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1.
It has been established that zeolites containing Pd and Cu ions catalyze the vapor phase oxidation of methylpyridines. In oxidation of 2-methylpyridine on PdCuNa-mordenite at 375 °C the yield of 2-pyridinecarbaldehyde is 40 % of its theoretical values.
, , Pd Cu, . 2- PdCuNa- 2- 375°C 40% .
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2.
The kinetics of decomposition of cumene hydroperoxide in the presence of 1,5,9-cyclododecatriene, catalyzed by MoO2(acac)2 has been studied at constant temperature (303 K) and at atmospheric pressure. The influence of substrate, catalyst and product concentrations on the rate has been established. The rate and equilibrium constants have been calculated.
1,5,9-. MoO2(acac)2. , .
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3.
The FeIII–MoVI–O catalyst was prepared from iso-ortho-Fe(OH)3 and -FeOOH. The catalysts differed markedly in their activity in methanol oxidation depending on the biography of their iron(III) oxide. The catalytic properties were found to depend on the pore structure of the catalyst.
Fe(III)–Mo(VI)–O, --Fe(OH)3 -FeOOH. , . , .
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4.
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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5.
The decomposition of isopropyl alcohol on natural chalcopyrite was studied by the microcatalytic pulse method in the region 473–673 K. The activity and selectivity of the catalyst was confronted with the temperature of its thermal activation. The apparent activation energies of decomposition were calculated for chalcopyrite activated in argon atmosphere at temperatures of 673, 773, and 873 K. The values of activation energy thus obtained are 61, 38, and 44 kJ mol–1 The liberation of sulfur from the lattice of chalcopyrite caused by thermal activation gives preference to dehydration over dehydrogenation at lower temperatures. The proportion of hydrogen and acetone in reaction products increases with temperature.
473–673 . , 673, 773 873 , 61, 38 44 /, . . .
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6.
The literature data on the degree of crystallinity of non-deformed poly(ethylene terephthalate) measured at various temperatures have been subjected to comparative analysis. There is no correlation between the results obtained by the different methods. The reason for this is shown to be the imperfections in the methods of determining the degree of crystallinity, which do not provide the true composition of the crystalline phase. Consideration has been paid to the validity of the main principles involved in the thermal method of determining the degree of crystallinity, so as to eliminate the imperfections in the existing methods and to provide the correct value of the mass of the crystalline phase. The phase composition of PET has been analyzed by the thermal method at different temperatures and conditions of crystallization. A marked difference from the literature data is observed in the range of low temperatures.
Zusammenfassung Eine vergleichende Analyse der Literaturangaben bezüglich des bei verschiedenen Temperaturen gemessenen Kristallisationsgrades von nicht-deformiertem Poly(äthylen-terephthalat) wurde durchgeführt. Zwischen den mit verschiedenen Methoden erhaltenen Ergebnissen besteht keine Korrelation. Es wurde gezeigt, daß der Grund hierfür in der Unvollkommenheit der Methoden zur Bestimmung des Kristallisationsgrades liegt, da diese nicht die wahre Zusammensetzung der Kristallinen Phase angeben. Die Gültigkeit der wichtigsten Prinzipien, welche die thermische Bestimmung des Kristallisationsgrades unter Ausschaltung der Unvollkommenheit der bestehenden Methoden gewährleisten und den richtigen Wert der Masse der kristallinen Phase angeben, wurden in Erwägung gezogen. Die Analyse der Phasenzusammensetzung von PET wurde durch die thermische Methode bei verschiedenen Temperaturen und Kristallisationsbedingungen durchgeführt. Ein deutlicher Unterschied zu den Literaturangaben kann im Bereich der niedrigen Temperaturen beobachtet werden.

