu(-CCH2)2]+ and [Cu(-C2H2) (-CCH2]+ complexes have been studied by the ab initio double-zeta basis set method. It has been established that all calculated compounds are stable to decomposition into two C2H2 molecules and Cu+ cation and into one C2H2 molecules and the respective monocomplex. Calculation results suggest the possibility of intramolecular acetylene-vinylidene rearrangement in the coordination sphere of Cu+.
ab initio : [Cu(-C2H2)2]+, [Cu(-CCH2)2]+, [Cu(-C2H2) (-CCH2)]+. C2H2 Cu+ C2H2 . - Cu+.
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4.
The kinetics of hydrogen bond dissociation and formation in solution has been studied by a lineshape analysis of the1H NMR signals of the proton donor (CF3COOH) and proton acceptor (DMF) between –100 and –170°C. It has been found that proton exchange is much slower than molecular exchange and it does not affect the lineshape. A stepwise mechanism has been confirmed.
( ) () — –100°–170°C. , . .
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5.
Conditions are found for the preparation of Pt catalysts providing the formation of epoxy-derivative in the reaction of cyclohexene with an O2/H2 mixture.
Pt .
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6.
Catalysts with nonuniform distribution of the catalytically active component (Pt) over their porous support (Al2O3) have been studied. A nonuniform activity distribution changes not only the reaction rate but also the kinetics can be different on these catalysts.
(Pt) (Al2O3). , , .
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7.
Complete methanation of CO2 and CO on a composite catalyst by onepass operation with a high space-time yield and 100% selectivity at a low temperature such as 270 °C was achieved. In simultaneous methanation, CO methanation accelerates CO2 methanation.
CO2 CO -, co 100%- , 270 °C. , CO CO2.
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8.
The conversion of n-hexane was studied on a Pt-Sn/Al2O3 catalyst, a PtSn alloy and on the corresponding Pt catalysts. The results indicate the same catalytic effect of tin in supported and unsupported catalysts. It is concluded that the role of tin is connected with alloy formation.
- Pt-Sn/Al2O3, PtSn Pt-. . , .
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9.
The activity of various MoO3–SiO2 and WO3–SiO2 catalysts for the aromatization of propylene and butadiene has been investigated. The results obtained show a comparatively high aromatization activity of the catalysts for propylene to benzene and toluene. The direct conversion of butadiene to ethylbenzene, using WO3 on acid treated silica, is considered to be an alternative reaction pathway to the known metathesis step to ethylene and benzene.
MoO3–SiO2 WO3–SiO2 . . , WO3 .
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10.
It is shown that, in contrast to classical impregnation methods, in bimetallic catalyst production the texture of the carrier is stabilized by introducing the promoting ion on the surface of Pt/Al2O3 with vapors of CrO2Cl2 or SnCl4. This is shown by a relatively slower decrease of the specific area and the volume of the pores upon calcination.
, Pt/Al2O3- CrO2Cl2 SnCl4 . .
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11.
IR studies of the effect of Zr, Ge, B and Co additives on the activity of the Pt/Al2O3 catalyst for dehydrocyclization have revealed their promoting action on both oxidation and reduction of platinum. Benzene yield depends on the degree of platinum reduction promoted by boron, whereas with increasing platinum oxidation, the cracking product yield decreases.
, , . , . . . .
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12.
New highly active catalysts for the metathesis of olefins have been obtained through the interaction of [Mo3O4 (C2O4)3 (H2O)3]2– anion with Al2O3 surface and further activation in H2 or CO atmosphere.
[Mo3O4 (C2O4)3 (H2O)3]2– Al2O3 H2 CO .
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13.
The effect of UO3 on the acidity of MoO3–UO3/SiO2 catalysts has been studied by means of infrared spectroscopy of adsorbed pyridine. The surface acidity exhibited a maximum for the same U/(U+Mo) atomic ratio (=0.11) that yielded a maximum in total conversion for isobutene oxidation. The catalytic properties for oxidation are discussed in terms of the acidic properties of the samples.
UO3 MoO3–UO3/SiO2 . U/(U+Mo)=0,11, . , .
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14.
Ligand exchange between the compounds Co(AA)2Py2 and Co(AA)Clpyx (x=1 or 3) formed in the, system, CO(AA)2–SnR2Cl2(R=Ph, Et) in chloroform with pyridine has been established to be catalyzed by SnR2Cl2. An interpretation of the catalytic action of SnR2Cl2 is suggested.
