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1.
The thermal (under high vacuum, 10–5 mm Hg) and thermoxidative decompositions of ternary grafted copolymers of ABS type were studied, the dependence of the characteristic thermal data on the overall composition being followed over narrow ranges of variation of comonomer content.It was found that the nature of the solid products obtained on thermal decomposition is dependent on the copolymer structure.
Zusammenfassung Die thermischen (unter Hochvakuum, 10–5 mm Hg) und thermooxidativen Zersetzungen ternärer Kopolymere der Typen ABS wurden untersucht, wobei die Abhängigkeit der charakteristischen thermischen Daten von der allgemeinen Zusammensetzung über enge Bereiche der Änderung des Komonomergehaltes verfolgt wurde. Es zeigte sich, daß die Beschaffenheit der bei der thermischen Zersetzung erhaltenen festen Produkte von der Kopolymerstruktur abhängig ist.

( 10–5 Hg) ABC. , . , , , .
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2.
Singlet triplet intersystem crossing quantum yields were determined for n-butyraldehyde, using the photosensitized cis-trans isomerization of piperylene to monitor the process. At room temperature and 313 nm, 0.58±0.05 and 0.72±0.05 were obtained for the triplet yield in the vapor phase and in isooctane, respectively.
- - - . 0,58±0,05 0,72±0,05 313 .


For Part I, see Ref. /1/  相似文献   

3.
Electron microscopy and Mössbauer spectroscopy studies of nickel-based Raney catalysts have revealed that the catalysts are formed through the successive aggregation of their structural elements. Catalyst particles are covered by a thin layer of nickel oxide.
. , . .
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4.
    
- 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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5.
m-Xylene conversion was studied over dealuminated Y type zeolites in hydrogen forms, SiO2 to Al2O3 ratios were varied from 4.86 to 12.95.
- . SiO2/Al2O3 4,86 12,95.
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6.
Studies of water vapor adsorption on polycrystalline Rh at T>315 K and P=(2–4)×10–2 Pa indicate that water is adsorbed dissociatively to Oads and Oads through a molecularly adsorbed species. Desorption activation energy is 46 and 69 kJ/mol for molecular and dissociative species, respectively.
Rh (2–4)·10–2 . , O OH - . 46 /, -69 /.
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7.
ESR studies of O2 adsorption on reduced anatase have been performed. The amount of O 2 species is determined by adsorbed surface oxygen and their parameters are changed by CO adsorption.
O2 . , O 2 , CO.
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8.
The kinetics and intermediates of the permanganate oxidation of trans-crotonic acid have been investigated in the pH range of 0.5–5.0 using the stoppedflow technique. The formation of manganese(III) as a short-lived intermediate has been established. The reaction is first order with respect to both MnO 4 and crotonic acid (crotonate). The resolved rate constants at 25°C are 730 and 410 M–1 sec–1 for the acid and the anion, respectively. The reaction mechanism is discussed.
pH=0,5–5,0, . (III) . MnO 4 , (). 25°C 730 410 M–1 –1 , . .
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9.
    
