EP1656464A1 - Method for the pyrometallurgical production of copper in a converter - Google Patents
Method for the pyrometallurgical production of copper in a converterInfo
- Publication number
- EP1656464A1 EP1656464A1 EP03818380A EP03818380A EP1656464A1 EP 1656464 A1 EP1656464 A1 EP 1656464A1 EP 03818380 A EP03818380 A EP 03818380A EP 03818380 A EP03818380 A EP 03818380A EP 1656464 A1 EP1656464 A1 EP 1656464A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gas
- melt
- converter
- copper
- slag
- 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
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
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/05—Refining by treating with gases, e.g. gas flushing also refining by means of a material generating gas in situ
-
- 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
- C22B15/003—Bath smelting or converting
- C22B15/0041—Bath smelting or converting in converters
-
- 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
- C22B15/006—Pyrometallurgy working up of molten copper, e.g. refining
Definitions
- the invention relates to a method for pyro-metallurgical production of copper in a converter.
- so-called blister copper for example copper stone and / or secondary raw materials are used as raw materials.
- the aim is to produce the so-called blister copper in a purity of at least 96% by weight, preferably over 99% by weight. It goes without saying that efforts are made to achieve purity levels as close as possible to 100% by weight.
- An essential part of this copper production is the so-called "conversion" in a converter. Such converters are known under the names Peirce Smith and Hoboken.
- a copper-containing melt is first filled into the converter (charged in the converter).
- “Slagging” includes the subsequent removal of the slag from the converter.
- the invention aims to optimize the known method.
- the copper production should be possible either in a shorter time and / or with a higher degree of purity.
- the invention is based on the following consideration: During the filling (charging) of the converter, no metallurgical work is carried out in the reactor. The furnace only serves as a “buffer” or “holding unit”. This also applies to the last process step, in which the melt is emptied from the converter.
- these process stages are also used for secondary metallurgical treatment of the melt.
- a treatment gas should be introduced into the molten metal (copper melt) when the converter is being charged.
- This has the advantage that the so-called "slagging" stage is practical starts charging at the same time and not with a delay.
- the converter can be used practically from the first second in the sense of a melt treatment.
- a rinsing treatment during the "detoxification” has the advantage that " the removal of foreign matter and the formation of the slag are accelerated.
- the rinsing treatment can be used for a further effect: by moving the metal bath in a targeted manner, the slag can be directed towards the converter opening, where it is then removed. This achieves a more precise separation between slag on the one hand and melt on the other hand and avoids the loss of melt observed in the prior art.
- the invention in its most general embodiment relates to a method for the pyrometallurgical production of copper in a converter, with the following features:
- the gas used in process stages a), b), c) and e) can, like the gas used in process stage d), consist predominantly or completely of oxygen.
- the proportion of oxygen can be specifically reduced and replaced by a proportion of inert gas.
- the proportion of oxygen can initially be significantly above 50%, while the proportion of inert gas at the end of this process step is over 50%. In this way, the proportion of copper (I) oxide can be minimized.
- the inert gas treatment can be continued in process stage e).
- the metal melt should also coexist during this emptying stage Gas is treated (treated).
- the secondary metallurgical treatment of the copper melt can thus be carried out over the entire conversion process.
- the gas (s) can be supplied via a large number of gas purging elements.
- gas purging elements gas purging stones
- gas purging elements with directional porosity and those with non-directional porosity can be used.
- the first group is characterized in that more or less rectilinear slots or channels are formed in the flushing elements, through which the gas is passed.
- Gas purging elements with undirected porosity are designed like a "sponge". The gas has to move through the body from pore to pore.
- Such gas purging elements can be used individually or in groups in the bottom and / or the wall of the converter.
- the invention provides that they can be activated individually, in preselectable groups or all together.
- Individual gas purging elements or groups of gas purging elements can in turn be charged with different gas or gas pressure.
- a corresponding gas control is preferably provided for this. This can be set to move the molten metal in such a way that the slag floating on it receives a certain direction of flow, for example in the direction of the tap opening.
- the process can be carried out in such a way that gas (s) is introduced (blown, injected) into the melt during all treatment stages and continuously.
- Both the gas and the amount of gas or the gas pressure can be changed during the individual treatment stages.
- gas flushing elements In the case of a converter which can hold 300 tons of copper blister, for example, 10 gas flushing elements can be provided, each with a flushing rate of, for example, 200 liters per minute.
