Catalyst agglomeration remediation

Patent metadata

Field	Value
Publication number	US-9623392-B2
Application number	US-201514642204-A
Country	US
Kind code	B2
Filing date	Mar 9, 2015
Priority date	Mar 9, 2015
Publication date	Apr 18, 2017
Grant date	Apr 18, 2017

Abstract

A process may include shutting down a reactor in which ethylbenzene is undergoing dehydrogenation to styrene in the presence of steam and a catalyst adapted to catalyze dehydrogenation of ethylbenzene to styrene. Shutting down the reactor may include reducing a temperature of the reactor. Shutting down the reactor may include supplying a purge stream to the reactor. Supplying a purge stream may include increasing a steam-to-ethylbenzene molar ratio of an input stream to the reactor. Supplying a purge stream may include supplying steam and one or more of H 2 , CO 2 , and styrene to the reactor. The process may include stopping supply of the purge stream to the reactor and supplying an inert gas purge stream to the reactor. Shutting down the reactor may be performed without use of a steam-only purge stream.

First claim

What is claimed is:

1. A process comprising:
shutting down a reactor wherein ethylbenzene is undergoing dehydrogenation to styrene in the presence of steam and a catalyst adapted to catalyze dehydrogenation of ethylbenzene to styrene, wherein shutting down the reactor comprises:
reducing a temperature of the reactor;
increasing a steam-to-ethylbenzene molar ratio of an input stream to the reactor to form a purge stream; and
supplying the purge stream to the reactor.

2. The process of claim 1 , wherein shutting down the reactor is performed without use of a steam-only purge stream.

3. The process of claim 1 , further comprising, after supplying the purge stream to the reactor, further reducing the temperature of the reactor.

4. The process of claim 3 , further comprising continuing to supply the purge stream to the reactor while further reducing the temperature of the reactor.

5. The process of claim 3 , further comprising stopping supply of the purge stream to the reactor before further reducing the temperature of the reactor.

6. The process of claim 3 , further comprising stopping supply of the purge stream to the reactor and supplying an inert gas purge stream to the reactor.

7. The process of claim 6 , further comprising, after supplying the inert gas purge stream to the reactor, further reducing the temperature of the reactor.

8. The process of claim 1 , further comprising stopping introduction of ethylbenzene to the reactor to form a steam-only purge stream, and supplying the steam-only purge stream to the reactor.

9. The process of claim 8 , wherein the temperature of the reactor is further reduced after supplying the steam-only purge stream to the reactor.

10. The process of claim 1 , wherein the purge stream has a steam-to-ethylbenzene molar ratio of from 12:1 to 50:1.

11. The process of claim 1 , wherein the temperature of the reactor is reduced to range from less than 650° C. to 360° C.

12. The process of claim 1 , wherein the steam-to-ethylbenzene molar ratio of the purge stream is continuously maintained at from 12:1 to 50:1 while the temperature of the reactor is within the range of 550° C. to 450° C. during the shutting down of the reactor.

13. The process of claim 1 , wherein the catalyst comprises potassium promoted iron oxide.

14. The process of claim 1 , wherein, after shutting down the reactor, the catalyst or agglomerated catalyst particles thereof exhibits an average crush strength that is lower than an average crush strength exhibited by the catalyst prior to shutting down the reactor.

15. The process of claim 1 , wherein the steam-to-ethylbenzene molar ratio of the purge stream is continuously maintained at from 12:1 to 50:1 from the time at which the purge stream is introduced into the reactor until the purge stream is replaced with an inert gas purge stream.

16. A process comprising:
shutting down a reactor wherein ethylbenzene is undergoing dehydrogenation to styrene in the presence of a catalyst adapted to catalyze dehydrogenation of ethylbenzene to styrene, wherein the catalyst comprises potassium, wherein shutting down the reactor comprises:
reducing a temperature of the reactor;
increasing a steam-to-ethylbenzene molar ratio of an input stream to the reactor to form a purge stream;
supplying the purge stream to the reactor; and
stopping supply of the purge stream to the reactor and supplying an inert gas purge stream to the reactor, wherein shutting down the reactor is performed without use of a steam-only purge stream.

17. A process comprising:
shutting down a reactor wherein ethylbenzene is undergoing dehydrogenation to styrene in the presence of a catalyst adapted to catalyze dehydrogenation of ethylbenzene to styrene, wherein shutting down the reactor comprises:
reducing a temperature of the reactor; and
supplying a purge stream to the reactor comprising steam, wherein the purge stream further comprises H 2 , CO 2 , styrene, or combinations thereof.

18. The process of claim 17 , wherein the purge stream further comprises H 2 .

19. The process of claim 17 , wherein the purge stream further comprises CO 2 .

20. The process of claim 17 , wherein the purge stream further comprises styrene.

Assignees

• Fina Technology

Inventors

• Pelati Joseph E

Classifications

• C07C2523/04

  Alkali metals · CPC title

• C07C5/333

  Catalytic processes · CPC title

• B01J2208/00681

  Agglomeration · CPC title

• B01J2208/00637

  Means for stopping or slowing down the reaction · CPC title

• B01J8/062

  being installed in a furnace · CPC title