HYDROCRACKING OF VACUUM DISTILLATE AND LUBRICANT BASE STOCK PRODUCTION

Authors

  • A.S. Nasution Research and Development Centre for Oil and Gas Technology "LEMIGAS"

DOI:

https://doi.org/10.29017/SCOG.7.1.1166

Keywords:

Hydrocracking, Vacuum Distillate, Lubricant

Abstract

Hydrocracking of vacuum distillate for middle distillate and lubricant base stock production has been carried out with temperature (from 400° to 420°). Hourly Liquid Space Velocity (from 0.422 to 0.88), Pressure (100 kg/cm2) and H2/Hydrocarbon ratio (1000 It/lt), by using a Catatest unit apparatus.

References

Rachman, S, Hendro, P. and Nasution, A.S, Hydroconversion-Study case for Mi- nas Residue, 2nd Annual IPA 1972, Pr.c., vol 1, p.

Nasution, A.S, Hydrocracking of vacuum distillate of Minas waxy residu for lubri- cant base stock and fuel oil production, 4th Annual IPA-1975, Fourth Annual Con- vention Proseeding vol 1, p 145- L91975).

Bennet, R.N, Am. Chem. Soc. New York Meeting, 645-662 (1972).

Wathive, Ch, Oil and Gas Journal, 112 (1969)

Billon, A, Revue IFP-XXIII, 1655 (1967).

Beuther, H, Ind. Chem. Prod. Res Dev., 3, (3), 174 (1964).

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Issue

Vol. 7 No. 1 (1984)

Section

Articles

License

Copyright (c) 1970 SCIENTIFIC CONTRIBUTIONS OIL AND GAS (SCOG)

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