WO2001021286A1 - Procede et appareil permettant d'extraire des particules solides d'un gaz - Google Patents
Procede et appareil permettant d'extraire des particules solides d'un gaz Download PDFInfo
- Publication number
- WO2001021286A1 WO2001021286A1 PCT/NL2000/000670 NL0000670W WO0121286A1 WO 2001021286 A1 WO2001021286 A1 WO 2001021286A1 NL 0000670 W NL0000670 W NL 0000670W WO 0121286 A1 WO0121286 A1 WO 0121286A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas flow
- separating
- vortex
- particles
- solid particles
- Prior art date
Links
- 239000002245 particle Substances 0.000 title claims abstract description 47
- 239000007787 solid Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 25
- 239000000126 substance Substances 0.000 claims abstract description 22
- 238000009833 condensation Methods 0.000 claims abstract description 7
- 230000005494 condensation Effects 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 79
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 239000003795 chemical substances by application Substances 0.000 claims description 13
- 239000003054 catalyst Substances 0.000 claims description 6
- 238000002309 gasification Methods 0.000 claims description 4
- 230000000593 degrading effect Effects 0.000 claims description 3
- 230000002708 enhancing effect Effects 0.000 claims description 3
- 239000000446 fuel Substances 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 230000001133 acceleration Effects 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000011345 viscous material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/02—Amassing the particles, e.g. by flocculation
- B01D51/06—Amassing the particles, e.g. by flocculation by varying the pressure of the gas or vapour
- B01D51/08—Amassing the particles, e.g. by flocculation by varying the pressure of the gas or vapour by sound or ultrasonics
-
- 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
- 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
Definitions
- the invention relates to a method for separating a substance from a gas, comprising of realizing a vortex in the gas and separating the gas flow transversely of the axial direction of the vortex into a primary partial gas flow and a secondary partial gas flow, wherein the secondary partial gas flow comprises a larger content of substance for separating than the primary partial gas flow.
- Such a method is known from WO-A-99/01194.
- the method described in this document relates to removing water from natural gas before the natural gas is distributed in a pipeline network.
- Natural gas naturally contains water in the form of water vapour, which is undesirable in respect of corrosion or clogging.
- the above stated method is applied to prevent this.
- the water vapour is condensed by cooling, thereby causing a difference in density of the gas flows, so that the effect of the method according to the present invention is enhanced.
- the object of the invention is to provide a method wherein solid particles can be removed from large volumes of gas without too great a pressure loss and without excessive use of energy. This objective is achieved in that the substance to be separated comprises initially solid particles .
- Solid particles are understood to mean not only dust particles, grains and other particles included in the classical definition of "solid”, but also particles of viscous material, such as tar particles.
- chemical or physical reaction agents are added to the gas flow prior to or during forming of the vortex in the gas flow.
- reaction agents physical or chemical reactions can be excited or enhanced which result in changes in the properties of the dust particles for separating, so that the separating mechanism has a better action. This is particularly effective when the reaction agents are suitable for enhancing the condensation on the solid particles of gases taken up in the gas flow.
- the particles are exposed to a catalyst for degrading the particles during performing of the method.
- the invention also relates to a device for separating substances from a gas flow, comprising a device for forming a vortex in the gas flow and separating means for separating the gas flow into a primary gas flow and a secondary gas flow, wherein the secondary gas flow comprises a larger content of the substance for separating than the primary gas flow, wherein the device is dimensioned to separate initially solid particles.
- a device for separating substances from a gas flow comprising a device for forming a vortex in the gas flow and separating means for separating the gas flow into a primary gas flow and a secondary gas flow, wherein the secondary gas flow comprises a larger content of the substance for separating than the primary gas flow, wherein the device is dimensioned to separate initially solid particles.
- acceleration to supersonic speeds takes place.
- the invention also relates to a device wherein the acceleration device is adapted to accelerate the gas flow to a supersonic speed.
- chemical or physical reaction agents are added to the gas flow prior to or during forming of the vortex in the gas flow.
- the present invention further relates to a device wherein a feed device is placed preceding the vortex for feeding chemical or physical reaction agents to the gas flow for the purpose of removing solid particles from a gas, comprising a device for forming a vortex in the gas flow and separating means for separating the gas flow into a primary gas flow and a secondary gas flow, wherein the secondary gas flow comprises a larger content of solid particles.
