IP Library Granted Patent US 8,850,802
Granted Patent B1
US 8,850,802 · App. 13/843,906 · Granted Oct 7, 2014

Catalytic reduction of NO

Inventors: Anders Andreasson (Västa Frölunda, SE); Guy Richard Chandler (Cambridge, GB); Claus Fnednch Goersman (Royston, GB); James Patrick Warren (Cambridge, GB); Georg Huethwohl (Soest, DE)
Assignees: Daimler AG; HJS Emission Technology GmbH & Co. KG; Johnson Matthey Public Ltd. Co.
F01N3/2882
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Quick Facts
Patent No.
US 8,850,802
App. No.
13/843,906
Granted
Oct 7, 2014
Kind
B1
Abstract

A system for NO x reduction in combustion gases, especially from diesel engines, incorporates an oxidation catalyst to convert at least a portion of NO to NO 2 , particulate filter, a source of reductant such as NH 3 and an SCR catalyst. Considerable improvements in NO x conversion are observed.

Claims (25)

1. A system for removing particulate matter and NOx from exhaust gas from a diesel engine, the system comprising:

an oxidation catalyst configured to receive the exhaust gas and convert NO in the exhaust gas to NO2 to create an adjusted gas stream;

a particulate trap downstream of the oxidation catalyst configured to receive the adjusted gas stream and trap the particulate matter in the adjusted gas stream to create a further adjusted gas stream;

a reductant fluid injector downstream of the particulate trap configured to inject reductant fluid comprising urea into the further adjusted gas stream to create a further adjusted gas stream mixed with reductant fluid; and

an SCR catalyst downstream of the reductant fluid injector configured to receive the further adjusted gas stream mixed with reductant fluid to create a final gas stream with a reduced NOx content by volume relative to the NOx content by volume of the exhaust gas;

wherein the oxidation catalyst is further configured to convert enough NO in the exhaust gas to NO2 such that the adjusted gas stream exiting the oxidation catalyst (1) causes a significant portion of particulate matter in the particulate trap to combust such that there is no significant accumulation of particulate matter in the particulate trap at a temperature lower than a temperature that the particulate matter in the particulate trap would combust in the presence of the exhaust gas in an identical system without an oxidation catalyst such that there is no significant accumulation of particulate matter in the particulate trap, and (2) has an NO to NO2 ratio adjusted for greater NOx reduction over the SCR catalyst taking into account the decrease in NO2 caused by combustion of particulate matter in the particulate trap, relative to a lower NOx reduction over an SCR catalyst in an identical system without an oxidation catalyst.

2. The system of claim 1 , wherein the diesel engine is a vehicle engine.

3. The system of claim 1 , wherein the diesel engine is a heavy duty diesel truck engine.

4. The system of claim 1 , wherein the diesel engine is a turbocharged heavy duty diesel truck engine.

5. The system of claim 4 , wherein the turbocharger is configured to cool the further adjusted gas stream.

6. The system of claim 1 , wherein the oxidation catalyst is configured to convert less than all of the NO in the exhaust gas to NO 2 .

7. The system of claim 4 , wherein the SCR catalyst is configured to convert more than 90% of the NO x in the further adjusted gas stream mixed with reductant fluid when the further adjusted gas stream mixed with reductant fluid is at least 225° C.

8. The system of claim 7 , wherein the system is configured to create a final gas stream with 67% less particulate matter than the exhaust gas.

9. A system for removing particulate matter and NOx from exhaust gas from a diesel engine, the system comprising:

an oxidation catalyst configured to receive the exhaust gas and convert NO in the exhaust gas to NO2 to create an adjusted gas stream;

a particulate trap downstream of the oxidation catalyst configured to receive the adjusted gas stream and trap the particulate matter in the adjusted gas stream to create a further adjusted gas stream;

a reductant fluid injector downstream of the particulate trap configured to inject reductant fluid comprising urea into the further adjusted gas stream to create a further adjusted gas stream mixed with reductant fluid; and

an SCR catalyst downstream of the reductant fluid injector configured to receive the further adjusted gas stream mixed with reductant fluid to create a final gas stream with a reduced NOx content by volume relative to the NO, content by volume of the exhaust gas;

wherein the oxidation catalyst is further configured to convert enough NO in the exhaust gas to NO2 such that the adjusted gas stream exiting the oxidation catalyst (1) causes particulate matter in the particulate trap to combust at a temperature lower than a temperature that the particulate matter in the particulate trap would combust in the presence of the exhaust gas in an identical system without an oxidation catalyst, and (2) has an NO to NO2 ratio adjusted for greater NOx reduction over the SCR catalyst taking into account the decrease in NO2 caused by combustion of particulate matter in the particulate trap, relative to a lower NOx reduction over an SCR catalyst in an identical system without an oxidation catalyst; and

wherein the system is configured to create a final gas stream with (1) 90% less NOx by volume than the exhaust gas when the further adjusted gas stream mixed with reductant fluid is at least 225° C., and (2) 67% less particulate matter by volume than the exhaust gas.

10. The system of claim 9 , wherein the diesel engine is a vehicle engine.

11. The system of claim 9 , wherein the diesel engine is a heavy duty diesel truck engine.

12. The system of claim 9 , wherein the diesel engine is a turbocharged heavy duty diesel truck engine.

13. The system of claim 12 , wherein the turbocharger is configured to cool the further adjusted gas stream.

14. The system of claim 9 , wherein the oxidation catalyst is configured to convert less than all of the NO in the exhaust gas to NO 2 .

Assignments (1)
CHANGE OF NAME Recorded Mar 15, 2016
From: HJS FAHRZEUGTECHNIK GMBH & CO. KG
To: HJS EMISSION TECHNOLOGY GMBH & CO. KG
Reel/Frame 038100/0475 →