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1.
Ammonia synthesis on nitrides CeN, UN1.70 and iron catalyst CA-1 has been examined at pressures of up to 100 bar. Reaction kinetics is described by the Temkin-Pyzhev equation. Activation energy for all samples is similar and equals about 200 kJ/mol. Specific catalytic activity of nitrides is lower than that of the iron catalyst by a factor of 3–4 for uranium and 10 for cerium.
100 CeN, UN1, 70 CA-1. -. 200 /. : 3–4 10 .
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2.
In the first period of the reaction at pH 8 slow evolution of CO2 and N2O was observed. After gas evolution ceased, on adding NaOH, formation of N2O again and, unexpectedly, H2 was found. The amount of H2 was measured as a function of reaction conditions. Illumination with visible light and the excess of the oxidant promote hydrogen evolution. The experiments in D2O resulted in H2, HD and D2. The non-statistical isotope distribution was interpreted by a kinetic isotope effect.
pH=8 CO2 N2O. NaOH, N2O , , H2. H2 . . D2O H2, HD D2. .
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3.
Activity of CaO–CaF2 catalysts in the Claus reaction has been studied as a function of catalyst composition and of the time of catalyst operation in the reaction. Opposite effects of low and high fluoride content on the Claus activity have been found. A new type of reducing centers is suggested to be responsible for the increase in the activity observed in the case of fluorine-rich catalysts.
CaO–CaF2 . , . , , .
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4.
NaNO3 addition to Co/Al2O3 results in an increase in the reducibility, in a smaller dispersity of the metal and in a decrease in the ethane hydrogenolysis rate due to a decorative effect.
NaNO3 Co/Al2O3 ,
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5.
Influence of HS-zeolite calcination up to 1023 K in air and steam on its adsorptive, acidic and catalytic properties in n-hexane cracking has been studied.
- 1023 , -.
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6.
Acid-base and radical properties of two sets of MgO–Na catalysts have been studied. The catalysts were prepared (I) by impregnation of MgO with NaOH in aqueous solution, and (II) by evaporation of metallic sodium onto a MgO surface. The catalyst prepared by the second method was much more basic than pure MgO (Ho=35) and showed a high activity in olefin isomerization.
- MgO–Na. 1) MgO (NaOH) 2) MgO. , , , MgO(H0=35), .
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7.
The rate of methane formation on zinc-chromium catalysts is described by zero-order rate law, If the catalyst is activated by copper, the rate of methane formation increases due to a decrease in the activation energy of the reaction. Presumably the formation of methane and methanol takes place on different active centers.
, . , . , .
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8.
The preparation and hydrolysis of silica supported vanadium catalysts have been investigated using VCl4 as a paramagnetic probe. Chemical analysis shows the possibility of the VCl4 molecule to react one, two, or three hydroxy groups of the surface. The type of reaction is influenced by the temperature of pretreatment of aerosil (TPA). ESR measurements show distortions of the tetrahedral coordination of the (SiO)nVCl4–n surface complex, which is strongest for the threefold attachment (n=3) of VCl4 to the surface. Hydrolysis is accompanied by an increase of the coordination number and leads to highly mobile vanadium species.
, VCl4 . , VCl4 , . . (SiO)nVCl4–n, VCl4 (n=3). .
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9.
Silanes of the type R1R2Si(H)CH2OEl(O)xR y 3 [R=organyl; El=C (x=y=1), S (x=2,y=1), P (x=1y=2)] undergo a thermally induced rearrangement to give silanes of the type R1R2Si (CH3)OEl(O)xR y 3 . The energetic (reaction enthalpy) and kinetic data (reaction order, enthalpy and entropy of activation) of this reaction were determined by means of differential scanning calorimetry. The results obtained are discussed in terms of mechanistic aspects.
Zusammenfassung Silane des Typs R1R2Si(H)CH2OE10xR y 3 mit R=organyl; E1=C (x=y=1), S(x=2, y=1) oder P (x=1,y=2) zeigen eine thermisch induzierte Umlagerung zu Silanen des Typs R1R2Si(CH3)OE10xR y 3 . Energetische (Reaktionsenthalpie) und kinetische Daten (Reaktionsordnung, Aktivierungsenthalpie und -entropie) dieser Umlagerungsreaktion wurden mittels DSC ermittelt. Die mechanistischen Aspekte der Ergebnisse werden diskutiert.

R1R2Si(H)OE1(O)xR y 3 , R= , E1=C (x=y=1), S (x=2,y=1), P (x=1,y=2), R1R2Si(CH3)OE1(O)xR y 3 . ( ) ( , ) . .

