Method for removing nitrogen oxides from an oxygen-containing flue gas stream

• US 20010038813A1
• Filed: 04/26/2001
• Published: 11/08/2001
• Est. Priority Date: 04/29/2000
• Status: Active Grant

• Current Assignee: Umicore AG & Company KG (Umicore S.A.)
• Original Assignee: dmc2 Degussa Metals Catalysts Cerdec AG (Vectra Corp.)
• Inventors: Lang, Jurgen, Gieshoff, Jurgen
• Granted Patent: US 6,517,794 B2
• Time in Patent Office: Days
• US Class Current: 423/239.1
• CPC Class Codes: B01D 2259/818 Employing electrical discharges or the generation of a plasma
• CPC Class Codes: B01D 53/56 Nitrogen oxides B01D53/60 takes precedence
• CPC Class Codes: B01D 53/8631 Processes characterised by a specific device
• CPC Class Codes: B01D 53/92 of engine exhaust gases exhaust or silencing apparatus for internal combustion engines, machines or engines in general, having means for purifying, rendering innocuous or otherwise treating exhaust gases F01N3/00
• CPC Class Codes: B01D 53/9431 Processes characterised by a specific device
• CPC Class Codes: F01N 2240/28 a plasma reactor
• CPC Class Codes: F01N 2610/02 the substance being ammonia or urea
• CPC Class Codes: F01N 3/0892 Electric or magnetic treatment, e.g. dissociation of noxious components electric filters F01N3/01; regeneration of exhaust filters F01N3/023; heating catalytic converters F01N3/2006
• CPC Class Codes: F01N 3/2832 granular, e.g. pellets

Abstract

A method for removing nitrogen oxides from a lean flue gas. The method is carried out by:

a) treating the flue gas in an electrical gas discharge,

b) passing the thus treated flue gas over a basic storage material to store the nitrogen oxides in the form of nitrates and release of the treated flue gas to the environment, and

c) regeneration of the storage material after depletion of its storage capacity by removing the storage material from the flue gas stream and treating it was a reducing regenerative gas stream while forming ammonia.

Claims

1. A method for removing nitrogen oxides from an oxygen-containing flue gas stream, comprising:

a) treating the flue gas in an electrical gas discharge,

b) passing the thus treated flue gas over a basic storage material to store the nitrogen oxides in the form of nitrates and release the treated flue gas to the environment, and

c) regeneration of the storage material after depletion of its storage capacity by removing the storage material from the flue gas stream and treating it with a reducing regenerative gas stream while forming ammonia.

2. The method as in

claim 1

, wherein (a) and (b) are run in parallel through arrangement of the storage material in said gas discharge.

3. The method as in

claim 1

, wherein said gas discharge and storage material are arranged successively in a single reactor.

4. The method as in

claim 1

, further comprising removing sulfur compounds from the flue gas before it enters the gas discharge.

5. The method as in

claim 4

, further comprising returning material to the process.

6. The method as in

claim 5

, which further comprising condensing the ammonia generated in (c) and recovering same.

7. The method as in

claim 6

, further comprising introducing the ammonia generated in (c) for selective catalytic reduction of another flue gas stream.

8. The method as in

claim 1

, wherein the regenerative gas stream contains carbon monoxide and steam and is recovered by a substoichiometrically operated combustion process.

9. The method as in

claim 1

, further comprising circulating the regenerative gas stream.

10. The method as in

claim 1

, further comprising subjecting the regenerative gas stream to a post-combustion before being released into the environment.

11. The method as in

claim 1

, wherein said gas discharge is operated in pulsed or modulated fashion.

12. The method as in

claim 1

, wherein the product of the electrode spacing and the gas pressure is between 0.1 and 100 mm•

bar.

13. The method as in

claim 1

, wherein said gas discharge is conducted as a surface sliding discharge.