WO1987006159A1 - Apparatus for separating mixtures - Google Patents
Apparatus for separating mixtures Download PDFInfo
- Publication number
- WO1987006159A1 WO1987006159A1 PCT/AU1987/000093 AU8700093W WO8706159A1 WO 1987006159 A1 WO1987006159 A1 WO 1987006159A1 AU 8700093 W AU8700093 W AU 8700093W WO 8706159 A1 WO8706159 A1 WO 8706159A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- inlet
- outlet
- hollow member
- hollow
- head section
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/02—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles without inserted separating walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
Definitions
- This invention relates generally to apparatus for separating mixtures of the type containing liquids, solids and/or gases and more particularly, though not exclusively, to the separation of multi-phase fluids, such as, for example, oil, water and/or gas.
- apparatus for separating multi-phase mixtures comprising an elongate hollow member having an inlet end and an outlet end and a central axis, inlet means for inlet of liquid mixture to be separated to the member at a location at the inlet end of the member and outlet means for outflow of separated streams of at least two components of the liquid mixture, being of different densities, and means for rotating said member to effect the separation of the components of the mixture when admitted via said inlet means, for said outflow via said outlet means.
- the inlet means comprises a hollow head section with one or more feed inlets extending to the open interior thereof , said head section including an open end, the inlet end of said member -2- being sealingly and rotatingly engaged within the open end of the head section whereby, in use, liquid mixture fed to the inlet means passes via the or each said feed inlet into the open interior of the head section and thence into the said hollow member via the open end of said head section and via an adjacent portion, such as via an open end, of the rotatable member.
- the or each said feed inlet may be arranged substantially tangentially to the central axis of the hollow member.
- the feed inlet is arranged substantially co-axially with the central axis of the hollow member.
- the mixture to be separated is fed into the hollow member axially with respect thereto.
- Means may be provided to assist in generating the rotational velocity of the mixture in addition to the rotating hollow member.
- the outlet means comprises a second hollow head section sealingly and rotatably engaged with the said other end of said rotatable hollow member and into the interior of which, in use, components of said mixture pass from said member, such as via an open end thereof,said second head section being provided with at least one take-off duct open to the interior of the second head section and positioned to remove one of the separated streams.
- the second head section may include a further one or more take-off ducts positioned to remove another of the separated streams.
- the outlet means may comprise one or more outlets arranged substantially tangentially to the central axis of the member for receiving the more dense separated stream and a co-axial outlet or outlets for removing the less dense separated stream of the mixture.
- the co-axial outlets are disposed at the outlet end of said member although in some instances the co-axial outlets may be disposed at the inlet end.
- the member includes therein a generally spiral or helix like separator element having a central axis co-axial with that of the hollow member the separator element being at least partially disposed within the hollow member for rotation therewith about the central axis.
- An axial passage or zone may be disposed in the region of the central axis extending between the inlet and outlet of the hollow member.
- the hollow member comprises a tapered hollow member with the larger end preferably forming the inlet, and the smaller end forming the outlet.
- Figure 1 is a schematic side elevation of one form of apparatus according to the invention
- Figure 2 is a schematic view of a part of another form of apparatus according to the invention
- Figure 3 is a schematic sectional view of apparatus which includes the part shown in Figure 2
- Figure 4 is a schematic layout of a system incorporating apparatus according to the invention.
- FIG 5 is a schematic view of apparatus according to a further embodiment of the invention.
- the apparatus 10 comprises a hollow rotatable member 12 which is in the form of an elongate hollow cylinder having an inlet end 13 and an outlet end 19.
- the hollow member 12 is mounted in be.aring 14, for rotation about its central axis X-X.
- a drive means comprising an electric motor 54 operatively connected to member 12 via belt 55 for causing rotation of the member 12.
- the apparatus further includes an inlet means 30 at one end thereof comprising a hollow structure 32 having an open end which communicates with hollow member 12.
- An inlet duct 36 in this case is in the form of a tangentially feed pipe which opens into the structure 32.
- An appropriate seal is provided between the structure 32 and the hollow member 12.
- Outlet 38 is provided in the structure 32 which operates in a manner which will be hereinafter described.
