IP Library Granted Patent US 6,890,501
Granted Patent B2
US 6,890,501 · App. 09/931,172 · Granted May 10, 2005

Method for simultaneously abating nitric oxides and nitrous oxides in gases containing them

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Quick Facts
Patent No.
US 6,890,501
App. No.
09/931,172
Granted
May 10, 2005
Kind
B2
Abstract

The invention concerns a method for purifying flue gases before they are released into the atmosphere of their nitrogen oxides N 2 O and NO x by reaction with ammonia by causing them to circulate at temperatures between 200 and 600° C. on a catalyst based on beta-zeolite loaded with iron. The invention is particularly useful for treating tail gases from factories producing nitric acid.

Claims (11)

1. Process for removing nitric oxides (NO x ) and nitrous oxide (N 2 O) from a gas comprising:

adding an amount of ammonia to said gas, said gas comprising NO x , N 2 O, oxygen and water, such that the amount of ammonia is at a value 0.7<X<1.4, wherein X is the voluminal ratio of ammonia/nitrogen oxides;

causing said gas to circulate at temperatures ranging between 200 and 600° C., on a catalyst comprising a iron beta-zeolite.

2. Process according to claim 1 , wherein said gas comprises between 100 and 7000 ppmv of NO x and N 2 O.

3. Process according to claim 1 , wherein said iron beta-zeolite comprises an iron beta-zeolite granule and an agglomeration binder.

4. Process according to claim 1 in which the iron beta-zeolite is a beta zeolite of Si/Al molar ratio ranging between 8 and 100, charged with iron by impregnation or exchange, in which the content by weight of iron ranges between 0.02 and 8%.

5. Process according to claim 4 , wherein the Si/Al molar ratio ranges between 8 and 20.

6. Process according to claim 4 , wherein the content by weight of iron ranges between 0.5-3%.

7. Process according to claim 1 , in which said gas circulates over the iron beta catalyst at voluminal velocities per hour (VVH) from 1000 to 50000 h −1 .

8. Process according to claim 1 , wherein the volume content of oxygen ranges between 1.5 and 5% and the volume content of water between 0.5 and 5%.

9. Process according to claim 1 , in which the gas is a tail gas from a nitric acid production factory.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 27, 2015
From: BOREALIS CHIMIE S.A.S.
To: CASALE S.A.
Reel/Frame 036187/0535 →
ENTITY CONVERSION Recorded Jul 20, 2015
From: BOREALIS CHIMIE S.A.
To: BOREALIS CHIMIE S.A.S.
Reel/Frame 036135/0639 →
CHANGE OF NAME Recorded Jul 16, 2015
From: GPN
To: BOREALIS CHIMIE S.A.
Reel/Frame 036114/0051 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 18, 2013
From: GRANDE-PAROISSE SA
To: GPN
Reel/Frame 031623/0609 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2005
From: DELAHAY, GERARD; MAUVEZIN, MATHIAS; NEVEU, BERNARD
To: GRANDE-PAROISSE S.A.
Reel/Frame 016926/0728 →
Priority Claims (1)
FR 99 01999 · Feb 18, 1999 · national
Continuity (2)
Continuation PCTFR000036700 · Feb 15, 2000
Related Publication 20020044902A1 · Apr 18, 2002