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1.
The effect of the degree of platinum crystallite size on the reaction rate, selectivity and activation energy of ethane and propane hydrogenolysis has been studied in the range of platinum crystallite size of 1.7–4.0 nm. In the same range of Pt crystallite size, the activation energy of both processes shows a clear minimum. The decrease in Pt crystallite size bellow 3.0 nm brings about rapid changes in the selectivity of propane hydrogenolysis.
( ) , -. 1,7–4,0 , .
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2.
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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3.
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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4.
V4+ ions in slightly associated states are supposed to play the role of V–P–O/SiO2 active sites. V4+ ions are reduced to V3+ during deactivation of the V–P–O/SiO2 catalyst.
V–P–O/SiO2 V4+ . V–P–O/SiO2 V4+ V3+.
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5.
17O,51V and31P NMR studies indicate that the anion structure of sodium vanadophosphate in an aqueous solution is close to that in crystals of the (CN3H6)8HPV14O42 7H2O salt.
17O,51V,31P , (CN3H6)8HPV14O42 7H2O.
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6.
Interaction of NO with NiCr2O4 has been studied at 473–1173 K. It has been established that on nickel-chromium spinels NO decomposition practically does not take place. Nitric oxide can interact only with prereduced samples to reoxidize them.
473–1173 NO NiCr2O4. , NO . (II) ; .
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7.
The effect of the cracking of14C-labelled cyclohexene on the chemisorption (thermodesorption) of hydrogen on a thermally treated Pt powder catalyst has been studied. It has been established that (i) under the usual conditions of regeneration (calcination of the catalyst at 500°C for 1–2 hrs in a stream of air) the products of cracking cannot be completely removed from the catalyst, and (ii) as compared with the pure catalyst, the carbon deposit content of the catalyst not only increases the amount of chemisorbed hydrogen but also leads to new desorption peaks on the thermodesorption curve.
, C14, () . (1) ( 500°C 1–2 ) (2) - - , : .
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8.
Sorption/evolution of oxygen from V2O5 in the temperature range of 480–520°C is due to a shift in the defect equilibrium 1/2 O2 (gas)+VoOo. A first-order kinetic equation can be derived under the assumption that the activation energy depends on the concentration of defects.
/ V2O5 480–520°C 1/2 O2 ()+VoOo. , , .
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9.
The initial stage of the Li2SO4·H2O single crystal isothermal dehydration has been studied by means of quartz crystal microbalance. As found, weight loss in the initial process may be considered as H2O molecule diffusion from a semiinfinite medium. The numerical values of the H2O molecule diffusion in Li2SO4·H2O have been calculated from the results obtained.
. - - - -. - Li2SO4·H2O.
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10.
[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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11.
    
Using the microcalorimetric technique, the differential adsorption heats of C2H4, C3H6 and CO on oxide catalysts containing Ti4+, Co2+, Ni2+, Zn2+, Ag+ and Cu+ cations have been determined.
C2H4, C3H6 CO , Ti4+, Co2+, Ni2+, Zn2+, Ag+ Cu+.
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12.
Desorption of hydrogen liberated in the process of water decomposition on bimetallic catalysts (3% Ir–Fe/Al2O3) at linear temperature growth was observed. In the case of iridium the amounts of desorbing hydrogen are relatively small, whereas for iron they are many times greater.
, 3% Ir–Fe/Al2O3 . , , .
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13.
SO 3 radicals are formed during the reaction between SO2 and MnO2-alumina, which suggests that SO 3 take part in the reduction of Mn4+ to Mn2+.
SO2 MnO2/Al2O3 SO 3 , , SO 3 Mn4+ Mn2+.
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14.
