


Vol 59, No 6 (2018)
- Year: 2018
- Articles: 15
- URL: https://journal-vniispk.ru/0023-1584/issue/view/9983
Article
A New Algorithm for the Reactivity Umpolung of Aliphatic Nitro Compounds
Abstract
A new four-stage algorithm for the reactivity umpolung of aliphatic nitro compounds has been proposed and experimentally confirmed. Bis(trialkylsilyloxy)iminium cations, which are key intermediates in the new scheme, have been qualitatively and quantitatively determined by the method of double nuclear magnetic resonance. Their thermodynamic parameters have been determined. The kinetics of coupling of these cations with π-nucleophiles has been measured experimentally, and the stereodynamics of the interaction of these cations has been discussed using a general model involving anomeric assistance. The utility and novelty of the proposed approach for the development of modern methodology of organic synthesis using available aliphatic nitro compounds as initial reagents have been demonstarted.



Kinetics Modeling of Fischer–Tropsch Synthesis on the Cobalt Catalyst Supported on Functionalized Carbon Nanotubes
Abstract
An active cobalt catalyst supported on functionalized carbon nanotubes was prepared and tested for CO hydrogenation to produce liquid hydrocarbons in the Fischer–Tropsch synthesis. The catalyst characterization was carried out using different methods including X-ray diffraction, transmission electron microscopy and BET surface area equation. The kinetic experiments were performed in a fixed-bed reactor under following conditions: T =200–240°C, P = 15–30 bars, GHSV = 0.5–1.5 nL \({\text{g}}_{{{\text{cat}}}}^{{ - 1}}\) h–1 and H2/CO feed ratio (mol/mol) = 1–2.5. Based on various mechanisms and Langmuir–Hinshelwood–Hougen–Watson type rate equations, eleven kinetic expressions for CO consumption were tested and the best-fitted model is achieved. In kinetic rate development, various rate-determining steps (RDS) are considered for evaluation of RDS effects. The kinetic parameters were estimated with nonlinear regression method using Levenberg–Marquardt method to make refined optimization. The obtained energy of activation was 78 kJ/mol for optimal kinetic model. The obtained results show that the best models for proposed elementary reactions involve the formation of surface species as RDS rather than syngas adsorption.



Synthesis and Characterization of CdS Photocatalyst with Different Morphologies: Visible Light Activated Dyes Degradation Study
Abstract
CdS nanoparticles (CdS NPs) and CdS nanoslabs (CdS NSs) were synthesized from the single source (SS) and multi-source (MS) precursors, respectively. Our target was to observe any change in morphology by altering the synthetic route. CdS NPs with spherical morphology (0.2–0.5 µm in diameter) were obtained by using the SS precursor route via the formation of a Cd-complex. CdS NSs (100–200 nm in length, 50–100 nm wide and 25–50 nm in thickness) were obtained by using the MS precursors, by direct addition of the ligand to metal salt. Both NPs and NSs were used for the degradation of four different cationic organic dyes viz., malachite green (MG), methylene blue (MB), rhodamine B (RhB) and methyl violet (MV) under visible light. CdS NPs synthesized from SS precursor exhibited higher photocatalytic activity than CdS NSs fabricated via MS precursor due to spherical morphologies (small size of particles increases the surface area) and higher band gap. On the other hand, CdS NSs show sheet or cube like morphologies. The kinetic study proved that the rate constants for the MG, MB, MV, and RhB degradation by CdS NPs (1.65 × 10–2, 1.25 × 10–2, 1.2 × 10–2, and 1.24 × 10–2 min–1, respectively) are higher than those for CdS NSs (1.45 × 10–2, 1.13 × 10–2, 1.05 × 10–2, 1.14 × 10–2 min–1, respectively). The precursors were characterized by 1H and 13C nuclear magnetic resonance. Phase pattern and composition of CdS were confirmed by X-ray diffraction and energy dispersive X-ray spectroscopy. Morphology and size were confirmed by transmission electron microscopy and scanning electron microscopy.



