Interaction of nitric oxide with NiCr2O4

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.

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473–1173 NO NiCr₂O₄. , NO . (II) ; .

     

CO/H2 and CO2/H2 reactions with amorphous carbon-metal catalysts

By metal impregnation of selected naturally occurring organic materials followed by controlled carbonization, metal semicoke catalysts can be readily prepared. These catalysts have been tested in the synthesis of hydrocarbons and alcohols from CO/H₂ and CO₂/H₂ mixtures. Fe and Co preparations have been used. Relatively high temperatures are required when using these catalysts, which are quite active for synthesis using CO₂ and H₂. The pressure (5150 kPa) is very favorable both for the synthesis of liquid hydrocarbons (C₅–C₃₀) and alcohols (C₁–C₅).

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. CO/H₂ CO₂/H₂. Fe Co. , CO₂ H₂. 5150 ) (C₅–C₃₀) (C₁–C₅).

     

X-ray study of Re/Al2O3 and Re+Pt/Al2O3 catalysts using synchrotron radiation

Uning synchrotron radiation, L_III rhenium absorption spectra have been studied for Re/Al₂O₃ and Re+Pt/Al₂O₃ catalysts obtained by impregnation. For individual rhenium compounds a linear dependence between the shift of absorption edge and the state of rhenium oxidation has been found. The absorption spectra of reduced catalysts are significantly broadened as compared with those of individual compounds of the same valency. This points to the presence of rhenium compounds in different oxidation states.

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L_III- , Re/Al₂O₃ Re+Pt/Al₂O₃, . . . .

     

Effect of alkali metal ions on the catalytic of Pd/SiO2?AlPO4 systems

The effect of different alkali metal hydroxides on the metallic dispersity and catalytic activity of SiO₂–AlPO₄ (8020, by mass) supported palladium catalysts has been studied. The reduction by hydrogen transfer of benzylideneacetone and styrene (using cyclohexene and n-octanol, respectively, as hydrogen donors) and the liquid phase reduction of cyclohexene at low pressure (5 bar) in a Parr type reactor have been used as test reactions to follow changes in the catalytic activity.

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(SiO₂–AlPO₄/8020 ). ( n-, , , (5 ) .

     

Non-conventional preparation of Ru/SiO2 catalysts

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.

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(Ru/SiO₂) -. .

     

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.

     

Preparation of active platinum hydrogenolysis catalyst supported on TiO2 phase dispersed on SiO2

Platinum catalysts supported on a TiO₂ phase well-dispersed on SiO₂ (TiO₂/SiO₂) exhibited a high activity for butane hydrogenolysis; activity was 12 orders of magnitude higher than those of platinum catalysts supported on SiO₂ and TiO₂.

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Pt, TiO₂, SiO₂ (TiO₂/SiO₂), ; 12 , SiO₂ TiO₂.

     

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.

     

X-ray spectral investigation by synchrotron radiation of supported Re/SiO2 and (Re+Pt)/SiO2 catalysts prepared via triethoxyrhenium

Using synchrotron radiation L_III absorption spectra of rhenium in Re/SiO₂ and (Re+Pt)/SiO₂ catalysts prepared via triethoxyrhenium have been studied. The conclusion has been drawn that reduced catalysts contain lowvalent rhenium ions and their composition is more uniform than that of the previously examined catalysts Re/Al₂O₃ and (Re+Pt)/Al₂O₃ prepared by a conventional impregnation technique.

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L_III- Re/SiO₂ (Re+Pt)/SiO₂, . , , Re/Al₂O₃ (Re+Pt)/Al₂O₃, .

     

Reactivity of electronically excited Br(2P1/2) atoms towards CH3F

The rate constants for Br(²P_1/2) and Br(²P_3/2) 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.

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Br(²P_1/2) Br(²P_3/2) Br+CH₃FHBr+CH₂F CH₃F. 60–200 °C 10^{–(2,6±0,5)} exp (10100±1000/RT).

     

Cyclohexene transformations over the TiCl4?Al2O3 system

Cyclohexene oligomerizes over the TiCl₄–Al₂O₃ system at 423 K. The length of the oligomer chain depends on the number of TiCl₃O–Al–groups on the alumina surface.

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TiCl₄–Al₂O₃ 423 . TiCl₃O–Al .

     

Sorption of H2, O2 and CO on bimetallic catalysts Pd?Ag/Al2O3 over a wide temperature range

Adsorption of hydrogen, oxygen and carbon monoxide on Pd–Ag/Al₂O₃ catalysts of different compositions within the temperature range from 293 to 773 K has been investigated. Adsorption measurements have been carried out by the pulse chromatographic method. The results obtained reflect interactions of the above adsorbates with the alloy surface, strongly enriched in silver atoms, as a result of surface segregation processes.

