Process for removing sulfur oxides and nitrogen oxides from flue gases

• US 4,174,373 A
• Filed: 08/29/1975
• Issued: 11/13/1979
• Est. Priority Date: 09/04/1974
• Status: Expired due to Term

• Current Assignee: Hitachi, Ltd.
• Original Assignee: Hitachi, Ltd.
• Inventors: Kaneko, Katsuhiro, Kanehori, Keiichi, Yoshida, Kazuetsu, Seki, Michiharu, Sakurai, Yo
• Primary Examiner(s): Peters, G. O.
• Application Number:
  US05/609,081
• Time in Patent Office: 1,537 Days
• Field of Search: 423/239, 423/213.2, 252/445
• US Class Current: 423/239.1
• CPC Class Codes: B01D 53/60 Simultaneously removing sulfur oxides and nitrogen oxides
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

A catalyst comprising carbonaceous materials such as activated carbon, etc. impregnated with bromine, iodine, chlorine or their compounds, is impregnated with a promoter containing a specific metal, and brought in contact with a flue gas in the presence of ammonia, whereby nitrogen oxides and sulfur oxides contained in the flue gas are removed with a very high percent removal. The removal can be carried out at a temperature much lower than that of the conventional process.

Claims

1. A process for removing at least one of nitrogen oxides and sulfur oxides contained in a flue gas, which comprises contacting a flue gas containing at least one of nitrogen oxides and sulfur oxides with a catalyst comprising a carbonaceous material impregnated with at least one of bromine, iodine, chlorine, ammonium bromide, ammonium iodide, ammonium chloride, hydrogen bromide, hydrogen iodide and hydrogen chloride, and at least one of metal elements of groups 1B, 3B, 4B, 5B, 6B, 2A, 3A and 8 of the periodic table as a promoter in the presence of ammonia.

2. A process according to claim 1, wherein the carbonaceous material is at least one of activated carbon, amorphous carbon, graphite, char coal and carbonized char.

3. A process according to claim 1, wherein the ammonia is supplied from an outside source.

4. A process according to claim 1, wherein the flue gas contains at least nitrogen oxides.

5. A process according to claim 1, wherein the flue gas contains at least nitrogen oxides and sulfur oxides.

6. A process according to claim 1, wherein at least 0.01 g of bromine, iodine or chlorine is impregnated per 1 kg of the carbonaceous material.

7. A process according to claim 1, wherein at least 0.01 g of the ammonium iodide, ammonium bromide, ammonium chloride, hydrogen bromide, hydrogen iodide or hydrogen chloride, in terms of bromine, iodine or chlorine, is impregnated per 1 kg of the carbonaceous material.

8. A process according to claim 1, wherein the promoter is vanadium pentoxide.

9. A process according to claim 1, wherein the promoter is in the form of oxide.

10. A process according to claim 1, wherein the promoter is in the form of sulfate.

11. A process according to claim 1, wherein the promoter is in the form of nitrate.

12. A process according to claim 1, wherein the promoter is in the form of chloride.

13. A process according to claim 1, wherein the promoter is in the form of organic acid salt.

14. A process according to claim 1, wherein 0.1 to 10% by weight of the promoter is impregnated on the basis of the carbonaceous material.

15. A process according to claim 1, wherein the flue gas is contacted with the carbonaceous material at a temperature of the room temperature to 200°

C.

26. A process according to claim 1, wherein the amount of ammonia present is stoichiometrically equivalent to or a little more than the total amount of said nitrogen oxides and sulfur oxides.

16. A process for removing nitrogen oxides from a gas mixture containing nitrogen oxides comprising simultaneously contacting said gas mixture with (1) ammonia and (2) a catalyst comprising a carbonaceous material impregnated with (a) at least one halogenous material selected from the group consisting of bromine, iodine, chlorine, ammonium bromide, ammonium iodide, ammonium chloride, hydrogen bromide, hydrogen iodide and hydrogen chloride and (b) at least one metal of groups 1B, 3B, 4B, 5B, 6B, 2A, 3A and 8 of the Periodic Table.

17. The process of claim 16, wherein said at least one metal is in the form of a salt when said carbonaceous material is impregnated with said at least one metal.

18. The process of claim 17, wherein said salt is selected from the group consisting of a sulphate salt, a nitrate salt, a chloride salt and an organic acid salt.

19. The process of claim 18, wherein said carbonaceous material is impregnated with 0.1 to 10% by weight of said at least one metal and at least 0.10 gm halogenous material measured as elemental halogen per kgm of said carbonaceous material.

20. The process of claim 16, wherein said gas mixture is contacted with said carbonaceous material at a temperature between room temperature and 200°

C.

21. The Process of claim 20, wherein said carbonaceous material is activated carbon.

22. The process of claim 21, wherein said at least one metal is vanadium or copper.

23. The process of claim 22, wherein said carbonaceous material has thereon vanadium pentoxide or copper oxide.

24. The process of claim 21, wherein ammonia is mixed with said gas mixture prior to contact of said gas mixture with said carbonaceous material.

25. The process of claim 21, wherein said gas mixture and said ammonia gas are separately fed to said carbonaceous material.