WO2015010500A1 - 铜冶炼炉渣贫化方法及装置 - Google Patents

铜冶炼炉渣贫化方法及装置 Download PDF

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Publication number
WO2015010500A1
WO2015010500A1 PCT/CN2014/077950 CN2014077950W WO2015010500A1 WO 2015010500 A1 WO2015010500 A1 WO 2015010500A1 CN 2014077950 W CN2014077950 W CN 2014077950W WO 2015010500 A1 WO2015010500 A1 WO 2015010500A1
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Prior art keywords
slag
copper
furnace body
copper smelting
depleting
Prior art date
Application number
PCT/CN2014/077950
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English (en)
French (fr)
Inventor
周松林
刘卫东
王虎
Original Assignee
阳谷祥光铜业有限公司
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Filing date
Publication date
Application filed by 阳谷祥光铜业有限公司 filed Critical 阳谷祥光铜业有限公司
Priority to RU2015121634A priority Critical patent/RU2633428C2/ru
Priority to US14/649,800 priority patent/US9903005B2/en
Priority to AU2014295665A priority patent/AU2014295665B2/en
Priority to JP2015545661A priority patent/JP6030246B2/ja
Priority to EP14830180.7A priority patent/EP3026131B1/en
Priority to ES14830180T priority patent/ES2735333T3/es
Publication of WO2015010500A1 publication Critical patent/WO2015010500A1/zh
Priority to CL2015001670A priority patent/CL2015001670A1/es

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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
    • C22B15/0002—Preliminary treatment
    • 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
    • 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
    • C22B15/0047—Smelting or converting flash smelting or converting
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B14/00—Crucible or pot furnaces
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B3/00—Hearth-type furnaces, e.g. of reverberatory type; Tank furnaces
    • F27B3/02—Hearth-type furnaces, e.g. of reverberatory type; Tank furnaces of single-chamber fixed-hearth type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B3/00—Hearth-type furnaces, e.g. of reverberatory type; Tank furnaces
    • F27B3/10—Details, accessories, or equipment peculiar to hearth-type furnaces
    • F27B3/20—Arrangements of heating devices
    • F27B3/205—Burners
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00—Charging; Discharging; Manipulation of charge
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00—Charging; Discharging; Manipulation of charge
    • F27D3/0033—Charging; Discharging; Manipulation of charge charging of particulate material
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D7/00—Forming, maintaining, or circulating atmospheres in heating chambers
    • F27D7/02—Supplying steam, vapour, gases, or liquids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00—Subject matter not provided for in other groups of this subclass
    • F27D99/0001—Heating elements or systems
    • F27D99/0033—Heating elements or systems using burners
    • 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
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B14/00—Crucible or pot furnaces
    • F27B2014/002—Smelting process, e.g. sequences to melt a specific material
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B14/00—Crucible or pot furnaces
    • F27B2014/002—Smelting process, e.g. sequences to melt a specific material
    • F27B2014/004—Process involving a smelting step, e.g. vaporisation
    • 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

  • Copper smelting furnace slag depletion method and device The application is submitted to the Chinese Patent Office on July 23, 2013, and the application number is 201310311055.X, and the invention name is "the method of depleting the copper smelting melting furnace slag and the slag slag used in the copper smelting melting furnace The priority of the Chinese Patent Application, the entire disclosure of which is incorporated herein by reference.
  • the invention relates to the field of non-ferrous metallurgy technology, in particular to a method for depleting copper smelting melting furnace slag and a depleting device for depleting copper smelting melting furnace slag. Background technique
  • one method is to indirectly form blister copper from the sulphide copper concentrate. This method generally involves two steps: first, desulfurization and iron removal of the sulphide copper concentrate, and smelting to obtain high-grade copper bismuth. Then, the obtained copper ruthenium is further desulfurized and iron-removed, and is blown to obtain crude copper. Another method is to directly produce blister copper from copper concentrate. In actual production, Australia's Olympic Dam smelter, Poland's Glogow smelter and Zambia's KCM smelter use copper concentrate to directly produce blister copper. Craft.
  • copper smelting methods have a common feature, that is, the amount of Cu 2 0 and Fe 3 0 4 is high in the produced slag.
  • the copper content is 10% to 20% (by weight), Fe.
  • the content of 3 0 4 is 30% to 50% (weight ratio).
  • the above processes are treated by depletion of the electric furnace to treat the slag to reduce the copper content in the slag.
  • a reducing agent is generally added, and the slag is treated by a reduction reaction, and the electric furnace can maintain the temperature to ensure the thermodynamic basis of the reduction reaction.
  • the depletion of electric furnace only provides a thermodynamic basis for the reduction reaction, and the reaction efficiency is low, which not only causes the Cu 2 0 and Fe 3 0 4 in the slag to be reduced for a long time, that is, the depletion time is long, the energy consumption is high, and
  • the treated slag has a copper content of 1% to 4% (by weight), that is, the copper content of the slag is still high, and it needs to be subjected to beneficiation and other treatments before being applied, which brings high investment and production costs. The problem is not conducive to production. Summary of the invention
  • the present invention provides a method for depleting a copper smelting melting furnace slag and a depleting device for depleting a copper smelting melting furnace slag, wherein the depleted slag has high reaction efficiency and can make copper in the final slag The content is reduced and can be applied without further processing such as beneficiation.
  • the invention provides a method for depleting a copper smelting melting furnace slag, comprising the following steps: in a depleting device, mixing copper smelting molten slag with a reducing agent and a pressurized inert gas, and then performing depletion to obtain a depleted slag
  • the pressure of the inert gas is from 100 kPa to 800 kPa.
