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1.
In this paper the adsorption properties towards oxygen and the catalytic oxidation properties of furan and n-butene-1 on a MnMoO4-based catalyst have been compared. Different forms of adsorbed oxygen are responsible either for the oxidation of furan to maleic anhydride or of furane and n-butene-1 to carbon oxides.
--q MnMoO4. , --1 .
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2.
The catalytic properties of cation-substituted forms of oxidized charcoal in the liquid-phase oxidation of cumene have been investigated. It has been shown that oxidized charcoal inhibits, and its salt forms catalyze the reaction. The catalytic activities of ion-substituted charcoals depend on both the nature of the metal and the amount of supported ions.
. , , — . , .
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3.
Data have been obtained on the activities of 19 alkali halides in photoadsorption of O2 and CO2, photooxidation of H2 and CO and photodecomposition of H2O and CO2.
19 O2 CO2, H2 CO H2O CO2.
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4.
Reduction of carbon dioxide with methane over Ni-catalyst   总被引:5,自引:0,他引:5  
The reaction CO2+CH4=2CO+2H2+60 kcal/mol was carried out over some transition metal catalysts (Ni, Fe and Co) and Ni/Al2O3 catalyst was then found to be the best for the reaction. The reaction rate expression and the apparent activation energy were also obtained over the Ni catalyst.
CO2+CH4=2CO+2H2+60 / (Ni, Fe Co). Ni/Al2O3 . Ni-.
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5.
Kinetics of Ru(III) catalyzed oxidation of methanol, ethanol, n-propanol, n-butanol, isopropanol and iso-butanol by N-bromosuccinimide (NBS) in the presence of Hg(II) acetate have been studied in acid medium. The oxidation exhibits a fractional order in [alcohol] and first order in [NBS]. The applicability of Taft's equation was tested. The probable mechanism is discussed.
, , -, -, - () Hg(II), Ru(III), . . . .
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6.
A fractal scaling law has been applied to products of carbon monoxide hydrogenation over silica supported rhodium catalysts. The results indicate structure sensitivity and that the type of structural sensitivity is product dependent.
, . , , .
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7.
Benzene alkylation by C2–C4 olefins in the presence of hydrogen over a steam-treated zeolite catalyst containing lanthanum and nickel, has been studied. The promoting action of hydrogen on benzene alkylation by propylene has been established.
C2–C4 , . .
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8.
Electron paramagnetic resonance studies on intermediates and final active catalyst material used for partial oxidation of anthracene to anthraquinone are reported.
, .
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9.
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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10.
Hydrogen adsorption on chromia supported Pd, Rh and Pt was studied under various pretreatment conditions. The reduction temperature influences strongly the hydrogen uptake for all these metals. Platinum supported on chromia shows an unusually high hydrogen adsorption stoichiometry.
Pd, Rh Pt, Cr2O3, . , . Cr2O3 .
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11.
Thermal studies on aluminium substituted copper chromite spinel oxide, CuCr2–x Al x O4 (x=0.2 tox=0.8) by DSC show that with 20% replacement of Cr by Al, the phase transition temperature of the spinel is lowered but on further increasing the percentage of Al the phase transition temperature becomes higher than that of CuCr2O4. The enthalpy change for phase transition however decreases gradually with increasingx.
Zusammenfassung Mittels DSC wurde ein aluminium-substituiertes Kupferchromitspinelloxid, CuCr2–x Al x O4 mitx=0,2-0,8 thermisch untersucht. Wird 20% des Cr durch Al ersetzt, sinkt die Phasenübergangstemperatur ab, bei weiterem Anwachsen des Aluminiumgehaltes steigt sie jedoch über die von CuCr2O4 hinaus an. Die Enthalpieänderung des Phasenüberganges steigt mit anwachsendemx allmählich an.

CuCr2–x Al x O4 (x=0,2–0,8) , 20% , , , , CuCr2O4. , x.


The authors thank Mrs P. P. De of Rubber Technology Centre, Indian Institute of Technology, Kharagpur for her help with the DSC studies.  相似文献   

12.
Thermal analysis of manganese dioxide in controlled atmospheres   总被引:1,自引:0,他引:1  
TG and DTA curves of-MnO2 have been obtained in nitrogen, air and oxygen. The reactions MnO2Mn2O3 and Mn2O3 Mn3O4 were observed in the ranges 450° to 600° and 750° to 1100° respectively, and the decomposition temperatures are affected by the partial pressure of oxygen. The endotherm at 1200° is unaffected by the atmosphere and is not accompanied by weight loss. It is, therefore, due to a polymorphic transformation of Mn3O4 rather than formation of MnO. Reaction to form MnO was observed by TG in nitrogen above 1400°, but did not occur on heating in oxygen to 1500°.
Zusammenfassung Die TG und DTA Kurven von-MnO2 wurden in Stickstoff, Luft und Sauerstoff ermittelt. Die Umwandlungen MnO2 Mn2O3 und Mn2O3 Mn3O4 wurden im Temperaturbereich von 450° bis 600° bzw. 750° bis 1100° beobachtet. Die Zersetzungstemperaturen werden durch den partiellen Sauerstoffdruck beeinflußt. Der endendothermische Vorgang von 1200° bleibt von der Atmosphäre unbeeinflußt, ist mit keinem Gewichtsverlust verbunden. Er ist eher einer polymorphen Umwandlung von Mn3O4 als der Bildung von MnO zuzuschreiben. Die Bildung von MnO wurde thermogravimetrisch in Stickstoff oberhalb 1400° beobachtet, nicht jedoch in Sauerstoff bis zu 1500°.

