Thermometrische und Enthalpimetrische Titrationsmethoden

Zusammenfassung Ausgehend von der allgemeinsten Form der Wärmeleistungsbilanzgleichung für thermometrische und enthalpiemetrische Titrationsmethoden werden die Möglichkeiten dieser Methoden in der analytischen Chemie und im Bereich der Stoffdatenbestimmung aufgezeigt und kritisch gewürdigt. Der Bedarf an zuverlässigen Stoffdaten erschließt den thermometrischen und enthalpiemetrischen Titrationsmethoden im Bereich der Thermo chemie der Lösungen neue Anwendungsgebiete.

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Starting from the most general form of the balance equation of thermal performance for thermometric and enthalpimetric methods of titration, the possibilities of these methods in analytical chemistry and in the field of determining data on materials are demonstrated and critically appreciated. The demand for reliable data on materials opens new fields of application of thermometric and enthalpimetric titration methods in the sphere of the thermal chemistry of solutions.

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Résumé A partir de la forme la plus générale de l'équation du bilan de puissance calorifique pour les méthodes de titrages thermométriques et enthalpimétriques, on montre les possibilités de ces méthodes en chimie analytique et dans le domaine de la détermination des données des substances et on en donne une appréciation critique. Les exigences sur les données sûres relatives aux constituants ouvrent aux méthodes de titrations thermpmétriques et enthalpimétriques de nouveaux domaines d'application dans le domaine de la thermochimie en solution.

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Vorgetragen anläßlich des II. Seminars Thermometrische Analyse (II. Thermometriás Szeminárium) Budapest, 2–7 September 1980.

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Teile dieser Arbeit sind Ergebnisse, die im Rahmen eines vom Bundesministerium für Forschung und Technologie gef6rderten Forschungsprogramms der DECHEMA (F91-J) am Lehrstuhl für Chemie VI der Universität Regensburg erhalten wurden. Herrn Prof. Dr. R. Wachter, Universität Regensburg, danke ich für Diskussionen und Hinweise.     

Effect of iron on the properties of supported Rh?Fe catalysts. Rh?Fe/Al2O3 catalysts

The chemical state of metals in Rh–Fe/Al₂O₃ catalysts has been examined. Iron forms clusters with rhodium, whose size and composition depend on the metal ratio in the catalyst. The structure of active sites affects the amount and adsorption heat of hydrogen and carbon monoxide and the mechanism of their interaction.

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Rh–Fe/Al₂O₃ , , . , .

     

State of copper ions, bond energy of oxygen and catalytic properties in hydrogen oxidation for a copper-magnesium system

The bond energy of surface oxygen in a copper-magnesium catalyst and its reactivity are shown to be greatly dependent on the structure of the nearer environment of copper ions. For catalysts prepared at low temperatures (773 K) this structure changes from a symmetrical square planar in CuO to an octahedral with various degrees of axial distortion depending on the copper content.

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, . , (773 ), CuO .

     

Mechanism of oxidation of molybdovanadophosphoric heteropoly blues by molecular oxygen. Trivanadium heteropoly blue

The oxidation of a heteropoly blue (HPB) of the composition Na_xH_9-xPMo₉V₃O₄₀ with molecular oxygen has been studied by the method of catalytic vanadyl oxidation. It is shown that the reduction of an oxygen molecule requires the addition of a fourth atom of V(IV) in the form of a vanadyl ion to the heteropoly anion.

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: Na_xH_9-xPMo₉V₃O₄₀. , V(IV), .

     

Исследование роли фосфиновых комплексов никеля различных степеней окисления в каталитической димеризации олефинов

Ni(II), Ni(I) Ni(O) . , , , Ni(O) Ni(I) - Ni(I) Ni(II) Ni(O).

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The interaction of organoaluminium compounds with phosphine complexes of Ni(II), Ni(I) and Ni(0) has been studied under the conditions of catalytic propylene dimerization. The active complexes are formed from Ni(II) compounds, the regeneration of the latter is ensured by repeated reduction, oxidation of Ni(0) to Ni(I), and by disproportionation of Ni(I) into Ni(II) and Ni(0).

