Hydrogenation of CO2 on Fe/carbon catalysts

The hydrogenation of CO₂ on activated carbon-supported iron catalysts has been carried out at atmospheric pressure and using a H₂/CO₂ ratio of 4. The specific activities for this reaction are lower than those obtained for the Fischer-Tropsch synthesis using the same catalysts. CO and CH₄ are the only products obtained in the hydrogenation of CO₂ under the experimental conditions used. The apparent activation energies determined for the production of CO are lower than those for the production of CH₄.

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CO₂ , , H₂/CO₂=4. , - . CO CH₄ , CO₂ . - CO , CH₄.

     

Reactions of butane and isobutane to CO and CO2 catalyzed by iron oxide treated with sulfate ion

Catalysts which were obtained by exposing Fe(OH)₃ and Fe₂O₃ prior to the crystallization to 0.5 N H₂SO₄ and then calcining in air at 500 °C were highly active for oxidations of butane and isobutane to CO and CO₂ below 300 °C, while iron oxides prepared without the sulfate treatment were completely inactive.

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, Fe(OH)₃ Fe₂O₃ 0,5 H₂SO₄ 500 °C CO CO₂, 300 °C, , , .

     

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. .

     

Kinetics and selectivity of the oxidation of alkanes in Cl2?H2O and Cl2?Hg2+?H2O solutions

Relative oxidation rate constants of several normal, iso-, cyclo-and methylcycloalkanes have been measured in Cl₂–H₂O and Cl₂–Hg²⁺–H₂O solutions at 343K. The selectivity of C–H bond dissociation in both systems is the same. HOCl is assumed to be the active species for the two systems.

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Cl₂–H₂O Cl₂–Hg²⁺–H₂O 343 , -,- ; C–H . , HOCl.

     

The consistency of repeated H2?O2 titration cycles on supported Pt catalysts

H₂ and O₂ uptakes at 296 K on a Pt/Al₂O₃ catalyst remained constant during repeated H₂–O₂ titration cycles conducted in a high vacuum adsorption system. Previously reported variations in these uptakes are attributed to adsorption of contaminants during desorption conditions. Also, it was found that nearly 40% of the H₂ adsorbed could be removed by degassing at 296 K for 1 hr.

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H₂ O₂ 296 Pt/Al/₂O₃ H₂–O₂, . . , 40% H₂ 1 296 .

     

V2O5/TiO2 oxidation catalysts, IV. Adsorption of acrolein on sodium-containing systems

Adsorption of acrolein on vanadia/titania catalysts fits a polymerization kinetics if Na–V compounds are not present or the vanadium content is lower than that corresponding to formation of a monolayer of vanadia on the titania support.

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, Na–V .

     

Gas-phase electrocatalytic reduction of CO2 to CO on carbon gas-diffusion electrode promoted by cobalt phthalocyanine

Cobalt phthalocyanine supported on a carbon gas-diffusion electrode has been found to be an active and stable electrocatalyst for the reduction of CO₂ to CO. Under mild conditions it gives 100% selectivity of this process at current densities up to 80 mA/cm².

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, , , CO₂ CO, 100% 80 /².

     

Catalytic activity of the Al2O3?Cr2O3?Fe2O3 system, I. Physico-chemical properties

The physico-chemical properties of a catalyst containing 90% Al₂O₃, 9% Cr₂O₃ and 1% Fe₂O₃ have been studied. Coexistence of acidic and basic (ionic) sites as well as electron acceptor radical centers have been found.

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- : 90% Al₂O₃, 9% Cr₂O₃ 1% Fe₂O₃. , () , - .

     

Thermal activation of Al2O3 supported MoO3 and WO3 metathesis catalysts

Alumina-supported MoO₃ and WO₃ catalysts were activated for the metathesis of propene by thermal treatment in Ar. Temperatures up to 1140 K are required for catalysts with low metal contents. These exhibit the highest specific activities though they are known to be highly resistant to reduction. It is proposed that the active sites are formed from Mo(VI) and W(VI) species under the conditions employed.

