WO1998015665A1 - Verfahren zum abreichern von hochschmelzenden materialien unter verwendung eines schmelzgefässes und eines elektro-reduktionsgefässes - Google Patents
Verfahren zum abreichern von hochschmelzenden materialien unter verwendung eines schmelzgefässes und eines elektro-reduktionsgefässes Download PDFInfo
- Publication number
- WO1998015665A1 WO1998015665A1 PCT/DE1997/002309 DE9702309W WO9815665A1 WO 1998015665 A1 WO1998015665 A1 WO 1998015665A1 DE 9702309 W DE9702309 W DE 9702309W WO 9815665 A1 WO9815665 A1 WO 9815665A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- electrodes
- metal
- slag
- vessel
- melt
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0054—Slag, slime, speiss, or dross treating
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/005—Smelting or converting in a succession of furnaces
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/04—Working-up slag
-
- 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
Definitions
- the invention relates to a method for depleting high-melting materials, in particular slags of minerals containing metal and / or metal oxides.
- the method has set itself the goal of achieving a higher level of separation of the metal to be extracted from the gaits using simple means and using energy sparingly.
- the first high-performance melting unit is followed by a second metallurgical vessel.
- This second metallurgical vessel is an oven vessel which is electrically heated in at least two electrodes.
- In the area of the hearth of this metallurgical vessel there is an intermediate product made of metal and / or metal mat and / or metal stone melt.
- An intermediate product is a slag bath layer.
- Slag from a steel converter can also be added.
- Coke for the reduction of oxidically or sulfidically bound metal and for the creation of a reducing atmosphere above the melt.
- the longest possible amount of slag is collected in the second metallurgical vessel.
- the metallurgical vessel is charged to such an extent that there is approximately 6 times the bath volume of the volume which is charged per hour. Due to the high bath volume, the longest possible residence time, ie settling and leaching time of the melt. The degree of depletion of the melt reaches its maximum. Due to the large volume of slag, the output can be made more resistance-sensitive, ie with lower current and therefore with lower electrical losses.
- the electrical energy is supplied to the electric furnace by means of carbon electrodes which are immersed in the melt. The heating mechanism is the current flow through the resistance of the slag between the electrodes and the
- the new charged material falls into the lower layers of the existing slag on the product bath.
- the material extracts heat from the product bath and absorbs heat from the slag.
- the depleted slag rises to the upper layers of the bath to the extent that the charged material absorbs heat to raise the temperature as well as to react and melt heat, reactions occur and metal fails. It can be seen that a sufficiently depleted final slag is found especially in the uppermost layers of the melt pool.
- the so-called final slag i.e. the slag with the highest degree of depletion, tapped.
- the slag tapping volume is approx. 20% of that in the furnace
- the tapping takes place at a level which ensures that after the tapping, the reclosable tap hole is still 150 to 200 mm below the total bath level.
- the intermediate product precipitated near the bottom is also tapped discontinuously, on a level that is between 40 to 60% of the level of the entire intermediate product.
- the intermediate product is used for further treatment, in particular for cleaning
- a new batch is fed into the metallurgical vessel.
- the slag is again heated from about 1200 to 1250 ° C to a temperature of 1300 to 1400 ° C.
- the distance between the electrodes used and the depth of immersion of the electrodes in the melt is such that 65 to 70% of the energy input takes place between the electrodes and the product bath.
- This electrical heating is carried out for the purpose of maintaining the temperature and increasing the temperature, and for supplying the heat required for the reactions to occur and for the purpose of increasing the viscosity.
- the heating mechanism is the current flow through the electrical resistors that form the slag between and under the electrodes.
- Figure 1 is a flow diagram of the overall process
- Figure 2 schematically shows the heating mechanism.
- FIG. 1 has a high-performance melting vessel 11 which has an oven bottom 14 and an oven wall 15.
- An opening 17 is provided in the furnace bottom 14, through which metal 12 is tapped, which is fed to a converter 51.
- An opening 18 is provided in the furnace wall 15, through which slag 13 is tapped, which is fed to the second metallurgical vessel 21.
- the metal 61 located in the converter 51 is charged into the high-performance melting vessel 11.
- the converter slag 62 is fed to the second metallurgical vessel 21 together with the tapping slag 13, with return material and with reducing agents.
- the return material is channel and pan outbreaks as well as residues from crushing processes and the like, which are fed as solid material to the electrically heated second vessel as solid material.
- the second vessel 21 has a furnace bottom 24, a furnace wall 25 and a lid 29 placed thereon.
- the operating states I, II and III are shown schematically in FIG.
- This metallic melt is always maintained as a sump with the exception of the first start-up phase.
- This metallic melt is an intermediate product consisting of metal, metal mat and metal stone.
- the slag 43, 44 is depleted in such a way that the uppermost slag layer 45 is without valuable material.
- the depleted slag 45 is tapped through a tap opening 23 to such an extent that the residual bath level is still approximately 150 to 200 mm above it.
- the intermediate product 41, 42 is tapped at a height h M , which is approximately half of the total metallic level H n .
- the metallic melt 28 tapped through the tap opening 22 is fed to the converter 51.
- the electrodes 26 projecting into the vessel 21 through the cover 29 are shown schematically in FIG.
