Patent US5022993A successfully refreshed from Google Patents.
US5022993A
Expired / Lapsed
US
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Process for treating wastewater
Assignee: Orange Water and Sewer Authority
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Filing: 1989-08-04
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Granted: 1991-06-11
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Expires: 2009-08-04
Abstract
Abstract The present invention entails a process for treating wastewater utilizing a return activated sludge process. Primary sludge is separated from the wastewater stream and conveyed into a fermentation tank and held a sufficient time to permit hydrolysis of suspended solids so as to produce soluble substrates. Part of the soluble substrates are mixed with nutrified return activated sludge and held for a selected time period to form conditioned return activated sludge. Thereafter, the conditioned return activated sludge is mixed in an initial aerobic treatment zone with pretreated wastewater. Thereafter, the mixed conditioned return activated sludge and pretreatd wastewater is conveyed through a series of treatment zones, which includes at least one anoxic treatment zone, to which part of the soluble substrates are added, where nitrogen and other pollutants are removed from the wastewater.
Inventors
- 👤 Ronald E. Williamson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 20:27
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/02; C02F3/12; C02F3/1205; C02F3/1215; C02F3/04; C02F3/30; C02F3/308; Y; Y02; Y02W; Y02W10/00; Y02W10/10; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903; Y10S210/906
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
352 words
A process for removing both phosphorus and nitrogen from wastewater comprising the steps of: (a) directing raw sewage into a primary treatment area and treating the same and in the process separating the raw sewage into settled sewage and raw sludge; (b) directing the settled sewage in and through a main stream secondary treatment area and particularly subjecting the settled sewage to a first aerobic treatment zone, followed by an anoxic treatment zone, after which the settled sewage is subjected to a second aerobic treatment zone; (c) passing the effluent from the main stream secondary treatment area to a settling zone and separating the secondary treatment effluent into purified wastewater and settled sludge; (d) returning the settled sludge to a sidestream sludge nutrification zone that lies outside of the main stream secondary treatment area; (e) directing the separated raw sludge from the primary treatment area to a sidestream fermenter and fermenting the raw sludge to produce a fermented supernatant that includes volatile fatty acids; (f) transferring fermenter supernatant from the fermenter and splitting the fermenter supernatant into at least two streams; (g) transferring one stream of the fermenter supernatant to the sidestream nutrification zone and mixing the fermenter supernatant with the settled sludge to form conditioned activated sludge and holding the conditioned activated sludge within the nutrification zone a selected time period; (h) conveying the conditioned activated sludge to the main treatment area and particularly to the first aerobic treatment zone that precedes the anoxic treatment zone and mixing the conditioned activated sludge with the settled sewage in the first aerobic treatment zone; (i) wherein the fermenter supernatant and the volatile fatty acids associated therewith form a favorable food source for phosphorus removing microorganisms that is consumed in the nutrification zone; and (j) transferring the other stream of the fermenter supernatant to the anoxic zone in the main stream and mixing the fermenter supernatant with the settled sewage to give rise to denitrification in the anoxic zone as the volatile fatty acids associated with the fermenter supernatant provides a favorable food source that is consumed by denitrifying microorganisms in the anoxic zone.
Claim 2
Dependent Claim
352 words
A process for removing both phosphorus and nitrogen from wastewater comprising the steps of: (a) directing raw sewage into a primary treatment area and treating the same and in the process separating the raw sewage into settled sewage and raw sludge; (b) directing the settled sewage in and through a main stream secondary treatment area and particularly subjecting the settled sewage to a first aerobic treatment zone, followed by an anoxic treatment zone, after which the settled sewage is subjected to a second aerobic treatment zone; (c) passing the effluent from the main stream secondary treatment area to a settling zone and separating the secondary treatment effluent into purified wastewater and settled sludge; (d) returning the settled sludge to a sidestream sludge nutrification zone that lies outside of the main stream secondary treatment area; (e) directing the separated raw sludge from the primary treatment area to a sidestream fermenter and fermenting the raw sludge to produce a fermented supernatant that includes volatile fatty acids; (f) transferring fermenter supernatant from the fermenter and splitting the fermenter supernatant into at least two streams; (g) transferring one stream of the fermenter supernatant to the sidestream nutrification zone and mixing the fermenter supernatant with the settled sludge to form conditioned activated sludge and holding the conditioned activated sludge within the nutrification zone a selected time period; (h) conveying the conditioned activated sludge to the main treatment area and particularly to the first aerobic treatment zone that precedes the anoxic treatment zone and mixing the conditioned activated sludge with the settled sewage in the first aerobic treatment zone; (i) wherein the fermenter supernatant and the volatile fatty acids associated therewith form a favorable food source for phosphorus removing microorganisms that is consumed in the nutrification zone; and (j) transferring the other stream of the fermenter supernatant to the anoxic zone in the main stream and mixing the fermenter supernatant with the settled sewage to give rise to denitrification in the anoxic zone as the volatile fatty acids associated with the fermenter supernatant provides a favorable food source that is consumed by denitrifying microorganisms in the anoxic zone.
Claim 3
Dependent Claim
44 words
The method of claim 1 wherein the series of treatment zones includes a series of anoxic treatment zones and wherein the process includes directing portions of the produced volatile fatty acids to each of the series of anoxic treatment zones to achieve effective denitrification.
Claim 4
Dependent Claim
90 words
The method of claim 1 including the step of passing the settled sewage through a fixed film reactor prior to the settled sewage being directed through the secondary treatment area, resulting in the removal of BOD from the sewage prior to the sewage being directed to the anoxic treatment zone thereby resulting in a relatively low BOD concentration in the settled sewage just prior to its entry into the anoxic zone compared to the BOD concentration of the settled sewage prior to its being passed through the fixed film reactor.
References Cited (Backward Citations)
US2517792A
Cited
US3300402A
Cited
US3654147A
Cited
US3930998A
Cited
US4141822A
Cited
JPS5389259A
Cited
DD137919A1
Cited
US4487697A
Cited
US4267038A
Cited
US4664804A
Cited
US4874519A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1994-06-10 | 1994-12-10 | 1995-06-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-06-10 | 1998-12-10 | 1999-06-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-06-10 | 2002-12-10 | 2003-06-11 | $7700.00 | Window Closed / Lapsed |