Influence of carbonate upon adsorption and isomerization of n-butenes on zeolite ZnA. Some conclusions from an infrared study

Upon the formation of carbonates inside zeolite ZnA, weakly bound species of adsorbed n-butenes are observed together with a significant change in the catalytic behavior.

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. ZnA - .

     

Determination of organic- and carbonate-carbon in freshwater lake sediments by a microcombustion procedure

A microcombustion procedure specific for the determination of total-, organic- and carbonate-C in freshwater lake sediments is described. The procedure involves combustion of the sample at 650° to obtain organic-C. Total-C is obtained by combustion at 950° and carbonate-C calculated by difference. The procedure was evaluated by differential thermal analyses of representative sediments and known carbonate minerals. A procedure for the identification of dolomite in lake sediments by differential thermal analysis under CO₂ is also described.

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Zusammenfassung Es wurde über ein zur Bestimmung des Gesamt-, Karbonat- und organischen Kohlenstoffgehaltes von Süßwasserrückständen geeigneten Mikroverbrennungsverfahren berichtet. Durch Verbrennen bei 650° erhält man den organischen Kohlenstoff, durch Verbrennen bei 950° den Gesamtkohlenstoff. Der Karbonatkohlenstoff ergibt sich aus der Differenz. Die Methode wurde durch differentialthermoanalytische Prüfung von charakteristischen Sedimenten und bekannten Karbonatmineralien getestet. Ein Verfahren zur Identifizierung von Dolomit in Seesedimenten durch Differentialthermoanalyse unter CO₂ wurde ebenfalls beschrieben.

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Résumé On décrit une méthode spécifique de microcombustion pour déterminer la teneur en carbone total, organique et carbonate dans des sédiments des lacs à eau froide. On reçoit le C organique par combustion à 650°, le C total par combustion à 950° et le carbone à l'état de carbonate, par la différence. On a évalué le procédé par ATD des sédiments représentatifs et de minérais de carbonate connus. On a décrit une méthode pour identifier le dolomite dans les sédiments des lacs, par ATD sous CO₂.

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, , C . C 650° 950°C, , C . . , , CO₂.

     

Influence of neodymium content on the catalytic properties of zeolite NDHNaY

The influence of neodymium content on the catalytic properties of a HNaY zeolite was investigated using the cracking of n-heptane as model reaction. Neodymium zeolites were found to be more active for cracking and hydrogen transfer reactions than zeolites containing lanthanum, cerium or praseodymium.

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HnaY . , , , .

     

Gas phase thermolysis of cyclohexyl thiol

The pyrolysis of cyclohexyl thiol has been studied in a static system at subambient pressures in the temperature range 420–497°C. It is proposed that in the presence of a large excess of cyclohexene the mechanism is a radical non-chain process.

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, , 420–497°C. , .

     

Selective hydrogenation of carbon monoxide to light olefins catalyzed by supported potassium tetracarbonylhydridoferrate

In the Fischer-Tropsch synthesis, potassium tetracarbonylhydridoferrate, KHFe (CO)₄, supported on HY-zeolite or silica gel exhibited high selectivity to light olefins without following the Schulz-Flory distribution.

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, KHFe(CO)₄, HY —, — .

     

Effect of radial distribution functions and poisson reparatition of reactants on the analysis of reactions involving long distance energy transfer

Starting from a uniform distribution and knowing the space dependent rate constant, it is possible to express the fluorescence quenching effect. In the case of long distance energy transfer (Forster), we show that the introduction of radial distribution functions and of non-uniform repartition of quenchers has only small effects on the kinetics of such reactions.

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. (Forster) , .

     

Pressure-jump method in the dehydrogenation of propane over chromia-alumina-potassium oxide

The pressure-jump method was applied to the dehydrogenation of C₃H₈ over a Cr₂O₃–Al₂O₃–K₂O catalyst in a closed static reactor at 443°C. The rate equation proposed for initial kinetics was shown to apply to the dehydrogenation of C₃H₈.

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C₃H₈ Cr₂O₃–Al₂O₃–K₂O 443°C. , , , C₃H₈.

     

Effect of the activation conditions on the catalytic properties of Pt/Al2O3 catalysts

The effect of the activation conditions of Pt/Al₂O₃ catalysts has been investigated in the hydrogenation of benzene and in the hydrogenolysis of ethane. Whatever the conditions of calcination or reduction, specific activities of all catalysts for benzene hydrogenation remain constant. On the other hand, for identical dispersities, the cacination in a wet argon flow increases the specific activity of platinum for hydrogenolysis of ethane, pointing out the role of wet pretreatment on defect building or on the faceting of supported metallic catalysts.

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Pt/Al₂O₃ . , . , , . .

