JPS57105235A - Multi-stage fluidized layer type reaction apparatus - Google Patents

Multi-stage fluidized layer type reaction apparatus

Info

Publication number
JPS57105235A
JPS57105235A JP17890480A JP17890480A JPS57105235A JP S57105235 A JPS57105235 A JP S57105235A JP 17890480 A JP17890480 A JP 17890480A JP 17890480 A JP17890480 A JP 17890480A JP S57105235 A JPS57105235 A JP S57105235A
Authority
JP
Japan
Prior art keywords
fluid
pipes
partition plates
falling
fluidized
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
JP17890480A
Other languages
Japanese (ja)
Inventor
Kenji Kojima
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.)
Hitachi Plant Construction Co Ltd
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Construction Co Ltd
Hitachi Plant Technologies 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 Hitachi Plant Construction Co Ltd, Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Construction Co Ltd
Priority to JP17890480A priority Critical patent/JPS57105235A/en
Publication of JPS57105235A publication Critical patent/JPS57105235A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • B01J8/26Chemical 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
    • B01J8/28Chemical 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

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 provide the titled apparatus necessitating no auxiliary fluid for falling a powder and making a superficial velocity constant comprising opening particle falling pipes which pierce perforated partition plates of a fluidized layer divided into plural stages in a vertical direction and of which a lower end part is tapered above the lower perforated partition plate respectively. CONSTITUTION:An inside of a shaft shaped container 1 is divided into plural stages by perforated partition plates 5, 6, 7 and each stages are filled with a solid particle respectively to form a multi-stage fluidized layer. Through the partition plates 5, 6, particle falling pipes 11, 12 are respectively pierced and upper end surfaces thereof are fixed to said partition plates so as to be brought in line with surfaces thereof as well as other ends thereof are opposed to the lower partition plates 6, 7. In the above described constitution, if moving layers are respectively formed in insides of the pipes 11, 12 preliminarily by known means, a fluid superficial velocity of a fluid upwardly flowing through the insides of the pipes 11, 12 is made extremely low. Therefore, particles fluidized on upper surfaces of the pipes 11, 12 are fallen and particles of the fluidized layers 8, 9 can be respectively moved to the lower stage layers 9, 10. Because of increment pressure difference generated at both ends of the pipe 11, the fluid superficial velocity of the fluid raising through the inside of the pipe 11 is increased and resistance imparted to the falling fluid is increased and, therefore, a particle amount of the layer is returned to a steady condition.
JP17890480A 1980-12-19 1980-12-19 Multi-stage fluidized layer type reaction apparatus Pending JPS57105235A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17890480A JPS57105235A (en) 1980-12-19 1980-12-19 Multi-stage fluidized layer type reaction apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17890480A JPS57105235A (en) 1980-12-19 1980-12-19 Multi-stage fluidized layer type reaction apparatus

Publications (1)

Publication Number Publication Date
JPS57105235A true JPS57105235A (en) 1982-06-30

Family

ID=16056712

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17890480A Pending JPS57105235A (en) 1980-12-19 1980-12-19 Multi-stage fluidized layer type reaction apparatus

Country Status (1)

Country Link
JP (1) JPS57105235A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0760106A (en) * 1993-08-26 1995-03-07 Rinkai:Kk Multistage fluidized-bed solid-liquid contact device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0760106A (en) * 1993-08-26 1995-03-07 Rinkai:Kk Multistage fluidized-bed solid-liquid contact device

Similar Documents

Publication Publication Date Title
ATE34109T1 (en) METAL POWDER AND METHOD OF PRODUCTION.
EP0104947A3 (en) Multiple particle washing system and method of use
ES8607762A1 (en) Method for uniformly distributing discrete particles on a moving porous web.
ES8400249A1 (en) Particle washing system and method of use.
ES8102839A1 (en) Process and apparatus for effecting mass transfer.
JPS57105235A (en) Multi-stage fluidized layer type reaction apparatus
JPS54139167A (en) Axial-flow decanter-shaped centrifugal separator
JPS6464516A (en) Wiring method through conduit having different diameters
ATE6441T1 (en) DEVICE FOR EXCHANGE OF HEAT BETWEEN SOLID PARTICLES AND A STREAM OF GAS.
El Masry et al. Pulsating slurry flow in pipelines
JPS53100271A (en) Flow rate detector
JPS56147620A (en) Method and apparatus for regulating concentration
Mikhalev Simulation of processes in a deforming(river) channel.
JPS5735295A (en) Method for heat recovery of raw gas produced from coke-furnace
JPS5774581A (en) Steam generator
SU1560948A1 (en) Method of drying fluid materials
GB1212300A (en) Elutriator
EP0081267A3 (en) Apparatus for contacting particulate solid material with a fluid
FR2298780A1 (en) Counterflow heat exchange system for granular and gaseous materials - has columnar containers in which solid moves downwards by gravity, against coolant gas flow
JPS6463079A (en) Separating method for fluid
JPS56161223A (en) Airtight discharge device for powdery body
JPS56155630A (en) Granulator utilizing jet layer
JPS52129680A (en) Coarse particle separator for fluidized bed reactor
Spiess Flow behavior of bulk solids in pneumatic filling installations
Grimmett et al. Physical and Operational Features of a Pulsed Continuous Countercurrent Liquid-solids Contactor