Low temperature urea-Scr operation in the presence of high sulphur flue gas

Patent metadata

Field	Value
Publication number	US-9782721-B2
Application number	US-201615009978-A
Country	US
Kind code	B2
Filing date	Jan 29, 2016
Priority date	Jan 30, 2015
Publication date	Oct 10, 2017
Grant date	Oct 10, 2017

Abstract

Systems and methods of continuous operation of a urea-SCR system at low temperatures (200-350° C.) in the presence of high SOx containing flue gas are described. The methods comprise introducing a solution of urea and an NO 2 forming compound, preferably an alkaline earth metal nitrate, into an exhaust stream before the exhaust stream contacts an SCR catalyst.

First claim

The invention claimed is:

1. A system comprising: (a) a solution comprising urea and at least one NO 2 forming compound, wherein the at least one NO 2 forming compound comprises: (i) a metal salt of a nitrate; (ii) a mixture of a metal containing compound and N 2 O 4 , N 2 O 5 , or mixtures thereof; or (iii) mixtures of (i) and (ii), (b) an SCR catalyst, (c) flue gas upstream of the SCR catalyst and comprising SOx at a concentration of 20 ppm or greater, and (d) a device for introducing the solution into a flue gas stream prior to the flue gas coming in contact with an SCR catalyst, where the introduction of the solution allows for the continuous operation of the system at temperatures in the range of about 250 to about 350° C.

2. The system of claim 1 , wherein the at least one NO 2 forming compound is a metal salt of a nitrate.

3. The system of claim 2 , wherein the metal salt of a nitrate is an alkaline earth metal nitrate, iron nitrate, manganese nitrate or mixtures thereof.

4. The system of claim 3 , wherein the metal salt of a nitrate is calcium nitrate or magnesium nitrate.

5. The system of claim 4 , wherein the metal salt of a nitrate comprises calcium nitrate.

6. The system of claim 1 , wherein the solution comprising urea and at least one NO 2 forming compound comprises Ca(NO 3 ) 2 .4[OC(NH 2 ) 2 ], 5Ca(NO 3 ) 2 .NH 4 NO 3 .10H 2 O or mixtures thereof.

7. The system of claim 1 , wherein the metal containing compound is a metal salt.

8. The system of claim 2 , wherein the metal salt is an alkaline earth metal salt, an iron salt, a manganese salt or mixtures thereof.

9. A method for reducing the amount of SO 3 in a flue gas, said method comprising introducing a solution comprising urea and at least one NO 2 forming compound into a flue gas stream prior to the flue gas coming in contact with an SCR catalyst, wherein the at least one NO 2 forming compound comprises: (i) a metal salt of a nitrate; (ii) a mixture of a metal containing compound and N 2 O 4 , N 2 O 5 , or mixtures thereof; or (iii) mixtures of (i) and (ii).

10. The method of claim 9 , wherein the flue gas contacts the SCR catalyst at a temperature in the range of about 200 to about 350° C.

11. The method of claim 9 , wherein said method also reduces the amount of phosphate.

12. The method of claim 9 , wherein the at least one NO 2 forming compound is a metal salt of a nitrate.

13. The method of claim 12 , wherein the metal salt of a nitrate is an alkaline earth metal nitrate, iron nitrate, manganese nitrate or mixtures thereof.

14. The method of claim 12 , wherein the metal salt of a nitrate is calcium nitrate or magnesium nitrate.

15. The method of claim 14 , wherein the metal salt of a nitrate comprises calcium nitrate.

16. The method of claim 9 , wherein the solution comprising urea and at least one NO 2 forming compound comprises Ca(NO 3 ) 2 .4[OC(NH 2 ) 2 ], 5Ca(NO 3 ) 2 .NH 4 NO 3 .10H 2 O or mixtures thereof.

17. The method of claim 9 , wherein the metal containing compound is a metal salt.

18. The method of claim 17 , wherein the metal salt is an alkaline earth metal salt, an iron salt, a manganese salt or mixtures thereof.

19. A method for reducing the formation of ammonium bisulphate in a urea-SCR system, the method comprising introducing a solution comprising urea and at least one NO 2 forming compound into a flue gas stream prior to the flue gas coming in contact with an SCR catalyst, wherein the at least one NO 2 forming compound comprises: (i) a metal salt of a nitrate; (ii) a mixture of a metal containing compound and N 2 O 4 , N 2 O 5 , or mixtures thereof; or (iii) mixtures of (i) and (ii).

20. The method of claim 19 , wherein the flue gas comprises SO x at a concentration of 20 ppm or greater prior to the flue gas coming in contact with the SCR catalyst, and the flue gas contacts the SCR catalyst at a temperature in the range of about 200 to about 350° C.

Assignees

• Johnson Matthey Plc

Inventors

• Foo Rodney
• Leppelt Rainer
• Muench Joerg Werner
• Dotzel Ralf
• Brandmair Maria

Classifications

• B01D53/8625 Primary

  Nitrogen oxides · CPC title

• F01N3/208

  Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent · CPC title

• B01D2255/9155

  Wall flow filters · CPC title

• F01N2610/02

  the substance being ammonia or urea · CPC title

• F01N2610/01

  the substance being catalytic material in liquid form · CPC title