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Vol 66, No 4 (2025)

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V РОССИЙСКИЙ КОНГРЕСС ПО КАТАЛИЗУ "РОСКАТАЛИЗ" (21–26.04.2025 г., САНКТ-ПЕТЕРБУРГ

Cross-linking of chitosan with ferulic acid in the presence of bacterial laccase: Investigation of the mechanism – the Michael addition reaction or the formation of Schiff bases?

Dmitruk A.R., Oskin P.V., Trubitsina L.I., Yushkin A.A., Alferov V.A., Leontievskiy A.A., Ponamoreva O.N.

Abstract

We demonstrate for the first time the feasibility of using bacterial laccase as a biocatalyst for oxidizing ferulic acid (FA) to enable nucleophilic crosslinking of chitosan under neutral conditions, targeting future applications in medicine and the food industry. We have established optimal conditions achieving a high degree of chitosan crosslinking (up to 85%). Employing quantum-chemical modeling and spectral analysis techniques, it was determined that the predominant mechanism for the nucleophilic attack of chitosan amino groups on the phenoxyl radical – the oxidation product of FA – involves Michael addition, followed by radical recombination. This process results in the formation of crosslinks consisting of β-β’ coupled FA dimers while retaining the phenoxyl functionalities.
Kinetics and Catalysis. 2025;66(4):251–261
pages 251–261 views

Features of propane dehydrogenation on Mn/γ-Al2O3 catalysts produced by various methods

Vosmerikov A.A., Stepanov A.A., Vosmerikova L.N.

Abstract

The physicochemical and catalytic properties of Mn-containing catalysts based on γ-Al2O3, obtained by various methods, were studied in the process of converting propane into olefin hydrocarbons. The dependence of the activity and selectivity of the catalytic systems on the localization of the introduced manganese and their acidic properties was shown. It was found that the greatest amount of olefin hydrocarbons during the conversion of propane is formed on the Mn-containing catalyst, into which manganese was introduced by the impregnation method. The nature and amount of carbon deposits formed on the studied catalysts during the propane conversion process were established. It was shown that the coke deposits formed on the Mn-containing catalysts have a virtually uniform structure and are characterized by a low degree of condensation, which allows for their relatively easy oxidative regeneration.
Kinetics and Catalysis. 2025;66(4):262-270
pages 262-270 views

Features of Catalytic Pyrolysis of C2−C4 Hydrocarbons on Nickel-tin Catalyst Obtained by Mechanochemical Alloying

Shivtsov D.M., Bauman Y.I., Mishakov I.V., Vedyagin A.A.

Abstract

Catalytic pyrolysis has been considered as one of the most effective methods for processing light C2+ hydrocarbons. In this study, a Ni−Sn catalyst was synthesized using mechanochemical alloying, and the influence of temperature (in the range of 600–750°C) on the decomposition of C2−C4 alkanes into a carbon nanomaterial was investigated. The Ni−Sn system demonstrated a high carbon yield exceeding 300 gC/gcat at T > 710°C. The calculated value of the apparent activation energy of reaction was 140 ± 5 kJ/mol. The effect of reaction temperature on the morphology, structure, and textural characteristics of produced carbon nanomaterial was explored. Regardless of the process temperature, the product consisted of nanofibers with thickness ranging from 5 to 100 nm. The obtained material exhibited a significant specific surface area (up to 450 m2/g) and high pore volume (up to 0.80 cm3/g).
Kinetics and Catalysis. 2025;66(4):271-280
pages 271-280 views

Bimetallic (Co, Fe, Ni)Mg4Al2On layered double hydroxides based catalysts for the process of ammonia decomposition

Fedorova Z.A., Borisov V.A., Abbas B., Pakharukova V.P., Gerasimov E.Y., Gladkiy A.Y., Shlyapin D.A., Snytnikov P.V.

Abstract

In this work, monometallic MMg4Al2On and bimetallic MxMyMg4Al2On (M – Co,Fe, Ni) layered double hydroxides based catalysts were synthesized by the coprecipitation method. It was found that the samples dried at 110°C are layered double hydroxides with a hydrotalcite structure. After calcination at 550°C, the samples form mixed oxides with a specific nanostructure, intermediate between the NaCl and spinel type structures. The samples are characterized by a high specific surface area (105–209 m2/g). The catalytic activity was studied in the ammonia decomposition process. Among all the catalysts, the Co0.5Ni0.5Mg4Al2On catalyst has the highest activity: at 550°C and GHSV 72000 mL h−1 gcat −1 ammonia conversion was 32%, which corresponds to H2 productivity of 25.7 mmol gcat −1 min−1. According to the TEM, it was found that the average size of metal particles in the Co0.5Ni0.5Mg4Al2On catalyst is 10–14 nm. The Co0.5Ni0.5Mg4Al2On catalyst showed stable activity during the all testing period in the ammonia decomposition process (~40 h).
Kinetics and Catalysis. 2025;66(4):281–292
pages 281–292 views

Kinetic regularities of CNF synthesis on Ni–Cu–Al2O3 catalyst in the reaction of CH4 decomposition

Afonnikova S.D., Shivtsov D.M., Veselov G.B., Ayupov A.B., Bauman Y.I., Mishakov I.V., Vedyagin A.A., Shelepova E.V.