- Outlet means 40 provided at the other end of the hollow member 12, this outlet means comprising structure 44 having an open end facing into the hollow member 12. This is similar in structure to the inlet means and includes a tangentially outlet duct 51 and an axial outlet duct 52.
- the apparatus generally indicated at 1 comprises a rotatable hollow member 5 in the form of a hollow cylinder having a central axis X-X with an inlet end and an outlet end.
- a generally spiral or helix like separator element 7 is at least partially disposed within the member 5 for rotation therewith about the central axis.
- An axis passage or zone in the region of the central axis X-X extends between the inlet and outlet ends of the hollow member.
- a multi-phase mixture for separation can enter the hollow member through the feed inlet 17 and is separated at least partially into separate phases with the less dense phase forming a central core in the axial passage or zone and the more dense phase being urged radially outwardly therefrom.
- the separated phases under the action of the rotating generator and hollow member can be delivered towards the outlet of the cavity where they can be discharged and collected in any suitable manner.
- the elongated member is of substantially constant cross-section.
- the elongated member comprises a tapered hollow element with the larger end preferably forming the inlet, and the smaller end forming the outlet.
- the tapered portion may have curved or straight walls or a combination of both. Furthermore, it may include parallel sided sections as well.
- the hollow member is mounted for rotation about the longitudinal axis between the open ends.
- the separator element 7 as shown in the form of a spiral or helical member which is secured at its outer peripheral edge to the inner surface of the hollow member 5.
- the separator element spiral is also of constant cross-sectional outer dimension, whereas in the case of the tapered main body, the spiral or helical element is configured to follow the taper of that of the body portion.
- the spiral of helical member comprises a ribbon-like flat strip which winds around its central axis and in spaced relation thereto so that the space between its inner peripheral edge and the central axis define the axial passage or zone referred to above.
- a central collecting tube 4 is disposed within the axial passage and extends partially along the length of the element.
- the apparatus a's shown further includes an outer housing 3 with the hollow member 5 being disposed therein for rotation relative thereto the feed inlet 17 being in housing 3.
- Take-off ports 15 and 16 are provided for receiving the phases separated during the passage of the mixture through the hollow member.
- the hollow member may be mounted for rotation relative to the housing by means of suitable bearings and seals may be provided at each end of the main body to provide a seal between its inlet and outlet ends.
- Drive means may be provided for rotating the main body.
- the drive means may comprise a motor operatively supported by the housing for rotating the main body relative thereto.
- Suitable transmission means, such as gearing or the like may provide for the rotation of the two members relative to one another. Any suitable form of drive means may be used such as an air motor, electric motor or the like.
- the apparatus of the present invention may be used in a system which may comprise a plurality of such apparatus arranged in series for selectively separating the various phases from one another.
- a system which may comprise a plurality of such apparatus arranged in series for selectively separating the various phases from one another.
- inlet 15 can be of the same diameter as body portion 6.
- the lightest phase of the mixture tends to concentrate in the core or passage 19 and can be collected at outlet 16.
- the heavier phase is caused to move towards the outer part of the generator and can be collected at outlet 17.
- FIG. 4 One example of a system for separating mixtures of oil/water/gas using apparatus according to the invention is shown in Figure 4.
- the mixture to be separated is delivered through a choke 20 to a first apparatus according to the invention 21.
- Gas is discharged through line
- the oil/water mixture is fed through line 27 to a second apparatus
- a gas detector 29 monitors the quality of gas entering the second apparatus 25.
- the separated water is passed through a cyclone separator 37 which may be of the type described by applicant in several of its co-pending applications.
- a pump 35 transfers the separated oil back to the second apparatus 25.
- the apparatus 10 shown in Figure 5 of the drawings is similar to that of Figure 1 and comprises a hollow rotatable member 12 which may, for example, be in the form of an elongate hollow cylinder of constant diameter, or of diameter which varies from place to place .along the length thereof, such as being tapered.
- a hollow rotatable member 12 which may, for example, be in the form of an elongate hollow cylinder of constant diameter, or of diameter which varies from place to place .along the length thereof, such as being tapered.
- the member 12 is mounted in bearing 14, for rotation about an axis X-X. As shown, this rotation is effected by drive means 22 comprising an electric motor 24 and co-operating gears 26, 28 coaxially mounted, respectively, on the member 12 and on the output shaft of the motor 24.
