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US3906080A Expired / Lapsed US ⏱️ 0.0 years remaining

Removal of sulfur dioxide from gases containing sulfur dioxide and oxygen

Assignee: Consolidation Coal Co
•
Filing: 1974-08-19
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Granted: 1975-09-16
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Expires: 1994-08-19
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Abstract

Abstract An improvement in the selective removal of SO2 from gases containing SO2 and O2 wherein a thiosulfate-rich aqueous solution containing a sulfite-forming additive is used as the selective SO2 absorbent, whereby a gas of substantially reduced SO2 content and a substantially unchanged O2 content is obtained.

Inventors

  • 👤 Everett Gorin
  • 👤 Metro D Kulik
  • 👤 Robert T Struck

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 20:11
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1493; B01D53/1456; B01D53/1481; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; C; C01; C01B; C01B17/00; C01B17/48; C01B17/50; C01B17/60; Y; Y02; Y02A; Y02A50/00; Y02A50/20

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 185 words
IN A PROCESS FOR REMOVING SULFUR DIOXIDE FROM A GAS STREAM CONTAINING SO2 AND 32 IN WHICH SAID GAS STREAM IS CONTACTED IN A SCRUBBER WITH AN AQUEOUS SOLUTION CONTAINING A SULFITEFORMING REAGENT SELECTED FROM THE CLASS CONSISTING OF ALKALI METAL HYDROXIDES AND CARBONATES AND AMMONIUM HYDROXIDE AND CORBONATE IN AT LEAST THE AMOUNT REQUIRED TO CONVERT THE PROMOTE REACTION OF THE SO2 WITH THE SULFITE-FORMING REAGENT, TO THEREBY YIELD AN EFFLUENT GAS STREAM OF REDUCED FULFUR DIOXIDE CONTENT AND AN EFFLUENT AQUEOUS SOLUTION CONTAINING ALKALI METAL OR AMMONIUM SULFITE, THE IMPROVEMENT WHICH COMPRISES: A. INTRODUCING FRESH AQUEOUS SCRUBBING SOLUTION INTO SAID SCRUBBER WHICH CONTAINS, IN ADDITION TO SAID SULFITE-FORMING REAGENT, AT LEAST 15 PERCENT BY WEIGHT OF AN ALKALI METAL OR AMMONIUM THIOSULFATE, AND THEREAFTER B. OPERATING THE SCRUBBER AT CONDITIONS SELECTED TO MAINTAIN THE PH OF THE SOLUTION LEAVING THE SCRUBBER BETWEEN 6.3 AND 8.0, AND TO YIELD AN EFFLUENT GAS STREAM WHICH IS SUBSTANTIALLY FREE OF SO2 AND AN EFFLUENT AQUEOUS SCRUBBING SOLUTION WHICH CONTAINS SUBSTANTIALLY ALL THE SULFITE PRODUCED IN THE SCRUBBER BY THE REACTION OF SO2 AND THE SULFITE-FORMING REAGENT.
Claim 2
Dependent Claim 185 words
IN A PROCESS FOR REMOVING SULFUR DIOXIDE FROM A GAS STREAM CONTAINING SO2 AND 32 IN WHICH SAID GAS STREAM IS CONTACTED IN A SCRUBBER WITH AN AQUEOUS SOLUTION CONTAINING A SULFITEFORMING REAGENT SELECTED FROM THE CLASS CONSISTING OF ALKALI METAL HYDROXIDES AND CARBONATES AND AMMONIUM HYDROXIDE AND CORBONATE IN AT LEAST THE AMOUNT REQUIRED TO CONVERT THE PROMOTE REACTION OF THE SO2 WITH THE SULFITE-FORMING REAGENT, TO THEREBY YIELD AN EFFLUENT GAS STREAM OF REDUCED FULFUR DIOXIDE CONTENT AND AN EFFLUENT AQUEOUS SOLUTION CONTAINING ALKALI METAL OR AMMONIUM SULFITE, THE IMPROVEMENT WHICH COMPRISES: A. INTRODUCING FRESH AQUEOUS SCRUBBING SOLUTION INTO SAID SCRUBBER WHICH CONTAINS, IN ADDITION TO SAID SULFITE-FORMING REAGENT, AT LEAST 15 PERCENT BY WEIGHT OF AN ALKALI METAL OR AMMONIUM THIOSULFATE, AND THEREAFTER B. OPERATING THE SCRUBBER AT CONDITIONS SELECTED TO MAINTAIN THE PH OF THE SOLUTION LEAVING THE SCRUBBER BETWEEN 6.3 AND 8.0, AND TO YIELD AN EFFLUENT GAS STREAM WHICH IS SUBSTANTIALLY FREE OF SO2 AND AN EFFLUENT AQUEOUS SCRUBBING SOLUTION WHICH CONTAINS SUBSTANTIALLY ALL THE SULFITE PRODUCED IN THE SCRUBBER BY THE REACTION OF SO2 AND THE SULFITE-FORMING REAGENT.
Claim 3
Dependent Claim 24 words
A process according to claim 1 in which the sulfite-forming reagent is an alkali metal carbonate and the thiosulfate is an alkali metal thiosulfate.
Claim 4
Dependent Claim 46 words
A process according to claim 2 in which the concentration of the sulfite-forming reagent is less than two percent by weight of the fresh solution entering the scrubber and the concentration of the thiosulfate in the same solution is between 15 and 75 percent by weight.
Claim 5
Dependent Claim 16 words
A process according to claim 3 wherein said pH is maintained between about 6.3 and 7.3.
Claim 6
Dependent Claim 150 words
A process for removing SO2 from a gas stream containing SO2 and O2 which comprises: a. passing said gas stream through a scrubber which is maintained between 125* and 160*F.; b. circulating an aqueous solution through said scrubber in intimate contact with said gas stream, said aqueous solution containing potassium carbonate in at least the amount required to convert the SO2 in the gas stream to sulfite; c. maintaining in said aqueous solution throughout its passage through said scrubber potassium thiosulfate having a concentration of at least 15 percent by weight of said solution; d. maintaining the pH of the aqueous solution leaving the scrubber between 6.3 and 8.0; e. withdrawing the effluent gas stream from said scrubber substantially free of SO2; and f. withdrawing the effluent aqueous solution from said scrubber with substantially alL the sulfite produced in the scrubber by the reaction of SO2 and the potassium carbonate.
Claim 7
Dependent Claim 150 words
A process for removing SO2 from a gas stream containing SO2 and O2 which comprises: a. passing said gas stream through a scrubber which is maintained between 125* and 160*F.; b. circulating an aqueous solution through said scrubber in intimate contact with said gas stream, said aqueous solution containing potassium carbonate in at least the amount required to convert the SO2 in the gas stream to sulfite; c. maintaining in said aqueous solution throughout its passage through said scrubber potassium thiosulfate having a concentration of at least 15 percent by weight of said solution; d. maintaining the pH of the aqueous solution leaving the scrubber between 6.3 and 8.0; e. withdrawing the effluent gas stream from said scrubber substantially free of SO2; and f. withdrawing the effluent aqueous solution from said scrubber with substantially alL the sulfite produced in the scrubber by the reaction of SO2 and the potassium carbonate.

References Cited (Backward Citations)

US2729543A Cited
US3431070A Cited
US3644087A Cited
US3635820A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-15 1979-03-17 1979-09-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-15 1983-03-17 1983-09-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-15 1987-03-17 1987-09-16 $7700.00 Window Closed / Lapsed

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