Résumé Etude de-MnO2 par TG et par ATD, dans l'azote, dans l'air et dans l'oxygène. Entre 450 et 600° on observe la réaction MnO2Mn2O3 et entre 750 et 1100° Mn2O3 Mn3O4. La pression partielle de l'oxygène influence la température de la décomposition. A 1200°, il apparaît un phénomène endothermique undépendant de la nature de l'atmosphère et qui ne s'accompagne d'aucune variation de poids. C'est pourquoi il est attribué à une transformation polymorphique de Mn3O4 plutôt qu'à la formation de MnO. Celle-ci s'observe en TG au-dessus de 1400°, dans l'azote, mais ne se produit pas par chauffage dans l'oxygène jusqu'à 1500°.

, -MnO2. , MnO2 Mn2O3 Mn2O3 Mn3O4 450°–600° 750°–1100°, , . 1200° . , n34, MnO. MnO 1400°, , 1500° .


The authors wish to thank Dr. D. Dollimore and Dr. R. C. Mackenzie for suggesting the problem, and the S.R.C. for a research assistantship to D.M.T.  相似文献   

13.
A flow reactor for kinetic studies of heterogeneous catalytic reactions with simultaneous X-ray phase analysis of the catalyst is described. As an example, the correlation between the selectivity of acetylene hydrogenation and the -Pd hydride concentration in palladium catalysts is shown.
, . -Pd .
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14.
A pulse-chromatographic method has been developed for the estimation of molybdenum surface by selective adsorption of oxygen at –78°C in cobalt-molybdenum-alumina catalysts. The surface concentrations of molybdenum in a series of catalysts of different compositions were compared with the activities for cyclohexene hydrogenation and for thiophene hydrogenolysis.
- –78°C -- . - .
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15.
The kinetics of formation of acetic acid, methanol, methyl acetate and hydroperoxide in the autoxidation (463–503 K) and initiated oxidation (413 K) of pentaerythritol tetraacetate has been studied. A scheme for product formation is proposed.
, , (463–503 ) (413 ) . .
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16.
H2S promotes remarkably the catalytic cracking of n-butane and the isomerization of cyclopropane over various Na zeolites, presumably because of the formation of new Brönsted acid sites on catalyst surface.
H2S - Na-, , .
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17.
The systems CuO–Al2O3 and ZnO–Al2O3, as model systems of low temperature shift catalysts, have been studied in the temperature interval 100–700°C. The changes of their phase composition and surface area, influenced by gas atmosphere have been studied by X-ray, IR analysis and low temperature nitrogen adsorption.
CuO–Al2O3 ZnO–Al2O3 CO 100–700°C. , - .
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18.
A method is proposed for the evaluation of quantum yields of photochemical reactions studied in the presence of absorbing additives using cylindrical sample tubes.
.
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19.
The results are presented of an experimental investigation of the kinetics of evolution of C n H m , CH4, CO and H2 in the course of shale thermal decomposition. The experiments were carried out with a complex experimental set-up consisting of a derivatograph, a chromatograph and a spectrophotometer, with shale samples of different fractions from different seams of basic commercial deposits. In spite of the differences in the sites of taking the samples and in their characteristics, the reaction rate curves for each gas are close to one another.
Zusammenfassung Ergebnisse einer experimentellen Untersuchung der Kinetik der Freisetzung von C n H m , CH4, CO und H2 im Verlaufe der thermischen Zersetzung von Schiefern werden mitgeteilt. Die Versuche wurden mit einer komplexen, aus einem Derivatograph, einem Chromatograph und einem Spektrophotometer bestehenden Ausrüstung vorgenommen. Untersucht wurden Schiefer von verschiedenen, kommerziell abgebauten Lagerstätten. Obwohl sich die Schieferproben hinsichtlich der Lage und der Charakteristik des Vorkommens unterscheiden, verlaufen doch die Reaktionsgeschwindigkeitskurven für jedes Gas nahezu gleich.

n m , 4, , H2 . , , , . , .
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20.
The capacity of ZnO with respect to the photo- and X-ray adsorbed, as well as postadsorbed oxygen is shown to depend on the temperature. It is suggested that this dependence cannot be attributed to either the thermal annealing of the induced sites or the thermal desorption of the adsorbed molecules.
O , - , , , . , .
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