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US5004552A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus and method for separating water from crude oil

Assignee: Nokia Deutschland GmbH
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Filing: 1990-06-14
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Granted: 1991-04-02
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Expires: 2010-06-14
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Abstract

Abstract Method and apparatus for separating water and crude oil mixtures and other two-phase fluid mixtures of components of different densities. The mixture is pumped through a conduit in the form of a vertical spiral at a velocity that impels the heavy phase toward the outside of the spiral. A fraction is withdrawn from the outside of the turns of the spiral and is led downwardly to the bottom of a vertical settling tank. Any light phase removed with the heavy phase floats to the top in the settling tank and is reintroduced at the top of the spiral.

Inventors

  • 👤 Ahmed M. Al-Yazdi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 21:45
CPC Classifications
C; C10; C10G; C10G33/00; C10G33/06; B; B01; B01D; B01D17/00; B01D17/02; B01D17/0208; B01D17/0214; B01D17/0217

Claims Analysis

Total Claims: 27
Claim 1
Independent Claim 116 words
Apparatus for separating a fluid mixture of a heavy phase from a light phase in a fluid mixture, comprising, a spiral conduit in the form of a vertical coil of a plurality of turns, an inlet at one end of said conduit and an outlet at a second end of said conduit, means for moving the mixture of phases through said conduit at a velocity such that said heavy phase segregates in said conduit along the outside of said turns of said coil, skimmer ports in said conduit along the outside of at least several upper turns of said coil; a separating tank, and take-off lines connecting the skimmer ports to said tank below said ports.
Claim 2
Dependent Claim 116 words
Apparatus for separating a fluid mixture of a heavy phase from a light phase in a fluid mixture, comprising, a spiral conduit in the form of a vertical coil of a plurality of turns, an inlet at one end of said conduit and an outlet at a second end of said conduit, means for moving the mixture of phases through said conduit at a velocity such that said heavy phase segregates in said conduit along the outside of said turns of said coil, skimmer ports in said conduit along the outside of at least several upper turns of said coil; a separating tank, and take-off lines connecting the skimmer ports to said tank below said ports.
Claim 3
Dependent Claim 112 words
Apparatus for separating a light phase from a heavy phase in a fluid mixture, comprising, a spiral conduit in the form of a vertical coil of a plurality of turns, an inlet at one end of said conduit and an outlet at a second end of said conduit, means for moving the mixture of phases through said conduit at a velocity such that said light phase segregates in said conduit along the inside of said turns of said coil, skimmer ports in said conduit along the inside of at least several upper turns of said coil, a separating tank, and take-off lines connecting the skimmer ports to said tank below said ports.
Claim 4
Dependent Claim 112 words
Apparatus for separating a light phase from a heavy phase in a fluid mixture, comprising, a spiral conduit in the form of a vertical coil of a plurality of turns, an inlet at one end of said conduit and an outlet at a second end of said conduit, means for moving the mixture of phases through said conduit at a velocity such that said light phase segregates in said conduit along the inside of said turns of said coil, skimmer ports in said conduit along the inside of at least several upper turns of said coil, a separating tank, and take-off lines connecting the skimmer ports to said tank below said ports.
Claim 5
Dependent Claim 26 words
The apparatus of claim 1 or 2 comprising a return line from said tank to said conduit, downstream of at least some of said skimmer ports.
Claim 6
Dependent Claim 27 words
The apparatus of claim 1 wherein a return line extends from said tank at a position adjacent the top thereof, to the inside wall of said coil.
Claim 7
Dependent Claim 19 words
The apparatus of claim 4 wherein said return line connects said tank to the topmost turn of said coil.
Claim 8
Dependent Claim 23 words
The apparatus of claim 2 wherein a return line extends from said tank at a position adjacent the bottom thereof, to said coil.
Claim 9
Dependent Claim 19 words
The apparatus of claim 6 wherein said return line connects said tank to the uppermost turn of said coil.
Claim 10
Dependent Claim 18 words
The apparatus of claim 1 or 2 wherein said tank is situated within the turns of said coil.
Claim 11
Dependent Claim 13 words
