IP Library Granted Patent US 7,070,746
Granted Patent B1
US 7,070,746 · App. 09/320,077 · Granted Jul 4, 2006

Process for nitrous oxide purification

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Quick Facts
Patent No.
US 7,070,746
App. No.
09/320,077
Granted
Jul 4, 2006
Kind
B1
Abstract

A method for purification of an oxygen contaminated nitrous oxide gas by feeding the nitrous oxide gas and a reducing agent such as hydrogen, carbon monoxide or ammonia into a de-oxidation reactor, performing de-oxidation by reacting the reducing agent with oxygen using a catalyst such as palladium or platinum in order to deplete the oxygen in the nitrous oxide gas, while limiting the amount of nitrous oxide removed from the nitrous oxide gas.

Claims (18)

1. A method for purification of a nitrous oxide gas containing O 2 , said method comprising:

feeding said nitrous oxide gas and a reducing agent selected from the group consisting of hydrogen, carbon monoxide, ammonia and mixtures thereof into a de-oxidation reactor;

performing de-oxidation by reacting said reducing agent with O 2 using a de-oxidation catalyst selected from the group consisting of palladium, platinum and mixtures thereof to form an inert, in order to deplete said O 2 in said nitrous oxide gas, while limiting the amount of nitrous oxide removed from said nitrous oxide gas.

2. A method according to claim 1 , wherein said reducing agent is hydrogen.

3. A method according to claim 1 , wherein said inert comprises water or carbon dioxide.

4. A method according to claim 1 , wherein said inert is water.

5. A method according to claim 1 , wherein said nitrous oxide gas further comprises NOx, nitrogen, carbon monoxide, carbon dioxide or organic compounds.

6. A method according to claim 5 , wherein said NOx is removed from said nitrous oxide gas by selective catalytic reduction using ammonia or a precursor thereof and a selective catalytic reduction catalyst.

7. A method according to claim 6 , wherein said selective catalytic reduction catalyst is selected from the group consisting of oxides of vanadium, titanium and mixtures thereof.

8. A method according to claim 6 , wherein said selective catalytic reduction is performed in a selective catalytic reduction reactor separate from said de-oxidation reactor.

9. A method according to claim 8 , wherein said selective catalytic reduction reactor is a lateral flow reactor.

10. A method according to claim 6 , wherein steam is used as a carrier gas for said nitrous oxide gas during said selective catalytic reduction.

11. A method according to claim 6 , wherein prior to said selective catalytic reduction, an oxygen containing gas is passed over said selective catalytic reduction catalyst.

12. A method according to claim 5 , wherein said carbon monoxide and organic compounds are removed from said nitrous oxide gas during said de-oxidation.

13. A method according to claim 1 , wherein said nitrous oxide gas comprises adipic acid off-gas.

14. A method according to claim 13 , wherein said off-gas comprises between 1000 ppmv and 10 vol. % O 2 , and between 100 ppmv and 1% NOx.

15. A method according to claim 1 , wherein up to 99 vol. % of said O 2 is removed from said nitrous oxide gas.

16. A method according to claim 1 , wherein said de-oxidation step is performed with more than one reactor.

Assignments (1)
CHANGE OF NAME Recorded May 23, 2012
From: ASCEND PERFORMANCE MATERIALS LLC
To: ASCEND PERFORMANCE MATERIALS OPERATIONS LLC
Reel/Frame 028260/0197 →