Processes for aromatization of naphtha isoparaffins

Patent metadata

Field	Value
Publication number	US-12264130-B2
Application number	US-202318324257-A
Country	US
Kind code	B2
Filing date	May 26, 2023
Priority date	May 26, 2023
Publication date	Apr 1, 2025
Grant date	Apr 1, 2025

Abstract

A method for upgrading a naphtha feed includes passing the naphtha feed to an adsorption unit to produce at least a paraffin stream and an isoparaffin stream, wherein the isoparaffin stream comprises isoparaffins and aromatics. Passing the isoparaffin stream to an isoparaffin aromatization catalytic unit that contacts the isoparaffin stream with at least one aromatization catalyst produces aromatics from the isoparaffins thereby yielding an aromatization effluent. The at least one aromatization catalyst may comprise ZSM-5 zeolite. Benzene, toluene, and/or xylene (BTX) may be separated from the aromatization effluent by separating the aromatics effluent into a gas stream and a liquid stream in a gas/liquid separator, wherein the liquid stream contains BTX. Passing the liquid stream to a BTX-separation unit may produce a BTX stream and a recycle stream, wherein the BTX stream contains benzene, toluene, and/or xylene.

First claim

What is claimed is:

1. A method for upgrading a naphtha feed, the method comprising:
passing the naphtha feed to an adsorption unit to produce at least a paraffins stream and an isoparaffins stream, wherein the isoparaffin stream comprises isoparaffins and aromatics; and
passing the isoparaffins stream to an isoparaffin aromatization catalytic unit that contacts the isoparaffins stream with at least one aromatization catalyst to produce aromatics from the isoparaffins thereby yielding an aromatization effluent, wherein the at least one aromatization catalyst comprises ZSM-5 zeolite.

2. The method of claim 1 , further comprising separating out an aromatization effluent from the isoparaffins stream in a BTX separation unit, wherein the BTX separation unit is upstream of the isoparaffin aromatization catalytic unit, and wherein the aromatization effluent comprises benzene, toluene, and/or xylene (BTX).

3. The method of claim 2 , wherein BTX is separated from the aromatization effluent by separating the aromatization effluent into a gas stream and a liquid stream in a gas/liquid separation unit, wherein the liquid stream contains benzene, toluene, and/or xylene; and passing the liquid stream back to the BTX separation unit.

4. The method of claim 1 , further comprising passing the isoparaffins stream to a reforming unit to produce a reformate; and passing the reformate to a BTX separation unit.

5. The method of claim 1 , wherein BTX is separated from the aromatization effluent by separating the aromatization effluent into a gas stream and a liquid stream in a gas/liquid separation unit, wherein the liquid stream contains benzene, toluene, and/or xylene; and
passing the liquid stream to a BTX separation unit to produce an aromatics effluent and an unconverted aromatics stream, wherein the aromatics effluent contains benzene, toluene, and/or xylene.

6. The method of claim 5 , further comprising passing the gas stream to a gas separation unit to produce an olefins stream, a byproduct stream, and an aromatic-rich stream.

7. The method of claim 5 , further comprising passing the unconverted aromatics stream back to the adsorption unit.

8. The method of claim 5 , further comprising passing the unconverted aromatics stream to a gasoline pool.

9. The method of claim 1 , further comprising:
passing the paraffin stream to a steam cracking unit to produce an ethylene stream; and
passing the ethylene stream to a gas separation unit.

10. The method of claim 1 , wherein the naphtha feed comprises from 30 weight percent (wt. %) to 60 wt. % isoparaffin based on a total weight of the naphtha feed.

11. The method of claim 1 , wherein the naphtha feed comprises from 20 wt. % to 40 wt. % isoparaffin based on a total weight of the naphtha feed and at least some aromatics.

12. The method of claim 1 , further comprising:
passing the naphtha feed to a splitter unit to produce a low temperature stream and a high temperature stream; and
passing the high temperature stream to the adsorption unit.

13. The method of claim 1 , wherein conversion of isoparaffins in the isoparaffins stream to aromatics is from 40% to 80%.

14. The method of claim 1 , wherein the isoparaffin aromatization catalytic unit operates at a temperature of from 300° C. to 600° C., a pressure of from 1 bar to 30 bar; and liquid hourly space velocity of from 0.2 h −1 to 5 h −1 , wherein the isoparaffin aromatization catalytic unit comprises at least two fixed-bed, swing reactors.

15. The method of claim 1 , wherein the ZSM-5 zeolite has a nano crystal scale between 100 nm and 750 nm.

16. The method of claim 1 , wherein the paraffin stream comprises C 1 -C 11 paraffins.

17. The method of claim 1 , wherein the isoparaffin stream comprises from 0.1 ppm to 2000 ppm of sulfur.

Assignees

• Saudi Arabian Oil Co

Inventors

• Al-Shafei Emad Naji
• Ding Lianhui
• Zhu Guanghui
• Albahar Mohammed Z
• Aljishi Mohammad F
• Alkhunaizi Mohammed A

Classifications

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• C07C5/41

  Catalytic processes · CPC title

• C07C5/393

  with cyclisation to an aromatic six-membered ring, e.g. dehydrogenation of n-hexane to benzene · CPC title

• B01D3/143

  by two or more of a fractionation, separation or rectification step · CPC title

• B01D19/00

  Degasification of liquids · CPC title