Petroleum Chemistry


Media registration certificate
: No. 0110162 dated 02/05/1993

Founders

  • Institute of Petrochemical Synthesis named after. A.V. Topchiev RAS;
  • Russian Academy of Sciences

Editor-in-Chief

  • Maksimov Anton Lvovich, Academician of the RAS, Doctor of Chemical Sciences,  Professor

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6 issues per year / Subscription

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White List (2nd level), Higher Attestation Commission List, RISC


"Neftehimiâ" founded in 1961, offers original papers and reviews of theoretical and experimental studies concerned with current problems of petroleum chemistry and processing such as chemical composition of crude oils and natural gas liquids; petroleum refining (cracking, hydrocracking, and catalytic reforming); catalysts for petrochemical processes (hydrogenation, isomerization, oxidation, hydroformylation, etc.); activation and catalytic transformation of hydrocarbons and other components of petroleum, natural gas, and other complex organic mixtures; new petrochemicals including lubricants and additives; environmental problems; and information on scientific meetings relevant to these areas.

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Current Issue

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Vol 66, No 2 (2026)

Cover Page

Full Issue

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Scientific and Technological Congress “Chemistry and Chemical Technologies in the Digital Age.” Announcement
Editorial b.
Abstract
5–9 октября 2026 года в Институте органической химии им. Н.Д. Зелинского РАН (г. Москва) состоится научно-технологический конгресс «ХИМИЯ И ХИМИЧЕСКИЕ ТЕХНОЛОГИИ В ЦИФРОВУЮ ЭПОХУ»
Petroleum Chemistry. 2026;66(2):103
pages 103 views

REVIEWS

Gas-Phase One-Step CO and CO2 Hydrogenation to Methyl Acetate and Other Oxygen-Containing C2 Compounds (Review)
Batova T.I., Obukhova T.K., Dement’ev K.I.
Abstract
This review analyzes the features of the direct one-step methyl acetate synthesis by CO and CO2 hydrogenation in the presence of bi- and multifunctional combined oxide-zeolite catalysts. The technological features of relay/tandem catalysis, as well as strategies for selecting catalysts for each reaction step based on the relay principle are discussed. Demonstrated are the importance of thermodynamic and kinetic matching of intermediate steps, the targeted reaction sequence, and the spatial arrangement of catalyst components. Summarized are approaches for improving and optimizing the composition of each component of multifunctional catalysts for the selective methyl acetate and ethanol synthesis by CO/CO2 hydrogenation. A comparison was made of the performance of methyl acetate synthesis by direct gas-phase CO/CO2 hydrogenation, as well as by dimethyl ether carbonylation (DME/CO and DME/CO/H2). In comparison with dimethyl ether carbonylation, where methyl acetate selectivity is virtually 100% at temperatures of 200–220°C and pressures of 0.1–2.0 MPa, methyl acetate selectivity reaches 75–90% in direct CO/CO2 hydrogenation, with CO and CO2 conversions being up to 5% and 20%, respectively, while the combined catalysts exhibit their efficiency over wider temperature and pressure ranges (200–300°C, 2–5 MPa).
Petroleum Chemistry. 2026;66(2):104–121
pages 104–121 views

