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GB2411365B - Downcomers for slurry bubble column reactors - Google Patents

Downcomers for slurry bubble column reactors

Info

Publication number
GB2411365B
GB2411365B GB0404069A GB0404069A GB2411365B GB 2411365 B GB2411365 B GB 2411365B GB 0404069 A GB0404069 A GB 0404069A GB 0404069 A GB0404069 A GB 0404069A GB 2411365 B GB2411365 B GB 2411365B
Authority
GB
United Kingdom
Prior art keywords
downcomers
bubble column
slurry bubble
column reactors
reactors
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.)
Expired - Fee Related
Application number
GB0404069A
Other versions
GB0404069D0 (en
GB2411365A (en
Inventor
Dag Schanke
Trond Myrstad
Pal Soraker
Olav Juliussen
Per Oscar Wiig
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.)
Petrosa
Equinor ASA
Original Assignee
Statoil ASA
Petro SA
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 Statoil ASA, Petro SA filed Critical Statoil ASA
Priority to GB0404069A priority Critical patent/GB2411365B/en
Publication of GB0404069D0 publication Critical patent/GB0404069D0/en
Priority to PCT/GB2005/000582 priority patent/WO2005082513A1/en
Priority to KR1020067019081A priority patent/KR20070019995A/en
Priority to JP2006553665A priority patent/JP2007526114A/en
Priority to EP05708383A priority patent/EP1720646A1/en
Publication of GB2411365A publication Critical patent/GB2411365A/en
Application granted granted Critical
Publication of GB2411365B publication Critical patent/GB2411365B/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/226—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
    • 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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
GB0404069A 2004-02-24 2004-02-24 Downcomers for slurry bubble column reactors Expired - Fee Related GB2411365B (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
GB0404069A GB2411365B (en) 2004-02-24 2004-02-24 Downcomers for slurry bubble column reactors
PCT/GB2005/000582 WO2005082513A1 (en) 2004-02-24 2005-02-17 Downcomers for slurry bubble column reactors
KR1020067019081A KR20070019995A (en) 2004-02-24 2005-02-17 Downcomer for Slurry Bubble Column Reactor
JP2006553665A JP2007526114A (en) 2004-02-24 2005-02-17 Downcomer for slurry foam column reactor
EP05708383A EP1720646A1 (en) 2004-02-24 2005-02-17 Downcomers for slurry bubble column reactors

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB0404069A GB2411365B (en) 2004-02-24 2004-02-24 Downcomers for slurry bubble column reactors

Publications (3)

Publication Number Publication Date
GB0404069D0 GB0404069D0 (en) 2004-03-31
GB2411365A GB2411365A (en) 2005-08-31
GB2411365B true GB2411365B (en) 2008-08-13

Family

ID=32050770

Family Applications (1)

Application Number Title Priority Date Filing Date
GB0404069A Expired - Fee Related GB2411365B (en) 2004-02-24 2004-02-24 Downcomers for slurry bubble column reactors

Country Status (5)

Country Link
EP (1) EP1720646A1 (en)
JP (1) JP2007526114A (en)
KR (1) KR20070019995A (en)
GB (1) GB2411365B (en)
WO (1) WO2005082513A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009149519A1 (en) * 2008-06-12 2009-12-17 Winwick Business Solutions Pty Ltd System for cultivation and processing of microorganisms and products therefrom
CN103962067B (en) * 2013-01-31 2017-02-08 中国科学院上海高等研究院 Method for carrying out slurry bed reaction

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5382748A (en) * 1992-12-18 1995-01-17 Exxon Research & Engineering Co. Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means
US5811468A (en) * 1997-05-06 1998-09-22 Exxon Research And Engineering Company Combination gas disengaging downcomer-rejuvenation tube for in-situ slurry catalyst rejuvenation (LAW541)
US5817702A (en) * 1997-05-02 1998-10-06 Exxon Research And Engineering Company Hydrocarbon synthesis catalyst slurry rejuvenation with gas disengagement
WO1998050494A1 (en) * 1997-05-06 1998-11-12 Exxon Research And Engineering Company Gas and solids reducing slurry downcomer
US20030073751A1 (en) * 2001-03-27 2003-04-17 Culross Claude Clarence Slurry catalyst rejuvenation in-situ in slurry reactor

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2204539A1 (en) * 1972-02-01 1973-08-23 Inst De Cercetari Pentru Chimi Chemical reactors - for end othermic or exothermic reactions carried out in presence of solid or liquid catalyst
US4455220A (en) * 1982-12-23 1984-06-19 Shell Oil Company Separation of fluid cracking catalyst particles from gaseous hydrocarbons
US4502947A (en) * 1984-05-21 1985-03-05 Mobil Oil Corporation Closed cyclone FCC catalyst separation method and apparatus
US4623446A (en) * 1984-05-21 1986-11-18 Mobil Oil Corporation Closed cyclone FCC catalyst separation with stripping gas injection and direct steam injection
US4996028A (en) * 1989-02-15 1991-02-26 Exxon Research And Engineering Company Trickle valve
US5811469A (en) * 1997-05-06 1998-09-22 Exxon Research And Engineering Company Slurry hydrocarbon synthesis with downcomer fed product filtration (LAW552)

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5382748A (en) * 1992-12-18 1995-01-17 Exxon Research & Engineering Co. Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means
US5817702A (en) * 1997-05-02 1998-10-06 Exxon Research And Engineering Company Hydrocarbon synthesis catalyst slurry rejuvenation with gas disengagement
US5811468A (en) * 1997-05-06 1998-09-22 Exxon Research And Engineering Company Combination gas disengaging downcomer-rejuvenation tube for in-situ slurry catalyst rejuvenation (LAW541)
WO1998050494A1 (en) * 1997-05-06 1998-11-12 Exxon Research And Engineering Company Gas and solids reducing slurry downcomer
US20030073751A1 (en) * 2001-03-27 2003-04-17 Culross Claude Clarence Slurry catalyst rejuvenation in-situ in slurry reactor

Also Published As

Publication number Publication date
EP1720646A1 (en) 2006-11-15
JP2007526114A (en) 2007-09-13
GB0404069D0 (en) 2004-03-31
GB2411365A (en) 2005-08-31
KR20070019995A (en) 2007-02-16
WO2005082513A1 (en) 2005-09-09

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Legal Events

Date Code Title Description
COOA Change in applicant's name or ownership of the application

Owner name: PETROSA

Free format text: FORMER APPLICANT(S): STATOIL ASA

Owner name: STATOIL ASA

Free format text: FORMER APPLICANT(S): STATOIL ASA

PCNP Patent ceased through non-payment of renewal fee

Effective date: 20170224