- the electrodes are immersed in the melt and the distance between the electrodes and the depth of immersion of the electrodes in the melt are such that 65 to 70% of the energy input takes place between the electrodes and the product bath.
- FIG. 2 shows the electrically heated second vessel 21 with the furnace wall 25, the furnace floor 24 and the lid 29. This is located near the furnace floor 24
- the electrodes 26 are arranged with respect to one another so that on the one hand there is a slag volume V h of the horizontal current flow and energy input and on the other hand there is one slag volume V v of the vertical current flow and energy input per electrode.
- V h slag volume of horizontal current flow and energy input
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Furnace Details (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU52212/98A AU5221298A (en) | 1996-10-10 | 1997-10-02 | Method for downgrading high-melting materials by using a melting tank and an electro-reduction tank |
EP97947002A EP0948656A1 (de) | 1996-10-10 | 1997-10-02 | Verfahren zum abreichern von hochschmelzenden materialien unter verwendung eines schmelzgefässes und eines elektro-reduktionsgefässes |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1996143459 DE19643459A1 (de) | 1996-10-10 | 1996-10-10 | Verfahren zum Abreichern von hochschmelzenden Materialien |
DE19643459.9 | 1996-10-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998015665A1 true WO1998015665A1 (de) | 1998-04-16 |
Family
ID=7809379
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE1997/002309 WO1998015665A1 (de) | 1996-10-10 | 1997-10-02 | Verfahren zum abreichern von hochschmelzenden materialien unter verwendung eines schmelzgefässes und eines elektro-reduktionsgefässes |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0948656A1 (de) |
AU (1) | AU5221298A (de) |
DE (1) | DE19643459A1 (de) |
WO (1) | WO1998015665A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10323507A1 (de) * | 2003-05-24 | 2004-12-09 | Sms Demag Ag | Verfahren zur Rückgewinnung von metallischen Elementen, insbesondere metallischem Chrom, aus metalloxidhaltigen Schlacken im Elektrolichtbogenofen |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1698443A (en) * | 1924-03-31 | 1929-01-08 | Hiram S Lukens | Method of removing copper oxide from copper |
GB800647A (en) * | 1956-01-02 | 1958-08-27 | Pyror Ltd | Methods of treating ores or concentrates containing iron sulphide |
DE2710970A1 (de) * | 1976-03-12 | 1977-09-15 | Boliden Ab | Verfahren zur gewinnung von roh- bzw. blasenkupfer aus sulfidischem kupferrohmaterial |
DE2941225A1 (de) * | 1979-10-11 | 1981-04-23 | Klöckner-Humboldt-Deutz AG, 5000 Köln | Verfahren und vorrichtung zur pyrometallurgischen gewinnung von kupfer |
EP0292992A2 (de) * | 1987-05-29 | 1988-11-30 | Falconbridge Limited | Wiedergewinnung von Nichteisenmetallen |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2251626A1 (en) * | 1973-11-21 | 1975-06-13 | Go Avtomobilny Z | Continuous refining of molten metals by liq. slag - esp. steel mfr. in refining chamber with continuous slag-regeneration |
US4214897A (en) * | 1978-01-13 | 1980-07-29 | Metallurgie Hoboken Overpelt | Process for the extraction of non-ferrous metals from slags and other metallurgical by-products |
FI71770C (fi) * | 1985-05-31 | 1987-02-09 | Outokumpu Oy | Reducering av smaelt metallurgiskt slagg kontinuerligt i en elektrisk ugn. |
DE3540490C1 (de) * | 1985-11-15 | 1987-03-12 | Voith Gmbh J M | Wickelmaschine zum Aufwickeln einer laengsgeteilten Bahn |
DE4116949A1 (de) * | 1991-05-24 | 1993-01-28 | Starck H C Gmbh Co Kg | Verfahren zur rueckgewinnung von wertstoffen aus schlacken von metallothermischen prozessen |
-
1996
- 1996-10-10 DE DE1996143459 patent/DE19643459A1/de not_active Ceased
-
1997
- 1997-10-02 WO PCT/DE1997/002309 patent/WO1998015665A1/de not_active Application Discontinuation
- 1997-10-02 AU AU52212/98A patent/AU5221298A/en not_active Abandoned
- 1997-10-02 EP EP97947002A patent/EP0948656A1/de not_active Ceased
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1698443A (en) * | 1924-03-31 | 1929-01-08 | Hiram S Lukens | Method of removing copper oxide from copper |
GB800647A (en) * | 1956-01-02 | 1958-08-27 | Pyror Ltd | Methods of treating ores or concentrates containing iron sulphide |
DE2710970A1 (de) * | 1976-03-12 | 1977-09-15 | Boliden Ab | Verfahren zur gewinnung von roh- bzw. blasenkupfer aus sulfidischem kupferrohmaterial |
DE2941225A1 (de) * | 1979-10-11 | 1981-04-23 | Klöckner-Humboldt-Deutz AG, 5000 Köln | Verfahren und vorrichtung zur pyrometallurgischen gewinnung von kupfer |
EP0292992A2 (de) * | 1987-05-29 | 1988-11-30 | Falconbridge Limited | Wiedergewinnung von Nichteisenmetallen |
Also Published As
Publication number | Publication date |
---|---|
DE19643459A1 (de) | 1998-04-16 |
EP0948656A1 (de) | 1999-10-13 |
AU5221298A (en) | 1998-05-05 |
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