IP Library Granted Patent US 10,493,436
Granted Patent B2
US 10,493,436 · App. 15/968,889 · Granted Dec 3, 2019

Method for the simultaneous removal of carbon monoxide and nitrogen oxides from flue or exhaust gas

Inventors: Francesco Castellino (Birkerød, DK); Viggo Lucassen Hansen (Brønshøj, DK)
Assignee: Haldor Topsoe A/S
B01J23/6482B01D53/9468B01J21/063B01J23/22B01J35/0006B01J35/023B01D2255/1023B01D2255/20707B01D2255/20723B01D2255/9022
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Quick Facts
Patent No.
US 10,493,436
App. No.
15/968,889
Granted
Dec 3, 2019
Kind
B2
Abstract

A method in which flue gas or exhaust gas containing harmful carbon monoxide, organic compounds (VOC) and NOx is contacted with a layered catalyst. A first layer of the catalyst comprises an oxidation catalyst. An underlying layer of the catalyst comprises a NH3-SCR catalyst for the simultaneous removal of the carbon monoxide and NOx.

Claims (10)

1. Method for the reduction of amounts carbon monoxide, volatile organic compounds and nitrogen oxides in flue or exhaust gas comprising the steps of:

introducing ammonia and/or a precursor thereof into the flue or exhaust gas;

converting the precursor, if any, into ammonia;

contacting the gas and the ammonia at a temperature of up to 350° C. with a layered catalyst comprising an upper first catalyst layer with an oxidation catalyst and an underlying second catalyst layer with an NH3-SCR catalyst supporting completely the first layer, and oxidizing at least part of the amounts of carbon monoxide and the volatile organic compounds in the upper first layer without affecting the ammonia further contained in the gas, and reducing the amounts of nitrogen oxides in the underlying second catalyst layer by reaction with the ammonia.

2. The method of claim 1 , wherein the oxidation catalyst in the first layer consists of palladium, vanadium oxide and titanium oxide.

3. The method of claim 2 , wherein the oxidation catalyst consists of 0.45 wt %, palladium, 4.5 wt % vanadium pentoxide and supported on titanium oxide.

4. The method of claim 1 , wherein the first catalyst layer has a layer thickness of between 10 and 200 micron.

5. The method of claim 1 , wherein the first catalyst layer has a layer thickness of between 10 and 50 micron.

6. The method of claim 1 , wherein the NH3-SCR catalyst in the second catalyst layer comprises oxides of tungsten, molybdenum, vanadium and titanium.

7. The method of claim 1 , wherein the flue or exhaust gas is additionally treated with a conventional not layered SCR catalyst either upstream or downstream the layered catalyst.

Assignments (1)
CHANGE OF NAME Recorded Oct 3, 2023
From: HALDOR TOPSØE A/S
To: TOPSOE A/S
Reel/Frame 065108/0028 →
Priority Claims (1)
DK 2013 00091 · Feb 14, 2013 · national
Continuity (2)
Division 14767003
Related Publication 20180250661A1 · Sep 6, 2018