Patent US4021202A successfully refreshed from Google Patents.
US4021202A
Expired / Lapsed
US
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Apparatus for removing sulfur dioxide from stack gases
Assignee: Combustion Equipment Associates Inc
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Filing: 1976-01-28
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Granted: 1977-05-03
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Expires: 1996-01-28
Abstract
Abstract Method and apparatus for removing sulfur dioxide from stack gases. The stack gases are scrubbed with an aqueous wash liquid containing one or more alkali metal compounds which react to form the bisulfite, sulfite and sulfate salts of the alkali metal. The spent absorbent liquid effluent is then treated with calcium compounds in at least two separate reaction stages, the conditions of ion concentration and pH of the first stage being maintained to favor the precipitation of calcium sulfate in the presence of SO 3 = ions. In the succeeding reaction stages the precipitation of the desired amount of SO 3 = ions is carried out to form calcium sulfite. The resulting compound of calcium with sulfite and sulfate (which may in part be in the form of mixed crystals) are removed and the regenerated liquid is recycled.
Inventors
- 👤 Edwin L. Field
- 👤 Charles R. Lamantia
- 👤 Richard R. Lunt
- 👤 James E. Oberholtzer
- 👤 James R. Valentine
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 13:32
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
61 words
An apparatus for removing sulfur dioxide from stack gases, comprising in combination (a) mass transfer means for contacting SO 2 -containing gases with a SO 2 -absorbent solution containing at least one alkali metal compound and including means to separately withdraw SO 2 -lean gases and spent absorbent wash-liquid effluent containing reactant bisulfite, sulfite and sulfate salts of said alkali metal;
Claim 2
Independent Claim
61 words
An apparatus for removing sulfur dioxide from stack gases, comprising in combination (a) mass transfer means for contacting SO 2 -containing gases with a SO 2 -absorbent solution containing at least one alkali metal compound and including means to separately withdraw SO 2 -lean gases and spent absorbent wash-liquid effluent containing reactant bisulfite, sulfite and sulfate salts of said alkali metal;
Claim 3
Dependent Claim
241 words
(b) first stage reactor means for reacting said salts of said alkali metal in said spent wash liquid effluent under conditions to favor the precipitation of sulfate ions as calcium salts in the presence of sulfite ions along with the precipitation of some sulfite ions as calcium salts to form a first solids/liquid slurry; (c) means to introduce a controlled amount of at least one calcium compound into said first stage reactor; (d) a second stage reactor separate from said first stage reactor for reacting a portion of said slurry from said first stage reactor under conditions to complete the precipitation of a predetermined amount of said bisulfite and sulfite alkali metal salts as calcium sulfite to form a second solids/liquid slurry; (e) means to introduce a controlled amount of at least one calcium compound into said second stage reactor; (f) solids/liquid separator means adapted to separate solids from said first and second slurries; (g) first slurry transfer means arranged to transfer a portion of said first slurry from said first stage reactor directly to said second stage reactor and the remainder of said first slurry from said first stage reactor directly to said solids/liquid separator means; (h) second slurry transfer means arranged to transfer said second slurry from said second stage reactor to said solids/liquid separator means; and (i) means to recycle liquid from said solids/liquid separator means as at least a portion of said SO 2 -absorbent wash liquid.
Claim 4
Dependent Claim
241 words
(b) first stage reactor means for reacting said salts of said alkali metal in said spent wash liquid effluent under conditions to favor the precipitation of sulfate ions as calcium salts in the presence of sulfite ions along with the precipitation of some sulfite ions as calcium salts to form a first solids/liquid slurry; (c) means to introduce a controlled amount of at least one calcium compound into said first stage reactor; (d) a second stage reactor separate from said first stage reactor for reacting a portion of said slurry from said first stage reactor under conditions to complete the precipitation of a predetermined amount of said bisulfite and sulfite alkali metal salts as calcium sulfite to form a second solids/liquid slurry; (e) means to introduce a controlled amount of at least one calcium compound into said second stage reactor; (f) solids/liquid separator means adapted to separate solids from said first and second slurries; (g) first slurry transfer means arranged to transfer a portion of said first slurry from said first stage reactor directly to said second stage reactor and the remainder of said first slurry from said first stage reactor directly to said solids/liquid separator means; (h) second slurry transfer means arranged to transfer said second slurry from said second stage reactor to said solids/liquid separator means; and (i) means to recycle liquid from said solids/liquid separator means as at least a portion of said SO 2 -absorbent wash liquid.
Claim 5
Dependent Claim
113 words
An apparatus in accordance with claim 1 including (j) auxiliary first stage reactor means for reacting said salts of said alkali metal in said spent wash liquid effluent under conditions essentially the same as in said first stage reactor means to form a third slurry; (k) means to divide said spent absorbent wash liquid effluent from said mass transfer means into first and second streams; (l) means to direct said first stream to said first stage reactor means and said second stream to said auxiliary first stage reactor means; and (m) third slurry transfer means arranged to transfer said third slurry from said auxiliary first stage reactor directly to said solids/liquid separator means.
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) | 1980-05-02 | 1980-11-01 | 1981-05-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-05-02 | 1984-11-01 | 1985-05-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-05-02 | 1988-11-01 | 1989-05-03 | $7700.00 | Window Closed / Lapsed |