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1.
    
A higher activity of Na–X than Na–Y in CH3SH+SO2 reaction at 343 was observed. The increase of the copper content in the samples causes an increase of their activity. Water, sulfur, dimethyl disulfide, dimethyl trisulfide and sometimes dimethyl sulfide are registered as reaction products. (CH3)2S3 is formed as a result of the reaction between sulfur and (CH3)2S2.
, Na–X , Na–Y CH3SH+SO2 343 . . , , , , . (CH3)2S2 (CH3)2S3.
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2.
The kinetics of Ln2O3 hydration (Ln=Sm, Ho, Yb, Lu) have been studied at room temperature and atmospheric pressure, as have the influence of the activation temperature and the method of preparation of the oxides.The best correlation coefficients are obtained for a diffusion mechanism. If a structural relationship between the C-Ln2O3 and their precursors is considered, the possibility arises of the existence of defect planes in the oxides prepared from the hydroxide and carbonate. This facilitates the hydration process through a diffusion mechanism in the case of the rare earth sesquioxides prepared from the above precursors.
Zusammenfassung Die Kinetik der Hydratisierung von Ln2O3 (Ln=Sm, Ho, Yb, Lu) wurde bei Raumtemperatur und atmosphärischem Druck bezüglich des Einflusses der Aktivierungstemperatur und der Art der Darstellung der Oxide untersucht. Die besten Korrelationskoeffizienten werden für einen Diffusionsmechanismus erhalten. Wenn die strukturelle Beziehung zwischen den C-Ln2O3 in Betracht gezogen wird, so ergibt sich die Möglichkeit der Existenz von defekten Gitterebenen in den aus Hydroxiden und Carbonaten hergestellten Oxiden. Dies erleichtert den Hydratisierungsprozeß durch einen Diffusionsmechanismus im Falle von aus den oben genannten Vorstufen hergestellten Sesquioxiden der Seltenen Erdmetalle.

Ln2O3, Ln=Sm, Ho, Yb, Lu, . . , , . .


We thank the CAICYT (Project No. 1377/82) for financial support.  相似文献   

3.
Catalytic and acidic properties of bifunctional catalysts containing faujasite, superhigh-silica zeolite and mordenite have been studied in isomerization of C8-alkylaromatic hydrocarbons.
C8 , , - .
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4.
Influence of the strength and concentration of non protic centers on the catalytic activity of metal-zeolite catalysts in isomerization of n-butane has been studied. A relationship between the specific activity and the center strength is suggested.
-. , .
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5.
Some peculiarities of reduction of one-electron oxidants, Ru(bpy) 3 3+ and Ru(bpy)2(py) 2 3+ , in the absence of catalysts (when oxidation of the oxidant's ligands occurs) and in their presence (when also oxidation of water to dioxygen occurs) are discussed. Both oxidation reactions are thought to have a common intermediate.
Ru(bpy) 3 3+ Ru(bpy)2(py) 2 3+ ( -) ( ). , .
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6.
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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7.
Comments are given on the paper Alternative Interpretation of Infrared Spectra of the Zeolite NaHY+Butene-1 System of Forster and Seelemann /2/. Our previous paper /1/ was partly revised but the usefulness of comprehensive studies by infrared and temperature-programmed desorption methods has been emphasized.
: NaHY+-1. [2]. [1] , - .
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8.
The products of selective oxidation are shown to be formed via a stepwise mechanism with participation of surface allylic complexes. A successive transformation of -allyl to -allyl and further to acrolein is possible. The products of complete oxidation may be formed through surface carbonate-carboxylate complexes via either a stepwise mechanism involving the catalyst's oxygen, or a concerted mechanism with the participation of molecular oxygen.
, . - -, . - , .
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9.
    
