HYDROCRACKING OF VACUUM DISTILLATE AND LUBRICANT BASE STOCK PRODUCTION
DOI:
https://doi.org/10.29017/SCOG.7.1.1166Keywords:
Hydrocracking, Vacuum Distillate, LubricantAbstract
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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