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1.
Ligand exchange between the compounds Co(AA)2Py2 and Co(AA)Clpyx (x=1 or 3) formed in the, system, CO(AA)2–SnR2Cl2(R=Ph, Et) in chloroform with pyridine has been established to be catalyzed by SnR2Cl2. An interpretation of the catalytic action of SnR2Cl2 is suggested.
, Co(AA2py2 Co(AA)Clpyx (x=1 3) (Co(AA)2–SnR2Cl2 (R=Ph, Et) , SnR2Cl2. SnR2Cl2.
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2.
Rate constants of the three-body recombination for the elementary three-molecule stages in hydrogen oxydation have been calculated.
, .
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3.
The amount of PdO not dissolving in dilute HCl as a function of its content in palladium catalysts calcined in air has been determined. Mean size of Pd particles in the same samples has been evaluated from oxygen chemisorption. A comparison of these data indicates their correlation, which permits to determine Pd dispersity variations according to the solubility of supported PdO before reduction.
. . , .
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4.
IR spectra of H2S adsorbed on various types of catalysts have been studied by monitoring changes in the properties of their surfaces from the spectra of probe molecules. It is shown that H2S is adsorbed only dissociatively on basic centers (BC); on proton centers (PC) it forms H-complexes, while with the participation of strong Lewis acid centers (LAC), it is adsorbed both associatively and dissociatively.
- H2S , -. , H2S (), () -, ()- , .
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5.
The effect of UO3 on the acidity of MoO3–UO3/SiO2 catalysts has been studied by means of infrared spectroscopy of adsorbed pyridine. The surface acidity exhibited a maximum for the same U/(U+Mo) atomic ratio (=0.11) that yielded a maximum in total conversion for isobutene oxidation. The catalytic properties for oxidation are discussed in terms of the acidic properties of the samples.
UO3 MoO3–UO3/SiO2 . U/(U+Mo)=0,11, . , .
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6.
The strength of protonic sites and the concentration of acid centers in V2O5/Al2O3 catalysts have been estimated according to pyridine and ammonium adsorption.
V2O5/Al2O3.
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7.
The presence of CO2 on TiO2 affects the process of oxygen photo-adsorption depending on the hydroxylation state of the surface. In dehydroxylated samples CO2 blocks the formation of O 3 and O 2 . On H2O2/TiO2 samples pretreated in the range of 150–200°C it leads to CO2–O 2 species.
, Cu(II). . .
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8.
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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9.
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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10.
From the analysis of the detailed reaction mechanism and taking into account vanadium complex formation processes, a steady state kinetic equation has been derived to describe experimental data in a wide range of reaction conditions.
, .
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11.
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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12.
Supported Ni-Pd/SiO2 catalysts of different Ni and Pd composition were studied in n-butane hydrogenolysis. The reaction rate, selectivity towards methane, ethane and propane were determined. On the basis of these data the relationship between the size and composition of the active center and the possibility of surface segregation of one of the components is discussed.
Ni-Pd/SiO2 Ni Pd -. , . .
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13.
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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14.
The activating effect of nickel on MoS2 impregnated with an aqueous solution of Ni(CH3COO)2 and sulfided has been established to be proportional to the amount of active nickel incorporated as Ni2+ cations in the MoS2 lattice. MoS2 capacity for active nickel is limited and determined by the preparation method of the parent MoS2.
MoS2 ( Ni(CH3COO)2, ) Ni2+, . MoS2 «» .
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15.
Comparison of adsorptive properties of Rh–Al2O3 catalysts in relation to H2, O2 and CO as adsorbates points to different surface interactions between the adsorbates and metallic surface of the catalysts. The differences may result from the changing composition of bimetal surface in relation to the catalyst composition and/or from the changing stoichiometry of surface interactions of the adsorbates.
H2, O2 CO Rh–Ag/Al2O3 . , , () .
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16.
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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17.
The activity of various MoO3–SiO2 and WO3–SiO2 catalysts for the aromatization of propylene and butadiene has been investigated. The results obtained show a comparatively high aromatization activity of the catalysts for propylene to benzene and toluene. The direct conversion of butadiene to ethylbenzene, using WO3 on acid treated silica, is considered to be an alternative reaction pathway to the known metathesis step to ethylene and benzene.
MoO3–SiO2 WO3–SiO2 . . , WO3 .
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18.
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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19.
XRD, isothermal and temperature-programmed reduction (TPR) experiments were carried out with SiO2, SiO2–Al2O3 and -Al2O3 supported catalysts. Molybdena is in a more disperse state on supports containing more alumina and it is more reducible on SiO2–Al2O3 than on SiO2 or -Al2O3. TPR curves were shown to reflect connections between reduction kinetics and dispersity.
-, , SiO2, SiO2–Al2O3 -Al2O3. , , SiO2–Al2O3 SiO2 -Al2O3. .
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20.
Using the flow ESR method, the rates of the reaction between the radical complex Ti(IV)(O 2 ) and one-electron reductants in aqueous solution have been measured. The redox potential for the Ti(IV) (O 2 )/Ti(IV) (O 2 2– ) couple is about 1.7 V.
Ti(IV)(O 2 ) . - Ti(IV)(O 2 )/Ti(IV)(O 2 2– ) 1,7 .
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