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1.
Unusual variations of selectivity are observed in the catalytic oxidation of butadiene on MoO3–TiO2 catalysts. A maximum of selectivity in furan and maleic anhydride is obtained at 400°C, since the oxidation of crotonaldehyde, dihydrofuran and furan are selective at all temperatures. Competitive oxidation of furan and crotonaldehyde proved that the aldehyde cannot be the unique intermediate for furan and maleic anhydride formation. Two mechanisms, involving various adsorbed species of butadiene, occur depending on the temperature and explain the decrease of the selectivity below 400°C.
MoO3–TiO2 . 400°C, , . , . , , , 400°C.
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2.
The effect of the support preparation technique (solgel and coprecipitation) on the final Pt/ZnAl2O4 catalyst is presented. The structural properties of the solids obtained are correlated to the selectivity and activity for isobutane dehydrogenation in H2 and He reaction media. If a highly dispersed catalyst is suitable, the support has to be prepared by the sol-gel method.
( — ) Pt/ZnAl2O4. H2 He. , — .
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3.
Relative oxidation rate constants of several normal, iso-, cyclo-and methylcycloalkanes have been measured in Cl2–H2O and Cl2–Hg2+–H2O solutions at 343K. The selectivity of C–H bond dissociation in both systems is the same. HOCl is assumed to be the active species for the two systems.
Cl2–H2O Cl2–Hg2+–H2O 343 , -,- ; C–H . , HOCl.
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4.
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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5.
Platinum(II) catalyzes the reduction of alkyl iodides to alkanes according to a mechanism involving oxidative addition of RI to Pt(II), reduction of the product complex RPt(IV) to RPt(II) by iodide ions and protolysis of the latter particle.
(II) , RI PtII, - RPtIV RPtII .
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6.
The acidic properties of a series of TiO2–SiO2 catalysts with different Ti/Si mole ratios have been studied. In order to determine the amount of acid centers and the acid strength distribution, the Benesi method of discontinuous titration has been used. Thermogravimetric measurements were also carried out.
TiO2–SiO2 Ti/Si. , - . .
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7.
Decomposition of N2O has been studied on pure La2CuO4, La2CuO4 with 5 and 10 wt. % LaNi5 and oxidized LaNi5 in the temperature range of 240–490 °C at 50 and 200 Torr initial pressures of N2O. The addition of LaNi5 decreases the energy of activation compared to that of La2CuO4 which has been explained based on the dispersity of NiO over La2CuO4.
N2O La2CuO4 La2CuO4 LaNi5 5–10 .%, 240–490°C N2O 50 200 . LaNi5 , . NiO La2CuO4.
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8.
The kinetics of Fe3+ and Cu2+ sorption from sulfate salt solutions by fibrous polyampholite have been studied.
Fe3+ Cu2+ , .
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9.
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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10.
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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11.
Ion-radical complexes Ti(IV) (O 2 ) are unreactive towards most oxidants except Ce(IV) and Cr2O 7 2– . The one-electron redox potential for the O2 coord./O 2 coord. couple lies between 1 and 1.6 V.
- O 2 Ti(IV) , Ce(IV) Cr2 O 7 2– . - O2 ./O 2 . 1 1,6 .
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12.
By IR spectroscopy and TPD the effect of vanadium content on the relative proportion of strongly acidic sites of V2O5/Al2O3 catalyst was studied.
- - V2O5/Al2O3.
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13.
According to kinetic studies on the reduction of commercial Co–Mo/Al2O3 and model catalysts in H2 at 523–773 K, the kinetic curves for the reduction process have been determined. The reduction rate is shown to be higher for the commercial catalyst. Activation energies Eact for the reduction of several forms of Mo and Co in Co–Mo/Al2O3 catalysts are presented.
H2 523–773 . , : Mo Co .
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14.
The species resulting in CO, CO+H2 or CO+D2O adsorption on supported Ni catalysts were followed by IR spectroscopy and their role in methane synthesis mechanism is discussed.
- , CO, CO+H2 CO+D2O . .
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15.
The activity of vanadia/titania catalysts in CO oxidation has been tested and found to be of the same order as that observed for unsupported vanadia; the simultaneous presence of vanadium-sodium compounds cancels the activity, probably because of the elimination of labile V=0 species at surface defects.
V2O5/TiO2 CO, V2O5; - , , V=0 .
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16.
Quasi-harmonic oscillations of chemiluminescence intensity at certain concentrations of the components for the (S–Cr2O 7 2– –UO 2 2+ ) system in concentrated sulfuric acid and chemiluminescence and dark stages with the participation of intermediates Cr(V), U(IV) and sulfur peroxide radicals (HS2O6 .) have been discovered. Chemiluminescence is attributed to the interaction of HS2O6 . compounds. The processes of deactivation of the excited states of uranyl involve the participation of Cr(V). A scheme for the oscillation chemiluminescence reactions is suggested.
(S–Cr2O 7 2– –UO 2 2+ ) H2SO4 , . Cr(V), U(IV) (HS2O6 .) HS2O6 . Cr(V) . .
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17.
The texture properties (specific surface area and porosity) of V2O5/TiO2 catalysts obtained from VO(acetylacetonate)2 have been studied. The presence of sodium leads to a marked decrease in the SBET values, probably as a consequence of the formation of Na-V bronzes, which lead to a rutilization of the support.
( ) V2O5/TiO2, - VO()2. SBET, , Na-V, .
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18.
Uncoordinated phosphine exchanges with that in Rh(AA)(CO)(PPh3) (AA—anthranilate and phenylanthranilate ions, respectively) via an SN2 mechanism.
Rh (AA) (CO) (PPh3) (AA — ) SN2.
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19.
The thermal decomposition of monomineral pyrite was studied in an inert atmostphere. From an analysis of the values of the thermal effects, an interpretation of the hree physicochemical processes recorded in the thermoanalytical curves is proposed.
Zusammenfassung Die thermische Zersetzung von monomineralem Pyrit wurde in inerter Atmosphäre untersucht. An Hand der Analyse der Werte der thermischen Effekte wird eine Beschreibung dreier, in den thermoanalytischen Kurven festgehaltener physikalischchemischer Vorgänge vorgeschlagen.

Résumé On a étudié la décomposition thermique de la pyrite, en atmosphère inerte. On propose une interprétation des trois processus physicochimiques enregistrés sur les courbes thermoanalytiques, qui repose sur l'analyse des effects thermiques.

- , .
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20.
By using the LKB 2277 thermal activity monitor, it is demonstrated that both ampoule and flow-through modes can be used to monitor the reaction parameters for chemical reactions. Theoretical relationships applicable to first-order reactions are proposed and compared with those reported in the literature. Mathematical relationships applicable to second-order reactions are also proposed. The experimental results confirmed the validity of the theoretical relationships and showed that flow microcalorimetry is a rapid technique in kinetic studies.
Zusammenfassung Es wird gezeigt, dass mit dem kalorimetrischen Messgerät LKB 2277 Untersuchungen zur Bestimmung der Parameter chemischer Reaktionen sowohl in Ampullen wie auch im Durchflussbetrieb möglich sind. Theoretische Beziehungen für Reaktionen 1. Ordnung werden abgeleitet und mit solchen aus der Literatur verglichen. Vorgeschlagen werden ferner mathematische Beziehungen, die sich auf Reaktionen 2. Ordnung anwenden lassen. Die experimentellen Ergebnisse bestätigen die Gültigkeit der theoretischen Beziehungen und zeigen, dass die Durchfluss-Mikrokalorimetrie eine Schnellmethode für kinetische Untersuchungen ist.

2277 , , , , , . , . , . , .
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