EP0815944A2 - Cyclone separator - Google Patents

Cyclone separator Download PDF

Info

Publication number
EP0815944A2
EP0815944A2 EP97304879A EP97304879A EP0815944A2 EP 0815944 A2 EP0815944 A2 EP 0815944A2 EP 97304879 A EP97304879 A EP 97304879A EP 97304879 A EP97304879 A EP 97304879A EP 0815944 A2 EP0815944 A2 EP 0815944A2
Authority
EP
European Patent Office
Prior art keywords
aperture
chamber
oil
cyclone separator
wall
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP97304879A
Other languages
German (de)
French (fr)
Other versions
EP0815944A3 (en
Inventor
Peter Gould
Martin Dennis Grewer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fjords Processing AS
Original Assignee
Kvaerner Process Systems AS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kvaerner Process Systems AS filed Critical Kvaerner Process Systems AS
Publication of EP0815944A2 publication Critical patent/EP0815944A2/en
Publication of EP0815944A3 publication Critical patent/EP0815944A3/en
Withdrawn legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12Construction of the overflow ducting, e.g. diffusing or spiral exits

Definitions

  • This invention relates to a cyclone separator of the type used to separate a mixture comprising a fluid of a first density and fluid of a second density, for example, oil and water.
  • the separation of a mixture of fluids, for example oil and water, into its individual constituents is achieved in a known type of hydrocyclone by the generation of a vortex in the mixture within the hydrocyclone effecting centrifugal separation of the mixture so as to produce an "oil-core".
  • the separated oil and water are collected individually at respective output ports.
  • transfer of the oil from the oil-core to the oil output port may be less than optimum, especially when the hydrocyclone is operating at low flow/pressure with consequent reduction in centrifugal forces in the mixture.
  • a cyclone separator comprising a first chamber within which a separation vortex is generated in use, said chamber having an end wall, an aperture in said end wall, and, directing means tapering inwardly from said chamber towards said aperture for guiding a core of said vortex within the first chamber towards the aperture.
  • said wall defines said directing means.
  • said directing means substantially surrounds said aperture.
  • said directing means is a frustum of a cone defined by said wall with said aperture at its apical region.
  • the hydrocyclone 2 of Figure 1 comprises a tapering tube element 4 having a water output port 10 at its narrower end and an opposite end portion 6 having one or more, desirably tangential, input ports 8, and an oil output port 12.
  • the end portion 6 comprises a first chamber 14 defined in part by the tapering outer wall 26 of the tapering element 4.
  • the mixture inlet ports 8 are disposed in the wall 26 of the chamber 14 so as to be in fluid communication therewith and the portion 6 further includes a second chamber 16, and a dividing wall 18 separating the first and second chambers 14, 16.
  • the dividing wall 18 has an aperture 20 located centrally therein and providing access from the chamber 14 to the chamber 16, the chamber 16 including the oil outlet port 12.
  • the dividing wall 18 has a main, annular portion 28 of frusto-conical shape which extends into the chamber 14 and tapers inwardly, having a generatrix inclined at an angle to a plane P which is perpendicular to a central axis A of the hydrocyclone 2.
  • the central portion 34 of the dividing wall 18 is also of a frusto-conical shape which tapers inwardly, but the portion 34 extends in the opposite direction to the portion 28, towards the second chamber 16, and has the aperture 20 disposed at its apical region 36.
  • an oil-water mixture is introduced into the hydrocyclone 2 via the inlet ports 8 so that a vortex is created within the first chamber 14 and the tube element 4.
  • the individual constituents i.e. the oil and the water are separated, the water component residing at the periphery of the vortex and the oil component residing at the core of the vortex (known as an "oil-core").
  • the pressure balance within the hydrocyclone creates a back pressure providing the oil-core with an axial velocity towards the dividing wall 18.
  • the inwardly tapering portion 34 of the wall 18 directs the peripheral portion of the oil-core towards the aperture 20 thereby minimising loss of transfer of the oil core from the first chamber to the oil output port 12 in low inlet flow and pressure operating conditions.
  • the oil channelled from the oil-core towards the aperture 20 by the portion 34 passes through the aperture 20 into the second chamber 16 and leaves the hydrocyclone 2 via the oil output port 12.
  • the water at the periphery of the vortex travels along the tube element 4 towards the water output port 10.
  • the main portion 28 can be formed so as to have a flat or bulged shape.
  • the portion 34 may have a shape other than a frusto-conical configuration provided that it possesses a shape having an opening wider than the widest expected "core" in use and capable of collecting and guiding fluid inwardly towards the aperture 20, for example a curved, dished shape.

Landscapes

  • Cyclones (AREA)

Abstract

A cyclone (2) comprises a first and second chambers (14, 16) separated by a wall (18) having an aperture (20). Frusto-conical directing means (34) is provided for guiding a fluid within the first chamber (14) towards the aperture (20).

