Performance of Pt?Sn/Al2O3?Cl catalysts in isopropanol decomposition

Highly dispersed TiO₂-supported copper with strong interactions with the support has been prepared. After reduction at 770 K, H₂ chemisorption is suppressed. Two types of copper sites exist, one easily and reversibly oxidized by O₂ at room temperature, and another interacting with the support.

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, TiO₂, . 770 H₂ . , O₂ , - .

     

Dispersity and reducibility of the molybdenum oxide phase in SiO2, SiO2?Al2O3 and γ-Al2O3 supported molybdena catalysts

XRD, isothermal and temperature-programmed reduction (TPR) experiments were carried out with SiO₂, SiO₂–Al₂O₃ and -Al₂O₃ supported catalysts. Molybdena is in a more disperse state on supports containing more alumina and it is more reducible on SiO₂–Al₂O₃ than on SiO₂ or -Al₂O₃. TPR curves were shown to reflect connections between reduction kinetics and dispersity.

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-, , SiO₂, SiO₂–Al₂O₃ -Al₂O₃. , , SiO₂–Al₂O₃ SiO₂ -Al₂O₃. .

     

On the deactivation of Fe2O3?MoO3/SiO2 catalysts in the oxidation of methanol to formaldehyde

The deactivation behavior of Fe₂O₃–MoO₃/SiO₂ catalysts with different Fe₂O₃+MoO₃ content in the oxidation of methanol to formaldehyde is investigated. A simplified reaction-deactivation kinetic model is presented and used to compare and discuss the different behaviors.

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Fe₂O₃–MoO₃/SiO₂ Fe₂O₃+MoO₃ . : -.

     

Effect of Sn addition on the catalytic properties of the metallic phase in Pt?Sn/Al2O3 catalysts

Platinum-tin/alumina supported catalysts have been studied. The TPR results show an assisted reduction of tin by platinum. The effect of alloying in cyclohexane dehydrogenation, o-xylene hydrogenation and cyclopentane hydrogenolysis is discussed.

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- , . . , - .

     

IR spectra of NO and NO+CO mixtures adsorbed on Fe2O3

The interaction of NO and NO+CO mixtures with Fe₂O₃ has been studied by IR spectroscopy. The conclusion has been made that adsorption bands in the region of 1200–1700 cm^–1 belong to nitrite-nitrate structures, the band at 1810 cm^–1 characterizes catalytically active particles of NO adsorbed on reduced surface sites, Fe²⁺, the bands at 2210 and 2240 cm^–1 are due to vibrations of gaseous N₂O.

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- NO NO+CO Fe₂O₃. , 1200–1700 ^–1 - ; 1810 ^–1 NO, , Fe²⁺; 2210 2240 ^–1 N₂O.

     

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 , .

     

Kinetics of oxidative sulfonation of butylamine in the presence of CuCl2

Kinetic regularities of butylamine sulfonation to N, N-dibutylsulfamide in the presence of copper(II) chloride have been studied. Reaction mechanism involves the formation of Cu(II) amine complexes, their subsequent interaction with SO₂ and the redox decomposition of an intermediate to final products.

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N-N- (II). Cu(II), SO₂ - .

     

Kinetics and mechanism of hydrazine oxidation by oxygenated Co2(L-his)4O2 complex

The kinetics of Co₂ (L-his)₄O₂ reduction by hydrazine in aqueous solution has been studied and the rate constants, the energy and entropy of activation have been determined.

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, , Co₂ (L-)₄O₂ .

     

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.

     

Rate of14N2 desorption from the surfaces of nitrides in the presence and absence of15N2 in the gas phase

The rates of¹⁴N₂ desorption from the surfaces of nitrides have been measured in the presence and absence of¹⁵N₂ in the gas phase. Whatever the adsorption heat and the form of surface species, the adsorption of¹⁵N₂ molecules does not affect the rate of¹⁴N₂ desorption.

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¹⁴N₂ ¹⁵N₂ . , ¹⁵N₂ ¹⁴N₂.

     

Sorption of palladium chloride complexes on Al2O3 surface

Three types of sorption interactions with the corresponding Pd aquachlorocomplexes [Pd(H₂O)₂Cl₂]⁰, [Pd(H₂O)Cl₃]^– and [PdCl₄]^2– have been discovered on -Al₂O₃ at surface concentrations for the active component and the competing HCl ranging within 0.05–1.25 and 1.2–4.8 mol m^–2, respectively.

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0,05–1,25 /² 1,2 4,8 /² -Al₂O₃ , : [Pd(H₂O)₂Cl₂]⁰, [Pd(H₂O)Cl₃]^– [PdCl₄]^2–.

