JP2004533505A - Ｆｃｃ反応器 - Google Patents

Ｆｃｃ反応器 Download PDF

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Publication number
JP2004533505A
JP2004533505A JP2002583537A JP2002583537A JP2004533505A JP 2004533505 A JP2004533505 A JP 2004533505A JP 2002583537 A JP2002583537 A JP 2002583537A JP 2002583537 A JP2002583537 A JP 2002583537A JP 2004533505 A JP2004533505 A JP 2004533505A
Authority
JP
Japan
Prior art keywords
reaction vessel
cyclone
gas
primary
conduit
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.)
Ceased
Application number
JP2002583537A
Other languages
English (en)
Japanese (ja)
Other versions
JP2004533505A5 (https=
Inventor
イェ−モン・チェン
トーマス・シャウン・デウィッツ
ヘンドリクス・アリエン・ディルクセ
ヒュベルタス・ウィルヘルムス・アルベルタス・ドリース
リチャード・アディソン・サンボーン
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of JP2004533505A publication Critical patent/JP2004533505A/ja
Publication of JP2004533505A5 publication Critical patent/JP2004533505A5/ja
Ceased legal-status Critical Current

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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
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/18—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with auxiliary fluid assisting discharge
    • 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
    • B01J8/26—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 two or more fluidised beds, e.g. reactor and regeneration installations
    • B01J8/28—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 two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
    • 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
    • B01J8/386—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 internally, i.e. the particles rotate within the vessel
    • 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
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Cyclones (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Signal Processing For Digital Recording And Reproducing (AREA)
  • Memory System Of A Hierarchy Structure (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Catalysts (AREA)
JP2002583537A 2001-04-20 2002-04-11 Ｆｃｃ反応器 Ceased JP2004533505A (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US28535901P 2001-04-20 2001-04-20
PCT/EP2002/004142 WO2002086019A2 (en) 2001-04-20 2002-04-11 Fcc reactor vessel

Publications (2)

Publication Number Publication Date
JP2004533505A true JP2004533505A (ja) 2004-11-04
JP2004533505A5 JP2004533505A5 (https=) 2005-12-22

Family

ID=23093889

Family Applications (2)

Application Number Title Priority Date Filing Date
JP2002583537A Ceased JP2004533505A (ja) 2001-04-20 2002-04-11 Ｆｃｃ反応器
JP2002583096A Ceased JP2004534112A (ja) 2001-04-20 2002-04-11 サイクロン分離器

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP2002583096A Ceased JP2004534112A (ja) 2001-04-20 2002-04-11 サイクロン分離器

Country Status (10)

Country Link
EP (2) EP1379607B1 (https=)
JP (2) JP2004533505A (https=)
AT (1) ATE427346T1 (https=)
AU (2) AU2002310844B2 (https=)
BR (2) BR0208964A (https=)
CA (2) CA2444620A1 (https=)
DE (1) DE60231800D1 (https=)
MX (2) MXPA03009472A (https=)
RU (2) RU2294954C2 (https=)
WO (2) WO2002085527A2 (https=)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012533428A (ja) * 2009-07-22 2012-12-27 ストーン アンド ウェブスター プロセス テクノロジー インコーポレーテッド 外部ｆｃｃライザーのための分離およびストリッピング装置

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102814151B (zh) * 2011-06-08 2014-02-26 富德（北京）能源化工有限公司 由含氧化合物制烯烃的流化床反应器和方法
DE102011088147A1 (de) 2011-12-09 2013-06-13 Evonik Industries Ag Verbundkörper, umfassend ein Verbundmaterial
EP2914362B1 (en) * 2012-10-31 2022-11-09 Dow Global Technologies LLC Process for minimizing attrition of catalyst particles
WO2015000938A1 (en) * 2013-07-02 2015-01-08 Shell Internationale Research Maatschappij B.V. A method of converting oxygenates to olefins
FR3082125B1 (fr) * 2018-06-06 2021-05-21 Ifp Energies Now Dispositif de distribution de melange polyphasique dans une enceinte comportant un milieu fluidise

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5039397A (en) * 1984-05-21 1991-08-13 Mobil Oil Corporation Closed cyclone FCC catalyst separation method and apparatus
US4988430A (en) * 1989-12-27 1991-01-29 Uop Supplying FCC lift gas directly from product vapors
US5449498A (en) * 1990-11-15 1995-09-12 Uop FCC stripper with multiple integrated disengager
FR2684566B1 (fr) * 1991-12-05 1994-02-25 Institut Francais Petrole Separateur extracteur cyclonique a co-courant.
US5298151A (en) * 1992-11-19 1994-03-29 Texaco Inc. Ebullated bed hydroprocessing of petroleum distillates
RU2112008C1 (ru) * 1995-11-01 1998-05-27 Владимир Петрович Агашков Способ переработки углеводородсодержащего сырья
US5869008A (en) * 1996-05-08 1999-02-09 Shell Oil Company Apparatus and method for the separation and stripping of fluid catalyst cracking particles from gaseous hydrocarbons
ES2244225T3 (es) * 1998-11-06 2005-12-01 Shell Internationale Research Maatschappij B.V. Aparato separador.
US6846463B1 (en) * 1999-02-23 2005-01-25 Shell Oil Company Gas-solid separation process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012533428A (ja) * 2009-07-22 2012-12-27 ストーン アンド ウェブスター プロセス テクノロジー インコーポレーテッド 外部ｆｃｃライザーのための分離およびストリッピング装置

Also Published As

Publication number Publication date
MXPA03009472A (es) 2004-02-12
JP2004534112A (ja) 2004-11-11
BR0208964A (pt) 2004-04-20
EP1379607B1 (en) 2009-04-01
CA2444620A1 (en) 2002-10-31
ATE427346T1 (de) 2009-04-15
MXPA03009473A (es) 2004-02-12
BR0208963A (pt) 2004-07-13
WO2002086019A2 (en) 2002-10-31
RU2298577C2 (ru) 2007-05-10
WO2002085527A2 (en) 2002-10-31
DE60231800D1 (de) 2009-05-14
WO2002085527A3 (en) 2003-02-13
RU2003133729A (ru) 2005-04-10
WO2002086019A3 (en) 2003-01-09
RU2003133727A (ru) 2005-04-10
CA2444613A1 (en) 2002-10-31
EP1379607A2 (en) 2004-01-14
RU2294954C2 (ru) 2007-03-10
AU2002310844B2 (en) 2006-12-14
EP1379608A2 (en) 2004-01-14
AU2002302533B2 (en) 2006-11-30

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