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EA200000090A1 - Способ для удаления газообразного компонента из текучей среды - Google Patents

Способ для удаления газообразного компонента из текучей среды

Info

Publication number
EA200000090A1
EA200000090A1 EA200000090A EA200000090A EA200000090A1 EA 200000090 A1 EA200000090 A1 EA 200000090A1 EA 200000090 A EA200000090 A EA 200000090A EA 200000090 A EA200000090 A EA 200000090A EA 200000090 A1 EA200000090 A1 EA 200000090A1
Authority
EA
Eurasian Patent Office
Prior art keywords
flow
specified
particles
medium
component
Prior art date
Application number
EA200000090A
Other languages
English (en)
Other versions
EA001591B1 (ru
Inventor
Марко Беттинг
Корнелис Антони Тьенк Виллинк
Йоханнес Мигюэль Хенри Мария Ван Вен
Original Assignee
Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
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 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. filed Critical Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
Publication of EA200000090A1 publication Critical patent/EA200000090A1/ru
Publication of EA001591B1 publication Critical patent/EA001591B1/ru

Links

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
    • B04C3/06—Construction of inlets or outlets to the vortex chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • 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
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
    • B01D5/0021—Vortex
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/24—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by centrifugal force
    • 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
    • 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
    • B04C3/02—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 with heating or cooling, e.g. quenching, means
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Cyclones (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Предложен способ для удаления заданного газообразного компонента из потока среды, содержащей множество газообразных компонентов. На поток воздействуют таким образом, чтобы он протекал через трубопровод со сверхзвуковой скоростью для того, чтобы температура среды понизилась ниже некоторой заданной температуры, при которой происходит либо конденсация, либо затвердевание компонента, подлежащего удалению, в результате чего образуются частицы указанного компонента. Указанный трубопровод имеет завихряющие средства, предназначенные для придания вихревого характера потока среды, побуждая тем самым частицы направляться в сторону внешнего, радиально расположенного участка зоны сбора частиц в потоке. В потоке генерируют ударную волну для того, чтобы уменьшить осевую скорость потока среды до подзвуковой скорости. Образовавшиеся частицы удаляются в виде отходящего потока из указанного внешнего, радиально расположенного участка зоны сбора частиц, причем указанную ударную волну генерируют в точке, расположенной за указанными завихряющими средствами (т. е. ниже в направлении потока), но перед указанной зоной сбора частиц.Международная заявка была опубликована вместе с отчетом о международном поиске.
EA200000090A 1997-07-02 1998-07-01 Способ удаления газообразного компонента из текучей среды EA001591B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP97202020 1997-07-02
PCT/EP1998/004178 WO1999001194A1 (en) 1997-07-02 1998-07-01 Removing a gaseous component from a fluid

Publications (2)

Publication Number Publication Date
EA200000090A1 true EA200000090A1 (ru) 2000-06-26
EA001591B1 EA001591B1 (ru) 2001-06-25

Family

ID=8228507

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200000090A EA001591B1 (ru) 1997-07-02 1998-07-01 Способ удаления газообразного компонента из текучей среды

Country Status (24)

Country Link
EP (1) EP1017465B1 (ru)
JP (1) JP4906170B2 (ru)
KR (1) KR100557269B1 (ru)
CN (1) CN1145513C (ru)
AR (1) AR013158A1 (ru)
AU (1) AU725574B2 (ru)
BR (1) BR9810386A (ru)
CA (1) CA2294708C (ru)
DE (1) DE69809274T2 (ru)
DK (1) DK1017465T3 (ru)
DZ (1) DZ2545A1 (ru)
EA (1) EA001591B1 (ru)
EG (1) EG21611A (ru)
ES (1) ES2186204T3 (ru)
ID (1) ID24531A (ru)
IL (1) IL133297A (ru)
JO (1) JO2025B1 (ru)
MY (1) MY129174A (ru)
NO (1) NO317006B1 (ru)
NZ (1) NZ501454A (ru)
PE (1) PE50999A1 (ru)
RO (1) RO120045B1 (ru)
WO (1) WO1999001194A1 (ru)
ZA (1) ZA985706B (ru)

