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US4126546A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for the filtration of a suspension or emulsion

Assignee: Axel Johnson Engineering AB
•
Filing: 1977-02-23
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Granted: 1978-11-21
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Expires: 1997-02-23
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Abstract

Abstract A suspension or emulsion is filtered by causing the same to flow upwards through a zone of filter medium of particle size forming a filter bed while the filter medium concurrently flows in a downward direction through the filter bed zone. Dirty filter medium at the bottom of the filter bed zone is transported to a wash device located above the filter bed zone and is washed as the dirty medium passes downward along a washpath in the wash device in counter current flow to wash liquid which passes upward though the wash device, whereafter the washed medium is returned to the top of the filter bed zone. A zone of filtrated liquid phase is maintained above the filter bed, and a portion of said filtrated liquid phase is supplied to the wash device as the wash liquid.

Inventors

  • 👤 Ulf R. Hjelmner
  • 👤 Hans F. Larsson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 14:05
CPC Classifications
B; B01; B01D; B01D24/00; B01D24/46; B01D24/4668; B01D24/4689; B01D24/02; B01D24/10; B01D24/16; B01D24/36

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 241 words
In a method for filtering wherein a suspension or emulsion to be filtered is supplied to a zone of particle filter medium forming a filter bed, the suspension 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 suspension past the inflow of the suspension 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, the improvement wherein 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, said separated transport of the dirty filter medium takes place upwards through 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.
Claim 2
Dependent Claim 241 words
In a method for filtering wherein a suspension or emulsion to be filtered is supplied to a zone of particle filter medium forming a filter bed, the suspension 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 suspension past the inflow of the suspension 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, the improvement wherein 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, said separated transport of the dirty filter medium takes place upwards through 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.
Claim 3
Dependent Claim 33 words
A method according to claim 1, characterized in that during the washing of said filter medium, the relative velocity between the filter medium and the wash liquid is increased momentaneously at least once.
Claim 4
Dependent Claim 28 words
A method according to claim 1, characterized in that during the washing of said filter medium, the flow velocity of the filter medium is decelerated at least once.
Claim 5
Dependent Claim 33 words
A method according to claim 3 characterized in that said deceleration takes place along a zone of the wash path followed by a momentaneous increase in the flow velocity of the filter medium.
Claim 6
Dependent Claim 27 words
A method according to claim 1 characterized in that caked aggregates of said dirty filter medium are broken up prior to the washing of said filter medium.
Claim 7
Dependent Claim 20 words
A method according to claim 1 wherein the quantity of the wash liquid flowing along the wash path is controlled.
Claim 8
Dependent Claim 30 words
A method according to claim 6, characterized in that the quantity of wash liquid is controlled by adjustment of the outflow of dirty wash liquid obtained during the washing step.
Claim 9
Dependent Claim 27 words
A method according to claim 6, characterized in that the quantity of wash liquid is controlled by changing the level of said zone of filtrated liquid phase.
Claim 10
Dependent Claim 43 words
A method according to claim 1 including the step of controlling the quantity of the filter medium which is transported to the wash path by quantity sensing or pressure sensing of the suspension prior to the supply thereof to the filter bed zone.
Claim 11
Dependent Claim 55 words
A method according to claim 1 wherein air is used for the transport of the dirty filter medium to said wash path, the supplied air for said transport being extruded into the dirty filter medium and, prior to said extrusion, being trapped and discharged to prevent the air from infiltrating into the filter bed zone.

References Cited (Backward Citations)

US2057887A Cited
US3395099A Cited
US3537582A Cited
US3512640A Cited
US3581895A Cited
US3563385A Cited
US3667604A Cited
US3707230A Cited
US3841485A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-11-20 1982-05-22 1982-11-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-11-20 1986-05-22 1986-11-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-11-20 1990-05-22 1990-11-21 $7700.00 Window Closed / Lapsed

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