Comparative kinetic and thermodynamic study on the chlorination of V2O5 with CCl4, COCl2 and Cl2

The chlorination kinetics of pure vanadia was studied via isothermal thermogravimetric measurements, with CCl₄, CoCl₂ and Cl₂ as chlorinating agents. At temperatures where chemical control was predominant, apparent activation energies of 77, 48 and 126 kJ: mol^–1 were obtained for chlorination by CCl₄, COCl₄ and Cl₂, respectively. For interpretation of the conversion vs. time curves in the whole conversion range, a non-uniform particle size distribution was assumed, where the reacting solid phase was considered to be composed of thin plates of different thicknesses. With this model, a fairly good correspondence was obtained between the measured and calculated kinetic curves. Selected thermodynamic calculation data on the V₂O₅ + CCl₄, V₂O₅ + COCl₂ and V₂O₅ + Cl₂ systems are presented.

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Zusammenfassung Mittels isothermen Thermogravimetriemessungen wurde die Kinetik der Chlorierung von reinem Vanadiumoxid mit CCl₄, COCl₂ und Cl₂ als Chlorierungsmittel untersucht. Bei Temperaturen mit vorherrschender chemischer Kontrolle wurde für die Chlorierung mit CCl₄, COCl₂ bzw. Cl₂ Bruttoaktivierungsenergien von 77, 48 bzw. 126 kJ/mol erhalten. Zur Interpretation der Konversion-Zeit-Diagramme im gesamten Conversionsbereich wurde eine nichteinheitliche Teilchengrösseverteilung angenommen, namentlich den Bestand der reagierenden Festphase aus dünnen Plättchen unterschiedlicher Dicke. Mit diesem Modell konnte eine recht gute Übereinstimmung zwischen errechneten und ermittelten kinetischen Kurven erhalten werden. Einige thermodynamische Rechenbeispiele für die Systeme V₂O₅ + CCl₄, V₂O₅ + COCl₂ und V₂O₅+Cl₂ wurden gegeben.

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, l₄, l₂ l₂. , l₄, l₂ l₂, 77, 48 126 ·^–1. — , . , . - . V₂O₅+CCl₄, V₂O₅+COCl₂ V₂O₅+Cl₂.

     

Catalytic properties of cobalt and manganese complexes with macromolecular ligands in the liquid-phase oxidation of ethylbenzene

The selective catalytic effect of transition metal complexes (in particular cobalt and manganese) with polymeric ligands is shown on the example of the liquid-phase oxidation of ethylbenzene. The catalytic activity depends on both the structure of the polymeric matrix and the nature of metal.

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( ) . , , .

     

Calculation of the mass transfer coefficient with a chemical reaction in a gas-liquid system

A solution of the problem of mass transfer in a turbulent boundary layer has been obtained with a first-order chemical reaction occurring in the liquid phase. The dependence of the enhancement factor for absorption and of the mass transfer coefficient on the model parameters can be used for building up a hierarchic model of the gas-liquid reactor.

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. .

     

Combination and disproportionation of methyl and 2-propyl radicals with 1,1,2-trimethylallyl radicals

The combinations and disproportionations of the CH₃ and 2-propyl (iP) radicals with the 1,1,2-trimethylallyl (TMA) radical have been studied in the gas phase in the temperature interval of 389–451 K and 490–540 K, respectively. For the ratios of the terminal (t) and non-terminal (n) combinations of the CH₃ and iP radicals with the TMA radical, values of 1.9±0.1 and 2.84±±0.10 were obtained, respectively. The ratios of the tt and tn and nn to tn combinations of the TMA radical were 1.59 and 0.46, respectively. The disproportionation-combination rations were (CH₃ , TMA)=0.022±±0.012 and (iP, TMA)=0.026±0.011.

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CH ₃ 2- (iP) 1,1,2- (TMA) : 389–451 K 490–540 K. (t) (n) TMA 1,9±0,1 2,84±0,10, . tt tn nn tn TMA 1,59 0,46, . (CH ₃ , TMA)=0,022±0,012 (iP, TMA)=0,026±0,011.

     

Influence of the crystallite size of platinum of the course of hydrogenolysis of ethane and propane over Pt/Al2O3 catalysts

The effect of the degree of platinum crystallite size on the reaction rate, selectivity and activation energy of ethane and propane hydrogenolysis has been studied in the range of platinum crystallite size of 1.7–4.0 nm. In the same range of Pt crystallite size, the activation energy of both processes shows a clear minimum. The decrease in Pt crystallite size bellow 3.0 nm brings about rapid changes in the selectivity of propane hydrogenolysis.

