WO2006092006A1 - Separator apparatus - Google Patents

Separator apparatus Download PDF

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Publication number
WO2006092006A1
WO2006092006A1 PCT/AU2006/000257 AU2006000257W WO2006092006A1 WO 2006092006 A1 WO2006092006 A1 WO 2006092006A1 AU 2006000257 W AU2006000257 W AU 2006000257W WO 2006092006 A1 WO2006092006 A1 WO 2006092006A1
Authority
WO
WIPO (PCT)
Prior art keywords
fluid
outlet
swirl vane
separator apparatus
fluid inlet
Prior art date
Application number
PCT/AU2006/000257
Other languages
French (fr)
Inventor
Kim Goh
Gary James BROWN
Peter Stewart Hay
Original Assignee
Alcoa Of Australia Limited
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
Priority claimed from AU2005900972A external-priority patent/AU2005900972A0/en
Application filed by Alcoa Of Australia Limited filed Critical Alcoa Of Australia Limited
Priority to AU2006220227A priority Critical patent/AU2006220227A1/en
Priority to CA002600889A priority patent/CA2600889A1/en
Priority to BRPI0607984-9A priority patent/BRPI0607984A2/en
Publication of WO2006092006A1 publication Critical patent/WO2006092006A1/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
    • B01D21/265—Separation of sediment aided by centrifugal force or centripetal force by using a vortex inducer or vortex guide, e.g. coil
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • B04C2003/006—Construction of elements by which the vortex flow is generated or degenerated

Definitions

  • the present invention relates to a separator apparatus. More particularly, the separator apparatus of the present invention is able to be provided "in-line" in a process stream.
  • the separator apparatus of the present invention has further particular application in circumstances requiring removal of solids entrained in process streams that are not suited to use of other forms of filtering.
  • gas with entrained solids, such as dust is directed tangentially into the top of a conical chamber. Entrained dust particles move toward the outside of the separator and are funnelled downwardly into a receiver. The clean gas is removed from the chamber through an upper central opening.
  • cyclones are used to remove both solids and liquids from gases.
  • the separator apparatus of the present invention has as one object thereof to overcome substantially the above mentioned problems associated with the prior art.
  • a separator apparatus characterised by a fluid inlet, a fluid outlet, a separated solids outlet and a swirl vane, the swirl vane being located down stream of the fluid inlet but upstream of the fluid outlet and separated solids outlet, the swirl vane further being arranged so as to impart to the fluid flow passing therethrough a flow such that entrained particles move radially outward due to inertia, the fluid outlet being arranged inline with the fluid inlet and swirl vane whereas the solids outlet is fed by a radially arranged collector.
  • the fluid outlet is of the same gauge as the fluid inlet.
  • the swirl vain is provided in a helical arrangement arranged axially along the flow path of the fluid inlet and fluid outlet.
  • the collector is offset with respect to the axial orientation of the fluid inlet and fluid outlet so as to enhance flow of entrained particles to the solids outlet.
  • the swirl vane is provided in the form of four individual vanes arranged in a helical manner about a central axis of the fluid- flow path.
  • a method for the introduction of a separator apparatus into an existing fluid flow line the method characterised by the removal of a portion of the existing fluid flow line and the introduction of an in-line separator apparatus as defined hereinabove.
  • Figure 1 is a cross-sectional side view of a separator apparatus in accordance with the present invention.
  • Figure 2 is a cross-sectional side view of a swirl vane provided in the separator apparatus of Figure 1 ;
  • Figure 3 is a cross-sectional axial view of the swirl vane taken at B-B of Figure 2.
  • FIG. 1 there is shown a separator apparatus 10 in accordance with the present invention.
  • the separator apparatus 10 is provided in a form suitable for introduction into a fluid low line in circumstances requiring the removal of entrained solids therefrom.
  • the separator apparatus 10 comprises a fluid inlet 12 and a fluid outlet 14. Substantially adjacent the fluid inlet 12 is provided a temperature indicator 16 and a pressure indicator 18. A further pressure indicator 20 is provided adjacent the fluid outlet 14.
  • the separator apparatus 10 further comprises a fluid flow modulating portion or swirl vane 22.
  • the swirl vane 22 is provided within the bore of a piping 24 that forms it and the remainder of the separator apparatus 10 in large part. - A -
  • a collector Down stream of the swirl vane portion 22 is provided a collector, the collector comprising a radially flared portion 26 of the separator apparatus and an off-set collecting surface 28, which in turn feeds solids to a solids outlet 30.
  • the fluid outlet 14 projects upstream through the collector surface 28 and terminates at a point generally mid-way between the up-stream radial flared portion 26 and the surface 28.
  • the swirl vane portion 22 comprising a pipe 32 defining a bore 34, an inlet end 36 and an outlet end 38.
  • a swirl vane 40 comprising 4 intersecting vanes 42, the intersection thereof is provided co-axially within the bore 34 of the pipe 32.
  • the vanes 42 are arranged so as to describe a helical structure within the pipe 32.
  • fluid flowing into the separator apparatus 10 has induced therein a swirling or rotational movement whereby entrained solids move radially outward due to inertia as they pass downstream of the swirl vane portion 22.
  • the solid particles generally move into the flared portion 26 and are collected against the collector wall 28 and fed to the solids outlet 30, whilst fluid containing substantially less entrained solids pass into the piping comprising the fluid outlet 14 and which is arranged co-axially with the swirl vane portion 22 and fluid inlet 12.
  • the separator apparatus 10 of the present invention is arranged such that it is substantially in-line or co-axial with regard to existing fluid flow, thereby allowing it to be inserted into an existing fluid flow line with minimal re-engineering required.
  • the separator apparatus 10 of the present invention will result in minimal heat loss from a fluid flow, particularly when compared with typical filter means that might otherwise be utilised.
  • the applicant considers the separator apparatus 10 to have particular application in the Bayer process when installed in vapour lines between flash tanks used for flashing hot pregnant liquor and shell and tube heat exchangers which utilise the hot vapour from flashing to heat spent liquor.
  • These heat exchangers are subject to clogging and scale build up, which may result in inefficient heat exchange and require costly and difficult maintenance.
  • the provision of separator apparatus' 10 in these vapour lines is expected to significantly improve the performance of the heat exchangers over time.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Cyclones (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

