US4897196A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Two-stage batch wastewater treatment
Assignee: US Filter Zimpro Inc
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Filing: 1988-02-17
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Granted: 1990-01-30
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Expires: 2008-02-17
Abstract
Abstract A two-stage, batch process for purifying wastewater containing organic and adsorbable pollutants includes the steps of introducing a predetermined quantity of the wastewater into an aeration and settling zone (12) of a primary treatment zone (10) and aerating said wastewater therein in the presence of a powdered adsorbent, such as activated carbon, and biologically active solids, terminating aeration and retaining the thus-treated wastewater in the aeration and settling zone (12) a sufficient time for a substantial portion of the suspended solids to settle by gravity. A predetermined amount of the partially-treated wastewater is withdrawn (26) from the aeration and settling zone (12) and introduced into a contact zone (28) wherein it is agitated, preferably by aeration, in the presence of a powdered adsorbent, agitation is terminated and the solids are allowed to settle by gravity. After completion of settling, clarified, substantially solids-free water is withdrawn (40) from the contact zone (28).
Inventors
- 👤 William M. Copa
- 👤 Thomas J. Vollstedt
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:56
CPC Classifications
C; C02; C02F; C02F9/00; C02F3/00; C02F3/02; C02F3/08; C02F3/085; C02F3/006; C02F3/12; C02F3/1205; C02F3/121; C02F3/1215; C02F3/1236; C02F3/1263; C02F2209/00; C02F2209/42; C02F2209/44; Y; Y02; Y02W; Y02W10/00; Y02W10/10
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
219 words
A process for purifying wastewater containing organic and adsorbable pollutants comprising the steps of: (a) introducing a predetermined quantity of the wastewater into a primary treatment zone including an aeration and settling zone; (b) aerating the wastewater in said aeration and settling zone with an oxygen-containing gas in the presence of sufficient amounts of a powdered adsorbent and biologically active solids to reduce the BOD, COD and TOC to desired levels; (c) terminating aeration and retaining said thus-treated wastewater in said aerating and settling zone a sufficient time for solids therein to settle by gravity and produce a first solids phase and a first aqueous phase containing a maximum predetermined amount of said solids; (d) withdrawing a predetermined amount of said first aqueous phase from said aeration and settling zone and transferring same into a contact zone; (e) agitating said first aqueous phase in said-contact zone in the presence of a powdered adsorbent for an agitation period sufficient to reduce the BOD, COD and TOC to desired levels; (f) terminating agitation and allowing solids in said thus-treated first aqueous phase to settle by gravity for a settling period sufficient to produce a clarified, substantially solids-free, second aqueous phase and a second solids phase; and (g) thereafter withdrawing a predetermined amount of said second aqueous phase from said contact zone.
Claim 2
Dependent Claim
219 words
A process for purifying wastewater containing organic and adsorbable pollutants comprising the steps of: (a) introducing a predetermined quantity of the wastewater into a primary treatment zone including an aeration and settling zone; (b) aerating the wastewater in said aeration and settling zone with an oxygen-containing gas in the presence of sufficient amounts of a powdered adsorbent and biologically active solids to reduce the BOD, COD and TOC to desired levels; (c) terminating aeration and retaining said thus-treated wastewater in said aerating and settling zone a sufficient time for solids therein to settle by gravity and produce a first solids phase and a first aqueous phase containing a maximum predetermined amount of said solids; (d) withdrawing a predetermined amount of said first aqueous phase from said aeration and settling zone and transferring same into a contact zone; (e) agitating said first aqueous phase in said-contact zone in the presence of a powdered adsorbent for an agitation period sufficient to reduce the BOD, COD and TOC to desired levels; (f) terminating agitation and allowing solids in said thus-treated first aqueous phase to settle by gravity for a settling period sufficient to produce a clarified, substantially solids-free, second aqueous phase and a second solids phase; and (g) thereafter withdrawing a predetermined amount of said second aqueous phase from said contact zone.
Claim 3
Dependent Claim
36 words
A process according to claim 1 wherein the total amount of adsorbent and biologically active solids present in said aeration and settling zone is about 10 to about 50,000 parts per million parts of the wastewater.
Claim 4
Dependent Claim
31 words
A process according to claim 2 wherein the amount of said adsorbent present in the aeration and settling zone is about 5 to about 20,000 parts per million of the wastewater.
Claim 5
Dependent Claim
12 words
A process according to claim 3 wherein said adsorbent is activated carbon.
Claim 6
Dependent Claim
30 words
A process according to claim 1 including the step of adding to said aeration and settling zone a flocculant aid for promoting settling of solids therein prior to terminating aeration.
Claim 7
Dependent Claim
14 words
A process according to claim 5 wherein said flocculant aid is a cationic polymer.
Claim 8
Dependent Claim
96 words
A process according to claim 1 wherein said primary treatment zone includes an inlet zone which is substantially isolated from and is in continuous fluid communication with said aeration and settling zone; in step (a) the wastewater continuously flows into said inlet zone at a first flow rate and passes therefrom into said agitation and settling zone; and in step (d) said first aqueous phase is withdrawn from said aeration and settling zone at a second flow rate greater than said first flow rate until said predetermined amount of said first aqueous phase has been withdrawn.
Claim 9
Dependent Claim
26 words
A process according to claim 7 wherein step (c) is commenced when the liquid level in said aeration and settling zone reaches a predetermined upper limit.
Claim 10
Dependent Claim
26 words
A process according to claim 8 wherein step (d) is continued until the liquid level of said first aqueous phase drops to a predetermined lower limit.
Claim 11
Dependent Claim
23 words
A process according to claim 1 wherein said agitation in said contact zone is carried out by introducing a pressurized oxygen-containing gas thereinto.
Claim 12
Dependent Claim
20 words
A process according to claim 1 wherein said agitation in said contact zone is carried out by mechanical agitation means.
Claim 13
Dependent Claim
36 words
A process according to claim 1 including the step of adding to said contact zone a flocculation aid for promoting settling of said adsorbent to said first aqueous phase near the end of said agitation period.
Claim 14
Dependent Claim
14 words
A process according to claim 12 wherein said flocculation aid is a cationic polymer.
Claim 15
Dependent Claim
29 words
A process according to claim 1 including the step of recycling at least a portion of said second solids phase from said contact zone to said primary treatment zone.
Claim 16
Dependent Claim
48 words
A process according to claim 14 including the step of withdrawing a portion of the mixed liquor solids phase from said primary treatment zone so as to maintain the amounts of said adsorbent and biologically active solids present in said aeration and settling zone at a predetermined level.
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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) | 1993-01-29 | 1993-07-31 | 1994-01-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-01-29 | 1997-07-31 | 1998-01-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-01-29 | 2001-07-31 | 2002-01-30 | $7700.00 | Window Closed / Lapsed |