Stereoselective hydrogenation of 2-hexyne on Cu/γ-Al2O3 catalysts

The stereoselective hydrogenation of 2-hexyne in ethanol on Cu/-Al₂O₃ catalysts (1–40 % Cu) at 4–10 atm and 80–120 °C has been studied. The reaction affordscis-2-hexene as the only reaction product in 100 % yield at [Cu] 30 %. For samples with 20 % Cu, hydrogenation proceeds in parallel with absorption of H₂ by the catalyst.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 7, pp. 1314–1315, July, 1993.     

Fuel Combustion Reactions and Catalysts: XXI. Synthesis and Characterization of Modified Mn–Al–O Catalysts for High-Temperature Oxidation

The phase composition of supported Mn–Al–O catalysts and their activity in the reaction of methane oxidation were studied depending on the composition of aluminum oxide supports (-Al₂O₃ with different -Al₂O₃ contents modified with individual Mg, La, and Ce oxides or Mg + La and Mg + Ce oxide mixtures) and calcination temperatures (500, 900, and 1300°C). It was found that the Mn–Al–O catalysts based on -alumina containing -Al₂O₃ and modified with Mg, La, or Ce additives are more active and thermally stable (up to 1300°C) than the samples based on pure -Al₂O₃. A conclusion was drawn that a higher degree of disorder of the structure of -Al₂O₃, compared to that of -Al₂O₃, is favorable for a deeper interaction of manganese and modifying additives with the support at the early stages of the synthesis and for the formation of Mn–Al compounds with complex composition (solid solutions and/or hexaaluminates) at 1300°C. These compounds are responsible for the stability and high activity of the catalysts in methane oxidation.     

Physicochemical properties of Ti-grafted SBA-15

Partial oxidation of n-heptane to syngas at 400–450°C was investigated over Rh and Rh-Ni based catalysts. The Rh/-Al₂O₃ catalyst exhibited much better catalytic activity than the Rh-Ni/-Al₂O₃ catalyst. A combination of the Rh-based catalyst with the WGS reaction catalyst (Fe₃O₄—Cr₂O₃) increases the hydrogen selectivity but has no distinct effect on shifting the balance of the partial oxidation of n-heptane.This revised version was published online in December 2005 with corrections to the Cover Date.     

Genesis of phase composition of supported Al?Fe?O catalysts

XPS, ESR and ESDR methods have been used for studying Al–Fe–O catalysts calcined at 620–1270 K. -Al₂O₃ interaction with impregnating solutions of iron oxalate complexes was shown to lead to the formation of isolated Fe³⁺ ions, and supported phases of solid solutions and associates at 620–820 K.     

Influence of MgO loading on the structure and catalytic performance of Pd/γ-Al2O3, I. Effect of interaction between MgO and γ-Al2O3

The influence of MgO dispersed on -Al₂O₃ in different amounts on the structure and performances of Pd/-Al₂O₃ catalysts has been studied by means of XRD, H₂–O₂ titration, BET and catalytic activity test for CO oxidation. It was found that introduction of MgO enhanced greatly the CO oxidation activity of catalyst. It seems that the enhanced activity stems from the stronger interaction between MgO and -Al₂O₃ at a given temperature (e.g. 450 °C).     

Partial Oxidation of Ethane to Syngas over Supported Metal Catalysts

The reaction performance for C₂H₆-O₂ to syngas over different supported metal catalysts was investigated in a flow-reactor. The activated behavior of ethane is different from that of methane over the supported nickel catalysts. Although there may exist a gas phase reaction at high temperatures, over a Ni (or Rh)/-Al₂O₃ catalyst, the partial oxidation of ethane to syngas is a heterogeneous process, while over a Pt (or Pd)/-Al₂O₃ catalyst, it may be a homo-heterogeneous process. The Ni/-Al₂O₃ and Rh/-Al₂O₃ catalysts are suitable for partial oxidation of ethane to syngas at high temperatures.     

