Abstract
A scheme for the combined processing of coal to produce synthetic jet fuel is proposed and experimentally verified. It has been established that using an approach including coal coking followed by gasification, Fischer–Tropsch synthesis, and hydroisomerization, the resulting kerosene fractions are characterized by low density values (0.741–0.751 kg/dm3 at 20°С) relative to the level specified by the technical requirements for Jet A-1 and T-8B jet fuel brands used today. With the use of the hydroisomerization process (Т = 330–345°С, pH2 = 72 bar) in the presence of a 2% Pt/Al-HMS (10) catalyst, it has been possible to obtain an isoparaffin fraction with the crystallization temperature below −56°С. The coal tar produced by coking of coal was subjected to deep hydrogenation to obtain a naphthenic jet fuel component characterized by the boiling range of 150–250°С, a density of about 0.873 kg/dm3 (20°С), and low sulfur and aromatics contents (3 ppm and 23 wt %, respectively). By compounding the isoparaffin and naphthenic fractions produced, experimental samples of synthetic jet fuels have been obtained that meet the technical requirements for Jet A-1 and T-8B fuels.
Similar content being viewed by others
REFERENCES
Aircraft Commerce IV–V (N75), 21 (2011).
R. H. Williams, E. D. Larson, L. Guangjian, and T. G. Kreutz, Energy Procedia 1, 4379 (2009).
M. Hook and K. Aleklett, Int. J. Energy Res. 34, 848 (2010).
A. S. Maloletnev and M. Ya. Shpirt, Ross. Khim. Zh. (Zh. Ross. Khim. Ob-va Im. D.I. Mendeleeva) 52 (6), 44 (2008).
I. Mochida, O. Okuma, and S.-H. Yoon, Chem. Rev. 114, 1637 (2014).
Chemical Technology of Solid Fossil Fuels, Ed. by G. N. Makarov and G. D. Kharlampovich (Khimiya, Moscow, 1986) [in Russian].
S. Choudhary, A. Thakur, A. Gupta, and S. B. Ambekar, Int. Res. J. Eng. Technol. 3, 2704 (2016).
M. Sadeqzadeh, in Proceedings of the World Congress on Engineering and Computer Science 2008 (WCECS 2008), October 22–24, San Francisco (2008).
G. I. Zorina and A. R. Brun-Tsekhovoi, Current State of the Coal Gasification Technology Abroad (TsNIITEneftekhim, Moscow, 1986) [in Russian].
L. M. Balster, E. Corporan, M. J. DeWitt, et al., Fuel Process. Technol. 89, 364 (2008).
K. Tao, H. Wang, H. He, et al., Fuel 90, 3404 (2011).
L. S. Yanovskii, E. P. Fedorov, N. I. Varlamova, et al., Dvigatel’ 80, 6 (2012).
E. P. Fedorov, N. I. Varlamova, L. S. Yanovskii, and I. M. Popov, Dvigatel’ 102, 8, (2015).
S. V. Lysenko, A. B. Kulikov, M. I. Onishchenko, et al., Moscow Univ. Chem. Bull. 71, 37 (2016).
M. V. Kulikova, O. S. Dement’eva, A. E. Kuz’min, and M. V. Chudakova, Pet. Chem. 56, 1140 (2016).
A. E. Kuz’min, M. V. Kulikova, and O. S. Dement’eva, Pet. Chem. 58, 557 (2018).
N. N. Mishin, A. B. Kulikov, and A. L. Maksimov, Pet. Chem. 54, 366 (2014).
Funding
This work was carried out as part of the state assignment of the Topchiev Institute of Petrochemical Synthesis of the Russian Academy of Sciences.
Author information
Authors and Affiliations
Corresponding author
Ethics declarations
One of the authors, A. Maksimov, is the editor-in-chief of the Petroleum Chemistry journal. Other authors declare that there is no conflict of interest requiring disclosure in this article.
Additional information
Translated by S. Zatonsky
Rights and permissions
About this article
Cite this article
Yanovskii, L.S., Varlamova, N.I., Popov, I.M. et al. Manufacturing of Coal-Based Synthetic Jet Fuels Interchangeable with JET A-1 and T-8B Petroleum Fuels. Pet. Chem. 60, 92–103 (2020). https://doi.org/10.1134/S0965544120010168
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1134/S0965544120010168