     

Novel evidence for the selective behaviour of tungsten carbide in liquid phase heterogeneous catalytic hydrogenation

Liquid (aqueous) phase catalytic hydrogenation of compounds containing two oxo-groups in -position (biacetyl, glyoxal, alloxan) was studied in the presence of tungsten carbide catalyst. It has been shown that only one of the oxo-groups is affected in the course of the process and is transformed into a >CH–OH group. Comparative studies carried out in the presence of platinum catalyst attest the selective behaviour of tungsten carbide.

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- - (, , ). , >C=O >CH–OH, . .

     

Studies of copper-modified V?Mo oxide catalyst for acrolein oxidation to acrylic acid

Modification of a V–Mo oxide catalyst by copper improves its catalytic properties due to the formation of a variable composition V–Cu–Mo–O phase with varying the ratio Mo/Me (Me=V+Cu).

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T–Cu–Mo–O, Mo/Me, Me=V+Cu.

     

Hydrocarbon hydrogenolysis on nickel-tin catalysts

Hydrogenolysis of ethane, n-hexane and cyclohexane has been studied on nickel-kieselguhr catalysts modified by organic and inorganic compounds of tin. Tin additives decrease nickel reactivity with respect to C–C dissociation, which is ascribed to the formation of surface intermetallides on the catalyst.

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, - - , . . C–C .

     

Location of chromium and nickel cations in stabilized Y zeolites

The influence of the hydrothermal treatment of stabilized and nonstabilized Y zeolites on the location of Cr and Ni cations was tested. A significant influence of the above treatment was found.

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Cr Ni. .

     

Catalytic activity of rhodium-indigo sulfonates in hydrogen-water isotope exchange

Rhodium indigo sulfonate complexes are effective catalysts of isotope exchange between hydrogen and water. A study has been made of the transformation of initial complexes into catalytically active forms. Kinetic regularities of isotope exchange and an equation for the reaction rate have been obtained.

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Enantioselective hydrogenation on heterogeneous metal catalysts

The rate of formation of the excess of one enantiomeric product in the enantioselective hydrogenation of ethyl acetoacetate (EAA) and acetylacetone (acac) on a Raney copper catalyst modified with chiral aminoacids (AmA) correlates with the formation constants of the mixed complexes [CU EAA AmA] and [Cu acac AmA].

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() - () , () [Cu··] [Cu··].

     

Vapor phase oxidation of 2-methylpyridine on vanadyl polyphosphates

Vanadyl -and -polyphosphates in vapor phase oxidation of 2-methylpyridine show comparable activity and selectivity to the formation of pyridine-2-carboxaldehyde as traditional vanadium-molybdeum oxide catalysts. A redox mechanism for the reaction of 2-methylpyridine oxidation on vanadyl polyphosphates is suggested with interaction between 2-methylpyridine and oxygen of the catalyst lattice as the rate-determining step.

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- - 2- -- . - 2- . - 2- .

     

Investigation of the chemisorption of propylene on zinc oxide by temperature-programmed desorption

The interactions of propylene with zinc oxide have been studied by temperature-programmed desorption (TPD) under experimental conditions free of inter- or intraparticle limitations or readsorption phenomena.The results indicate that propylene is adsorbed on two types of active sites, and the Arrhenius parameters for the corresponding desorption processes have been calculated; moreover, on the basis of these results, important hypotheses can be made regarding the reaction mechanisms of the total oxidation and the dehydroaromatization of propylene on zinc oxide.The experiments confirm that thermal methods can be successfully used in the interesting and important field of heterogeneous catalysis.

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Zusammenfassung Die Wechselwirkungen von Propylen mit Zinkoxid wurden durch temperaturprogrammierte Desorption (TPD) unter Versuchsbedingungen frei von inter- oder intrapartikulären Begrenzungen oder Readsorptionserscheinungen untersucht.Die Ergebnisse zeigen, daß Propylen an zwei Typen von aktiven Stellen adsorbiert wird. Die Arrhenius-Parameter für die entsprechenden Desorptionsprozesse wurden berechnet. Aufgrund dieser Ergebnisse können wichtige Hypothesen bezüglich des Reaktionsmechanismus der totalen Oxidation und der Dehydroaromatisierung von Propylen an Zinkoxid aufgestellt werden.Die Versuche bestätigen, daß thermische Methoden auf dem interessanten und wichtigen Gebiet der heterogenen Katalyse mit Erfolg eingesetzt werden können.

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- , . , . . , . , .

