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  1. No Access

    Article

    The Influence of Test Conditions for the Second Hydrocracking Stage Catalysts on the Time to Reach Steady-State Activity

    Catalysts of the second stage of hydrocracking are tested under different conditions, reducing the time required to reach the level of steady-state activity. Tests are performed on a laboratory testbench under...

    I. S. Golubev, P. P. Dik, M. O. Kazakov, O. V. Klimov in Catalysis in Industry (2023)

  2. No Access

    Article

    Dynamics of Silicon Sorption on the NiMo/Al2O3 Guard Bed Catalyst During Hydrotreating of Diesel

    The dynamics of the silicon sorption on the NiMo/Al2O3 guard-bed catalyst containing ~2.0 wt % Ni and ~6.0 wt % Mo during hydrotreating of diesel was studied. The catalyst bed was divided into five equal sections...

    I. S. Golubev, P. P. Dik, R. V. Petrov, I. A. Mik, N. V. Bessonova in Petroleum Chemistry (2023)

  3. No Access

    Article

    Effects of Tar Hydrocracking on Subsequent Carbonization

    The study investigated thermal carbonization of oil tar in comparison with tar carbonization over a Ni/Sibunit catalyst at 450–600°C. The addition of Ni/Sibunit to the tar slightly enhanced the yield of coke. ...

    V. V. Chesnokov, P. P. Dik, A. S. Chichkan, V. N. Parmon in Petroleum Chemistry (2022)

  4. No Access

    Article

    Conversion of Oil Shale Hydroconversion Products in the Presence of Supported Nickel–Molybdenum Sulfide Catalysts

    The conversion of oil shale (OS) in a hydrogen medium at a pressure of 6.0 MPa and a temperature of 400°C with the subsequent refining of the resulting products in the presence of NiMo sulfide catalysts suppor...

    P. P. Dik, M. O. Kazakov, A. V. Saiko, O. V. Klimov, V. Yu. Pereyma in Petroleum Chemistry (2020)

  5. No Access

    Article

    Hydrogenation of Bituminous Sand

    The effect of the conditions of bituminous sand hydrogenation on the yields and properties of the resulting liquid hydrocarbons was studied. It was found that, on the hydrogenation of bituminous sand, hydrocar...

    M. O. Kazakov, P. P. Dik, O. V. Klimov, O. O. Mironenko in Solid Fuel Chemistry (2018)

  6. No Access

    Article

    Influence of Temperature on the Hydrogenation of Oil Shale from the Kashpir Deposit

    The effect of the hydrogenation temperature of oil shale from the Kashpir deposit on the yield and the properties of the resulting liquid hydrocarbons and gasoline and diesel fractions separated from them was ...

    M. O. Kazakov, P. P. Dik, O. V. Klimov, A. V. Shaverina in Solid Fuel Chemistry (2018)

  7. No Access

    Article

    Hydrocracking of Vacuum Gasoil on NiMoW/AAS-Al2O3 Trimetallic Catalysts: Effect of the W : Mo Ratio

    The effect of the W: (W + Mo) atomic ratio in NiMoW trimetallic catalysts on their catalytic and physicochemical properties is studied. The catalysts are prepared by impregnating a carrier containing amorphous...

    P. P. Dik, V. Yu. Pereima, K. A. Nadeina, M. O. Kazakov in Catalysis in Industry (2018)

  8. Chapter and Conference Paper

    NiMo/USY-Alumina Catalysts with Different Zeolite Content for Vacuum Gas Oil Hydrocracking Over Stacked Beds

    The stacked beds comprising hydrotreating catalyst as the top layer, hydrocracking catalyst based on amorphous silica-alumina as the interlayer and hydrocracking catalyst based on USY zeolite as the bottom lay...

    P. P. Dik, V. P. Doronin, E. Yu. Gerasimov in Proceedings of the Scientific-Practical Co… (2018)

  9. No Access

    Article

    Hydrocracking of Vacuum Gasoil on NiMo/AAS-Al2O3 Catalysts Prepared from Citric Acid: Effect of the Catalyst Heat Treatment Temperature

    Ni-Mo bimetallic catalysts are prepared by impregnating a carrier containing amorphous aluminosilicate (AAS) and aluminum oxide using a solution with Ni, Mo, and citric acid. The temperature of the catalysts r...

