Interaction of V2O5 with oxygen in the gas phase

Sorption/evolution of oxygen from V₂O₅ in the temperature range of 480–520°C is due to a shift in the defect equilibrium 1/2 O₂ (gas)+V_oO_o. A first-order kinetic equation can be derived under the assumption that the activation energy depends on the concentration of defects.

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/ V₂O₅ 480–520°C 1/2 O₂ ()+V_oO_o. , , .

     

Experimental study of the initial stage of Li2SO4·H2O single crystal dehydration in vacuum

The initial stage of the Li₂SO₄·H₂O single crystal isothermal dehydration has been studied by means of quartz crystal microbalance. As found, weight loss in the initial process may be considered as H₂O molecule diffusion from a semiinfinite medium. The numerical values of the H₂O molecule diffusion in Li₂SO₄·H₂O have been calculated from the results obtained.

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. - - - -. - Li₂SO₄·H₂O.

     

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) ; .

     

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. .

     

Catalysts for metathesis of olefins obtained through [Mo3O4(C2O4)3 (H2O)3]2? coordinated to γ-Al2O3

New highly active catalysts for the metathesis of olefins have been obtained through the interaction of [Mo₃O₄ (C₂O₄)₃ (H₂O)₃]^2– anion with Al₂O₃ surface and further activation in H₂ or CO atmosphere.

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[Mo₃O₄ (C₂O₄)₃ (H₂O)₃]^2– Al₂O₃ H₂ CO .

     

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, . . . .

     

Kinetics of CO2 formation in thermal destruction of brown coals

The previously suggested approach to the problem of kinetic system identification /1/ was used for the system of independent first order reactions. The analysis of the curves of CO₂ formation in thermal destruction of brown coal indicates that both structure and model parameters of real processs can be identified in terms of the continuity concepts.

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(I) ë . CO₂ , , .

     

n-Hexane cracking over heteropoly acids, 2. Catalytic activity and thermal stability of H4SiW12O40, H6P2W18O62 and H6P2W21O71(H2O)3

The catalytic activity of three heteropoly acids has been studied in n-hexane cracking. Only H₄SiW₁₂O₄₀ does not decompose into oxides at the reaction temperature. Its acidic form is active in cracking but its dehydration leads to an inactive compound.

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-. H₄SiW₁₂O₄₀ . , .

     

Temperature-programmed hydrogen desorption from water on bimetallic catalysts Ir?Fe/Al2O3

Desorption of hydrogen liberated in the process of water decomposition on bimetallic catalysts (3% Ir–Fe/Al₂O₃) at linear temperature growth was observed. In the case of iridium the amounts of desorbing hydrogen are relatively small, whereas for iron they are many times greater.

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, 3% Ir–Fe/Al₂O₃ . , , .

     

Influence of the crystallite size of platinum of the course of hydrogenolysis of ethane and propane over Pt/Al2O3 catalysts

The effect of the degree of platinum crystallite size on the reaction rate, selectivity and activation energy of ethane and propane hydrogenolysis has been studied in the range of platinum crystallite size of 1.7–4.0 nm. In the same range of Pt crystallite size, the activation energy of both processes shows a clear minimum. The decrease in Pt crystallite size bellow 3.0 nm brings about rapid changes in the selectivity of propane hydrogenolysis.

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( ) , -. 1,7–4,0 , .

     

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.

     

Influence of the chlorine content of Al2O3 on its catalytic activity and coke formation

The catalytic activities of aluminas with different chlorine contents for cumene cracking, o-xylene isomerization, n-hexane isomerization and cracking and methylcyclopentane cracking were studied. The catalytic activity and the acidity increase continuously when the chlorine content increases. Coke formation is only noticiable with methylcyclopentane, increasing with the chlorine content of the alumina.

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, -, - . . - , - .

     

Studies on the V2O5?TiO2 system, V. Equilibrium pressures

The oxygen equilibrium pressures from pure V₂O₅ and co-precipitated V₂O₅–TiO₂ system were measured in the range of 200–450 °C. The behavior of the equilibrium pressure with changes of temperature of the samples with and without TiO₂ is attributed to Ti⁴⁺ interaction with the V₂O₅ lattice.

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V₂O₅ - V₂O₅–TiO₂ 200–450°C. TiO₂ Ti⁺⁴ V₂O₅.

     

Reactivity of the CCl3CH2CH2. radical in processes of homo-and cotelomerization of olefins with carbon tetrachloride

From the kinetic studies of CCl₃CH₂CH₂Br addition to 1-hexene, the rate constant of addition of the CCl₃CH₂CH ₂ ^. ( _e ¹ R) radical to 1-hexene [1g _e ¹ k_h=(5.2±0.1)–(13 000±800)/RT] has been determined. From the cotelomerization data, rate constants of the interaction of _e ¹ R-radical with ethylene [1g _e ¹ k_e=(6.1±0.2)–(21 400±1 200)/RT] and carbon tetrachloride [1g _e ¹ k_t=(7.5±0.2)–(37 000±1 200)/RT] have been calculated.

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CCl₃CH₂CH₂Br 1-. CCl₃CH₂CH ₂ ^. - _e ¹ R^.)- 1- (1g ¹ K=(5,2±0,1)–(13 000±800)/RT), 1- , ¹ R- (1g ¹ K=(6,1±0,2)–(21 400±1200/RT) CCl₄ (1g ¹ K=(7,5±0,2–(37 000±1 200)/RT).

     

Toluene steam dealkylation over Rh/Al2O3. Effect of the support

Rh catalysts supported on different -aluminas were prepared and tested under identical conditions. Both catalytic activity and selectivity seem to depend on the surface concentration of acid sites. The bifunctional character of the catalyst and the role played by the support in activating the reactants are confirmed.

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, - . , . , .

     

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.

     

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-.

     

Influence of Zr, Ge, B and Co additives on the activity of Pt/Al2O3 catalysts for dehydrocyclization

IR studies of the effect of Zr, Ge, B and Co additives on the activity of the Pt/Al₂O₃ catalyst for dehydrocyclization have revealed their promoting action on both oxidation and reduction of platinum. Benzene yield depends on the degree of platinum reduction promoted by boron, whereas with increasing platinum oxidation, the cracking product yield decreases.

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, , . , . . . .

     

Kinetics of tritium isotope exchange between H2S and CH3OH vapor in glass vessels

Two different mechanisms of tritium exchange between and CH₃OH vapor in glass vessels have been found: (i) bimolecular exchange in the gas phase, (ii) pseudomonomolecular exchange between gaseous and CH₃OH adsorbed on the surface. The total and partial orders, rate constants and activation energies are given.

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, CH₃OH , : 1) 2) CH₃OH, . , .

     

ESR study of SO2 on MnO2-alumina

SO ₃ ^– radicals are formed during the reaction between SO₂ and MnO₂-alumina, which suggests that SO ₃ ^– take part in the reduction of Mn⁴⁺ to Mn²⁺.

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SO₂ MnO₂/Al₂O₃ SO ₃ ^– , , SO ₃ ^– Mn⁴⁺ Mn²⁺.