- the method enables a significantly accelerated pyrometallurgical copper production with a degree of purity that corresponds at least to the degree of purity according to the state of the art and can be significantly above 99.5% by weight.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Heat Treatment Of Articles (AREA)
Abstract
Description
Claims
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/EP2003/009367 WO2005021808A1 (en) | 2003-08-23 | 2003-08-23 | Method for the pyrometallurgical production of copper in a converter |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1656464A1 true EP1656464A1 (en) | 2006-05-17 |
EP1656464B1 EP1656464B1 (en) | 2007-01-03 |
Family
ID=34259098
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03818380A Expired - Lifetime EP1656464B1 (en) | 2003-08-23 | 2003-08-23 | Method for the pyrometallurgical production of copper in a converter |
Country Status (9)
Country | Link |
---|---|
US (1) | US20060236812A1 (en) |
EP (1) | EP1656464B1 (en) |
JP (1) | JP4477580B2 (en) |
CN (1) | CN100357463C (en) |
AT (1) | ATE350500T1 (en) |
CA (1) | CA2539011A1 (en) |
DE (1) | DE50306237D1 (en) |
ES (1) | ES2279232T3 (en) |
WO (1) | WO2005021808A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT503456A1 (en) * | 2006-03-27 | 2007-10-15 | Mettop Metallurg Optimierungs | PROCESS FOR PYROMETALLURGIC PRODUCTION OF COPPER |
CL2008000116A1 (en) * | 2008-01-15 | 2008-03-14 | Univ De Chile 51 Empresa Nac D | CONTINUOUS INTENSIVE PIROMETALURGICAL METHOD OF CONVERSION OF LIQUID COPPER MATA THAT INCLUDES FEEDING THIS KILL WITHIN THE FIRST OXIDATION REACTOR, SUPPLY GASES TO THE PACKED MILK AND SILICONE FLOODS, BLEED THE ESCORAL, FOOD METAL |
DE502009000332D1 (en) * | 2009-05-20 | 2011-03-03 | Refractory Intellectual Prop | Metallurgical melting and treatment unit |
CN102605191B (en) * | 2012-04-16 | 2013-12-25 | 阳谷祥光铜业有限公司 | Method for directly producing row copper by copper concentrate |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3941587A (en) * | 1973-05-03 | 1976-03-02 | Q-S Oxygen Processes, Inc. | Metallurgical process using oxygen |
CA1190751A (en) * | 1982-06-18 | 1985-07-23 | J. Barry W. Bailey | Process and apparatus for continuous converting of copper and non-ferrous mattes |
JPS61127835A (en) * | 1984-11-26 | 1986-06-16 | Sumitomo Metal Mining Co Ltd | Blowing method of copper converter |
CA1322659C (en) * | 1987-03-23 | 1993-10-05 | Samuel Walton Marcuson | Pyrometallurgical copper refining |
CA2041297C (en) * | 1991-04-26 | 2001-07-10 | Samuel Walton Marcuson | Converter and method for top blowing nonferrous metal |
US5215571A (en) * | 1992-10-14 | 1993-06-01 | Inco Limited | Conversion of non-ferrous matte |
US5360204A (en) * | 1993-09-20 | 1994-11-01 | Keibler-Thompson Corp. | Boom and lance for removing slag from crucible |
AUPM657794A0 (en) * | 1994-06-30 | 1994-07-21 | Commonwealth Scientific And Industrial Research Organisation | Copper converting |
DE10259434B3 (en) * | 2002-12-19 | 2004-08-26 | Refractory Intellectual Property Gmbh & Co.Kg | Gas purging device for metallurgical melting vessels |
-
2003
- 2003-08-23 AT AT03818380T patent/ATE350500T1/en not_active IP Right Cessation
- 2003-08-23 CA CA002539011A patent/CA2539011A1/en not_active Abandoned
- 2003-08-23 US US10/566,289 patent/US20060236812A1/en not_active Abandoned
- 2003-08-23 DE DE50306237T patent/DE50306237D1/en not_active Expired - Lifetime
- 2003-08-23 CN CNB03826952XA patent/CN100357463C/en not_active Expired - Fee Related
- 2003-08-23 EP EP03818380A patent/EP1656464B1/en not_active Expired - Lifetime
- 2003-08-23 WO PCT/EP2003/009367 patent/WO2005021808A1/en active IP Right Grant
- 2003-08-23 JP JP2005508352A patent/JP4477580B2/en not_active Expired - Fee Related
- 2003-08-23 ES ES03818380T patent/ES2279232T3/en not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
---|
See references of WO2005021808A1 * |
Also Published As
Publication number | Publication date |
---|---|
DE50306237D1 (en) | 2007-02-15 |
JP4477580B2 (en) | 2010-06-09 |
EP1656464B1 (en) | 2007-01-03 |
WO2005021808A1 (en) | 2005-03-10 |
ES2279232T3 (en) | 2007-08-16 |
CN100357463C (en) | 2007-12-26 |
AU2003258656A1 (en) | 2005-03-16 |
US20060236812A1 (en) | 2006-10-26 |
ATE350500T1 (en) | 2007-01-15 |
CN1820087A (en) | 2006-08-16 |
JP2007515549A (en) | 2007-06-14 |
CA2539011A1 (en) | 2005-03-10 |
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