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MoO₃ WO₃, Al₂O₃, . 1140 . , , . , , Mo W.

     

Vapor phase oxidation of 2-methylpyridine on V2O5/TiO2 (anatase) catalysts

The influence of catalyst composition and reaction parameters on the yield of pyridine-2-carboxaldehyde has been studied for the title process. It has been established that monolayer vanadia on TiO₂ (anatase) is a highly selective catalyst for the partial oxidaton of 2-methylpyridine to pyridine-2-carboxaldehyde.

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-2-. , TiO₂ () 2- -2-.

     

IR-spectroscopic studies of the interaction of propylene and acrolein with a CoMoO4 catalyst

IR spectra of propylene and acrolein adsorbed at different temperatures on CoMoO₄ supported on MgO were recorded. Four different surface species were found: a -complex, an oxygen bonded carbonyl complex, acrylic acid and a carboxylate type complex. The mechanism of their transoformation is discussed.

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- CoMoO₄ MgO. , 4 : -, , , . .

     

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, .

     

Effect of CO2 on O2 photo-adsorption on anatase

The presence of CO₂ on TiO₂ affects the process of oxygen photo-adsorption depending on the hydroxylation state of the surface. In dehydroxylated samples CO₂ blocks the formation of O ₃ ^– and O ₂ ^– . On H₂O₂/TiO₂ samples pretreated in the range of 150–200°C it leads to CO₂–O ₂ ^– species.

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, Cu(II). . .

     

Temperature programmed desorption of hydrogen from 5 % Rh/ZrO2 catalyst

A considerable effect of the conditions of hydrogen adsorption (temperature, time) and the number of measurement cycles H_T–O_T on results of hydrogen TPD for Rh/ZrO₂ catalyst has been observed. Deactivation of rhodium surface at room temperature, conditioned by high temperature reduction seems to be due to a strongly temperature-activated hydrogen adsorption.

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(, ) H_T–O_T Rh/ZrO₂. , , .

     

Infrared studies of CO2(CO)8 adsorption on zeolites Y

Co₂(CO)₈ sublimed onto the surface of HY, CeY, CoY and two dealuminated forms of NaY zeolite is converted at room temperature to Co₄(CO)₁₂ and other surfacebound cobalt carbonyl species. The reaction proceeds in a different way on each of the above zeolites, depending also on their pretreatment.

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Co₂(CO)₈, HY, CeY, CoY NaY, Co₄(CO)₁₂ - . - .

     

Peculiarities of propylene metathesis over catalysts prepared by anchoring of Mo(V) oxalate to γ-Al2O3

Propylene metathesis over catalysts prepared by coordination of Mo(V) oxalate to -Al₂O₃ has been studied.

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, (V) -Al₂O₃.

     

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 , .

     

Gas-phase hydroformylation of propylene on Ru/SiO2 catalysts

Ru/SiO₂ catalysts prepared by reduction of supported RuCl₃·xH₂O are active in gas-phase hydroformylation of propylene at low pressure (ca. 0.3 MPa) of H₂+CO+C₃H₆ mixtured and show unexpectedly high selectivity towards unbranched oxo-products. Data concerning the effect of electronic state and dispersity of Ru on their catalytic behavior have been obtained.

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Ru/SiO₂, RuCl₃·xH₂O, (0,3 ) - . .

     

Application of the vapor phase supporting (VPS) method for preparing SnO2/SiO2 catalysts

Supported SnO₂/SiO₂ catalysts have been prepared by the reaction of the surface hydroxy groups of silica gel and gas phase tin chloride (PS method). The catalytic properties have been examined in the reaction of 2-propanol to show the effect of VPS cycles on the amount and nature of the active sites.

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SnO₂/SiO₂ . 2- VPS .

     

Reactivity of Cl(2P1/2) atoms towards CH3F

The photochlorination of methyl fluoride has been studied at low pressures. Excited (²P_1/2) chlorine atoms have been found to participate in the reaction. The ratio of the excited and ground state rate constants has been estimated at room temperature.

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. (²P_1/2) . .