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( ) , -. 1,7–4,0 , .

     

Study of hydroisomerization of n-hexane on natural mordenite catalyst

A mordenite-containing rock sample from the Tokaj Mountains (Hungary) and its various forms modified by chemical treatment have been tested for catalytic properties during isomerization of n-hexane. Addition of Pt to the catalyst leads to a sharp decrease in the rate of cracking and in the rate of deactivation and this results in a catalyst of high selectivity for hexane isomers.

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(), , , , -. Pt , .

     

Reduction of benzylideneaniline over supported Pd catalysts

In this work we have carried out a study on the liquid phase hydrogenation of benzylideneaniline, using dihydrogen over various supported Pd catalysts. Benzyl-ideneaniline reduction can be classified as insensitive to the catalyst structure. On the other hand, no compensating effect has been observed in performing the reaction over different supported Pd catalysts.

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Pd , . . Pd , .

     

An approximation to the dependence of activation energies of simple catalytic reactions and the initial heats of adsorption of gases on metals on the nature of adsorbent and adsorbate

The activation energy, E, of simple catalytic reactions over 3d-oxides and the initial heats of adsorption, Q_ads, of gases on metals are related in a complex way to the enthalpy of formation of oxides and to the electronegativity of the gases involved in the processes.

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, , 3d- , Q_ads, , .

     

Reactivity and stability of monomeric forms of iron phthalocyanines

The effect of preparation methods of monomeric iron phthalocyanine on Mössbauer perameters and transformations was investigated. The form of iron phthalocyanine influences the reactivity and stability against oxidative destruction to iron oxides.

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. .

     

Kinetic isotope effect in trans-alkylation with ethylbenezene

Kinetic isotope effect (KIE) measurements in the trans-alkylation of toluene and benzene with ethylbenzene in hexane in the presence of AlBr₃ at 313 K indicate that deuterium in the toluene methyl group causes a small inverse KIE characteristic for a -complex transiton state. The small direct KIE found for the reaction with C₂D₅C₆H₅ does not agree with a mechanism involving alkyl-and -phenylalkyl cations.

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() - AlBr₃ 313 . , , - C₂D₅C₆H₅ , - -.

     

Formation of aromatic carbonium ions on V2O5/Al2O3

A comparison of IR spectra of individual toluene, mesitylene, hexamethylbenzene, triene and their carbonium ions with IR spectra of the same molecules adsorbed on V₂O₅/Al₂O₃ has indicated the formation of carbonium ions on catalyst surface.

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- , , , , - , V₂O₅/Al₂O₃ Al₂O₃, t, V₂O₅/Al₂O₃ .

     

Kinetics and mechanism of the permanganate oxidation of trans-crotonic acid

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.

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pH=0,5–5,0, . (III) . MnO ₄ ^– , (). 25°C 730 410 M^{–1 –1} , . .

     

Synthesis and thermostability of the binary condensed phosphates

Some condensed phosphates, especially cyclo-tetraphosphates have been synthetized as new binary compounds and their existence has been proved. The synthesis of cyclo-CdMgP₄O₁₂ is shown as an example. The products crystallize in the monoclinic system (C2c group) and are stable to 900°C. The synthesis is based on a thermal procedure making use of the reversible transformation of cyclo-tetraphosphates to higher linear phosphates (the 1.method) and on a calcination of the starting binary dihydrogenphosphate at quasi-isothermal-isobaric conditions (the 2.method).

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Zusammenfassung Einige kondensierte Phosphate, im besonderen Zyklotetraphosphate wurden als neue binäre Verbindungen hergestellt. Als Beispiel wird Zyklo-Cd MgP₄ O₁₂ angeführt. Das Produkt kristallisiert monoklin /Gruppe C2/c/ und ist bis 900°C stabil. Die Synthese basiert auf einem thermischen Verfahren unter Anwendung des reversiblen Überganges von Zyklotetraphosphaten zu höhereren linearen Phosphaten /Verfahren 1/ und auf dem Kalzinieren der binären Ausgangsverbindung Dihydrogenphos phat bei quasi-isothermen-isobaren Bedingungen /Verfahren 2/.

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$ , . - dMgP₄O_I2. $ / 2/ $ 900°. $ $ , — $ - .

     

Displacement of hydrogen from rhodium surface by carbon monoxide under conditions of pulsed-gas chromatography

Interaction of carbon monoxide with hydrogen on the surface of rhodium catalysts has been investigated under conditions of pulsed-gas chromatography within the temperature range of –80 to 500 °C. At temperatures up to about 180 °C adsorbed hydrogen was found to be displaced to the gaseous phase as a result of carbon oxide adsorption. At higher temperatures conversion of carbon monoxide and hydrogen to methane takes place.

