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GB1358904A - Helical flow centrifugal separators - Google Patents

Helical flow centrifugal separators

Info

Publication number
GB1358904A
GB1358904A GB4929871A GB4929871A GB1358904A GB 1358904 A GB1358904 A GB 1358904A GB 4929871 A GB4929871 A GB 4929871A GB 4929871 A GB4929871 A GB 4929871A GB 1358904 A GB1358904 A GB 1358904A
Authority
GB
United Kingdom
Prior art keywords
flow
tube
crude gas
gas
chamber
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.)
Expired
Application number
GB4929871A
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.)
Siemens Corp
Original Assignee
Siemens Corp
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 Siemens Corp filed Critical Siemens Corp
Publication of GB1358904A publication Critical patent/GB1358904A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00Apparatus 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
    • 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
    • B04C5/02Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
    • B04C5/04Tangential inlets

Landscapes

  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Cyclones (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

1358904 Centrifugal separators SIEMENS AG 22 Oct 1971 [24 July 1971] 49298/71 Heading B2P A device for generating a helical flow in crude gas entering a helical flow centrifugal separator for the removal of solid or liquid impurities from the gas comprises an input tube 2, Figs. 1a and 1b, defining a zone closed at one end 7 and having an outlet at the opposite end, the end 7 having a form as at 12 such that in its region the zone diverges in the direcion from the end 7 to the opposite end, and one or more crude gas inlets 8, 9 opening into the region of the end 7 as such an angle that inflowing crude gas will have a helical flow imparted to it in the zone. The tube 2 is mounted in the vortex chamber 1 of the separator and is formed at its bottom with an annular conical surface 12 which merges into a central, streamlined, flow-stabilizing body 14. Auxiliary gas is supplied through a conduit 6 and a chamber 5 to infeed conduits 4 opening into the vortex chamber 1 and inclined obliquely downwardly to the chamber axis to create a potential helical flow 15 which entrains particles centrifugally hurled out of the rotary flow 13 created in the chamber 1. A portion 20 of the flow 15 discharges the particles, via an annular gap 17 constituted by the provision of a flange 16 on the tube 2, into a bin 18. Another portion of the flow 15 is split off at 19 from the portion 20 and is directed towards the vorex chamber axis above the crude gas inlet and combines with the rotary flow 13 to increase its helical motion. In a modification, Fig. 2 (not shown), the base of the tube 2 is designed as a cone and no central stabilizing body is provided. The crude gas feed conduits debouch into the tube obliquely from below and substantially parallel to the slope of the conical bottom. In a further modification, Fig. 3b, the crude gas enters the tube 2 through two parallel feed conduits 22, 23 opening into the tube at locations 24, 25 offset through at least 90‹ from each other. In a still further modification, Fig. 4a, in order to prevent adhesive particles of impurites from adhering to the inflow tube, a supplementary gas film is formed on the inner surface of the tube by feeding supplementary gas from an annular chamber 28 through nozzles 26, 27 inclined obliquely upwardly in the direction of the crude gas flow 13 to form a helical gas flow 29 which envelopes the inner crude gas flow.
GB4929871A 1971-07-24 1971-10-22 Helical flow centrifugal separators Expired GB1358904A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2137128A DE2137128C3 (en) 1971-07-24 1971-07-24 Device for generating swirl in a rotary flow vortex

Publications (1)

Publication Number Publication Date
GB1358904A true GB1358904A (en) 1974-07-03

Family

ID=5814734

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4929871A Expired GB1358904A (en) 1971-07-24 1971-10-22 Helical flow centrifugal separators

Country Status (11)

Country Link
US (1) US3744220A (en)
JP (1) JPS5250069Y2 (en)
AT (1) AT321256B (en)
CH (1) CH525714A (en)
CS (1) CS163258B2 (en)
DE (1) DE2137128C3 (en)
ES (1) ES198138Y (en)
FR (1) FR2147545A5 (en)
GB (1) GB1358904A (en)
HU (1) HU170072B (en)
RO (1) RO61563A (en)

