PROCESS AND APPARATUS FOR RECOVERING HYDROPROCESSED HYDROCARBONS WITH SINGLE PRODUCT FRACTIONATION COLUMN

• US 20140262946A1
• Filed: 03/15/2013
• Published: 09/18/2014
• Est. Priority Date: 03/15/2013
• Status: Active Grant

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Zhu, Xin X., Bowman, David M., Kapil, Anubhav, Van Wees, Mark
• Granted Patent: US 9,150,797 B2
• Time in Patent Office: Days
• US Class Current: 208/100
• CPC Class Codes: C10G 2400/04 Diesel oil
• CPC Class Codes: C10G 47/02 characterised by the catalyst used
• CPC Class Codes: C10G 47/26 suspended in the oil, e.g. slurries
• CPC Class Codes: C10G 49/22 Separation of effluents
• CPC Class Codes: C10G 7/00 Distillation of hydrocarbon oils

Abstract

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.

Claims

1. A hydroprocessing process comprising:

hydroprocessing a hydrocarbon feed stream in a hydroprocessing reactor to provide hydroprocessing effluent stream;

stripping a hydroprocessing effluent stream in a stripper column;

providing a cold stripped stream and a hot stripped stream;

fractionating the hot stripped stream in 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 directly to 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 1 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 and a hot stripped stream;

fractionating the hot 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.