     

Various dynamic behavior of Ag+-induced oscillations in uncatalyzed bromate oscillators

Silver ion induces the uncatalyzed bromate oscillators /aromatics-bromate-acid/on a variety of dynamic behavior, including high frequency and complex oscillations. The behavior of a reacting system depends on the chemical composition of the armatics, the time of addition of Ag⁺, and the concentration of Ag⁺. The chemistry underlying the phenomena is discussed.

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(--) , . , Ag⁺ Ag⁺. .

     

Thermal behaviour of some new hydrazinium fluorometallates

Three new hydrazinium(1+) fluoro complexes, N₂H₅AsF₆, (N₂H₅)₂ZrF₆ and (N₂H₅)₂HfF₆, were prepared and characterized by means of chemical analysis, IR and Raman spectroscopy and X-ray powder diffraction. Study of their thermal behaviour via TG, DTG and DTA measurements showed that they decompose in stages; the decomposition of N₂H₅AsF₆ proceeded in two steps, through the intermediate NH₄AsF₆; (N₂H₅)₂ZrF₆. Decomposed in three steps, through (NH₄)₂ZrF₆ and NH₄ZrF₅. The thermal decomposition of (N₂H₅)₂HfF₆ is more complex; in the first step (NH₄)₂HfF₆ with some N₂H₅HfF₅ was obtained, and in the second NH₄HfF₅. The intermediates were identified by means of chemical analysis and vibrational spectroscopy.

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Zusammenfassung Die Hydrazinium(1+)-fluorokomplexe N₂H₅AsF₆, (N₂H₅)₂ZrF₆ und (N₂H₅)₂HfF₆ wurden dargestellt und durch chemische Analyse, IR- und Ramanspektren sowie Röntgenbeugungsdiagramme charakterisiert. Die Untersuchung ihres thermischen Verhaltens durch simultane TG-DTG-DTA-Messungen zeigte, dass sie sich schrittweise zersetzen: N₂H₅AsF₆ zersetzt sich in 2 Stufen mit NH₄AsF₆ als Zwischenprodukt; (N₂H₅)₂ZrF₆ zersetzt sich in 3 Stufen über (NH₄)₂ZrF₆ und NH₄ZrF₅. Die thermische Zersetzung von (N₂H₅)₂HfF₆ ist komplizierter, der erste Schritt liefert (NH₄)₂HfF₆ mit wenig N₂H₅HfF₅, der zweite NH₄HfF₅. Die Zwischenprodukte wurden durch chemische Analyse und Schwingungsspektroskopie identifiziert.

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N₂H₅AsF₆, (N₂H₅)₂ZrF₆ (N₂H₅)₂HfF₆, - , ., , . , N₂H₅AsF₆ NH₄AsF₆, (N₂H₅)₂ZrF₆ — (NH₄)₂ZrF₆ NH₄ZrF₅. (N₂H₅)₂HfF₆ : (NH₄)₂HfF₆ N₂H₅HfF₅, NH₄HfF₅. .

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We thank Miss B. Sedej for chemical analysis. The work was financed through the Research Community of Slovenia.     

Thermolysis of complex cyanides,XX. thermal decomposition of Zn[Fe (CN)5NO] · 3H2O and identification of the products of decomposition

The thermal decomposition of Zn[Fe (CN)₅NO] was studied by thermal analysis, IR and Mössbauer spectroscopy. The experimental results showed that the decomposition starts with cyanogen formation, giving a tetracoordinated cyano-nitrosyl intermediate. The NO ligand elimination is followed by a structural rearrangement to Fe[Zn (CN)₄].

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Zusammenfassung Die thermische Zersetzung von Zn[Fe (CN)₅NO] wurde derivatographisch und mittels IR- und Mössbauer-Spektroskopie untersucht. Die Zersetzung beginnt mit Dizyanentwicklung unter Bildung eines tetrakoordinierten Cyano-nitrosyl-Intermediärs. Der Eliminierung des NO-Liganden folgt eine zu Fe[Zn (CN)₄] führende strukturelle Umordnung.

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Zn[Fe(CN)₅NO] , ë . , , - . NO , Fe[Zn(CN)₄].

     

Propylene oxidation over tin-molybdenum oxide catalysts

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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. , .

     

Differential thermoanalyse in der Strukturuntersuchung der als Formmassenbindestoffe in der Giessereitechnik angewandten montmorillonitischen Formlehme

Zusammenfassung Die Differentialthermoanalyse eignet sich zur Bestimmung der thermischen Stabilität der in Formmassen angewandten montmorillonitischen Bindestoffe. Mit der DTA-Methode können die bei hohen Temperaturen in diesen Bindestoffen auftretenden strukturellen Änderungen bestimmt werden. Waschöl erhöht die Dehydratisierungs- und Dehydroxylierungstemperatur des montmorillonitischen Bindestoffes. In der Folge steigert also die Suszeptibilität des Obigen zur Hydratation und auch die thermische Stabilität.