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2220535C2 (en) * 1972-04-26 1974-03-07 Siemens Ag, 1000 Berlin U. 8000 Muenchen Rotary flow vortex for the sifting of fine-grained particles
CA1005363A (en) * 1972-06-12 1977-02-15 Robin E. Schaller Vortex forming apparatus and method
JPS49107448A (en) * 1973-02-15 1974-10-12
DE2341789C3 (en) * 1973-08-17 1980-02-28 Siemens Ag, 1000 Berlin Und 8000 Muenchen Arrangement for energy recovery in the clean gas outlet of a rotary flow vortex «
US3985526A (en) * 1976-01-08 1976-10-12 Aerodyne Development Corporation Dust collector with spaced volutes
JPS5465628U (en) * 1977-10-18 1979-05-10
JPS59190307U (en) * 1983-06-01 1984-12-17 石川島播磨重工業株式会社 Air bubble remover
DE3520032A1 (en) * 1985-06-04 1986-12-04 Istvàn Oberwil Majoros DEVICE FOR CONVERTING A FLUID FLOW
DE3523571C1 (en) * 1985-07-02 1986-11-20 Carl Still Gmbh & Co Kg, 4350 Recklinghausen Method and device for dedusting hot gases laden with solids
JPS62261842A (en) * 1986-05-09 1987-11-14 Nippon Air Curtain Kk Artificial tornado generating mechanism and utilization thereof
DE4434038A1 (en) * 1994-09-23 1996-03-28 Voest Alpine Krems Finaltech Device for separating at least one substance from a medium
US5971765A (en) * 1996-03-22 1999-10-26 Reel Efx, Inc. Method and system for generating artificial tornadoes and related vortex phenomena
FI107435B (en) * 1996-11-19 2001-08-15 Foster Wheeler Energia Oy Centrifugal separator device and process for separating particles from hot gas of a fluidized bed reactor
DE29621183U1 (en) * 1996-12-06 1997-02-20 Eder Maschinenfabrik GmbH & Co. KG, 84048 Mainburg Device for separating liquids and / or solids or gases with a different specific weight from a gas stream
US6279254B1 (en) 1998-10-26 2001-08-28 James C. Gill Fan advertising device
MY134342A (en) * 2001-12-31 2007-12-31 Shell Int Research Multistage fluid separation assembly and method
EP2131712B1 (en) * 2007-03-16 2013-07-10 LG Electronics Inc. Vacuum cleaner and dust separating apparatus thereof
CN101677731B (en) * 2007-04-12 2012-05-30 Lg电子株式会社 Dust separating apparatus of vacuum cleaner
KR100833361B1 (en) * 2007-05-07 2008-05-28 엘지전자 주식회사 Dust separator of vacuum cleaner
US8366802B2 (en) * 2008-07-14 2013-02-05 Metso Paper Sweden Ab Cyclone with improved separation of gas from gas laden liquid streams also at reduced flow volumes
IT1393821B1 (en) * 2009-04-20 2012-05-11 Progettazioni Innovative Di Gandinil & C S A S CYCLONE ASPIRATOR
CN101708416B (en) * 2009-11-30 2012-11-07 龙波 Facility for efficiently eliminating harmful substances such as smoke, dust, sulphur, and the like in fume gas
EP2512683B1 (en) * 2009-12-15 2015-03-18 Basf Se Cyclonic separator for the separation of liquid drops from a gas flow
GB2486910B (en) * 2010-12-30 2014-05-14 Cameron Int Corp Apparatus and method for fluid separation
CN106000665A (en) * 2016-05-31 2016-10-12 上海市政工程设计研究总院(集团)有限公司 Hydraulic cyclone separator with two inlets
RU2667548C1 (en) * 2017-07-27 2018-09-21 Федеральное государственное бюджетное научное учреждение "Всероссийский научно-исследовательский институт молочной промышленности (ФГБНУ "ВНИМИ") Disperse-liquid gases purification in the field of centrifugal forces method and device for its implementation
EP4329916B1 (en) 2021-04-26 2025-03-26 Basf Se Apparatus and method for separating liquid droplets from a gas stream by means of a centrifugal drum separator
EP4545173A1 (en) * 2023-10-23 2025-04-30 Toni Küpfer SA Mixing device, in particular for a sludge treatment system

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2320345A (en) * 1939-11-22 1943-06-01 Foster Wheeler Corp Apparatus for the separation of fluids
US3358844A (en) * 1965-08-17 1967-12-19 Siemens Ag Device for increasing the total amount of separation of a vortex separator

Also Published As

Publication number Publication date
DE2137128B2 (en) 1978-02-09
HU170072B (en) 1977-03-28
RO61563A (en) 1977-03-15
FR2147545A5 (en) 1973-03-09
CS163258B2 (en) 1975-08-29
JPS5250069Y2 (en) 1977-11-14
AT321256B (en) 1975-03-25
DE2137128C3 (en) 1978-10-05
JPS5110677U (en) 1976-01-26
ES198138Y (en) 1975-10-16
ES198138U (en) 1975-05-16
DE2137128A1 (en) 1973-02-08
CH525714A (en) 1972-07-31
US3744220A (en) 1973-07-10

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee