GB1358904A - Helical flow centrifugal separators - Google Patents
Helical flow centrifugal separatorsInfo
- 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
Links
- 230000004048 modification Effects 0.000 abstract 3
- 238000012986 modification Methods 0.000 abstract 3
- 239000002245 particle Substances 0.000 abstract 3
- 239000000853 adhesive Substances 0.000 abstract 1
- 230000001070 adhesive effect Effects 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 230000000087 stabilizing effect Effects 0.000 abstract 1
Classifications
-
- 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
-
- 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
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction 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
- B04C5/04—Tangential 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.
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)
| 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)
| 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 |
-
1971
- 1971-07-24 DE DE2137128A patent/DE2137128C3/en not_active Expired
- 1971-09-09 CH CH1326571A patent/CH525714A/en not_active IP Right Cessation
- 1971-09-22 CS CS6749A patent/CS163258B2/cs unknown
- 1971-09-28 ES ES1971198138U patent/ES198138Y/en not_active Expired
- 1971-10-01 RO RO68332A patent/RO61563A/ro unknown
- 1971-10-06 AT AT862471A patent/AT321256B/en not_active IP Right Cessation
- 1971-10-21 FR FR7137917A patent/FR2147545A5/fr not_active Expired
- 1971-10-22 GB GB4929871A patent/GB1358904A/en not_active Expired
- 1971-10-26 US US00192142A patent/US3744220A/en not_active Expired - Lifetime
- 1971-11-01 HU HUSI1233A patent/HU170072B/hu unknown
-
1975
- 1975-06-03 JP JP1975075209U patent/JPS5250069Y2/ja not_active Expired
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 |