Characterization of \(\text{SO}_{4}^{{2 - }}\)/ZnO and Photodegradation Kinetics of 2,4-Dichlorophenoxyacetic Acid (2,4-D)
Abstract
This work is a theoretical and practical study on the synthesis and characterization of a ZnO photocatalyst doped with \({\text{SO}}_{4}^{{2 - }}.\) X-ray diffraction analysis, band gap energy ranges and BET surface area measurements demonstrated that \({\text{SO}}_{4}^{{2 - }}\) had an impact on the photocatalyst properties of ZnO, when this material was used for the production of oxidizing agents by the action of ultraviolet radiation. Significant changes in the band gap energy were observed for ZnO doped with 3 mol of \({\text{SO}}_{4}^{{2 - }}.\) The photodegradation of 2,4-dichlorophenoxyacetic acid (2,4-D) was evaluated, a toxic pesticide found in agricultural effluents in Sinaloa (Mexico). Degradation process was monitored in photoreactors of 500 mL, in which the maximum degradation efficiency was achieved after 6 h. A removal efficiency of 38.4% (1.55 mmol/L) was found with an undoped ZnO, while an efficiency of 82.3% (3.4 mmol/L) was observed with \({\text{SO}}_{4}^{{2 - }}\) doped ZnO. Based on the results obtained, the photocatalysts used in this study can be considered as promising materials to mitigate pollution problems coming from agricultural activities in these regions.



Formal Kinetic Description of Photocatalytic Hydrogen Evolution from Ethanol Aqueous Solutions in the Presence of Sodium Hydroxide
Abstract
The dependences of the rate of the photocatalytic hydrogen production in ethanol aqueous solutions on the concentration of ethanol and sodium hydroxide on the 1% Pt/10% Ni(OH)2/Cd0.3Zn0.7S photocatalyst under visible light irradiation (λ = 450 nm) are studied. To describe kinetic data, the Langmuir–Hinshelwood equation was modified. An equation was proposed that reflects the dependence of the reaction rate on the concentration of NaOH, and an equation was derived for the first time that shows the dependence of the rate of photocatalytic hydrogen production from the concentrations of both reactants, ethanol and sodium hydroxide. The validity of the proposed equations was confirmed by their use for the description of the experimental data obtained in this work and reported earlier.



Effect of Transition Metal Compounds on the Cyclohexene Oxidation Catalyzed by N-Hydroxyphthalimide
Abstract
N-Hydroxyphthalimide (NHPI) is an efficient organic catalyst in the oxidation reactions of organic compounds occurring via a radical mechanism, often used together with redox-active ions or transition metal complexes. In this work the catalytic action of NHPI is studied together with Cu(II), Fe(III), and Mo(VI) compounds in the reaction of aerobic oxidation of cyclohexene in an acetonitrile solution at 60°C. It was found that iron(III) benzoate accelerates the reaction by rapidly generating the active form of the phthalimide-N-oxyl radical (PINO) catalyst, but does not cause decomposition of the hydroperoxide. The oxidation product is 2-cyclohexenyl hydroperoxide formed with a selectivity of 85% at a cyclohexene conversion of 50%. Copper(II) acetate initiates oxidation and is capable of catalyzing the radical decomposition of the hydroperoxide and secondary oxidation of allyl oxygenates. When reaching a cyclohexene conversion close to 80%, the overall selectivity to the main products, 2-cyclohexenyl hydroperoxide and 2-cyclohexen-1-on, was 70%. The addition of iron(III) and molybdenum(VI) compounds led to the intensive generation of hydroperoxide and its activation as an electrophilic reactant capable of cyclohexene epoxidation. As a result of the use of the multifunctional three-component NHPI–Mo(VI)–Fe(III) catalyst, cyclohexene oxidation by molecular oxygen occurred with the formation of epoxycyclohexane. The selectivity to the products of cyclohexene epoxidation was close to 50%, which is a value expected from theory.



Propane Dehydrogenation on Chromium Oxide and Gallium Oxide Catalysts in the Presence of CO2
Abstract
The catalytic and physicochemical properties of GaOx/SiO2 and CrOx/SiO2 supported onto silica gels as catalysts for propane dehydrogenation were studied with the use of stationary and nonstationary (a response method) techniques, TPR-H2, TPD-NH3, and UV spectroscopy, and the effect of CO2 on the course of dehydrogenation reaction was examined. It was found that the relatively low acidity of silica gels prevents intense coke deposition and has a positive effect on the stability of catalyst operation. At the same time, the acid hydroxyls of these supports play an important role in the formation of a disperse active surface. In the case of the GaOx/SiO2 catalysts, the insufficient dispersity of the active phase is a reason for the low specific activity of these systems. It was found that the appearance and growth of catalytic activity with temperature was accompanied by the formation of the reduced forms of gallium oxide, the fraction of which was limited under the conditions of dehydrogenation (600°C). It was established that CO2 hindered the adsorption of propane on the surface of catalysts to decrease its conversion; at the same time, it prevented the adsorption of propylene and its further conversion into coke. In the case of the chromium systems, the increase in the yield of propylene and in the stability of operation due to the oxidation of coke and hydrogen upon the introduction of CO2 prevailed over a negative effect. This negative effect was more pronounced for the gallium catalysts, and this led to a decrease of the propylene yield.