The apparatus of claim 1 or 2 wherein said tank is vertically elongated.
Claim 12
Dependent Claim 33 words
The apparatus of claim 1 or 2 wherein said said skimmer ports are in successive turns of said coil and each port is connected downwardly by a separate takeoff line to said tank.
Claim 13
Dependent Claim 17 words
The apparatus of claim 1 or 2 wherein the takeoff lines enter said tank adjacent its bottom.
Claim 14
Dependent Claim 20 words
The apparatus of claim 1 or 2 wherein said conduit leads said mixture upwardly from said inlet through said turns.
Claim 15
Dependent Claim 15 words
The apparatus of claim 1 or 2 wherein said spiral has more than 4 turns.
Claim 16
Independent Claim 191 words
The method of separating a heavy phase and a light phase in a fluid mixture, comprising, passing the mixture through a vertical, spiral tubular coil, at a velocity sufficiently high that the heavy phase is concentrated toward the outside of the turns of the coil as the mixture flows around the spiral and the light phase is concentrated toward the inside of the turns, withdrawing a fraction of the fluid from at least one upper turn of the coil, said fraction being withdrawn from the outside of said coil if the heavy phase is to be removed and from the inside of said coil if the light phase is to be removed, conducting the withdrawn fraction downwardly to a settling tank, permitting the withdrawn fraction to further separate into the heavy phase and the light phase, and admitting light phase from the top of said settling tank to said coil adjacent the top of the coil if the heavy phase is to be removed, and heavy phase from the bottom of said settling tank to said coil adjacent the top of said coil if the light phase is to be removed.
Claim 17
Independent Claim 191 words
The method of separating a heavy phase and a light phase in a fluid mixture, comprising, passing the mixture through a vertical, spiral tubular coil, at a velocity sufficiently high that the heavy phase is concentrated toward the outside of the turns of the coil as the mixture flows around the spiral and the light phase is concentrated toward the inside of the turns, withdrawing a fraction of the fluid from at least one upper turn of the coil, said fraction being withdrawn from the outside of said coil if the heavy phase is to be removed and from the inside of said coil if the light phase is to be removed, conducting the withdrawn fraction downwardly to a settling tank, permitting the withdrawn fraction to further separate into the heavy phase and the light phase, and admitting light phase from the top of said settling tank to said coil adjacent the top of the coil if the heavy phase is to be removed, and heavy phase from the bottom of said settling tank to said coil adjacent the top of said coil if the light phase is to be removed.
Claim 18
Dependent Claim 14 words
The method of claim 14 wherein said mixture is passed upwardly through said coil.
Claim 19
Dependent Claim 22 words
The method of claim 14 wherein said withdrawn fraction is the heavy phase and is withdrawn from the outside of said coil.
Claim 20
Dependent Claim 22 words
The method of claim 14 wherein said withdrawn fraction is the light phase and is withdrawn from the inside of said coil.
Claim 21
Dependent Claim 16 words
The method of claim 14 wherein said withdrawn fraction is withdrawn substantially tangentially from said coil.
Claim 22
Dependent Claim 30 words
The method of claim 14 wherein said light phase is introduced from the top of said settling tank to said coil on the inside of a turn of said coil.
Claim 23
Dependent Claim 22 words
The method of claim 14 wherein said withdrawn fraction enters said tank below said coil and near the bottom of said tank.
Claim 24
Dependent Claim 20 words
The method of claim 14 wherein said heavy phase settles to and is drained from the bottom of the tank.
Claim 25
Dependent Claim 22 words
The method of claim 14 wherein the velocity of the withdrawn fraction is reduced as it is conducted downwardly to said tank.
Claim 26
Dependent Claim 24 words
The method of claim 14 wherein said heavy phase is introduced from the bottom of said settling tank to a turn of said coil.
Claim 27
Dependent Claim 20 words
The method of claim 14 wherein said light phase floats to and is drained from said top of the tank.

References Cited (Backward Citations)

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US3768658A Cited
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US3875061A Cited
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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) 1994-04-01 1994-10-01 1995-04-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-04-01 1998-10-01 1999-04-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-04-01 2002-10-01 2003-04-02 $7700.00 Window Closed / Lapsed

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