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–80 500 °C. 180 °C . .

     

Beckmann rearrangement of cyclohexanone oxime p-toluenesulfonate on acidic catalysts

The Beckmann rearrangement of cyclohexanone oxime p-toluenesulfonate has been studied using several catalysts. The reaction is catalyzed by weakly acidic sites and seems to occur by way of O-(p-toluenesulfonyl)--caprolactim.

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- -, . - -(-)--.

     

On some peculiarities of phthalimide formation in the oxidative ammonolysis of o-xylene

In the oxidative ammonolysis of o-xylene on oxide catalysts, phthalimide can be obtained from phthalodinitrile through an intermediate phthalocyanine step. The catalyst ability to form phthalocyanine can be used to estimate its selectivity to phthalimide.

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- . .

     

Thermal investigation of active carbons in presence of air

Thermal analysis data on the oxidation reaction between air and active carbons obtained during activation by carbon dioxide are presented. The correlation between the modified DTA curves and the TG curves leads to the conclusion that the oxidation of active carbons in the temperature range from 20 to 1000° is a two-step process. It is pointed out that the oxidation reactions in the low-temperature region (450–550°) are governed by the oxygen content of the samples, whereas the reactions in the higher temperature region (550–850°) are controlled by the diffusion process.

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Zusammenfassung Die thermoanalytischen Ergebnisse über die während der Aktivierung durch Kohlendioxid stattfindende Oxidationsreaktion zwischen Luft und Aktivkohlen werden vorgestellt. Die Korrelation zwischen den modifizierten DTA-Kurven und den TG-Kurven führte zur Schlußfolgerung, daß die Oxidation der Aktivkohlen im Temperaturbereich von 20 bis 1000° ein Zweistufen-Vorgang ist. Es wird betont, daß die Oxidationsreaktion im niedrigen Temperaturbereich (450 bis 550°) durch den Sauerstoffgehalt der Proben gesteuert wird, während er im Bereich der höheren Temperaturen (550 bis 850°) durch Diffusionsvorgänge geregelt wird.

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Résumé On présente les résultats de l'étude par analyse thermique de la réaction d'oxydation des charbons actifs par l'air qui a lieu lors de l'activation par l'anhydride carbonique. La corrélation entre les courbes ATD modifiées et les courbes TG conduit à la conclusion que l'oxydation des charbons actifs s'effectue entre 20 et 1000°, suivant un processus en deux étapes. Dans l'intervalle des températures faibles (450 à 550°) les réactions d'oxydation sont gouvernées par la teneur en oxygène des échantillons tandis qu aux températures plus élevées (550 à 850°) elles le sont par le processus de diffusion.

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, . , 20 1000° . , (450–550°) , (550–850°) .

     

DSC characterization of ZSM-5/MgO/Al2O3 catalysts

The physico-chemical characterization of magnesium-modified ZSM-5 zeolite catalysts has been performed by differential scanning calorimetry. Evidence has been found of the formation of magnesium oxide and the magnesium spinel phase in alumina-bonded ZSM-5 catalysts. DSC proved a suitable technique for characterization of these systems.

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Zusammenfassung Mg-modifizierte ZSM-5-Zeolithkatalysatoren wurden durch DSC charakterisiert. Es wurden Beweise für die Bildung von Magnesiumoxid und Magnesiumspinell in ZSM-5/Aluminiumoxid-Katalysatoren gefunden. DSC hat sich zur Characterisierung dieser Systeme als geeignet erwiesen.

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- 3CM-5, . - - . .

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This work was carried out within the Progetto finalizzato Energetica 2 of the National Research Council of Italy.     

Tracer study of complete oxidation complexes in the oxidative dehydrogenation of butylene

A tracer technique using divinyl-¹⁴C was used to determine the butylene and divinyl contents in the surface complexes of complete oxidation during the oxidative dehydrogenation of butylenes over Bi–Mo, Fe–Sb and Fe₂O₃ catalysts. The rate of decomposition of the surface complexes was found to be independent of their relative butylene and divinyl content.

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–C¹⁴ Bi–Mo, Fe–Sb Fe₂O₃ ., .

     

Transient phenomena in o-xylene oxidation in a fluidized bed reactor

The effect of stirring a vanadium-titanium-tellurium catalyst on the yield of the selective oxidation products for oxidation of o-xylene in fluidized bed reactors has been studied. It is shown that the stirring of catalyst pellets increases the yield of phthalic anhydride.

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-- - . , .