초록

High boiling hydrocarbon materials are hydrocracked in a multiple stage process having ebullating or fixed catalyst bed hydrogenation reactor stages in series. Between the hydrogenation reactors is an interstage feed of 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 a feed portion of said feedstock comprising contacting said feed portion with hydrogen in a first reactor containing a bed of catalyst particles thereby forming an effluent mixture o

1. A method of hydrocracking a high boiling hydrocarbon feedstock comprising the steps of: a. partially hydrocracking a feed portion of said feedstock comprising contacting said feed portion with hydrogen in a first reactor containing a bed of catalyst particles thereby forming an effluent mixture of C4-light ends and lower boiling hydrocarbons and higher boiling hydrocarbons;b. blending an aromatic solvent with said effluent mixture thereby forming a blended effluent mixture, said aromatic solvent comprising from 5 to 10 volume % of the volume of said feed portion;c. further hydrocracking said blended effluent mixture comprising contacting said blended effluent mixture with hydrogen in a second reactor containing a bed of catalyst particles thereby forming a further effluent stream containing additional lower boiling hydrocarbons and the remaining unconverted higher boiling hydrocarbons; andd. separating said further effluent stream into a plurality of hydrocarbon product streams.2. A method as recited in claim 1 wherein said lower boiling hydrocarbons boil below about 650° F. and said higher boiling hydrocarbons boil above about 650° F.3. A method as recited in claim 1 wherein said first and second reactors are ebullating bed reactors.4. A method as recited in claim 1 wherein said first and second reactors are fixed bed reactors.5. A method as recited in claim 1 wherein each of said first and second reactors are selected from fixed bed and ebullating bed reactors.6. A method as recited in claim 1 and further comprising blending a second portion of said feedstock with said effluent mixture to form said blended effluent mixture wherein said second portion of said feedstock comprises from 10 to 20 volume % of said feed portion of said feedstock.