초록 ▼

High boiling hydrocarbon materials are hydrocracked in a multiple stage process having ebullating catalyst bed hydrogenation reactor stages in series. Between the hydrogenation reactors is an interstage separator/stripper to separate a vapor phase and to strip the liquid phase with hydrogen to produ

High boiling hydrocarbon materials are hydrocracked in a multiple stage process having ebullating catalyst bed hydrogenation reactor stages in series. Between the hydrogenation reactors is an interstage separator/stripper to separate a vapor phase and to strip the liquid phase with hydrogen to produce a heavier, more concentrated liquid phase as the feed to the next ebullating bed reactor stage in the series. The feed to the second stage may be blended with an aromatic solvent and/or a portion of the high boiling hydrocarbon feedstock.

대표청구항 ▼

1. A method of hydrocracking a high boiling hydrocarbon feedstock comprising the steps of:a. partially hydrocracking said feedstock comprising contacting said feedstock with hydrogen in a first reactor containing an ebullating bed of catalyst particles thereby forming an effluent mixture of C4-light

1. A method of hydrocracking a high boiling hydrocarbon feedstock comprising the steps of:a. partially hydrocracking said feedstock comprising contacting said feedstock with hydrogen in a first reactor containing an ebullating bed of catalyst particles thereby forming an effluent mixture of C4-light ends and lower boiling hydrocarbons and higher boiling hydrocarbons; b. passing said partially hydrocracked effluent mixture from said first reactor into a separation/stripping zone at a pressure in the range of 1500 to 3000 psig and separating therein said partially hydrocracked effluent mixture into a vapor portion containing C4-light ends and lower boiling hydrocarbons and a liquid portion containing higher boiling hydrocarbons and concurrently stripping therein said higher boiling liquid portion with hydrogen to separate an additional vapor portion containing additional C4-light ends and lower boiling hydrocarbons and produce a combined vapor stream containing said vapor portion and said additional vapor portion and produce a stripped liquid stream containing more concentrated higher boiling hydrocarbons; c. further hydrocracking said stripped liquid stream comprising contacting said stripped liquid stream with hydrogen in a second reactor containing an ebullating bed of catalyst particles thereby forming a further effluent stream containing additional lower boiling hydrocarbons and the remaining unconverted higher boiling hydrocarbons; d. combining said combined vapor stream from step b and said further effluent stream from step c; and e. separating said combined streams from step d into a plurality of hydrocarbon product streams.