Abstract

The work is aimed at studying the kinetic patterns of carbon nanofiber (CNF) growth on the Ni–Cu–Al2O3 catalyst in the methane decomposition reaction. The catalyst was prepared by mechanochemical activation in an Activator-2S planetary mill. The dependence of the catalytic activity of the Ni–Cu alloy on the hydrogen concentration (0–28 vol. %) in the decomposed mixture (CH4/H2) was studied in a flow gravimetric setup with a McBain balance. It is shown that in the absence of hydrogen, the CNF accumulation rate rapidly decreases. The introduction of 10 vol. % hydrogen in the reaction mixture allows stabilizing the CNF formation rate over 90 min of the reaction (600°C, CNF yield = 41.4 g/gcat). The observed reaction order with respect to hydrogen was estimated to be –0.18 at low H2 concentrations (0–16 vol. %) and –1.5 at its higher content in the reaction mixture (16–28 vol. %). The effect of pyrolysis temperature on the nature of the CNF accumulation kinetics was studied in the range of 550–700°C. The values of the observed activation energy (Ea) were determined at different time intervals of the process. It was found that Ea does not depend on the presence of hydrogen in the reaction mixture. The morphology and structure of the CNF samples obtained at different hydrogen contents in the reaction mixture were studied by transmission electron microscopy. It was shown that with increasing hydrogen concentration, there is a tendency to form larger CNF with a defective structure. The textural characteristics of the carbon material were measured by argon adsorption at 87 K. The specific surface area of the CNF varies from 90 to 150 m²/g depending on the reaction conditions. The obtained results can be used in the development of a mathematical model of a catalytic pyrolysis reactor of methane.
Kinetics and Catalysis. 2025;66(4):293-307
pages 293-307 views

Formation of the Active State of Catalysts Based on Nickel-Substituted Copper Aluminates NixCu1-xAl2O4 (x = 0.1–0.5) and their Catalytic Properties in the Dry Reforming of Methane Reaction

Shutilov A.A., Marchuk A.S., Fedorova V.E., Sadovskaya E.M., Eremeev N.F., Zenkovets G.A.

Abstract

NixCu1-xAl2O4 (x = 0.1–0.5) catalysts, obtained by co-precipitation method from nickel, copper and aluminum water nitrate solution with followed drying and calcination in air at 750°C were synthesized. They are characterized by a spinel structure, in which nickel and copper ions are stabilized. Reducing of obtained catalysts in a hydrogen-containing medium and further work in the dry reforming of methane reaction leads to formation of highly dispersed particles of Ni0–Cu0 alloy. Up to 28 wt % of active phase are formed and stabilized on the spinel surface. The investigation of the influence of catalyst composition on their activity in the DRM reaction accompanied the long tests on stream showed that the Ni0.35Cu0.65Al2O4 catalyst demonstrates highest activity. At 750°C and contact time of τ = 30 ms, total convertion of CH4 is 89%, the CO2 conversion is 86%, the hydrogen yield is 48%, the H2/CO ratio is 0.75. This catalyst is stably working in the DRM reaction mixture for 20 h. The regularities of the formation of active state for this catalyst were studied by the XRD method in situ.
Kinetics and Catalysis. 2025;66(4):308-326
pages 308-326 views

Formation and Properties of Co Oxidation Catalysts Based on Amorphous Pd and Pt Nanoparticles

Gurevich S.A., Yavsin D.A., Rostovshchikova T.N.

Abstract

In this paper, the advantages of the laser electrodispersion (LED) method for the synthesis of highly active crust-type catalysts containing coatings of amorphous Pd and Pt nanoparticles are demonstrated. Using examples of complete and selective oxidation of CO (CO-TOX and CO-PROX) under different conditions, a comparative analysis of recently obtained data on the structure and catalytic behavior of highly dispersed Pd and Pt nanoparticles deposited on carbon, oxide and aluminosilicate supports using the LED method was carried out. The properties of such samples with reduced metal content (down to 10–3 wt %) are compared with the characteristics of supported catalysts prepared by the standard impregnation method. The structure features and catalytic behavior of LED catalysts caused by the highly dispersed and amorphous state of metal nanoparticles are revealed.
Kinetics and Catalysis. 2025;66(4):327-339
pages 327-339 views

Periodic Transformations of the Catalyst During Self-Oscillating Methane Oxidation on Bulk Nickel

Bychkov V.Y., Gusenkov A.V., Rudenko E.I., Silchenkova O.N., Korchak V.N.

Abstract

Periodic changes in the composition and morphology of the surface of Ni foil (2 × 8 and 6 × 6 mm) and nickel foam during self-oscillations of the methane oxidation reaction rate were studied using mass spectrometry, thermogravimetry, XRD, SEM, and EMF. Self-oscillations of the reaction rate were observed in the flow of a mixture of 42.3% CH4 − 7.7% O2 − 3.8% Ar − 46.2% in the temperature range of 500−700°C. It is shown that the period of one oscillation consists of two phases with different catalytic activity. In the first phase, partial oxidation of methane occurs, the rate of which decreases with time. In the second phase, there is a total oxidation of methane, the rate of which increases towards the end of this phase. At various points in the oscillation cycle, the reaction was interrupted and samples were obtained to study the composition and morphology of the surface. It has been established that oxygen in the form of NiO and carbon in the form of graphite-like structures periodically accumulate on the Ni surface under conditions of self-oscillation. The dynamics of accumulation/conversion of NiO and surface carbon during various phases of the oscillatory cycle, which correlate with the above-mentioned changes in catalytic activity, has been quantitatively studied.
Kinetics and Catalysis. 2025;66(4):340-354
pages 340-354 views

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