Stereoselective hydrogenation of 11-hexadecyne-l-ol on supported copper catalysts

Hydrogenation of 11-hexadecyne-l-ol on 5–30 % copper catalysts supported on -A1₂O₃ and MgCO₃ results incis-11-hexadecyne-1-ol in 100 % yield. Hydrogenation does not occur on 5–30 % Cu/ZnO catalysts. The difference in behavior of the catalysts is connected with the valent state of copper on the surface and different hydrogen chemisorption.Positive conclusion on the application No. 930071.1 of 16.06.93 for the Kazakhstan preliminary Patent (A. M. Pak, O. 1. Kartonozhkina, and G. T. lzdebskaya).Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 5, pp. 1147–1150, May, 1996.     

Effect of oxides on the activity of Co-carbonyl catalysts for hydrocarbon synthesis from CO and H2

The effect of Zr, Mg, and Mn oxides on the activity and selectivity of Fischer-Tropsch catalysts prepared under mild conditions by supporting cobalt carbonyl (SiO₂, SiO₂-Al₂O₃, and -Al₂O₃) is studied. The activating action of the additives is caused by their reaction with the support and depends significantly on its nature.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 11, pp. 2425–2428, November, 1989.     

Oxidation of methane, butane and carbon monoxide on Al?Fe oxide catalysts

The activity of the catalysts obtained by supporting Fe³⁺ oxalate complexes on -and -Al₂O₃ in oxidation of CH₄, C₄H₁₀ and CO has been studied. The composition of the impregnating solution and the temperature of catalyst thermal treatment were varied. The most active catalysts were prepared by impregnation of -Al₂O₃ with (NH₄)₃[Fe(C₂O₄)₃] solutions at pH=2.0–3.5. Their activity appears to be close to that of Al-Mg-Cr catalysts in butane oxidation and even exceeds this in CO oxidation.     

The properties of supported rhenium catalysts in the dehydrogenation of cyclohexane

The 2 % Re/sibunite catalyst is more active than 2 % Re/-Al₂O₃ and 2 % Re/-Al₂O₃ catalysts in the dehydrogenation of cyclohexane into benzene (T = 350 °C,w = 0.5 h–1). The substitution of NH₄ReO₄ by HReO₄ in the preparation of the catalyst enhances its activity by a factor of 1.3. Treatment with HNO₃ or oxalic acid increases the selectivity by a factor of 1.2 and 1.35, respectively, the overall conversion of cyclohexane being 32–40 %.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 8, pp. 2119–2121, August, 1996.     

Heterogeneous-catalytic fischer reaction

The catalytic synthesis of 7-azaindole and its 2-methyl derivative has been accomplished for the first time by cyclization of acetaldehyde and acetone 2-pyridylhydrazones in the presence of -Al₂O₃ and fluorinated aluminum oxide. The temperature dependence of the yields of reaction products — azaindoles and 2-aminopyridine — was studied. The cyclization of acetaldehyde 2-pyridylhydrazone proceeds under more severe conditions. The maximum yield of 7-azaindole is 15% at 450° on fluorinated aluminum oxide. The yield of 2-methyl-7-azaindole reaches 50% at 315°. Fluorinated aluminum oxide displays higher catalytic activity.See [1] for communication III.Translated from Khimiya Geterotsiklicheskikh Soedinenii, No. 5, pp. 656–658, May, 1972.     

Heterogeneous catalytic transformation of isobutyl benzoate by the inverse Tishchenko reaction

Using the catalytic transformation of isobutyl benzoate at 663 K in the presence of 12 % MnO₂/-Al₂O₃ in a He atmosphere as an example, it has been shown that the inverse Tishchenko reaction can take place at a temperature above 600 K. Isobutyl benzoate gives isobutanal and benzaldehyde as well as products of their transformation,i.e., benzyl isobutyrate, isobutanol, benzyl alcohol, and toluene.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 8, pp. 1494–1496, August, 1994.     

Effect of properties of aluminum oxide on selectivity of Pt/Al2O3 in dehydrogenation of n-alkanes

Conclusions The selectivity of Al-Pt catalysts (0.25% Pt) in the dehydrogenation of n-decane and n-hexane to n-alkenes depends on the properties of the aluminum oxide and increases in the order: Pt/-Al₂O₃2O₃s > Pt/-Al₂O₃.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 11, pp. 2615–2618, November, 1978.     

