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1.
The pressure-jump method was applied to the dehydrogenation of C3H8 over a Cr2O3–Al2O3–K2O catalyst in a closed static reactor at 443°C. The rate equation proposed for initial kinetics was shown to apply to the dehydrogenation of C3H8.
C3H8 Cr2O3–Al2O3–K2O 443°C. , , , C3H8.
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2.
The thermal properties of complex carbon-silica adsorbents (carbosils) were investigated using differential thermal analysis. The adsorbents were prepared by pyrolysis of methylene chloride. Pyrolysis reaction on silica surface was carried out at different temperatures (400–700 °C) and at different pressures of CH2Cl2 vapours. Thermal analysis was carried out in air atmosphere. The following parameters characterizing the properties of the adsorbents were determined: carbon content, specific surface area, carbon layer thickness, pore volume, mean pore radius, differential of heats of adsorption ofn-hexane and benzene, and micrographs. The correlation between topography and morphology of carbon deposits (dependent on the parameters of the pyrolysis process) and the courses of DTA and TG curves corresponding to individual carbosils have been determined.
Zusammenfassung Mittels DTA wurden die thermischen Eigenschaften von komplexen Kohlenstoff-Silikaadsorptionsmitteln (Carbosil) untersucht. Die Adsorptionsmittel wurden durch Pyrolyse von Methylenchlorid gefertigt. Die Pyrolyse wurde an der Oberfläche von Silika bei verschiedenen Temperaturen (400–700 °C) und bei verschiedenen CH2Cl2-Drücken durchgeführt. Die Thermoanalyse geschah in Luftatmosphäre. Folgende Parameter zur Charakterisierung der Eigenschaften der Adsorbenten wurden ermittelt: Kohlenstoffgehalt, spezifische Oberfläche, Kohlenstoffschichtdicke, Porenvolumen, Porendurchmesser, Ableitung der Adsorptionswärme vonn-Hexan und Benzol sowie Oberflächenmikrogramme. Es konnte der Zusammenhang zwischen Topografie und Morfologie der Kohlenstoffablagerungen (abhängig von den Parametern des Pyrolysevorganges) sowie dem Verlauf der DTA- und TG-Kurven der entsprechenden Carbosile festgestellt werden.

- (). . (400–700°) . . : , , , , - , . , , .
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3.
A mathematical model is suggested for the simultaneous absorption of two gases entering into a catalytic reaction in a plug-flow reactor (PFR). The effect of its parameters on the reaction process is analyzed.
, . .
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4.
A solid solution of vanadium in MoO3 with a solubility limit of about 3 mol.% V2O5 is shown to be formed. Its catalytic properties are discussed.
MoO3 3 . % V2O5 .
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5.
The thermal decomposition of propane has been studied by pulse chromatographic method within the temperature range of 975–1083 K. The kinetic parameters of the reaction have been determined.
- 975–1083 . .
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6.
    
It has been found that there is a strong dependence of the rate of benzil hydrogenation on the structure and basicity of maines. This observation is interpreted in terms of heterolytic activation of hydrogen by cobaloxime.
. .
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7.
The oxidation of ethanol on CuO, CuO/Al2O3 and Pt/Al2O3 catalysts has been studied at various concentrations of alcohol, oxygen and water vapor in the reaction mixture. The reaction order and activation energies have been determined for both complete and partial oxidation processes. A consecutive oxidation scheme is suggested.
CuO, CuO/Al2O3 Pt/Al2O3 , . . .
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8.
Crystals of mordenite were grown on metallic Cr surface by the vapor phase method. The material of zeolite coating on metal surface has been characterized by X-ray powder diffraction and microprobe. It is shown by the results that this material possesses good catalytic properties.
(Cr) . . , .
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9.
The kinetics of the two reactions hexacyanoferrate (III)-iodide and peroxodisulfate-iodide in several isodielectric water-cosolvent mixtures have been studied. The results can be rationalized as a consequence of the cosolventwater interaction.
(III) -. -.
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10.
It has been found that when the reaction is carried out at pressures of the reaction mixture ranging from 1 to 400 Pa, small surface coverages by adsorbed oxygen, carbonate groups and irreversibly adsorbed carbon-containing particles are obtained. Rate relaxations are due to the concentration variations of adsorbed oxygen and CO3ads groups.
, 1–400 , , . CO3.
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11.
Benzyl chloride transformation has been studied over Rh/TiO2 under SMSI state to give evidence for the transfer of electrons from support to metal.
Rh/TiO2, . .
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12.
Studies of 1-ethyl-(-14C)-indane dehydroisomerization over a Pt/Al2O3 catalyst (AP-64) have revealed that 34.5% or 16.5% of the initial tracer label migrates into the -position of the expanded methylnaphthalene ring when the catalyst is pretreated at 763 K in Ar or H2, respectively. The reaction mechanism is discussed.
1--(14C)- -64. , 763 - 34,5% , —16,5%. .
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13.
Catalytic properties of V2O5/SiO2 in benzene oxidation by N2O were examined. Sodium additive was shown to affect the catalyst operation stability.
V2O5/SiO2 N2O. .
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14.
Field emission microscopy and thermal desorption studies of hydrogen adosrption on a monocrystal tip and a polycrystalline rhenium wire indicate dissociative adsorption which proceeds with an initial sticking coefficient of So0.2 and an isosteric adsorption heat of about 138 kJ/mol.
. , , So0.2 138 /.
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15.
    
, 1.2·1018/2 3.6·1018/2, . , .
The endothermic stage of desctruction of Al2O3 crystal lattice begins with the adsorption of a monolayer of chloride and hydrogen ions (1.2×1018 m–2 and 3.6×1018 m–2, respectively). The abrupt change in the Al content of the solution is attributed to the release of low-coordinate aluminium ions from the environment of the cationic vacancies of the oxide lattice.
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16.
It has been shown that in the interaction of zinc oxide and phosgene, the most active are the samples having oxygen vacancies. A mechanism for this process is suggested.
, , . .
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17.
The possibility of obtaining tetramers from durene or diphenyl oxide in the presence of H5PMo10V2O40, a reversible oxidant, and palladium acetate as catalyst is demonstrated.
— H5PMo10V2O40 .
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18.
A catalyst grain is shown to consist of microparticles constituting a metal nucleus of aluminium covered by an oxide (-Al2O3) film. On this film a nickel-aluminium spinel is localized with metallic nickel (Ni0) particles on its surface. This morphological structure of catalysts accounts for the increased electron density on nickel particles and hence for the high catalytic activity in steam reforming of methane.
, , , (-Al2O3). - , (Ni0). , , .
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19.
Catalytic properties of Pd black-oxide systems have been studied in hydrogenation of crotonaldehyde. It has been revealed that the additions of basic and amphoteric oxides (MgO, Fe2O3 and ZnO) increase the hydrogenation rate of the ethylenic bond in crotonaldehyde.
Pd-- . , (MgO, Fe2O3, ZnO) .
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20.
According to IR spectroscopic studies, a Ti–Mo heteropolyacid is formed on the surface of Ti–Mo catalysts prepared from ammonium paramolybdate and TiO2.
- , Ti–Mo TiO2 Ti–Mo .
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