Studies of the reactions of Br(2P3/2) and Br(2P1/2) with SiH4

Photobromination of SiH₄ under uv-irradiation at various wavelengths has been studied. Rate constants for the elementary reactions Br(²P_3/2)+SiH₄HBr+SiH₃ (k=3.2×10^–11 exp(–21.8±2.5)/RT, cm³/s) and Br^* (²P_1/2)+SiH₄HBr+SiH₃ (k^*=(3±1)×10^–13 cm³/s) have been determined in the temperature range from 300 to 415 K.

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- . Br(²P_3/2)+SiH₄HBr+SiH₃, k=3,2×10^–11 exp (–21,8±2,5)/RT ³/ Br^*(²P_1/2)+SiH₄HBr+SiH₃, k^*=(3±1)×10^{–13 3}/ 300–415 K.

     

Mechanism of ascorbic acid oxidation by molecular oxygen in aqueous pyridine catalyzed by CO2+, Ni2+, Mn2+ and Zn2+

Data on the radical non-chain mechanism of ascorbic acid oxidation by molecular oxygen catalyzed by Co²⁺, Ni²⁺, Mn²⁺ and Zn²⁺ ions are reported.

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Co²⁺, Ni²⁺, Mn²⁺ Zn²⁺.

     

Dispersity and reducibility of the molybdenum oxide phase in SiO2, SiO2?Al2O3 and γ-Al2O3 supported molybdena catalysts

XRD, isothermal and temperature-programmed reduction (TPR) experiments were carried out with SiO₂, SiO₂–Al₂O₃ and -Al₂O₃ supported catalysts. Molybdena is in a more disperse state on supports containing more alumina and it is more reducible on SiO₂–Al₂O₃ than on SiO₂ or -Al₂O₃. TPR curves were shown to reflect connections between reduction kinetics and dispersity.

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-, , SiO₂, SiO₂–Al₂O₃ -Al₂O₃. , , SiO₂–Al₂O₃ SiO₂ -Al₂O₃. .

     

Application of the vapor phase supporting (VPS) method for preparing SnO2/SiO2 catalysts

Supported SnO₂/SiO₂ catalysts have been prepared by the reaction of the surface hydroxy groups of silica gel and gas phase tin chloride (PS method). The catalytic properties have been examined in the reaction of 2-propanol to show the effect of VPS cycles on the amount and nature of the active sites.

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SnO₂/SiO₂ . 2- VPS .

     

Sulfurization of Pt/Al2O3?Cl catalysts. IV. Adsorption sites of H2S on Al2O3, Al2O3?Cl and Pt/Al2O3?Cl

Chemisorption of H₂S on Al₂O₃, Al₂O₃–Cl and Pt/Al₂O₃–Cl has been studied by gravimetry and IR spectroscopy. The influence of the amount of Cl on the H₂S adsorption equilibrium value and the nature of the adsorption sites at low and high coverages are discussed.

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H₂S Al₂O₃, Al₂O₃–Cl Pt/Al₂O₃–Cl . Cl H₂S, .

     

Kinetics of Fe3+ and Cu2+ sorption by fibrous polyampholite

The kinetics of Fe³⁺ and Cu²⁺ sorption from sulfate salt solutions by fibrous polyampholite have been studied.

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Fe³⁺ Cu²⁺ , .

     

CeO2-supported nickel catalysts. Evidence of a strong metal-support ineraction

An increase of the reduction temperature of a Ni/CeO₂ solid results in a continuous decrease of the catalytic activity toward C₂H₆ hydrogenolysis and of the quantity of adsorbed H₂. O₂ treatments with subsequent reduction at low temperature restore a part of the initial properties. This behavior, typical of a strong metal support interaction, is similar to that of Ni/TiO₂, Ni/SiO₂ and Ni/ZrO₂ solids and shows that the SMSI phenomenon is general.

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Ni/CeO₂ C₂H₆ H₂. . , (), Ni/TiO₂, Ni/SiO₂ Ni/ZrO₂ , .

