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1.
Photoadsorption activity of SnO2 with respect to O2 and NO after CO chemisorption has been revealed to be drastically increased. Photoadsorption is suggested to be sensitized by surface carbonates formed due to CO chemisorption.
. , .
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2.
Gravimetric measurements show that SO2 is chemisorbed on fully hydroxylated alumina samples. Infrared results from SO2 adsorption on silica indicate that the species are not hydrogen-bonded. Experiments carried out with preadsorption of CO2 on alumina provide evidence that SO2 interacts with free hydroxy groups leading to-SO3H species.
, SO2 . SO2 , . , CO2 , , SO2 , -SO3H.
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3.
Approximate equation to calculate the effectiveness factor of catalyst for SO2 oxidation to SO3 has been derived. Calculated data agree well with those predicted by a quasi-homogeneous model.
. .
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4.
TPD studies of the established formation of ethane, ethylene and propylene in the irradiated CH4/TiO2 system indicate that the process is most effective under X-ray or long-wavelength light irradiation behind the edge of the fundamental absorption band of the oxide.
, CH4/TiO2, .
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5.
Catalytic ammoxidation of propylene was studied using Fe2O3–MoO3/SiO2 catalysts, which have been prepared following a special method. Interaction of ammonia with the catalysts was studied by means of IR spectroscopy and gravimetrically using a McBain balance. Introduction of iron into MoO3/SiO2 catalysts modifies acidic as well as redox properties.
Fe2O3–MoO3/SiO2 . . - . MoO3/SiO2 , .
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6.
By metal impregnation of selected naturally occurring organic materials followed by controlled carbonization, metal semicoke catalysts can be readily prepared. These catalysts have been tested in the synthesis of hydrocarbons and alcohols from CO/H2 and CO2/H2 mixtures. Fe and Co preparations have been used. Relatively high temperatures are required when using these catalysts, which are quite active for synthesis using CO2 and H2. The pressure (5150 kPa) is very favorable both for the synthesis of liquid hydrocarbons (C5–C30) and alcohols (C1–C5).
. CO/H2 CO2/H2. Fe Co. , CO2 H2. 5150 ) (C5–C30) (C1–C5).
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7.
Adsorption of hydrogen, oxygen and carbon monoxide on Pd–Ag/Al2O3 catalysts of different compositions within the temperature range from 293 to 773 K has been investigated. Adsorption measurements have been carried out by the pulse chromatographic method. The results obtained reflect interactions of the above adsorbates with the alloy surface, strongly enriched in silver atoms, as a result of surface segregation processes.
, Pd–Ag/Al2O3 293–773 K. . , , .
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8.
Cyclohexene oligomerizes over the TiCl4–Al2O3 system at 423 K. The length of the oligomer chain depends on the number of TiCl3O–Al–groups on the alumina surface.
TiCl4–Al2O3 423 . TiCl3O–Al .
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9.
By means of thin-layer and gas chromatography the reaction products have been determined in the oscillation system of aniline, KBrO3 and H2SO4. These products include: 2-bromoaniline, 4-bromoaniline, 2,4-dibromoaniline, 2,4,6-tribromoaniline, 1,4-benzoquinone, 2-bromo-1,4-benzoquinone, 2,6-dibromo-1,4-benzoquinone and a brominated oxidation product. The brominated aniline derivatives do not exhibit an oscillating behavior, and the addition of these substances to an oscillating mixture damps the course of other oscillations.
, KBrO3 H2SO4. : 2-, 4-, 2,4-, 2,4,6-, 1,4-, 2--1,4-, 2,6--1,4- . , , , .
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10.
The anodic and cathodic polarization of a platinum electrode in K2O–V2O5 melt have been studied. The dissolved oxygen is shown to be ionized. Diffusion coefficients of oxygen in K2O–V2O5 and Na2O–V2O5 melts at various temperatures and K/V ratios are presented.
K2O–V2O5. , . K2O–V2O5, Na2O–V2O5 K/V.
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11.