RESEARCH ARTICLES

Effectiveness of Impact of Acidic Oil-Displacing Compositions Based on Ternary Deep Eutectic Solvents on the Viscosity and Composition of Heavy Oil of the Usinskoye Field When Simulating the Oil Displacement Process in Laboratory Conditions
Sholidodov M.R., Altunina L.K.
Abstract
The article presents the results of a comprehensive study of the effectiveness of acidic oil-displacing compositions based on ternary deep eutectic solvents (DES) “pentaerythritol — boric acid — urea”, “glycerin — boric acid — urea” and “sorbitol — boric acid — urea” for increasing oil recovery from high-viscosity oil formations of the Usinskoye field. Using physical modeling of the oil displacement process, it was demonstrated that these compositions significantly increase the oil displacement efficiency (up to 45%). The key mechanism of action was found to be a change in the colloidal structure of heavy oil: the compositions interact with the resin fraction, resulting in a decrease in viscosity, an increase in the proportion of light hydrocarbons (especially n-alkanes), and improved filtration performance. The results were confirmed by IR spectrum, chromatograph mass spectrometry, and component analysis, which together substantiate the potential of these compositions for use in enhanced oil recovery technologies.
Petroleum Chemistry. 2026;66(2):122–133
pages 122–133 views
Preparative Isolation and Characterization of Vanadyl Porphyrins Contained in Gilsonite
Tazeev D.I., Mironov N.A., Milordov D.V., Tazeeva E.G., Yakubova S.G., Akhmetova G.R., Yakubov M.R.
Abstract
Gilsonite (natural asphalt) was employed for the first time as a raw material for the preparative isolation of spectrally pure petroleum vanadyl porphyrins using sulfocationite sorbents in an extraction-chromatographic procedure. The isolation process includes sequential extraction of vanadyl porphyrins from gilsonite with N, N-dimethylformamide (DMF), chromatographic fractionation of the extract on moistened silica gel, and final purification of the vanadyl porphyrin concentrate on a silica-gel-based sulfocationite. It was shown that the use of the sulfocationite enables the separation of vanadyl porphyrins into two fractions differing in color (red and green), composition, and spectral characteristics. The red fraction is enriched in etioporphyrin- and DPEP (deoxophylloerythroporphyrin)-type vanadyl porphyrins, whereas the green fraction predominantly contains rhodo derivatives containing a fused benzene ring. The isolated fractions were characterized by UV-visible spectroscopy and MALDI-TOF mass spectrometry. The proposed extraction-chromatographic approach can be applied to evaluate gilsonite as a promising feedstock for the production of natural petroleum porphyrins, which are potential components of functional materials, dyes, catalysts, and photoactive systems.
Petroleum Chemistry. 2026;66(2):134–143
pages 134–143 views
Dependence of the Properties of NiMo/ZSM-23-Al2O3 Hydroisomerization Catalysts on Their Activation Method
Bogomolova T.S., Smirnova M.Y., Klimov O.V., Noskov A.S.
Abstract
Bifunctional hydroisomerization NiMo/ZSM-23-Al2O3 catalysts with different concentrations of active metals were synthesized, followed by activation by one of the methods: sulfidation or reduction. The catalysts were studied using a combination of physicochemical methods and tested in the conversion of n-decane and hydrotreated diesel fraction. The properties of NiMo/ZSM-23-Al2O3 catalysts were shown to depend on the metal concentration and activation method. It was ascertained that reductive activation leads to the production of more active and isoselective catalysts compared to sulfidation due to the formation of highly dispersed bimetallic particles of the active component uniformly distributed over the support surface. It was found that in the conversion of diesel fraction the required temperature of the cold filter plugging point for the reduced catalyst was reached 17°C lower, and the product yield was ~3 wt.% higher compared to the sulfide sample. In testing on real feedstock, the reduced NiMo catalysts demonstrated similar properties to those of noble metal-based isodewaxing catalysts.
Petroleum Chemistry. 2026;66(2):144–156
pages 144–156 views
Dependence of the Catalytic Activity and Physicochemical Properties of the CоMо/Al2O3 Catalyst on the Phosphorus Content in the Carrier
Yudincev S.V., Pimerzin A.A.
Abstract
Modified aluminophosphate carriers were synthesized by the method of impregnation of the industrial γ-Al2O3 carrier (Alumac-3, Alumac Construct) with solutions of ammonium hydrophosphate of various concentrations, the physicochemical characteristics of which were determined by the methods of IR spectroscopy, X-ray fluorescence analysis, low-temperature nitrogen adsorption and temperature-programmed desorption of ammonia. Their physicochemical properties were determined using IR-spectroscopy, X-ray fluorescence analysis, low-temperature nitrogen adsorption, and temperature-programmed ammonia desorption. Studies of the carriers showed that increasing the phosphorus concentration in the carrier alters its textural and acidic properties. When phosphorus is added to the carrier, the average pore diameter and volume decrease, and the specific surface area decreases significantly, while the pore size distribution remains unchanged. Temperature-programmed ammonia desorption data indicate a shift in the peaks of acid sites of varying strengths toward higher temperatures and an increase in overall acidity with increasing phosphorus concentration in the carrier. Based on the obtained supports, sulfide CoMoS catalysts were synthesized, followed by a study of their properties in dibenzothiophene (DBT) hydrodesulfurization and naphthalene hydrogenation reactions in the presence of quinoline. It was found that modification of the standard support (γ-Al2O3) of the cobalt-molybdenum catalyst with phosphorus (phosphorus content of 0.93 wt%) leads to an increase in conversion in the DBT hydrodesulfurization reaction by 16.1% and in the naphthalene hydrogenation reaction by 3%.
Petroleum Chemistry. 2026;66(2):157–167
pages 157–167 views