Patent US4246102A successfully refreshed from Google Patents.
US4246102A
Expired / Lapsed
US
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Method for separating pollutants from liquid
Assignee: Rederi Nordstjernan AB
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Filing: 1977-11-28
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Granted: 1981-01-20
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Expires: 1997-11-28
Abstract
Abstract In the particular embodiment of the invention described in the specification, a liquid to be purified passes first through a screen, a sand trap, a first sedimentation basin, an aeration basin and a second sedimentation basin, and then through a final purification step for chemical admixture and passage upwardly through a particulate filter bed. The particulate filter material is circulated continuously from the bottom of the filter bed through a washing device and the cleaned particulate material is deposited at the top of the filter bed. Sludge collected from the sedimentation basins and the washing device is treated in thickeners and digesters.
Inventors
- 👤 Ulf R. Hjelmner
- 👤 Hans F. Larsson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 07:25
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/52; C02F1/5281; B; B01; B01D; B01D24/00; B01D24/02; B01D24/10; B01D24/16; B01D24/46; B01D24/4668; B01D24/4689
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
317 words
In a method for filtering wherein liquid comprising a suspension or emulsion to be filtered is supplied to a zone of particle filter medium forming a filter bed, the liquid being filtered flows, during the filtration thereof, in an upward direction through the filter bed and is discharged from the filter bed as filtrated liquid phase, and wherein the filter medium during the filtration flows in a downward direction through the filter bed in counter-current to the liquid being filtered, past the inflow of the liquid and thereafter is transported separated from the filter bed to a wash path for washing the dirty filter medium during flow along the wash path in counter-current to a wash liquid, whereupon the washed filter medium is returned to the filter bed zone to its top surface, at least a part of the filtrated liquid phase which is discharged from the filter bed zone is maintained above this zone as a zone of filtrated liquid phase in direct contact with the filter bed zone, and said counter-current washing of the dirty filter medium along the wash path takes place during flow of the dirty filter medium in counter-current to a portion of said filtrated liquid phase utilized as wash liquid, said portion of said filtrated liquid phase being supplied to the wash path from said zone of filtrated liquid phase, the improvement comprising adding to the liquid to be filtered chemicals facilitating at least one of the processes of precipitation and flocculation, continuously directing the liquid containing the chemicals from the chemical addition location directly to a zone of moving particulate filter material forming the filter bed, absent intermediate passage through any flocculation tank and absent intermediate passage through any sedimentation basin, passing the liquid containing the chemicals through the filter bed to provide at least one of the precipitation and flocculation processes within the moving particulate material of the bed.
Claim 2
Dependent Claim
317 words
In a method for filtering wherein liquid comprising a suspension or emulsion to be filtered is supplied to a zone of particle filter medium forming a filter bed, the liquid being filtered flows, during the filtration thereof, in an upward direction through the filter bed and is discharged from the filter bed as filtrated liquid phase, and wherein the filter medium during the filtration flows in a downward direction through the filter bed in counter-current to the liquid being filtered, past the inflow of the liquid and thereafter is transported separated from the filter bed to a wash path for washing the dirty filter medium during flow along the wash path in counter-current to a wash liquid, whereupon the washed filter medium is returned to the filter bed zone to its top surface, at least a part of the filtrated liquid phase which is discharged from the filter bed zone is maintained above this zone as a zone of filtrated liquid phase in direct contact with the filter bed zone, and said counter-current washing of the dirty filter medium along the wash path takes place during flow of the dirty filter medium in counter-current to a portion of said filtrated liquid phase utilized as wash liquid, said portion of said filtrated liquid phase being supplied to the wash path from said zone of filtrated liquid phase, the improvement comprising adding to the liquid to be filtered chemicals facilitating at least one of the processes of precipitation and flocculation, continuously directing the liquid containing the chemicals from the chemical addition location directly to a zone of moving particulate filter material forming the filter bed, absent intermediate passage through any flocculation tank and absent intermediate passage through any sedimentation basin, passing the liquid containing the chemicals through the filter bed to provide at least one of the precipitation and flocculation processes within the moving particulate material of the bed.
Claim 3
Dependent Claim
25 words
A method according to claim 1, including the step of homogenizing the liquid and the chemical before the liquid is supplied to the filter bed.
