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1.
The adsorption of NH3 on Cr–Mo and Cr–Mo–Te catalysts has been investigated by IR spectroscopy. It is shown that there are both electron acceptor and proton donor acid centers on the surface of these catalysts. The introduction of tellurium into a Cr–Mo catalyst decreases adsorption on the electron acceptor centers.
NH3 Cr–Mo Cr–Mo–Te . , -, - . Cr–Mo .
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2.
The rates of ammonia decomposition on polycrystalline Ir and Pd wires were measured at temperatures between 900 and 2000 K and at pressures between 50 and 770 Torr. Rates on Ir were fitted with a Langmuir-Hinshelwood unimolecular reaction rate expression. Rates on Pd could not be fitted with a rate expression, although activation energies were obtained.
Ir Pd 900–2000 50–770 . Ir --. Pd . .
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3.
Influence of the strength and concentration of non protic centers on the catalytic activity of metal-zeolite catalysts in isomerization of n-butane has been studied. A relationship between the specific activity and the center strength is suggested.
-. , .
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4.
Zusammenfassung Für eine anwendungstechnische Beurteilung von amorphen synthetischen Kieselsäuren sind neben der Dispersität und Morphologie insbesondere auch strukturelle Eigenschaften bedeutsam. Die vorliegende Veröffentlichung zeigt, daß auf der Basis von thermoanalytischen Untersuchungen eine Unterscheidung unterschiedlicher Kieselsäuretypen möglich ist. Aus den TG- und DTA-Ergebnissen sind dabei Aussagen über die Art und Menge des adsorptiv bzw. chemisch gebundenen Wassers, sowie die oxydative Zersetzung des organischen Beschichtungsmittels abzuleiten.
Besides dispersity and morphology, structural characteristics are of importance for the estimation of amorphous synthetic silicic acids with regard to their application. The present publication shows that it is possible to identify the different silicic acid types on the basis of thermoanalytical studies. The TG and DTA results provide information on the type and quantity of adsorbed or chemically bound water, and on the oxidative decomposition of the organic coating agent.

, . . , .
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5.
It is evident that thermal analysis studies of Australian coals are of primary significance in the rationalisation of the various physical and chemical processes inherent in energy generation from these fossil fuels. To data, considerable such data has been accumulated correlating combustion efficiency with the coal primary structure, surface phenomena, included metal ions, volatile matter release profiles, particle size and corresponding char properties. The kinetics of these complex processes are now also modelled.
Zusammenfassung Für die Rationalisierung der physikalischen und chemischen Prozesse bei der Energiegewinnung aus australischer Kohle sind thermoanalytische Untersuchungen dieser fossilen Rohstoffe von erstrangiger Bedeutung. Es wurde eine bedeutende Menge von Angaben gesammelt, die eine Beziehung zwischen dem Verbrennungsgrad und der Primärstruktur der Kohle, Oberflächenerscheinungen, enthaltenen Metallionen, des Emissionsprofiles flüchtiger Verbindungen, der Partikelgröße und der entsprechenden Halbkokseigenschaften herstellen. Die Kinetik dieser komplexen Vorgänge wurde nun auch modelliert.

, , . , , , , , . .
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6.
The results of the infrared spectroscopic study of the interaction between furan and a vanadium oxide catalyst permit to suppose that the intermediates in furan oxidation are surface succinyl oxide and maleates.
, , , - .
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7.
    