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, Pd–Ag/Al₂O₃ 293–773 K. . , , .

     

Intramolecular cyclization of Z,E,E-1,5,9,-cyclododecatriene by the Cp2TiCl2?LiAlH4 system

The system Cp₂TiCl₂–LiAlH₄, in the absence of ethereal solvents, catalyzes the intramolecular cyclization of Z,E,E-1,5,9-cyclododecatriene, yielding a mixture of C₁₂ hydrocarbons consisting mainly of cis, anti, cis-and cis, syn, trans-tricyclo [7.3.0.0^2,6] dodec-7-ene and 5,6,7,8,9,10-hexahydrobenzocyclooctene.

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Cp₂TiCl₂–LiAlH₄, , Z,E,E,-1,5,9-, C₁₂, , , - , , - [7.3.0.0.^2,6] -7, 5,6,7,8,9,10-.

     

Catalytic properties of Ni/WS2 samples in thiophene hydrogenolysis

The interaction of diallylnickel with WS₂ produces catalysts whose activity is 10–50 times higher than that of the parent sulfide. The atomic catalytic activity referred to supported nickel is independent of the catalyst type and the sulfur removed in temperature programmed reduction.

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, WS₂ , 10–50 . , , .

     

Effect of electronic interaction between metal and support: How the nature of Ru/Al2O3 is modified

It is a well known fact that when supported on different supports, a transition metal may show different catalytic behavior. In some cases it is claimed that the differences in the acidity of supports are due to this phenomenon. In this work, by adding increasing amounts of MgO to Al₂O₃, the number of acid sites and hence the acidity of Al₂O₃ were monotonically decreased. The behavior of Ru supported on these mixed supports was investigated with IR, and it is concluded that the interaction between metal and acid sites on the surface is the most important factor for the changing properties.

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, , . . Al₂O₃ MgO Al₂O₃. Ru -, , -.

     

Gas-phase hydrogenation of styrenes by transfer over Pd/AlPO4 catalysts

This paper reports the results obtained in the hydrogenation of styrene and -methylstyrene by transfer over Pd catalysts supported on AlPO₄, using cyclohexene as donor. The catalysts were activated in the pulse reactor itself and retained hydrogen which was subsequently used to reduce the olefins. The amount of ethylbenzene yielded from styrene can be accounted for on the basis of hydrogen transferred in a concerted fashion by cyclohexene and hydrogen stored over the catalyst surface during treatment with cyclohexene intended to reduce the impregnating metal salt.

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- , AlPO₄, . . , , , , .

     

Molecular isotope exchange of14CO in surface carbonyl complexes of rhodium

Molecular isotope exchange of CO with¹⁴CO for Rh₆(CO)₁₆/Sn(II)–SiO₂, Rh₆(CO)₁₆/Al₂O₃, Rh(I)(CO)₂/Al₂O₃, Rh₄(CO)₁₂/Al₂O₃ carbonyl complexes of rhodium has been studied. Estimates of the activation energies and a mechanism of the CO exchange are suggested.

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, (Rh₆(CO)₁₆/Sn(II)–SiO₂, Rh₆(CO)₁₆/Al₂O₃, Rh^I(CO)₂/Al₂O₃, Rh₄(CO)₁₂/Al₂O₃), ¹⁴CO. CO .

     

High-temperature reduction of SO2 by methane at various CH4/SO2 ratios

The character of the effect of initial reaction mixture and temperature on the selectivity of catalytic reduction of sulfur dioxide by methane in the presence of oxygen has been studied.

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.

     

Catalytic hydrogenation of olefins with the VCl4?Mg?H2 system in tetrahydrofuran

The hydrogenation of olefins with the VCl₄–Mg–H₂ system in tetrahydrofuran was examined. The yield was found to depend on the Mg: VCl₄ mole ratio. The maximum yield of cyclohexene hydrogenation is achieved at C₆H₁₀/VCl₄=4. Addition of AlCl₃ or triphenylphosphine increases the yield of hydrogenation to a mole ratio C₆H₁₂/VCl₄=7.

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: VCl₄–Mg–H₂ . , Mg:VCl₄. C₆H₁₀/VCl₄=4. AlCl₃ C₆H₁₂/VCl₄=7.

     

Effect of iron on the behavior of Fe2O3?MoO3/SiO2 ammoxidation catalysts

Catalytic ammoxidation of propylene was studied using Fe₂O₃–MoO₃/SiO₂ catalysts, which have been prepared following a special method. Interaction of ammonia with the catalysts was studied by means of IR spectroscopy and gravimetrically using a McBain balance. Introduction of iron into MoO₃/SiO₂ catalysts modifies acidic as well as redox properties.

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Fe₂O₃–MoO₃/SiO₂ . . - . MoO₃/SiO₂ , .