Method for removing cobalt deposits in a high-pressure olefin hydroformylation reactor

Patent metadata

Field	Value
Publication number	US-10385422-B2
Application number	US-201414909852-A
Country	US
Kind code	B2
Filing date	Jul 30, 2014
Priority date	Aug 8, 2013
Publication date	Aug 20, 2019
Grant date	Aug 20, 2019

Abstract

Method of removing cobalt deposits in a reactor for the cobalt-catalyzed high-pressure hydroformylation of olefins by treatment with aqueous nitric acid, wherein the reactor is at least partly filled with aqueous nitric acid and the temperature of the aqueous nitric acid is increased during the treatment.

First claim

The invention claimed is:

1. A method of removing cobalt deposits from a reactor, the method comprising; at least partly filling the reactor with aqueous nitric acid, the nitric acid reacting with cobalt present in the reactor to form a nitrogen oxide offgas, and
measuring the nitric acid concentration and/or the cobalt ion concentration of the aqueous nitric acid in the reactor over time, and if a change in the acid concentration, and/or the cobalt ion concentration in the nitric acid, falls below a determined set limit value, the temperature of the aqueous nitric acid in the reactor is increased, wherein the reactor is a high-pressure, olefin hydroformylation reactor.

2. The method according to claim 1 , further comprising combining the nitrogen oxide offgas with a gas that includes molecular oxygen, wherein at least part of the combined offgas is absorbed into an aqueous liquid.

3. The method according to claim 2 , wherein the aqueous liquid is conveyed in countercurrent to the nitrogen oxide offgas in a scrubbing column, and a gas that includes molecular oxygen is combined with the offgas and/or introduced into the scrubbing column.

4. The method according to claim 1 , wherein the partly filling of the reactor includes circulating the aqueous nitric acid in the reactor.

5. The method according to claim 1 , further comprising removing an exhausted aqueous nitric acid from the reactor it the acid concentration drops below a set acid limit value, or the cobalt ion concentration rises above a set cobalt ion limit value.

6. The method according to claim 5 , wherein the set acid limit value is about 25 g HNO 3 per liter.

7. The method according to claim 5 , further comprising recovering the cobalt from the exhausted aqueous nitric acid.

8. The method according to claim 7 , wherein the recovery of the cobalt comprises treating the exhausted aqueous nitric acid with hydroxide and/or oxide anions to form a cobalt salt, which precipitates and separated off, and the cobalt salt is treated with acetic acid.

9. The method according to claim 1 , wherein the increasing of the temperature of the aqueous nitric acid includes removing at least part of the acid from the reactor, heating the removed acid, and returning the heated acid to the reactor.

10. The method according to claim 1 , further comprising cleaning the reactor with water following the treatment with aqueous nitric acid.

11. The method according to claim 1 , wherein the reactor is flushed with water or steam following the treatment with aqueous nitric acid.

12. The method according to claim 1 , wherein the temperature of the aqueous nitric acid is increased from a first temperature in a range from 10 to 40° C. to a final temperature in a range from 60 to 80° C.

13. The method according to claim 12 , wherein the final temperature is from 70 to 80° C.

14. The method according to claim 12 , wherein the final temperature is from 75 to 80° C.

15. The method according to claim 14 , wherein the temperature is increased stepwise by from 10 to 25° C., until the final temperature is reached.

16. The method according to claim 12 , wherein the temperature is increased stepwise by from 6 to 40° C., until the final temperature is reached.

17. The method according to claim 12 , wherein the temperature is increased stepwise by from 8 to 30° C., until the final temperature is reached.

18. The method according to claim 12 , wherein the temperature is increased stepwise by from 10 to 25° C., until the final temperature is reached.

Assignees

• Basf Se

Inventors

• Rudolph Jens
• Papp Rainer

Classifications

• B01J2219/00252

  Formation of deposits other than coke · CPC title

• B01J19/246

  internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s) · CPC title

• B01J2219/00247

  Fouling of the reactor or the process equipment · CPC title

• C07C45/50

  by oxo-reactions · CPC title

• B08B9/08

  Cleaning containers, e.g. tanks · CPC title