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1.
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.
Fe2O3–MoO3/SiO2 . . - . MoO3/SiO2 , .
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2.
A supported ruthenium catalyst on alumina prepared from Ru3(CO)12 has been studied by infrared and X-ray photoelectron spectroscopy (XPS). The triatomic cluster is retained on the support but breaks down at 150°C. Complete elimination of the carbonyl groups requires heating at 350°C under vacuum. XPS studies show that the decomposed catalyst does not change on further reduction in H2 at 400°C. The ruthenium atoms remain trapped within the pores of the support.
Al2O3, Ru3(CO)12, (XPS). , 150°C . 350°C . XPS , H2 400°C . .
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3.
The character of the effect of initial reaction mixture and temperature on the selectivity of catalytic reduction of sulfur dioxide by methane in the presence of oxygen has been studied.
.
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4.
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.
Fe2O3–MoO3/SiO2 Fe2O3+MoO3 . : -.
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5.
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.
473–1173 NO NiCr2O4. , NO . (II) ; .
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6.
ESR studies of O2 adsorption on reduced anatase have been performed. The amount of O 2 species is determined by adsorbed surface oxygen and their parameters are changed by CO adsorption.
O2 . , O 2 , CO.
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7.
Three reforming catalysts Pt/Al2O3, Pt–Ir/Al2O3 and Pt–Re/Al2O3 have been sulfurated by H2S and tested by their activities in benzene hydrogenation. By treatment at 500°C under hydrogen flow only a part of the initial activity of the non-sulfurated catalyst is retained. So only a part of the adsorbed sulfur is easily removed in these conditions. The remaining sulfur for each of the catalysts (Pt/Al2O3, Pt–Ir/Al2O3 and Pt–Re/Al2O3) gives the same atomic ratio of 0.5 sulfur atom per accessible metallic atom.
Pt/Al2O3, Pt–Ir/Al2O3 Pt–Pe/Al2O3 . 500°C H2 . . ., . (Pt/Al2O3, Pt–Ir/Al2O3 Pt–Pe/Al2O3) 0,5.
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8.
3 % Ir/Al2O3 catalysts have been studied by means of temperature programmed reduction and oxidation. With growing degree of metal oxidation (higher Tox) reducibility of the catalysts at low temperatures decreases.
3% Ir/Al2O3 . ( ) .
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9.
The anodic and cathodic polarization of a platinum electrode in K2O–V2O5 melt have been studied. The dissolved oxygen is shown to be ionized. Diffusion coefficients of oxygen in K2O–V2O5 and Na2O–V2O5 melts at various temperatures and K/V ratios are presented.
K2O–V2O5. , . K2O–V2O5, Na2O–V2O5 K/V.
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10.
Coke deposition during cyclopentane reaction was investigated on Pt/Al2O3 catalysts of varying dispersity. For all working pressures the higher the metallic accessibility, the higher the amount of coke deposited on the catalyst. Nevertheless, coke deposited on the less dispersed catalysts is more toxic for the metallic function. An increasing metal accessibility improves the graphitization of coke on the support and so, prevent the deactivation of the metal of a bifunctional catalyst.
Pt/Al2O3 . , , , . , , , . , .
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11.
Photoadsorption activity of SnO2 with respect to O2 and NO after CO chemisorption has been revealed to be drastically increased. Photoadsorption is suggested to be sensitized by surface carbonates formed due to CO chemisorption.
. , .
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12.
Upon the decomposition of silica-supported ammonium paramolybdate, hexagonal MoO3 is formed at 300–350 °C. Irreversible transformation of hexagonal to rhombic MoO3 is observed with increasing calcination temperature. The hexagonal MoO3 structure is probably stabilized by the insertion of ammonium and silicon ions into the lattice of molybdenum trioxide.
, , 300–359 °C . MoO3 . MoO3, , MoO3.
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13.
Applying IR spectroscopy for studying the Ziegler system Co(acac)3/Mg(Bu)2 (Bu=n-butyl) in tetrahydrofuran, it could be shown that the following reactions take place: reduction of cobalt (III), exchange of the acetylacetonate groups and their interaction with Mg(Bu)2.
Co(acac)3/Mg(Bu)2 (Bu=-) - , (III), Mg(Bu)2.
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14.
The interaction of diallylnickel with WS2 produces catalysts whose activity is 10–50 times higher than that of the parent sulfide. The atomic catalytic activity referred to supported nickel is independent of the catalyst type and the sulfur removed in temperature programmed reduction.
, WS2 , 10–50 . , , .
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15.
Approximate equation to calculate the effectiveness factor of catalyst for SO2 oxidation to SO3 has been derived. Calculated data agree well with those predicted by a quasi-homogeneous model.
. .
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16.
Irradiation of a C6F5H–C6F5D mixture at 1 Torr by a tunable CO2 pulse laser brings about chiefly dissociation of one component depending on the frequency of emission absorbed by the proper molecules. The addition of radical acceptors increases the selectivity by suppressing secondary reactions.
C6F5H C6F5D 1 CO2-, , . .
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17.
The effect of different alkali metal hydroxides on the metallic dispersity and catalytic activity of SiO2–AlPO4 (8020, by mass) supported palladium catalysts has been studied. The reduction by hydrogen transfer of benzylideneacetone and styrene (using cyclohexene and n-octanol, respectively, as hydrogen donors) and the liquid phase reduction of cyclohexene at low pressure (5 bar) in a Parr type reactor have been used as test reactions to follow changes in the catalytic activity.
(SiO2–AlPO4/8020 ). ( n-, , , (5 ) .
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18.
Reduction kinetics of NiO–MoO3 catalysts in H2 at 573–723 K has been studied. Reduction activation energies Ea have been determined. The degree of NiO–MoO3 reduction is shown to increase with increasing NiO content.
NiO–MoO3 H2 573–723 . E NiO–MoO3 . , NiO–MoO3 NiO .
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19.
The catalytic activity for skeletal isomerization of 1-butene on ZrO2 supported on Al2O3 and doped with sulfate ion has been found to be higher than on pure ZrO2/Al2O3, Al2O3 containing sulfate ion and a commercial SiO2–Al2O3 of Ho<–13.7. Sulfate ion was capable of transforming ZrO2/Al2O3 into a solid superacid.
1- ZrO2, Al2O3 , , ZrO2, , Al2O3, , SiO2–Al2O3 Ho < –13,7. ZrO2/Al2O3 .
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20.
CH4 photooxidation on V/SiO2 catalyst in the presence of gaseous oxygen has been studied by the mass-spectometric method. It has been established that CO2 forms due to the interaction of CH4 with surface oxygen anions bonded to vanadium ions. Photodecomposition of V4+O 2 species formed in O2 adsorption on reduced vanadium ions leads to the reoxidation of the latter.
- CH4 V/SiO2 . , CO2 CH4 , . V4+O 2 O2 , .
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