JPS57210906A - Reducing method for iron oxide - Google Patents
Reducing method for iron oxideInfo
- Publication number
- JPS57210906A JPS57210906A JP9540081A JP9540081A JPS57210906A JP S57210906 A JPS57210906 A JP S57210906A JP 9540081 A JP9540081 A JP 9540081A JP 9540081 A JP9540081 A JP 9540081A JP S57210906 A JPS57210906 A JP S57210906A
- Authority
- JP
- Japan
- Prior art keywords
- coke
- zone
- pipe
- catalysts
- iron oxide
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0033—In fluidised bed furnaces or apparatus containing a dispersion of the material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
PURPOSE:To remove coke thoroughly and to improve the reducibility of iron by providing fluidized bed zones wherein the combustion of coke, the generation of CO and the reduction of iron oxide are effected respectively independently to a regeneration tower for iron oxide type catalysts for catalytic cracking of asphalt. CONSTITUTION:Part of iron oxide type catalysts stuck with coke are supplied through a pipe 8 into the 1st fluidized bed zone B in the 1st reaction tower 7, and are fluidized by the air supplied through a pipe 9, whereby the coke is burned. The generated CO2 rich gas is delivered in the bottom part of the 2nd fluidized bed zone C. The remaining catalysts stuck with coke are fluidized by the CO2 rich gas from the zone B; at the same time, they cause producer gas reaction, thereby producing gaseous CO. This gas is fed into the bottom part of the 3rd fluidized bed zone D in the 2nd reaction tower 11 through a pipe 10. On the other hand, the catalysts stuck with unreacted coke in the zone C are returned through a downcomer 12 into the zone B, where the coke is burned almost perfectly. Further, the catalysts removed of the coke almost completely in the zones B, C are supplied through a pipe 13 into the zone D, where they are fluidized by the CO through the pipe 10 and are reduced. These catalysts are removed through a pipe 14.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9540081A JPS57210906A (en) | 1981-06-22 | 1981-06-22 | Reducing method for iron oxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9540081A JPS57210906A (en) | 1981-06-22 | 1981-06-22 | Reducing method for iron oxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS57210906A true JPS57210906A (en) | 1982-12-24 |
Family
ID=14136605
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9540081A Pending JPS57210906A (en) | 1981-06-22 | 1981-06-22 | Reducing method for iron oxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57210906A (en) |
-
1981
- 1981-06-22 JP JP9540081A patent/JPS57210906A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS55104920A (en) | Manufacture of lightened oil and hydrogen from heavy oil | |
KR100191974B1 (en) | Catalyst regeneration process | |
ZA888821B (en) | Olefins production process | |
IN162321B (en) | ||
GB1536158A (en) | Method of regenerating a cracking catalyst with substantially complete combustion of carbon monoxide | |
KR930023474A (en) | Method and apparatus for direct reduction of particulate iron-oxide containing material | |
JPS5827837B2 (en) | Processing method for sulfur-containing heavy oil | |
EP0154492A3 (en) | Multiple-stage reactor system for a moving catalyst bed | |
GB2082624A (en) | Method of gas production | |
US4325812A (en) | Process for cracking heavy hydrocarbons into light oils and producing hydrogen | |
ES8106558A1 (en) | Method of making sponge iron | |
ES465092A1 (en) | Method for processing coke oven gas | |
US3787192A (en) | Process for coal gasification | |
JPS57210906A (en) | Reducing method for iron oxide | |
US3303017A (en) | Metal treating process | |
JPS6470608A (en) | Fluid burning method | |
US4080196A (en) | Method of operating a vertical shaft furnace | |
JPS5641306A (en) | Iron making method by direct reduction of iron oxide | |
GB1535797A (en) | Fluidized cracking catalyst regeneration process and apparatus | |
JPH0360416A (en) | Method for partially oxidizing carbonaceous fuel | |
JPS60133088A (en) | Catalytic cracking of heavy oil and production of hydrogen | |
JPS57188607A (en) | Fluidized-bed reducing method for iron ore for manufacturing reduced iron and fuel gas simultaneously | |
JPS56119716A (en) | Treatment for exhaust gas of fluidized bed reaction furnace | |
JPS5595604A (en) | Reducing method for sulfur dioxide with coal | |
JPS535209A (en) | Method and apparatus for gasification of heavy hydrocarbons |