US4452699A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of improving the SVI of mixed liquor in aeration tank
Assignee: Shinryo Air Conditioning Co Ltd
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Filing: 1982-04-28
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Granted: 1984-06-05
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Expires: 2002-04-28
Abstract
Abstract In the treatment of wastewater by the activated sludge process, mixed liquor in the aeration tank or settled sludge is drawn from the system and concentrated. The concentrated sludge is returned to the aeration tank either immediately or after being mixed with separated water and settled sludge to thereby reduce the SVI of the mixed liquor in the aeration tank.
Inventors
- 👤 Akira Suzuki
- 👤 Yasumi Shioya
- 👤 Keiichi Kimura
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 21:18
CPC Classifications
C; C02; C02F; C02F11/00; C02F11/12; C02F11/121; C02F11/123; C02F1/00; C02F1/24; C02F3/00; C02F3/02; C02F3/12; C02F3/1205; C02F3/1215; Y; Y02; Y02W; Y02W10/00; Y02W10/10
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
237 words
A method for improving the SVI of mixed liquor in the aeration tank of an activated sludge plant which includes said aeration tank and a sedimentation tank, which comprises the setps of: (a) introducing to a concentration line comprising a combination of an atmospheric flotation concentrator and a roll press type dehydrator, at least one component from the group consisting of mixed liquor in said aeration tank, mixed liquor drawn from a line connecting the aeration tank to a sedimentation tank and settled sludge flowing out of the sedimentation tank; thereby producing concentrated sludge having a solid content ranging from 4% to 12% by weight, wherein said atmospheric flotation concentrator includes (i) a foaming zone for blowing air under atmospheric pressure into a liquid phase containing a coagulant and a foaming agent, (ii) a mixing zone for mixing bubbles formed in the foaming zone with at least one component from the group consisting of the mixed liquor in the aeration tank, the mixed liquor drawn from a line connecting the aeration tank to the sedimentation tank and the settled sludge flowing out of the sedimentation tank, and (iii) a flotation tank for separating the mixture resulting in step (ii) into concentrated sludge and separated water, and further concentrating the concentrated sludge flowing out of said atmospheric flotation concentrator by said roll press dehydrator; and (b) returning said concentrated sludge and said separated water to said aeration tank.
Claim 2
Independent Claim
237 words
A method for improving the SVI of mixed liquor in the aeration tank of an activated sludge plant which includes said aeration tank and a sedimentation tank, which comprises the setps of: (a) introducing to a concentration line comprising a combination of an atmospheric flotation concentrator and a roll press type dehydrator, at least one component from the group consisting of mixed liquor in said aeration tank, mixed liquor drawn from a line connecting the aeration tank to a sedimentation tank and settled sludge flowing out of the sedimentation tank; thereby producing concentrated sludge having a solid content ranging from 4% to 12% by weight, wherein said atmospheric flotation concentrator includes (i) a foaming zone for blowing air under atmospheric pressure into a liquid phase containing a coagulant and a foaming agent, (ii) a mixing zone for mixing bubbles formed in the foaming zone with at least one component from the group consisting of the mixed liquor in the aeration tank, the mixed liquor drawn from a line connecting the aeration tank to the sedimentation tank and the settled sludge flowing out of the sedimentation tank, and (iii) a flotation tank for separating the mixture resulting in step (ii) into concentrated sludge and separated water, and further concentrating the concentrated sludge flowing out of said atmospheric flotation concentrator by said roll press dehydrator; and (b) returning said concentrated sludge and said separated water to said aeration tank.
Claim 3
Dependent Claim
39 words
A method according to claim 1 wherein the amount of solids being returned from said concentration line to said aeration tank is at least 5% of the amount of total solids in the mixed liquor in said aeration tank.
Claim 4
Dependent Claim
14 words
A method according to claim 1 wherein said coagulant is a cationic polymeric flocculant.
Claim 5
Dependent Claim
85 words
A method according to claim 1 wherein before returning the concentrated sludge and separated water in step (b), said concentrated sludge and separated water, as well as at least one from the group consisting of the settled sludge, mixed liquor in the aeration tank and mixed liquor drawn from a line connecting the aeration tank to the sedimentation tank are directed to a mixing tank, and at least part of the mixed sludge flowing out of the mixing tank is returned to the aeration tank.
Claim 6
Dependent Claim
20 words
A method according to claim 4 wherein said concentrated sludge has a solids content between 8 and 12% by weight.
Claim 7
Dependent Claim
22 words
A method according to claim 4 wherein the mixing tank is fed with only the concentrated sludge, separated water and settled sludge.
Claim 8
Dependent Claim
24 words
A method according to claim 4 wherein all of the mixed sludge flowing out of the mixing tank is returned to the aeration tank.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-06-05 | 1987-12-05 | 1988-06-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-06-05 | 1991-12-05 | 1992-06-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-06-05 | 1995-12-05 | 1996-06-05 | $7700.00 | Window Closed / Lapsed |