    P. P. Dik, K. A. Nadeina, M. O. Kazakov, O. V. Klimov in Catalysis in Industry (2018)

  10. No Access

    Article

    Hydroconversion of Oil Shale on Natural Mineral Matrices

    The hydroconversion of high-sulfur oil shale in the presence of natural mineral matrices: shale ash, sandstone, and clay has been investigated. It has been shown that mineral matrices containing clays and iron...

    M. O. Kazakov, O. V. Klimov, P. P. Dik, A. V. Shaverina in Petroleum Chemistry (2017)

  11. No Access

    Article

    Influence of the conditions of hydrogenation treatment of black oil on the yield and properties of the products obtained

    The conversion of black oil in hydrogen (hydroconversion) and nitrogen (pyrolysis) media was studied. The influence of the hydrogen pressure and temperature of the hydrotreating of black oil on the yield and p...

    M. O. Kazakov, P. P. Dik, O. V. Klimov in Russian Journal of Applied Chemistry (2016)

  12. No Access

    Article

    Hydrocracking of vacuum gas oil in the presence of catalysts NiMo/Al2O3–amorphous aluminosilicates and NiW/Al2O3–amorphous aluminosilicates

    Supported nickel–molybdenum and nickel–tungsten hydrocracking catalysts prepared using a support that consists of 70% Al2O3 and 30% amorphous aluminosilicate were characterized by nitrogen and mercury porosimetry...

    V. Yu. Pereyma, P. P. Dik, O. V. Klimov in Russian Journal of Applied Chemistry (2015)

  13. No Access

    Article

    A new catalyst for the deep hydrotreatment of vacuum gas oil, a catalytic cracking feedstock

    A new CoNiMo/Al2O3 deep vacuum gas oil hydrotreatment catalyst designed for the production of catalytic cracking feedstocks containing 200–500 ppm of sulfur is developed. The method for its preparation includes t...

    O. V. Klimov, G. I. Koryakina, E. Yu. Gerasimov, P. P. Dik in Catalysis in Industry (2015)

  14. No Access

    Article

    Vacuum gasoil hydrocracking over three-layered packages consisting of supported sulfide NiMo and NiW catalysts

    A method for vacuum gas oil hydrocracking using a three-layered package of catalysts is proposed, in which the top layer is NiMo/Al2O3, the middle is NiM/AAS-Al2O3 and the bottom is NiM/Y-Al2O3, where M is molybd...

    P. P. Dik, V. Yu. Pereyma, O. V. Klimov, G. I. Koryakina in Catalysis in Industry (2014)

  15. No Access

    Article

    Silica-alumina based nickel-molybdenum catalysts for vacuum gas oil hydrocracking aimed at a higher diesel fraction yield

    Nickel-molybdenum hydrocracking catalysts based on amorphous silica-aluminas (ASAs) with Si/Al = 0.3–1.5 have been prepared using chemicals and methods available for catalyst plants. The acidic properties of t...

    P. P. Dik, O. V. Klimov, S. V. Budukva, K. A. Leonova in Catalysis in Industry (2014)

  16. No Access

    Article

    Textural characteristics of sulphided hydrotreatment catalysts prepared using Co–Mo complex compounds

    Sulphided Co–Mo catalysts prepared by supporting (CoL)2[Mo4(C6H5O7)2O11xH2O on γ-Al2O3 were studied. Pores with diameters less than 40 Å in the catalysts preliminary dried at 120 °C were observed. The volume of...

    K. A. Leonova, O. V. Klimov, E. Yu. Gerasimov, P. P. Dik, V. Yu. Pereyma in Adsorption (2013)

  17. No Access

    Article

    Synthesis of carbon nanostructures on nickel catalysts from liquid hydrocarbons under conventional and microwave heating

    E. I. Udalov, V. V. Chesnokov, P. P. Dik, Yu. Yu. Tanashev in Doklady Physical Chemistry (2010)