     

The general applicability of the Kissinger equation in thermal analysis

Computer modelling calculations will be presented which verify the fact that, if a single reaction follows either Arrhenius or transition state kinetic theory over its entire extent, then the maximum rate of reaction data obeys the modified Kissinger equation, irrespective of the applicable kinetic model. The magnitude of the Kissinger parameter correction term is dependent on the model, ranging from about 0.4% for n^th order and random nucleation, Avrami-Erofeev models to 17% for three dimensional diffusion controlled reactions. The consequences of selecting the incorrent kinetic model in interpreting experimental thermoanalytical data will be examined, thereby giving a rational explanation for the wide range of published kinetic parameters for a number of solid state decompositions.

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Zusammenfassung Computer-Modellberechnungen werden dargelegt, die die Tatsache bestätigen, daß die maximale Reaktionsgeschwindigkeit unabhängig vom angewandten Modell von der modifizierten Kissinger-Gleichung beschrieben wird, wenn eine einzelne Reaktion über den gesamten Verlauf hinweg entweder der kinetischen Arrhenius- oder der Übergangszustands-Theorie folgt. Die Größe der Kissinger-Parameter hängt vom Modell ab und liegt zwischen 0,4% für Avrami-Erofeev-Modelle mitn-ter Ordnung und ungeordneter Kristallkeimbildung und 17% für dreidimensionale diffusionskontrollierte Reaktionen. Die bei Wahl eines falschen kinetische Modells für die Interpretierung thermoanalytischer Daten eintretenden Folgen werden untersucht, wobei eine vernünftige Erklärung für die große Streuung von publizierten kinetischen Parametern einer Anzahl von Festkörperzersetzungsreaktionen gegeben wird.

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, , , , . 0,4% n- - 17% — - . , .

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Presented at the 13th North American Thermal Analysis Society Conference, Sept. 1984, Philadelphia, PA, paper 55.This work was conducted as a part of the Kentucky Energy Resource Utilization Program supported by the Commonwealth of Kentucky, Kentucky Energy Cabinet.     

Selective dehydrogenation of tetralin on zeolites

The dehydrogenation of tetralin on two zeolite catalysts has been studied, the experiments were planned statistically according to the Orthogonal Central Composite Design. In order to determine the influence of coke deposits, the time-on-stream theory of catalyst decay is applied too.

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. . .

     

Influence of the various forms of molybdena on the adsorptive and catalytic (dehydrogenation and hydrogenolysis) properties of molybdena-alumina catalysts

The contents of three forms of molybdenum oxide compounds in molybdena-alumina catalysts have been determined by their solubility in water and ammonia. The form which is readily soluble in water and reducible to Mo(IV) at 400°C and P_H2=10⁵ Pa is active in cyclohexane dehydration, and the forms soluble in water and ammonia are active in thiophene hydrogenolysis.

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. , 400°C P_{H 2}=I Mo(IV); — .

     

Stoichiometry as canonical transformation of chemical kinetics

Applying the apparatus of differential manifolds and that of classical conservative point mechanics, it is shown that stoichiometry plays the role of canonical transformations in chemical reaction kinetics.

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, , .

     

Interaction between peroxyl radicals of polyatomic esters and aromatic nitrons

Reactivity and rate constants in reactions between peroxyl radicals of ethylene glycol diacetate and aromatic nitrons have been investigated.

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.

     

Comparison of the sulfurization of CoMoK/Al2O3 catalyst with H2S and CS2

Only H₂S consumption and H₂O formation was found in the sulfurization of CoMoK/Al₂O₃ water gas shift catalyst with H₂S/H₂, but CO₂ was formed first, then CH₄, H₂O and H₂S appeared in the later part of TPS with CS₂/H₂. Carbon deposition on the catalyst during the sulfurization with CS₂/H₂ caused a lower activity than the catalyst sulfurized with H₂S but could be removed in the run of WGS reaction.

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, CoMoK/Al₂O₃, H₂S/H₂ H₂S H₂O, CS₂/H₂ CO₂ CH₄, H₂O H₂S. CS₂/H₂ H₂S, , .

     

Effect of medium composition on the monooxygenase activity of immobilized hemin in aniline oxidation

The effect of the composition of the reaction medium on the rate of aniline oxidation to p-aminophenol by hydrogen peroxide on hemin immobilized on -propylimidazole-modified silica has been studied. Organic solvent additives (alcohols, esters and nitriles) are shown to increase the reaction rate. The observed effect is attributed to the decrease of the medium dielectric constant.

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