Hydrogenation of CO2 on carbon-supported nickel and cobalt

The hydrogenation of CO₂ has been studied at atmospheric pressure on Co/C and Ni/C catalysts and the results are compared with those obtained on unsupported Co and Ni. Specific activites in the form of turnover frequencies for CO₂ hydrogenation decrease with increasing metal dispersity. Carbon supported Co and Ni present a smaller selectivity for methane than bulk metals. Higher specific activities and smaller activation energies are obtained on Co catalysts, compared with those determined for Ni catalysts.

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CO₂ Co/ Ni/ Co Ni . CO₂ . Co Ni , . .

     

Temperature dependence of CO insertion on S-, Ag-, and Cu-promoted Rh/SiO2 catalysts

The addition of sulfur and silver to Rh/SiO₂ inhibits hydrogenation of C₂H₄, but promotes CO insertion and extends the linearity of Arrhenius curves for CO insertion above 543 K.

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Rh/SiO₂ C₂H₄, CO CO 543 .

     

Structure of vanadium phosphate anion in solutions from17O,51V and31P NMR data

¹⁷O,⁵¹V and³¹P NMR studies indicate that the anion structure of sodium vanadophosphate in an aqueous solution is close to that in crystals of the (CN₃H₆)₈HPV₁₄O₄₂ 7H₂O salt.

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¹⁷O,⁵¹V,³¹P , (CN₃H₆)₈HPV₁₄O₄₂ 7H₂O.

     

A novel method for the preparation of extensively dealuminated faujasites

Open structure faujasites may be dealuminated with retention of crystallinity using phosgene (or similar reactants) provided the sample has been made ultrastable in a previous procedure.

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( ) . .

     

Effect of TiO2 crystal modification on catalytic properties of cobalt-titanium dioxide catalysts for Fischer-Tropsch synthesis

CO hydrogenation on cobalt-rutile and cobalt-anatase catalysts with various amounts of cobalt at 480–570 K has been studied. C₁–C₁₅ hydrocarbons are formed on cobalt-rutile catalysts at 478–523 K. During the initial period of catalyst operation a counterclockwise hysteresis is observed. Cobalt-anatase catalysts remain inactive up to 670 K.

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CO - - - 480–570 . - 478–523 C₁–C₁₅. . - 670 .

     

Catalytic activity of the Al2O3?Cr2O3?Fe2O3 system II. Influence of nitrogen bases on hydrocarbon aromatization

The physico-chemical properties of the Al₂O₃–Cr₂O₃–Fe₂O₃ catalyst system have been correlated with n-hexane dehydrocyclization. Using a poisoning technique, the ionic and radical steps of the reaction have been determined.

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- Al₂O₃–Cr₂O₃–Fe₂O₃ -. , .

     

Temperature programmed reduction and oxidation of Ir/Al2O3 catalysts

3 % Ir/Al₂O₃ catalysts have been studied by means of temperature programmed reduction and oxidation. With growing degree of metal oxidation (higher T_ox) reducibility of the catalysts at low temperatures decreases.

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3% Ir/Al₂O₃ . ( ) .

     

Hexadiene formation during decomposition of 2-propanol over Ca?P?O catalysts

Hexadiene formation from 2-propanol was investigated in view of acid-base properties of Ca–P–O catalysts with the Ca/P atomic ratio varying from 1.5 to 5.0. The catalytic activity in hexadiene formation increased up to a maximum at Ca/P=2.0, having almost the same amount of weak acidic sites as weak basic sites, and decreased with futher increase in Ca/P ratio.

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2- - Ca–P–O Ca/P, 1,5 5,0. , Ca/P=2, , Ca/P.

     

Strong H2 chemisorption on Al2O3 or SiO2 supported group VIII metals

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.

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VIII , SiO₂ Al₂O₃. .

     

Infrared spectra of nitric oxide adsorbed on photoreduced V/SiO2 catalyst

Studies of the IR spectra of surface species produced via NO adsorption on selectively photoreduced V/SiO₂ catalysts indicate that at low coverages NO is adsorbed on V³⁺ ions to form strongly bonded mononitrosyl species V³⁺...... NO. With increasing NO coverage, V³⁺ is oxidized to V⁴⁺, which is accompanied by the appearance of gaseous N₂O and weak adsorption of NO on V⁴⁺.

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- , NO V/SiO₂ . , V³⁺ NO V³⁺... NO. V³⁺ V⁴⁺, N₂O NO V⁴⁺.

     

Oxidizing supported reagents, III. Oxidation of alcohols by new supported K2Cr2O7 reagents

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.

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K₂Cr₂O₇ . . .

     

A differential scanning calorimetric study of some phenol derivatives

Differential scanning calorimetry has been applied to derive the fusion enthalpies and entropies of series of mono and dimethylphenols, mono and dichlorophenols, and mono and dinitrophenols.

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Zusammenfassung DSC wurde verwendet zur Ermittlung der Schmelzenthalpie und Entropie der Reihen von Mono- und Dimethylphenolen, Mono- und Dichlorphenolen, Mono- und Dinitrophenolen.

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- , - , - .