Claim 4
Dependent Claim
33 words
A method according to claim 2, wherein the homogenizing is accomplished by dividing the liquid flow into separate flow paths and rejoining the liquid flow before passing the liquid into the filter bed.
Claim 5
Dependent Claim
17 words
A method according to claim 2, wherein the homogenizing is accomplished by applying energy to the liquid.
Claim 6
Dependent Claim
20 words
A method according to claim 1, wherein a part of the soiled wash liquid is returned to the filtering process.
Claim 7
Dependent Claim
40 words
A method according to claim 5, wherein the soiled wash liquid is supplied to a treatment process for sludge material separated from the liquid in the filtering process, said treatment process being carried out in parallel with the filtering process.
Claim 8
Dependent Claim
29 words
A method according to claim 6, wherein a part of the soiled liquid being treated in the treatment process is the liquid that is returned to the filtering process.
Claim 9
Dependent Claim
36 words
A method according to claim 1, including the step of causing the relative velocity between the filter particles and the wash liquid to be increased instantaneously at least once during the washing of said filter particles.
Claim 10
Dependent Claim
26 words
A method according to claim 1, wherein the flow velocity of the filter particles is decelerated at least once during the washing of said filter medium.
Claim 11
Dependent Claim
30 words
A method according to claim 1, wherein the deceleration of the filter particles is followed by the instantaneous increase in relative velocity of the filter particles and the wash liquid.
Claim 12
Dependent Claim
44 words
In the method according to claim 1, an improved liquid purification step comprising monitoring at least one operating characteristic of the filter, and controlling the dosage of the chemicals added to the liquid in said step of adding chemicals responsive to the characteristic monitored.
Claim 13
Dependent Claim
57 words
The method according to claim 11, wherein the step of continuously removing soiled particles includes supplying air to lift the soiled particles upwards apart from and through the bed to a particle washing means, sensing at least one of the operating characteristics of the filter and controlling the air supply responsive to that at least one characteristic.
Claim 14
Dependent Claim
202 words
In a process for separating pollutants from a liquid, an improved liquid purification step, wherein pollutants are assembled and separated from the liquid, comprising adding to the liquid to be filtered chemicals facilitating at least one of the processes of precipitation and flocculation, continuously directing the liquid containing the chemicals from the chemical addition located directly to a zone of moving particulate filter material forming a filter bed, absent intermediate passage through any flocculation tank and absent intermediate passage through any sedimentation basin, passing the liquid containing the chemicals through the filter bed to provide at least one of the precipitaton and flocculation processes within the moving particulate material of the bed, moving the particulate material of the filter bed relative to the liquid and in addition to the movement of the liquid, removing soiled particulate material and pollutants from the filter bed, cleaning the particulate material, and returning the particulate material to the filter bed, said steps of removing, cleaning and returning the particulate material being simultaneous with the passing of liquid through the filter bed and including the step of supplying air to transport soiled filter particles from the filter bed to a wash path for said step of cleaning.
Claim 15
Dependent Claim
202 words
In a process for separating pollutants from a liquid, an improved liquid purification step, wherein pollutants are assembled and separated from the liquid, comprising adding to the liquid to be filtered chemicals facilitating at least one of the processes of precipitation and flocculation, continuously directing the liquid containing the chemicals from the chemical addition located directly to a zone of moving particulate filter material forming a filter bed, absent intermediate passage through any flocculation tank and absent intermediate passage through any sedimentation basin, passing the liquid containing the chemicals through the filter bed to provide at least one of the precipitaton and flocculation processes within the moving particulate material of the bed, moving the particulate material of the filter bed relative to the liquid and in addition to the movement of the liquid, removing soiled particulate material and pollutants from the filter bed, cleaning the particulate material, and returning the particulate material to the filter bed, said steps of removing, cleaning and returning the particulate material being simultaneous with the passing of liquid through the filter bed and including the step of supplying air to transport soiled filter particles from the filter bed to a wash path for said step of cleaning.
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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) | 1984-01-20 | 1984-07-21 | 1985-01-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-01-20 | 1988-07-21 | 1989-01-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-01-20 | 1992-07-21 | 1993-01-20 | $7700.00 | Window Closed / Lapsed |