Xylene separation process

Patent metadata

Field	Value
Publication number	US-10093598-B2
Application number	US-201515548072-A
Country	US
Kind code	B2
Filing date	Dec 28, 2015
Priority date	Feb 19, 2015
Publication date	Oct 9, 2018
Grant date	Oct 9, 2018

Abstract

A process is described for separating paraxylene from a multicomponent fluid mixture of C8 aromatics. A mixture of C8 aromatics is fed to a simulated moving-bed adsorptive apparatus. The location of the feed to the apparatus is moved at set intervals. The rate of flow of feed to the apparatus is varied during each interval to enhance the separation of paraxylene from the multicomponent mixture.

First claim

What is claimed is:

1. A process for separating at least one C8 aromatic from a mixture of at least two C8 aromatics by simulated moving-bed adsorptive separation, said process comprising the steps of:
(a) introducing a feed stream, which comprises at least two C8 aromatics, into a simulated moving-bed adsorptive apparatus, wherein said simulated moving-bed adsorptive apparatus comprises multiple beds containing adsorbent material;
(b) introducing a desorbent stream, which comprises desorbent, into the simulated moving-bed adsorptive apparatus;
(c) withdrawing an extract stream, which comprises desorbent and at least one C8 aromatic, from the simulated moving-bed adsorptive apparatus;
(d) withdrawing at least one raffinate stream, which comprises at least one C8 aromatic, which is different from the C8 aromatic in the extract stream of step (c), from the simulated moving-bed adsorptive apparatus;
(e) maintaining a flow of circulating fluid throughout the simulated moving-bed adsorptive apparatus; and
(f) switching the flow of streams into and out of the simulated moving-bed adsorptive apparatus to a bed downstream in terms of the direction of the circulating fluid at set time interval X,
wherein the rate flow of feed introduced in step (a) is varied during time interval X.

2. The process of claim 1 , wherein the mixture of at least two C8 aromatics comprises paraxylene, orthoxylene, metaxylene and ethylbenzene, and
wherein the extract stream of step (c) comprises paraxylene.

3. The process of claim 1 , wherein the mixture of at least two C8 aromatics comprises orthoxylene, metaxylene and ethylbenzene, and
wherein the extract stream of step (c) comprises ethylbenzene.

4. The process of claim 2 , wherein a single raffinate stream is withdrawn from the simulated moving-bed adsorptive apparatus.

5. The process of claim 2 , wherein more of the at least one multicomponent feed is introduced into the simulated moving-bed adsorptive apparatus during the latter portion of time interval X than in the earlier portion of time interval X.

6. The process of claim 5 , wherein less than 30% of the at least one multicomponent feed is introduced into the simulated moving-bed adsorptive apparatus during a time subinterval of from 0 to 40% of X,
wherein at least 70% of the at least one multicomponent feed is introduced into the simulated moving-bed adsorptive apparatus during a time subinterval of from 40 to 100% of X.

7. The process of claim 5 , wherein less than 10% of the feed, which is introduced in time interval X, is introduced during a time subinterval of from 0 to 20% of X,
wherein less than 15% of the feed, which is introduced in time interval X, is introduced during a time subinterval of from 20 to 40% of X,
wherein at least 15% of the feed, which is introduced in time interval X, is introduced during a time subinterval of from 40 to 60% of X,
wherein at least 20% of the feed, which is introduced in time interval X, is introduced during a time subinterval of from 60 to 80% of X, and
wherein at least 20% of the feed, which is introduced in time interval X, is introduced during a time subinterval of from 80 to 100% of X.

8. The process of claim 5 , wherein less of the raffinate stream is withdrawn from the simulated moving-bed adsorptive apparatus during the latter portion of time interval X than in the earlier portion of time interval X.

9. The process of claim 8 , wherein at least 60% of the raffinate stream is withdrawn from the simulated moving-bed adsorptive apparatus during a time subinterval of from 0 to 40% of X,
wherein less than 40% of the raffinate stream is withdrawn from the simulated moving-bed adsorptive apparatus during a time subinterval of from 40 to 100% of X.

10. The process of claim 8 , wherein at least 25% of the raffinate stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 0 to 20% of X,
wherein at least 25% of the raffinate stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 20 to 40% of X,
wherein less than 15% of the raffinate stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 40 to 60% of X,
wherein less than 15% of the raffinate stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 60 to 80% of X, and
wherein less than 20% of the raffinate stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 80 to 100% of X.

11. The process of claim 2 , wherein more of the extract stream is withdrawn from the simulated moving-bed adsorptive apparatus during the latter portion of time interval X than in the earlier portion of time interval X.

12. The process of claim 11 , wherein less than 30% of the extract stream is withdrawn from the simulated moving-bed adsorptive apparatus during a time subinterval of from 0 to 40% of X,
wherein at least 70% of the extract stream is withdrawn from the simulated moving-bed adsorptive apparatus during a time subinterval of from 40 to 100% of X.

13. The process of claim 12 , wherein less than 15% of the extract stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 0 to 20% of X,
wherein less than 15% of the extract stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 20 to 40% of X,
wherein at least 15% of the extract stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 40 to 60% of X,
wherein at least 20% of the extract stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 60 to 80% of X, and
wherein at least 20% of the extract stream, which is withdrawn in time interval X, is withdrawn during a time subinterval of from 80 to 100% of X.

14. The process of claim 1 , wherein at least two raffinate streams are withdrawn from the simulated moving-bed adsorptive apparatus,
wherein a first raffinate stream comprises ethylbenzene and desorbent, and
wherein a second raffinate stream comprises orthoxylene, metaxylene and desorbent.

15. The process any one of claim 1 , wherein the at least one multicomponent feed further comprises n-nonane,
wherein three raffinate streams are withdrawn from the simulated moving-bed adsorptive apparatus,
wherein a first raffinate stream comprises ethylbenzene and desorbent,
wherein a second raffinate stream comprises orthoxylene, metaxylene and desorbent, and
wherein a third raffinate stream comprises n-nonane and desorbent.

16. The process of claim 4 , wherein the extract stream from step (c) is passed to a first distillation zone to separate paraxylene from desorbent,
wherein the raffinate stream is passed to a second distillation zone to separate ethylbenzene, orthoxylene and metaxylene from desorbent.

17. The process of claim 14 , wherein the extract stream from step (c) is passed to a first distillation zone to separate paraxylene from desorbent,
wherein the first raffinate stream is passed to a second distillation zone to separate ethylbenzene from desorbent, and
wherein the second raffinate stream is passed to a third distillation zone to separate orthoxylene and metaxylene from desorbent.

18. The process of claim 15 , wherein the extract stream from step (c) is passed to a first distillation zone to separate paraxylene from desorbent,
wherein the first raffinate stream is passed to a second distillation zone to separate ethylbenzene from desorbent,
wherein the second raffinate

Assignees

• Exxonmobil Chemical Patents Inc
• Georgia Tech Res Inst

Inventors

• Ou John D
• Abichandani Jeevan S
• Kawajiri Yoshiaki
• Guo Siwei

Classifications

• C07C7/13

  by molecular-sieve technique · CPC title

• C07C15/073

  Ethylbenzene · CPC title

• C07C15/08 Primary

  Xylenes · CPC title

• C07C7/04

  by distillation · CPC title

• B01D15/1828 Primary

  characterised by process features · CPC title