WO1998015661A1 - Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens - Google Patents
Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens Download PDFInfo
- Publication number
- WO1998015661A1 WO1998015661A1 PCT/AT1997/000214 AT9700214W WO9815661A1 WO 1998015661 A1 WO1998015661 A1 WO 1998015661A1 AT 9700214 W AT9700214 W AT 9700214W WO 9815661 A1 WO9815661 A1 WO 9815661A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- reducing gas
- fine
- gas
- line
- iron
- Prior art date
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
- C21B13/0006—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
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- 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
- 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
- C21B13/0026—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state introduction of iron oxide in the flame of a burner or a hot gas stream
-
- 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
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/10—Reduction of greenhouse gas [GHG] emissions
- Y02P10/134—Reduction of greenhouse gas [GHG] emissions by avoiding CO2, e.g. using hydrogen
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S75/00—Specialized metallurgical processes, compositions for use therein, consolidated metal powder compositions, and loose metal particulate mixtures
- Y10S75/961—Treating flue dust to obtain metal other than by consolidation
Definitions
- the invention relates to a process for the production of molten pig iron or intermediate steel products from finely particulate iron oxide carriers and lumpy iron-containing material, such as partially and / or reduced iron sponge, in a melt-down gasification zone of a melt-down gasifier, in which carbon-containing material and oxygen-containing gas are supplied with simultaneous formation of a Reducing gas in a bed formed from solid carbon carriers, the iron-containing material is melted down, if appropriate after prior reduction, whereby fine-particle iron oxide carriers, such as iron-containing fine ore and ore dust and oxidic iron fine dust, are introduced into a reducing gas stream leaving the melter gasifier, the reducing gas from which the particulate material formed therefrom is freed, the deposited fine particulate material into the melting gasification zone via a dust return line by means of a dust burner is introduced and the reducing gas is used to reduce iron oxide-containing material, as well as a plant for performing the method.
- fine-particle iron oxide carriers such as iron-containing fine ore
- a method of this type is known from EP-A-0 576 414.
- the known method it is possible to use fine ore and / or ore dust in larger quantities in addition to lump ore, such as in an iron and steel mill.
- the oxidic fine particles introduced into the reducing gas flow are conveyed via a dust return line into the melting gasification zone of the melting gasifier.
- the dust return line has a dust lock and a pneumatic conveying system as well as a dust burner, the dust lock overcoming the pressure difference between the melter gasifier and the solids separator, for example a cyclone, which in turn frees the reducing gas from the fine particles.
- the invention aims at avoiding these disadvantages and difficulties and has as its object to further develop the above-described method in such a way that fine ore and / or ore dust, such as oxidative fine iron dust accumulating in a metallurgical plant, is produced in large quantities Amounts can be used, whereby a disturbance of the melting gasification process is avoided. This should also be possible without great expenditure on equipment.
- This object is achieved in that the separated fine-particulate material in the dust return line via a fluidized bed lock, formed by the separated fine-particulate material and reducing gas, is conveyed to the dust burner and thereby reduced.
- a variant in which the reducing gas supplied to the dust return line is used optimally is characterized in that the fluidized bed lock forms a countercurrent fluidized bed zone, formed by the separated fine-particle material through which reducing gas flows in countercurrent to the material, and a direct current fluidized bed zone of the deposited fine particulate material, through which the reducing gas flows in cocurrent to the material, preferably in a substantially larger amount than in the countercurrent fluidized bed zone, in which the fine particulate material is reduced.
- the fine-particle iron ore is advantageously introduced into the reducing gas stream shortly after it has left the melter gasifier, the fine-particle iron ore advantageously being introduced into the reducing gas stream, preferably after it has cooled to 800 to 900 ° C, is blown in.
- a central material jet formed by the fine particulate iron ore and a carrier gas is introduced into the reducing gas and at least one gas jet formed by a secondary gas is directed against the material jet, the gas jet atomizes the material jet and the fine particles are evenly distributed in the reducing gas
- the gas jet preferably sets the material jet at a torque about the axis of the material jet and the fine particles emerge from the material jet by centrifugal forces and the latter is dissolved.
