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1.
Mono-, di- and triphosphine ligands anchored by a Si–C bond to the surface of silica have been synthesized. Complexes of Pd(II) and Pd(O) with these ligands have been obtained. On the basis of elemental analysis and UV spectroscopy, structures of the complexes formed are suggested. The catalytic properties of the above complexes in the selective hydrogenation of cyclopentadiene are compared.
-, - , Si–C . Pd(II) Pd(O) . - . .
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2.
It has been established that in hydrogenation of 4-tert-butylphenol over Rh/-Al2O3 in isopropanol the addition of CH3COOH increases the yield of 4-tert-butylcyclohexanol.
, CH3COOH -4- 4- Rh/-Al2O3 .
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3.
The thermal behaviour of synthetic montmorillonite of relatively simple chemical composition has been studied and interpreted. Montmorillonite was prepared by hydrothermal synthesis at 300° and 8.8 MPa during 165 hours. With the methods of DTA, DTG, TG, X-ray diffraction analysis, infrared spectroscopy and electron microscopy it was proved that the synthetic montmorillonite is a monomineral sample and no differences from natural montmorillonite were observed.
Zusammenfassung Das thermische Verhalten synthetischer Montmorillonite verhältnismässig einfacher chemischer Zusammensetzung wurde untersucht und gedeutet. Montmorillonit wurde durch hydrothermische Synthese bei 300°C und 8.8 MPa in 165 Stunden hergestellt. Durch die Methoden der DTA, DTG, TG, Röntgendiffraktionsanalyse, Infrarotspektroskopie und Elektronenmikroskopie wurde erwiesen, daß synthetische Montmorillonit eine monominerale Probe ist und keine Abweichungen von natürlichem Montmorillonit beobachtet werden konnten.

. 165 300° 8.8 . , , , , , .
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4.
    
The choice of parameters according to the interacting bond method (IBM)/1/is under discussion for systems containing OH and CO-bond interacting with MgO crystal (100) plane. Various CO2 chemisorption forms on pure and hydroxylated surfaces are compared by a rough estimate of chemisorption heats.
(MBC) (1) ( (100) , OH CO. CO2 , .
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5.
    
