WO2009070058A2 - Séparateur centrifuge servant à séparer des particules de liquide d'un flux gazeux - Google Patents
Séparateur centrifuge servant à séparer des particules de liquide d'un flux gazeux Download PDFInfo
- Publication number
- WO2009070058A2 WO2009070058A2 PCT/RU2008/000800 RU2008000800W WO2009070058A2 WO 2009070058 A2 WO2009070058 A2 WO 2009070058A2 RU 2008000800 W RU2008000800 W RU 2008000800W WO 2009070058 A2 WO2009070058 A2 WO 2009070058A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas stream
- centrifugal separator
- separator
- central pipe
- gas
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 37
- 239000002245 particle Substances 0.000 title abstract 4
- 238000000926 separation method Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000007599 discharging Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 38
- 239000003921 oil Substances 0.000 abstract description 2
- 238000005201 scrubbing Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000011044 inertial separation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
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
- B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/14—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces arranged in a star shape
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- 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
- B04C3/06—Construction of inlets or outlets to the vortex chamber
-
- 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
- Centrifugal separator for separating liquid droplets from the gas stream
- the invention relates to the field of devices used to separate droplet moisture from a gas stream, and can be used for wet cleaning of gases emitted into the atmosphere, as well as the separation of water, oil and gas condensate drops from a gas stream, in any industry.
- Known is a foam-vortex apparatus for cleaning gases from liquid droplets, comprising a partially filled housing with nozzles for introducing gas and liquid, and a tube is located along the axis of the housing, the bottom of which is installed with a gap relative to the bottom the apparatus is a hollow cylinder, and in the upper part of the body above the liquid bath there are a vortex chamber and a separator.
- a disadvantage of the known apparatus should be recognized as the low efficiency of gas purification due to imperfections in the design of the apparatus.
- centrifugal separator comprising a housing with a lid, a tangentially mounted nozzle for the input of the gas to be cleaned, a transverse baffle mounted above it with vertical tubular straight-through separation elements mounted therein with swirls at the inlet and cooling system, as well as in the housing the outlet pipe for purified gas is fixed.
- the cooling system includes vertical heat pipes, the evaporation zones of which are in the form of axial displacers - fairings are located in the separation elements, and finned condensation zones are brought out through the housing cover.
- a disadvantage of the known apparatus should be recognized as the low efficiency of gas purification due to imperfection of the apparatus design.
- Known is a gas-liquid separator containing a vertical cylindrical body, pipelines for supplying a gas-liquid mixture and for removing gas and liquid, drain pipes, a partition separating the separator into chambers, while it is additionally equipped with a gas equalizing pipe connecting the separator body to the gas discharge pipe while the partition in the separator housing is conical, one of the chambers, the inlet one, is equipped with drain pipes and a concentrically mounted drop chamber with a swirl, bottom part and drain pipes, the lower ends of which are located below the ends of the drain pipes of the inlet chamber and are installed in the water seal in the lower part of the housing.
- a disadvantage of the known apparatus should be recognized as the low efficiency of gas purification due to imperfection of the apparatus design.
- Also known is a separator designed to remove moisture from a gas stream, comprising a housing, in the lower part of which there is a collector of separated liquid and an axial nozzle for introducing a shared flow, in addition, a blade swirl with hollow blades, a central pipe are placed in the housing with a conical bottom, which is the upper cover of the swirler, while the lower part of the conical bottom is connected by a pipe with a collection of separated liquid.
- an annular pocket with a cutter is additionally located in the upper part of the housing, in the upper part of the housing, in the upper part of the housing, in the upper part of the housing.
- centrifugal separator comprising a housing, a collector of separated liquid and an axial nozzle for introducing a shared stream, a blade swirler, a central tube with a conical bottom representing the upper cover of the swirl and having a nozzle for draining the separated liquid, while in the upper part of the housing there is an annular pocket with a flow shutoff.
- the separator is additionally equipped with an annular visor installed in the central tube and an additional blade swirl connected by a nozzle to the upper part of the annular channel and confused nozzles attached to the flow shutoff and the central tube to divert the cleaned stream.
- the technical result obtained by the implementation of the invention is to increase the efficiency of separation of liquid droplets from a high-speed gas stream.
- the centrifugal separator for separating liquid droplets from the gas stream comprises a cylindrical body with axial nozzles for introducing and discharging the gas stream and a separated liquid output unit located on the end surface of the housing, and in the housing coaxially from the gas inlet side sequentially located swirl and central tube.
- a conical displacer is installed in the perforated central pipe, and between the central pipe and the conical displacer along the entire length there are blades of the separation stage, and between the central pipe and the housing at the same level there are hydraulic shutter blades.
- the blades of the separation stage are made in the form of plates that rise in a spiral in the direction of flow.
- the shutter blades are made in the form of vertical plates, bent along the radius and the course of rotation of the main stream, and from the side of the central perforated pipe the edges of the plates are tightly connected, and from the side of the body are installed with a gap.
- the separator may contain an additional unit for outputting the separated liquid located on the opposite end surface of the housing.
