JPS5645755A - Two phase fluidized type reaction apparatus - Google Patents

Two phase fluidized type reaction apparatus

Info

Publication number
JPS5645755A
JPS5645755A JP12161179A JP12161179A JPS5645755A JP S5645755 A JPS5645755 A JP S5645755A JP 12161179 A JP12161179 A JP 12161179A JP 12161179 A JP12161179 A JP 12161179A JP S5645755 A JPS5645755 A JP S5645755A
Authority
JP
Japan
Prior art keywords
liquid
solid phase
reaction apparatus
spindly
type reaction
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.)
Granted
Application number
JP12161179A
Other languages
Japanese (ja)
Other versions
JPS596173B2 (en
Inventor
Tatsu Fukushima
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.)
Tokyo Rikakikai Co Ltd
Original Assignee
Tokyo Rikakikai Co 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 Tokyo Rikakikai Co Ltd filed Critical Tokyo Rikakikai Co Ltd
Priority to JP54121611A priority Critical patent/JPS596173B2/en
Publication of JPS5645755A publication Critical patent/JPS5645755A/en
Publication of JPS596173B2 publication Critical patent/JPS596173B2/en
Expired 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
    • B01J8/24—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
    • B01J8/20—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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To make it possible to operate continuously by sending a liquid into a spindly or a cylindrical reactor from a lower end portion thereof to a vertical upward direction and from a circumference thereof to a tangential direction to react a liquid and a solid phase at a high yield without using a gas phase. CONSTITUTION:To a reaction apparatus contacting a liquid and a solid phase, a spindly or a cylindrical reactor 4 having a max. diameter portion in a middle portion, an inflow port 6 for flowing into a liquid of a lower end in this reactor 4 to a vertical upward direction, an inflow port 8 for flowing into a tangential direction against the circumference thereof and a liquid outflow port 9 are equipped. Thereby, the complicated flow is generated in a liquid and a solid phase uniformly and the continuous operation can be carried out in a high yield and, moreover, a gas and a volatile substance can be exhausted by suctioning when they are generated.
JP54121611A 1979-09-21 1979-09-21 Two-phase flow reactor Expired JPS596173B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54121611A JPS596173B2 (en) 1979-09-21 1979-09-21 Two-phase flow reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54121611A JPS596173B2 (en) 1979-09-21 1979-09-21 Two-phase flow reactor

Publications (2)

Publication Number Publication Date
JPS5645755A true JPS5645755A (en) 1981-04-25
JPS596173B2 JPS596173B2 (en) 1984-02-09

Family

ID=14815531

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54121611A Expired JPS596173B2 (en) 1979-09-21 1979-09-21 Two-phase flow reactor

Country Status (1)

Country Link
JP (1) JPS596173B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011078184A1 (en) * 2009-12-25 2011-06-30 ダイヤニトリックス株式会社 Method for producing acrylamide using microbial catalyst

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011078184A1 (en) * 2009-12-25 2011-06-30 ダイヤニトリックス株式会社 Method for producing acrylamide using microbial catalyst
JPWO2011078184A1 (en) * 2009-12-25 2013-05-09 ダイヤニトリックス株式会社 Method for producing acrylamide using microbial catalyst
US8980588B2 (en) 2009-12-25 2015-03-17 Mitsubishi Rayon Co., Ltd. Method for producing acrylamide using microbial catalyst
JP5831231B2 (en) * 2009-12-25 2015-12-09 三菱レイヨン株式会社 Method for producing acrylamide using microbial catalyst

Also Published As

Publication number Publication date
JPS596173B2 (en) 1984-02-09

Similar Documents

Publication Publication Date Title
GB1064965A (en) Electrolyte flow interruptor
GB1172680A (en) Apparatus for Contacting Liquids and Gases.
GB1070777A (en) Tray for contacting liquids and gases
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
GB1439946A (en) Spent catalyst regeneration apparatus
GB1500864A (en) Loop reactor
JPS5645755A (en) Two phase fluidized type reaction apparatus
JPS5220388A (en) Furnace system for chemical reaction
JPS53103983A (en) Separating apparatus for liquid
GB1514824A (en) Apparatus suitable for use in a method of spray-drying a liquid
EP0136394A3 (en) Method and apparatus for solution of gas in liquid
MY102345A (en) Process for converting a gaseous feed into an at least partly liquid product.
JPS53120681A (en) Reacting method with suspended catalyst
GB1362218A (en) Centrifugal separators
GB1413442A (en) Sludge heat treatment apparatus
JPS5219892A (en) Control bar drive means
GB910424A (en) Improved gas purifying apparatus
JPS52110278A (en) Gas/liquid contact apparatus of large self-suction capacity
SU566601A1 (en) Device for separation of a two-phase mixture
JPS57111304A (en) Polymerization of propylene
JPS5513105A (en) Waste gas treatment apparatus
JPS51124989A (en) Sampling apparatus for liquid
JPS53144465A (en) Vortex tube
JPS5234556A (en) Device of activated sludge process
JPS5217083A (en) Flow chopper device