Method for the reduction of sulfur trioxide in an effluent

• US 4,822,577 A
• Filed: 07/14/1988
• Issued: 04/18/1989
• Est. Priority Date: 07/14/1988
• Status: Expired due to Fees

• Current Assignee: Fuel Tech Incorporated
• Original Assignee: Fuel Tech Incorporated
• Inventors: Sprague, Barry N., Sullivan, James C., Epperly, William R.
• Primary Examiner(s): HELLER, GREGORY
• Application Number:
  US07/219,297
• Time in Patent Office: 278 Days
• Field of Search: 423/242 R, 423/243, 423/244 R, 423/244 A
• US Class Current: 423/242.5
• CPC Class Codes: B01D 53/507 by treating the gases with other liquids
• 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 method is presented for the selective gas-phase reduction of sulfur trioxide in the effluent from the combustion of a carbonaceous fuel, the method comprising introducing a treatment agent comprising hydrogen peroxide or an oxygenated hydrocarbon having at least two carbon atoms into the effluent at an effluent temperature of no greater than about 1450° F.

Claims

1. A method for the selective reduction of sulfur trioxide in the effluent from the combustion of a carbonaceous fuel, the method comprising introducing a treatment agent comprising hydrogen peroxide or an oxygenated hydrocarbon having at least two carbon atoms into the effluent at an effluent temperature of between about 1000°

F. and about 1450°

F.

2. The method of claim 1 wherein said oxygenated hydrocarbon is selected from the group consisting of alcohols, sugars, lignin derivatives, carboxylic acids, peroxides, aldehydes, ethers, esters, ketones, and mixtures thereof.

3. The method of claim 2 wherein said oxygenated hydrocarbon is selected from the group consisting of ethylene glycol, molasses, glycerin, tetrahydrofuran, acetone, ammonium acetate, citric acid, sucrose, and mixtures thereof.

4. The method of claim 1 wherein the effluent temperature is between about 1100°

F. and about 1350°

F.

5. The method of claim 1 wherein the weight ratio of said oxygenated hydrocarbon to sulfur trioxide in the effluent is about 3:

1 to about 8;

1.

6. The method of claim 1 wherein said treatment agent comprises an aqueous dispersion.

7. The method of claim 6 wherein said oxygenated hydrocarbon is present in said dispersion in an amount of about 1% to about 25% by weight.

8. The method of claim 1 wherein the pollutant being reduced comprises both nitrogen oxides and sulfur trioxide.

9. A method for the reduction of nitrogen oxides while concommitantly reducing the concentration of sulfur trioxide in the effluent from the combustion of a carbonaceous fuel, the method comprising introducing into the effluent a treatment agent comprising hydrogen peroxide or an oxygenated hydrocarbon having at least two carbon atoms at an effluent temperature of between about 1000°

F. and about 1450°

F.

10. The method of claim 9 wherein said oxygenated hydrocarbon is selected from the group consisting of alcohols, sugars, lignin derivatives, carboxylic acids, peroxides, aldehydes, ethers, esters, ketones, and mixtures thereof.

11. The method of claim 10 wherein said oxygenated hydrocarbon is selected from the group consisting of ethylene glycol, molasses, glycerin, tetrahydrofuran, ammonium acetate, citric acid, acetone, sucrose, and mixtures thereof.

12. The method of claim 9 wherein the effluent temperature is between about 1100°

F. and about 1300°

F.

13. The method of claim 9 wherein the weight ratio of said oxygenated hydrocarbon to sulfur trioxide in the effluent is about 3:

1 to about 8;

1.

14. The method of claim 9 wherein said treatment agent comprises an aqueous dispersion.

15. The method of claim 14 wherein said oxygenated hydrocarbon is present in said dispersion in an amount of about 1% to about 25% by weight.