  • the depleting device comprises:
  • the furnace body comprises a molten pool, and the furnace body is provided with a gas nozzle, a feeding port and a slag discharge port;
  • the gas nozzle is located on a side wall of the furnace body and leads to a middle portion of the molten pool.
  • the copper smelting molten slag and the reducing agent are respectively introduced into the depleting device through the feeding port through the launder;
  • the inert gas is introduced into the depleting device through the gas nozzle.
  • the top of the furnace body is provided with a fuel burner
  • a fuel and a combustion improver are introduced into the fuel burner.
  • the combustion improver is industrial oxygen having an oxygen concentration of more than 95% by weight.
  • the inert gas is nitrogen.
  • the temperature of the copper smelting molten slag is 1050 ° C to 1350 ° C.
  • the reducing agent is a copper concentrate containing FeS and Cu 2 S.
  • the ratio of the sulfur content in the reducing agent to the oxygen content in the copper smelting melting furnace slag is (0.6-1.5): 1 (mass ratio).
  • the invention provides a depleting device for the depletion of copper smelting molten slag, comprising:
  • the furnace body comprises a molten pool, and the furnace body is provided with a gas nozzle, a feeding port and a slag discharge port;
  • the gas nozzle is located on a side wall of the furnace body and leads to a middle portion of the molten pool.
  • the present invention introduces a copper smelting molten slag and a reducing agent into a depleting device, and introduces a pressurized inert gas into the depleting device, and the pressure of the inert gas is 100 kPa to 800 kPa. After mixing, it is depleted to obtain a depleted slag.
  • the invention utilizes the sensible heat of the copper smelting molten slag to melt the reducing agent, and reduces the Cu 2 0 and Fe 3 0 4 in the slag by the reducing agent; the introduced inert gas forms a strong agitation to the reaction material, and the molten slag is boiled.
  • the invention promotes the rapid renewal of the reaction substance by the strong stirring of the inert gas, and strengthens the reaction process.
  • the slag property is rapidly changed, and the collision bonding probability between the droplets is increased, and therefore, the strengthening process of the present invention can lower the copper content in the final slag.
  • Fig. 1 is a schematic view showing the structure of a depletion device for copper smelting and melting furnace slag depletion according to an embodiment of the present invention. detailed description
  • the invention provides a method for depleting a copper smelting melting furnace slag, comprising the following steps: in a depleting device, mixing copper smelting molten slag with a reducing agent and a pressurized inert gas, and then performing depletion to obtain a depleted Slag; the pressure of the inert gas is from 100 kPa to 800 kPa.
  • the method for depleting the copper smelting and melting furnace slag provided by the present invention is an improved method for slag depletion, which can reduce the copper content in the treated slag and make the final
  • the slag does not need to be processed by beneficiation, etc., and can be used as raw materials for other industries after granulation, with low investment and production costs.
  • the present invention can produce copper bismuth, i.e., water copper, while depleting the copper smelting molten slag, which can be returned as a cold raw material to the upper copper smelting process.
  • the copper smelting molten slag and the reducing agent are introduced into the depleting device, and the pressurized inert gas is introduced into the depleting device, and the pressure of the inert gas is 100 kPa to 800 kPa, and the mixture is depleted after mixing. , get the slag after depletion.
  • the copper smelting melting furnace slag is a slag rich in Cu 2 0 and Fe 3 0 4 which is generated in a copper smelting process which is well known to those skilled in the art.
  • the present invention has no particular limitation on the composition of the copper smelting melting furnace slag, wherein copper is in an oxidized state, and the content is generally 10% to 20% (weight) Ratio); Fe 3 0 4 is generally in a content of 30% to 50% by weight.
  • the copper smelting molten slag has sensible heat, and the temperature thereof is preferably 1050 ° C to 1350 ° C.
  • the invention utilizes the sensible heat of the copper smelting molten slag to melt the reducing agent, does not need to add extra heat to help the reducing agent to melt, has better energy saving effect and saves economic cost.
  • the reducing agent is mixed with the copper smelting molten slag to reduce Cu 2 0 and Fe 3 0 4 in the slag, and the copper in the slag is enriched and settled at the bottom of the depleting device, so that the upper slag is depleted.
  • the reducing agent is not particularly limited in the present invention, and is preferably a copper concentrate containing FeS and Cu 2 S, which has a low production cost and is environmentally friendly.
  • the copper concentrate containing FeS and Cu 2 S is a copper concentrate containing telluride which is used in the ordinary copper smelting process in the art, and is mainly composed of chalcopyrite, and the present invention has no particular limitation on its source.
  • FeS in the copper concentrate converts the copper oxide Cu 2 0 carried in the original slag into sulfide Cu 2 S, newly formed Cu 2 S and copper concentrate
  • the Cu 2 S and FeS carried in the combination can form a copper crucible; the FeS in the copper concentrate simultaneously reduces the high-valent oxide Fe 3 0 4 of the iron in the slag to a low-valent oxide FeO to change the slag type, that is, the slag
  • the iron compound carried in the transformation is converted from high melting point Fe 3 0 4 to low melting point FeO, FeO further slag with SiO 2 carried in the slag to form lower melting point 2FeO ⁇ Si0 2 , so that the final slag
  • the nature of the transformation the viscosity is reduced, which is conducive to the settlement and separation of the copper slag, so that the copper content of the upper slag is reduced.
  • the molten slag is mixed with copper concentrate in proportion, and the ratio (S/0) of the sulfur content in the copper concentrate to the oxygen content in the copper smelting melting furnace slag is preferably (0.6-1.5): 1 (quality More preferably, it is (0.6-1.2): 1 (mass ratio).
