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Priority to KR7401972ApriorityCriticalpatent/KR790000669B1/en
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Production Of Liquid Hydrocarbon Mixture For Refining Petroleum
(AREA)
Abstract
LGP was selectively prepd. from hydrocarbon of b.p.<=315≰C. The hydrocarbon and H2 were contacted with catalyst contg. VIII metal at 21.4-124 atm, 316-454≰C, 1-10LHSV, 890-2670v/v H2 recycle ratio based on fresh feed of H2. The catalyst carrier was prepd. by calcing gel which was prepd. by mixing mordenite in halogenated aluminium sol., and thus homogeneously contained 20-30 wt.% of fine mordenite particle.
KR7401972A1974-03-261974-03-26Hydrocracking process for production of l p g
KR790000669B1
(en)