- Good contact of the fine particles with the reducing gas can also be ensured by blowing the fine-particle iron ore in the reducing gas stream in the opposite direction to the flow of the same.
- the dust recirculation device is formed by a countercurrent fluidized bed reactor and a downstream direct current fluidized bed reactor, a line supplying reducing gas opening into both the countercurrent and the direct current fluidized bed reactor.
- the feed line for fine-particle iron ore preferably opens into the beginning of the reducing gas line, ie shortly after its connection to the melter gasifier.
- a preferred embodiment is characterized in that the feed line for fine-particle iron ore is formed by an injection nozzle protruding through the wall of the reducing gas line, which has a central tube which conducts fine particles and a carrier gas and is provided at the mouth of the central tube with at least one nozzle which connects to a Gas line for supplying a secondary gas is connected, the longitudinal axis of the nozzle enclosing an angle with the longitudinal central axis of the central tube, the angle advantageously being in the range between 20 and 60 °.
- the longitudinal axis of the nozzle is preferably skewed with respect to the longitudinal central axis of the central tube, with an angle in the range between the projected longitudinal axis of the nozzle and the longitudinal central axis of the central tube when the longitudinal axis of the nozzle is projected perpendicularly to a plane through the longitudinal central axis of the central tube and the nozzle mouth is formed between 30 and 60 °.
- a further preferred embodiment is characterized in that the conveying line for fine-particle iron ore opens into the reducing gas line with a lance directed opposite the flow in the reducing gas line.
- FIG. 1 schematically illustrating a system for carrying out the method according to the invention according to a first embodiment
- FIG. 2 illustrating a detail of the system according to a modified embodiment
- 3 and 4 show a device for introducing the fine particulate iron oxide carrier, etc. 3 in longitudinal section and FIG. 4 in cross section along the line IV-IV of FIG. 3rd
- a moving bed is understood to mean a continuously moving stream of material, the moving particles of which come into contact with a flowing reducing gas.
- a material flow that moves continuously downward due to the action of gravity is used.
- a reactor with a Venturi fluidized bed, a circulating fluidized bed, a fluidized bed or a reactor with traveling grate or a rotary kiln can also be provided as the reduction reactor.
- the shaft furnace 1 is connected to a melter gasifier 3, in which a reduction gas is generated from coal and oxygen-containing gas, which is fed to the shaft furnace 1 via a reduction gas line 4, a gas cleaning device 5, such as a hot gas cyclone, for drying in the reduction gas line 4 -Dusting is provided.
- a melter gasifier 3 in which a reduction gas is generated from coal and oxygen-containing gas, which is fed to the shaft furnace 1 via a reduction gas line 4, a gas cleaning device 5, such as a hot gas cyclone, for drying in the reduction gas line 4 -Dusting is provided.
- the melter gasifier 3 has a feed line 6 for solid carbon carriers, a feed line 7 for oxygen-containing gases and, if appropriate, feed lines 8 for carbon carriers which are liquid or gaseous at room temperature, such as hydrocarbons, and for burnt additives.
- Molten pig iron 10 or molten steel raw material and molten steel slag 1 which are tapped off via a tap 12, collects in the melter gasifier 3 in a lower section I below the melter gasification zone 9.
- a bed 13 preferably a fixed bed and / or a fluidized bed, is formed from the solid carbon carriers.
- the upper section III provided above the middle section II functions as a calming space for the reducing gas which forms in the melter gasifier 3 and entrained solid particles with the gas stream formed by the reducing gas.
- the iron ore reduced in the direct reduction zone 14 to sponge iron in the shaft furnace 1 in a direct reduction zone 14 is fed together with the aggregates burned in the direct reduction zone 14 via a conveyor line 15 connecting the shaft furnace 1 to the melter gasifier 3, for example by means of discharge screws etc.
- One of the top parts of the shaft furnace 1 closes Export gas discharge line 16 for the export gas resulting from reduction gas in the direct reduction zone 14.
