JPS5775135A - Ultrahigh pressure device - Google Patents

Ultrahigh pressure device

Info

Publication number
JPS5775135A
JPS5775135A JP55151396A JP15139680A JPS5775135A JP S5775135 A JPS5775135 A JP S5775135A JP 55151396 A JP55151396 A JP 55151396A JP 15139680 A JP15139680 A JP 15139680A JP S5775135 A JPS5775135 A JP S5775135A
Authority
JP
Japan
Prior art keywords
thermal decomposition
furnace
fed
raw materials
produced
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
JP55151396A
Other languages
Japanese (ja)
Other versions
JPS597499B2 (en
Inventor
Yoshiaki Ishii
Naoyoshi Ando
Tsutomu Kume
Shosaku Fujinami
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP55151396A priority Critical patent/JPS597499B2/en
Publication of JPS5775135A publication Critical patent/JPS5775135A/en
Publication of JPS597499B2 publication Critical patent/JPS597499B2/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
    • B01J8/26—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 two or more fluidised beds, e.g. reactor and regeneration installations
    • 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
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PURPOSE:To improve the yeild of recovered gases and widen the range of incineration or thermal decomposition objects by supplying combustibles other than char to a combustion furnace in thermal decomposition of org. raw materials. CONSTITUTION:Raw materials to be thermally decomposed such as biomass, municipal refuse and the like fed through a dryer 33 to a thermal decomposition furnace 1, where they are thermally decompose by the endothermic reaction of thermal decomposition. Part of the produced gas is recirculated to the furnace 1 and is supplied as a fluidizing gas. The heat medium lowered of temp. by the endothermic reaction of thermal decomposition is fed by carrying the char content produced at the same time to a lifting mechanism 26. Here, the char content burns by reacting with the air lifting the heat medium and further it is perfectly burned by the fluidized bed of a combustion furnace 2, by which its temp. is raised. The oil and tar separated with a water treatment device 30 for condensate are also fed to the fluidized bed of the furnace 2 and are burned as well. By this mechanism, various org. raw materials are used as burning materials and the yield of the gases produced by thermal decomposition is improved.
JP55151396A 1980-10-30 1980-10-30 Thermal reaction method Expired JPS597499B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55151396A JPS597499B2 (en) 1980-10-30 1980-10-30 Thermal reaction method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55151396A JPS597499B2 (en) 1980-10-30 1980-10-30 Thermal reaction method

Publications (2)

Publication Number Publication Date
JPS5775135A true JPS5775135A (en) 1982-05-11
JPS597499B2 JPS597499B2 (en) 1984-02-18

Family

ID=15517663

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55151396A Expired JPS597499B2 (en) 1980-10-30 1980-10-30 Thermal reaction method

Country Status (1)

Country Link
JP (1) JPS597499B2 (en)

Also Published As

Publication number Publication date
JPS597499B2 (en) 1984-02-18

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