Conversion of aromatic complex bottoms to useful products in an integrated refinery process

Patent metadata

Field	Value
Publication number	US-11613714-B2
Application number	US-202117147784-A
Country	US
Kind code	B2
Filing date	Jan 13, 2021
Priority date	Jan 13, 2021
Publication date	Mar 28, 2023
Grant date	Mar 28, 2023

Abstract

Systems and integrated methods are disclosed for processing aromatic complex bottoms into high value products. The system includes an adsorption column, the adsorption column in fluid communication with an aromatics complex and operable to receive and remove polyaromatics from an aromatic bottoms stream. The adsorption column producing a cleaned aromatic bottoms stream with reduced polyaromatic content and a reject stream including the removed polyaromatics. In some embodiments, the reject stream is recycled for further processing, passed to a coke production unit to produce high quality coke, or both.

First claim

What is claimed is:

1. A system for processing aromatic complex bottoms into high value products, the system comprising:
an inlet stream comprising crude oil;
an atmospheric distillation unit (ADU), the ADU in fluid communication with the inlet stream, and operable to separate the inlet stream into an ADU tops stream and an ADU middle stream, the ADU tops stream comprising naphtha, and ADU middle stream comprising diesel;
a naphtha hydrotreating unit (NHT), the NHT in fluid communication with the ADU and operable to treat with hydrogen the naphtha in the ADU tops stream;
a naphtha reforming unit (NREF), the NREF in fluid communication with the NHT and operable to reform a hydrotreated naphtha stream produced by the NHT, and the NREF, further operable to produce separate hydrogen and reformate streams;
an aromatics complex (ARC), the ARC in fluid communication with the NREF and operable to receive the reformate stream produced by the NREF, and the ARC further operable to separate the reformate stream into a gasoline pool stream, an aromatics stream, and an aromatic bottoms stream;
an adsorption column, the adsorption column in fluid communication with the ARC and operable to receive the aromatic bottoms stream produced by the ARC, and the adsorption column further operable to remove polyaromatics from the aromatic bottoms stream to produce a cleaned aromatics bottoms stream with reduced polyaromatic content and a reject stream comprising the removed polyaromatics; and
a coke production unit (CPU), the CPU in fluid communication with the adsorption column and operable to receive at least a portion of the reject stream produced by the adsorption column, and the CPU further operable to produce high quality coke from the reject stream.

2. The system of claim 1 , wherein the system further comprises a diesel hydrotreating unit (DHT), the DHT in fluid communication with a diesel inlet stream, the diesel inlet stream comprising fluid flow from the ADU middle stream, and the DHT operable to treat the diesel inlet stream with hydrogen.

3. The system of claim 2 , wherein the reject stream is in fluid communication with the diesel inlet stream such that the diesel inlet stream comprises fluid flow from the reject stream in combination with the fluid flow from the ADU middle stream.

4. The system of claim 1 , wherein the reject stream is in fluid communication with the ADU such that at least a portion of the reject stream may be recycled back to the ADU.

5. The system according to claim 1 , wherein the aromatic bottoms stream comprises aromatic compounds with boiling points in the range of about 100° C. to about 350° C.

6. The system according to claim 1 , wherein the cleaned aromatic bottoms stream is used as a gasoline blending component without any further treatment.

7. The system according to claim 1 , wherein the cleaned aromatic bottoms stream is processed further to produce benzene, toluene, and xylenes.

8. The system according to claim 1 , wherein the high quality coke comprises needle or graphite quality coke.

9. The system according to claim 1 , wherein the system further comprises a hydrodearylation system, the hydrodearylation system intermediately positioned in fluid communication between the ARC and the adsorption column and operable to receive and process the aromatic bottoms stream for provision as a hydrodearylated effluent stream to the adsorption column.

10. The system according to claim 1 , wherein the system further comprises a fluidized catalytic cracking unit, the fluidized catalytic cracking unit intermediately positioned in fluid communication between the ARC and the adsorption column and operable to receive and process the aromatic bottoms stream for provision as a catalytic cracking products stream to the adsorption column.

11. The system according to claim 1 , wherein the system further comprises a hydrogenation reactor, the hydrogenation reactor intermediately positioned in fluid communication between the ARC and the adsorption column and operable to receive and process the aromatic bottoms stream for provision as a hydrogenated effluent stream to the adsorption column.

12. The system according to claim 1 , wherein the system further comprises a hydrocracking reactor, the hydrocracking reactor intermediately positioned in fluid communication between the ARC and the adsorption column and operable to receive and process the aromatic bottoms stream for provision as a hydrocracked effluent stream to the adsorption column.

13. The system according to claim 1 , wherein the ARC comprises a transalkylation unit.

14. The system according to claim 1 , wherein the adsorption column comprises a zeolite-based adsorbent.

15. The system according to claim 14 , wherein the zeolite-based adsorbent is selected from FAU, BEA, MOR, and MFI framework zeolites.

16. The system according to claim 1 , wherein the adsorption column comprises an activated carbon based adsorbent.

Assignees

• Saudi Arabian Oil Co

Inventors

• Koseoglu Omer Refa
• Hodgkins Robert Peter

Classifications

• C10G11/18

  according to the "fluidised-bed" technique · CPC title

• C10G69/10 Primary

  hydrocracking of higher boiling fractions into naphtha and reforming the naphtha obtained · CPC title

• C10G45/02

  to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing · CPC title

• B01D15/424

  Elution mode · CPC title

• C10G25/03

  with crystalline alumino-silicates, e.g. molecular sieves · CPC title