JPS6438136A - Three phase fluidized reaction device - Google Patents

Three phase fluidized reaction device

Info

Publication number
JPS6438136A
JPS6438136A JP19262787A JP19262787A JPS6438136A JP S6438136 A JPS6438136 A JP S6438136A JP 19262787 A JP19262787 A JP 19262787A JP 19262787 A JP19262787 A JP 19262787A JP S6438136 A JPS6438136 A JP S6438136A
Authority
JP
Japan
Prior art keywords
gas
suction pipe
liquid
conical member
flows
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
JP19262787A
Other languages
Japanese (ja)
Inventor
Masahito Kaneko
Kazuto Kobayashi
Masami Kondo
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP19262787A priority Critical patent/JPS6438136A/en
Publication of JPS6438136A publication Critical patent/JPS6438136A/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
    • 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

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 improve the separability of gas and liquid in the upper part of suction pipe in a three phase fluidized reaction device in which the liquid is recycled through the suction pipe in the device after passing through the fluidized layer, by providing one or plural upwardly convex conical members to the outer periphery of suction pipe. CONSTITUTION:One conical member 14, for instance, which is upwardly convex like an umbrella is provided on the outer periphery of middle part of the suction pipe 11. In this constitution, a part of gas-liquid mixing fluid which flows out from a catalyst layer and flows to the direction shown by arrows is caught by the conical member 14 when it flows between the reactor main body 1 and the suction pipe 11. The gas in the conical member is integrated into large bubbles 16 and flows out from the conical member 14. The liquid is separated from gas due to the density difference and flows out from the conical member 14. The gas and liquid passing by the conical member 14 and the gas and liquid flowing out from the conical member 14 are separated into gas and liquid at the suction part 10 of the suction pipe 11, and the separated liquid is introduced to the suction pipe 11. Though the gas of small bubbles is also introduced into the suction pipe 11, a large part of gas is discharged to the outside of reactor because a large part of gas is formed into the bubbles of large diameter.
JP19262787A 1987-08-03 1987-08-03 Three phase fluidized reaction device Pending JPS6438136A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19262787A JPS6438136A (en) 1987-08-03 1987-08-03 Three phase fluidized reaction device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19262787A JPS6438136A (en) 1987-08-03 1987-08-03 Three phase fluidized reaction device

Publications (1)

Publication Number Publication Date
JPS6438136A true JPS6438136A (en) 1989-02-08

Family

ID=16294394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19262787A Pending JPS6438136A (en) 1987-08-03 1987-08-03 Three phase fluidized reaction device

Country Status (1)

Country Link
JP (1) JPS6438136A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102190365A (en) * 2011-05-18 2011-09-21 宁波永峰环保工程科技有限公司 Three-phase bicirculating ozone catalytic fluidized bed and wastewater treatment method thereof
KR20180078333A (en) * 2014-04-25 2018-07-09 미쯔비시 케미컬 주식회사 Fluid bed reactor and method of producing nitrile compound using same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102190365A (en) * 2011-05-18 2011-09-21 宁波永峰环保工程科技有限公司 Three-phase bicirculating ozone catalytic fluidized bed and wastewater treatment method thereof
KR20180078333A (en) * 2014-04-25 2018-07-09 미쯔비시 케미컬 주식회사 Fluid bed reactor and method of producing nitrile compound using same

Similar Documents

Publication Publication Date Title
US5622545A (en) Separator for removing gases from water
US4753258A (en) Treatment basin for semiconductor material
US3488927A (en) Gas-liquid cyclone separator
US4320092A (en) Reaction vessel
EP0086736A3 (en) Process and device for the separation of solid and/or liquid particles from gases or of solids from liquids and for the separation of gases or liquids of differing densities
ATE172385T1 (en) FUMIGATION/FLOTATION REACTOR WITH ARRANGEMENTS FOR SEPARATING SOLIDS FROM LIQUIDS
TW324037B (en) Purifier with inverted rotating separator
EP0255642A3 (en) Liquid-gas dispersion reactor
JPS5940491B2 (en) Apparatus and method for dissolving gas in a liquid
EP0829305A3 (en) Flotation type separator
GR3000316T3 (en) Apparatus for generating waves
BE1002190A3 (en) SUSPENSION RECEPTION TANK CONTAINING SOLID SUBSTANCES.
JPS6438136A (en) Three phase fluidized reaction device
SE8204816L (en) VIRVELBEDDSREAKTOR
ES8205425A1 (en) MOBILE CATALYST BED REACTOR
DE59508120D1 (en) Device for separating liquids of different densities
JPS5753226A (en) Device for mixing gas into liquid or suspension
PE20010616A1 (en) METHOD FOR LEACHING SOLID MATERIAL FROM SLUDGE
ATE48242T1 (en) DEVICE FOR TREATMENT OF A HIGHLY FOAMING LIQUID WITH A GAS.
RU2301103C2 (en) Internal device for separation of the mixture containing one gaseous phase and one liquid phase
US6491826B1 (en) Systems and methods for separation of organics from fluids
HU211098B (en) Apparatus for carrying out pneumatic flotation
ATE135602T1 (en) IMPROVED SEPARATOR AND IMPROVEMENTS RELATED TO SEPARATORS
GB1377002A (en) Gas purifier unit
JPH0490458A (en) Gas-liquid separator