     

V2O5/TiO2 oxidation catalysts, III. Oxidation of CO on pure and sodium-doped systems

The activity of vanadia/titania catalysts in CO oxidation has been tested and found to be of the same order as that observed for unsupported vanadia; the simultaneous presence of vanadium-sodium compounds cancels the activity, probably because of the elimination of labile V=0 species at surface defects.

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V₂O₅/TiO₂ CO, V₂O₅; - , , V=0 .

     

Investigation of n-heptane conversion over Pt?Al2O3 catalysts under gradientless reforming conditions

The rates of the total and individual directions of n-heptane conversion in reforming over platinum-on-alumina catalysts were shown to be independent of dilution with hydrogen. They can be described by simple equations following from kinetic concepts in ideal adsorbed layers.

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, - , .

     

Structure, activity and selectivity of V2O5-TiO2 catalysts for o-xylene conversion

The formation of needle shaped crystallites of V₆O₁₃ at low V concentrations on V₂O₅-anatase coated catalysts explains the low selectivity for phthalic anhydride during o-xylene oxidation. The (010) plane of V-oxide, most active for selective oxidation of o-xylene, is not accessible and the contact of this plane with the anatase faces promotes the anatase-rutile transformation and the incorporation and blocking of V⁴⁺ ions.

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V₆O₁₃ V , V₂O₅-, -. (010) , -, , - V⁺⁴.

     

Hydrogen pressure dependence of the reaction of neopentane with hydrogen over Pd/SiO2 and Pt/SiO2 catalysts

H₂ pressure influences in different ways the reaction rates of neopentane conversion over Pd/SiO₂ and Pt/SiO₂ catalysts. It seems that on Pt/SiO₂ both isomerization and hydrogenolysis involve a common surface intermediate (probably an adalkyl), whereas on Pd/SiO₂ the hydrogenolysis goes via more dehydrogenated species than those involved in isomerization.

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H₂ Pt/SiO₂ Pd/SiO₂. , Pt/SiO₂ (, ), Pd/SiO₂ , .

     

Calculation of recombination rate constants in (H2?O2) system

Rate constants of the three-body recombination for the elementary three-molecule stages in hydrogen oxydation have been calculated.

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, .

     

Veränderung des thermischen Verhaltens von Kaolinit durch mechanische Aktivierung

Zusammenfassung Es ist bekannt, daß die Eigenschaften von Kaolinit nicht nur durch eine Kalzinierung oberhalb 600 °C, sondern auch durch intensive mechanische Beanspruchung stark verändert werden können. Die durch eine Intensivmahlung erzeugte Reaktivitätssteigerung kann durch eine Verbesserung der Säurelösbarkeit des Al₂O₃-Anteiles, das veränderte thermische Verhalten und strukturelle Veränderungen gekennzeichnet werden. In der vorliegenden Arbeit geht es um einen Beitrag zur methodischen Aufklärung der strukturellen und thermischen Veränderungen von Kaolinit, insbesondere durch Einsatz thermoanalytischer und IR-spektroskopischer Methoden. Als intensives Zerkleinerungsaggregat wurde eine Scheibenschwingmühle eingesetzt.

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It is already known that the properties of kaolinite can be changed substantially not only by calcination above 600° but also by intensive mechanical stress.A reactivity increase induced by intensive grinding can be characterized by an increase of acid solubility of the Al₂O₃ content, by changed thermal behaviour and by structural changes. The paper presented contributes to the methodic explanation of structural and thermal changes of kaolinite, especially by the use of thermoanalytical and IR spectroscopic methods. The intensive grinding was performed in a vibration-disc mill.

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Résumé Il est déjà connu que les propriétés de la kaolinite peuvent être profondément modifiées non seulement par calcination au-dessus de 600 °C, mais aussi par contrainte mécanique intense.Une augmentation de la réactivité induite par broyage intense peut être caractérisée par une augmentation de la teneur en Al₂O₃ déterminée par solubilité en milieu acide, par le changement du comportement thermique et par des modifications structurales. Le présent article contribue à l'explication méthodique des changements structuraux et thermiques de la kaolinite, spécialement à l'aide des méthodes d'analyse thermique et de spectroscopie infrarouge. Le broyage intense a été effectué dans un broyeur à disques vibrants.

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, 600°, . l₂₃ , . . .

     

IR spectra of oxygen adsorbed on SnO2

IR spectra of oxygen adsorbed on SnO₂ with and without lattice defects have been studied. At low temperatures oxygen is adsorbed on defect SnO₂ in two forms of O ₂ ^– . This supports the earlier results obtained by ESR. The low-temperature forms of adsorbed oxygen (unrevealed in ESR spectra) were detected on defectless SnO₂. High-temperature forms of adsorbed oxygen appear in the IR-spectra as bands due to vibrations of the cation-oxygen bond.

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- SnO₂. , O ₂ ^– , . SnO₂ .

     

Role of tin in a PtSb alloy and a Pt-Sn/Al2O3 reforming catalyst

The conversion of n-hexane was studied on a Pt-Sn/Al₂O₃ catalyst, a PtSn alloy and on the corresponding Pt catalysts. The results indicate the same catalytic effect of tin in supported and unsupported catalysts. It is concluded that the role of tin is connected with alloy formation.

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- Pt-Sn/Al₂O₃, PtSn Pt-. . , .