Patent US4632810A successfully refreshed from Google Patents.
US4632810A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for treating waste gas to separate and recover gypsum and dust therein
Assignee: Mitsubishi Heavy Industries Ltd
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Filing: 1985-02-27
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Granted: 1986-12-30
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Expires: 2005-02-27
Abstract
Abstract The present invention is directed to a method for treating a waste gas to separate and recover gypsum and a dust therein, characterized by comprising the steps of causing the waste gas to pass through a dry dust collector; introducing the gas into a gas absorber, in which a slurry containing at least one of calcium hydroxide or calcium carbonate as an absorbent is employed to remove SO 2 and the dust passed through the dry dust collector from the waste gas; blowing air into the resultant absorbing liquid in the gas absorber to oxidize the absorbing liquid and to thereby produce gypsum; delivering them to an absorbing liquid tank, in which the slurry mainly containing the gypsum grains is separated from the other slurry mainly containing the dust by partition walls disposed therein; and directly taking out the respective slurries separately from the absorbing liquid tank.
Inventors
- 👤 Naoharu Shinoda
- 👤 Atsushi Tatani
- 👤 Naohiko Ukawa
- 👤 Masakazu Onizuka
- 👤 Taku Shimizu
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 09:26
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: 3
Claim 1
Independent Claim
254 words
A process of treating waste gas which includes, dust and SO 2 , comprising the steps of: (a) spraying a slurry mainly containing dust into waste gas on the upstream side of a dry dust collector, (b) removing coarse dust and dried solid material resulting from spraying in step (a) while the waste gas flows through said dry dust collector, thereafter introducing the waste gas into a wet type absorbing unit, feeding said wet type absorbing unit with at least one of calcium hydroxide and calcium carbonate which serve as absorbent, thus removing SO 2 in the waste gas and fine dust in the wet type absorbing unit, said fine dust being such that it has passed through said dry dust collector, (c) blowing air into an absorbing liquid tank in which absorbing liquid to be fed to the wet type absorbing unit is stored, oxidizing said absorbing liquid to produce gypsum and preparing absorbing liquid in which a second slurry of fine dust particles and gypsum particles is contained, and (d) separating first slurry and second slurry from the thus prepared absorbing liquid while the latter is kept in the stirred state with a partition disposed in the absorbing liquid tank, said first slurry including mainly gypsum particles and said second slurry including mainly fine dust particles, thereafter taking out both of the first and second slurry separately from the absorbing liquid tank, and delivering said second slurry to step (a) without requiring treatment of drainage waste water and sludge in the process.
Claim 2
Dependent Claim
254 words
A process of treating waste gas which includes, dust and SO 2 , comprising the steps of: (a) spraying a slurry mainly containing dust into waste gas on the upstream side of a dry dust collector, (b) removing coarse dust and dried solid material resulting from spraying in step (a) while the waste gas flows through said dry dust collector, thereafter introducing the waste gas into a wet type absorbing unit, feeding said wet type absorbing unit with at least one of calcium hydroxide and calcium carbonate which serve as absorbent, thus removing SO 2 in the waste gas and fine dust in the wet type absorbing unit, said fine dust being such that it has passed through said dry dust collector, (c) blowing air into an absorbing liquid tank in which absorbing liquid to be fed to the wet type absorbing unit is stored, oxidizing said absorbing liquid to produce gypsum and preparing absorbing liquid in which a second slurry of fine dust particles and gypsum particles is contained, and (d) separating first slurry and second slurry from the thus prepared absorbing liquid while the latter is kept in the stirred state with a partition disposed in the absorbing liquid tank, said first slurry including mainly gypsum particles and said second slurry including mainly fine dust particles, thereafter taking out both of the first and second slurry separately from the absorbing liquid tank, and delivering said second slurry to step (a) without requiring treatment of drainage waste water and sludge in the process.
Claim 3
Dependent Claim
19 words
The process of claim 1 wherein a baffle board is provided in liquid chamber defined by said partition wall.
References Cited (Backward Citations)
US3903243A
Cited
US3929968A
Cited
US4080428A
Cited
US4487784A
Cited
DE3218470A1
Cited
US4579069A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-12-29 | 1990-06-30 | 1990-12-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-12-29 | 1994-06-30 | 1994-12-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-12-29 | 1998-06-30 | 1998-12-30 | $7700.00 | Window Closed / Lapsed |