Process for removing sulfur dioxide from flue gas

• US 4,291,004 A
• Filed: 09/28/1979
• Issued: 09/22/1981
• Est. Priority Date: 09/28/1979
• Status: Expired due to Term

• Current Assignee: Betz Laboratories, Inc. (General Electric Company)
• Original Assignee: Betz Laboratories, Inc. (General Electric Company)
• Inventors: McCaffrey, Craig R., Barraclough, Gary O.
• Primary Examiner(s): Vertiz, O. R.
• Assistant Examiner(s): Heller, Gregory A.
• Application Number:
  US06/079,672
• Time in Patent Office: 725 Days
• Field of Search: 423/242 A, 423/242 R, 423/243, 423/244 A, 423/244 R, 210/732
• US Class Current: 423/242.7
• CPC Class Codes: B01D 53/507 by treating the gases with other liquids

Abstract

A process for removing sulfur dioxide from flue gas is disclosed which utilizes, as a scrubber sludge dewatering aid, polyethylene oxide or derivative thereof.

Claims

1. A flue gas desulfurization process comprising in sequence:

(1) contacting sulfur dioxide-containing flue gas with scrubbing liquor to remove sulfur dioxide therefrom and produce scrubber sludge,

(2) subjecting said scrubber sludge to primary dewatering,

(3) adding to said scrubber sludge an effective amount as a dewatering aid of polyethylene oxide compound having the formula

space="preserve" listing-type="equation">R--CH.sub.2 CH.sub.2 --O--.sub.X H,

where X is about 2-40 and R is OH, sorbitan monooleate--O--, soya amine, ##STR3## where R₁, R₂ and R₃ are selected from the group consisting of hydrogen and alkyl such that the sum of the total number of carbon atoms in R₁, R₂ and R₃ is an average of from about 8 to 20, and

(4) subjecting said scrubber sludge to secondary dewatering.

2. The process of claim 1, wherein said dewatering aid is added in a liquid hydrocarbon solvent and is added in an amount of from about 0.5 pound to about 15 pounds/ton of scrubber sludge.

3. The process of claim 2, wherein X is about 3-15.

4. The process of claim 3, wherein said primary dewatering step comprises treating said scrubber sludge in a thickener.

5. The process of claim 4, wherein said secondary dewatering comprises vacuum filtration.

6. The process of claim 5, wherein said flue gas is produced by an industrial boiler and wherein said scrubbing liquor comprises an aqueous slurry of lime and fly ash.

7. The process of claim 6, wherein said dewatering aid is added in an amount of from about 2 pounds to about 5 pounds/ton of scrubber sludge, and wherein said liquid hydrocarbon solvent is kerosene.

8. The process of claim 3 or 7, wherein said scrubber sludge comprises an aqueous slurry of calcium sulfate, calcium sulfite and fly ash.

9. A flue gas desulfurization process comprising in sequence:

(1) contacting sulfur dioxide-containing flue gas with scrubbing liquor to remove sulfur dioxide therefrom and produce scrubber sludge,

(2) subjecting said scrubber sludge to primary dewatering,

(3) adding to said scrubber sludge an effective amount as a dewatering aid of polyethylene oxide compound having the formula;

##STR4## where R₁, R₂ and R₃ are selected from the group consisting of hydrogen and alkyl such that the sum of the total number of carbon atoms in R₁, R₂ and R₃ is from about 8 to 20 and X is from about 1 to 10, and

(4) subjecting said scrubber sludge to secondary dewatering.

10. The process of claim 9, wherein said dewatering aid is added in liquid hydrocarbon solvent and is added in an amount of from about 0.5 pound to about 15 pounds/ton of scrubber sludge.

11. The process of claim 10, wherein said primary dewatering step comprises treating said scrubber sludge in a thickener.

12. The process of claim 11, wherein said secondary dewatering step comprises vacuum filtration.

13. The process of claim 9, wherein X is about 2 to 5 and the total number of carbon atoms in R₁, R₂ and R₃ is about 10 to 15.

14. The process of claim 10, wherein said dewatering aid is added in an amount of from about 2 pounds to about 5 pounds/ton of scrubber sludge.

15. The process of claim 14, wherein said primary dewatering step comprises treating said scrubber sludge in a thickener.

16. The process of claim 15, wherein said secondary dewatering step comprises vacuum filtration.

17. The process of claim 16, wherein said flue gas is produced by an industrial boiler and wherein said scrubbing liquor comprises an aqueous slurry of lime and fly ash.

18. The process of claim 17, wherein said scrubber sludge comprises an aqueous slurry of calcium sulfate, calcium sulfite and fly ash.

19. The process of claim 18, wherein said hydrocarbon solvent is kerosene.

20. The process of claim 19, wherein said dewatering aid has the formula C₁₃ H₂₇ O(CH₂ CH₂ O)₃ H.

21. A flue gas desulfurization process comprising in sequence:

(1) contacting sulfur dioxide-containing flue gas with scrubbing liquor to remove sulfur dioxide therefrom and produce scrubber sludge,

(2) subjecting said scrubber sludge to primary dewatering, PG,28

(3) adding to said scrubber sludge an effective amount as a dewatering aid, polyethylene glycol in liquid hydrocarbon solvent, in an amount of from about 0.5 pounds to about 15 pounds/ton of said scrubber sludge, and

(4) subjecting said scrubber sludge to secondary dewatering.