Effect of oxygen on NO reduction over nickel chromite catalysts

Reduction rates of NO_x in HO_x+CO(H₂)+O₂ mixtures over a pure nickel chromite catalyst and samples supported on -Al₂O₃ and faience are high. At a space velocity of 10,000 h^–1, the complete reduction of nitrogen oxides by hydrogen and by carbon monoxide is achieved at 400–450°C and 450–500°C, respectively. Hence these catalysts can be recommended as a basis to develop commercial catalysts for NO_x removal from oxygen-containing exhaust gases.

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-Al₂O₃ NO_x NO_x–CO (H₂)–O₂ . 10 ·^–1 400–450°C, — 450–500°C. .

     

Partial kinetic models in the H2?O2 system

Using the concepts of maximum mechanism and non-equilibrium free energy, some partial kinetic models of hydrogen oxidation have been found by means of solving a direct kinetic problem. It is shown that the basic difference in the kinetic models of ignition is the initial period of the process (induction period) while the mechanism of the well-developed process slightly depends on the initial conditions and remains mainly the same for the parameters under study.

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H₂–O₂ ( ) . , ( ), , .

     

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 . -, -, - .

     

On the classification and coding of linear reaction mechanisms

Non-oriented kinetic graphs are classified and coded according to their topological properties.

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Reported in part at The 5th All-Union Meeting on Homogeneous Catalysis, Alma-Ata, October 1979     

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.

     

Methods for finding steady-state solutions of mathematical models for chemico-technological schemes

Gradient and Newton methods are suggested for searching for steady-state solutions of chemico-technological schemes to obtain synthetic fuels.

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- .

     

Relative rate coefficients of⊙OH-radical interactions in nonaqueous medium

For measuring relative rate coefficients of OH-radical reactions in organic media a competitive method has been used. As reference, 2-propanol was applied. For ethylbenzene and 1-phenylethanol the rate coefficients of H-abstraction relative to that of 2-propanol are 1.4 and 2.9, respectively.

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OH. 2-. H 1-, 2-, 1,4 2,9, .

     

On the catalytic system MgO?Na

Acid-base and radical properties of two sets of MgO–Na catalysts have been studied. The catalysts were prepared (I) by impregnation of MgO with NaOH in aqueous solution, and (II) by evaporation of metallic sodium onto a MgO surface. The catalyst prepared by the second method was much more basic than pure MgO (H_o=35) and showed a high activity in olefin isomerization.

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- MgO–Na. 1) MgO (NaOH) 2) MgO. , , , MgO(H₀=35), .

     

Mass-spectrometric detection of an unstable product in silver-methanol interaction

The low pressure interaction of methanol vapors with a silver catalyst was studied by mass spectrometry. An unstable product contributing to m/e-15 was detected in this reaction. While yield of formaldehyde increased with addition of oxygen, the unstable product showed towards oxygen a reversed, decreasing trend.

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- , m/e=15. , .