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
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/0006—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state
  • C21B13/0013—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state introduction of iron oxide into a bath of molten iron containing a carbon reductant
  • C21B13/002—Reduction of iron ores by passing through a heated column of carbon
• • 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
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/14—Multi-stage processes processes carried out in different vessels or furnaces
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
  • C21B2100/40—Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
  • C21B2100/44—Removing particles, e.g. by scrubbing, dedusting

Definitions

• the invention relates to a device and a method for producing metals and / or metal precursors, in particular pig iron and / or pig iron precursors, a metal-containing feedstock being melted in a melting unit and additionally generating an, in particular at least partially reducing, working gas in the melting unit, and that generated working gas is withdrawn.
• the withdrawn working gas if necessary after cleaning, in particular as a conveying gas, is used at least in part for a, preferably pneumatic, transport of an, in particular fine-particle, at least partially reduced metal-containing material, results in a particularly effective utilization of the working gas generated in the melting unit , This improves the economy of the operation of the melting unit or the entire metallurgical plant.
• a melting unit for generating working gas is known to the person skilled in the art from patent publication WO9704136A1. So far, this working gas has been introduced directly into a treatment reactor, for example a shaft furnace. Separate, elaborately designed pneumatic systems were provided for the conveyance of fine particulate matter.
• the present invention is particularly suitable for the transport of hot (at least above the ambient temperature) at least partially directly reduced material.
• the temperature of such a material is more than 100 ° C. or 200 ° C., preferably more than 300 ° C., particularly preferably more than 400 ° C. or 500 ° C.
• the working gas flows around the material during transport, and the material is in turn separated from the working gas after the transport has taken place.
• the working gas in particular after the separation from the material, is introduced into a treatment unit, preferably for at least partially reducing and / or preheating a solid.
• a treatment reactor is operated for the treatment, in particular for at least partial reduction and / or preheating, of an, in particular fine-particulate and metal-containing, feed material, the treated feed material discharged from the treatment reactor being transported into a by the, preferably pneumatic Melting unit and / or another unit for further processing of the treated input material is promoted.
• the treatment reactor is a reduction reactor, in particular a fluidized bed reactor for reducing fine particulate solids, as is known, for example, from patent publication US5961690A1.
• the feed material is cached after the treatment in the treatment reactor, preferably in an intermediate container, particularly preferably in a fluidized bed lock.
• the feed material is removed and transported by the working gas, preferably from the intermediate container, after the intermediate storage.
• the feed material treated in the treatment reactor is introduced at least partially, optionally via a fluidized bed lock and / or another intermediate vessel, as feed material into the melting unit and melted.
• the invention is further characterized by a device according to claim 8.
• one or more lines are provided for transferring the working gas from the melting unit to the device for transporting the material.
• a treatment reactor is provided for the treatment, in particular for the at least partial reduction and / or preheating, of a particularly fine-particulate and metal-containing feed material, the device being connected to the treatment reactor for transport and being suitable for transporting the treated feed material.
• the device for transporting the treated feed material leads to the melting aggregate and / or to another device for further processing of the feed material.
• an intermediate container in particular a fluidized bed lock, is provided after the treatment reactor, from which, by means of the working gas generated in the melting unit, the feed material discharged from the treatment reactor can be removed.
• a gas-solid separation device in which the working gas can be separated from the material transported, in particular from an intermediate container, transported by the device for transport.
• the working gas conveys the feed to a gas-solid separation device, in particular to a solid cyclone, in which the working gas is subsequently separated from the metal-containing feed.
• the feedstock if appropriate via a fluidized bed lock and / or another intermediate vessel, is introduced into a melting unit or another technical device for further refining or processing.
• the melting unit is set up to melt the treated, in particular pre-reduced and / or preheated, feed material.
• the device for transport is a line leading from the treatment reactor to a melting unit, in particular at least partially bricked up and / or fireproof-lined, for the pneumatic transport of the treated feedstock.
• a feed line for the working gas generated in the melting unit is provided on the device for transport, in particular for transporting the treated feedstock.
• a suitable control device is provided, by means of which the gas flow and / or the flow in the device for transport, in particular the line for pneumatic transport, can be controlled.
• this control device is arranged on the melting unit, wherein a controllable volume of working gas, for example via a torch, is optionally derived and is therefore not available for operating the device for transporting the material.
• the invention presents a novel method for the production of metals and / or metal precursors, in particular pig iron and / or pig iron precursors, from a fine-particulate and metal-containing feedstock, the implemented conveyor system dispensing with moving parts.
• the treated feed material is conveyed uncooled from the treatment reactor by means of the pneumatic conveying via the melting unit, separated there from the conveying gas flow and conveyed for example by means of gravity conveying or by blowing into the melting unit, in particular into a melter gasifier.
• the device for transport (the conveyor system) has no moving parts. This eliminates the high maintenance costs that are known from other pneumatic conveyor systems.
• the invention is shown according to a special and non-limiting embodiment with the aid of a schematic sketch. It shows:
• a melter gasifier (1) generates reducing gas at a temperature between 500 and 900 ° C, in particular a temperature of 800 ° C to 850 ° C, which is dedusted in cyclones (3) and discharged in a brick pipe (7).
• This pipeline (7) is led to the feed point of the DRI (directly reduced iron ore), where DRI is fed into the reducing gas stream with the aid of a fluidized bed lock (10) becomes.
• the DRI comes from a treatment reactor, preferably a reduction furnace, in particular a fluidized bed reduction reactor (12).
• the reducing gas with the DRI is now led in the rising reducing gas line (8) over the melter gasifier and reaches a separating cyclone (6). There the DRI is separated from the reducing gas. Again with the help of a fluidized bed lock (4), the DRI enters the melter gasifier via gravity through several inlet pipes (5). The reducing gas separated from the DRI is now conducted again in a pipeline section (9) under the reactor (12).
• a highly functional pneumatic conveyor system is implemented by the reducing gas lines (8) and (9) and by the fluidized bed lock (10).

