초록 ▼

A catalytic hydrocracking process which comprises (a) introducing a reduced crude into a fractionation zone to produce a vacuum gas oil stream having a propensity to form polynuclear aromatic compounds in a hydrocracking zone and a slop wax stream; (b) contacting the vacuum gas oil stream in a hydro

A catalytic hydrocracking process which comprises (a) introducing a reduced crude into a fractionation zone to produce a vacuum gas oil stream having a propensity to form polynuclear aromatic compounds in a hydrocracking zone and a slop wax stream; (b) contacting the vacuum gas oil stream in a hydrocracking zone with added hydrogen and a metal promoted hydrocracking catalyst at elevated temperature and pressure sufficient to gain a substantial conversion to lower boiling products; (c) partially condensing the hydrocarbon effluent from the hydrocracking zone and separating the same into a low boiling hydrocarbon product stream and an unconverted hydrocarbon stream boiling above about 650°F. (343°C.) and containing trace quantities of polynuclear aromatic compounds; and (d) introducing at least a portion of the unconverted hydrocarbon stream containing polynuclear aromatic compounds into the fractionation zone thereby recovering a substantial portion of the polynuclear aromatic compounds in the slop wax stream which significantly minimizes the introduction of the polynuclear aromatic compounds into the hydrocracking zone.

대표청구항 ▼

A catalytic hydrocracking process which comprises: (a) introducing a reduced crude into a fractionation zone to produce a vacuum gas oil stream having a propensity to form polynuclear aromatic compounds in a hydrocracking zone and a slop wax stream; (b) contacting said vacuum gas oil stream in a hyd

A catalytic hydrocracking process which comprises: (a) introducing a reduced crude into a fractionation zone to produce a vacuum gas oil stream having a propensity to form polynuclear aromatic compounds in a hydrocracking zone and a slop wax stream; (b) contacting said vacuum gas oil stream in a hydrocracking zone with added hydrogen and a metal promoted hydrocracking catalyst at elevated temperature and pressure sufficient to gain a substantial conversion to lower boiling products; (c) partially condensing the hydrocarbon effluent from said hydrocracking zone and separating the same into a low boiling hydrocarbon product stream and an unconverted hydrocarbon stream boiling above about 650°F. (343°C.) and containing trace quantities of polynuclear aromatic compounds; and (d) introducing at least a portion of said unconverted hydrocarbon stream containing polynuclear aromatic compounds into said fractionation zone thereby recovering a substantial portion of said polynuclear aromatic compounds in said slop wax stream which significantly minimizes the introduction of said polynuclear aromatic compounds into said hydrocracking zone.