Synthesis of Dimethyl Ether from Syngas on the Catalysts with the ZSM-5 Zeolites
Abstract
Several bifunctional catalysts for dimethyl ether (DME) synthesis from syngas are prepared on the basis of commercial methanol-synthesis Megamax 507 catalyst. Commercial HZSM-5 zeolites with a SiО2/Al2О3 ratios of 23, 80, and 307 and γ-alumina were used as dehydration components. Physicochemical characteristics of zeolites and alumina are studied: temperature-programmed desorption of ammonia, the porosity, and the specific surface area. The activity of catalyst in DME synthesis is studied in a microcatalytic flow-type setup at a pressure of 3 MPa in a temperature range of 200–260°С with a productivity based on syngas of up to 30000 L \({\text{kg}}_{{{\text{cat}}}}^{{ - 1}}\) h–1. The composition of syngas was (vol %): CO, 21; CO2, 6; Н2, 67; N2, 6 . It is shown that zeolites, especially with silica/alumina ratios of 23 and 80, are more active than alumina in methanol dehydration to DME, but in the presence of these zeolites, traces of hydrocarbons were detected at 260°С. The zeolite with a silica/alumina ratio of 307 is the most interesting of the studied zeolites. Hydrocarbons are almost not formed on it, and its activity in methanol dehydration is somewhat higher than that of alumina. The behavior of the methanol-synthesis component of the bifunctional catalyst is studied: the apparent activation energy of methanol synthesis and the degree of approaching to equilibrium are estimated depending on the catalyst load.



Effect of the Chemical Atmosphere of the Thermolysis of the Complex PdAg2(OAc)4(HOAc)4 on the Formation of Active Centers in Pd–Ag/CeO2 Catalysts for the Low-Temperature Oxidation of Carbon Monoxide
Abstract
The Pd–Ag/CeO2 catalysts were prepared by the impregnation of highly dispersed CeO2 with a solution of the heteroatomic complex PdAg2(OAc)4(HOAc)4. Samples obtained after the thermolysis of PdAg2(OAc)4(HOAc)4 in N2 and H2 contained Pd–Ag alloy and Pd particles immobilized on CeO2. The Pd0–CeO2 metal oxide centers formed at the interface were highly active in the low-temperature reaction of CO oxidation. The particles of Pd were absent from the Pd–Ag/CeO2 sample prepared by the decomposition of PdAg2(OAc)4(HOAc)4 in an atmosphere of O2; in this case, a significant portion of the Pd–Ag phase was covered with a film of CeO2, which dramatically slowed down the rate of reaction at low temperatures.



Model Bimetallic Pd–Ag/HOPG Catalysts: An XPS and STM Study
Abstract
A series of model bimetallic Pd–Ag catalysts with different ratios of metals and size distributions of supported particles was prepared by successive metal deposition onto a modified surface of highly oriented pyrolytic graphite (HOPG). X-ray photoelectron spectroscopy (XPS) and scanning tunneling microscopy (STM) were used to characterize the structural and electronic properties, as well as the morphology of nanoparticles at all stages of catalyst preparation. The use of the method made it possible to obtain bimetallic particles with various structures: alloyed, core–shell, and those consisting of individual monometallic particles. The XPS method with synchrotron radiation was used to determine the patterns in the formation of alloyed bimetallic particles, their chemical composition, structure, and the ranges of thermal stability under conditions of ultrahigh vacuum.



An XPS Study of the Interaction of a Palladium Foil with NO2
Abstract
The interaction of a palladium foil with nitrogen dioxide in a temperature range of 30–450°C at three NO2 pressures of 10–6, 10–5, and 10–4 mbar was studied by X-ray photoelectron spectroscopy (XPS). In all cases, a three-dimensional oxide film was formed on the surface of palladium metal starting with a temperature of 150°C. Based on the measurements of the Pd 3d5/2, Pd 3p3/2, and O 1s binding energies and the [Pd] : [O] atomic ratio, it was found that the film consisted of the palladium oxide PdO. The oxide film thickness d was estimated based on the weakening of the Pd 3d line of metallic palladium. As the interaction temperature was increased, d initially increased to reach a maximum of ~3.5–5 nm; thereafter, it began to decrease due to the decomposition of PdO to a metallic state.