. , , . , , . , , . . .
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7.
Dehydroxylation and catalytic conversion of m-xylene over dealuminated zeolites were studied.
- .
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8.
The maximum product size obtained during methanol to hydrocarbons transformation on medium and large pore zeolites and amorphous silica-aluminas is not governed by shape selectivity but it is a consequence of operational conditions and other process characteristics such as the occurrence of cracking reactions.
, , , .
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9.
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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10.
The influence of preparation of tin-molybdenum catalysts on their phase composition and activity has been elucidated. The mutual dissolution of Sn and Mo oxides leads to a considerable increase in their activities and selectivities in the partial oxidation of propylene to acetone.
. , .
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11.
Catalytic dimerization of propylene in the presence of macromolecular nickel complexes containing organophosphorus ligands has been studied. It has been established that the substitution of alkoxy groups of phosphorus atoms in the polymeric ligands does not affect the dimer composition but permits, within certain limits, to control catalyst activity.
, . , , .
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12.
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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13.
A series of heterogeneous polymeric molybdenum containing catalysts on the basis of weak acid cation exchanger Amberlite IRC-84 in an organic and water medium was prepared. The catalysts activity and selectivity in the epoxidation of propylene with tert-butyl hydroperoxide are compared. Data about the chemical structure of catalytically active molybdenum containing centres of the modified cation exchanger were obtained.
, , IRC-84 . .. , .
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14.
Methane adsorbed on MgO is activated to form CH3 fragments stabilized on cations and OH groups.
, MgO CH3-, OH-.
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15.
The rate of catalytic deactivation of H-ZSM-5 type zeolites and the nature of the resulting carbonaceous deposits have been studied in relation to zeolite Si/Al ratio, modifier content, and experimental reaction temperature.The conversion of 1-hexene carried out in a static cyclic system over a temperature range of 398–523 K has been used as a test reaction. The zeolites with higher aluminium content in the lattice have been found to exhibit not only enhanced activity over the initial period of operation but also slower deactivation and this in spite of the more intense carbon deposit buildup. The lower-temperature deposits are mostly saturated hydrocarbons in nature. As the zeolite Si/Al ratio is increased and reactant contact time protracted, the degree of carbonization of the deposit rises but only slightly. At elevated experimental reaction temperatures and particularly in the presence of water vapor, the effect is becoming increasingly pronounced.
H-ZSM-5 Si/Al , . 1- 398–523 . à , , . . Si/Al , , . , .
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16.
It is shown that the oxidative condensation of ethane on CoMo/-Al2O3 catalysts is in principle possible. The conceivable paths of this reaction are analyzed.
- .
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17.
A solution of diphenylamine in benzene is shown to produce cation-radicals on the surface of aluminosilicate, alumina and silica, whose electron acceptor properties for diphenylamine decrease in the sequence: aluminosilicata > alumina > silica.
, , . : > > .
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18.
The heats of adsorption of CO2 and NH3 were studied for sodium, lithium, calcium and decationized forms of natural mordenites. The exchange of Na+ for Ca2+ leads to increasing adsorption heats at low coverages. For CO2 the region of elevated heats corresponds to the formation of Ca2+ ... CO2 adsorption complexes. Two molecules of NH3 probably interact with each Ca2+ ion (or with the Li+ ions in Li-mordenite). The heats of adsorption of NH3 on decationized mordenite are much higher than those on calcium mordenite.
Zusammenfassung Adsorptionswärmen von CO2 und NH3 an der Na-, Li-, Ca- und dekationisierten Form von natürlichem Mordenit wurden bestimmt. Der Austausch von Na+ gegen Ca2+ führt zu einer Erhöhung der Adsorptionswärmen bei geringen Bedeckungen. Bei CO2 erfolgt im Bereich hoher Adsorptionswärmen die Bildung des Adsorptionskomplexes Ca2+ ...CO2. Mit jedem Ca2+-Ion (bzw. Li+-Ion im Li-Mordenit) treten wahrscheinlich zwei NH3-Moleküle in Wechselwirkung. An dekationisiertem Mordenit sind die Adsorptionswärmen von NH3 höher als an Ca-Mordenit.

, , . . Ca2+ ... CO2. B , , ( -). , -.


The authors would like to thank Dr. I. A. Belitsky for supplying the sample of natural mordenite. They also thank Professor S. P. Zhdanov for his interest and encouragement of this work.  相似文献   

19.
The uptake of sulfur reduces the overall activity of PtMo/Al2O3 and enhances that of CoMo/Al2O3 in conversion of cyclohexanol. Significant changes in selectivity indicate the existence of different active sites of the initial catalyst for hydro-dehydrogenation and dehydration. The differences in catalytic activity expressed in terms of overall TOF decrease with increasing sulfur treatment like for Ru and Ir promoted catalysts.
PtMo/Al2O3 CoMo/Al2O3. - . Ru .
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20.
Hydrogenation of C2H2:C2H4 mixtures using a double labelling method has been studied. Both in the presence and absence of ethylene the rate of acetylene hydrogenation on its partial pressure proceeds through a maximum and the rate is higher when ethylene is added. Using14C–C2H2 it was demonstrated that at low acetylene partial pressures the main route of acetylene hydrogenation was the formation of ethane and C4 hydrocarbons. Using14C–C2H4 it was also shown that at certain acetylene partial pressures the formation of ethane from ethylene completely ceased. Different surface species are suggested and a reaction mechanism is proposed.
C2H2:C2H4, . , , . C14–C2H2, , C4. C14–C2H4, , . .
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