- the export gas drawn off via the export gas discharge line 16 is first subjected to cleaning in a scrubber 17 in order to free it of dust particles as completely as possible to lower the water vapor content, so that it can then be available for further use
- a portion of the reducing gas formed in the melter gasifier 3 is fed back into the feed line 4 via a gas shearer 1 which is re-shaped in the gas purification device 5 and via a line 19 with a gas compressor 20, in order to prevent the reducing gas emerging from the melter gasifier 3 in a very hot state before entering to condition the gas cleaning device 5, in particular to cool it to a temperature range favorable for the direct reduction process in the shaft furnace 1.
- Excess reducing gas can optionally be mixed with the export gas emerging from the shaft furnace 1 for the purpose of keeping the system pressure constant by means of a compensating line 21
- Fine particulate iron oxide carriers such as iron-containing fine ore and ore dust and oxidic iron fine dust, are introduced into the reducing gas stream via a delivery line 22, which merges into the reducing gas line 4.
- the opening 23 of the delivery line 22 into the reducing gas line 4 takes place - seen in the direction of flow of the reducing gas - after the opening 24 of the line 19 feeding a cooled reducing gas, thereby avoiding agglomeration of the fine particles caused by heat
- a first pre-reduction of the oxidic fine particles takes place.
- the fine particles are separated in the gas cleaning device 5 and introduced into the melter gasifier 3 via a dust recirculation device, which is generally designated 25
- the dust recirculation device 25 is formed by a feed line 26, a countercurrent fluidized bed reactor 27, into which the feed line 26 merges, and a direct current fluidized bed reactor 28 arranged downstream of the fine particles, one of which goes from this direct current fluidized bed reactor Conveying line 29 for the fine particles, which leads to a dust burner 30 arranged in the melting gasification zone 9 or above it.
- An oxygen line 31 also flows into this dust burner 30
- Both the countercurrent fluidized bed reactor 27 and the downstream DC fluidized bed reactor 28 are acted upon by reducing gas, which leads to the formation and maintenance of the counter or DC stiomic fluidized beds 32, 33 Reduction gas is fed in via branch lines 34, 35 starting from the reduction gas line 4.
- a gas return line 36 is provided, which starts from the countercurrent fluidized bed reactor 27 and via an injector 37 into the reducing gas line 4 flows into.
- the delivery line 22 for the iron oxide-containing fine particles opens into the reducing gas line 4 preferably via a device for blowing in these fine particles.
- This device has an injection nozzle 38 which projects through the wall 39 of the reducing gas line 4 into the interior 40 thereof.
- the injection nozzle 38 has a central tube 41 to which the delivery line 22 is connected and through which the fine particles are blown to the mouth 42 with the aid of a carrier gas, so that a material jet formed by the fine particles forms at the mouth 42.
- the central tube 41 is provided peripherally surrounding a plurality of nozzles 43, which are connected to a gas line 44 for supplying a secondary gas, etc. each via gas guide tubes 45.
- These gas guide tubes 45 are designed as tubes which are arranged parallel to the longitudinal central axis 46 of the central tube 41 and are provided in an annular space 47 which peripherally surrounds the central tube 41 and into which the gas line 44 opens.
- This annular space 47 is delimited on the outside by a jacket 48, which is closed on the end face at the mouth 42 and on the opposite end face by means of end flanges 49, 50.
- the gas guide tubes 45 can be rotated relative to the end flanges 49, 50 by means of gas-tight bearings 51, 52.
- the opposite ends of the gas guide tubes 45 are closed with flanges 53, 54.
- pivots 55 are arranged, which project outward through the outside end flange 50, which delimits the annular space 47 on the outside.
- Drives (not shown in more detail) for rotating the gas guide tubes 45 about their longitudinal axes 56 are provided on the pivot pins 55.
- the nozzles 43 are arranged on the inside flanges 53 of the gas guide tubes 45, which enclose an angle ⁇ with the longitudinal central axis 46 of the central tube. The gas supply to the gas guide tubes 45 and finally the nozzles 43 takes place via the annular space 47 and openings 57 of the gas guide tubes 45.
- the gas jets flowing out of the nozzles 43 can be varied in their position relative to the material jet, etc. to the effect that the gas jets can be brought from a position intersecting the longitudinal central axis 46 of the central tube 41 into a position oblique to this longitudinal central axis 46.
