Catalytic hydrogenation of carbon monoxide on RuFe/SiO2 catalysts

The H₂+CO reaction on silica supported Ru, Fe and RuFe catalysts prepared from metal carbonyl clusters has been investigated under atmospheric and 20 bar pressure. According to the change of selectivity values with temperature and with pressure, the participation of surface carbon proposed earlier by several authors seems to be confirmed by this work.

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H₂+CO Ru, Fe RuFe, , 20 . , , , .

     

A new method for preparation of Mo/Al2O3 catalysts for olefin metathesis

A new method of preparation of highly active catalysts for metathesis of -olefins through the anchoring of [Mo₂O₄(C₂O₄)₂(H₂O)₂]^2– anion to the surface of -Al₂O₃ with further thermal activation in H₂ and CO is proposed.

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- [Mo₂O₄(C₂O₄)₂(H₂O₂]^2– -Al₂O₃ H₂ CO.

     

Acio-Base properties and actvity of complex oxide catalysts for m-xylene ammoxidation

Introduction of small quantities of alkaline and alkalineearth metal oxides into supported Sb–Bi–V oxide catalysts increasses the concentration of surface basic centers and increases significantly its activity in m-xylene ammoxidation. Promoting effect is suggested to be due to the heterolytic type of the primary activation of hydrocarbon.

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- -. .

     

Structure sensitivity and coke formation on Pt/Al2O3 catalysts

The initial rate of carbon formation during cyclopentane reaction has been studied on different Pt/Al₂O₃ catalysts of varying metal dispersity. It has been shown that coke deposition on the metal is a structure sensitive reaction which is preferably produced on large metallic particles. On the other hand, coke deposition on the whole catalyst is relevant to cyclopentadiene formation and is a structure insensitive reaction since the initial rate of coke deposition on the whole catalyst is proportional to the metallic surface area.

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Pt/Al₂O₃ . , , . , , , .. .

     

Lattice oxygen removal from V6O13 by the TPD method

Removal of the lattice oxygen from the V₆O₁₃ phase has been measured and the activation energy determined.

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V₆O₁₃ .

     

n-Hexane cracking over heteropoly acids, 1. Treatment of data and temperature dependence of the catalyitc activity of H3PW12O40

The catalytic activity of H₃PW₁₂O₄₀ has been investigated in n-hexane cracking as a function of the reaction temperature. It has been shown that both the polyacid and the anhydride phase formed by its dehydration are active catalysts for this reaction.

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H₃PW₁₂O₄₀ - . , , , , .

     

X-ray studies of ZSM-5 zeolites with framework cations of various sizes

From a comparison of the X-ray difractograms for various ZSM-5 zeolites the isomorphous substitution of framework Si⁴⁺ by large cations (Al³⁺, Ga³⁺, Fe³⁺) is suggested to be ordered as contrasted to the statistical substitution by small ones (B³⁺).

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ZSM-5 , Si⁴⁺ (Al³⁺, Ga³⁺, Fe³⁺) , (B³⁺).

     

Temperature-programmed reduction of bimetallic Ir?Fe/Al2O3 catalysts

Investigations on the temperature-programmed reduction of 3% Ir–Fe/Al₂O₃ catalysts after their oxidation at different temperatures T_ox have been carried out. A substantial promoting effect of iridium on the reducibility of iron has been observed for all the investigated catalysts, at T_ox applied.

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- 3% Ir–Fe/Al₂O₃ (T_ox). T_ox.

     

Chlorination of V2O5 by CCl4. The proposed reaction mechanism

Initial stage of the reaction of CCl₄ with V₂O₅ has been studied by MS and XPS techniques. According to the proposed mechanism dissociatively chemisorbed CCl₄ transforms to CO₂ via adsorbed COCl₂, while surface vanadium atoms involved are gaining step by step two chlorine atoms before the formation of the volatile end-product VOCl₃.

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CCl₄ V₂O₅ . - CCl₄ CO₂ COCl₂, VOCl₃.

     

51V-,29Si- and27Al-NMR studies of the interaction of active component of vanadium catalysts for SO2 oxidation with supports

NMR studies have revealed that silicas and aluminosilicates interact with the active components of vanadium catalysts, in the former case merely yielding surface compounds.

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, , .

     

Hydrogenation of CO2

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.

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CO₂ : Fe/MgO, Ni/Ti, Cr/Zn . 15 250–350°C. : RGWS, F.T. .

     

Mechanism of methane photooxidation on V/SiO2 catalyst

CH₄ photooxidation on V/SiO₂ catalyst in the presence of gaseous oxygen has been studied by the mass-spectometric method. It has been established that CO₂ forms due to the interaction of CH₄ with surface oxygen anions bonded to vanadium ions. Photodecomposition of V⁴⁺O ₂ ^– species formed in O₂ adsorption on reduced vanadium ions leads to the reoxidation of the latter.

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- CH₄ V/SiO₂ . , CO₂ CH₄ , . V⁴⁺O ₂ ^– O₂ , .

     

Non-catalyzed oscillation reaction in aniline-KBrO3?H2SO4 system, I. Potentiometric study of oscillations

The non-catalyzed oscillation reaction of the aniline-KBrO₃–H₂SO₄ system has been followed potentiometrically. The concentration regions of the beginning of oscillation are given in a triangular diagram. Also studied was the dependence of the induction period on concentration of the participants, which was described by a kinetic equation. The oscillation region extends to lower KBrO₃ concentrations, the number of the oscillation jumps increases, and the induction period is shortened with increasing acidity.

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-KBrO₃–H₂SO₄. . . KBrO₃, .

     

Synthesis and properties of composite catalysts containing Pd and Ho2O3 particles in pores of carbon carrier

Specific activity (TOF) of the catalysts prepared through the interaction of C₃H₅PdC₅H₅ with the surface of evacuated Ho₂O₃/C is two orders of magnitude higher compared to that of Pd/C in the synthesis of both CH₃OH and CH₄. Deactivation data suggest that CH₃OH and CH₄ are formed on different active sites.

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, C₃H₅PdC₅H₅ Ho₂O₃/C, Pd/C CH₃OH, CH₄. CH₃OH CH₄ .

     

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. . , , .

     

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 , .

     

Influence of porous support structure and active component composition on deactivation of vanadium catalysts in SO2 oxidation

The effect of porous support structure and active component composition of vanadium catalysts on the crystallization character of this component has been studied in SO₂ oxidation at low temperatures and conversion degrees. The tendency to crystallization is shown to drop with decreasing support pore radius and with increasing K/V molar ratio.

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. , K/V.

     

Chemical oscillatory reaction in a hydrodynamic oscillator

The periodic mixing of the reactants (bromate-thiocyanate or bromate-hydroxylamine) by the hydrodynamic oscillator gives rise to both periodic and aperiodic chemical oscillations.

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(- -) , .

     

Mass-spectrometric analysis of SO3 in SO2 oxidation over vanadium catalysts

The detailed composition of the reaction mixture and, in particular, SO₃ concentration, in SO₂ oxidation over vanadium catalysts, have been determined experimentally. Both oxidized and reduced catalysts were shown to absorb a considerable amount of SO₃, the desorption rate of SO₃ being lower than that of its adsorption.

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, , . , , SO₃, .

     

Kinetics of SO2 oxidation on K2S2O7?V2O5 catalyst in non-steady conditions

Studies of SO₂ oxidation on a molten component of vanadium catalysts in non-steadystate conditions indicates that the kinetics agree fairly well with an oxidation-reduction mechanism. In the low temperature range (<790 K) tetravalent vanadium can be partially crystallized.

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. , - . ( 790 ) .