Method and system for selective noncatalytic NOx reduction

Patent metadata

Field	Value
Publication number	US-10105645-B2
Application number	US-201615561762-A
Country	US
Kind code	B2
Filing date	Mar 22, 2016
Priority date	Mar 26, 2015
Publication date	Oct 23, 2018
Grant date	Oct 23, 2018

Abstract

Disclosed herein are methods for treating an exhaust stream comprising NOx, the methods comprising receiving an exhaust stream and combining it with at least one nitrogen-containing reagent to form a combined stream, heating the combined stream to a reaction temperature ranging from about 870° C. to about 1100° C. to react at least a portion of the nitrogen-containing component, cooling the reacted stream in a first cooling step to a first temperature, and optionally further cooling the reacted stream in a second cooling step to a second temperature, wherein the first cooling step comprises heat exchange between at least a portion of the exhaust stream and at least a portion of the reacted stream. Exhaust treatment systems are also disclosed herein.

First claim

What is claimed is:

1. A method for treating an exhaust stream, comprising:
receiving an exhaust stream comprising NO x ;
combining the exhaust stream with at least one nitrogen-containing reagent to form a combined stream;
heating the combined stream to a reaction temperature ranging from about 870° C. to about 1100° C. to react at least a portion of the nitrogen-containing reagent; and
cooling the reacted stream in a first cooling step to a first temperature; and
wherein the first cooling step comprises heat exchange between at least a portion of the exhaust stream and at least a portion of the reacted stream.

2. The method of claim 1 , wherein the at least one nitrogen-containing reagent is chosen from ammonia, urea, cyanuric acid, hydrazine, and combinations thereof.

3. The method of claim 1 , wherein the normal stoichiometric N/NO x molar ratio between the at least one nitrogen-containing reagent and the NO in the exhaust stream ranges from about 1 to about 3.

4. The method of claim 1 , wherein the combined stream further comprises at least one gas chosen from air, oxygen, hydrogen, and combinations thereof.

5. The method of claim 1 , further comprising holding at the reaction temperature for a residence time ranging from about 0.1 seconds to about 3 seconds.

6. The method of claim 1 , wherein at least about 30% by weight of the NO x in the exhaust stream is reacted.

7. The method of claim 1 , wherein the first temperature ranges from about 700° C. to about 900° C.

8. The method of claim 1 , further comprising cooling the reacted stream in a second cooling step to a second temperature, wherein the second cooling step comprises heat exchange between an external stream and at least a portion of the reacted stream.

9. The method of claim 8 , wherein the second temperature ranges from about 300° C. to about 500° C.

10. The method of claim 8 , wherein the external stream comprises ambient air.

11. The method of claim 1 , further comprising combining the reacted stream with a second external stream after the first cooling step.

12. The method of claim 1 , further comprising preheating the exhaust stream to a temperature ranging from about 200° C. to about 800° C. prior to the combining step.

13. The method of claim 1 , wherein the exhaust stream comprises nitric oxide (NO), nitrogen dioxide (NO 2 ), nitrogen tetroxide (N 2 O 4 ), nitrogen pentoxide (N 2 O 5 ), or combinations thereof.

14. A method for treating an exhaust stream, comprising:
receiving an exhaust stream comprising NO x ;
preheating the exhaust stream to a first temperature;
combining the exhaust stream with at least one nitrogen-containing reagent to form a combined stream;
heating the combined stream to a reaction temperature ranging from about 870° C. to about 1100° C. to react at least a portion of the nitrogen-containing reagent; and
cooling the reacted stream in a first cooling step to a second temperature;
wherein at least one of cooling the reacted stream and preheating the exhaust stream comprises heat exchange between at least a portion of the reacted stream and at least a portion of the exhaust stream.

15. The method of claim 14 , wherein the first temperature ranges from about 200° C. to about 800° C.

16. The method of claim 14 , wherein the at least one nitrogen-containing reagent is chosen from ammonia, urea, cyanuric acid, hydrazine, and combinations thereof.

17. The method of claim 14 , further comprising holding at the reaction temperature for a residence time ranging from about 0.1 seconds to about 3 seconds.

18. The method of claim 14 , wherein the second temperature ranges from about 700° C. to about 900° C.

19. The method of claim 14 , further comprising cooling the reacted stream in a second cooling step to a third temperature ranging from about 300° C. to about 500° C.

20. A system for treating an exhaust stream comprising NO x , the system comprising:
a heating vessel for heating a combined stream comprising the exhaust stream and at least one nitrogen-containing reagent to a reaction temperature; and
a first heat exchanger for cooling the reacted stream to a first temperature; and
wherein the first heat exchanger transfers heat energy between at least a portion of the exhaust stream and at least a portion of the reacted stream.

21. The system of claim 20 , further comprising a vessel for receiving the exhaust stream and combining the exhaust stream with the at least one nitrogen-containing reagent.

22. The system of claim 20 , further comprising a reaction vessel for holding the combined stream at the reaction temperature for a residence time sufficient to react at least a portion of the nitrogen-containing reagent.

23. The system of claim 20 , further comprising a second heat exchanger for further cooling the reacted stream to a second temperature.

Assignees

• Corning Inc

Inventors

• Chung Mao Lin
• Li Chun-Ho
• Maslyn Matthew James
• Wu Fang Chih

Classifications

• B01D53/343 Primary

  Heat recovery · CPC title

• B01D53/56

  Nitrogen oxides (B01D53/60 takes precedence) · CPC title

• B01D2251/2067

  Urea · CPC title

• B01D2259/65

  Employing advanced heat integration, e.g. Pinch technology · CPC title

• B01D2251/206

  Ammonium compounds · CPC title