Reactivity of Cl(2P1/2) atoms towards CH3F

The photochlorination of methyl fluoride has been studied at low pressures. Excited (²P_1/2) chlorine atoms have been found to participate in the reaction. The ratio of the excited and ground state rate constants has been estimated at room temperature.

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. (²P_1/2) . .

     

Observation conditions and thermal stability of O2? on SnO2

A sharp change in the relaxational characteristics of O ₂ ^– anion radicals on SnO₂ is observed under physical adsorption of O₂ molecules in an amount less than 10¹⁶ m^–3. The thermal stability of sites for O ₂ ^– stabilization on SnO₂ is analyzed. Molecular oxygen, forming O₂, is shown to desorb with increasing temperature without participating in reoxidation of the oxide.

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O ₂ ^– SnO₂ O₂ 10¹⁶ M^–2. O ₂ ^– SnO₂. , O₂, O ₂ ^– , .

     

Catalysts for metathesis of olefins, prepared by anchoring of MoO2(acac)2 to Al2O3

New highly active catalysts for metathesis of olefins were obtained through the interaction of bis(acetylacetonato)dioxymolybdenum(VI) with surface OH groups of -Al₂O₃ and subsequent reduction in H₂ or CO.

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()(VI) OH -Al₂O₃ H₂ CO .

     

Kinetic studies of hydrogen and carbon monoxide adsorption on Re2O7/Al2O3 catalysts

Kinetic studies of hydrogen and carbon monoxide adsorption on reduced Re₂O₇/Al₂O₃ catalysts have revealed that its activation energy decreases with increasing reduction degree of rhenium oxide. Adsorption of gases is suggested to take place on metallic rhenium atoms.

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- . , . , .

     

Kinetics of isotope exchange of dioxygen with a powdered high-temperature superconducting material Ba2YCu3O7?x

It has been found that the rate of isotope exchange in Ba₂YCu₃O_7–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.

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Ba₂YCu₃O_7–x–O₂ . -, -, - .

     

Interaction of propylene with a V2O5/Al2O3 catalyst

IR-spectroscopic studies indicate that on the oxidized surface of V₂O₅/Al₂O₃ catalysts propylene interacts mainly with Brönsted acid centers to form an alcoholate type complex transforming into acetone. On the reduced surface propylene is stabilized as a -complex of V³⁺ and V⁴⁺ ions.

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- , V₂O₅/Al₂O₃ , . - V³⁺ V⁴⁺.

     

Electroconductivity changes of Na-modified TiO2 and Pt/TiO2 films

Electrolytic supporting of metallic sodium on the surface of TiO₂ and Pt/TiO₂ films is shown to change significantly the Fermi level of the semiconductor substrate already at small concentrations of sodium. The steady-state catalytic activity changes only at high concentrations of supported sodium, varying the chemical composition of the active phase. The contact process does not play any significant role in the catalytic process.

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, TiO₂ Pt/TiO₂ . , . .

     

Reduction kinetics of NiO-MoO3 catalysts

Reduction kinetics of NiO–MoO₃ catalysts in H₂ at 573–723 K has been studied. Reduction activation energies E_a have been determined. The degree of NiO–MoO₃ reduction is shown to increase with increasing NiO content.

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NiO–MoO₃ H₂ 573–723 . E NiO–MoO₃ . , NiO–MoO₃ NiO .

     

31P-NMR studies on the interaction between Rh(AA)(CO)(PPh3) complexes and free PPh3

Uncoordinated phosphine exchanges with that in Rh(AA)(CO)(PPh₃) (AA—anthranilate and phenylanthranilate ions, respectively) via an S_N2 mechanism.

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Rh (AA) (CO) (PPh₃) (AA — ) S_N2.

     

Aromatization of propylene and butadiene over MoO3?SiO2 and WO3?SiO2 catalysts

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.

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MoO₃–SiO₂ WO₃–SiO₂ . . , WO₃ .

     

IR-spectroscopic studies of strength and concentration of acid centers on V2O5/Al2O3 catalysts

The strength of protonic sites and the concentration of acid centers in V₂O₅/Al₂O₃ catalysts have been estimated according to pyridine and ammonium adsorption.