Abstract A separator apparatus (10) characterised by a fluid inlet (12), a fluid outlet (14), a separated solids outlet (30) and a swirl vane (22), the swirl vane (22) being located down stream of the fluid inlet (12) but upstream of the fluid outlet (14) and separated solids outlet (30), the swirl vane (22) further being arranged so as to impart to the fluid flow passing therethrough a flow such that entrained particles move radially outward due to inertia, the fluid outlet (14) being arranged in-line with the fluid inlet (12) and swirl vane (22) whereas the solids outlet (30) is fed by a radially arranged collector.

Description

"Separator Apparatus"
Field of the Invention
The present invention relates to a separator apparatus. More particularly, the separator apparatus of the present invention is able to be provided "in-line" in a process stream. The separator apparatus of the present invention has further particular application in circumstances requiring removal of solids entrained in process streams that are not suited to use of other forms of filtering.
Background Art
The most commonly utilised separation apparatus for dust collection, or the separation of solids entrained in a gas stream, is the cyclone separator. In a typical separator, gas with entrained solids, such as dust, is directed tangentially into the top of a conical chamber. Entrained dust particles move toward the outside of the separator and are funnelled downwardly into a receiver. The clean gas is removed from the chamber through an upper central opening. Importantly, cyclones are used to remove both solids and liquids from gases.
In many circumstances it is necessary to retro-fit a separator into an existing fluid-flow line. Due to the physical constraints of the existing flow-line, with regard to space and orientation, it may not be possible to utilise a typical cyclone separator. In such circumstances filters of various forms may be utilised. However, in circumstances requiring minimum heat loss, filters are often inappropriate.
The separator apparatus of the present invention has as one object thereof to overcome substantially the above mentioned problems associated with the prior art.
The preceding discussion of the background art is intended to facilitate an understanding of the present invention only. It should be appreciated that the discussion is not an acknowledgement or admission that any of the material referred to was part of the common general knowledge in Australia or any other country or region as at the priority date of the application.
Throughout the specification, unless the context requires otherwise, the word "comprise" or variations such as "comprises" or "comprising", will be understood to imply the inclusion of a stated integer or group of integers but not the exclusion of any other integer or group of integers.
Disclosure of the Invention
In accordance with the present invention there is provided a separator apparatus characterised by a fluid inlet, a fluid outlet, a separated solids outlet and a swirl vane, the swirl vane being located down stream of the fluid inlet but upstream of the fluid outlet and separated solids outlet, the swirl vane further being arranged so as to impart to the fluid flow passing therethrough a flow such that entrained particles move radially outward due to inertia, the fluid outlet being arranged inline with the fluid inlet and swirl vane whereas the solids outlet is fed by a radially arranged collector.
Preferably, the fluid outlet is of the same gauge as the fluid inlet.
Still preferably, the swirl vain is provided in a helical arrangement arranged axially along the flow path of the fluid inlet and fluid outlet.
Still further preferably, the collector is offset with respect to the axial orientation of the fluid inlet and fluid outlet so as to enhance flow of entrained particles to the solids outlet.
In one form of the present invention the swirl vane is provided in the form of four individual vanes arranged in a helical manner about a central axis of the fluid- flow path.