, Co(AA2py2 Co(AA)Clpyx (x=1 3) (Co(AA)2–SnR2Cl2 (R=Ph, Et) , SnR2Cl2. SnR2Cl2.
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15.
The hydrogenation of CO2 has been studied on three different series of catalysts: Fe/MgO, Ni/Ti, Cr/Zn doped with potassium. Reaction was carried out in a conventional flow microreactor system at 15 bar at 250–350°C. Three independent competing reactions: Reverse gas-water shift (RGWS), Fischer-Tropsch (FT) and methanol synthesis were observed.
CO2 : Fe/MgO, Ni/Ti, Cr/Zn . 15 250–350°C. : RGWS, F.T. .
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16.
The laser heating procedure has been used to study chain reactions under strictly homogeneous conditions. The rate constants for the initiation and overall chain decomposition of methanol have been determined.
. - 1000–1100 °.
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17.
Cluster models for various types of OH groups of alumina have been calculated in terms of the MINDO/3 method. Dependence of the acidity and stretching vibration frequencies of OH groups on the number and coordination of neighboring aluminium atoms has been analyzed.
MINDO/3 OH- . OH- .
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18.
On the basis of X-ray identification and studies of magnetic properties, it has been found that coprecipitated hydroxides of iron(III) and zinc(II) transform, after being boiled in distilled water, into a mixture of hydrated oxides, the ferromagnetic modification of iron(III) oxide,-Fe2O3, being responsible for the ferromagnetic behaviour of the mixture. The highest specific magnetization value is obtained for the stoichiometry ZnO: Fe2O3=0.275: 0.725.Since for spinel stoichiometry, Zn(OH)2/2 Fe(OH)3, the magnetic property drops to near zero, formation of zinc ferrite cannot be excluded. However, the poor crystalline shape of this phase, as usually happens when the technique adopted here is involved, does not allow direct confirmation of the existence of that phase by diffraction methods.
Zusammenfassung Aufgrund von röntgenographischen Untersuchungen und von magnetischen Messungen wurde festgestellt, daß die beim Kochen gemeisam gefällter Hydroxide Zn(OH)2/Fe(OH)3 im Wasser entstehenden hydratisierten Oxide ferromagnetische Eigenschaften besitzen, die durch Anwesenheit von -Fe2O3 bedingt sind.Die höchste spezifische Sättigungsmagnetisierung weist ein Präparat mit einer Stöchiometrie ZnO Fe2O3=0.275 0.725 auf.Bei spineller Stöchiometrie: Zn(OH)2/2 Fe(OH)3, fallen die magnetischen Eigenschaften bis in die Nähe des Nullwertes herab. Man kann daher die Entstehung von Zinkferrit nicht ausschließen. Eine eindeutige röntgenographische Bestätigung dieser Phase ist durch die schlechte kristalline Form dieser Phasen, welche meistens bei einer solchen präparativen Technik entstehen, nicht möglich.

Résumé L'identification aux rayons X et l'étude des propriétés magnétiques montrent que les hydroxydes coprécipités de fer (III) et zinc (II) se transforment, après ébullition dans l'eau distillée en un mélange d'oxydes hydratés, la modification ferromagnétique de l'oxyde de fer (III), Fe2O3 étant responsable du comportement ferromagnétique de ce mélange. On obtient la valeur la plus élevée de la magnétisation spécifique pour le rapport stoechiométrique ZnO Fe2O3=0.275 0.725.Etant donné que pour la stoechiométrie du spinelle: Zn(OH)2/2 Fe(OH)3, le ferromagnétisme tombe à une valeur proche de zéro, on ne peut pas exclure la formation de ferrite de zinc. Cependant, la forme mal cristallisée de cette phase, obtenue généralement, ne permet pas de confirmer directement l'existence de cette phase par les méthodes de diffraction.

- , , () (II) , (), -Fe2O3, . ZnO: Fe2O3=0.275: 0.725. : Zn(OH)2/2Fe(OH)3 , . , , .
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19.
A metal-supported catalyst (Ru/SiO2) has been prepared using the sol-gel technique. The structural properties of the solid obtained are compared to those of a conventionally impregnated catalyst.
(Ru/SiO2) -. .
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20.
It has been found that the rate of isotope exchange in Ba2YCu3O7–x–O2 system is high. Its kinetics is exponential, first order with respect to dioxygen and the exchange is of the mixed first/third type.
Ba2YCu3O7–x–O2 . -, -, - .
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