WO2009110627A1 - 鋼屑中の銅の除去方法 - Google Patents
鋼屑中の銅の除去方法 Download PDFInfo
- Publication number
- WO2009110627A1 WO2009110627A1 PCT/JP2009/054370 JP2009054370W WO2009110627A1 WO 2009110627 A1 WO2009110627 A1 WO 2009110627A1 JP 2009054370 W JP2009054370 W JP 2009054370W WO 2009110627 A1 WO2009110627 A1 WO 2009110627A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- hot metal
- copper
- sulfur
- steel
- flux
- 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
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
- C22B9/106—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents the refining being obtained by intimately mixing the molten metal with a molten salt or slag
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/04—Removing impurities other than carbon, phosphorus or sulfur
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
- C21C1/025—Agents used for dephosphorising or desulfurising
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/064—Dephosphorising; Desulfurising
- C21C7/0645—Agents used for dephosphorising or desulfurising
-
- 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
- C22B15/0056—Scrap 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
- 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
-
- 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
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C2200/00—Recycling of waste material
-
- 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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/005—Preliminary treatment of scrap
-
- 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 present invention removes copper in copper scrap, which is a quality problem when manufacturing high-grade steel using steel scrap as an iron source (steel scrap). ) It is about the method.
- the iron source used in the steelmaking process is mainly composed of hot metal obtained by reducing iron ore in a blast furnace.
- Steel scrap generated in the processing process of steel materials, old products such as buildings and machinery products A considerable amount of steel scrap is also generated.
- the production of hot metal in the blast furnace requires a great deal of energy to reduce and melt iron ore, whereas steel scraps only require heat of melting, and if steel scraps are used in the steelmaking process, There is an advantage that the amount of energy used for reducing heat of iron ore can be reduced. Therefore, it is desirable to promote the use of steel scrap from the viewpoint of global warming prevention by energy saving and CO 2 reduction.
- steel scrap was often used by directly putting it into steel furnaces such as converters and electric furnaces.
- steel furnaces such as converters and electric furnaces.
- various steel scraps are used as the iron source, it is difficult to adjust the composition of the molten steel produced.
- the converter uses the heat of combustion of carbon in the hot metal as the melting heat of steel scrap, so it is difficult to maintain the temperature required in the next process if the mixing ratio of steel scrap is increased.
- the electric furnace has a drawback in terms of energy consumption, which is low in energy efficiency.
- Patent Document 1 Japanese Patent Laid-Open No. Hei 4 198431
- Patent Document 1 describes a method in which Na2 2 A method is disclosed in which a copper component in molten iron is separated and removed into a Na 2 S flux as Cu 2 S by contact reaction with a flux containing S as a main component. Disclosure of the invention
- the Na 2 S flux power sulfur (S) component is mixed in the molten iron.
- the ratio of the Cu concentration in the slag formed on the molten iron as the flux melts and the Cu concentration in the molten iron ie, the distribution ratio
- the ratio of the Cu concentration in the slag formed on the molten iron as the flux melts and the Cu concentration in the molten iron is about 30 at most. It is necessary to prevent the deterioration.
- Patent Document 1 does not disclose any desulfurization of high-carbon molten iron after copper removal. Furthermore, in Patent Document 1, the force of performing copper removal treatment by stirring the hot metal and slag by blowing Ar gas from the bottom of the reaction vessel (hot metal hot pot) is insufficient in stirring the slag, and the bottom of the hot metal hot pot Installation of gas tuyeres complicates equipment. Furthermore, in order to make up for the lack of stirring, it is equipped with an electric heating device to maintain the reaction temperature between 1200 and 1500, and a covered reaction vessel is used to block contact with the atmosphere. Is a big deal.
- the present invention has been made in view of the above circumstances, and the purpose of the present invention is to produce copper with high efficiency and large scale when manufacturing high-grade steel using copper-containing steel scrap as an iron source. It is to provide a method of removing without requiring.
- the method for removing copper in steel scraps according to the first invention for solving the above-mentioned problem is to produce a hot metal for steel making by melting the copper-containing steel scraps by addition of carbon, and then to the hot metal.
- the copper contained is removed using a sulfur-containing flux, and then the sulfur contained in the hot metal is removed.
- a method for removing copper in copper scrap according to a second invention is characterized in that, in the first invention, the sulfur-containing flux contains Na 2 S as a main component or mainly comprising of. is there.
- the method for removing copper in steel scrap according to the third invention is the method of removing copper in the first or second invention, wherein a material mainly composed of Na 2 C0 3 and an iron monosulfur alloy are used as starting materials for the sulfur-containing flux. It is characterized by its use.
- the method for removing copper in steel scrap according to the fourth invention is the method for removing copper in the first to third inventions, wherein the hot metal before removing copper by the sulfur-containing flux has a temperature of 12003 ⁇ 4 or more and 1500 or less, The carbon concentration is 2 mass% or more and the copper concentration is 0.1 mass% or more and 1.0 mass% or less ⁇ :. '
- a method for removing copper from copper scraps in the fourth aspect wherein the temperature of the hot metal before removing copper by the sulfur-containing flux is 1250 "3 ⁇ 4: 1350 It is characterized by.
- the method for removing copper in steel scraps according to a sixth aspect of the present invention provides the method for removing copper in steel scraps according to any one of the first to fifth aspects, wherein the hot metal before removing copper by the sulfur-containing flux has a sulfur concentration of 0.01 mass%. This is the feature.
- a seventh aspect of the present invention there is provided a method for removing copper in steel scraps according to any one of the first to sixth aspects, wherein the copper contained in the hot metal is removed by a mechanical stirring type refiner (refining equipment with mechanical stirrers). It is characterized in that it is performed in.