  • the present invention provides the power to boil molten slag and produce a strong agitation by introducing a pressurized inert gas into the above reaction material.
  • the introduced inert gas forms a strong agitation of the reaction material to boil the molten slag
  • the copper concentrate containing FeS and Cu 2 S is taken into the molten slag to force Cu 2 0, Fe 3 0 4 and FeS collision polymerization for interaction, which promotes the formation of Cu 2 S and FeS droplets to form copper ruthenium, and the resulting FeO and SiO 2 slag form a separate slag phase and copper 4 ⁇ phase.
  • the invention promotes the rapid renewal of the reaction substance by the strong agitation of the inert gas, strengthens the reaction process, rapidly changes the slag property, and improves the collision bonding probability between the droplets. Therefore, the strengthening process of the present invention can make the final slag
  • the copper content in the reduction is reduced.
  • stirring with an inert gas prevents the reducing agent and the reduced Cu 2 S and FeO from being oxidized, and the amount of the reducing agent used is not increased, the efficiency is high, and the cost is low.
  • the pressure of the inert gas is from 100 kPa to 800 kPa, preferably 200 kPa to 600 kPa, more preferably 300 kPa to 500 kPa.
  • the inert gas is preferably nitrogen gas, which increases the contact between the reaction materials and improves the reaction efficiency. At the same time, nitrogen as an inert gas does not oxidize the reduced Cu 2 S and FeO again, which is beneficial to the slag depletion.
  • the copper smelting molten slag is introduced into a depleted unit, the reducing agent is added in proportion, and a pressurized inert gas is introduced into the depleting unit.
  • the depletion device preferably employs the following depletion device.
  • the present invention provides a depletion device for copper smelting and melting furnace slag depletion, comprising: a furnace body, the furnace body comprising a molten pool, wherein the furnace body is provided with a gas nozzle, a feeding port and a slag discharge port;
  • the gas nozzle is disposed on a side wall of the furnace body and leads to a middle portion of the molten pool.
  • the depletion device provided by the invention is used for depletion of copper smelting and melting furnace slag, which is beneficial for reducing the copper content in the treated slag.
  • the depletion device for the copper smelting and melting furnace slag depletion provided by the embodiment of the present invention is a side-blown metallurgical furnace, the structure of which is shown in FIG. 1 , and FIG. 1 is a depletion of the copper smelting and melting furnace slag depletion provided by the embodiment of the present invention. Schematic diagram of the structure of the device.
  • Fig. 1 is a copper smelting molten slag
  • 2 is a reducing agent
  • 3 is a pressurized inert gas
  • 4 is a furnace body
  • 411 is a gas nozzle
  • 412 is a fuel burner
  • 413 is a feeding port
  • 414 is a rising smoke.
  • Road 415 is the copper sump discharge port
  • 416 is the slag discharge port
  • 5 is the fuel
  • 6 is the combustion improver
  • 7 is the slag layer
  • 8 is the copper ruthenium layer.
  • the furnace body 4 includes a molten pool in which slag depletion is mainly performed.
  • the furnace body 4 further includes a rising flue 414 communicating with the molten pool, and the furnace gas containing S0 2 generated during the depletion process is discharged from the rising flue 414, and is cooled and dusted. After emptying.
  • the furnace body 4 is provided with a feed port 413 through which copper smelting molten slag and a reducing agent are added.
  • the copper smelting molten slag 1 and the reducing agent 2 are respectively introduced into the depleting device through the feed tank 413 through the launder.
  • the furnace body 4 is provided with a gas nozzle 411 which is located on the side wall of the furnace body 4 and leads to the middle portion of the molten pool; the middle portion of the molten pool is also the position corresponding to the formed slag layer.
  • the gas nozzles 411 may be located on one side wall of the furnace body 4 or on both side walls of the furnace body 4. In the present invention, the number of the gas nozzles on one side wall may be one or more, preferably five.
  • the inert gas 3 is preferably introduced into the depletion device through the gas nozzle 411.
  • the gas nozzle 411 is located on the side wall of the furnace body 4 and can be immersed in the melt of the molten pool, that is, can be introduced into the slag layer, the introduced inert gas 3 can better provide boiling of the molten slag and strong stirring. The power will not re-grow the product into the slag, which is conducive to the sedimentation and separation of the product, and the efficiency is high.
  • the top of the furnace body 4 is provided with a fuel burner 412 into which the fuel 5 and the oxidant 6 are introduced.
  • the present invention preferably maintains the heat balance of the reduction reaction by burning the fuel 5 in the fuel burner 412.
  • the fuel enthalpy is generally used in the art; the oxidant is preferably industrial oxygen having an oxygen concentration of more than 95% by weight to ensure a small amount of furnace gas, so that the heat loss carried away by the furnace gas is sufficient small.
  • the amount of the fuel and the combustion improver to be used in the present invention is not particularly limited, and the heat generated by the combustion can maintain the heat balance of the reduction reaction.
  • the furnace body 4 is provided with a slag discharge port 416.
  • the feed port 413 is located at the top of one end of the furnace body 4, and the reaction material can be continuously added in proportion
  • the slag discharge port 416 is located at the lower portion of the other end of the furnace body 4, and the new slag can be continuously continuous It is discharged and granulated and used as a raw material for other industries.
  • the furnace body 4 is provided with a copper sluice vent 415 located in the furnace body.
  • the lowermost part of 4 is at the same end as the slag discharge port 416.
  • the copper matte can be discharged from the copper crucible discharge port 415 and granulated for use as a raw material for producing blister copper.