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V₂O₅/Al₂O₃.

     

Effect of vanadium content on the character of acidic sites on V2O5/Al2O3 catalysts

By IR spectroscopy and TPD the effect of vanadium content on the relative proportion of strongly acidic sites of V₂O₅/Al₂O₃ catalyst was studied.

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- - V₂O₅/Al₂O₃.

     

Temperature-programmed reduction of CuO?NiO/Al2O3 catalysts

Reducibility of NiO/Al₂O₃ and CuO–NiO/Al₂O₃ catalysts has been studied by the TPR method within the temperature range 293–873 K. The results suggest that the copper content essentially does not influence the reducibility of NiO/Al₂O₃.

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NiO/Al₂O₃ CuO–NiO/Al₂O₃ TPR 293–873 . , NiO/Al₂O₃.

     

Effect of reduction of bismuth molybdate Bi2(MoO4)3 on its activity in isomerization of butene-1 to butenes-2

The reduction of bismuth molybdate Bi₂(MoO₄)₃ by hydrogen increases its activity in isomerization of butene-1 to butenes-2 due to the activation effect of oxygen vacancies.

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Bi₂(MoO₄)₃ -І -2, .

     

Temperature programmed desorption of NH3 and H2O from NH4NaX and CoNH4NaX zeolites

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.

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- () NH₃ H₂O NH₄X CoNH₄X . NH₃ NH₃ =qs . . Co²⁺ CoNH₄X.

     

Acid-base properties of Al2O3/MgO oxides, V. Decomposition of diacetonealcohol

The activity of MgO–Al₂O₃ mixed oxides in the decomposition of diacetonealcohol was studied using a micro slurry reactor, which allowed pretreatment of the catalyst in situ. The rate constant was used to characterize the strength of the basic surface sites. A reaction order of one and a decrease of the rate constant from MgO to Al₂O₃ was observed.

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MgO–Al₂O₃ . , . . MgO Al₂O₃.

     

Studies on nickel oxide mixed catalysts, V. Propene dimerization on Nio?Al2O3/SiO2 catalysts

The catalytic activity of various NiO–Al₂O₃/SiO₂ catalysts has been investigated in a tubular fixed-bed reactor at high pressure. High selectivities to propene dimers were obtained on catalysts with a high Ni/Al ratio. The surface acidity of the catalysts influences strongly the selectivity and the product distribution.

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NiO–Al₂O₃/SiO₂ . , Ni/Al . .

     

13C NMR studies of the interaction of CO with H2 over Rh/La2O3 catalyst

¹³C NMR studies have revealed that the interaction of CO with H₂ over a Rh/La₂O₃ catalyst yields surface particles containing carbonyl groups. Depending on the CO/H₂ ratio, carbonyl groups transform to various products: either alcohols and ethers or acids and esters.

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¹³C , CO H₂ Rh/La₂O₃ , . CO H₂ : .

     

Performance of a cobalt oxide catalyst in the oxidation of NH3 to NO

The cause for a fall in the conversion of NH₃ to NO within 73 hours from 97% to 78% with a cobalt oxide catalyst was investigated. Results show that sintering, change in valence and cation distribution in Co₃O₄ contribute to the decrease in activity. Incorporation of ThO₂ and K₂O improves the performance of the catalyst.

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NH₃ NO 73 97% 78%. , , Co₃O₄. ThO₂ K₂O NH₃ NO.

     

ESR characteristics of paramagnetic species on Pd/La2O3 catalysts

Reduction of Pd/La₂O₃ catalysts by H₂ and CO at room temperature leads to the formation of Pd⁺ ions stabilized in bulk and the subsurface layer. Hydrogen spillover seems to enhance the process. O ₂ ^– and (CO) ₂ ^– radicals are formed after adsorption of CO and O₂ at 295 K.

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Pd/La₂O₃ CO Pd⁺ . . CO O₂ (CO) ₂ ^– O ₂ ^– La₂O₃.