In accordance with the present invention there is further provided a method for the introduction of a separator apparatus into an existing fluid flow line, the method characterised by the removal of a portion of the existing fluid flow line and the introduction of an in-line separator apparatus as defined hereinabove.
Brief Description of the Drawings
The separator apparatus of the present invention will now be described, by way of example only, with reference to one embodiment thereof and the accompanying drawings, in which:-
Figure 1 is a cross-sectional side view of a separator apparatus in accordance with the present invention;
Figure 2 is a cross-sectional side view of a swirl vane provided in the separator apparatus of Figure 1 ; and
Figure 3 is a cross-sectional axial view of the swirl vane taken at B-B of Figure 2.
Best Mode(s) for Carrying Out the Invention
In Figure 1 there is shown a separator apparatus 10 in accordance with the present invention. The separator apparatus 10 is provided in a form suitable for introduction into a fluid low line in circumstances requiring the removal of entrained solids therefrom.
The separator apparatus 10 comprises a fluid inlet 12 and a fluid outlet 14. Substantially adjacent the fluid inlet 12 is provided a temperature indicator 16 and a pressure indicator 18. A further pressure indicator 20 is provided adjacent the fluid outlet 14.
The separator apparatus 10 further comprises a fluid flow modulating portion or swirl vane 22. The swirl vane 22 is provided within the bore of a piping 24 that forms it and the remainder of the separator apparatus 10 in large part. - A -
Down stream of the swirl vane portion 22 is provided a collector, the collector comprising a radially flared portion 26 of the separator apparatus and an off-set collecting surface 28, which in turn feeds solids to a solids outlet 30. The fluid outlet 14 projects upstream through the collector surface 28 and terminates at a point generally mid-way between the up-stream radial flared portion 26 and the surface 28.
In Figures 2 and 3 there is shown the swirl vane portion 22 comprising a pipe 32 defining a bore 34, an inlet end 36 and an outlet end 38. Within the bore 34 is located a swirl vane 40 comprising 4 intersecting vanes 42, the intersection thereof is provided co-axially within the bore 34 of the pipe 32. The vanes 42 are arranged so as to describe a helical structure within the pipe 32.
In use, fluid flowing into the separator apparatus 10 has induced therein a swirling or rotational movement whereby entrained solids move radially outward due to inertia as they pass downstream of the swirl vane portion 22. The solid particles generally move into the flared portion 26 and are collected against the collector wall 28 and fed to the solids outlet 30, whilst fluid containing substantially less entrained solids pass into the piping comprising the fluid outlet 14 and which is arranged co-axially with the swirl vane portion 22 and fluid inlet 12.
The separator apparatus 10 of the present invention is arranged such that it is substantially in-line or co-axial with regard to existing fluid flow, thereby allowing it to be inserted into an existing fluid flow line with minimal re-engineering required.
Further, the separator apparatus 10 of the present invention will result in minimal heat loss from a fluid flow, particularly when compared with typical filter means that might otherwise be utilised. Largely for this reason the applicant considers the separator apparatus 10 to have particular application in the Bayer process when installed in vapour lines between flash tanks used for flashing hot pregnant liquor and shell and tube heat exchangers which utilise the hot vapour from flashing to heat spent liquor. These heat exchangers are subject to clogging and scale build up, which may result in inefficient heat exchange and require costly and difficult maintenance. The provision of separator apparatus' 10 in these vapour lines is expected to significantly improve the performance of the heat exchangers over time.
Modifications and variations such as would be apparent to the skilled addressee are considered to fall within the scope of the present invention.