- the apparatus 10 further includes, at one end of the member 12, an inlet means 30 comprising a hollow structure 32 in this case being formed of a hollow cylinder structure 32 closed at one end by an end wall 34 and having an open opposite end into which one open end of the member 12 extends.
- the structure 32 has an inlet duct 36 in this case in the form of a tangential feed pipe which opens into the structure 32 at a location towards the closed end thereof.
- seal means (not shown) which is effective to peripherally seal an annular gap between the outer surface of the member 12 and the inner surface of the open end of the structure 32 into which the member 12 extends, whilst permitting free rotation of the member 12 -relative to structure 32.
- the separator 10 is provided with outlet means 40.
- outlet means 40 This is shown as comprising an elongate hollow outlet structure 44.
- Structure 44 includes a hollow generally tapered member 44a of circular cross-section which extends into an adjacent open end of the member 12. Seal means (not shown) is provided for sealing the annular gap between the periphery of the outer surface of the member 44a, where it extends into the member 12, and the inner surface of the open end of the member 12 at that location.
- the member 44a opens to an outlet duct 46 for take-off of one component of the liquid to be separated in the separator.
- Duct 46 may comprise an extension of the member 44a.
- a second outlet duct 48 is also provided, this being in the form of a tube which extends into the duct 46 and is open to the duct 46 centrally thereof, leaving a space of annular form between the periphery of this tube and the interior surface of the duct 46.
- the sealing means provided between outlet structure 40 and the member 12, is so arranged as to permit free rotation of the member 12 whilst still maintaining a fluid tight seal between the ember 12 and the outlet structure. Since the sealing means between inlet structure 32 and the member 12 is also so characterized, the structures 32 and 40 may be stationary, notwithstanding that the member 12 in use is rotated.
- liquid mixture to be separated is passed into the inlet means 30 via the duct 32, and thence passes within the internal cylindrical interior of the inlet structure 32, with a helical motion around the common axis of the structure 32 and the member 12. Thence, the liquid to be separated passes into the member 12 undergoes a helical motion about axis X-X and travels lengthwise along member 12, whilst being to centrifugal action whereby at the end of the member 12 nearest structure 44, the more dense of the constituent components of the mixture are thrown outwardly to occupy a layer of annular form around the internal periphery of the member 12, whilst the less dense components occupy a central core close to the axis X-X of the member 12.
- the so separated components are then passed axially through the member 44, the more dense components passing directly out the duct 46 whilst the less dense components are passed out the duct 48 which, as explained previously, is open at a location positioned centrally about the axis 20.
- member 44a is shown as being tapered, it may be of any other form such as parallel sided cylindrical.
Landscapes
- Cyclones (AREA)
- Centrifugal Separators (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019870701149A KR880701135A (en) | 1986-04-07 | 1987-04-06 | Mixture sorter of multiphase |
DK613187A DK613187D0 (en) | 1986-04-07 | 1987-11-23 | Apparatus for separating mixtures |
NO875064A NO875064D0 (en) | 1986-04-07 | 1987-12-04 | MIXTURE SEPARATION DEVICE. |
GB8823327A GB2209691B (en) | 1986-04-07 | 1988-10-05 | Apparatus for separating mixtures |
SE8803546A SE8803546L (en) | 1986-04-07 | 1988-10-06 | DEVICE FOR SEPARATION OF MIXTURES |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AUPH535186 | 1986-04-07 | ||
AUPH5351 | 1986-04-07 | ||
AUPH787286 | 1986-09-05 | ||
AUPH7872 | 1986-09-05 | ||
AUPI0345 | 1987-02-13 | ||
AUPI034587 | 1987-02-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1987006159A1 true WO1987006159A1 (en) | 1987-10-22 |
