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Removal of bicyclic aromatic hydrocarbons in hydrorefining reaction-fuel fractions

Conclusions

  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).

  4. 4.

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

  5. 5.

    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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Additional information

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). https://doi.org/10.1007/BF00719484

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Keywords

  • Hydrogenation
  • Hydrocarbon
  • Naphthalene
  • Aromatic Hydrocarbon
  • Kerosene