  • the material and size of the furnace body, the gas nozzle, and the fuel burner are not particularly limited, and may be commonly used in the art.
  • the dimensions of the feed port, the slag discharge port, the copper slag discharge port, the molten pool and the ascending flue are technical contents well known to those skilled in the art, and the present invention is also not particularly limited thereto.
  • the copper smelting molten slag 1 is introduced into the furnace body 4 through the feeding port 413 through the launder, and the FeS and Cu are added in proportion through the feeding port 413 through the launder.
  • S copper concentrate 2 S copper concentrate 2, and continuously introduces a pressurized inert gas 3 through a gas nozzle 411 immersed in the melt of the molten pool on the two side walls of the furnace body 4 to boil the molten slag and copper The concentrate is taken up into the molten slag to form a mixture.
  • the sensible heat of the slag melts the copper concentrate
  • the FeS in the copper concentrate reduces the Cu 2 0 in the slag to Cu 2 S, and at the same time reduces the Fe 3 0 4 in the slag to FeO, and the introduced
  • the inert gas forms a strong agitation of the reaction material, forcing Fe 3 0 4 , Cu 2 0, FeS to collide and polymerize for interaction, and the generated Cu 2 S and FeS droplets are combined to form copper ruthenium, and the generated FeO and Si0 2 are generated.
  • Slag formation in the furnace body A separate slag layer 7 and a copper ruthenium layer 8 are formed in 4.
  • the embodiment of the present invention introduces the fuel 5 and the combustion improver 6 into the fuel burner 412 provided at the top of the furnace body 4, and maintains the heat balance of the reduction reaction by burning the fuel 5 therein, and the combustion improver 6 for the combustion of the fuel 5 is Industrial oxygen, whose oxygen concentration is greater than 95% (weight ratio), to ensure a small amount of furnace gas, so as to ensure that the heat loss carried away by the furnace gas is sufficiently small.
  • the lowermost copper crucible discharge port 415 discharges the copper crucible in the liquid phase, and the depleted liquid phase slag is discharged through the slag discharge port 416. Further, the furnace gas containing S0 2 generated in the above process is discharged from the ascending flue 414, and is evacuated after being cooled, dusted, and removed.
  • the slag contains copper at 0.35% (by weight) or less, and can be used as a raw material for other industries after granulation; the copper bismuth contains 45% to 65% by weight of copper, and the granules thereof After being converted, it can be returned to the copper smelting process as a cold raw material.
  • the method for depleting copper smelting and melting furnace slag provided by the invention has high reaction efficiency and low tail copper content.
  • the method of the invention not only has simple process, convenient control and operation, but also has small equipment, low energy consumption, low investment and is suitable for promotion.
  • the copper smelting melting furnace slag used in the following examples has a copper content of 20%, an oxygen content of 30%, and a temperature of 1250 ° C.
  • the mass ratio of copper, sulfur and iron in the copper concentrate is 1: 1 : 1 , the quality of these three main components accounts for 75% of the total mass of copper concentrate.
  • the copper smelting molten slag 1 is introduced into the furnace body 4 through the feed tank 413 through a launder, and the copper concentrate containing FeS and Cu 2 S is proportionally added from the feed port 413 through the launder. 2.
  • the original slag is treated at 100t/h, and the copper concentrate is added at 20t/h; the pressure of nitrogen is 100 kPa; the ratio of sulfur content in copper concentrate to oxygen content in copper smelting furnace slag (S/0) is (0.6) ⁇ 1.2 ): 1 (mass ratio;).
  • the fuel 5 and the industrial oxygen gas 6 are introduced into the fuel burner 412 provided at the top of the furnace body 4, and the heat balance of the reduction reaction is maintained by burning the fuel 5 therein.
  • the slag of the depleted liquid phase is discharged through the slag discharge port 416, and the lowermost copper ruthenium is discharged through the ruthenium discharge port 415. Further, the furnace gas containing S0 2 generated in the above process is discharged from the ascending flue 414, and is evacuated after being cooled, dusted, and removed.
  • the slag contained 0.35% by weight of copper, and the copper ruthenium contained 45% by weight (by weight) according to the testing standards in the art.
  • the ratio of sulfur content in copper concentrate to oxygen content in copper smelting melting furnace slag (S/0) is (0.6 ⁇ 1.2): 1 (mass ratio), and the method of Example 1 is used.
  • the copper smelting and melting furnace slag is depleted to obtain separate copper crucibles and depleted slag.
  • the slag contained 0.35% by weight of copper, and the copper ruthenium contained 45% by weight (by weight) according to the testing standards in the art.
  • the method for depleting the copper smelting molten slag provided by the present invention can reduce the copper content in the treated slag, so that the final slag does not need to be subjected to beneficiation and the like, and can be used as raw materials for other industries after granulation. , investment and production costs are lower. Further, the present invention can produce copper bismuth, i.e., water copper, which can be used as a cold raw material to be returned to the upper copper smelting process while depleting the copper smelting molten slag.
  • copper bismuth i.e., water copper
  • the method of the invention has the advantages of simple process, convenient control and convenient operation, and is suitable for promotion.