Description

This invention relates to a cyclone separator of the type used to separate a mixture comprising a fluid of a first density and fluid of a second density, for example, oil and water.
The separation of a mixture of fluids, for example oil and water, into its individual constituents is achieved in a known type of hydrocyclone by the generation of a vortex in the mixture within the hydrocyclone effecting centrifugal separation of the mixture so as to produce an "oil-core". The separated oil and water are collected individually at respective output ports. However, it has been found that transfer of the oil from the oil-core to the oil output port may be less than optimum, especially when the hydrocyclone is operating at low flow/pressure with consequent reduction in centrifugal forces in the mixture.
According to a first aspect of the present invention, there is provided a cyclone separator comprising a first chamber within which a separation vortex is generated in use, said chamber having an end wall, an aperture in said end wall, and, directing means tapering inwardly from said chamber towards said aperture for guiding a core of said vortex within the first chamber towards the aperture.
Desirably said wall defines said directing means.
Conveniently said directing means substantially surrounds said aperture.
Preferably said directing means is a frustum of a cone defined by said wall with said aperture at its apical region.
The invention will now be described, in more detail, with reference to the accompanying drawings, in which:
  • Figure 1 shows a cross-sectional view of a hydrocyclone according to an embodiment of the present invention; and
  • Figure 2 shows a part of Figure 1 in more detail.
  • The hydrocyclone 2 of Figure 1 comprises a tapering tube element 4 having a water output port 10 at its narrower end and an opposite end portion 6 having one or more, desirably tangential, input ports 8, and an oil output port 12.
    Referring to Figure 2, the end portion 6 comprises a first chamber 14 defined in part by the tapering outer wall 26 of the tapering element 4. The mixture inlet ports 8 are disposed in the wall 26 of the chamber 14 so as to be in fluid communication therewith and the portion 6 further includes a second chamber 16, and a dividing wall 18 separating the first and second chambers 14, 16. The dividing wall 18 has an aperture 20 located centrally therein and providing access from the chamber 14 to the chamber 16, the chamber 16 including the oil outlet port 12.
    The dividing wall 18 has a main, annular portion 28 of frusto-conical shape which extends into the chamber 14 and tapers inwardly, having a generatrix inclined at an angle to a plane P which is perpendicular to a central axis A of the hydrocyclone 2. The central portion 34 of the dividing wall 18 is also of a frusto-conical shape which tapers inwardly, but the portion 34 extends in the opposite direction to the portion 28, towards the second chamber 16, and has the aperture 20 disposed at its apical region 36.
    In use, an oil-water mixture is introduced into the hydrocyclone 2 via the inlet ports 8 so that a vortex is created within the first chamber 14 and the tube element 4.
    The individual constituents, i.e. the oil and the water are separated, the water component residing at the periphery of the vortex and the oil component residing at the core of the vortex (known as an "oil-core"). The pressure balance within the hydrocyclone creates a back pressure providing the oil-core with an axial velocity towards the dividing wall 18. The inwardly tapering portion 34 of the wall 18 directs the peripheral portion of the oil-core towards the aperture 20 thereby minimising loss of transfer of the oil core from the first chamber to the oil output port 12 in low inlet flow and pressure operating conditions.
    The oil channelled from the oil-core towards the aperture 20 by the portion 34 passes through the aperture 20 into the second chamber 16 and leaves the hydrocyclone 2 via the oil output port 12.
    The water at the periphery of the vortex travels along the tube element 4 towards the water output port 10.
    Although the above examples have been described in the context of the dividing wall 18 having the main portion 28 of frusto-conical shape, it is not intended that the invention be limited to such a configuration, other configurations being possible. For example, the main portion 28 can be formed so as to have a flat or bulged shape. Similarly, the portion 34 may have a shape other than a frusto-conical configuration provided that it possesses a shape having an opening wider than the widest expected "core" in use and capable of collecting and guiding fluid inwardly towards the aperture 20, for example a curved, dished shape.
    Additionally, although the above examples have been described in the context of an oil-water mixture, it is not intended that the invention be limited to such a mixture and the use of other mixtures is envisaged, for example water/gas or powder/water. In this respect, it is not intended that the definition of the term fluid be limited to liquids and gasses alone, but instead to include powders or solids suspended in liquids or gases.