Landscapes

• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Dispersion Chemistry (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Furnace Details (AREA)
• Manufacture Of Iron (AREA)
• Crucibles And Fluidized-Bed Furnaces (AREA)
• Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Applications Claiming Priority (3)

Publications (1)

Family

ID=3669980

Family Applications (1)

Country Status (13)

Families Citing this family (3)

Family Cites Families (9)

• 2002
  • 2002-02-14 AT AT0023402A patent/AT411265B/de not_active IP Right Cessation
• 2003
  • 2003-02-10 EP EP03739386A patent/EP1474536A2/de not_active Withdrawn
  • 2003-02-10 RU RU2004127460/02A patent/RU2313580C2/ru not_active IP Right Cessation
  • 2003-02-10 KR KR1020047012611A patent/KR20040077964A/ko not_active Application Discontinuation
  • 2003-02-10 BR BR0307067-0A patent/BR0307067A/pt not_active Application Discontinuation
  • 2003-02-10 US US10/503,117 patent/US7425230B2/en not_active Expired - Fee Related
  • 2003-02-10 WO PCT/EP2003/001280 patent/WO2003068994A1/de active Application Filing
  • 2003-02-10 CA CA002472721A patent/CA2472721A1/en not_active Abandoned
  • 2003-02-10 CN CNB038038986A patent/CN100557035C/zh not_active Expired - Fee Related
  • 2003-02-10 JP JP2003568105A patent/JP4237633B2/ja not_active Expired - Fee Related
  • 2003-02-10 AU AU2003210232A patent/AU2003210232B2/en not_active Ceased
  • 2003-10-02 UA UA20040907523A patent/UA79961C2/uk unknown
• 2004
  • 2004-07-13 ZA ZA200405550A patent/ZA200405550B/en unknown
• 2008
  • 2008-07-31 US US12/184,035 patent/US7638088B2/en not_active Expired - Fee Related
  • 2008-09-25 AU AU2008227074A patent/AU2008227074A1/en not_active Abandoned

Non-Patent Citations (1)

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