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Abstract

一种铜冶炼贫化方法及装置，所述方法为将铜冶炼熔融炉渣（1）与还原剂（2）及带压力的惰性气体（3）混合，进行贫化。所述贫化装置包括炉体（4），炉体（4）上设置有加料口（413）和炉渣排放口（416），以及设置在炉体侧墙上的气体喷嘴（411）。

Description

铜冶炼炉渣贫化方法及装置 本申请要求于 2013 年 07 月 23 日提交中国专利局、 申请号为 201310311055.X,发明名称为 "铜冶炼熔融炉渣贫化的方法及用于铜冶炼熔融 炉渣贫化的贫化装置"的中国专利申请的优先权， 其全部内容通过引用结合在 本申请中。
技术领域
本发明涉及有色冶金技术领域，特别涉及一种铜冶炼熔融炉渣贫化的方法 及用于铜冶炼熔融炉渣贫化的贫化装置。 背景技术
在铜火法冶金行业，一种方法是由硫化物铜精矿间接生成粗铜， 这种方法 一般包括两个步骤：首先将硫化物铜精矿进行脱硫除铁，熔炼得到高品位铜锍， 然后将得到的铜锍进一步脱硫除铁， 吹炼得到粗铜。 另一种方法是釆用铜精矿 直接生产粗铜， 在实际生产中， 澳大利亚的 Olympic Dam 冶炼厂、 波兰的 Glogow冶炼厂以及赞比亚的 KCM冶炼厂釆用的就是由铜精矿直接生产粗铜 的工艺。 这些铜冶炼的方法具有一个共同的特点， 就是在生产所得炉渣中， Cu20和 Fe304的量都较高， 一般说来， 铜含量为 10%~20% (重量比）， Fe304 含量为 30%~50% (重量比）。
由于炉渣中铜含量较高， 上述工艺都釆用电炉贫化的方式，对炉渣进行处 理， 以降低炉渣中的含铜量。 在电炉贫化的过程中， 一般添加还原剂， 通过还 原反应来处理炉渣， 并且电炉可以维持温度， 保证还原反应的热力学基础。 但 是， 电炉贫化只为还原反应提供了热力学基础， 反应效率较低， 不但致使渣中 Cu20和 Fe304被还原的时间过长， 即贫化的时间长， 能耗高， 而且处理后的 炉渣含铜量为 1%~4% (重量比）， 即炉渣的含铜量仍然较高， 需要再进行选矿 等处理才能再应用， 这样就带来了投资和生产成本较高的问题， 不利于生产。 发明内容
为了解决以上技术问题，本发明提供一种铜冶炼熔融炉渣贫化的方法及用 于铜冶炼熔融炉渣贫化的贫化装置， 该方法贫化炉渣的反应效率高， 能使最终 炉渣中的铜含量降低， 无需再进行选矿等处理即可应用。 本发明提供一种铜冶炼熔融炉渣贫化的方法， 包括以下步骤： 在贫化装置中，将铜冶炼熔融炉渣和还原剂及带压力的惰性气体混合后进 行贫化， 得到贫化后的炉渣； 所述惰性气体的压力为 100kPa~800kPa。
优选的， 所述贫化装置包括：
炉体， 所述炉体内包括熔池， 所述炉体上设置有气体喷嘴、 加料口和炉渣 排放口；
所述气体喷嘴位于所述炉体的侧墙上， 且通向所述熔池的中部。
优选的，所述铜冶炼熔融炉渣和还原剂分别通过流槽由所述加料口引到贫 化装置中；
所述惰性气体通过所述气体喷嘴导入贫化装置中。
优选的， 所述炉体的顶部设置有燃料烧嘴；
向所述燃料烧嘴内导入燃料和助燃剂。
优选的， 所述助燃剂为氧浓度大于 95% (重量比） 的工业氧气。
优选的， 所述惰性气体为氮气。
优选的， 所述铜冶炼熔融炉渣的温度为 1050 °C~1350°C。
优选的， 所述还原剂为含有 FeS和 Cu2S的铜精矿。
优选的， 所述还原剂中含硫量与所述铜冶炼熔融炉渣中含氧量之比为 ( 0.6-1.5 ): 1 (质量比）。
本发明提供一种用于铜冶炼熔融炉渣贫化的贫化装置， 包括：
炉体， 所述炉体内包括熔池， 所述炉体上设置有气体喷嘴、 加料口和炉渣 排放口；
所述气体喷嘴位于所述炉体的侧墙上， 且通向所述熔池的中部。
与现有技术相比， 本发明将铜冶炼熔融炉渣和还原剂引到贫化装置中， 并 向所述贫化装置中导入带压力的惰性气体， 所述惰性气体的压力为 100kPa~800kPa, 混合后进行贫化， 得到贫化后的炉渣。 本发明利用铜冶炼熔 融炉渣的显热使还原剂熔化，通过所述还原剂将炉渣中的 Cu20和 Fe304还原； 导入的惰性气体对反应物料形成强烈的搅拌，使熔融炉渣沸腾， 并将还原剂卷 入熔融炉渣中，迫使 Cu20、 Fe304和还原剂碰撞聚合进行交互反应，形成渣相。 本发明通过惰性气体的强烈搅拌，促进反应物质的快速更新，强化了反应进程， 使渣性迅速被改变， 同时提高了液滴间的碰撞结合几率， 因此， 本发明此强化 过程能使最终炉渣中的铜含量降低。 实践表明， 本发明最终炉渣中的铜含量降 低到 0.35% (重量比 ) 以下， Fe304含量降低到 4% (重量比 ) 以下， 贫化后的 炉渣无需再进行选矿等处理， 可直接釆用粒化工艺粒化后用作其他工业的原 料。 附图说明
