IP Library › Granted Patent US 7,455,820
Granted Patent B2
US 7,455,820 · App. 11/323,298 · Granted Nov 25, 2008

Process for removing sulfur dioxide and nitrogen oxides from flue gas using chlorine dioxide

Assignee: Korea Institute of Energy Research
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Quick Facts
Patent No.
US 7,455,820
App. No.
11/323,298
Granted
Nov 25, 2008
Kind
B2
Abstract

Disclosed herein is a process for removing sulfur dioxide (SO 2 ) and nitrogen oxides (NO x ) from flue gas using chlorine dioxide (ClO 2 ). In the process, chlorine dioxide is allowed to react with flue gas in an alkaline solution so as to be able to simultaneously remove sulfur dioxide and nitrogen oxides from the flue gas. In the simultaneous removal of sulfur dioxide and nitrogen oxides from flue gas using the process, chlorine dioxide is produced by side reactions, and the produced chlorine dioxide can be used to remove sulfur dioxide and nitrogen oxides from flue gas.

Claims (18)

1. A process for removing sulfur dioxide and nitrogen oxides from flue gas, comprising reacting chlorine dioxide with the flue gas in an alkaline reaction solution so as to simultaneously remove sulfur dioxide and nitrogen oxides from the flue gas.

2. The process of claim 1 , wherein the chlorine dioxide is obtained by reducing chlorate with a reducing agent.

3. The process of claim 1 , wherein the concentration of the chlorine dioxide is adjusted by the supply rate of a reducing agent.

4. The process of claim 1 , wherein the chlorine dioxide is introduced into the reaction solution by a carrier gas selected from the group consisting of air, nitrogen and flue gas.

5. The process of claim 1 , wherein the chlorine dioxide is supplied into the reaction solution within a closed reactor having a total volume of 2.5 liters by a carrier gas having a flow rate of 2-10 liters/min per liter of the reaction solution.

6. The process of claim 1 , wherein the reaction between the chlorine dioxide and the flue gas is carried out at a temperature of 20-60° C.

7. The process of claim 1 , wherein the pH of the reaction solution is maintained in a range of 7-11.

8. The process of claim 1 , wherein the flue gas contains 4-10% of oxygen.

9. The process of claim 1 , wherein the concentration of the sulfur dioxide in the flue gas is 200-700 ppm.

10. The process of claim 1 , wherein the concentration of nitrogen oxides in the flue gas is 150-1,000 ppm.

11. The process of claim 2 , wherein the reducing agent is at least one selected from the group consisting of sulfur dioxide (SO 2 ), sodium chloride (NaCl), hydrochloric acid (HCl), methanol (CH 3 OH), and hydrogen peroxide (H 2 O 2 ).

12. The process of claim 7 , wherein alkali metal hydroxide or alkaline metal hydroxide is added to the reaction solution in order to maintain the pH of the reaction solution in a range of 7-11.

13. The process of claim 2 , wherein the chlorate comprises sodium chlorate.

14. A process for removing sulfur dioxide and nitrogen oxides from flue gas, comprising reacting chlorine dioxide with the flue gas in a reaction solution so as to simultaneously remove sulfur dioxide and nitrogen oxides from the flue gas, wherein the reaction solution has a pH of 3.5-6.

15. The process of claim 14 , wherein the reaction solution has a pH of 3.5-5.

16. A process tor removing sulfur dioxide and nitrogen oxides from flue gas, comprising:

reacting chlorine dioxide with flue gas in a reaction solution so as to simultaneously remove sulfur dioxide and nitrogen oxides from the flue gas,

wherein the chlorine dioxide is obtained by reducing chlorate with a reducing agent, the reducing agent being at least one selected from the group consisting of sulfur dioxide (SO 2 ), sodium chloride (NaCl) and hydrochloric acid (HCl), methanol (CH 3 OH), and hydrogen peroxide (H 2 O 2 ); the chlorine dioxide is supplied into the reaction solution within a closed reactor having a total volume of 2.5 liters by a carrier gas having a flow rate of 2-10 liters/min per liter of the reaction solution; the reaction between the chlorine dioxide and the flue gas is carried out at a temperature of 20-60° C.; and the pH of the reaction solution is maintained in a range of 3.5-5.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 4, 2006
From: LEE, HYUNG-KEUN; CHOI, WON-KIL; JO, HANG-DAE; JIN, DONG-SEOP; SESHWAL, BAL RAJ
To: KOREA INSTITUTE OF ENERGY RESEARCH
Reel/Frame 017583/0654 →
Priority Claims (1)
KR 10-2005-0034119 · Apr 25, 2005 · national
Continuity (1)
Related Publication 20060239878A1 · Oct 26, 2006