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1.
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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2.
Following hydrogen treatments at high temperature a decrease in hydrogen chemisorption at room temperature is observed in almost all group VIII elements supported on SiO2 or Al2O3. The effect is attributed to self inhibition by strongly chemisorbed hydrogen on the metals.
VIII , SiO2 Al2O3. .
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3.
Six MoS2/SiO2 samples were characterized by XRD, BET surface area, ESR and NO adsorption measurements. Correlation was found between the amount of Mo5+, sulfur radicals and adsorption capacity for oxygen and NO.
MoS2/SiO2 , , , NO. Mo5+, NO.
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4.
The nature of supported KMnO4 reagents on several solids (SiO2 AlPO4, BPO4 and sepiolite) is discussed. The oxidation of PhCHO to PhCO2H was the test reaction. The KMnO4 supported reagent is shown to be a mixture of physisorbed KMnO4 and Mn(IV). The influence of the nature of the solvent is discussed.
, (SiO2, AlPO4, BPO4 ). PhCHO PhCO2H. KMnO4 KMnO4 Mn(IV). .
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5.
The influence of ZSM-5 on the behavior of a Pt–Re/Al2O3 catalyst was studied in normal heptane reforming in order to compare activity, selectivity and life of Pt–Re/Al2O3 and a mixture of Pt–Re/Al2O3 and ZSM-5 catalysts. It is suggested that the presence of ZSM-5 results in less pronounced catalyst deactivation but not in a sufficient increase in aromatic selectivity.
ZSM-5 Pt–Re/Al2O3 - , Pt–Re/Al2O3 ZSM-5. , ZSM-5 , , .
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6.
The preparation of vanadium-phosphorus catalysts is described, showing the considerable influence of phosphorus on the concentration of V4+ ions. The oxidation properties were studied by chemical analysis and electron spin resonance. Moreover, ESR spectra show a strong influence of moisture on the structure of the catalysts.
- , V+4. , . , , .
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7.
By metal impregnation of selected naturally occurring organic materials followed by controlled carbonization, metal semicoke catalysts can be readily prepared. These catalysts have been tested in the synthesis of hydrocarbons and alcohols from CO/H2 and CO2/H2 mixtures. Fe and Co preparations have been used. Relatively high temperatures are required when using these catalysts, which are quite active for synthesis using CO2 and H2. The pressure (5150 kPa) is very favorable both for the synthesis of liquid hydrocarbons (C5–C30) and alcohols (C1–C5).
. CO/H2 CO2/H2. Fe Co. , CO2 H2. 5150 ) (C5–C30) (C1–C5).
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8.
Decomposition of cumene hydroperoxide in the presence of the acetylacetonate complex of MoO 2 2+ supported on a matrix of SiO2 has been studied. The reaction is first order with respect to the catalyst. The initial rate remains unchanged at concentration at cumene hydroperoxide concentrations above 0.08 mol/dm3. A two-stage mechanism of hydroperoxide decomposition is suggested.
MOO 2 2+ , SiO2. , . 0,08 /3 . .
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9.
Uning synchrotron radiation, LIII rhenium absorption spectra have been studied for Re/Al2O3 and Re+Pt/Al2O3 catalysts obtained by impregnation. For individual rhenium compounds a linear dependence between the shift of absorption edge and the state of rhenium oxidation has been found. The absorption spectra of reduced catalysts are significantly broadened as compared with those of individual compounds of the same valency. This points to the presence of rhenium compounds in different oxidation states.
LIII- , Re/Al2O3 Re+Pt/Al2O3, . . . .
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10.
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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11.
In this work we studied and compared the catalytic activity of various supported Pt systems on the gas-phase hydrogenation of o-, m- and p-xylene. We analyzed the influence of different catalyst preparation variables (solvent, precursor, salt, support and catalyst reduction temperature used) on the catalytic activity and selectivity towards the corresponding cis-and trans-dimethylcyclohexanes.
- o-, m- -. (, , ) - -.
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12.
The effect of Fe2O3 additives on crotonaldehyde hydrogenation over group VIII metals has been studied. Iron oxide added to platinum black exerts a modifying effect on the reduction of the carbonyl group of croton-aldehyde inhibiting hydrogenation of the C=C bond conjugated with a C=O group.
Fe2O3 VIII -. , , - , C=C , C=O-.
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13.
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.
H2 O2 296 Pt/Al/2O3 H2–O2, . . , 40% H2 1 296 .
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14.
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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15.
Kinetic studies of SO2 oxidation by Cu(II) complexes in aqueous solutions containing halide ions X(X=Cl, Br and I) indicate that the highest activity is observed for mixed chloro-iodo complexes of Cu(II). A reaction mechanism is suggested where the principal role is assigned to CuX 4 2– aq complexes and HSO3 radicals.
SO2 Cu(II) , X(X=Cl Br, I). , - Cu(II). CuX2–aq HSO3.
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16.
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.
, Cu(II). . .
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17.
Supported Ni-Pd/SiO2 catalysts of different Ni and Pd composition were studied in n-butane hydrogenolysis. The reaction rate, selectivity towards methane, ethane and propane were determined. On the basis of these data the relationship between the size and composition of the active center and the possibility of surface segregation of one of the components is discussed.
Ni-Pd/SiO2 Ni Pd -. , . .
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18.
The strength of protonic sites and the concentration of acid centers in V2O5/Al2O3 catalysts have been estimated according to pyridine and ammonium adsorption.
V2O5/Al2O3.
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19.
With increasing the lead content both CO and hydrogen sorption drop considerably. The influence of lead can be observed starting from a concentration of 0.5%. This may indicate that the surface is enriched in lead atoms.
CO, H2. , 0,5%. .
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20.
17O,51V and31P NMR studies indicate that the anion structure of sodium vanadophosphate in an aqueous solution is close to that in crystals of the (CN3H6)8HPV14O42 7H2O salt.
17O,51V,31P , (CN3H6)8HPV14O42 7H2O.
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