A negative influence of low concentration and of high dispersity of -Al2O3 supported rhenium (1.04 wt.% and 10.4 wt.% l=1.5–7.1 nm) on its specific activity for hydrogenation and hydrogenolysis of benzene at 365–573 K is described.
, -Al2O3 (1,04 .% 10,4 .%, l=1,5–7,1 ), 363–573 .
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10.
The hydrogen sorption of carbon-supported platinum catalysts, studied by the potentiodynamic method, differs significantly from that of unsupported platinum. The difference depends on the preparation method and on the nature of the support. Possible explanations are suggested as (i) some kind of interaction between metal and support atoms during impregnation, (ii) high dispersity (amorphous structure) and (iii) hydrogen spillover onto the carbon support.
Pt/C, . . (I) , (II) ( ), (III) .
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11.
Magnesia aerogel activated by hydrogen spillover at 430 °C or at 200 °C becomes a catalyst for the hydrogenation of ethylene. This catalytic activity, observed already at 50 °C, is further enhanced by a treatment in oxygen at 430 °C.
, 430 200°C, . 50°C 430°C.
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12.
Chloroquine sulphate, like the phosphate, is an antimalarial formulation widely used in the tropics. The stability of such formulations is therefore of interest in the combat against malaria. A DSC study has been made of the effects of exposure to the sun, heat and UV radiation on the stability of chloroquine sulphate, similarly as performed earlier for chloroquine phosphate. When freshly recrystallized from a water-acetone mixture, chloroquine sulphate exhibits two endothermic peaks, at 169.4° and 204.7°, for the expulsion of crystal water (one molecule) and for the melting process, respectively. The exposure of chloroquine sulphate to the sun, heat and UV radiation leads to splitting of the peak for melting.
Zusammenfassung Chloroquine-Sulfat ist ebenso wie das entsprechende Phosphatderivat ein in den Tropen weitverbreitet angewandtes Antimalaria-Präparat. Die Stabilität dieses Präparates hat damit Bedeutung für die Malariabekämpfung. Die vorliegende Arbeit ist eine Erweiterung einer Untersuchung über den Effekt der Einwirkung.von Sonne, Hitze und UV-Strahlen auf die Stabilität von Chloroquine-Phosphat auf Chloroquine-Sulfat. Aus Wasser-Aceton-Mischungen frisch kristallisiertes Chloroquine-Sulfat zeigt zwei endotherme Peaks bei 169,4 und 204,7 °C, die durch Abgabe von Kristallwasser (ein Molekül) bzw. durch den Schmelzvorgang bedingt sind. Wird Chloroquine-Sulfat der Sonne, Wärme oder UV-Licht ausgesetzt, so wird der dem Schmelzvorgang zuzuscheibende Peak aufgespalten.

, -, , . . , . , , 169,4 204,7°, , , . , .
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13.
Several new supported K2Cr2O7 reagents are used in the oxidation of secondary alcohols. The influence of the number of active sites and the nature of solid support on the yield is discussed. The influence of the structure of alcohol on the yield of ketone is analyzed.
K2Cr2O7 . . .
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14.
    
- 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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15.
    
A simple method for preparing carbohydrate-bis-phosphinites of methyl -D-glucopyranosides of glucose and galactose protected by benzylidene groups in 4,6-position leads to chelating ligands which are useful in the asymmetric hydrogenation of prochiral aminoacid precursors catalyzed by rhodium(I), producing optical yields up to 75%. Cationic complexes are particularly active.
--D- 4,6- - (I) 75%. .
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16.
Zusammenfassung Die Kinetik der Ausbrennung organischer Stoffe im Ziegelscherben wird verfolgt und erläutert. Die Möglichkeiten der Beeinflussung des energetischen Aufwandes unter Nutzung moderner analytischer Methoden sind festzustellen. Bei einem diffusen Ausbrennen ist die Dichte und Durchlässigkeit des Scherbens massgebend. Praktische Anwendungsmöglichkeiten verschiedener auszubrennender Stoffe in unterschiedlichen Rohstoffen der Ziegelindustrie.
The kinetics of burn-out of organic materials in bricks has been followed and explained. It is to establish that using new analytical methods the energy consumption can be influenced. The diffuse burn-out is determined by the density and permeability of bricks. There is a possibility for practical use of the results in the brick-industry with the different compounds to be burnt out from various raw materials.

$ . , . . .
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17.
Chemical oscillatory behavior in the uncatalyzed bromate oxidation of hydroquinone and nitrophenols is reported. The reaction is strongly inhibited by stirring. Effect of one-electron redox couples (EZ catalysts) on the system is described.
. . - ( EZ) .
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18.
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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19.
Yields of n-C4H10 have been measured from the flow pyrolysis of C2H4 at 897 (±7) K. From 77 to 720 Torr the order of n-C4H10 formation was found to be 2.0±0.3 The rate constant for the reaction, was estimated to be 2.4(±0.6)×10–4l mol–1s–1.
-C4H10 C2H4 897 (±7) . -C4H10 77 720 2.0±0.3. 2C2H4C2H3+C2H5 2,4 (±0,6)×10–4 –1–1.
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20.
Through simulation of TPD model curves for desorption from adsorption sites of different strength could be shown that the use of non-linear temperature programmes influences the complex desorption process in such a manner that the appearing desorption maxima are better visible.Because in case of using non-linear temperature programmes the overlapping of different desorption processes is smaller it is possible to evaluate approximately the activation parameters for the single steps from the complex desorption curve.
Zusammenfassung Durch Simulationsrechnungen für ein einfaches Modell der Desorption von Adsorptionsplätzen verschiedener Stärke kann gezeigt werden, daß bei Verwendung nichtlinearer Temperaturprogramme auftretende Desorptionsmaxima der komplexen Desorptionskurve besser erkennbar sind Da bei nichtlinearer Temperaturführung die Überlagerung mehrerer Prozesse geringer ist, können die Aktivierungsparameter der einzelnen Prozesse näherungsweise aus der komplexen Desorptionskurve ermittelt werden.

, , , . e , , , .
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