- the position of the gas jets relative to the material jet can be changed periodically.
- the angle ⁇ , which the gas jets enclose with the longitudinal central axis 46 of the central tube 41, is preferably in a range between 20 and 60 °, the angle ⁇ not having to be the same for all gas jets.
- a plurality of nozzles 43 are arranged uniformly distributed around the entire circumference of the mouth 42 of the central tube 41. Under certain circumstances, however, it may be sufficient if a plurality of nozzles 43 are provided on only one circumferential half of the mouth 42 of the central tube 41.
- the gas jets are preferably formed by an inert gas. Inert gas can also serve as the carrier gas. Instead of the nozzles 43, an annular gap could also be provided in the end flange 49, through which a fan-shaped gas jet is directed against the material jet. If the position of their gas jets to the material jet does not have to be changed, the gas guide tubes 45 can be dispensed with; the nozzles 43 can then be inserted rigidly in the end flange 49.
- the iron ore blown into the reducing gas and finely distributed in the reducing gas with the aid of the secondary gas immediately after entering the reducing gas line 4 is reduced, at least partially reduced, within this line 4.
- fine-grained metallurgical waste materials or circuit materials in oxidized and / or metallic form and possibly additionally carbon-containing substances can also be introduced via the device according to the invention.
- the oxide-containing fine particles are introduced by means of a lance 58 opening into the interior of the reducing gas line 4, in which the ore formed by fine particles is conveyed by means of a carrier gas.
- the ore emerges in the opposite direction to the reducing gas stream and is immediately finely distributed in it by vortex formation, see above that in this embodiment too, a pre-reduction which occurs immediately after entry is ensured within the reducing gas line 4.
- the fine ore has the following analysis (in% by weight).
- the grain size distribution is as follows:
- the returned amount of cooling gas is 3,360 Nm '/ h, which results in a Total reduction gas volume that enters the gas cleaning device 5 is 41,680 NmVh.
- the analysis of the reducing gas upstream of the confluence of the delivery line 22 and the reducing gas line 4 is shown in Table III below (in% by volume).
- the temperature of the reducing gas is 22 900 ° C. at the mouth 23 of the delivery line 22.
- the reducing gas emerging from the melter gasifier 3 is loaded with dust.
- the dust content is 130 g / Nm ⁇ the dust has the following analysis (% by weight).
- the reducing gas has a temperature of 750 ° C to 800 ° C.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU44444/97A AU4444497A (en) | 1996-10-08 | 1997-10-06 | Method for producing liquid pig iron or steel fabricated materials and installation for implementing said method |
EP97942698A EP0948654B1 (de) | 1996-10-08 | 1997-10-06 | Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens |
US09/284,104 US6264725B1 (en) | 1996-10-08 | 1997-10-06 | Method for producing liquid pig iron or steel fabricated materials and installation for implementing said method |
DE59704212T DE59704212D1 (de) | 1996-10-08 | 1997-10-06 | Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens |
JP51701298A JP4317266B2 (ja) | 1996-10-08 | 1997-10-06 | 液状銑鉄の製造方法およびその方法を実施するためのプラント |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT0177996A AT404138B (de) | 1996-10-08 | 1996-10-08 | Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens |
ATA1779/96 | 1996-10-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998015661A1 true WO1998015661A1 (de) | 1998-04-16 |