- the proposed centrifugal separator in a preferred embodiment is schematically shown in the drawing, with the following notation: housing 1, inlet flange 2, pipe 3 for introducing a gas stream, swirler 4, central perforated pipe 5, conical displacer 6, flow straightener 7, pipe 8 for the output of the cleaned gas stream, the output flange 9, the blade 10 of the hydraulic lock, the blade 11 of the separation stage, the node 12 and the additional node 13 output of the separated liquid, the throttle device 14.
- the centrifugal separator for separating liquid droplets from the gas stream comprises a housing 1 provided with an axial pipe 3 for introducing a gas stream with an inlet flange 2.
- a swirl 4 is connected coaxially to the pipe 3 and connected to a central perforated rotor 4 pipe 5.
- a conical displacer 6 is installed in the central perforated pipe 5, around which along its entire length there are blades 11 of the separation stage.
- the output of the purified gas is carried out by means of a pipe 8 and an output flange 9.
- a flow rectifier 7 can be installed between the central perforated pipe 5 and the pipe 8.
- the separated liquid is discharged by means of a unit 12.
- the housing 1 can be equipped with an additional node 13 for outputting the separated liquid located on the opposite side of the housing 1.
- the nodes 12 and 13 for outputting the separated liquid can be equipped with throttling devices 14, through which the flow rate is selected for specified characteristics flow at the inlet to the separator.
- the device operates as follows.
- a gas stream with a small moisture content in the form of water droplets or gas condensate enters through the inlet flange 2 and pipe 3 to the swirler 4, where its flow pattern changes from translational along the pipe into a spiral in a spiral.
- swirler 4 the flow is divided into several independent parallel flows, which then go in the channel formed from the inside by a conical displacer 6, and from the outside - the Central perforated pipe 5 and the blades 11 of the separation stage.
- the flow in the channel of such geometry has a diffuser character.
- moisture is pushed to the inner walls of the central pipe 5.
- the droplets fall on the inner surface of the wall of the housing 1 and the outer surface of the blades 10 of the hydraulic lock. Here they are collected and drained due to the force of gravity to the lower part of the housing 1, from where moisture is removed through the node 12 to remove the separated liquid by blowing.
- the node 12 for outputting the separated liquid may be equipped with a throttle device 14, the flow rate through which is selected for the specified flow characteristics at the inlet to the separator.
- the housing 1 can be equipped with an additional node 13 for outputting the separated liquid located on the opposite side of the housing 1. The presence of an additional node allows you to use one separator in any position. After the cone displacer 6 in front of the outlet pipe 8, a flow rectifier 7 can be installed to relieve the flow swirl at the outlet of the separator.
- the hydraulic shutter blades 10 are made of vertical plates bent along the radius and the direction of rotation of the main flow, the edges of which are tightly connected on the side of the central perforated pipe and have a gap in the case side. Thus, a hydrodynamic lock is formed for the return exit of moisture droplets.
- modules can be optimized for specific flow characteristics and installed in series for deep gas dehydration.
- modules optimized for somewhat different input conditions and get a device that works in a fairly wide range of environmental parameters.
- Based on the proposed design it is possible to develop a series of separation devices that can be installed on pipelines with a diameter of 30 to 1500 mm.
- the proposed design can work both vertically and horizontally, as well as “upside down” and in any other intermediate position, which greatly simplifies the layout of the separator with other equipment. This is possible due to the fact that the centrifugal force that occurs when the flow swirls is several times higher than gravity.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Centrifugal Separators (AREA)
- Cyclones (AREA)
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2707189A CA2707189C (en) | 2007-11-29 | 2008-12-25 | Centrifugal separator for separating liquid particles from a gas flow |
US12/745,412 US8500836B2 (en) | 2007-11-29 | 2008-12-25 | Centrifugal separator for separating liquid particles from a gas flow |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2007143974 | 2007-11-29 | ||
RU2007143974/15A RU2363520C1 (ru) | 2007-11-29 | 2007-11-29 | Центробежный сепаратор для отделения капель жидкости от газового потока |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2009070058A2 true WO2009070058A2 (fr) | 2009-06-04 |
