Patent US4134830A successfully refreshed from Google Patents.
US4134830A
Expired / Lapsed
US
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Method of purifying waste water
Assignee: Svenska Sockerfabriks AB
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Filing: 1977-08-18
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Granted: 1979-01-16
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Expires: 1997-08-18
Abstract
Abstract A method of biologically purifying waste water rich in carbohydrates or proteins, wherein the waste water is treated in an anaerobic stage while leading off generated methane gas, sludge-bearing water formed being subjected to sludge separation during formation of a first sludge concentrate which is returned to the anaerobic stage, and that the water thus treated is treated in an aerobic stage, sludge-bearing water formed being subjected to slude separation during formation of a second sludge concentrate, of which at least a portion is returned to the aerobic stage, while possible excess is returned to the anaerobic stage, a portion of the first, and possibly also of the second sludge concentrate being led off for disposal.
Inventors
- 👤 Harald Skogman
- 👤 Lennart Huss
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 03:19
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/30; C02F3/28; Y; Y02; Y02E; Y02E50/00; Y02E50/30
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
164 words
A method of biologically purifying waste water rich in carbohydrates or proteins comprising: (a) subjecting the waste water to an anaerobic fermentation state wherein the waste water is biologically treated with methane producing organisms under anaerobic conditions wherein substantial portions of methane gas are generated and a first sludge-bearing water is produced; (b) collecting said generated methane gas; (c) leading off said generated methane gas; (d) subjecting said first sludge-bearing water to sludge separation to form a first sludge concentrate and a first aqueous effluent; (e) returning said first sludge concentrate to the anaerobic fermentation state; (f) subjecting said first aqueous effluent to an aerobic fermentation stage to form a second sludge-bearing water; (g) subjecting said second sludge-bearing water to sludge separation to form a second sludge concentrate; (h) returning a fraction of said second sludge concentrate to the aerobic fermentation stage, returning the remainder of said second sludge concentrate to the anarerobic fermentation stage; and (i) discharging said first sludge concentrate for disposal.
Claim 2
Independent Claim
164 words
A method of biologically purifying waste water rich in carbohydrates or proteins comprising: (a) subjecting the waste water to an anaerobic fermentation state wherein the waste water is biologically treated with methane producing organisms under anaerobic conditions wherein substantial portions of methane gas are generated and a first sludge-bearing water is produced; (b) collecting said generated methane gas; (c) leading off said generated methane gas; (d) subjecting said first sludge-bearing water to sludge separation to form a first sludge concentrate and a first aqueous effluent; (e) returning said first sludge concentrate to the anaerobic fermentation state; (f) subjecting said first aqueous effluent to an aerobic fermentation stage to form a second sludge-bearing water; (g) subjecting said second sludge-bearing water to sludge separation to form a second sludge concentrate; (h) returning a fraction of said second sludge concentrate to the aerobic fermentation stage, returning the remainder of said second sludge concentrate to the anarerobic fermentation stage; and (i) discharging said first sludge concentrate for disposal.
Claim 3
Dependent Claim
58 words
The method of claim 1 wherein the waste water is rich in proteins, wherein ammonium ions are formed in the anaerobic fermentation stage, and wherein before the first aqueous effluent is subjected to the aerobic fermentation stage, partly removing said ammonium ions to such a degree that nutritional salt balance is maintained for fermentation in the aerobic stage.
Claim 4
Dependent Claim
26 words
The method of claim 2, wherein the ammonium ions are removed by adding alkali to the first aqueous effluent and driving off the ammonia released thereby.
Claim 5
Dependent Claim
20 words
The method of claim 3, wherein the amount of alkali is adjusted so that a pH of 9-11 is obtained.
Claim 6
Dependent Claim
25 words
The method of claim 3, wherein the ammonia released in the first aqueous effluent is driven off by blowing air through said first aqueous effluent.
Claim 7
Dependent Claim
21 words
The method of claim 2, wherein the ammonium ions are removed by passing the first aqueous effluent through a cation exchanger.
Claim 8
Dependent Claim
13 words
The method of claim 6, wherein a sodium saturated cation exchanger is used.
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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) | 1982-01-15 | 1982-07-17 | 1983-01-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-15 | 1986-07-17 | 1987-01-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-15 | 1990-07-17 | 1991-01-16 | $7700.00 | Window Closed / Lapsed |