Abnormal fluctuations of chemiluminescence intensities have been observed in the CH2(COOH)2–BrO3–Ru(bipy) 3 2+,3+ system, when catalyst concentrations are insufficient for stable self-oscillations to be generated. Amplitude distribution of these fluctuations (reaction noise) are of the bell shape, which is typical for the normal Gaussian distribution. Their nature is similar to the large-scale fluctuations that are the nuclei for dissipative structures.
CH2(COOH)2–BrO 3 –Ru(bipy) 3 2+,3+ , . ( ) , . , , .
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10.
Kinetic equations of the isotopic exchange in a system with one elementary reaction have been derived. A principle of quasistationarity in the isotopic kinetics has been formulated.
. .
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11.
The effect of Fe2O3 additives on crotonaldehyde hydrogenation over group VIII metals has been studied. Iron oxide added to platinum black exerts a modifying effect on the reduction of the carbonyl group of croton-aldehyde inhibiting hydrogenation of the C=C bond conjugated with a C=O group.
Fe2O3 VIII -. , , - , C=C , C=O-.
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12.
The cubic spinel Fe2MoO4 was studied in air by DTA, DTG, TG and X-ray in the temperature interval 298–1173 K. From these studies, it was concluded that above the Néel temperature Fe2MoO4 undergoes an irreversible crystalline phase transition from cubic to tetragonal at 623 K, wherec/a is 1.022. Above 723 K, surface oxidation followed by bulk oxidation of the spinel occurs. At 948 K, after about half the total weight gain due to oxidation, a compound is formed which was confirmed by X-ray as ferrimolybdite, Fe2O3·3–4 MoO3, indicating that in Fe2MoO4 the Mo4+ is more readily oxidized than the Fe2+. Above 940 K, further oxidation of Fe2+ and Mo4+ into their respective oxide occurs. About 13 % of the MoO3 vaporizes, and the rest melts at 1028 K.
Zusammenfassung Das kubische Spinell Fe2MoO4 wurde in Luft im Temperaturbereich von 298 bis 1173 K durch DTA, DTG, TG und Röntgen untersucht. Aus diesen Studien wurde gefolgert, daß oberhalb der Neel Temperature ein irreversibler kristalliner Phasenübergang des Fe2MoO4 aus der kubischen in die tetragonale Form bei 623 K stattfindet, wobeic/a=1.022 beträgt. Oberhalb von 725 K findet eine Oberflächenoxidierung des Spinels statt, der eine allgemeine Oxidation folgt. Bei 948 K, nachdem etwa die Hälfte der infolge der Oxidation auftretenden Gewichtszunahme erfolgte, wird eine durch Röntgen als Ferrimolybdit bestätigte Verbindung gebildet (Fe2O3·3–4 MoO3), welche zeigt, daß in Fe2MoO4 das Mo4+ leichter oxidiert wird als das Fe2+. Oberhalb von 940 K erfolgt eine weitere Oxidation von Fe2+ und Mo4+ zu ihren entsprechenden Oxiden. Etwa 13% des MoO3 verdampft und das übrige schmilzt bei 1028 K.

, , Fe2MoO4 298–1173 . , Fe2MoO4 623 , / 1.022. 723 , , . 948 Fe2O3. 3–43, . , Fe2MoO4 Mo4+ , Fe2+. 940 Fe2+ Mo4+ . 13% MoO3 , 1028 .


The author wishes to thank the Chemistry Division of BARC for helping with the high-temperature X-ray pattern.  相似文献   

13.
Steady-state kinetics of combined heterogeneous catalytic hydrogenation and hydroformylation of propylene on Rh–Co-containing catalysts has been studied at atmospheric pressure and T=140–170 °C. A reaction mechanism is suggested. The kinetic model adequately describes all observations.
- Rh–Co- 140–170 °C. . , .
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14.
Pt/sol and Pt/support catalysts with 6–15 Å Pt particles have been established to be low active in the hydrogenation of propargyl alcohol, butyn-l-ol-3 and dimethylethynylcarbinol. The specific catalytic activity significantly rises with increasing dPt above 15 Å and after the thermal treatment of highly dispersed catalysts in a hydrogen flow.
, -30 -- 6–15 Å , -1, -3 . dPt>15 Å .
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15.
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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16.
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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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.
The conditions and premises of the kinetic evaluation of thermoanalytical curves on the basis of chemical kinetics are demonstrated, and the limits of their availability are pointed out. For reactions with an unclear structural and chemical course, some appropriate definitions of terms are proposed.The possibilities of the use of the inflection points of the reaction rate versus time curve are presented. New methods of determination of kinetic parameters are described, including the ratio of the degrees of reactionx, the ratio of the reaction ratesx and the ratio of the tangent slopesx at these points.
Zusammenfassung Bedingungen und Voraussetzungen der kinetischen Auswertung thermoanalytischer Meßkurven auf der Basis der chemischen Kinetik werden dargestellt, gleichzeitig wird auf die Grenzen ihrer Gültigkeit hingewiesen. Für Reaktionen mit unklarem chemischem oder strukturellem Ablauf werden geeignete neue Bezeichnungen definiert.Die Möglichkeit zur Verwendung der Wendepunkte der Kurve Reaktionsgeschwindigkeit gegen Zeit vorgestellt. Neue Methoden werden beschrieben, die zur Bestimmung kinetischer Parameter das Verhältnis der Umsätzex 1 x 2, das Verhältnis der Reaktionsgeschwindigkeitenx 1/x 2, und das Verhältnis der Tangentensteigungenx 1/x 2 an den Wendepunkten verwenden.

. . . — . , (x), () () .
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19.
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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20.
Thermal desorption spectra of oxygen desorbed from rhodium have been analyzed in terms of models accounting for the effect of lateral interactions between adsorbed particles and of their diffusion into the bulk of metal on the desorption kinetics of O2. Complex configuration of these spectra is ascribed to the processes of formation/decomposition of surface Rh oxides and the diffusion of particles into the near-surface layers of metal and back to the surface.
- , O2 . - O2 Rh - .
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