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10.
The effects of mono-and diolefins on ethanal pyrolysis are summarized and discussed. It is shown that an addition and a hydrogen transfer mechanism, separately or together, may account for the experimental results obtained with various mono- and diolefins.
- . , , , , - .
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11.
In an analysis of the possible mechanism and kinetics of a thermal decomposition reaction with the formation of a solid product, the following features were considered: the collective rearrangement character of the transformation; the formation of a product with a different non-equilibrium defectiveness and free energy; the free energy relationship in the series of processes leading to products with different dispersions; the formation of intermediate structures; and the spinodal character of their decomposition. Relationships are presented between the rate of solid product formation, the process temperature, and the surface area and size of the particles.
Zusammenfassung In einer Analyse des möglichen Mechanismus und der Kinetik einer unter Bildung eines festen Produktes verlaufenden thermischen Zersetzungsreaktion werden folgende Besonderheiten erörtert: der kollektive Umordnungscharakter der Umwandlung, die Bildung eines Produktes mit unterschiedlicher Nichtgleichgewichts-Gitterstörung und unterschiedlicher freier Energie, die Beziehung der freien Energie in zu Produkten unterschiedlicher DispersitÄt führenden Prozessen, die Bildung intermediÄrer Strukturen und der spinodalen Charakter ihrer Zersetzung. Beziehungen zwischen der Bildungsgeschwindigkeit des festen Produktes, der Temperatur des Prozesses und der OberflÄchengrö\e und Grö\e der Partikel werden angegeben.

: ; ; , ; . , , .
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12.
It has been found that the rate of isotope exchange in Ba2YCu3O7–x–O2 system is high. Its kinetics is exponential, first order with respect to dioxygen and the exchange is of the mixed first/third type.
Ba2YCu3O7–x–O2 . -, -, - .
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13.
The effect of reoxidation temperature on TPR of 5% Rh/Al2O3 catalyst and its mechanical mixture with ZnO has been investigated. The results suggest bimodal character of supported rhodium and surprisingly high effect of this metal on ZnO reduction in the mixture.
5% Rh/Al2O3 ZnO. , ZnO .
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14.
Catalysts prepared by pyrolysis of Co2(CO)8 on oxide supports have been studied in the hydrogenation of CO. It is shown that MgO and -Al2O3-based catalysts are less active than those supported on SiO2, TiO2 and ZrO2. The application of -Al2O3 as a support increases the relative yield of light hydrocarbons.
, Co2(CO)8 , CO. , MgO -Al2O3 SiO2, TiO2 ZrO2. -Al2O3 .
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15.
The treatment of Fe(III)NaY zeolite with NaCl solution does not lead to a back-exchange of ferric species but the cationic Fe rearranges into new complexes which are more deeply reduced by hydrogen and less self-reduced by vacuum heat treatment than the parent Fe species in FeNaY zeolite.
Fe(III)NaY NaCl . , Fe , , , Fe FeNaY.
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16.
A method has been developed that allows the deconvolution of up to 15 overlapping solidstate reactions without previous assumptions. Both the kinetic parameters and the reaction mechanisms fitted by the unit reactions can be determined from a series of non-isothermal experiments carried out at different heating rates.
Zusammenfassung Es wurde eine methode zur Dekonvolution von bis zu 15 einander überlappenden Festphasenreaktionen entwickelt, die keinerlei vorherige Annahmen notwendig macht. Mittels einer Reihe nichtisothermer Experimente mit unterschiedlichen Aufheizgeschwindigkeiten können sowohl die kinetischen Parameter als auch der Reaktionsmechanismus der Teilreaktionen bestimmt werden.

, 15. .
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17.
The kinetics of the oxidation of benzyl alcohol by potassium chlorochromate, KCrClO3, has been studied in dimethyl sulfoxide-dichloromethane medium. The reaction is catalyzed by acid. The effects of temperature and solvent composition were studied and activation parameters evaluated. Probable mechanisms are discussed.
, KCrClO3, . . . .
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18.
It has been established that P, Cs and Cu additives to V–Mo–O catalysts affect essentially both binding energy of surface oxygen and mobility of bulk oxygen.
P, Cs Cu V–Mo–O .
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19.
A derivatograph was used for the thermal modification of the surface properties of different silica gels. Analogous investigations were carried out with an isothermal method. The possibility of using the thermal method of temperature programming to modify adsorbents is discussed.
Zusammenfassung Ein Derivatograph wurde zur thermischen Modifizierung der Oberflächeneigenschaften von verschiedenen Kieselgelen benutzt. Analoge Untersuchungen wurden unter isothermen Bedingungen ausgeführt. Möglichkeiten zur Modifizierung von Adsorbentien mit der temperaturprogrammierten thermischen Methode wurden diskutiert.

. . , .
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20.
The kinetics of cumene hydroperoxide-dependent aniline hydroxylation to p-aminophenol with hemoglobin (Hb3+) participation has been studied in a phosphate buffer at pH 7.4 and 37°C. The data obtained point to hemoglobin complexing with aniline and cumene hydroperoxide (CHP). The character of aniline hydroxylation by the CHP-Hb3+ system is discussed.
37°C pH 7,4 - (Ho3+). Hb3+ . -Hb3+.
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