IP Library Granted Patent US 7,235,223
Granted Patent B2
US 7,235,223 · App. 10/660,521 · Granted Jun 26, 2007

Method for operating a flue gas purification plant

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Quick Facts
Patent No.
US 7,235,223
App. No.
10/660,521
Granted
Jun 26, 2007
Kind
B2
Abstract

In a method for operating a flue gas purification plant ( 10 ) including a plurality of parallel of absorber chambers ( 11 ), in which in each absorber chamber ( 11 ), CO and NO are simultaneously oxidized by a catalyst in a first absorber ( 15 ) according to the SCONOx principle and the resulting NO 2 is absorbed on the catalyst surface, in which SO 2 is furthermore oxidized by a catalyst in a second absorber ( 14 ) upstream of the first absorber ( 15 ) according to the SCOSOx principle and the resulting SO 3 is absorbed on the catalyst surface. The absorber chambers ( 11 ) are successively regenerated by a regeneration gas containing hydrogen and/or hydrogen compounds in regularly repeating regeneration cycles affecting all the absorber chambers ( 11 ). In order to improve reliability and reduce operating costs in such a method, the regeneration time of the second absorber ( 14 ) within the regeneration cycle is respectively selected to be long enough to guarantee sufficient regeneration of the second absorber ( 14 ).

Claims (15)

1. A method for operating a flue gas purification plant having a plurality of parallel absorber chambers, the method comprising:

simultaneously oxidizing CO and NO in each absorber chamber with a first single catalyst in a first absorber, and absorbing the resulting NO 2 on the catalyst surface;

oxidizing SO 2 with a second catalyst in a second absorber upstream of the first absorber, and absorbing the resulting SO 3 on the catalyst surface;

successively regenerating the absorber chambers with a regeneration gas containing hydrogen, hydrogen compounds, or both, in regularly repeating regeneration cycles affecting all the absorber chambers; and

selecting the regeneration time of the second absorber within each of said regeneration cycles to be long enough for regeneration of the second absorber.

2. The method as claimed in claim 1 , comprising:

allocating a regeneration time for each absorber chamber within the regeneration cycle;

regenerating the second absorber in a first time segment; and

regenerating the first absorber in a subsequent second time segment, wherein the first time segment is at least about 5 minutes, for full regeneration of an absorber chamber in the regeneration time.

3. The method as claimed in claim 2 , wherein the second time segment is at least about 3 minutes.

4. The method as claimed in claim 1 , comprising regenerating the first and second absorbers independently of one another.

5. The method as claimed in claim 1 , comprising:

regenerating the first absorbers of the absorber chambers in a first regeneration cycle; and regenerating the second absorbers of the absorber chambers in a second regeneration cycle;

wherein the second regeneration cycle lasts substantially longer than the first regeneration cycle.

6. The method as claimed in claim 5 , wherein only the second absorber of an absorber chamber is regenerated in each first regeneration cycle.

Assignments (1)
CHANGE OF NAME Recorded Aug 17, 2016
From: ALSTOM TECHNOLOGY LTD
To: GENERAL ELECTRIC TECHNOLOGY GMBH
Reel/Frame 039714/0578 →