Patent US3977965A successfully refreshed from Google Patents.
US3977965A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of biological purification of sewage
Assignee: Akavadan AS
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Filing: 1975-01-27
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Granted: 1976-08-31
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Expires: 1995-01-27
Abstract
Abstract A method of biological purification of sewage in a purification plant in order to decompose organic material and in order to remove inorganic compounds, mainly nitrogen compounds, wherein the plant comprises three tanks only, of which at least two sequentially serve as a feeding tank for the sewage and at least one as a clarification tank, and wherein the sewage at any time is subjected to an aerobic treatment in the plant by means of aeration and simultaneous circulation of the sewage, and wherein a tank, which during a period serves as feeding tank, at least during a part of such period is driven in such a manner that sewage is only circulated, substantially, under anaerobic conditions, the tank being indirectly connected, during at least said part of said period, to a tank serving as clarification tank, viz. via the tank not serving as clarification tank, and by establishing aerobic conditions in a tank after each anaerobic treatment therein and before it is used as clarification tank or is connected to a tank, serving as clarification tank.
Inventors
- 👤 Bent Kure Tholander
- 👤 Svend Krarup
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 20:04
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/02; C02F3/12; C02F3/1236; C02F3/1257; C02F3/1263; C02F3/30; C02F3/301; C02F3/302; Y; Y02; Y02W; Y02W10/00; Y02W10/10; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
616 words
A method for biologically purifying sewage utilizing a first, a second and a third treatment tank, said method comprising: coupling said tanks in a first series flow-arrangement, in which said first tank serves as the initial tank, said second tank as the middle tank and said third tank as the final tank and, during a first phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said second tank and from said second tank to said third tank; during a portion of said first phase, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and, during another portion of said first phase, treating the sewage in said first tank for denitrification by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said first tank as an energy source for said denitrification, during said first phase, moreover, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said first phase by uncoupling said first tank from said first series flow-arrangement and, thereafter, during a second phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said third tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank, while continuing to treat the sewage in said uncoupled first tank for nitrification by circulating the sewage under aerobic conditions; terminating said second phase by re-arranging said tanks in a second series flow-arrangement, in which said second tank serves as the initial tank, said first tank as middle tank and said third tank as the final tank and during a third phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said first tank and from said first tank to said third tank; during a portion of said third phase, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and, during another portion of said third phase, treating the sewage in said second tank for denitrification by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said second tank as an energy source for said denitrification, during said third phase, moreover, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrate from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said third phase by uncoupling said second tank from said second series flow-arrangement and thereafter, during a fourth phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said third tank, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank, while continuing to treat the sewage in said uncoupled second tank for nitrification by circulating the sewage under aerobic conditions; terminating said fourth phase by rearranging said tanks in said first series flow-arrangement and repeating the method.
Claim 2
Independent Claim
616 words
A method for biologically purifying sewage utilizing a first, a second and a third treatment tank, said method comprising: coupling said tanks in a first series flow-arrangement, in which said first tank serves as the initial tank, said second tank as the middle tank and said third tank as the final tank and, during a first phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said second tank and from said second tank to said third tank; during a portion of said first phase, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and, during another portion of said first phase, treating the sewage in said first tank for denitrification by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said first tank as an energy source for said denitrification, during said first phase, moreover, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said first phase by uncoupling said first tank from said first series flow-arrangement and, thereafter, during a second phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said third tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank, while continuing to treat the sewage in said uncoupled first tank for nitrification by circulating the sewage under aerobic conditions; terminating said second phase by re-arranging said tanks in a second series flow-arrangement, in which said second tank serves as the initial tank, said first tank as middle tank and said third tank as the final tank and during a third phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said first tank and from said first tank to said third tank; during a portion of said third phase, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and, during another portion of said third phase, treating the sewage in said second tank for denitrification by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said second tank as an energy source for said denitrification, during said third phase, moreover, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrate from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said third phase by uncoupling said second tank from said second series flow-arrangement and thereafter, during a fourth phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said third tank, treating the sewage in said first tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank, while continuing to treat the sewage in said uncoupled second tank for nitrification by circulating the sewage under aerobic conditions; terminating said fourth phase by rearranging said tanks in said first series flow-arrangement and repeating the method.