A, , . -- . - - .
The molecular sieve selectivity of cationic and decationized type A zeolite, erionite and mordenite has been investigated in cracking and hydrocracking reactions. The selectivity of sodalite catalysts conforms with, whereas that of erionite catalysts is in contrast to the correspondig activity. The substrate reactivity influences the selectivity in a variety of ways.
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8.
The coking resistance of six alumina supported nickel catalysts in n-butane steam reforming mainly depends on the average size of nickel crystallites. Thus, by using suitable preparative methods, it is possible to produce good, coking resistant nickel catalysts even with Al2O3 support.
Al2O3 -, , . . ., , - Al2O3.
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9.
Various catalysts were prepared by impregnating a commercial alumina with solutions containing the complex dichlorobis(trichlorostannato)platinate (II). [Pt Cl2 (SnCl3)2]2–. After reduction, 1–20 fold variations in the catalytic activity in benzene hydrogenation were observed in direct proportion to the stability of the complex in the impregnating solution.
, — - ( ()-(II) [PtCl2(SnCl3)2]–2. , 1–20 . .
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10.
Catalytic deactivation dynamics of zeolites in multicycle processes has been calculated. It has been revealed that in naphthalene sorption on NaX zeolites surface deactivation is predominant with its similarity criterion close to unity and a high fraction of deactivation. Calculated data for several multicycle processes are given.
. , NaX . .
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11.
The fall-off curves were calculated for the unimolecular decomposition of the trifluoromethyl hypofluorite at 475.8, 496.9 and 507.3 K by means of the Reduced Kassel Integral in Factorized Form.
475,8,496,9 507,3 .
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12.
CO2 undergoes cycloaddition to propyne on a cationic rhodium site with the assistance of O2–/OH of support or iron oxide over Rh4 and Fex Rhy carbonyl clusterderived catalysts.13CO12 labeling and FTIR studies suggest that monodentate carbonate formed on the catalyst surface is most likely a key species to offer an active CO2 to be converted into a carbonyl intermediate prior to the product 4,6-dimethyl-2-pyrone.
CO2 O2–/OH Rh4 Fex Rhy. 13CO2 , CO2 , 4,6--2-.
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13.
Thermal dissociation processes of-diketonate adducts with the composition ML2 · 2B (L = acetylacetone and its substituted derivatives;M = Ni, Co;B = H2O, BuNH2CH3OH, Py, NH3) were investigated. Kinetics of dissociation were studied in a flow reactor. For dehydration processes a compensation relationship is observed (lgA=E+b), demonstrating analogous mechanisms.A semi-quantitative series of the thermodynamic stabilities of the dihydrates is obtained from experimental data at quasi-equilibrium conditions (Q-derivatograph).
Zusammenfassung Es wurden die thermischen Dissoziationsprozesse von-Diketonataddukten der Zusammensetzung ML2 · 2B (L=Azetylazeton und dessen substituierte Abkömmlinge;M=Ni, Co;B=H2O, BuNH2, CH3OH, Py, NH3) untersucht. Die Kinetik der Dissoziation wurde in einem Flowreaktor untersucht. Als Beweis für die Ähnlichkeit der Mechanismen der Dehydrierungsprozesse konnte eine lgA=aE+b Beziehung festgestellt werden. Von unter Quasi-Gleichgewichtsbedingungen gewonnenen Daten konnte eine semiquantitative Serie der thermodynamischen Stabilitäten der Dihydrate abgeleitet werden (Q-Derivatograph).

- ML2·2B (L = ;M= Ni, Co;B=H2O, BuNH2, CH3OH, Py, NH3). ; (lgA=aEs+b) . (Q- ).
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14.
Liquid phase oxidation of cycloalkane diheteroanalogs catalyzed by compounds of Cu2+, Ni2+, Co2+, Cr3+, Fe3+ has been studied. It has been established that these catalysts can be applied to intensify, oxidize and increase the selectivity of this process.
: Cu2, Ni2+, Co2+, Cr3+, Fe3+. .
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15.
By comparison of the catalytic hydrogenation and electrochemical reduction of NO on platinum black catalysts it has been shown that the hydrogenation of NO to ammonia and to hydroxylamine occurs in the diffusion controlled region only.
NO , NO .
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16.
The nature of adsorbed sulfonium and phosphonate ylids on a new barium hydroxide catalyst (C-200) is analyzed by IR. The catalytic activity of C-200 in solid-liquid phase transfer conditions is explained by these IR studies.
(C-200) . C-200 - .
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17.
According to the GC-MS analysis of the composition of liquid hydrocarbons obtained in methanol conversion on ZSM-5 zeolites and the selectivity of cyclohexene conversion on these catalysts, the sequence of the aromatization reaction steps is discussed.
-- , ZSM-5, .
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18.
The influence of ammonia on the direction of the oxidative transformations of propylene has been studied. Ammonia has been shown to block the surface oxygen of antimony catalysts. As a result, an increase in the selectivity with respect to the products of partial oxidation is observed.
. , , .
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19.
To check coke formation on metallic (Pto) and acidic (Al3+) centers of Pt/Al2O3 and Pt–Sn/Al2O3 catalysts, the application of IR spectroscopy of adsorbed CO for detecting Pto–CO (2070 cm–1) and Al3+–CO (2190 cm–1) bonds has been substantiated. Decrease in the number of active Pto and Al3+ centers is shown to correlate with that in the dehydrogenation rate of cyclohexane and in the isomerization rate of heptane, respectively.
(Pto) (Al3+) Pt/Al2O3 Pt–Sn/Al2O3 - CO Pto–CO (2070 –1) Al3+–CO (2190 –1). , Pto , Al3+- .
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20.
The earlier proposed pulse flow method for the determination of surface OH groups based on the reaction of gaseous dimethylzinc tetrahydrofuranate with active hydrogen was applied to alumina and silica-alumina catalysts. The concentrations of OH groups found by this method are in a good agreement with the published data, obtained by deuterium exchange and gravimetry.
, , OH, , - . OH, , , .
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