US4655925A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Activated sludge method
Assignee: Nishihara Environment Co Ltd
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Filing: 1985-01-18
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Granted: 1987-04-07
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Expires: 2005-01-18
Abstract
Abstract A method of removing nitrogen and phosphorus from waste water by using an activated sludge including aerobic bacteria is disclosed. The waste water is fed continuously and gradually into a treatment basin in which the sludge is contained so that a mixed liquor consisting of the waste water and the sludge is formed therein. A cycle consisting of an agitating step and an aerating step is repeated at least two times and each cycle is finished within two hours, with the ratio of the agitating time to the aerating time being between one to one and to one. In the agitating step, the mixed liquor presents an anoxic condition and a succeeding anaerobic condition. Denitrification occurs in the anoxic condition and the aerobic bacteria release phosphorus in the anaerobic condition. During the aerating step, nitrification is caused while the bacteria excessively ingest phosphorus from the mixed liquor.
Inventors
- 👤 Shin-ichi Tabata
- 👤 Tomio Suzuki
- 👤 Youichi Hamamoto
- 👤 Noboru Hayakawa
- 👤 Kaoru Watanabe
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:48
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/02; C02F3/12; C02F3/1205; C02F3/1215; C02F3/1236; C02F3/1263; C02F3/30; C02F3/301; C02F3/308; G; G01; G01N; G01N33/00; G01N33/18; G01N33/1806; Y; Y02; Y02W; Y02W10/00; Y02W10/10; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903; Y10S210/906
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
226 words
A method of removing nitrogen and phosphorus from waste water by using activated sludge including aerobic bacteria and changing alternately operational modes in a treatment basin, in accordance with a time schedule, which comprises the steps of: adding the waste water continuously and gradually into a mixed liquor in a treatment basin which consists of the waste water and the sludge; agitating the mixed liquor in said treatment basin during continuous and gradual adding of the waste water until it presents an anoxic condition and a succeeding anaerobic condition so that denitrification is caused in the anoxic condition and phosphorus is then released from the sludge in the anaerobic condition; aerating the mixed liquor in the aerobic condition during the continuous and gradual adding of the waste water into the mixed liquor in the aerobic condition so that nitrification is accomplished while phosphorus is ingested by the sludge; repeating a cycle consisting of said agitating and aerating steps at least two times so that each cycle is finished within two hours, the ratio of the agitating time to the aerating time being between one to one and five to one; settling the agitated and aerated mixed liquor for separating it into a supernatant liquid and the sludge; and discharging the supernatant liquid as an effluent and reusing the settled sludge for the treatment of waste water.
Claim 2
Independent Claim
226 words
A method of removing nitrogen and phosphorus from waste water by using activated sludge including aerobic bacteria and changing alternately operational modes in a treatment basin, in accordance with a time schedule, which comprises the steps of: adding the waste water continuously and gradually into a mixed liquor in a treatment basin which consists of the waste water and the sludge; agitating the mixed liquor in said treatment basin during continuous and gradual adding of the waste water until it presents an anoxic condition and a succeeding anaerobic condition so that denitrification is caused in the anoxic condition and phosphorus is then released from the sludge in the anaerobic condition; aerating the mixed liquor in the aerobic condition during the continuous and gradual adding of the waste water into the mixed liquor in the aerobic condition so that nitrification is accomplished while phosphorus is ingested by the sludge; repeating a cycle consisting of said agitating and aerating steps at least two times so that each cycle is finished within two hours, the ratio of the agitating time to the aerating time being between one to one and five to one; settling the agitated and aerated mixed liquor for separating it into a supernatant liquid and the sludge; and discharging the supernatant liquid as an effluent and reusing the settled sludge for the treatment of waste water.
Claim 3
Dependent Claim
44 words
The method as set forth in claim 1, wherein said settling step is conducted in said treatment basin while the feeding of the waste water thereinto is stopped, and a part of the settled sludge is drawn out from said treatment basin, if necessary.
Claim 4
Dependent Claim
43 words
The method as set forth in claim 2, wherein during said aerating step, the feeding rate of air is controlled so as to adjust the concentration of dissolved oxygen in the mixed liquor to a predetermined value for ensuring denitrification and phosphorus removal.
Claim 5
Dependent Claim
44 words
The method as set forth in claim 1, wherein said settling step is performed in said treatment basin while the feeding of the waste water thereinto is continued, and a part of the settled sludge is drawn out from said treatment basin, if necessary.
Claim 6
Dependent Claim
43 words
The method as set forth in claim 4, wherein during said aerating step, the feeding rate of air is controlled so as to adjust the concentration of dissolved oxygen in the mixed liquor to a predetermined value for ensuring denitrification and phosphorus removal.
Claim 7
Dependent Claim
43 words
The method as set forth in claim 1, wherein during said aerating step, the feeding rate of air is controlled so as to adjust the concentration of dissolved oxygen in the mixed liquor to a predetermined value for ensuring denitrification and phosphorus removal.
Claim 8
Dependent Claim
50 words
The method as set forth in claim 1, wherein said agitated and aerated mixed liquor is transferred to a settling basin and said settling step is performed therein, whereby the waste water is continuously treated, the settled sludge being returned to said treatment basin for the treatment of waste water.
Claim 9
Dependent Claim
43 words
The method as set forth in claim 7, wherein during said aerating step, the feeding rate of air is controlled so as to adjust the concentration of dissolved oxygen in the mixed liquor to a predetermined value for ensuring denitrification and phosphorus removal.
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) | 1990-04-06 | 1990-10-06 | 1991-04-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-04-06 | 1994-10-06 | 1995-04-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-04-06 | 1998-10-06 | 1999-04-07 | $7700.00 | Window Closed / Lapsed |