WO2009070058A3 WO2009070058A3 (fr) | 2009-08-06 |
Family
ID=40679186
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU2008/000800 WO2009070058A2 (fr) | 2007-11-29 | 2008-12-25 | Séparateur centrifuge servant à séparer des particules de liquide d'un flux gazeux |
Country Status (4)
Country | Link |
---|---|
US (1) | US8500836B2 (ru) |
CA (1) | CA2707189C (ru) |
RU (1) | RU2363520C1 (ru) |
WO (1) | WO2009070058A2 (ru) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2446001C1 (ru) * | 2010-10-26 | 2012-03-27 | Александр Владимирович Яшин | Сепаратор для осушки газа |
RU2462294C1 (ru) * | 2011-04-25 | 2012-09-27 | Общество с ограниченной ответственностью Инновационно-инжиниринговое предприятие "Нефтегазовые технологии" | Устройство для очистки газа и воздуха |
CN102423549B (zh) * | 2011-08-02 | 2013-12-18 | 中国科学院力学研究所 | 一种管道式导流片型油水分离器的除水装置和油水旋流分离器 |
RU2477646C1 (ru) * | 2011-10-14 | 2013-03-20 | Сергей Викторович Демихов | Центробежный сепаратор |
US9327214B2 (en) | 2012-02-13 | 2016-05-03 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
US9938812B2 (en) | 2012-02-13 | 2018-04-10 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
US9909405B2 (en) | 2012-02-13 | 2018-03-06 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
CA2836437A1 (en) | 2013-12-16 | 2015-06-16 | Specialized Desanders Inc. | An desanding apparatus and a method of using the same |
RU2597604C1 (ru) * | 2015-04-29 | 2016-09-10 | Открытое акционерное общество "Татнефть" имени В.Д. Шашина | Газожидкостной сепаратор |
RU2658037C1 (ru) * | 2017-08-29 | 2018-06-19 | Федеральное государственное бюджетное образовательное учреждение высшего образования Северо-Кавказский горно-металлургический институт (государственный технологический университет) (СКГМИ (ГТУ) | Капельно-жидкостный уловитель |
JP7495205B2 (ja) * | 2018-11-29 | 2024-06-04 | 株式会社デンソー | エアクリーナ |
CN109806673A (zh) * | 2019-03-06 | 2019-05-28 | 中国石油大学(北京) | 一种用于气体消泡的气液分离装置 |
CN114570120B (zh) * | 2022-05-06 | 2022-07-22 | 北京石油化工学院 | 一种适应入***气率大范围变化的双级管式气液分离器 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU827123A1 (ru) * | 1978-01-30 | 1981-05-07 | Предприятие П/Я В-8796 | Центробежный сепаратор |
RU2177821C1 (ru) * | 2001-03-30 | 2002-01-10 | Российский заочный институт текстильной и легкой промышленности | Устройство для очистки газа от мелкодисперсных примесей |
US20070163215A1 (en) * | 2003-10-07 | 2007-07-19 | Lagerstadt Torgny | Centrifugal separator for cleaning gases |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE624585A (ru) * | 1961-11-22 | |||
US3815339A (en) * | 1971-04-15 | 1974-06-11 | Gutehoffnungshuette Sterkrade | Centrifugal vapor-liquid separator |
US5130082A (en) * | 1990-12-20 | 1992-07-14 | General Electric Company | Low pressure drop gas-liquid separator |
GB9211663D0 (en) * | 1992-06-02 | 1992-07-15 | Merpro Azgaz Ltd | Liquid/gas seperator |
CN1082461A (zh) | 1992-08-07 | 1994-02-23 | 邓延忠 | 转筒式离心分离机 |
US5334239A (en) * | 1993-11-29 | 1994-08-02 | The United States Of America As Represented By The United States Department Of Energy | Passive gas separator and accumulator device |
RU2133136C1 (ru) | 1998-03-25 | 1999-07-20 | Дочернее акционерное общество "Центральное конструкторское бюро нефтеаппаратуры" РАО "ГАЗПРОМ" | Центробежный сепаратор |
EP1237641B1 (en) * | 1999-11-23 | 2015-09-09 | Marina Ellen Marinella Pavlatos | Engine with upstream and rotationally attached guard |
RU2190450C2 (ru) | 2000-10-30 | 2002-10-10 | Ооо Мнпп "Ратон" | Газожидкостной сепаратор |
RU2236888C1 (ru) | 2003-04-10 | 2004-09-27 | ЗАО НТК "МодульНефтеГазКомплект" | Сепаратор |
JP2007503296A (ja) | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | 電気化学セルスタックの処理ガスストリームから液体を分離する装置 |
-
2007
- 2007-11-29 RU RU2007143974/15A patent/RU2363520C1/ru not_active IP Right Cessation
-
2008
- 2008-12-25 WO PCT/RU2008/000800 patent/WO2009070058A2/ru active Application Filing
- 2008-12-25 US US12/745,412 patent/US8500836B2/en not_active Expired - Fee Related
- 2008-12-25 CA CA2707189A patent/CA2707189C/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU827123A1 (ru) * | 1978-01-30 | 1981-05-07 | Предприятие П/Я В-8796 | Центробежный сепаратор |
RU2177821C1 (ru) * | 2001-03-30 | 2002-01-10 | Российский заочный институт текстильной и легкой промышленности | Устройство для очистки газа от мелкодисперсных примесей |
US20070163215A1 (en) * | 2003-10-07 | 2007-07-19 | Lagerstadt Torgny | Centrifugal separator for cleaning gases |
Also Published As
Publication number | Publication date |
---|---|
RU2363520C1 (ru) | 2009-08-10 |
US8500836B2 (en) | 2013-08-06 |
CA2707189A1 (en) | 2009-06-04 |
US20110078987A1 (en) | 2011-04-07 |
WO2009070058A3 (fr) | 2009-08-06 |
CA2707189C (en) | 2013-03-12 |
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