- a feed device is placed preceding the vortex for feeding chemical or physical reaction agents to the gas flow.
- the device shown in figure 1 comprises a tube l which is provided with a first venturi 2. Downstream of the venturi 2 are arranged baffles 3 for forming of a swirl or vortex in the subsequent part of the tube.
- a device 4 is further arranged downstream for separating the gas flow into a primary gas flow, which is designated with arrow 5, and a secondary gas flow, which is designated with arrow 6.
- a primary gas flow which is designated with arrow 5
- a secondary gas flow which is designated with arrow 6.
- a pump or other device is of course placed upstream to cause the gas flow. It will be apparent that it is likewise possible to place a pump downstream.
- Use is made in the drawn embodiment of an additional acceleration device in the form of an extra venturi 8.
- Use is further made in the device of a feed channel 7 which is suitable for feeding chemical or physical reaction agents in the form of for instance gases or vapours . As a result of this reaction it is possible to have chemical reactions occur prior to the venturi 2.
- a layer of catalyst material 9 is applied in the vicinity of the discharge channels for the secondary gas flows 6. There is after all in the vicinity of these channels the greatest likelihood of sticky particles making contact with the wall and adhering to the wall .
- the catalyst material converts the adhered particles into fluid or gaseous material which can be readily taken up into the secondary gas flow.
- chemical or physical reaction agents are added to the gas flow prior to or during forming of the vortex in the gas flow.
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU79693/00A AU7969300A (en) | 1999-09-24 | 2000-09-20 | Method and apparatus for removing solid particles from a gas |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL1013135A NL1013135C2 (nl) | 1999-09-24 | 1999-09-24 | Werkwijze en inrichting voor het verwijderen van vaste deeltjes uit een gas. |
NL1013135 | 1999-09-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001021286A1 true WO2001021286A1 (fr) | 2001-03-29 |
Family
ID=19769934
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NL2000/000670 WO2001021286A1 (fr) | 1999-09-24 | 2000-09-20 | Procede et appareil permettant d'extraire des particules solides d'un gaz |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU7969300A (fr) |
NL (1) | NL1013135C2 (fr) |
WO (1) | WO2001021286A1 (fr) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003092858A1 (fr) * | 2002-04-29 | 2003-11-13 | Shell Internationale Research Maatschappij B.V. | Separation de fluide supersonique amelioree, par injection en pulverisation |
US6962199B1 (en) | 1998-12-31 | 2005-11-08 | Shell Oil Company | Method for removing condensables from a natural gas stream, at a wellhead, downstream of the wellhead choke |
CN100357018C (zh) * | 2005-06-07 | 2007-12-26 | 蒋遂安 | 一种反应物质发生快速反应的方法 |
US7318849B2 (en) | 2002-04-29 | 2008-01-15 | Shell Oil Company | Cyclonic fluid separator equipped with adjustable vortex finder position |
US7494535B2 (en) | 2002-09-02 | 2009-02-24 | Shell Oil Company | Cyclonic fluid separator |
WO2009084945A1 (fr) * | 2007-12-28 | 2009-07-09 | Twister B.V. | Procédé de séparation et de solidification du dioxyde de carbone d'un écoulement de fluide et ensemble de séparation de fluides |
EP2226109A1 (fr) * | 2009-03-04 | 2010-09-08 | J.E.H. Tetteroo | Installation et procédure d'échantillonnage de particules fines |
CN105189954A (zh) * | 2013-03-13 | 2015-12-23 | 巴斯夫公司 | 用于贫燃发动机的旋风分离器颗粒过滤 |
EP3363520A1 (fr) * | 2017-02-17 | 2018-08-22 | General Electric Company | Procédé et dispositif de séparation gaz-liquide |