图 1 为本发明实施例提供的用于铜冶炼熔融炉渣贫化的贫化装置的结构 示意图。 具体实施方式
为了进一步理解本发明， 下面结合实施例对本发明优选实施方案进行描 述， 但是应当理解， 这些描述只是为进一步说明本发明的特征和优点， 而不是 对本发明权利要求的限制。
本发明提供了一种铜冶炼熔融炉渣贫化的方法， 包括以下步骤： 在贫化装置中，将铜冶炼熔融炉渣和还原剂及带压力的惰性气体混合后进 行贫化， 得到贫化后的炉渣； 所述惰性气体的压力为 100kPa~800kPa。
为适应冶金工艺的发展，克服现有技术的不足， 本发明提供的铜冶炼熔融 炉渣贫化的方法是一种炉渣贫化的改进方法， 能降低处理后的炉渣中的含铜 量， 使最终炉渣无需再进行选矿等处理， 粒化后即可作为其他工业的原料， 投 资和生产成本较低。
并且， 本发明对铜冶炼熔融炉渣进行贫化的同时， 能生产得到铜锍， 即水 铜， 其可作为冷原料返回到上道铜冶炼工序。
本发明实施例将铜冶炼熔融炉渣和还原剂引到贫化装置中，并向所述贫化 装置中导入带压力的惰性气体， 所述惰性气体的压力为 100kPa~800kPa, 混合 后进行贫化， 得到贫化后的炉渣。
在本发明中，所述铜冶炼熔融炉渣为本领域技术人员熟知的铜冶炼过程中 产生的富含 Cu20和 Fe304、 呈熔融状态的炉渣。 本发明对所述铜冶炼熔融炉 渣的组分没有特殊限制， 其中， 铜是氧化态的， 含量一般为 10%~20% (重量 比）； Fe304—般为含量为 30%~50% (重量比）。所述铜冶炼熔融炉渣具有显热， 其温度优选为 1050°C~1350°C。 本发明利用铜冶炼熔融炉渣的显热使还原剂熔 化， 无需补充额外的热量来帮助还原剂熔化， 节能效果较好， 节省经济成本。
本发明釆用还原剂与所述铜冶炼熔融炉渣混合，将炉渣中的 Cu20和 Fe304 还原， 炉渣中的铜得到富集并沉降在贫化装置底部， 使上层炉渣得到贫化。 本 发明对所述还原剂没有特殊限制， 优选为含有 FeS和 Cu2S的铜精矿， 生产成 本较低， 且较为环保。 所述含有 FeS和 Cu2S的铜精矿为本领域普通铜冶炼工 艺釆用的含有锍化物的铜精矿，以黄铜矿为主，本发明对其来源没有特殊限制。
在本发明实施例的贫化过程中，所述铜精矿中的 FeS将原炉渣中携带的铜 的氧化物 Cu20转化成硫化物 Cu2S, 新生成的 Cu2S与铜精矿中携带的 Cu2S 和 FeS能结合形成铜锍；所述铜精矿中的 FeS同时将炉渣中的铁的高价氧化物 Fe304还原成低价氧化物 FeO而改变渣型， 即炉渣中携带的铁的化合物发生转 变，由高熔点的 Fe304转换为低熔点的 FeO , FeO进一步的与炉渣中携带的 Si02 造渣， 形成更低熔点的 2FeO · Si02, 使最终炉渣的性质发生转变， 粘性降低， 利于铜锍的沉降、 分离， 使上层炉渣铜含量降低。 所述熔融炉渣与铜精矿成比 例混合， 所述铜精矿中含硫量与所述铜冶炼熔融炉渣中含氧量之比 （S/0 )优 选为 ( 0.6-1.5 ): 1 (质量比）, 更优选为 ( 0.6-1.2 ): 1 (质量比）。
本发明通过向上述反应物料中导入带压力的惰性气体，提供使熔融炉渣沸 腾和产生强烈的搅拌作用的动力。在本发明实施例中， 导入的惰性气体对反应 物料形成强烈的搅拌， 使熔融炉渣沸腾， 并将含有 FeS和 Cu2S的铜精矿卷入 熔融炉渣中， 迫使 Cu20、 Fe304和 FeS碰撞聚合进行交互反应， 促使生成的 Cu2S与 FeS小液滴相互结合生成铜锍， 生成的 FeO与 Si02造渣， 形成分开的 渣相和铜 4巟相。
本发明通过惰性气体的强烈搅拌，促进反应物质的快速更新， 强化了反应 进程， 使渣性迅速被改变， 同时提高了液滴间的碰撞结合几率， 因此， 本发明 此强化过程能使最终炉渣中的铜含量降低。 另外， 釆用惰性气体进行搅拌， 能 避免还原剂和被还原的 Cu2S、 FeO被氧化， 还原剂的使用量不会增加， 效率 较高, 成本较低。
在本发明中， 所述惰性气体的压力为 100kPa~800kPa , 优选为 200kPa~600kPa, 更优选为 300kPa~500kPa。 所述惰性气体优选为氮气， 增加 反应物料之间的接触， 提高反应效率， 同时氮气作为惰性气体不会将还原的 Cu2S和 FeO再次被氧化， 利于炉渣贫化。
本发明优选将铜冶炼熔融炉渣引到贫化装置中，按比例加入还原剂， 并向 所述贫化装置中导入带压力的惰性气体。在本发明中， 所述贫化装置优选釆用 以下的贫化装置。
本发明提供了一种用于铜冶炼熔融炉渣贫化的贫化装置， 包括： 炉体， 所述炉体内包括熔池， 所述炉体上设置有气体喷嘴、 加料口和炉渣 排放口；
所述气体喷嘴设置于所述炉体的侧墙上， 且通向所述熔池的中部。
本发明提供的贫化装置用于铜冶炼熔融炉渣贫化，利于降低处理后的炉渣 中的含铜量。