Catalytic Etching of Platinoid Gauzes During the Oxidation of Ammonia by Air. Reconstruction of the Surface of a Platinoid Gauze Backside in the Course of Ammonia Oxidation at 1133 K
Abstract
Scanning electron microscopy and energy-dispersive X-ray spectroscopy were used to study microstructure, morphology and chemical composition of the surface and near-surface layers of polycrystalline wire of commercial platinoid gauzes containing Pt (81 wt %), Pd (15 wt %), Rh (3.5 wt %), and Ru (0.5 wt %) after ammonia oxidation (10 vol % NH3) by air at 1133 K for 50 h in the presence of these gauzes. Upon the completion of the catalytic reaction of ammonia oxidation, reconstruction (catalytic etching) of the surface layer on the backside of gauze wire (in the direction of the gas flow) was observed, in which the regions with different degrees of etching were identified. The analysis of these regions showed that the catalytic etching of the platinoid wire is initiated by etching the surface layer in the region of grain boundaries and dislocations in the course of highly exothermic catalytic reaction of ammonia oxidation by oxygen penetrated in the regions of defects. The regions with minimal etching contain smooth grains with crystalline terraces, 50 nm high, and with etching pits with size of ~72 nm in a concentration of 4.2 × 108 cm–2. The region with medium etching includes rough grains with etching pits with size of ~85 nm in a concentration of 2.5 × 108 cm–2. The regions with maximal etching consist of recrystallized grains with large pores with sizes of 350–400 nm in concentration of 8.9 × 106 cm–2. These grains are separated by voids with a width of 1–5 μm and a depth of 10 μm, which increases the specific surface area in the surface layer of wire. The growth of the specific surface area of the platinoid wire is accompanied by an increase in the volume rate of ammonia oxidation and, as a result, local overheating due to the high exothermicity of the reaction. With increasing temperature, the rate of diffusion of metal atoms increases, which, in turn, accelerates etching in this region. These processes lead to increasing the region of etching along the wire, which points to the autocatalytic regime of etching of platinoid gauzes in ammonia oxidation by oxygen.



The Reasons for Nonlinear Phenomena in Oxidation of Methane over Nickel
Abstract
The catalytic oxidation of methane over nickel foil is studied. It is shown that, under the oxygen-lean conditions in the regime of a flow-type reactor, nonlinear phenomena can appear in the form of self-sustained oscillations of the reaction rate and the catalyst temperature. To determine the reasons for self-sustained oscillations, X-ray diffraction and mass spectrometry in the operandо mode were used. It was found that the appearance of oscillations in the methane oxidation is due to periodical oxidation–reduction of the surface layer of nickel foil; metallic nickel has a higher catalytic activity than NiO. The oscillations of the catalyst temperature are determined by the occurrence of exothermic and endothermic processes associated with the reduction of nickel oxide and methane oxidation on the surface of metallic nickel.



Initial Stages of Deuterium Adsorption on Gold Nanoparticles
Abstract
The parameters of deuterium adsorption on the surface of gold nanoparticles supported onto highly oriented pyrolytic graphite were determined. It was established that surface coverage with the adsorbate at a level of single nanoparticles began at a graphite–gold interface; thereafter, the entire surface was filled.



Effect of Topochemical Processes in the Synthesis of FeK/C Catalysts on Their Activity and Selectivity in the Fischer–Tropsch Synthesis
Abstract
Iron-containing catalysts promoted with potassium supported on a carbon carrier were prepared by changing the sequence of the introduction of components (iron and potassium) into the carrier (activated carbon) using an impregnation method. After calcination, the catalysts contained hematite and magnetite; in this case, the particle sizes of iron oxides depended on the sequence of the introduction of a potassium promoter. A minimum particle size was observed upon the subsequent introduction of initially potassium from nitrate and then iron. The activation of all of the catalysts in a flow of CO/H2 resulted in the formation of Hägg carbide (Fe5C2). It was shown that the catalyst with the smallest carbide particle size was the most active in the hydrogenation of CO.


