US3980756A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Air pollution control system
Assignee: Combustion Engineering Inc
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Filing: 1974-01-28
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Granted: 1976-09-14
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Expires: 1994-01-28
Abstract
Abstract Gases containing SO 2 from a furnace are contacted in the scrubbing zone of a scrubber with an aqueous scrubbing medium containing solid alkaline earth metal carbonate, seed crystals of alkaline earth metal sulfate and dissolved alkaline earth metal carbonate and sulfate and having a pH of from 6.0 to 6.5. The SO 2 reacts to form sulfites and bisulfites. The scrubbing medium is then withdrawn from the scrubbing zone and discharged to a reaction tank. Air is blown through the scrubbing medium in the reaction tank and then up into and through the scrubber and scrubbing zone. The oxygen reacts with sulfite to form sulfate in both the reaction tank and the scrubbing zone. The amount of oxygen is controlled so that the pH in the scrubber will not drop below about 4.5 and so as to oxidize not more than about 30 to 50% of the sulfite. Fresh additives in the form of alkaline earth metal carbonate or alkaline earth metal oxide which has been formed by calcining alkaline earth metal carbonate in the furnace is also introduced into the reaction tank and the pH returned to 6.0 to 6.5. A portion of the medium from the reaction tank is returned to the scrubbing zone and the remainder is further treated with oxygen to convert the remaining sulfite to sulfate which is precipitated and separated from the liquid. The liquid is then returned to the scrubbing cycle.
Inventors
- 👤 Donn Lewis Dixson
- 👤 Carl Richard Bozzuto
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 18:49
CPC Classifications
C; C01; C01F; C01F11/00; C01F11/46; C01F11/464; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
308 words
A method of removing SO 2 from a flue gas stream from a furnace comprising the steps of: a. contacting said flue gas in a scrubbing zone of a scrubber with an aqueous scrubbing medium containing solid alkaline earth metal carbonate, seed crystals of alkaline earth metal sulfate and dissolved alkaline earth metal carbonate and sulfate and having a pH of from 6.0 to 6.5 whereby said SO 2 reacts with said aqueous scrubbing medium to form sulfites and bisulfites; b. contacting an oxygen-containing gas with said aqueous scrubbing medium in said scrubbing zone, the amount of said oxygen being such that said oxygen reacts with only a portion of said sulfite to form sulfate thereby reducing the pH to 4.5; c. withdrawing said aqueous scrubbing medium from said scrubbing zone; d. contacting an oxygen-containing gas with said withdrawn aqueous scrubbing medium and introducing into said withdrawn aqueous scrubbing medium an additive material selected from the group consisting of alkaline earth metal carbonate and an alkaline earth metal oxide formed by calcining alkaline earth metal carbonate in said furnace, the amount of said additive material being selected to replace the amount of precipitated alkaline earth metals separated in step (g) and the amount of said oxygen-containing gas being such that said oxygen reacts with only a portion of the remaining sulfite to form sulfate and whereby the pH is maintained from 6.0 to 6.5; e. recycling a portion of said aqueous scrubbing medium from step (d) to step (a); f. contacting an oxygen-containing gas with the remaining portion of said aqueous scrubbing medium from step (d) to convert substantially all of the remaining sulfite to sulfate; g. separating precipitated alkaline earth metal sulfate from said oxidized remaining portion of said aqueous medium from step (f); and h. recycling said aqueous scrubbing medium from step (g) to step (d).
Claim 2
Independent Claim
308 words
A method of removing SO 2 from a flue gas stream from a furnace comprising the steps of: a. contacting said flue gas in a scrubbing zone of a scrubber with an aqueous scrubbing medium containing solid alkaline earth metal carbonate, seed crystals of alkaline earth metal sulfate and dissolved alkaline earth metal carbonate and sulfate and having a pH of from 6.0 to 6.5 whereby said SO 2 reacts with said aqueous scrubbing medium to form sulfites and bisulfites; b. contacting an oxygen-containing gas with said aqueous scrubbing medium in said scrubbing zone, the amount of said oxygen being such that said oxygen reacts with only a portion of said sulfite to form sulfate thereby reducing the pH to 4.5; c. withdrawing said aqueous scrubbing medium from said scrubbing zone; d. contacting an oxygen-containing gas with said withdrawn aqueous scrubbing medium and introducing into said withdrawn aqueous scrubbing medium an additive material selected from the group consisting of alkaline earth metal carbonate and an alkaline earth metal oxide formed by calcining alkaline earth metal carbonate in said furnace, the amount of said additive material being selected to replace the amount of precipitated alkaline earth metals separated in step (g) and the amount of said oxygen-containing gas being such that said oxygen reacts with only a portion of the remaining sulfite to form sulfate and whereby the pH is maintained from 6.0 to 6.5; e. recycling a portion of said aqueous scrubbing medium from step (d) to step (a); f. contacting an oxygen-containing gas with the remaining portion of said aqueous scrubbing medium from step (d) to convert substantially all of the remaining sulfite to sulfate; g. separating precipitated alkaline earth metal sulfate from said oxidized remaining portion of said aqueous medium from step (f); and h. recycling said aqueous scrubbing medium from step (g) to step (d).
Claim 3
Dependent Claim
60 words
A method as recited in claim 1 wherein said steps (b) and (d) of contacting an oxygen-containing gas with said aqueous scrubbing medium in said scrubbing zone and with said withdrawn aqueous scrubbing medium comprise the steps of passing said oxygen-containing gas serially through said withdrawn aqueous scrubbing medium and then through said aqueous scrubbing medium in said scrubbing zone.
Claim 4
Dependent Claim
38 words
A method as recited in claim 2 wherein said step of introducing said additive material into said withdrawn aqueous scrubbing medium comprises the step of introducing said alkaline earth metal oxide with said flue gas into said scrubber.
Claim 5
Dependent Claim
45 words
A method as recited in claim 2 wherein said step of introducing said additive material into said withdrawn aqueous scrubbing medium comprises the steps of forming a slurry of alkaline earth metal carbonate and water and introducing said slurry into said withdrawn aqueous scrubbing medium.
Claim 6
Dependent Claim
36 words
A method as recited in claim 2 and further including the step of recycling a portion of said precipitated sulfate from step (g) to step (d) as seed crystals to aid in the precipitation of sulfate.
Claim 7
Dependent Claim
32 words
A method as recited in claim 2 wherein said portion of sulfite oxidized to sulfate in step (b) comprises from 30 to 50% of the sulfite present in said aqueous scrubbing medium.
Claim 8
Dependent Claim
29 words
A method as recited in claim 2 wherein said alkaline earth metal carbonate comprises a material selected from the group consisting of calcium carbonate, magnesium carbonate and mixture thereof.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-09-14 | 1980-03-15 | 1980-09-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-09-14 | 1984-03-15 | 1984-09-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-09-14 | 1988-03-15 | 1988-09-14 | $7700.00 | Window Closed / Lapsed |