Family
ID=27157293
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU1987/000093 WO1987006159A1 (en) | 1986-04-07 | 1987-04-06 | Apparatus for separating mixtures |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0299966A4 (en) |
JP (1) | JPH01502407A (en) |
KR (1) | KR880701135A (en) |
GB (1) | GB2209691B (en) |
SE (1) | SE8803546L (en) |
WO (1) | WO1987006159A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE9415521U1 (en) * | 1994-09-24 | 1995-02-02 | Gall, Holger, 21629 Neu Wulmstorf | Device for the mechanical extraction of vegetable oil |
GB2346336A (en) * | 1999-02-06 | 2000-08-09 | Frymate Limited | Apparatus for separating solids from oil |
WO2003101619A1 (en) * | 2002-05-28 | 2003-12-11 | Baker Hughes Incorporated | Centrifugal separator bowl assembly with flow guide |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1374377A (en) * | 1919-07-14 | 1921-04-12 | Julius T Jaeger | Centrifugal pulp-thickener |
US1634759A (en) * | 1924-07-30 | 1927-07-05 | Sharples Separator Company | Centrifugal milk separator |
AU4585072A (en) * | 1971-08-30 | 1974-02-28 | The Garrett Corporation And Signal Oil And Gas Company | Centrifugal separator discharge. control system |
AU6414674A (en) * | 1973-01-16 | 1975-06-19 | Signal Oil And Gas Company | Centrifugal separator for three phase mixture |
AU8743275A (en) * | 1975-01-03 | 1977-06-16 | Alfa-Laval A.B. | Centrifuge apparatus |
AU9149682A (en) * | 1981-12-18 | 1983-06-23 | Imperial Chemical Industries Plc | Centrifugal separation process |
AU6704186A (en) * | 1986-01-02 | 1987-07-09 | Neyrtec Industrie | A rotary vortex separator for a heterogeneous liquid |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1282172A (en) * | 1960-12-09 | 1962-01-19 | Rateau Soc | Improvement in centrifugal separators |
-
1987
- 1987-04-06 KR KR1019870701149A patent/KR880701135A/en not_active Application Discontinuation
- 1987-04-06 WO PCT/AU1987/000093 patent/WO1987006159A1/en not_active Application Discontinuation
- 1987-04-06 EP EP19870902326 patent/EP0299966A4/en not_active Withdrawn
- 1987-04-06 JP JP62502564A patent/JPH01502407A/en active Pending
-
1988
- 1988-10-05 GB GB8823327A patent/GB2209691B/en not_active Expired - Fee Related
- 1988-10-06 SE SE8803546A patent/SE8803546L/en not_active Application Discontinuation
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1374377A (en) * | 1919-07-14 | 1921-04-12 | Julius T Jaeger | Centrifugal pulp-thickener |
US1634759A (en) * | 1924-07-30 | 1927-07-05 | Sharples Separator Company | Centrifugal milk separator |
AU4585072A (en) * | 1971-08-30 | 1974-02-28 | The Garrett Corporation And Signal Oil And Gas Company | Centrifugal separator discharge. control system |
AU6414674A (en) * | 1973-01-16 | 1975-06-19 | Signal Oil And Gas Company | Centrifugal separator for three phase mixture |
AU8743275A (en) * | 1975-01-03 | 1977-06-16 | Alfa-Laval A.B. | Centrifuge apparatus |
AU9149682A (en) * | 1981-12-18 | 1983-06-23 | Imperial Chemical Industries Plc | Centrifugal separation process |
AU6704186A (en) * | 1986-01-02 | 1987-07-09 | Neyrtec Industrie | A rotary vortex separator for a heterogeneous liquid |
Non-Patent Citations (1)
Title |
---|
See also references of EP0299966A4 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE9415521U1 (en) * | 1994-09-24 | 1995-02-02 | Gall, Holger, 21629 Neu Wulmstorf | Device for the mechanical extraction of vegetable oil |
GB2346336A (en) * | 1999-02-06 | 2000-08-09 | Frymate Limited | Apparatus for separating solids from oil |
WO2003101619A1 (en) * | 2002-05-28 | 2003-12-11 | Baker Hughes Incorporated | Centrifugal separator bowl assembly with flow guide |
Also Published As
Publication number | Publication date |
---|---|
GB2209691A (en) | 1989-05-24 |
EP0299966A4 (en) | 1990-02-05 |
SE8803546D0 (en) | 1988-10-06 |
KR880701135A (en) | 1988-07-25 |
GB8823327D0 (en) | 1989-03-01 |
EP0299966A1 (en) | 1989-01-25 |
JPH01502407A (en) | 1989-08-24 |
GB2209691B (en) | 1990-10-31 |
SE8803546L (en) | 1988-10-08 |
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