초록 ▼

A hot stripped hydroprocessed stream from a stripper column may be sent directly to a vacuum fractionation column instead of being first processed in an atmospheric fractionation column. If a separate warm stripper column is used, both the warm stripped stream and a hot stripped stream may be fracti

A hot stripped hydroprocessed stream from a stripper column may be sent directly to a vacuum fractionation column instead of being first processed in an atmospheric fractionation column. If a separate warm stripper column is used, both the warm stripped stream and a hot stripped stream may be fractionated in the same fractionation column, particularly a vacuum fractionation column.

대표청구항 ▼

1. A hydroprocessing process comprising: hydroprocessing a hydrocarbon feed stream in a hydroprocessing reactor to provide a hydroprocessing effluent stream;passing said hydroprocessing effluent stream through a hot separator to provide a hot overhead stream and a separator hot hydroprocessing efflu

1. A hydroprocessing process comprising: hydroprocessing a hydrocarbon feed stream in a hydroprocessing reactor to provide a hydroprocessing effluent stream;passing said hydroprocessing effluent stream through a hot separator to provide a hot overhead stream and a separator hot hydroprocessing effluent stream;passing said hot overhead stream to a warm separator to provide a warm overhead stream and a separator warm hydroprocessing effluent stream;passing said warm overhead stream to a cold separator to provide a separator cold hydroprocessing effluent stream;stripping said separator hot hydroprocessing effluent stream, said separator warm hydroprocessing effluent stream and said separator cold hydroprocessing effluent stream in a stripper column;providing a cold stripped stream and a hot stripped stream; andfractionating the hot stripped stream in a vacuum product fractionation column. 2. The hydroprocessing process of claim 1 further comprising providing said cold stripped stream and said hot stripped stream from the same stripping column. 3. The hydroprocessing process of claim 1 further comprising providing all of said hot stripped stream to the vacuum product fractionation column at below atmospheric pressure. 4. The hydroprocessing process of claim 1 further comprising transporting said hot stripped stream in direct communication with said vacuum fractionation column. 5. The hydroprocessing process of claim 1 further comprising stripping a relatively hot hydroprocessing effluent stream in a hot stripper column to provide said hot stripped stream. 6. The hydroprocessing process of claim 5 further comprising stripping a relatively cold hydroprocessing effluent stream in a cold stripper column to provide said cold stripped stream and recovering the cold stripped stream from a bottom of the cold stripper column as a diesel stream. 7. The hydroprocessing process of claim 6 further comprising fractionating a condensed cold overhead stream in a debutanizer column. 8. The hydroprocessing process of claim 1 further comprising stripping a relatively warm hydroprocessing effluent stream in a warm stripper column to provide a warm stripped stream and fractionating said warm stripped stream in said vacuum fractionation column. 9. The hydroprocessing process of claim 8 further comprising stripping an overhead stream of said hot stripper column in said warm stripper column. 10. The hydroprocessing process of claim 9 further comprising heating said hot stripped stream in a fired heater but not heating said warm stripped stream in a fired heater before fractionating said warm stripped stream and said hot stripped stream. 11. The hydroprocessing process of claim 1 wherein said hydroprocessing reactor is a slurry hydrocracking reactor. 12. A slurry hydrocracking process comprising: slurry hydrocracking a hydrocarbon feed stream in a slurry hydrocracking reactor to provide hydroprocessing effluent stream;stripping a hydroprocessing effluent stream in a stripper column;providing a cold stripped stream, a warm stripped stream and a hot stripped stream;heating said hot stripped stream in a fired heater but not heating said warm stripped stream in a fired heater; andfractionating the hot stripped stream and said warm stripped stream in a vacuum product fractionation column. 13. The slurry hydrocracking process of claim 12 further comprising providing said cold stripped stream and said hot stripped stream from the same stripping column. 14. The slurry hydrocracking process of claim 12 further comprising stripping a relatively warm hydroprocessing effluent stream in a warm stripper column to provide said warm stripped stream and stripping a relatively hot hydroprocessing effluent stream in a hot stripper column to provide said hot stripped stream. 15. The slurry hydrocracking process of claim 14 further comprising fractionating said warm stripped stream and said hot stripped stream in a vacuum fractionation column at below atmospheric pressure. 16. The slurry hydrocracking process of claim 15 further comprising stripping a relatively cold hydroprocessing effluent stream in a cold stripper column to provide said cold stripped stream. 17. The slurry hydrocracking process of claim 16 further comprising recovering the cold stripped stream from a bottom of the cold stripper column as a diesel stream. 18. A slurry hydrocracking process comprising: slurry hydrocracking a hydrocarbon feed stream in a slurry hydrocracking reactor to provide hydroprocessing effluent stream;stripping a relatively cold hydroprocessing effluent stream in a cold stripper column to provide a cold stripped stream;stripping a relatively warm hydroprocessing effluent stream in a warm stripper column to provide a warm stripped stream;stripping a relatively hot hydroprocessing effluent stream in a hot stripper column to provide a hot stripped stream;fractionating said warm stripped stream and said hot stripped stream in the same fractionation column. 19. The slurry hydrocracking process of claim 18 further comprising a cold stripped stream from a bottom of the cold stripper column as a diesel stream. 20. The slurry hydrocracking process of claim 18 further comprising heating said hot stripped stream in a fired heater but not heating said warm stripped stream in a fired heater before fractionating said warm stripped stream and said hot stripped stream.