    Claims (4)

    1. A cyclone separator comprising a first chamber (14) within which a separation vortex is generated in use, said chamber having an end wall (18), an aperture (20) in said end wall, and the cyclone being characterised by directing means (34) tapering inwardly from said chamber (14) towards said aperture (20) for guiding a core of said vortex within the first chamber towards the aperture.
    2. A cyclone separator as claimed in Claim 1, characterised in that said wall (18) defines said directing means (34).
    3. A cyclone separator as claimed in Claim 1 or claim 2, characterised in that said directing means (34) substantially surrounds said aperture (20).
    4. A cyclone separator as claimed in any one of Claims 1 to 3, characterised in that said directing means (34) is a frustum of a cone defined by said wall (18) with said aperture (20) at its apical region.
    EP97304879A 1996-07-06 1997-07-03 Cyclone separator Withdrawn EP0815944A3 (en)

    Applications Claiming Priority (2)

    Application Number Priority Date Filing Date Title
    GB9614258 1996-07-06
    GBGB9614258.3A GB9614258D0 (en) 1996-07-06 1996-07-06 A cyclone

    Publications (2)

    Publication Number Publication Date
    EP0815944A2 true EP0815944A2 (en) 1998-01-07
    EP0815944A3 EP0815944A3 (en) 1998-11-18

    Family

    ID=10796506

    Family Applications (1)

    Application Number Title Priority Date Filing Date
    EP97304879A Withdrawn EP0815944A3 (en) 1996-07-06 1997-07-03 Cyclone separator

    Country Status (4)

    Country Link
    EP (1) EP0815944A3 (en)
    CA (1) CA2209954A1 (en)
    GB (1) GB9614258D0 (en)
    NO (1) NO973130L (en)

    Citations (4)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    GB260776A (en) * 1925-11-05 1926-11-11 Wilfred Rothery Wood Improvements in cyclone separators or driers
    DE1245267B (en) * 1958-08-22 1967-07-20 Siemens Ag Centrifugal dust separator with a cyclone and a fine dust secondary separator in the form of a rotary flow vortex
    EP0566432A1 (en) * 1992-04-15 1993-10-20 Elf Aquitaine Production Three-phase cyclone separator
    DE9412631U1 (en) * 1994-08-05 1994-10-13 Ltg Lufttechnische Gmbh, 70435 Stuttgart cyclone

    Patent Citations (4)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    GB260776A (en) * 1925-11-05 1926-11-11 Wilfred Rothery Wood Improvements in cyclone separators or driers
    DE1245267B (en) * 1958-08-22 1967-07-20 Siemens Ag Centrifugal dust separator with a cyclone and a fine dust secondary separator in the form of a rotary flow vortex
    EP0566432A1 (en) * 1992-04-15 1993-10-20 Elf Aquitaine Production Three-phase cyclone separator
    DE9412631U1 (en) * 1994-08-05 1994-10-13 Ltg Lufttechnische Gmbh, 70435 Stuttgart cyclone

    Also Published As

    Publication number Publication date
    NO973130D0 (en) 1997-07-04
    CA2209954A1 (en) 1998-01-06
    GB9614258D0 (en) 1996-09-04
    NO973130L (en) 1998-01-07
    EP0815944A3 (en) 1998-11-18

    Similar Documents

    Publication Publication Date Title
    EP1028811B1 (en) Cyclone separator
    US7399412B2 (en) Guide means for centrifugal force separators, especially cyclone separators
    US6190543B1 (en) Cyclonic separator
    EP1059993B1 (en) Cleaning apparatus
    US4711720A (en) Tangentially staged hydrocyclones
    AU2002354406A1 (en) Cyclone separator, liquid collecting box and pressure vessel
    CA2215040A1 (en) Centrifugal separator assembly and method for separating particles from hot gas
    GB2424605A (en) Multi-cyclone apparatus for a vacuum cleaner
    CA1334838C (en) Apparatus for separating solid particles from a fluid
    EP1028812B1 (en) Cyclone separator
    EP0360360B1 (en) Swirl tube separator
    JPH0571303B2 (en)
    GB2330786A (en) Cyclone separator
    EP0815944A2 (en) Cyclone separator
    US5180493A (en) Rotating hydrocyclone separator with turbulence shield
    HU209077B (en) Method and apparatus for separating materials from media
    GB2367019A (en) Cyclone separator
    AU656957B2 (en) Hydrocyclone separator with turbulence shield
    US5133861A (en) Hydricyclone separator with turbulence shield
    JPH05301061A (en) Dust collecting apparatus
    GB1168989A (en) Centrifugal-Type Particle-Fluid-Separators
    WO1988002280A1 (en) Cyclone separator
    EP0231931A2 (en) A cyclone with forced gas stream whirling
    FI80836C (en) Two-phase or multi-phase cyclone separator or sorter
    SU982742A1 (en) Centrifugal separator

    Legal Events

    Date Code Title Description
    PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

    Free format text: ORIGINAL CODE: 0009012

    AK Designated contracting states

    Kind code of ref document: A2

    Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

    PUAL Search report despatched

    Free format text: ORIGINAL CODE: 0009013

    AK Designated contracting states

    Kind code of ref document: A3

    Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

    AKX Designation fees paid
    STAA Information on the status of an ep patent application or granted ep patent

    Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

    18D Application deemed to be withdrawn

    Effective date: 19990519

    REG Reference to a national code

    Ref country code: DE

    Ref legal event code: 8566