     

Kinetics and selectivity of the oxidation of alkanes in Cl2?H2O and Cl2?Hg2+?H2O solutions

Relative oxidation rate constants of several normal, iso-, cyclo-and methylcycloalkanes have been measured in Cl₂–H₂O and Cl₂–Hg²⁺–H₂O solutions at 343K. The selectivity of C–H bond dissociation in both systems is the same. HOCl is assumed to be the active species for the two systems.

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Cl₂–H₂O Cl₂–Hg²⁺–H₂O 343 , -,- ; C–H . , HOCl.

     

M?ssbauer spectroscopic studies of the state of Pt?Sn/Al2O3 catalyst for hydrocarbon conversion

Mössbauer spectroscopic studies of the state of Pt–Sn catalyst for hydrocarbon conversion supported on prechlorinated -Al₂O₃ indicate that, unlike nonchlorinated Al₂O₃, this system is much more reduced and besides Pt₃Sn–PtSn₂, its surface contains sigfificant amounts of Sn(II) and Sn(IV) chlorides bonded to the surface.

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Pt–Sn , -Al₂O₃. , Al₂O₃, Pt–Sn Pt₃Sn–PtSn₂ Sn(II) (IV), .

     

Hydrocondensation of CO2: Reaction of CO2(CO)/H2 on CuO/ZnO contact masses

The hydrocondensation of CO₂ and CO with and without added MeOH, HCHO and (CH₃)₂CHOH has been studied on CuO/ZnO contact masses in a static reactor at different pressures and reaction times.

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CO₂ CO MeOH, HCHO (CH₃)₂CHOH CuO/ZnO .

     

Cyclohexane photooxygenation by air oxygen in CH2Cl2 in the presence of chromium oxocomplex-iodosylbenzene system

Cyclohexane is oxidized by air oxygen in CH₂Cl₂ solution to yield cyclohexanol, cyclohexanone and cyclohexyl chloride when irradiated by light (>310 nm) in the presence of (Bu₄N)₂CrO₄ or (Bu₃SnO)₂CrO₂. The addition of PhIO greatly accelerates the reaction and increases the yield of products. The reaction mixture contains neither cyclohexanol nor cyclohexanone when the photoreaction in the presence of the Cr(VI)–PhIO system is carried out in argon atmosphere. Hence neither iodosylbenzene nor oxochromium compounds can be oxygen atom donors in alkane oxygenation. The accelerating effect of iodosylbenzene may be due to the enhanced oxidizing power of photo-excited oxochromium species when coordinated to iodosylbenzene.

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CH₂Cl₂ , , (>310 ) (Bu₄N)₂CrO₄ (Bu₃SnO)₂CrO₂. PhIO . Cr(VI)–PhIO , , . , ( ) . .

     

51V NMR studies of systems V2O5-KHSO4 and V2O5?K2SO4

Systems V₂O₅–KHSO₄ and V₂O₅–K₂SO₄ have been studied by the⁵¹V NMR method. The first system demonstrates the same states of vanadium as the previously studied V₂O₅–K₂S₂O₇, in this system a compound with an equimolar ratio of components has been found. In V₂O₅–K₂SO₄ the state of vanadium differs from the above systems and the formation of a compound with V/K=4 is observed.

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⁵¹V KHSO₄–V₂O₅ K₂SO₄–V₂O₅. , K₂S₂O₇–V₂O₅, . K₂SO₄–V₂O₅ V/K4.

     

Thermal decomposition of 10-molybdo-2-vanadosilicic heteropolyacid:29Si and51V-NMR study

Thermal decomposition of 10-molybdo-2-vanadosilicic heteropolyacid has been studied by²⁹Si and⁵¹V-NMR method.²⁹Si-NMR MAS spectra of solid samples indicate that the HPA begins to decompose at T<300°C and the decomposition is complete at 300–400°C.

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²⁹Si ⁵¹V Si–Mo-V () 12- . ²⁹Si MAS , 300°C 300–400°C.