Claim 3
Dependent Claim
97 words
A method as set forth in claim 1, wherein the sewage in said first tank is treated for nitrification by circulating the sewage under aerobic conditions during a first portion of said first phase and for denitrification by circulating the sewage under anaerobic conditions during the remaining portion of said first phase, and wherein the sewage in said second tank is treated for nitrification by circulating the sewage under aerobic conditions during a first portion of said third phase and for denitrification by circulating the sewage under anaerobic conditions during the remaining portion of said third phase.
Claim 4
Independent Claim
607 words
A method for biologically purifying sewage utilizing a first, a second and a third treatment tank, said method comprising: coupling said tanks in a first series flow-arrangement in which said first tank serves as the initial tank, said second tank as the middle tank and said third tank as the final tank and, during a first phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said second tank and from said second tank to said third tank; during said first phase treating the sewage in said first tank for denitrification of nitrates present therein by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said first tank as an energy source for said denitrification, during said first phase, moreover, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said first phase by uncoupling said first tank from said first series flow-arrangement and, thereafter, during a second phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said third tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank and, during a first portion of said second phase, treating the sewage in said uncoupled first tank for nitrification by circulating the sewage under aerobic conditions and, during the remaining portion of said second phase treating the sewage in said uncoupled first tank for clarification; terminating said second phase by rearranging said tanks in a second series flow-arrangement in which said third tank serves as the initial tank, said second tank as the middle tank and said first tank as the final tank, and during a third phase of the process, feeding raw sewage to said third tank and transferring sewage from said third tank to said second tank and from said second tank to said first tank; during said third phase, treating the sewage in said third tank for denitrification of nitrates present therein by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said third tank as an energy source for said denitrification, during said third phase moreover treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said first tank for clarification and removing clarified water from said first tank; terminating said third phase by uncoupling said third tank from said second series flow-arrangement and thereafter, during a fourth phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said first tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said first tank for clarification and removing clarified water from said first tank and, during a first portion of said fourth phase, treating the sewage in said uncoupled third tank for nitrification by circulating the sewage under aerobic conditions and, during the remaining portion of said second phase treating the sewage in said uncoupled third tank for clarification, rearranging said tanks at the end of said fourth phase in said first series flow-arrangement and repeating the method.
Claim 5
Independent Claim
607 words
A method for biologically purifying sewage utilizing a first, a second and a third treatment tank, said method comprising: coupling said tanks in a first series flow-arrangement in which said first tank serves as the initial tank, said second tank as the middle tank and said third tank as the final tank and, during a first phase of the process, feeding raw sewage to said first tank and transferring sewage from said first tank to said second tank and from said second tank to said third tank; during said first phase treating the sewage in said first tank for denitrification of nitrates present therein by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said first tank as an energy source for said denitrification, during said first phase, moreover, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said third tank for clarification and removing clarified water from said third tank; terminating said first phase by uncoupling said first tank from said first series flow-arrangement and, thereafter, during a second phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said third tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said third tank for clarification and removing clarified water from said third tank and, during a first portion of said second phase, treating the sewage in said uncoupled first tank for nitrification by circulating the sewage under aerobic conditions and, during the remaining portion of said second phase treating the sewage in said uncoupled first tank for clarification; terminating said second phase by rearranging said tanks in a second series flow-arrangement in which said third tank serves as the initial tank, said second tank as the middle tank and said first tank as the final tank, and during a third phase of the process, feeding raw sewage to said third tank and transferring sewage from said third tank to said second tank and from said second tank to said first tank; during said third phase, treating the sewage in said third tank for denitrification of nitrates present therein by circulating the sewage under anaerobic conditions while utilizing raw sewage received by said third tank as an energy source for said denitrification, during said third phase moreover treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage and treating the sewage in said first tank for clarification and removing clarified water from said first tank; terminating said third phase by uncoupling said third tank from said second series flow-arrangement and thereafter, during a fourth phase of the process, feeding raw sewage to said second tank and transferring sewage from said second tank to said first tank, treating the sewage in said second tank for nitrification by circulating the sewage under aerobic conditions so as to produce nitrates from the sewage, treating the sewage in said first tank for clarification and removing clarified water from said first tank and, during a first portion of said fourth phase, treating the sewage in said uncoupled third tank for nitrification by circulating the sewage under aerobic conditions and, during the remaining portion of said second phase treating the sewage in said uncoupled third tank for clarification, rearranging said tanks at the end of said fourth phase in said first series flow-arrangement and repeating the method.
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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) | 1979-08-31 | 1980-03-01 | 1980-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-08-31 | 1984-03-01 | 1984-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-08-31 | 1988-03-01 | 1988-08-31 | $7700.00 | Window Closed / Lapsed |