PL1658891T3 - Sposób regulacji ilości obiegowego materiału stałego w cyrkulacyjnym układzie reaktora ze złożem fluidalnym - Google Patents

Sposób regulacji ilości obiegowego materiału stałego w cyrkulacyjnym układzie reaktora ze złożem fluidalnym

Info

Publication number
PL1658891T3
PL1658891T3 PL05021919T PL05021919T PL1658891T3 PL 1658891 T3 PL1658891 T3 PL 1658891T3 PL 05021919 T PL05021919 T PL 05021919T PL 05021919 T PL05021919 T PL 05021919T PL 1658891 T3 PL1658891 T3 PL 1658891T3
Authority
PL
Poland
Prior art keywords
amount
reactor system
cyclone reactor
particles circulating
process regulating
Prior art date
Application number
PL05021919T
Other languages
English (en)
Inventor
Ulrich Muschelknautz
Bernhard Röper
Original Assignee
General Electric Technology Gmbh
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 General Electric Technology Gmbh filed Critical General Electric Technology Gmbh
Publication of PL1658891T3 publication Critical patent/PL1658891T3/pl

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
    • B01J8/1863—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised followed by a downward movement outside the reactor and subsequently re-entering it
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • 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

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Cyclones (AREA)
PL05021919T 2004-10-22 2005-10-07 Sposób regulacji ilości obiegowego materiału stałego w cyrkulacyjnym układzie reaktora ze złożem fluidalnym PL1658891T3 (pl)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004051477A DE102004051477B4 (de) 2004-10-22 2004-10-22 Verfahren zur Regulierung der Feststoffumlaufmenge eines zirkulierenden Wirbelschichtreaktorsystems
EP05021919A EP1658891B1 (de) 2004-10-22 2005-10-07 Verfahren zur Regulierung der Feststoffumlaufmenge eines zirkulierenden Wirbelschichtreaktorsystems

Publications (1)

Publication Number Publication Date
PL1658891T3 true PL1658891T3 (pl) 2008-05-30

Family

ID=35788407

Family Applications (1)

Application Number Title Priority Date Filing Date
PL05021919T PL1658891T3 (pl) 2004-10-22 2005-10-07 Sposób regulacji ilości obiegowego materiału stałego w cyrkulacyjnym układzie reaktora ze złożem fluidalnym

Country Status (5)

Country Link
US (1) US7316564B2 (pl)
EP (1) EP1658891B1 (pl)
CN (1) CN100512942C (pl)
DE (2) DE102004051477B4 (pl)
PL (1) PL1658891T3 (pl)

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CA2471048C (en) * 2002-09-19 2006-04-25 Suncor Energy Inc. Bituminous froth hydrocarbon cyclone
US7736501B2 (en) * 2002-09-19 2010-06-15 Suncor Energy Inc. System and process for concentrating hydrocarbons in a bitumen feed
JP5260034B2 (ja) * 2007-11-30 2013-08-14 三菱重工業株式会社 粉体分離装置及び固体燃料用バーナ
CA2689021C (en) 2009-12-23 2015-03-03 Thomas Charles Hann Apparatus and method for regulating flow through a pumpbox
CN102240614A (zh) * 2011-04-28 2011-11-16 广州迪森热能技术股份有限公司 生物质烟气旋风分离器
CN102213415A (zh) * 2011-04-28 2011-10-12 广州迪森热能技术股份有限公司 生物质烟气制备系统
FI123720B (fi) * 2011-10-17 2013-10-15 Maricap Oy Pneumaattisen materiaalinsiirtojärjestelmän erotuslaite ja menetelmä
CN103506056B (zh) * 2012-06-28 2015-09-30 广东先导稀材股份有限公司 无筛板的流化床及三氯化硼的制备方法
US9511339B2 (en) * 2013-08-30 2016-12-06 Honeywell International Inc. Series coupled fluidized bed reactor units including cyclonic plenum assemblies and related methods of hydrofluorination
DE102013112977B4 (de) * 2013-11-25 2015-08-06 Pfannenberg Gmbh Luftdurchtrittsvorrichtung  zur  Zuführung  gereinigter  Luft  in  einen  Innenraum eines Schaltschrankes und Schaltschrank mit einer solchen Luftdurchtrittsvorrichtung
DE102013020888A1 (de) * 2013-12-11 2015-06-11 Khd Humboldt Wedag Gmbh Kreislaufmahlanlage mit Vorsichter und Kugelmühle
CN103769014B (zh) * 2014-01-24 2016-07-20 神华集团有限责任公司 一种沸腾床反应器
KR101700436B1 (ko) * 2015-06-29 2017-01-31 한국전력공사 순환유동층 보일러의 열교환장치
CN108410507B (zh) * 2018-04-20 2021-04-09 中国科学院工程热物理研究所 旋风分离器及预热式气化系统
CN109340743B (zh) * 2018-09-29 2020-03-17 上海晓清环保科技有限公司 一种细煤粒循环流化床锅炉
CN109746130A (zh) * 2019-03-23 2019-05-14 湖北华电襄阳发电有限公司 生物质气化循环流化床旋风分离器装置
CN112390261A (zh) * 2019-08-13 2021-02-23 斯特里特技术有限公司 气相二氧化硅颗粒分离脱氢的系统和方法
CN112122019B (zh) * 2020-09-02 2021-10-15 东莞福莱仕智能电子科技有限公司 一种旋风分离装置及清洁设备
CN112138879B (zh) * 2020-09-02 2021-09-07 东莞福莱仕智能电子科技有限公司 一种旋风分离排尘方法
CN112043202B (zh) * 2020-09-02 2021-11-02 东莞福莱仕智能电子科技有限公司 一种旋风分离器及清洁设备

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US3273320A (en) * 1963-07-15 1966-09-20 Exxon Research Engineering Co Cyclone separator for high temperature operations
DE2524469A1 (de) * 1969-09-29 1976-05-13 Nils Anders Lennart Wikdahl Verfahren und vorrichtung zum trennen von gasgemischen
US3802570A (en) * 1972-10-25 1974-04-09 M Dehne Cyclone separator
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Also Published As

Publication number Publication date
EP1658891A1 (de) 2006-05-24
DE102004051477B4 (de) 2008-10-02
US7316564B2 (en) 2008-01-08
DE502005002150D1 (de) 2008-01-17
DE102004051477A1 (de) 2006-04-27
CN1817437A (zh) 2006-08-16
CN100512942C (zh) 2009-07-15
US20060230995A1 (en) 2006-10-19
EP1658891B1 (de) 2007-12-05

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