本发明实施例提供的用于铜冶炼熔融炉渣贫化的贫化装置为侧吹冶金炉， 其结构参见图 1 , 图 1为本发明实施例提供的用于铜冶炼熔融炉渣贫化的贫化 装置的结构示意图。
在图 1中， 1为铜冶炼熔融炉渣， 2为还原剂， 3为带压力的惰性气体， 4 为炉体， 411为气体喷嘴， 412为燃料烧嘴， 413为加料口， 414为上升烟道， 415为铜锍排放口， 416为炉渣排放口， 5为燃料， 6为助燃剂， 7为炉渣层， 8为铜锍层。
在本发明中， 炉体 4内包括熔池， 主要在其中进行炉渣贫化。 在本发明的 一个实施例中， 炉体 4内还包括与所述熔池相通的上升烟道 414, 贫化过程中 产生的含有 S02的炉气由上升烟道 414排出， 经过降温、 除尘后排空。
炉体 4上设置有加料口 413 , 通过其加入铜冶炼熔融炉渣和还原剂。 作为 优选，铜冶炼熔融炉渣 1和还原剂 2分别通过流槽由加料口 413引到贫化装置 中。
炉体 4上设置有气体喷嘴 411 , 其位于炉体 4的侧墙上， 且通向所述熔池 的中部； 所述熔池的中部也就是形成的渣层所对应的位置。 气体喷嘴 411可以 位于炉体 4的一个侧墙上， 也可以位于炉体 4的两个侧墙上。 在本发明中， 一 个侧墙上的所述气体喷嘴的数量可以为 1个或多个， 优选为 5个。 在本发明中， 惰性气体 3优选通过气体喷嘴 411导入贫化装置中。 由于气 体喷嘴 411位于炉体 4的侧墙上， 且能浸没于熔池的熔体中， 也就是能导入渣 层中， 导入的惰性气体 3 能更好地提供使熔融炉渣沸腾和产生强烈搅拌的动 力， 不会将产物重新搅起而进入炉渣， 利于产物的沉降、 分离， 效率较高。
在本发明的一个实施例中， 炉体 4的顶部设置有燃料烧嘴 412 , 向其中导 入燃料 5和助燃剂 6。 本发明优选通过在燃料烧嘴 412内燃烧燃料 5 , 产生的 热量可维持还原反应的热平衡。 所述燃料釆用本领域常用的即可； 所述助燃剂 优选为氧浓度大于 95% (重量比）的工业氧气， 以保证较小的炉气量， 从而使 由炉气带走的热量损失足够小。本发明对所述燃料和助燃剂的用量没有特殊限 制， 燃烧产生的热量能维持还原反应的热平衡即可。
在本发明中，炉体 4上设置有炉渣排放口 416。在本发明的一个实施例中， 加料口 413位于炉体 4的一端的顶部， 可成比例地连续加入反应物料， 而炉渣 排放口 416位于炉体 4的另一端的下部，新炉渣可由此连续排出并被粒化， 用 作其他工业的原料。
在本发明的一个实施例中， 炉体 4上设置有铜锍排放口 415 , 其位于炉体
4的最下部， 与炉渣排放口 416同一端。 铜锍可由铜锍排放口 415排出并被粒 化， 用作生产粗铜的原料。
本发明对所述炉体、 气体喷嘴、 燃料烧嘴的材质和尺寸没有特殊限制， 釆 用本领域常用的即可。 所述加料口、 炉渣排放口、 铜锍排放口、 熔池和上升烟 道的尺寸为本领域技术人员熟知的技术内容， 本发明对此也无特殊限制。
本发明实施例进行炉渣贫化时，在炉体 4的一端，铜冶炼熔融炉渣 1通过 流槽由加料口 413引到炉体 4中，通过流槽由加料口 413按比例加入含有 FeS 和 Cu2S的铜精矿 2, 并通过炉体 4的两个侧墙上的、 浸没于熔池的熔体中的 气体喷嘴 411连续导入带压力的惰性气体 3 , 使熔融炉渣沸腾， 并将铜精矿卷 入熔融炉渣中， 形成混合体。
在此过程中，炉渣的显热使铜精矿熔化，铜精矿中的 FeS将炉渣中的 Cu20 还原成 Cu2S, 同时将炉渣中的 Fe304还原成 FeO, 而导入的惰性气体对反应物 料形成强烈的搅拌， 迫使 Fe304、 Cu20、 FeS碰撞聚合进行交互反应， 促使生 成的 Cu2S与 FeS小液滴相互结合生成铜锍，生成的 FeO与 Si02造渣，在炉体 4内形成分开的炉渣层 7和铜锍层 8。
并且， 本发明实施例向设置于炉体 4顶部的燃料烧嘴 412 中导入燃料 5 和助燃剂 6, 通过在其中燃烧燃料 5维持还原反应的热平衡， 而用于燃料 5燃 烧的助燃剂 6是工业氧气， 其氧浓度大于 95% (重量比）， 以保证较小的炉气 量， 从而保证由炉气带走的热量损失足够小。
在炉体 4的另一端， 最下部的铜锍排放口 415排出液相的铜锍， 而贫化后 的液相的炉渣通过炉渣排放口 416 排出。 另外， 上述过程中产生的含有 S02 的炉气由上升烟道 414排出， 经过降温、 除尘、 脱^ 后排空。
贫化完成后， 得到分开的铜锍和贫化后的炉渣。 按照本领域的检测标准， 所述炉渣含铜在 0.35% (重量比）以下， 其粒化后可作为其他工业的原料； 所 述铜锍含铜 45%~65% (重量比 ), 其粒化后可作为冷原料返回到上道铜冶炼工 序。
综上所述， 本发明提供的铜冶炼熔融炉渣贫化的方法反应效率高，尾渣含 铜低。 另外， 本发明所述方法不但工艺简单， 控制、 操作方便， 而且设备小， 能耗低， 投资少， 适于推广。