WO2022263688A1 (fr) * | 2021-06-15 | 2022-12-22 | Arquimea Group S.A. | Système de condensation de la vapeur d'eau atmosphérique |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE202007010816U1 (de) * | 2007-08-02 | 2008-12-11 | Mann+Hummel Gmbh | Ölabscheidevorrichtung, insbesondere zur Kurbelgehäuseentlüftung |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1206007A (en) * | 1967-01-26 | 1970-09-23 | Eidgenoess Flugzeugwerk Emmen | Devices for separating a liquid and/or a vapour from a flowing carrier gas stream |
US3894851A (en) * | 1972-02-07 | 1975-07-15 | Midwest Research Inst | Removal of particulate matter with supersonic droplets |
US4285916A (en) * | 1978-08-29 | 1981-08-25 | Baisden C Robert | Exhaust gas pollution control system |
US4292050A (en) * | 1979-11-15 | 1981-09-29 | Linhardt & Associates, Inc. | Curved duct separator for removing particulate matter from a carrier gas |
EP0496128A1 (fr) * | 1991-01-25 | 1992-07-29 | Stork Product Engineering B.V. | Procédé et dispositif pour séparer un gaz d'un mélange gazeux |
WO1995003872A1 (fr) * | 1993-07-27 | 1995-02-09 | Europäische Atomgemeinschaft (Euratom) | Machine permettant de separer des particules d'aerosol |
US5857326A (en) * | 1997-11-24 | 1999-01-12 | General Motors Corporation | Exhaust poison trap |
WO1999001194A1 (fr) * | 1997-07-02 | 1999-01-14 | Shell Internationale Research Maatschappij B.V. | Procede servant a supprimer un constituant gazeux depuis un liquide |
WO2000040834A1 (fr) * | 1998-12-31 | 2000-07-13 | Shell Internationale Research Maatschappij B.V. | Procede d'evacuation de condensables d'un flux de gaz naturel, au niveau d'une tete de puits, en aval de la duse de tete de puits |
-
1999
- 1999-09-24 NL NL1013135A patent/NL1013135C2/nl not_active IP Right Cessation
-
2000
- 2000-09-20 WO PCT/NL2000/000670 patent/WO2001021286A1/fr active Application Filing
- 2000-09-20 AU AU79693/00A patent/AU7969300A/en not_active Abandoned
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1206007A (en) * | 1967-01-26 | 1970-09-23 | Eidgenoess Flugzeugwerk Emmen | Devices for separating a liquid and/or a vapour from a flowing carrier gas stream |
US3894851A (en) * | 1972-02-07 | 1975-07-15 | Midwest Research Inst | Removal of particulate matter with supersonic droplets |
US4285916A (en) * | 1978-08-29 | 1981-08-25 | Baisden C Robert | Exhaust gas pollution control system |
US4292050A (en) * | 1979-11-15 | 1981-09-29 | Linhardt & Associates, Inc. | Curved duct separator for removing particulate matter from a carrier gas |
EP0496128A1 (fr) * | 1991-01-25 | 1992-07-29 | Stork Product Engineering B.V. | Procédé et dispositif pour séparer un gaz d'un mélange gazeux |
WO1995003872A1 (fr) * | 1993-07-27 | 1995-02-09 | Europäische Atomgemeinschaft (Euratom) | Machine permettant de separer des particules d'aerosol |
WO1999001194A1 (fr) * | 1997-07-02 | 1999-01-14 | Shell Internationale Research Maatschappij B.V. | Procede servant a supprimer un constituant gazeux depuis un liquide |
US5857326A (en) * | 1997-11-24 | 1999-01-12 | General Motors Corporation | Exhaust poison trap |
WO2000040834A1 (fr) * | 1998-12-31 | 2000-07-13 | Shell Internationale Research Maatschappij B.V. | Procede d'evacuation de condensables d'un flux de gaz naturel, au niveau d'une tete de puits, en aval de la duse de tete de puits |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6962199B1 (en) | 1998-12-31 | 2005-11-08 | Shell Oil Company | Method for removing condensables from a natural gas stream, at a wellhead, downstream of the wellhead choke |
WO2003092858A1 (fr) * | 2002-04-29 | 2003-11-13 | Shell Internationale Research Maatschappij B.V. | Separation de fluide supersonique amelioree, par injection en pulverisation |