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The hitherto presented results of researches of DTA of montmorillonite binding agent, applied in the moulding sand for foundry practice. With the aid of this method the temperature of dehydratation and dehydroxylation of binding agent with the addition and without of wash oil have been defined.As a result of our investigations it has been found that the same oil rises the appearance of these effects.With the aid of DTA these has also been defined structural changes occurring in montmorillonite binding agent, subjected to the activity of high temperature.

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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.

     

Kinetics of product formation in the initial phase of oxidative degradation of pentaerythritol tetraacetate

The kinetics of formation of acetic acid, methanol, methyl acetate and hydroperoxide in the autoxidation (463–503 K) and initiated oxidation (413 K) of pentaerythritol tetraacetate has been studied. A scheme for product formation is proposed.

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, , (463–503 ) (413 ) . .

     

On the alcohol inhibition of the reacting BZ system

The effect of aliphatic alcohols on the reacting BZ system has been studied and the mechanism of alcohol inhibition interpreted.

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.

     

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 ., .

     

Dispersity and reducibility of the molybdenum oxide phase in SiO2, SiO2?Al2O3 and γ-Al2O3 supported molybdena catalysts

XRD, isothermal and temperature-programmed reduction (TPR) experiments were carried out with SiO₂, SiO₂–Al₂O₃ and -Al₂O₃ supported catalysts. Molybdena is in a more disperse state on supports containing more alumina and it is more reducible on SiO₂–Al₂O₃ than on SiO₂ or -Al₂O₃. TPR curves were shown to reflect connections between reduction kinetics and dispersity.

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-, , SiO₂, SiO₂–Al₂O₃ -Al₂O₃. , , SiO₂–Al₂O₃ SiO₂ -Al₂O₃. .

     

Low-temperature ortho-para conversion of hydrogen on films of rare-earth metals and their copper alloys

Kinetic data for the ortho-para conversion of H₂ at 77 k rear earth metals (REM) and their Cu alloy films are given. Conversion on the surface of Sc, Y, La, Yb and Lu has been shown previously to follow a chemical mechanism, for the others it is magnetic. When alloyed with Cu, the specific catalytic activity (K_sp) of Sc, Y, La, Yb and Lu sharply increases. A sharp increase of K_sp is also observed on Cu alloys of Ce, Sm, Nd, Pr, Eu and Gd and the chemical conversion mechanism becomes predominant. On Tb, Dy, Er, Ho and Tm, K_sp rises only slightly and the magnetic mechanism preserves.

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- H₂ 77 P3M . , Sc, Y, La, Yb Lu , . Cu () Sc, Y, La, Yb, Lu, Ce, Sm, Nd, Pr, Eu Gd, . Ha Tb, Dy, Er, Ho Tm .

     

Studies on the thermal decompositions of As-triazine derivatives and their compounds with metal ions

The thermal decompositions of the new complex salts of Mn(II), Co(II), Ni(II), Cu(II) and Zn(II) with 5,6-diethoxyearbonylmethyl-3-seleno-1,2,4-triazine (HSeTEK) and 5,6-diethoxycarbonylmethyl-3-thio-1,2,4-triazine (HTTEK) were investigated on the basis of the respective thermal curves. The thermoanalytical investigations indicate that HSeTEK, HTTEK, and their complexes with metal ions all undergo three-stage changes as the temperature is raised. The stages of pyrolysis established from the thermal data were compared, and the rates and stages of pyrolysis were related to the structures of the compounds.

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Zusammenfassung Die thermische Zersetzung der neuen Komplexsalze von Mn(II), Co(II), Ni(II) und Cu(II) mit 5,6-Diäthoxycarbonylmethyl-3-seleno-1,2,4-triazin (HSeTEK) und 5,6-Diäthoxycarbonylmethyl-3-thio-1,2,4-triazin (HTTEK) wurden auf der Grundlage der entsprechenden thermischen Kurven untersucht. Die thermoanalytischen Untersuchungen zeigen, daß HSeTEK, HTTEK und deren mit Metallionen gebildeten Komplexe bei Temperaturerhöhung einer jeweils dreistufigen Umwandlung unterliegen. Die auf der Basis der thermischen Daten festgestellten Pyrolysestufen wurden verglichen und Geschwindigkeit und Abschnitte der Pyrolyse mittels der Struktur der Verbindungen erläutert.

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, , 5,6- -3--1,2,4- 5,6 5,6 -3--1,2,4-. , . . - .