Family
ID=3520802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AT1997/000214 WO1998015661A1 (de) | 1996-10-08 | 1997-10-06 | Verfahren zur herstellung von flüssigem roheisen oder stahlvorprodukten sowie anlage zur durchführung des verfahrens |
Country Status (10)
Country | Link |
---|---|
US (1) | US6264725B1 (de) |
EP (1) | EP0948654B1 (de) |
JP (1) | JP4317266B2 (de) |
KR (1) | KR100441793B1 (de) |
AT (1) | AT404138B (de) |
AU (1) | AU4444497A (de) |
DE (1) | DE59704212D1 (de) |
TW (1) | TW364925B (de) |
WO (1) | WO1998015661A1 (de) |
ZA (1) | ZA979015B (de) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000073515A1 (fr) * | 1999-05-26 | 2000-12-07 | Paul Wurth S.A. | Procede de production de metal liquide a partir de particules prereduites et dispositif de fusion couple a un four de traitement thermique par un dispositif de transfert de particules |
WO2011141209A1 (de) * | 2010-05-11 | 2011-11-17 | Siemens Vai Metals Technologies Gmbh | Verfahren und vorrichtung zur herstellung von zumindest teilweise reduzierten metallerzen und/oder metallen |
AT512017A1 (de) * | 2011-09-30 | 2013-04-15 | Siemens Vai Metals Tech Gmbh | Verfahren und vorrichtung zur roheisenerzeugung |
EP2664681A1 (de) | 2012-05-16 | 2013-11-20 | Siemens VAI Metals Technologies GmbH | Verfahren und Vorrichtung zum Einbringen von feinteilchenförmigem Material in die Wirbelschicht eines Reduktionsaggregates |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT404022B (de) * | 1996-11-08 | 1998-07-27 | Voest Alpine Ind Anlagen | Verfahren und anlage zur herstellung von flüssigem roheisen oder stahlvorprodukten aus eisenhältigemmaterial |
AU2002952062A0 (en) * | 2002-10-15 | 2002-10-31 | D.Wilson Investments Pty. Ltd. | Process and apparatus for extracting zinc |
US20050151307A1 (en) * | 2003-09-30 | 2005-07-14 | Ricardo Viramontes-Brown | Method and apparatus for producing molten iron |
JP5598423B2 (ja) * | 2011-06-01 | 2014-10-01 | 新日鐵住金株式会社 | 予備還元塊成化物の製造方法 |
Citations (5)
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---|---|---|---|---|
GB827957A (en) * | 1955-03-15 | 1960-02-10 | British Iron Steel Research | Improvements in the production of metal from ores and in apparatus therefor |
DE1086256B (de) * | 1952-07-23 | 1960-08-04 | Werner Wenzel Dr Ing | Verfahren und Einrichtung zur Eisengewinnung aus staubfoermigen bzw. feinkoernigen Eisenerzen mittels Brennstoffen in feinem Verteilungsgrad oberhalb des Schmelzpunktes der nicht gasfoermigen Reaktionsprodukte |
US4490170A (en) * | 1981-11-27 | 1984-12-25 | Outokumpu Oy | Method for forming a directional and controlled suspension spray of a pulverous material and a reaction gas |
WO1990007010A1 (en) * | 1988-12-20 | 1990-06-28 | Commonwealth Scientific And Industrial Research Organisation | Manufacture of iron and steel in a duplex smelter and solid state oxide suspension prereducer |
WO1990015162A1 (en) * | 1989-06-02 | 1990-12-13 | Cra Services Limited | Pre-heating and pre-reduction of metal oxide ore using high temperature off-gases |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT401777B (de) * | 1992-05-21 | 1996-11-25 | Voest Alpine Ind Anlagen | Verfahren und anlage zur herstellung von flüssigen roheisen oder flüssigen stahlvorprodukten |
KR100241009B1 (ko) * | 1995-12-29 | 2000-03-02 | 이구택 | 용융환원공정에서의 미분광취입방법 |
-
1996
- 1996-10-08 AT AT0177996A patent/AT404138B/de not_active IP Right Cessation
-
1997
- 1997-10-06 AU AU44444/97A patent/AU4444497A/en not_active Abandoned
- 1997-10-06 JP JP51701298A patent/JP4317266B2/ja not_active Expired - Fee Related
- 1997-10-06 US US09/284,104 patent/US6264725B1/en not_active Expired - Fee Related