为了进一步理解本发明，下面结合实施例对本发明提供的铜冶炼熔融炉渣 贫化的方法及用于铜冶炼熔融炉渣贫化的贫化装置进行具体描述。
以下实施例中使用的铜冶炼熔融炉渣中铜含量为 20%、 含氧量为 30%, 其温度为 1250°C ; 铜精矿中铜、 硫、 铁三种主要成分的质量比为 1 : 1 : 1 , 这三 种主要成分的质量占铜精矿总质量的 75%。
实施例 1
在图 1所示的贫化装置中，铜冶炼熔融炉渣 1通过流槽由加料口 413引到 炉体 4中， 通过流槽由加料口 413按比例加入含有 FeS和 Cu2S的铜精矿 2, 并通过炉体 4的两个侧墙上的、浸没于熔池的熔体中的气体喷嘴 411连续导入 带压力的氮气 3 , 混合后进行贫化， 在炉体 4内形成分开的炉渣层 7和铜锍层 8。
其中， 处理原炉渣 100t/h, 投加铜精矿 20t/h; 氮气的压力为 lOOkPa; 铜 精矿中含硫量与铜冶炼熔融炉渣中含氧量之比 （S/0 )为 （0.6~1.2 )： 1 (质量 比；)。 向设置于炉体 4顶部的燃料烧嘴 412中导入燃料 5和工业氧气 6, 通过在 其中燃烧燃料 5维持还原反应的热平衡。
贫化后的液相的炉渣通过炉渣排放口 416排出，最下部的铜锍经铜锍排放 口 415排出。 另外， 上述过程中产生的含有 S02的炉气由上升烟道 414排出， 经过降温、 除尘、 脱^ 后排空。
得到分开的铜锍和贫化后的炉渣后，按照本领域的检测标准， 所述炉渣含 铜 0.35% (重量比 ), 所述铜锍含铜 45% (重量比）。
实施例 2
按照氮气的压力为 800kPa, 铜精矿中含硫量与铜冶炼熔融炉渣中含氧量 之比（S/0 )为 （0.6~1.2 )： 1 (质量比）， 釆用实施例 1的方法进行铜冶炼熔融 炉渣贫化， 得到分开的铜锍和贫化后的炉渣。
得到分开的铜锍和贫化后的炉渣后，按照本领域的检测标准， 所述炉渣含 铜 0.35% (重量比 ), 所述铜锍含铜 45% (重量比）。
由以上实施例可知，本发明提供的铜冶炼熔融炉渣贫化的方法能降低处理 后的炉渣中的含铜量，使最终炉渣无需再进行选矿等处理，粒化后即可作为其 他工业的原料， 投资和生产成本较低。 并且， 本发明对铜冶炼熔融炉渣进行贫 化的同时，能生产得到铜锍，即水铜，其可作为冷原料返回到上道铜冶炼工序。
另外， 本发明所述方法还具有工艺简单， 控制、 操作方便等优点， 适于推 广。
以上实施例的说明只是用于帮助理解本发明的方法及其核心思想。应当指 出， 对于本技术领域的普通技术人员来说， 在不脱离本发明原理的前提下， 还 可以对本发明进行若干改进和修饰，这些改进和修饰也落入本发明权利要求的 保护范围内。

Claims

权 利 要 求
1、 一种铜冶炼熔融炉渣贫化的方法， 包括以下步骤：
在贫化装置中，将铜冶炼熔融炉渣和还原剂及带压力的惰性气体混合后进 行贫化， 得到贫化后的炉渣； 所述惰性气体的压力为 100kPa~800kPa。
2、 根据权利要求 1所述的方法， 其特征在于， 所述贫化装置包括： 炉体， 所述炉体内包括熔池， 所述炉体上设置有气体喷嘴、 加料口和炉渣 排放口；
所述气体喷嘴位于所述炉体的侧墙上， 且通向所述熔池的中部。
3、 根据权利要求 2所述的方法， 其特征在于， 所述铜冶炼熔融炉渣和还 原剂分别通过流槽由所述加料口引到贫化装置中；
所述惰性气体通过所述气体喷嘴导入贫化装置中。
4、 根据权利要求 3所述的方法， 其特征在于， 所述炉体的顶部设置有燃 料烧嘴；
向所述燃料烧嘴内导入燃料和助燃剂。
5、 根据权利要求 4所述的方法， 其特征在于， 所述助燃剂为氧浓度大于 95% (重量比） 的工业氧气。
6、 根据权利要求 1~5任一项所述的方法， 其特征在于， 所述惰性气体为 氮气。
7、 根据权利要求 1~5任一项所述的方法， 其特征在于， 所述铜冶炼熔融 炉渣的温度为 1050°C~1350°C。
8、 根据权利要求 1~5任一项所述的方法， 其特征在于， 所述还原剂为含 有 FeS和 Cu2S的铜精矿。
9、 根据权利要求 8所述的方法， 其特征在于， 所述还原剂中含硫量与所 述铜冶炼熔融炉渣中含氧量之比为 （0.6~1.5 )： 1 (质量比）。
10、 一种用于铜冶炼熔融炉渣贫化的贫化装置， 包括：
炉体， 所述炉体内包括熔池， 所述炉体上设置有气体喷嘴、 加料口和炉渣 排放口；
所述气体喷嘴位于所述炉体的侧墙上， 且通向所述熔池的中部。
PCT/CN2014/077950 2013-07-23 2014-05-21 铜冶炼炉渣贫化方法及装置 WO2015010500A1 (zh)

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