The spectrum of an intermediate, ascribed to nitrosopentane, has been detected in the photolysis of SO2-pentane-NO mixtures. This may be explained by a radical photolysis mechanism involving an initial H-atom abstraction from the pentane molecule by SO2.
SO2--NO , . , H .
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12.
Irradiation of a C6F5H–C6F5D mixture at 1 Torr by a tunable CO2 pulse laser brings about chiefly dissociation of one component depending on the frequency of emission absorbed by the proper molecules. The addition of radical acceptors increases the selectivity by suppressing secondary reactions.
C6F5H C6F5D 1 CO2-, , . .
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13.
A supported ruthenium catalyst on alumina prepared from Ru3(CO)12 has been studied by infrared and X-ray photoelectron spectroscopy (XPS). The triatomic cluster is retained on the support but breaks down at 150°C. Complete elimination of the carbonyl groups requires heating at 350°C under vacuum. XPS studies show that the decomposed catalyst does not change on further reduction in H2 at 400°C. The ruthenium atoms remain trapped within the pores of the support.
Al2O3, Ru3(CO)12, (XPS). , 150°C . 350°C . XPS , H2 400°C . .
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14.
The detailed composition of the reaction mixture and, in particular, SO3 concentration, in SO2 oxidation over vanadium catalysts, have been determined experimentally. Both oxidized and reduced catalysts were shown to absorb a considerable amount of SO3, the desorption rate of SO3 being lower than that of its adsorption.
, , . , , SO3, .
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15.
CH4 photooxidation on V/SiO2 catalyst in the presence of gaseous oxygen has been studied by the mass-spectometric method. It has been established that CO2 forms due to the interaction of CH4 with surface oxygen anions bonded to vanadium ions. Photodecomposition of V4+O 2 species formed in O2 adsorption on reduced vanadium ions leads to the reoxidation of the latter.
- CH4 V/SiO2 . , CO2 CH4 , . V4+O 2 O2 , .
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16.
Three reforming catalysts Pt/Al2O3, Pt–Ir/Al2O3 and Pt–Re/Al2O3 have been sulfurated by H2S and tested by their activities in benzene hydrogenation. By treatment at 500°C under hydrogen flow only a part of the initial activity of the non-sulfurated catalyst is retained. So only a part of the adsorbed sulfur is easily removed in these conditions. The remaining sulfur for each of the catalysts (Pt/Al2O3, Pt–Ir/Al2O3 and Pt–Re/Al2O3) gives the same atomic ratio of 0.5 sulfur atom per accessible metallic atom.
Pt/Al2O3, Pt–Ir/Al2O3 Pt–Pe/Al2O3 . 500°C H2 . . ., . (Pt/Al2O3, Pt–Ir/Al2O3 Pt–Pe/Al2O3) 0,5.
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17.
Following hydrogen treatments at high temperature a decrease in hydrogen chemisorption at room temperature is observed in almost all group VIII elements supported on SiO2 or Al2O3. The effect is attributed to self inhibition by strongly chemisorbed hydrogen on the metals.
VIII , SiO2 Al2O3. .
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18.
Studies of SO2 oxidation on a molten component of vanadium catalysts in non-steadystate conditions indicates that the kinetics agree fairly well with an oxidation-reduction mechanism. In the low temperature range (<790 K) tetravalent vanadium can be partially crystallized.
. , - . ( 790 ) .
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19.
Adsorption heats of hydrogen, oxygen and carbon monoxide on titanium nitrides have been measured calorimetrically in the temperature range from 473 to 673 K. With increasing Me/N ratio, the adsorption heat of oxygen grows.
, 473–673 . Me/N.
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20.
The deactivation behavior of Fe2O3–MoO3/SiO2 catalysts with different Fe2O3+MoO3 content in the oxidation of methanol to formaldehyde is investigated. A simplified reaction-deactivation kinetic model is presented and used to compare and discuss the different behaviors.
Fe2O3–MoO3/SiO2 Fe2O3+MoO3 . : -.
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