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Manufacturing costs of gas turbine fuels

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Chemistry and Technology of Fuels and Oils Aims and scope

Conclusions

Technical and economic calculations have shown:

  1. 1)

    The manufacturing cost of GTF from coking distillates is lower than from diesel fuel fractions by 20% (unfinished) or 50% (hydrofinished).

  2. 2)

    The manufacturing cost of GTF from thermal cracking distillates is the same as from the unfinished diesel fuel fraction and 1.3 times lower than from the hydrofinished diesel fuel fraction.

  3. 3)

    The manufacturing cost of GTF from residual products, because of the necessity of a separation stage, is 40–60% greater than the cost of fuels from coking distillates.

  4. 4)

    It is possible to reduce significantly the cost of GTF from residual products by obtaining them from petroleums subjected to intensive desalination.

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Literature cited

  1. V. G. Nikolaeva, B. F. Korobov, A. Ya. Dukhnina, and O. I. Maslova, Mashgiz (1962), p. 172.

  2. V. G. Nikolaeva, A. Ya. Dukhnina, B. F. Korobov, et al., Khim. i Tekhnol. Topliv i Masel, No. 3 (1962).

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Authors and Affiliations

  1. All-Union Scientific Research Institute for Petroleum Refining, USSR

    V. G. Nikolaeva, S. A. Feigin, B. I. Moloshnikova, A. Ya. Dukhnina, G. I. Levinson & A. A. Perchenko

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  1. V. G. Nikolaeva
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  2. S. A. Feigin
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  3. B. I. Moloshnikova
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  4. A. Ya. Dukhnina
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  5. G. I. Levinson
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  6. A. A. Perchenko
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Additional information

Translated from Khimlya i Tekhnologiya Topliv i Masel, No. 6, pp. 28–31, June, 1968.

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Nikolaeva, V.G., Feigin, S.A., Moloshnikova, B.I. et al. Manufacturing costs of gas turbine fuels. Chem Technol Fuels Oils 4, 426–429 (1968). https://doi.org/10.1007/BF00718960

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  • DOI: https://doi.org/10.1007/BF00718960

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