Selective reforming process to produce gasoline blending components and aromatics

Patent metadata

Field	Value
Publication number	US-11072748-B2
Application number	US-201916707534-A
Country	US
Kind code	B2
Filing date	Dec 9, 2019
Priority date	Dec 9, 2019
Publication date	Jul 27, 2021
Grant date	Jul 27, 2021

Abstract

Improved catalytic reforming processes and systems employ reforming reactors in a more efficient manner and can avoid problems associated with yield loss. Aromatics and isoparaffins are separated prior to passing to a reforming unit. An integrated process for producing gasoline blending components includes: separating a naphtha feedstream into an aromatic-rich stream and an aromatic-lean stream; separating the aromatic-lean stream into an isoparaffin-rich stream and an isoparaffin-lean stream; and catalytically reforming the isoparaffin-lean stream to produce a reformate stream.

First claim

The invention claimed is:

1. An integrated process for producing gasoline blending components comprising:
separating a naphtha feedstream into an aromatic-rich stream and an aromatic-lean stream;
separating the aromatic-lean stream into an isoparaffin-rich stream and an isoparaffin-lean stream; and
catalytically reforming the isoparaffin-lean stream by dehydrogenation of naphthenes to aromatics, isomerization of n-paraffins to iso-paraffins, and dehydrocyclization of paraffins to aromatics, to produce a reformate stream.

2. The process as in claim 1 , further comprising recovering at least a portion of the isoparaffin-rich stream as gasoline blending components.

3. The process as in claim 1 , further comprising recovering at least a portion of the aromatic-rich stream as gasoline blending components.

4. The process as in claim 1 , further comprising passing at least a portion of the aromatic-rich stream to an aromatic complex for recovery of aromatic products.

5. The process as in claim 1 , further comprising recovering at least a portion of the reformate stream as gasoline blending components.

6. The process as in claim 1 , further comprising passing at least a portion of the reformate stream to the step of separating the naphtha feedstream.

7. The process as in claim 1 , further comprising separating at least a portion of the isoparaffin rich stream into a light isoparaffin rich stream and a heavy isoparaffin rich stream, recovering at least a portion of the light isoparaffin rich stream as gasoline blending components, and passing at least a portion of the heavy isoparaffin rich stream to the step of catalytically reforming.

8. The process as in claim 1 , wherein separating the naphtha feedstream into an aromatic-lean fraction and an aromatic-rich fraction comprises:
subjecting the naphtha feedstream and an effective quantity of extraction solvent to an extraction zone to produce an extract containing a major proportion of the aromatic content of the hydrocarbon feed and a portion of the extraction solvent, and a raffinate containing a major proportion of the non-aromatic content of the hydrocarbon feed and a portion of the extraction solvent;
separating at least a substantial portion of the extraction solvent from the raffinate and recovering the aromatic-lean fraction; and
separating at least a substantial portion of the extraction solvent from the extract and recovering the aromatic-rich fraction.

9. The process as in claim 8 , wherein the extraction solvent is selected from the group consisting of furfural, N-methyl-2-pyrrolidone, dimethylformamide, oxidized disulfide oil, dimethylsulfoxide, phenol, nitrobenzene, sulfolanes, acetonitrile, glycols and combinations comprising at least two of the foregoing.

10. The process as in claim 1 , wherein separating the aromatic-lean stream into the isoparaffin-rich stream and the isoparaffin-lean stream comprises adsorbing on an adsorbent material normal paraffin and naphthene compounds from the aromatic-lean stream while rejecting isoparaffin compounds pass with the isoparaffin-rich stream, and desorbing the adsorbent material to recover the iso-paraffin lean stream.

11. An integrated system for producing gasoline blending components comprising:
a first separation zone operable to separate a naphtha feedstream into an aromatic-rich stream and an aromatic-lean stream, the first separation zone comprising one or more feed inlets in fluid communication with a source of the naphtha feedstream, one or more first outlets for discharging the aromatic-rich stream, one or more second outlets for discharging the aromatic-lean stream;
a second separation zone operable to separate the aromatic-lean stream into an isoparaffin-rich stream and an isoparaffin-lean stream, the second separation zone comprising one or more inlets in fluid communication with the second outlet of the first separation zone, one or more first outlets for discharging the isoparaffin-rich stream, and one or more second outlets for discharging the isoparaffin-lean stream; and
a catalytic reforming zone operable to produce a reformate comprising at least one inlet in fluid communication with the second outlet of the second separation zone; and at least one outlet for discharging reformate, said catalytic reforming zone selected from a semi-regenerative unit, a cyclic regeneration unit, and a continuous catalyst regeneration unit.

12. The system as in claim 11 , further comprising a gasoline pool comprising at least one inlet, said at least one inlet of the gasoline pool being in fluid communication with the first outlet of the second separation zone.

13. The system as in claim 11 , further comprising a gasoline pool comprising at least one inlet, said at least one inlet of the gasoline pool being in fluid communication with the first outlet of the first separation zone.

14. The system as in claim 11 , further comprising an aromatic complex comprising at least one inlet in fluid communication with the first outlet of the first separation zone, and at least one outlet for discharging aromatic products.

15. The system as in claim 11 , further comprising a gasoline pool comprising at least one inlet, said at least one inlet of the gasoline pool being in fluid communication with the catalytic reforming zone outlet.

16. The system as in claim 11 , wherein the catalytic reforming zone outlet is in fluid communication with the feed inlet of the first separation zone.

17. The system as in claim 11 , further comprising:
a third separation zone operable to separate the paraffin-rich stream into a light isoparaffin-rich stream and a heavy isoparaffin-rich stream,
the third separation zone comprising one or more inlets in fluid communication with the first outlet of the second separation zone, one or more first outlets for discharging the light isoparaffin-rich stream, and one or more second outlets for discharging the heavy isoparaffin-rich stream; and
wherein the second outlet of the third separation zone is in fluid communication with the catalytic reforming zone inlet.

18. The system as in claim 11 , wherein the first separation zone is selected from the group consisting of mixer-settlers, centrifugal contactors, tray columns, packed bed columns, rotating disc contactors or pulse columns.

19. The system as in claim 11 , wherein the second separation zone comprises an adsorbent treatment zone containing an effective quantity of adsorbent material and operable to selectively adsorb normal paraffin and naphthene compounds from the aromatic-lean stream, wherein rejected isoparaffin compounds are discharged from the first outlet, and wherein paraffin and naphthene compounds are desorbed and discharged from the second outlet.

Assignees

• Saudi Arabian Oil Co

Inventors

• Koseoglu Omer Refa
• Al-Shareef Ali H

Classifications

• C10G2300/1096

  Aromatics or polyaromatics · CPC title

• C10G2400/02

  Gasoline · CPC title

• C10G35/085 Primary

  containing platinum group metals or compounds thereof · CPC title

• C10G21/20

  Nitrogen-containing compounds · CPC title

• C10G21/22

  Compounds containing sulfur, selenium, or tellurium · CPC title