Kinetic parameters of thermal decomposition of compounds of general formulaM 2 I M II[Ni(NO2)6], whereM I= K+, Rb+ or Cs+ andM II= Ca2+, Sr2+ or Ba2+, were investigated on the basis of the respective thermal curves. Calculations of the reaction order and activation energy carried out by the Coats-Redfern method and by Doyle's method (modified by Zsakó) gave similar results, The reaction order is 2 for all the compounds investigated. In the group of potassium salts the activation energy increases fromM II=Ca2+ toM II=Ba2+. In the groups of rubidium and caesium salts, the lowest activation energy is observed whenM II=Sr2+. Such behaviour of the nitritonickelates is explained in terms of structures and the principle of maximum density.
Zusammenfassung Die kinetischen Parameter der thermischen Zersetzung von Verbindungen der allgemeinen FormelM 2 I M II [Ni(NO2)6] (M I= K+, Rb+ oder Cs+ und MII = =Ca2+, Sr2+ oder Ba2+) wurden auf Grund der entsprechenden thermischen Kurven untersucht. Die an Hand der Coats-Redfern Methode und der durch Zsakó modifizierten Doyleschen Methode durchgeführten Berechnungen der Reaktionsordnung und der Aktivierungsenergie ergaben ähnliche Resultate. Die Reaktionsordnung ist 2 für sämtliche untersuchten Verbindungen. In der Gruppe der Kaliumsalze steigt die Aktivierungsenergie vonM II=Ca2+ in RichtungM II=Ba2+ an. In der Gruppe der Rubidium- und Caesiumsalze wird die niedrigste Aktivierungsenergie beiM II=Sr2+ beobachtet. Dieses Verhalten der Nitritonickelate wird durch die Strukturen und das Prinzip der maximalen Dichte erklärt.

1 2 II[Ni(NO2)6], I= +, Rb+Cs+,a II= 2+,8r2+2+. , - ( ), . 2. + 2+. II=S2+. .
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15.
A study has been made of temperature programmed desorption (TPD) of NH3 and H2O from samples of NH4X and CoNH4X zeolites of various degree of exchange. NH3 TPD peaks could be explained by interaction of NH3 with different Brönsted and Lewis acidic centers. Moreover a water peak at high temperatures allowed interpretations of the dehydroxylation, and by reason of the characteristic desorption temperatures a particular state of the Co2+ ions in the CoNH4X zeolites is postulated.
- () NH3 H2O NH4X CoNH4X . NH3 NH3 =qs . . Co2+ CoNH4X.
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16.
Molecular nitrogen and irradiation temperature are shown to affect the radiationchemical yield of O st in the radiolysis of N2O adsorbed on alumina with large surface areas and to exert no influence in the case of small surface areas of Al2O3.
, - O st N2O, Al2O3 .
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17.
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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18.
From the kinetic studies of CCl3CH2CH2Br addition to 1-hexene, the rate constant of addition of the CCl3CH2CH 2 . ( e 1 R) radical to 1-hexene [1g e 1 kh=(5.2±0.1)–(13 000±800)/RT] has been determined. From the cotelomerization data, rate constants of the interaction of e 1 R-radical with ethylene [1g e 1 ke=(6.1±0.2)–(21 400±1 200)/RT] and carbon tetrachloride [1g e 1 kt=(7.5±0.2)–(37 000±1 200)/RT] have been calculated.
CCl3CH2CH2Br 1-. CCl3CH2CH 2 . - e 1 R.)- 1- (1g 1 K=(5,2±0,1)–(13 000±800)/RT), 1- , 1 R- (1g 1 K=(6,1±0,2)–(21 400±1200/RT) CCl4 (1g 1 K=(7,5±0,2–(37 000±1 200)/RT).
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19.
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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20.
The rate constants for Br(2P1/2) and Br(2P3/2) atoms in the reaction Br+CH3FHBr+CH2F in photobromination of CH3F have been determined. Their ratio is 10–(2.6±0.5) exp(10100±1000/RT) in the temperature range of 60–200 °C.
Br(2P1/2) Br(2P3/2) Br+CH3FHBr+CH2F CH3F. 60–200 °C 10–(2,6±0,5) exp (10100±1000/RT).
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