     

Reactivity of coordinated O2? ion-radicals in the oxidation of organic compounds

By the flow ESR method, the rates of the reaction of the radical complex Ti(IV)(O ₂ ^– ) with some aromatic compounds in aqueous solution have been measured. An elementary step of these reactions seems to be one-electron oxidation with the formation of a substrate cation-radical.

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- Ti(IV)(O ₂ ^– ) . - -.

     

Sulfurization of Pt/Al2O3?Cl catalysts. IV. Adsorption sites of H2S on Al2O3, Al2O3?Cl and Pt/Al2O3?Cl

Chemisorption of H₂S on Al₂O₃, Al₂O₃–Cl and Pt/Al₂O₃–Cl has been studied by gravimetry and IR spectroscopy. The influence of the amount of Cl on the H₂S adsorption equilibrium value and the nature of the adsorption sites at low and high coverages are discussed.

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H₂S Al₂O₃, Al₂O₃–Cl Pt/Al₂O₃–Cl . Cl H₂S, .

     

Catalytic activity of the CaO?CaF2 system

Cao–CaF₂ catalysts containing 0–100%CaF₂ have been studied concerning their activity in different reactions. Maxima of activity for butene isomerization and isopropanol decomposition as well as selectivity for the alcohol dehydration were found for the sample with equimolar ratio of the components. No sample was active in cumene cracking. Suggestions are made concerning the reaction mechanisms and the active centers involved.

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CaO–CaF₂, 0–100% CaF₂, . , , . . .

     

Stopped-flow study of the oxidation of ascorbic acid by the oxo-bridged trinuclear ruthenium complex [(NH3)5RuORu(NH3)4 ORu(NH3)5]7+

The kinetics of the oxidation of ascorbic acid by [(NH₃)₅RuORu(NH₃)₄ORu(NH₃)₅]⁷⁺ has been studied by the stopped-flow method. The activation parameters have been calculated and a possible mechanism is suggested.

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[(NH₃)₅RuORu(NH₃)₄ORu·(NH₃)₅]⁷⁺ . .

     

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 - . , , , , .

     

Influence of added copper on the activity of Ni/Al2O3 catalysts in the hydrogenolysis of n-butane

The influence of small Cu admixture to the Ni/Al₂O₃ system on its activity in the hydrogenolysis of n-butane was studied in the temperature range of 723–573 K. The activity was measured in a gradientless reactor. Cu added to Ni/Al₂O₃ was found to have a strong influence on the overall activity, selectivity and ratio for n-butane hydrogenolysis. A mechanism of hydrogenolysis of n-butane on the Ni–Cu/Al₂O₃ system is proposed.

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Cu Ni/Al₂O₃ - 723–573°. . Cu Bi/Al₂O₃ -. - Ni–Cu/Al₂O₃.

     

Cyclohexane photooxygenation by air oxygen in CH2Cl2 in the presence of chromium oxocomplex-iodosylbenzene system

Cyclohexane is oxidized by air oxygen in CH₂Cl₂ solution to yield cyclohexanol, cyclohexanone and cyclohexyl chloride when irradiated by light (>310 nm) in the presence of (Bu₄N)₂CrO₄ or (Bu₃SnO)₂CrO₂. The addition of PhIO greatly accelerates the reaction and increases the yield of products. The reaction mixture contains neither cyclohexanol nor cyclohexanone when the photoreaction in the presence of the Cr(VI)–PhIO system is carried out in argon atmosphere. Hence neither iodosylbenzene nor oxochromium compounds can be oxygen atom donors in alkane oxygenation. The accelerating effect of iodosylbenzene may be due to the enhanced oxidizing power of photo-excited oxochromium species when coordinated to iodosylbenzene.

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CH₂Cl₂ , , (>310 ) (Bu₄N)₂CrO₄ (Bu₃SnO)₂CrO₂. PhIO . Cr(VI)–PhIO , , . , ( ) . .

     

Electronic spectral study of the interaction of CoNaX zeolite with C1?C5 hydrocarbons

Interaction of both satured and unsaturated hydrocarbons with tetrahedral Co²⁺ ion complexes lodged in the zeolite skeleton is reported on the basis of diffuse reflectance spectra. While saturated hydrocarbons do not affect the coordination sphere of the Co-complex, the unsaturated hydrocarbons change considerably the distortion of the tetrahedral Co-complex.

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- Co²⁺ - . - Co-, - - Co-.

     

Kinetics of Co?Mo/Al2O3 catalyst reduction

According to kinetic studies on the reduction of commercial Co–Mo/Al₂O₃ and model catalysts in H₂ at 523–773 K, the kinetic curves for the reduction process have been determined. The reduction rate is shown to be higher for the commercial catalyst. Activation energies E_act for the reduction of several forms of Mo and Co in Co–Mo/Al₂O₃ catalysts are presented.

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H₂ 523–773 . , : Mo Co .