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Removal of bicyclic aromatic hydrocarbons in hydrorefining reaction-fuel fractions


  1. 1.

    Hydrorefining of the 130–215‡ aviation kerosene fraction into which 3% naphthalene by wt. has been introduced over aluminum-cobalt-molybdenum catalyst has been studied.

  2. 2.

    It has been shown that at 275–300 ‡C the degree of naphthalene hydrogenation is 85-75%; thereupon the desulfurization of the raw material takes place to the extent of 69–84%.

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Literature cited

  1. 1.

    Ya. M. Paushkin, The Chemistry of Reaction Fuels [in Russian], Izd. Akad. Nauk SSSR (1962), pp. 158–163.

  2. 2.

    Ya. B. Chertkov, Present-Day and Prospective Hydrocarbon Reaction and Diesel Fuels [in Russian], Izd. Khimiya (1968), pp. 26–33.

  3. 3.

    A. A. Krichko, D. V. Skvortsov, G. A. Titova, B. S. Filippov, and I. E. Dogadkina, Khim. i Tekhnol. Topliv i Masel, No. 1 (1969).

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    A. D. Gulli and P. Uillen, Newest Developments in Petrochemistry and Petroleum Refining [in Russian], Vols. VII–VIII, Izd. Khimiya (1968), p. 206.

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    A. S. éigenson, A. A. Krichko, B. L. Kozik, S. V. Pestrikov, S. R. Mamina, Yu. F. Sokov, Z. D. Putilova, and V. V. Fryazinov, Khim. i Tekhnol. Topliv i Masel, No. 11 (1966).

  6. 6.

    Yu. E. Smol'nik, A. S. Zhurba, G. I. Cherednichenko, and N. G. Yampol'skii, Hydrocatalytic Improvement of Light Petroleum Products from Eastern Ukrainian Petroleums [in Russian], UkrNIINTI, Kiev (1969), p. 55.

  7. 7.

    E. S. Churshukov and A. I. Stekhun, Neftekhimiya i Neftepererabotka, No. 5 (1970).

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Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 6, pp. 5–6, June, 1972.

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Zhurba, A.S., Smol'nik, Y.E., Katrush, R.V. et al. Removal of bicyclic aromatic hydrocarbons in hydrorefining reaction-fuel fractions. Chem Technol Fuels Oils 8, 402–403 (1972).

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  • Hydrogenation
  • Hydrocarbon
  • Naphthalene
  • Aromatic Hydrocarbon
  • Kerosene