Claims

Claims
1. A separator apparatus characterised by a fluid inlet, a fluid outlet, a separated solids outlet and a swirl vane, the swirl vane being located down stream of the fluid inlet but upstream of the fluid outlet and separated solids outlet, the swirl vane further being arranged so as to impart to the fluid flow passing therethrough a flow such that entrained particles move radially outward due to inertia, the fluid outlet being arranged in-line with the fluid inlet and swirl vane whereas the solids outlet is fed by a radially arranged collector.
2. An apparatus according to claim 1 , wherein the fluid outlet is of the same gauge as the fluid inlet.
3. An apparatus according to claim 1 or 2, wherein the swirl vain is provided in a helical arrangement arranged axially along the flow path of the fluid inlet and fluid outlet.
4. An apparatus according to any one of the preceding claims, wherein the collector is offset with respect to the axial orientation of the fluid inlet and fluid outlet so as to enhance flow of entrained particles to the solids outlet.
5. An apparatus according to any one of the preceding claims, wherein the swirl vane is provided in the form of four individual vanes arranged in a helical manner about a central axis of the fluid-flow path.
6. In accordance with the present invention there is further provided a method for the introduction of a separator apparatus into an existing fluid flow line, the method characterised by the removal of a portion of the existing fluid flow line and the introduction of an in-line separator apparatus as defined hereinabove.
7. A separator apparatus substantially as hereinbefore described with reference to the accompanying drawings.
8. A method for the introduction of a separator apparatus into an existing fluid flow line, the method being substantially as hereinbefore described with reference to the accompanying drawings.
PCT/AU2006/000257 2005-03-02 2006-02-28 Separator apparatus WO2006092006A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
AU2006220227A AU2006220227A1 (en) 2005-03-02 2006-02-28 Separator apparatus
CA002600889A CA2600889A1 (en) 2005-03-02 2006-02-28 Separator apparatus
BRPI0607984-9A BRPI0607984A2 (en) 2005-03-02 2006-02-28 separating instrument and method for introducing a separating instrument into an existing fluid flow line

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AU2005900972A AU2005900972A0 (en) 2005-03-02 Separator Apparatus
AU2005900972 2005-03-02

Publications (1)

Publication Number Publication Date
WO2006092006A1 true WO2006092006A1 (en) 2006-09-08

Family

ID=36940774

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU2006/000257 WO2006092006A1 (en) 2005-03-02 2006-02-28 Separator apparatus

Country Status (5)

Country Link
CN (1) CN101142029A (en)
BR (1) BRPI0607984A2 (en)
CA (1) CA2600889A1 (en)
RU (1) RU2403983C2 (en)
WO (1) WO2006092006A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8951336B2 (en) * 2009-03-23 2015-02-10 Shell Oil Company Vessel for removing solid particles from gases
AT508900B1 (en) * 2010-01-19 2011-05-15 Univ Wien Tech DEVICE AND METHOD FOR REMOVING WOVEN PARTS
CN102343188A (en) * 2011-10-27 2012-02-08 北京德天御投资管理有限责任公司 Dust removing device applied to pipeline
DE102011122322A1 (en) * 2011-12-23 2013-06-27 Mann + Hummel Gmbh Centrifugal separator and filter arrangement
CN104826402A (en) * 2015-04-20 2015-08-12 北京石油化工学院 Compact type in-line liquid separator
CN108124430B (en) * 2016-12-26 2020-08-28 江门市蓬江区鑫浩源科技有限公司 Vortex solid-liquid separator
CN106861940B (en) * 2017-02-17 2019-04-16 太原理工大学 Multi-product water-only cyclone is selected in a kind of underflow again

