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1.
Catalytic properties of Cu(Acac)2 anchored to shock-compressed MgO and MgF2 in model reactions of hydrogenation and isomerization of heptene-1 have been studied. It is shown that by changing the defect structure of the support via shock treatment at various temperatures, the activity and selectivity of metal complex catalysts can be affected.
Cu(Acac)2, MgO MgF2 -1. , , , .
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2.
Several effects on the hydrogenation of carbon monoxide in propanol in presence of ruthenium catalysts are examined. The homologation reaction is not observed, only propyl formate and propyl acetate are produced with any ruthenium catalyst. The pH-value is an important parameter: in acid media, the yield of propyl formate is noticeably increased indicating different catalytic active species. The addition of cesium salts is also benefitial for formate formation. This is not the case when water is associated with propanol as solvent. Finally, no ethylene glycol is detected. The process is found to be homogeneous and methanol seems to be the precursor of methyl formate.
, . , . : , . . , . . , -, .
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3.
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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4.
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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5.
A study has been made of temperature programmed desorption (TPD) of NH3 and H2O from samples of NH4X and CoNH4X zeolites of various degree of exchange. NH3 TPD peaks could be explained by interaction of NH3 with different Brönsted and Lewis acidic centers. Moreover a water peak at high temperatures allowed interpretations of the dehydroxylation, and by reason of the characteristic desorption temperatures a particular state of the Co2+ ions in the CoNH4X zeolites is postulated.
- () NH3 H2O NH4X CoNH4X . NH3 NH3 =qs . . Co2+ CoNH4X.
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6.
Reducibility of NiO/Al2O3 and CuO–NiO/Al2O3 catalysts has been studied by the TPR method within the temperature range 293–873 K. The results suggest that the copper content essentially does not influence the reducibility of NiO/Al2O3.
NiO/Al2O3 CuO–NiO/Al2O3 TPR 293–873 . , NiO/Al2O3.
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7.
The kinetics and mechanism of redox reactions of U3+ ions with 2-chloro and 2-bromopropanoic acids were studied. The influence of pH led to the determination of the rate constants corresponding to two parallel steps. The influence of binary mixtures on the reaction rate was followed. The kinetic results for halogen-substituted carboxylic acids forming an isokinetic series have been compared.
U+3 2-- 2- . pH . . , .
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8.
The rate constants for Br(2P1/2) and Br(2P3/2) atoms in the reaction Br+CH3FHBr+CH2F in photobromination of CH3F have been determined. Their ratio is 10–(2.6±0.5) exp(10100±1000/RT) in the temperature range of 60–200 °C.
Br(2P1/2) Br(2P3/2) Br+CH3FHBr+CH2F CH3F. 60–200 °C 10–(2,6±0,5) exp (10100±1000/RT).
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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.
For the first time ESR spectra of47Ti-enriched Ziegler system Ti-TIBA in toluene have been studied. For the ratio Ti/Al1, more accurate h. f. s. constants have been found. For Ti/Al1/15 no h. f. s. have been observed, which is ascribed to ordering due to the cooperative Jahn-Teller effect.
TiCl4+ 47Ti. Ti/Al1 . Ti/Al1/15 , -.
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11.
Radical intermediates formed at 25°C in the presence and absence of oxygen during the photolysis of anthraquinone in aromatic, cyclic and aliphatic hydrocarbon solvents were trapped by 2,6-dichloronitrosobenzene, 2,6-dibromonitrosobenzene and 2,4,6-tribromonitrosobenzene. The resulting nitroxide radicals have been characterized in situ by ESR spectra.
: 2,6-, 2,6- 2,4,6-— , , 25°C. .
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12.
The activity in n-butane hydrogenolysis of Rh/TiO2 (0.6 wt.% Rh) catalysts prepared by ion exchange and reduced at different heating rates is reported. The heating rate has no major effect on the properties of the catalysts (similar dispersions and activities are achieved). Carbonaceous residues formed at high temperature are removed by hydrogen at room temperature, thus leading to recovery of the activity.
Rh/TiO2 (0,6 .% Rh), , -. : . , , , , , .
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13.
The oxidation of methane on supported chromia was studied at temperatures varying between 423 and 743 K and CH4/O2 ratios between 1 and 9 in a differential reactor. The main reaction products observed were carbon monoxide and formaldehyde. The rates of reaction obey a power law expression.
, 423 743 CH4/O2 1 9, . . .
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14.
The chemisorption of hydrogen on Ni/SiO2 has been studied by measuring temperature programmed desorption on various samples under various experimental conditions. Two peaks are found, which can be related to a weakly and to a strongly bound species of chemisorbed hydrogen. Their analysis has been performed by a method which makes possible to determine whether a certain kinetic model can describe the entire desorption process or to assign a clear meaning to the corresponding kinetic parameters.
Ni/SiO2 - . . , , , , .
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15.
V4+ ions in slightly associated states are supposed to play the role of V–P–O/SiO2 active sites. V4+ ions are reduced to V3+ during deactivation of the V–P–O/SiO2 catalyst.
V–P–O/SiO2 V4+ . V–P–O/SiO2 V4+ V3+.
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16.
Conditions are found for the preparation of Pt catalysts providing the formation of epoxy-derivative in the reaction of cyclohexene with an O2/H2 mixture.
Pt .
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17.
The physico-chemical characterization of magnesium-modified ZSM-5 zeolite catalysts has been performed by differential scanning calorimetry. Evidence has been found of the formation of magnesium oxide and the magnesium spinel phase in alumina-bonded ZSM-5 catalysts. DSC proved a suitable technique for characterization of these systems.
Zusammenfassung Mg-modifizierte ZSM-5-Zeolithkatalysatoren wurden durch DSC charakterisiert. Es wurden Beweise für die Bildung von Magnesiumoxid und Magnesiumspinell in ZSM-5/Aluminiumoxid-Katalysatoren gefunden. DSC hat sich zur Characterisierung dieser Systeme als geeignet erwiesen.

- 3CM-5, . - - . .


This work was carried out within the Progetto finalizzato Energetica 2 of the National Research Council of Italy.  相似文献   

18.
New highly active catalysts for metathesis of olefins were obtained through the interaction of bis(acetylacetonato)dioxymolybdenum(VI) with surface OH groups of -Al2O3 and subsequent reduction in H2 or CO.
()(VI) OH -Al2O3 H2 CO .
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19.
    
- 1- (I) 2--1-(II) CCl4. CCl3- I(lgKI=5,1±0,1–11300±1300/19,14T II(lgKII=4,6±0,1–8800±400/19,14T). - , .
The kinetics of interaction of 1-propene (I) and 2-methyl-1-propene (II) with CCl4, initiated by X-rays, has been studied. The rate constants for the addition of CCl3 radicals to I and II are lgkI=(5.1±0.1)–(11300+1200)/19.14T and lgkII=(4.6±0.1)–(8800±400)/19.14T, respectively. The Mellous-Burton method has been applied for the calculation of transfer constants for polychloroalkyl radicals containing one or two monomeric units.
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20.
ESR studies of the thermal stability of anion radicals O on the MgO surface have revealed that most stable (at T>420 K) are O with g 2=2.032 and g 3=2.044, whereas anion radicals with g 1=2.042 are destroyed at T<400 K and possess the highest heat of [O·O2] complex formation.
- O MgO. , O g 2=2.032 g 3=2.044, 420 , O g 1=2.042 400 . , [O·O2] - O g 1=2.042.
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