The heterogeneous oxidation of n-decane initiated by azo-bis(isobutyronitrile) on quartz surface has been investigated in the temperature range of 80–100°C. At 100°C after the complete consumption of the initiator the oxidation proceeds at a measurable rate. Though heterogeneous oxidation is in many aspects similar to liquid phase oxidation, differences can be observed due to the specific role of the surface.
80–100°C - , - (). 100°C . , , , .
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6.
Studies of the reduction of nitrobenzene in the catalytic hydrogenation on soluble rhenium thiocomplexes and solid ReS2 and Re2S7 indicate that on homogeneous and heterogeneous rhenium sulfides it follows the same mechanism. Thiocomplexes are considered as possible analogs of the active sites in ReS2 and Re2S7 sulfide catalysts.
ReS2 Re2S7. , . ReS2 Re2S7.
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7.
The conditions for the formation of O 2 on VCl4/SiO2 catalysts have been investigated. It is shown that thermal vacuum treatment (TVT) of unhydrolyzed catalysts leads to partial hydrolysis of the surface vanadium complex caused by the silanol groups of the support. The ability of the catalysts to generate O 2 radicals was found to depend on the degree of hydrolysis caused by thermal vacuum treatment.
O 2 VCl4/SiO2. , , . , O 2 , .
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8.
The reactivity of allyl (o-halophenyl) ethers with zerovalent nickel complexes, with triphenylphosphine and pyridine as ligands, leading to benzo[b]furan derivatives has been checked. Cyclization products were not isolated, but deallylation, substitution, reduction and rearrangement products were obtained in low to moderate yields. Mechanisms are proposed to explain the formation of these side products.
-(o-) , , [b] . , , , , . .
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9.
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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10.
Activity and stability of rhodium catalysts is found to vary in parallel with metal dispersity. Treatment of reduced samples by air leads to a considerable (3–5 fold) increase of their activity in hydrogenation of 3-thiolene-1,1-dioxide to thiolane-1,1-dioxide.
. (3–5 ) 3--1, 1- -1, 1-.
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11.
The effect of inorganic salts (NaNO3, NaCl, Na2SO4, NaHCO3 and Na3PO4) on the selectivity of competitive hydrogenation of 2-methyl-3-butene-2-ol and 2-phenylpropene at 20 °C and atmospheric pressure on a 5%Pt/act. C catalyst in methanol solution was investigated. The dependence of the selectivity and of the initial rate of hydrogenation of the given equimolar mixture on the amount of sodium phosphate used in the modification of the platinum catalyst was measured.
(NaNO3, NaCl, Na2SO4, NaHCO3, Na3PO4) 2--3--2- 2- 20 °C 5% Pt . Na3PO4 .
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12.
Liquid-phase catalytic hydrogenatio of E-cinnamaldehyde was carried out by using new supported nickel catalysts (Ni/AlPO4, Ni/AlPO4–Al2O3 and Ni/AlPO4–SiO2) in methanol as solvent under low hydrogen pressure (4.1 bar) and 298 K. The kinetic orders are zero in H2 and aldehyde. The selectivity to the hydrogenaton of the C=C double bond is very high (>99%)
- (Ni/AlPO4, Ni/AlPO4–Al2O3 Ni/AlPO4–SiO2) (4,1 ) 298 . H2 . C–C (>90%).
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13.
The oxidation of amino acids by chloramine-T (CAT) in HCl medium at 30°C indicates simultaneous catalysis by H+ and Cl ions in the HCl concentration range of 0.04–0.12 M. The reaction is first order with respect to concentrations [CAT], [H+] and [arginine], but zero order with respect to [histidine]. The rate depends also on Cl concentration following 0.7th order. At HCl concentrations >0.12 M, the rate equation is:w=k[CAT] [amino acid]0.6 and is independent of the [Cl]. A suitable mechanism has been suggested.
-T (CAT) HCl (30°C) H+, Cl [HCl]=0,04–0,12M. [CAT], [H+] [] []. [Cl]0,7. [HCl]>0,12M =k · [CAT][]0,6 [Cl]. .
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14.
By IR and Raman spectroscopy it has been shown that excess MoO3 is bound molecularly on the surface of CdMoO4, presumably on sites of C2 and Ci symmetry. This increases the activity and selectivity of the catalyst in methanol oxidation to formaldehyde.
, , MoO3 CdMoO4, C2 Ci. .
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15.
The calorimetric methods used for the measurement of the enthalpy of formation of metallic systems are described and discussed. Special attention is paid to direct reaction calorimetry, dissolution calorimetry, precipitation calorimetry, combustion calorimetry... and non-reacting calorimetry is considered as an additional method from this point of view. Emphasis is placed on their particular field of application. Some recent developments are given.
Zusammenfassung Kalorimetrische Verfahren zut Messung der Bildungsenthalpie von metallischen Systemen wurden beschrieben und diskutiert. Besondere Aufmerksamkeit wurde dabei der Hinreaktionskalorimetrie, der Lösungskalorimetrie, der Fällungskalorimetrie, der Verbrennungskalorimetrie geschenkt, Nichtreaktionskalorimetrie wurde als eine zusätzliche Methode in dieser Hinsicht betrachtet. Das spezielle Anwendungsgebiet dieser Verfahren wird hervorgehoben und einige Neuentwicklungen gegeben.

, . , , , . . .
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16.
Modification of a V–Mo oxide catalyst by copper improves its catalytic properties due to the formation of a variable composition V–Cu–Mo–O phase with varying the ratio Mo/Me (Me=V+Cu).
T–Cu–Mo–O, Mo/Me, Me=V+Cu.
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17.
Porphyrin immobilized on silica and its complex with cobalt have been prepared and identified. Oxidation kinetics is described by the Michaelis-Menten equation.
- . - --.
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18.
The function of SO2 in CO oxidation on Pd-V catalysts is to transform a rapid heterogeneous-homogeneous process to a slower heterogeneous one. High concentrations of CO also exert the same effect. In the heterogeneous process an increase in the SO2 concentration increasing the degree of catalyst reduction with and without Pd additives, promotes CO oxidation.
CO - SO2 - . CO. SO2, , , CO.
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19.
The compensation effect (lgZ=aE+wb) appearing at the thermolysis of one substance under different experimental conditions is discussed. The compensation effect of one and the same substance has no other physical meaning except the simple confirmation of the analytical relationship between lgZ andE that follows from the Arrhenius equation, and of the impossibility to determineZ from any independent experiment. Values of the coefficienta can not be the measure of the ruptured bond strength.
(lgZ=+b), . , lgZ E ( ) Z . a .
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20.
    
- 1962 . .
The kinetics of reduction of a low-temperature CO shift catalyst (1962, GDR) by hydrogen at 150°C has been studied by the static circulation method. An empirical equation has been obtained for the range of maximum reaction rates.
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