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US3957471A (en) * 1973-12-21 1976-05-18 Hoei Kogyo Kabushiki Kaisha Exhaust gas purifier
DE2633588A1 (en) * 1976-07-27 1978-02-09 Bassfeld Hans Joachim Dipl Kfm SEPARATOR FOR SOLID AND LIQUID PARTICLES FROM FLOWING GASES
SU742673A1 (en) * 1978-11-22 1980-06-25 Уральский Филиал Всесоюзного Дважды Ордена Трудового Красного Знамени Теплотехнического Научно-Исследовательского Института Им.Ф.Э.Дзержинского Dust concentrator
GB1592051A (en) * 1977-11-03 1981-07-01 Rolls Royce Cyclone separators
US4311494A (en) * 1977-09-26 1982-01-19 Facet Enterprises, Inc. Axial flow gas cleaning device
GB2287895A (en) * 1993-11-16 1995-10-04 Rolls Royce Plc Particle separation
WO1996011047A1 (en) * 1994-10-06 1996-04-18 Arnold, Adrian, Christopher Removal of particulate material
JP2001183489A (en) * 1999-12-24 2001-07-06 Hitachi Ltd Steam separator and boiling water reactor
WO2002009846A2 (en) * 2000-07-28 2002-02-07 Honeywell International Inc. Two-stage water extractor
US20020144931A1 (en) * 2000-06-02 2002-10-10 Sechrist Paul A. Cyclone for separating fine solid particles from a gas stream
US20040025481A1 (en) * 2002-08-06 2004-02-12 Visteon Global Technologies, Inc. Dust pre-separator for an automobile engine
EP1493489A1 (en) * 2003-07-04 2005-01-05 Mann+Hummel Gmbh Cyclone separator

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Publication number Priority date Publication date Assignee Title
US3957471A (en) * 1973-12-21 1976-05-18 Hoei Kogyo Kabushiki Kaisha Exhaust gas purifier
DE2633588A1 (en) * 1976-07-27 1978-02-09 Bassfeld Hans Joachim Dipl Kfm SEPARATOR FOR SOLID AND LIQUID PARTICLES FROM FLOWING GASES
US4311494A (en) * 1977-09-26 1982-01-19 Facet Enterprises, Inc. Axial flow gas cleaning device
GB1592051A (en) * 1977-11-03 1981-07-01 Rolls Royce Cyclone separators
SU742673A1 (en) * 1978-11-22 1980-06-25 Уральский Филиал Всесоюзного Дважды Ордена Трудового Красного Знамени Теплотехнического Научно-Исследовательского Института Им.Ф.Э.Дзержинского Dust concentrator
GB2287895A (en) * 1993-11-16 1995-10-04 Rolls Royce Plc Particle separation
WO1996011047A1 (en) * 1994-10-06 1996-04-18 Arnold, Adrian, Christopher Removal of particulate material
JP2001183489A (en) * 1999-12-24 2001-07-06 Hitachi Ltd Steam separator and boiling water reactor
US20020144931A1 (en) * 2000-06-02 2002-10-10 Sechrist Paul A. Cyclone for separating fine solid particles from a gas stream
WO2002009846A2 (en) * 2000-07-28 2002-02-07 Honeywell International Inc. Two-stage water extractor
US20040025481A1 (en) * 2002-08-06 2004-02-12 Visteon Global Technologies, Inc. Dust pre-separator for an automobile engine
EP1493489A1 (en) * 2003-07-04 2005-01-05 Mann+Hummel Gmbh Cyclone separator

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Also Published As

Publication number Publication date
RU2007134437A (en) 2009-04-10
RU2403983C2 (en) 2010-11-20
CN101142029A (en) 2008-03-12
BRPI0607984A2 (en) 2009-10-27
CA2600889A1 (en) 2006-09-08

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