Regeneration of catalyst/absorber

• US 5,953,911 A
• Filed: 02/04/1998
• Issued: 09/21/1999
• Est. Priority Date: 02/04/1998
• Status: Expired due to Term

• Current Assignee: Emerachem Holdings LLC
• Original Assignee: GOAL Line Environmental Technologies LLC
• Inventors: Guth, Eugene D., Wagner, Gregory J., Campbell, Larry E.
• Primary Examiner(s): Lopez, F. Daniel
• Assistant Examiner(s): TRAN, BINH Q
• Application Number:
  US09/018,720
• Time in Patent Office: 594 Days
• Field of Search: 60/297, 60/295, 60/274, 60/301, 502/34
• US Class Current: 60/295
• CPC Class Codes: B01D 53/8631 Processes characterised by a specific device
• CPC Class Codes: B01D 53/8643 Removing mixtures of carbon monoxide or hydrocarbons and nitrogen oxides
• CPC Class Codes: B01D 53/9431 Processes characterised by a specific device
• CPC Class Codes: B01D 53/96 Regeneration, reactivation or recycling of reactants
• CPC Class Codes: B01J 23/90 Regeneration or reactivation
• CPC Class Codes: B01J 38/04 Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst

Abstract

Hydrocarbon in a carrier of nitrogen or steam is passed over a devitalized supported noble metal/alkali or alkaline earth catalyst/absorber, such as Pt on an alumina monolith coated with potassium carbonate, which has sorbed NOx from engine exhaust to restore and regenerate the devitalized catalyst/absorber for reuse. The hydrocarbon undergoes a shift reaction to produce CO in situ which is the reactant gas for the regeneration.

Claims

1. A method of regenerating a devitalized catalyst/absorber comprising an oxidation catalyst component selected from platinum, palladium, rhodium, cobalt, nickel, iron, copper, molybdenum or combinations thereof disposed on a high surface area support and an absorber material selected from a hydroxide, carbonate, bicarbonate or mixture thereof of an alkali or alkaline earth or mixtures thereof and having nitrogen oxides absorbed therein or thereon, said method comprising the steps of:

providing a stream of regenerating gas comprising hydrocarbon and an inert carrier gas; and

passing said stream of regenerating gas over said devitalized catalyst/absorber for an effective time, at an effective temperature and at an effective space velocity to remove said nitrogen oxides from said devitalized absorber to form a regenerated catalyst/absorber.

2. The method according to claim 1 wherein said temperature is in the range of 250°

F. to 750°

F.

3. The method according to claim 2 wherein said hydrocarbon comprises C₁ -C₁₂ hydrocarbon.

4. The method according to claim 1 wherein said hydrocarbon comprises methane.

5. The method according to claim 4 wherein said methane is contained in a natural gas stream.

6. The method according to claim 1 wherein said hydrocarbon comprises propane.

7. The method according to claim 1 wherein said hydrocarbon comprises propylene.

8. The method according to claim 1 wherein said hydrocarbon comprises toluene.

9. The method according to claim 1 wherein the space velocity is in the range of 10 hr^-1 to 100,000 hr^-1.

10. The method according to claim 9 wherein the space velocity is in the range of 500 to 16,000 hr^-1.

11. The method according to claim 1 wherein said catalyst component is coated with said absorber.

12. The method according to claim 11 wherein the absorber comprises a coating of an alkali or alkaline earth carbonate or bicarbonate thereon.

13. The method according to claim 12 wherein the alkali or alkaline earth carbonate comprises potassium carbonate.

14. The method according to claim 1 wherein the catalyst comprises platinum.

15. The method according to claim 1 wherein the catalyst/absorber comprises an alumina support with a platinum coating thereon.

16. The method according to claim 1 wherein said inert carrier gas comprises nitrogen, helium, nitrogen or steam.