Study of amorphous Ni-La-B/g-Al2O3 catalysts for the production of hydrogen peroxide from carbon monoxide, water and oxygen

Summary Novel amorphous Ni-La-B/-Al₂O₃ catalysts have been developed for the production of hydrogen peroxide from carbon monoxide, water and oxygen. The experimental investigation confirmed that the catalyst dried at 120ºC in air shows the best initial activity. The deactivation of amorphous Ni-La-B/-Al₂O₃ catalysts was also studied.     

Alkylation of benzene by propane over zeolite-containing pentasil-alumina compositions and dealuminated pentasils

The alkylation of benzene by propane over pentasil-aluminum compositions (HTsVM--Al₂O₃) has been studied for a wide range of compositions and also over dealuminated and dehydroxylated samples. It has been established that Al₂O₃ plays little if any part in this reaction. As the proportion of HTsVM in the composition is increased the yield of alkyaromatic hydrocarbon increases, reaching a maximum (36%) for pure HTsVM. Dealumination and dehydroxylation of the HTsVM led to a significant reduction in the yield of alkylation products. It was concluded the Brønsted acid centers of the zeolite are responsible for bringing about the alkylation of benzene by the lower alkanes.DeceasedN. D. Zelinskii Institute of Organic Chemistry, Russian Academy of Sciences, 117913 Moscow. Translated fromIzvestiya Akademii Nauk, Seriya Khimicheskaya, No. 12, pp. 2708–2712, December, 1992.     

Rhodium-technetium catalysts in the dehydrogenation of cyclohexane

The catalytic properties of a Rh-Tc/support (-Al₂O₃, SiO₂, or MgO) system in the dehydrogenation of cyclohexane have been investigated. A nonadditive increase in the catalytic activity of bimetallic catalysts in comparison with monometallic systems has been established. This effect depends on the ratio of the amounts of the supported metals and on the nature of the support. Diffuse reflectance spectra showed the presence of ionic forms of the metals in the bimetallic catalysts. Analysis of the catalytic and optical properties allowed one to draw the conclusion that the synergistic effect is explained by the formation of Rh_xTc_y clusters.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 9, pp. 1563–1566, September, 1994.     

Transformations of isobutylene in the presence of various types of zeolites

Conclusions In contrast to zeolites with ultrahigh silica content, type A, X, Y, and M zeolites in the Na form and also those modified by decationization, cation exchange, and addition of-Al₂O₃, Al₂O₃-SiO₂, Pt, and Rh show a low activity in the aromatization reaction of C₃-C₄ olefins at 450–550°C at times of contact of 2–14.4 sec. The zeolites studied become rapidly deactivated as the result of intense coke formation.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 6, pp. 1300–1304, June, 1981.     

Hydrogenating Activity and Adsorption Capacity of Supported Nickel Catalysts Modified by Heteropoly Compounds

The catalytic activity, adsorption capacity, and pore structure of low-percentage nickel catalysts supported on -Al₂O₃or activated carbon and modified by tungsten heteropoly compounds are studied. The activity, selectivity, and thermal stability of the catalysts in the vapor-phase hydrogenation of olefins and aromatic hydrocarbons are higher than those for conventional nickel catalysts. The concentration of nickel in the catalysts is 10–15 times lower than that in commercial catalysts. However, the modified catalysts have higher specific surface areas of metal, higher dispersion, a uniform distribution of metal particles, and a pore-radius distribution other than in the support. The study of water adsorption and desorption showed that the heteropoly compound modifying the -Al₂O₃support covers the support surface completely, and supported nickel interacts with the active surface of the modifying agent rather than with Al₂O₃. A hydrogenation mechanism is proposed, which involves H₂dissociation on Ni particles and the subsequent diffusion of hydrogen atoms via a spillover mechanism to the adsorbed organic compound with the participation of the OH groups of the modifying agent.     

Catalytic decompostiton of methyl nitrite over supported palladium catalysts in vapor phase

The vapor phase catalytic decomposition of methyl nitrite over supported palladium catalysts has been investigated. The catalytic activities were ranked in the following order: Pd/-Al₂O₃> Pd/A.C > Pd/-Al₂O₃ >Pd-Ti/-Al₂O₃. The acidic supports, such as HY zeolite, -Al₂O₃ and SiO₂ also exhibited moderate activity for methyl nitrite decomposition reactions. Several unusual features in the present decomposition reactions of methyl nitrite are discussed. A possible successive dehydrogenation mechanism was proposed to explain the facts observed in this study.