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CA2286509C (en) 1998-10-16 2005-04-26 Translang Technologies Ltd. Method of and apparatus for the separation of components of gas mixtures and liquefaction of a gas
GC0000091A (en) * 1998-12-31 2004-06-30 Shell Int Research Method for removing condensables from a natural gas stream.
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
US6524368B2 (en) * 1998-12-31 2003-02-25 Shell Oil Company Supersonic separator apparatus and method
NL1013135C2 (nl) * 1999-09-24 2001-03-30 Kema Nv Werkwijze en inrichting voor het verwijderen van vaste deeltjes uit een gas.
MY134342A (en) * 2001-12-31 2007-12-31 Shell Int Research Multistage fluid separation assembly and method
US7318849B2 (en) 2002-04-29 2008-01-15 Shell Oil Company Cyclonic fluid separator equipped with adjustable vortex finder position
EA006303B1 (ru) 2002-04-29 2005-10-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Повышение эффективности сверхзвуковой сепарации текучей среды за счет инжекции распыляемого материала
US7494535B2 (en) 2002-09-02 2009-02-24 Shell Oil Company Cyclonic fluid separator
JP4285108B2 (ja) * 2003-06-25 2009-06-24 東京エレクトロン株式会社 トラップ装置、処理システム及び不純物除去方法
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WO2007031476A1 (en) * 2005-09-12 2007-03-22 Twister B.V. Method and device for enhancing condensation and separation in a fluid separator
MY148819A (en) 2006-06-29 2013-06-14 Shell Int Research Cyclonic liquid degassing separator and method for degassing a fluid mixture
WO2008017577A1 (de) * 2006-08-07 2008-02-14 Alstom Technology Ltd Verfahren zur abtrennung von co2 aus einem gasstrom, co2-abtrennvorrichtung zur durchführung des verfahrens, dralldüse für eine co2-abtrennvorrichtung sowie anwendung der co2-abtrennvorrichtung
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
EP2085587A1 (en) * 2008-02-04 2009-08-05 ALSTOM Technology Ltd Low carbon emissions combined cycle power plant and process
WO2010074565A1 (en) 2008-12-22 2010-07-01 Twister B.V. Method of removing carbon dioxide from a fluid stream and fluid separation assembly
EP2226109A1 (en) 2009-03-04 2010-09-08 J.E.H. Tetteroo Installation and procedure for sampling of fine particles
CN101700456B (zh) * 2009-10-16 2012-05-23 西安交通大学 激波可控超音速气体除湿装置
CN102102505B (zh) * 2009-12-16 2014-01-15 中国石油天然气股份有限公司 一种提高井下蒸汽干度注汽管柱及其注汽方法
CN101829456B (zh) * 2010-05-21 2012-01-04 福建鑫泽环保设备工程有限公司 烟囱脱水装置
CA2800823A1 (en) 2010-06-01 2011-12-08 Shell Internationale Research Maatschappij B.V. Low emission power plant
US8858680B2 (en) 2010-06-01 2014-10-14 Shell Oil Company Separation of oxygen containing gases
WO2011153146A1 (en) 2010-06-01 2011-12-08 Shell Oil Company Separation of gases produced by combustion
US8858679B2 (en) 2010-06-01 2014-10-14 Shell Oil Company Separation of industrial gases
CN102095609B (zh) * 2010-11-18 2012-08-22 山西省电力公司电力科学研究院 烟气采样脱水装置
CN102166436B (zh) * 2011-01-20 2013-10-02 上海益道投资管理有限公司 多组分污染流体净化方法及设备
WO2013033425A1 (en) 2011-08-31 2013-03-07 Alliant Techsystems Inc. Inertial extraction system
EP2610296A1 (de) 2011-12-29 2013-07-03 Lanxess Deutschland GmbH Verfahren zur Herstellung von gereinigten Nitrilkautschuken
DE102013104645A1 (de) * 2013-05-06 2014-11-06 Dieffenbacher GmbH Maschinen- und Anlagenbau Vorrichtung und Verfahren zum Abscheiden von Fremdpartikeln aus einem Gasstrom
WO2017112419A1 (en) 2015-12-22 2017-06-29 Eastman Chemical Company Supersonic treatment of vapor streams for separation and drying of hydrocarbon gases
CN107413085A (zh) * 2016-05-23 2017-12-01 中石化洛阳工程有限公司 一种油气管道在线除砂装置
CN107525293A (zh) * 2016-06-20 2017-12-29 通用电气公司 制冷系统和方法以及用于生产液化天然气的系统和方法
RU2688509C1 (ru) * 2018-08-28 2019-05-21 Общество с ограниченной ответственностью "Газпром проектирование" Способ обогащения гелием гелийсодержащего природного газа
DE102019214756A1 (de) * 2019-09-26 2021-04-01 Robert Bosch Gmbh Vorrichtung zur Abscheidung von Wasser aus einem Wasser-Dampf-Luft-Gemischstrom
CN110732188B (zh) * 2019-10-21 2020-11-17 西安交通大学 一种管内相分隔分流式高流速气液分离装置和方法
CN112495321B (zh) * 2020-11-20 2023-01-20 邵阳学院 一种采用拉法尔效应冷凝生物油的装置
KR102593784B1 (ko) * 2021-08-11 2023-10-25 (주)에이치앤지텍 압축 공기용 디퓨저 및 이에 의한 압축 공기 측정 장치

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Also Published As

Publication number Publication date
MY129174A (en) 2007-03-30
CA2294708A1 (en) 1999-01-14
EP1017465B1 (en) 2002-11-06
BR9810386A (pt) 2000-09-05
AU725574B2 (en) 2000-10-12
DZ2545A1 (fr) 2003-02-08
IL133297A0 (en) 2001-04-30
ZA985706B (en) 1999-01-27
KR100557269B1 (ko) 2006-03-07
EG21611A (en) 2001-12-31
ID24531A (id) 2000-07-20
KR20010014338A (ko) 2001-02-26
NO317006B1 (no) 2004-07-19
CN1145513C (zh) 2004-04-14
ES2186204T3 (es) 2003-05-01
WO1999001194A1 (en) 1999-01-14
CN1261814A (zh) 2000-08-02
JP2002507152A (ja) 2002-03-05
JP4906170B2 (ja) 2012-03-28
CA2294708C (en) 2007-08-28
NZ501454A (en) 2000-09-29
AU8857098A (en) 1999-01-25
DE69809274D1 (de) 2002-12-12
JO2025B1 (en) 1999-05-15
DE69809274T2 (de) 2003-08-28
PE50999A1 (es) 1999-05-28
EA001591B1 (ru) 2001-06-25
EP1017465A1 (en) 2000-07-12
RO120045B1 (ro) 2005-08-30
NO996546D0 (no) 1999-12-29
DK1017465T3 (da) 2002-11-25
IL133297A (en) 2003-10-31
AR013158A1 (es) 2000-12-13
NO996546L (no) 1999-12-29

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MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

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