     

Electronic spectroscopy of the state of cu2+ ions in CuO?TiO2 catalysts

Diffuse reflectance spectroscopy of supported CuO–TiO₂ catalysts have revealed that, depending on the CuO content and the calcination temperature, either Cu²⁺ ions incorporated into the TiO₂ lattice, or surface oxide clusters, primary oxide aggregates and CuO_1+X phase bonded to the support by Ti–O–Cu bridges, are formed.

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, CuO–TiO₂ Cu²⁺, TiO₂, , CuO_1+x Ti–O–Cu .

     

Localization of gallium in erionite type Ga?Al zeolites by71Ga,27Al and29Si NMR

The state of Al³⁺, Ga³⁺ and Si⁴⁺ in erionites obtained by hydrothermal crystallization from Ga–Al–Si gels has been examined. The results suggest that gallium cations can isomorphously substitute a part of silicon cations in the zeolite framework, to a notable extent in the sites having no aluminium cations in the second coordination sphere of silicon.

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Al³⁺, Ga³⁺ Si⁴⁺ , . , , .

     

Role of strongly bound vanadia in V2O5/Al2O3 catalysts for selective catalytic reduction of nitric oxide by ammonia

V₂O₅/Al₂O₃ catalysts prepared by impregnation and by ammonia treatment of impregnated samples were tested for activity in the NO–NH₃ reaction. The ammonia treated samples, with higher proportions of strongly bound vanadia, were found to be comparable in activity to the impregnated catalysts and equally sensitive to the presence of oxygen.

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V₂O₅/Al₂O₃, , NO–NH₃. .

     

Structure sensitivity of methane oxidation on Pt/SiO2 of widely varying dispersity

Methane oxidation on Pt/SiO₂ is a structure sensitive reaction at 260–335°C. The higher the percentage exposed, the lower the turnover frequency with decreasing reaction order in P_{CH 4} from 1.0 to 0.5 and slightly decreasing the activation energies of reaction from 90 to 80 kJ/mol, caused by the shift of rate-determining step.

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Pt/SiO₂ 260–335°C . , P_{CH 4} 1,0 0,5 90 80 /. , .

     

The consistency of repeated H2?O2 titration cycles on supported Pt catalysts

H₂ and O₂ uptakes at 296 K on a Pt/Al₂O₃ catalyst remained constant during repeated H₂–O₂ titration cycles conducted in a high vacuum adsorption system. Previously reported variations in these uptakes are attributed to adsorption of contaminants during desorption conditions. Also, it was found that nearly 40% of the H₂ adsorbed could be removed by degassing at 296 K for 1 hr.

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H₂ O₂ 296 Pt/Al/₂O₃ H₂–O₂, . . , 40% H₂ 1 296 .

     

Modification of the catalytic activity of Ni/SiO2 in ethane hydrogenolysis, benzene and co hydrogenation by reduction at high temperatures and restoration by O2?H2 treatments

An increase of the temperature of reduction of Ni/SiO₂ from 900 to 1120 K results in a decrease of catalytic activity per unit area in benzene hydrogenation and ethane hydrogenolysis. O₂–H₂ treatments restore the activities. This behavior is similar to that observed on Pt-based catalysts. In contrast, the CO+H₂ reaction on nickel is not affected by such treatments.

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Ni/SiO₂ 900 1120 . O₂–H₂ . , , CO+H₂ .

     

Effect of the activation conditions on the catalytic properties of Pt/Al2O3 catalysts

The effect of the activation conditions of Pt/Al₂O₃ catalysts has been investigated in the hydrogenation of benzene and in the hydrogenolysis of ethane. Whatever the conditions of calcination or reduction, specific activities of all catalysts for benzene hydrogenation remain constant. On the other hand, for identical dispersities, the cacination in a wet argon flow increases the specific activity of platinum for hydrogenolysis of ethane, pointing out the role of wet pretreatment on defect building or on the faceting of supported metallic catalysts.

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Pt/Al₂O₃ . , . , , . .