IJAMSC  Vol.3 No.3 , September 2015
Regeneration of Nickel-Molybdenum Catalysts DN-3531 and Criterion 514 Used in Kerosene and Gas Oil Hydrotreating by Supercritical Carbon Dioxide Extraction
ABSTRACT
Results of research of supercritical fluid CO2-regeneration process of Nickel-Molybdenum Catalysts DN-3531 and Criterion 514 are given. Regeneration was carried out with the use of pure supercritical carbon dioxide and mixture of supercritical carbon dioxide and various polar cosolvents. Regeneration process is carried out along isotherms, in the temperature range of 323 - 383 K, at pressures of P = 20 MPa and 30 MPa. Results of surface assessment of the catalyst samples regenerated show high effectiveness of suggested method.

Cite this paper
Jaddoa, A. , Bilalov, T. , Gumerov, F. , Gabitov, F. and Neindre, B. (2015) Regeneration of Nickel-Molybdenum Catalysts DN-3531 and Criterion 514 Used in Kerosene and Gas Oil Hydrotreating by Supercritical Carbon Dioxide Extraction. International Journal of Analytical Mass Spectrometry and Chromatography, 3, 37-46. doi: 10.4236/ijamsc.2015.33005.
References
[1]   Rakhmanov, A. (2009) Technical Regulation . Informal Document No. WP.29-148-1.

[2]   Boreskov, G.K. (1971) Catalysis. Nauka Publisher, Novosibirsk, 267 p.

[3]   Speight, J.G. (2000) The Desulfurization of Heavy Oils and Residua. Marcel Dekker Inc., New York.

[4]   Satterfield, Ch. (1976) Practical Course of Heterogeneous Catalysis. Khimiya Publisher, Moscow, 240 p.

[5]   Kutepov, A.M., Bondareva, T.M. and Berengarten, M.T. (2004) General Chemical Engineering: A Textbook for Technical Colleges. Academkniga Publisher, Moscow, 528 p.

[6]   Mukhlenov, I.P., et al. (1984) General Chemical Technology. Volume 2, Most Important Chemical Production. Vysshaya Shkola Publisher, Moscow, 263 p.

[7]   Parkash, S. (2003) Refining Process Handbook. Elsevier, Amsterdam.

[8]   Gary, J.H., Handwerk, G.E. and Kaiser, M.J. (2007) Petroleum Refining: Technology and Economics. 5th Edition, CRC Press, Boca Raton, 488 p.

[9]   Babich, I.V. and Moulijn, J.A. (2003) Science and Technology of Novel Processes for Deep Desulfurization of Oil Refinery Streams. Fuel, 82, 607-631.
http://dx.doi.org/10.1016/S0016-2361(02)00324-1

[10]   Javadli, R. and de Klerk, A. (2012) Desulfurization of Heavy Oil. Applied Petrochemical Research, 1, 3-19.
http://dx.doi.org/10.1007/s13203-012-0006-6

[11]   Steiner, P. and Blekkan, E.A. (2002) Catalytic Hydrodesulfurization of a Light Gas Oil over a NiMo Catalyst: Kinetics of Selected Sulfur Components. Fuel Processing Technology, 79, 1-12.

[12]   Masagutov, R.M., Morozov, B.F. and Kutepov, B.I. (1987) Regeneration of Catalysts in Oil Refining and Petrochemicals. Chemistry Publisher, Moscow, 144 p.

[13]   Kurganov, V.М., Kushner, V.E. and Agafonov, А.V. (1973) Steam-Air Regeneration of Hydrotreating Catalysts. TsNIITEneftehim Publisher, Moscow, 71 p.

[14]   Krylov, O.V. (2004) Heterogeneous Catalysis: The Manual for Higher Schools. Akademkniga, Moscow, 679 p.

[15]   Bilalov, T.R. and Gumerov, F.M. (2011) The Manufacturing Processes and Catalyst Regeneration/Thermodynamic Basis of Production Processes and Regeneration of Palladium Catalysts Using Supercritical Carbon Dioxide. LAP LAMBERT Academic Publishing GmbH & Co. KG., Dudweiler Landstr., 153 p.

[16]   Samakhov, А.А., Zaidman, N.M., Chizhik, M.D. and Buyanov, R.А. (1976) Changes of Catalyst Activity during Service. Nauka Publisher, Novosibirsk, 108 p.

[17]   Brunauer, S., Emmett, P.H. and Teller, E. (1938) Adsorption of Gases in Multi Molecular Layers. Journal of the American Chemical Society, 60, 309-319.

[18]   Dimbat, M., Porter, P.E. and Stross F.H. (1956) Apparatus Requirements for Quantitative Applications. Journal of the American Chemical Society, 28, 290-297.

[19]   Gumerov, F.M., Sabirzyanov, A.N. and Gumerova, G.I. (2007) Sub- and Supercritical Fluids in Polymer Processing. Fen Publisher, Kazan, 336 p.

[20]   Bilalov, T.R., Gumerov, F.M., Gabitov, F.R., Kharlampidi, K.E., Fedorov, G.I., Sagdeev, A.A., Yarullin, R.S. and Yakushev, I.A. (2009) The Synthesis and Regeneration of Palladium Catalysts with the Use of Supercritical Carbon Dioxide. Russian Journal of Physical Chemistry B, 3, 80-92.

[21]   Tyapkin, E.V., Sharafutdinov, I.R. and Gumerov, F.M. (2006) Regeneration of PU Brand Palladium Catalyst with the Use of Supercritical Extraction Process. Proceedings of the III International Scientific and Practical Conference “Supercritical Fluid Technologies: The Innovative Potential of Russia”, Rostov, 67-69.

[22]   Galimova, A.T., Sagdeev, A.A. and Gumerov, F.M. (2013) Research of Solubility of Substances Deactivating Catalyst Oxide of Aluminum Possessing Activity in Supercritical Carbon Dioxide. Proceedings of the Higher Educational Institutions, Series of Chemistry and Chemical Engineering, 56, 65-68.

[23]   Knunyants, I.L. (1988) Chemical Encyclopedia. Volume 1, Sovietswkayaenciklopediya Publisher, Moscow, 623 p.

[24]   Sánchez-Delgado, R.A. (2002) Organometallic Modeling of the Hydrodesulfurization and Hydrodenitrogenation Reactions. Springer Science & Business Media, New York, 209 p.

 
 
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