- 1997-10-06 KR KR10-1999-7003029A patent/KR100441793B1/ko not_active IP Right Cessation
- 1997-10-06 WO PCT/AT1997/000214 patent/WO1998015661A1/de active IP Right Grant
- 1997-10-06 DE DE59704212T patent/DE59704212D1/de not_active Expired - Lifetime
- 1997-10-06 EP EP97942698A patent/EP0948654B1/de not_active Expired - Lifetime
- 1997-10-08 ZA ZA9709015A patent/ZA979015B/xx unknown
- 1997-12-16 TW TW086118745A patent/TW364925B/zh not_active IP Right Cessation
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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DE1086256B (de) * | 1952-07-23 | 1960-08-04 | Werner Wenzel Dr Ing | Verfahren und Einrichtung zur Eisengewinnung aus staubfoermigen bzw. feinkoernigen Eisenerzen mittels Brennstoffen in feinem Verteilungsgrad oberhalb des Schmelzpunktes der nicht gasfoermigen Reaktionsprodukte |
GB827957A (en) * | 1955-03-15 | 1960-02-10 | British Iron Steel Research | Improvements in the production of metal from ores and in apparatus therefor |
US4490170A (en) * | 1981-11-27 | 1984-12-25 | Outokumpu Oy | Method for forming a directional and controlled suspension spray of a pulverous material and a reaction gas |
WO1990007010A1 (en) * | 1988-12-20 | 1990-06-28 | Commonwealth Scientific And Industrial Research Organisation | Manufacture of iron and steel in a duplex smelter and solid state oxide suspension prereducer |
WO1990015162A1 (en) * | 1989-06-02 | 1990-12-13 | Cra Services Limited | Pre-heating and pre-reduction of metal oxide ore using high temperature off-gases |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000073515A1 (fr) * | 1999-05-26 | 2000-12-07 | Paul Wurth S.A. | Procede de production de metal liquide a partir de particules prereduites et dispositif de fusion couple a un four de traitement thermique par un dispositif de transfert de particules |
LU90399B1 (fr) * | 1999-05-26 | 2000-12-27 | Wurth Paul Sa | Proc-d- de couplage r-duction-fusion et dispositif de transfert de particules - chaud |
WO2011141209A1 (de) * | 2010-05-11 | 2011-11-17 | Siemens Vai Metals Technologies Gmbh | Verfahren und vorrichtung zur herstellung von zumindest teilweise reduzierten metallerzen und/oder metallen |
AT512017A1 (de) * | 2011-09-30 | 2013-04-15 | Siemens Vai Metals Tech Gmbh | Verfahren und vorrichtung zur roheisenerzeugung |
AT512017B1 (de) * | 2011-09-30 | 2014-02-15 | Siemens Vai Metals Tech Gmbh | Verfahren und vorrichtung zur roheisenerzeugung |
US9428818B2 (en) | 2011-09-30 | 2016-08-30 | Primetals Technologies Austria GmbH | Method and device for producing pig iron |
EP2664681A1 (de) | 2012-05-16 | 2013-11-20 | Siemens VAI Metals Technologies GmbH | Verfahren und Vorrichtung zum Einbringen von feinteilchenförmigem Material in die Wirbelschicht eines Reduktionsaggregates |
WO2013171001A1 (de) | 2012-05-16 | 2013-11-21 | Siemens Vai Metals Technologies Gmbh | Verfahren und vorrichtung zum einbringen von feinteilchenförmigem material in die wirbelschicht eines wirbelschichtreduktionsaggregates |
US9512496B2 (en) | 2012-05-16 | 2016-12-06 | Primetals Technologies Austria GmbH | Method and device for introducing fine particle-shaped material into the fluidised bed of a fluidised bed reduction unit |
Also Published As
Publication number | Publication date |
---|---|
KR100441793B1 (ko) | 2004-07-27 |
ATA177996A (de) | 1998-01-15 |
EP0948654A1 (de) | 1999-10-13 |
AT404138B (de) | 1998-08-25 |
KR20000048978A (ko) | 2000-07-25 |
AU4444497A (en) | 1998-05-05 |
ZA979015B (en) | 1998-05-11 |
JP2001501675A (ja) | 2001-02-06 |
US6264725B1 (en) | 2001-07-24 |
EP0948654B1 (de) | 2001-08-01 |
DE59704212D1 (de) | 2001-09-06 |
TW364925B (en) | 1999-07-21 |
JP4317266B2 (ja) | 2009-08-19 |
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