US7261766B2 (en) | 2002-04-29 | 2007-08-28 | Shell Oil Company | Supersonic fluid separation enhanced by spray injection |
US7318849B2 (en) | 2002-04-29 | 2008-01-15 | Shell Oil Company | Cyclonic fluid separator equipped with adjustable vortex finder position |
US7494535B2 (en) | 2002-09-02 | 2009-02-24 | Shell Oil Company | Cyclonic fluid separator |
CN100357018C (zh) * | 2005-06-07 | 2007-12-26 | 蒋遂安 | 一种反应物质发生快速反应的方法 |
WO2009084945A1 (fr) * | 2007-12-28 | 2009-07-09 | Twister B.V. | Procédé de séparation et de solidification du dioxyde de carbone d'un écoulement de fluide et ensemble de séparation de fluides |
CN101959574A (zh) * | 2007-12-28 | 2011-01-26 | 缠绕机公司 | 从流体流和流体分离组合件中移除和固化二氧化碳的方法 |
EA018055B1 (ru) * | 2007-12-28 | 2013-05-30 | Твистер Б.В. | Способ удаления и отверждения диоксида углерода из потока текучей среды и устройство разделения текучей среды |
US8475572B2 (en) | 2007-12-28 | 2013-07-02 | Twister B.V. | Method of removing and solidifying carbon dioxide from a fluid stream and fluid separation assembly |
EP2226109A1 (fr) * | 2009-03-04 | 2010-09-08 | J.E.H. Tetteroo | Installation et procédure d'échantillonnage de particules fines |
CN105189954A (zh) * | 2013-03-13 | 2015-12-23 | 巴斯夫公司 | 用于贫燃发动机的旋风分离器颗粒过滤 |
EP2971627A1 (fr) * | 2013-03-13 | 2016-01-20 | BASF Corporation | Filtration particulaire à cyclone pour moteurs à mélange pauvre |
EP3363520A1 (fr) * | 2017-02-17 | 2018-08-22 | General Electric Company | Procédé et dispositif de séparation gaz-liquide |
WO2022263688A1 (fr) * | 2021-06-15 | 2022-12-22 | Arquimea Group S.A. | Système de condensation de la vapeur d'eau atmosphérique |
Also Published As
Publication number | Publication date |
---|---|
AU7969300A (en) | 2001-04-24 |
NL1013135C2 (nl) | 2001-03-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2423167C2 (ru) | Многоступенчатая сепараторная емкость | |
US7048782B1 (en) | Apparatus and process for power recovery | |
WO2001021286A1 (fr) | Procede et appareil permettant d'extraire des particules solides d'un gaz | |
AU2008226388B2 (en) | Filter apparatus and method | |
CA2707363C (fr) | Application de microturbines pour reguler les emissions de gaz associe | |
JP6180525B2 (ja) | コークスキャッチャー | |
US4368677A (en) | Pulse combustion system for boilers | |
US20040011200A1 (en) | Method of converting a downflow/upflow wet flue gas desulfurization (wfgd) system to an upflow single-loop wfgd system | |
JPS5824174B2 (ja) | 排ガス処理法 | |
US20120269708A1 (en) | Method and installation for separating acid components, dust and tar from hot gases of gasification installations | |
US20050022667A1 (en) | Low-energy venturi pre-scrubber for an air pollution control system and method | |
RU2444408C2 (ru) | Система впуска для установки крекинга с псевдоожиженным катализатором с двумя трубами с восходящим потоком | |
JP2000509419A (ja) | パーホレーション・バレルを有するアンダーフロー・サイクロン | |
JP2982977B2 (ja) | 流動床反応炉装置の運転方法および流動床反応炉装置 | |
CA2067388A1 (fr) | Methode et dispositif d'epuration de gaz d'echappement | |
US20020100710A1 (en) | Desorbtion process and apparatus | |
CN1330428C (zh) | 一种防结焦旋风分离器 | |
KR100743399B1 (ko) | 반도체 제조공정에서 발생하는 염소가스와 과불화물의처리장치 | |
RU2462292C2 (ru) | Система для очистки дымовых газов | |
CN110115925B (zh) | 一种降低活性焦吸附塔入口烟气温度的工艺方法及装置 | |
US6248154B1 (en) | Operation process of a pumping-ejection apparatus and related apparatus | |
CN101007297A (zh) | 用于能量回收的装置和方法 | |
CN109321282A (zh) | 耦合发电中清除生物质燃气输送管道中焦油的方法 | |
CN220003436U (zh) | 气液分离装置和气液分离系统 | |
EP0576497A1 (fr) | Procede et appareil de raffinage d'huiles lubrifiantes usagees |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2000970292 Country of ref document: EP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 2000970292 Country of ref document: EP |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |