US3944649A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Multistage process for removing sulfur dioxide from stack gases
Assignee: Combustion Equipment Associates Inc
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Filing: 1973-12-13
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Granted: 1976-03-16
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Expires: 1993-12-13
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 compounds 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
2026-11-03 08:21
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
259 words
In a process for removing sulfur dioxide from stack gases which includes the steps of contacting stack gases with an aqueous wash liquid comprising a solution of one or more alkali metal compounds thereby to form a spent absorbent liquid containing the bisulfite, sulfite and sulfate salts of said alkali metal and then subsequently recovering at least a portion of the alkali metal ion values by reacting said bisulfite, sulfite and sulfate salts in said spent absorbent liquid with one or more calcium compounds to precipitate calcium sulfite and calcium sulfate, the improvement comprising (1) carrying out the step of reacting said bisulfite, sulfite and sulfate salts with said calcium compounds in multiple stages, said spent absorbent liquid introduced into the first stage having a total oxidizable sulfur concentration of at least about 0.1 molar, a ratio of bisulfite to sulfite ions of at lest one and a sulfate ion concentration of between about 0.1 and 2.8 molar whereby the reaction conditions of said first of said multiple stages are maintained to effect the precipitation of a solids mixture of calcium sulfate and calcium sulfite in said first stage, said solids mixture having greatly enhanced settling and filtration characteristics, (2) limiting the mean residence time of said solids mixture in said first stage to not more than 30 minutes, and (3) transferring at least a portion of said solids mixture of calcium sulfate and calcium sulfite formed in said first stage to one or more succeeding stages to serve as seed crystals for the further precipitation of calcium salts.
Claim 2
Dependent Claim
259 words
In a process for removing sulfur dioxide from stack gases which includes the steps of contacting stack gases with an aqueous wash liquid comprising a solution of one or more alkali metal compounds thereby to form a spent absorbent liquid containing the bisulfite, sulfite and sulfate salts of said alkali metal and then subsequently recovering at least a portion of the alkali metal ion values by reacting said bisulfite, sulfite and sulfate salts in said spent absorbent liquid with one or more calcium compounds to precipitate calcium sulfite and calcium sulfate, the improvement comprising (1) carrying out the step of reacting said bisulfite, sulfite and sulfate salts with said calcium compounds in multiple stages, said spent absorbent liquid introduced into the first stage having a total oxidizable sulfur concentration of at least about 0.1 molar, a ratio of bisulfite to sulfite ions of at lest one and a sulfate ion concentration of between about 0.1 and 2.8 molar whereby the reaction conditions of said first of said multiple stages are maintained to effect the precipitation of a solids mixture of calcium sulfate and calcium sulfite in said first stage, said solids mixture having greatly enhanced settling and filtration characteristics, (2) limiting the mean residence time of said solids mixture in said first stage to not more than 30 minutes, and (3) transferring at least a portion of said solids mixture of calcium sulfate and calcium sulfite formed in said first stage to one or more succeeding stages to serve as seed crystals for the further precipitation of calcium salts.
Claim 3
Dependent Claim
21 words
A process in accordance with claim 1 wherein said spent absorbent liquor has a pH from between about 4.5 and 6.8.
Claim 4
Dependent Claim
71 words
A process in accordance with claim 1 including the step of separating out that portion of said solids mixture formed in said first of said multiple stages not transferred to said one or more succeeding stages along with solids formed in said one or more suceeding stages from said spent absorbent liquid to form a regenerated wash liquid suitable, with the addition of any required make-up alkali metal values, for recycling.
Claim 5
Dependent Claim
41 words
A process in accordance with claim 3 wherein said first of said multiple stages includes an auxiliary first stage, the reaction conditions and solids mixture residence time in which are essentially the same as in said first of said multiple stages.
Claim 6
Dependent Claim
27 words
A process in accordance with claim 4 including the step of separating out the solids mixture formed in said auxiliary first stage from said spent absorbent liquid.
Claim 7
Dependent Claim
54 words
A process in accordance with claim 5 wherein said step of separating out said solids mixture formed in said auxiliary first stage from said spent absorbent liquid is performed separately from said step of separating out said solids formed in said first and said one or more succeeding stages from said spent absorbent liquid.
Claim 8
Dependent Claim
47 words
A process in accordance with claim 5 wherein said solids mixture and said spent absorbent liquid from said auxiliary first stage are added to said solids mixture and said spent absorbent liquid from said first and said one or more succeeding stages prior to said separating step.
Claim 9
Dependent Claim
21 words
A process in accordance with claim 1 wherein said alkali metal is sodium and said alkali metal compound is sodium hydroxide.
Claim 10
Dependent Claim
20 words
A process in accordance with claim 1 wherein said calcium compound is calcium hydroxide, calcium carbonate or a 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) | 1979-03-16 | 1979-09-15 | 1980-03-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-03-16 | 1983-09-15 | 1984-03-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-03-16 | 1987-09-15 | 1988-03-16 | $7700.00 | Window Closed / Lapsed |