JPS6490030A - Three-phase fluidized reactor - Google Patents

Three-phase fluidized reactor

Info

Publication number
JPS6490030A
JPS6490030A JP24586687A JP24586687A JPS6490030A JP S6490030 A JPS6490030 A JP S6490030A JP 24586687 A JP24586687 A JP 24586687A JP 24586687 A JP24586687 A JP 24586687A JP S6490030 A JPS6490030 A JP S6490030A
Authority
JP
Japan
Prior art keywords
suction pipe
suction
liquid
inlet part
conical shape
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.)
Pending
Application number
JP24586687A
Other languages
Japanese (ja)
Inventor
Masahito Kaneko
Kazuto Kobayashi
Haruyoshi Fujita
Masami Kondo
Masanori Nakamura
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.)
Ryomei Engineering Co Ltd
Mitsubishi Heavy Industries Ltd
Original Assignee
Ryomei Engineering Co Ltd
Mitsubishi Heavy Industries Ltd
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 Ryomei Engineering Co Ltd, Mitsubishi Heavy Industries Ltd filed Critical Ryomei Engineering Co Ltd
Priority to JP24586687A priority Critical patent/JPS6490030A/en
Publication of JPS6490030A publication Critical patent/JPS6490030A/en
Pending legal-status Critical Current

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
    • B01J8/20—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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To efficiently separate gas from liquid, to restrain the amount of gas contained in the suction liquid and to stably operate the pump by providing a suction pipe inlet part of reverse conical shape and suction members of reverse conical shape coaxial with the suction pipe inlet part on the inlet part of a liquid suction pipe. CONSTITUTION:A three-phase fluidized layer is formed by supplying gas and liquid to a solid particle layer 2 from the bottom part through dispersers 11, and the liquid passed through the fluidized layer is sent out through the suction pipe 9 provided vertically on the center of the layer through the layer, and returned again to the reactor by a pump 13 to be circulated. The suction pipe inlet part 6 of reverse conical shape coaxial with the suction pipe 9 is provided on the upper part of the suction pipe, and moreover the suction members 7, 7' of reverse conical shape coaxial with the suction pipe 9 are provided on the inside of the suction inlet part 6. As a result, the gas is prevented from being accompanied with the suction liquid, and the circulating pump is prevented from the deterioration of discharge capacity, and the stable operation range of reactor is obtained.
JP24586687A 1987-10-01 1987-10-01 Three-phase fluidized reactor Pending JPS6490030A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24586687A JPS6490030A (en) 1987-10-01 1987-10-01 Three-phase fluidized reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24586687A JPS6490030A (en) 1987-10-01 1987-10-01 Three-phase fluidized reactor

Publications (1)

Publication Number Publication Date
JPS6490030A true JPS6490030A (en) 1989-04-05

Family

ID=17139983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24586687A Pending JPS6490030A (en) 1987-10-01 1987-10-01 Three-phase fluidized reactor

Country Status (1)

Country Link
JP (1) JPS6490030A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999003574A1 (en) * 1997-07-15 1999-01-28 Sasol Technology (Proprietary) Limited A process for producing liquid and, optionally, gaseous products from gaseous reactants
JP2007501121A (en) * 2003-05-16 2007-01-25 サソル テクノロジー （プロプリエタリ） リミテッド Method for producing a liquid product from a gaseous reactant and optionally producing a gaseous product
CN108291829A (en) * 2015-11-24 2018-07-17 斯伦贝谢技术有限公司 Stratified flow multi-phase flowmeter

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999003574A1 (en) * 1997-07-15 1999-01-28 Sasol Technology (Proprietary) Limited A process for producing liquid and, optionally, gaseous products from gaseous reactants
JP2007501121A (en) * 2003-05-16 2007-01-25 サソル テクノロジー （プロプリエタリ） リミテッド Method for producing a liquid product from a gaseous reactant and optionally producing a gaseous product
CN108291829A (en) * 2015-11-24 2018-07-17 斯伦贝谢技术有限公司 Stratified flow multi-phase flowmeter
CN108291829B (en) * 2015-11-24 2021-03-02 斯伦贝谢技术有限公司 Multiphase flow measurement system and method

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