- the method for removing copper in steel scraps provides the method for removing copper contained in the hot metal in any one of the first to sixth aspects of the invention, wherein the sulfur-containing flux is transferred to a carrier gas. At the same time, it is characterized by being blown into hot metal in a reaction vessel (refining vessels).
- the sulfur-containing flux may be blown and added (indicating added).
- the starting material for the sulfur-containing flux for example, soda ash and At least a part of (Losulfur) may be blown into the hot metal in the reaction vessel together with the carrier gas.
- a part of the starting material is blown, only a starting material not containing sulfur (for example, soda ash) may be blown, and a starting material containing sulfur (for example, ferrosulfur) may be supplied by other means.
- a ninth aspect of the present invention there is provided a method for removing copper from steel scraps according to any one of the first to eighth aspects, wherein the copper-containing steel scrap is a vertical furnace in which a carbon bed is formed. It is characterized by the fact that it is used for carburizing and melting.
- a method for removing copper from copper scraps according to any one of the first to sixth aspects, wherein the copper-containing steel scraps are added using a vertical furnace in which a carbon material bed is formed. It is characterized by melting the charcoal and removing the copper in the hot metal by supplying the sulfur-containing flux to the hot metal flowing from the vertical furnace to the hot metal holding vessel (tilting runner at casthouse). is there.
- the method for removing copper in the copper scrap according to the eleventh invention is characterized in that, in any one of the first to tenth inventions, the removal of sulfur contained in the hot metal is performed with a mechanical stirring type scouring apparatus. To do.
- the method for removing copper in steel scraps according to the twelfth aspect of the present invention is the method of removing copper in the first to eleventh aspects of the invention, in which the blast furnace hot metal is mixed with the hot metal after the copper is removed by the sulfur-containing flux, It is characterized by removing sulfur contained in the hot metal mixed with blast furnace hot metal.
- Fig. 1 is a graph showing the relationship between the hot metal temperature before copper removal (horizontal axis: C) and the copper removal rate (%: vertical axis) after copper removal. -Best mode for carrying out the invention
- the sulfur-containing flux is brought into contact with the hot metal, and the copper in the hot metal is separated and removed into the sulfur-containing flux as copper sulfide (Cu 2 S).
- the sulfur-containing flux those containing an alkali metal or alkaline earth metal sulfide as a main component are suitable.
- An iron-sulfur alloy (ferrosulfur) may be mixed to increase the sulfur content in the sulfur-containing flux.
- a flux mainly composed of Na 2 S is particularly suitable. Flux field mainly composed of Na 2 S.
- Na 2 C0 3 sina ash
- iron-sulfur alloy Feuerosulfur
- the cost and copper removal efficiency can be reduced.
- the material and the iron one sulfur alloy mainly containing Na 2 C0 3 is contacted with the hot metal, Na 2 S is produced in the flux, which is the copper removal effect as the main component in the flux Therefore, it is not necessary to manufacture Na 2 S in advance.
- the amount of sulfur in the sulfur-containing flux and the amount of flux used may be selected as appropriate in consideration of costs, copper removal efficiency, and the target copper concentration.
- the flux mainly containing Na 2 S in terms of more efficient copper removal, it is desirable mole fraction of Na 2 S in the flux is about 0.2 or more.
- the sulfur-containing fluxes for example, those mainly composed of alkali metal or alkaline earth metal sulfides
- the sulfur-containing material has a molar fraction of S of about 0.2 or more.
- a weight ratio of the two is preferably about 1: 0.4 to 1: 4, and the mole fraction of S is The expected formation Na 2 S should be about 0.2 or more in terms of molar fraction.
- copper removal with a sulfur-containing flux is a process with a low power distribution ratio (the ratio of the Cu concentration in the flux to the Cu concentration in the hot metal) that has been confirmed in principle. It is effective to promote the mass transfer on the slag side formed in the reaction vessel by adding a sulfur-containing flux. For this purpose, it is effective to stir the slag layer.
- the strength of copper removal treatment in the hot metal stage The temperature range of hot metal (at 1200-1400) is lower than the temperature range of molten steel (at 1550-1700), and the slag fluidity is also low. Since it is low, the effect of promoting copper removal by stirring slag is large.
- a typical example of the mechanical stirring type scouring apparatus is stirring using an impeller (also referred to as “stirring blade”).
- the impeller was immersed in the hot metal contained in a ladle-shaped reaction vessel (generally from above), and this impeller was rotated about its axis to be added to the hot metal and hot metal.
- This is a method of forcibly stirring the sulfur-containing flux.
- the sulfur-containing flutter put on the hot metal is sufficiently entrained in the hot metal, and the hot metal and the sulfur-containing flux are stirred with extremely high efficiency.
- the mechanical agitation method allows slag to be contained in hot metal.
- the carrier gas also functions as a stirring gas
- the stirring strength of hot metal and hot metal slag is much better than that of a mechanical stirring type smelting device, but much better than the gas stirring method. Is called.
- an inert gas such as Ar gas or a reducing gas such as propan may be supplied onto the hot metal bath surface in order to prevent air from entering the atmosphere.
- hot metal before copper removal treatment that is, the temperature and carbon 'copper' sulfur etc. composition of steel containing carbon containing steel containing carbon scraps produced by carburizing and dissolving copper-containing copper scrap is a method of processing equipment. It can be determined appropriately according to the capacity and characteristics of the hot metal flux.
- the guideline is described below.
- the temperature of the hot metal before the copper removal treatment is 1200 or more and 1500 or less, preferably 1250 ° C or more and 1350 or less. If the hot metal temperature is less than 12003 ⁇ 4, there is a concern about the solidification and solidification of the flux and the hot metal itself due to the low temperature. In particular, considering the temperature guarantee in the subsequent desulfurization process and converter decarburization process, it is desirable to set it to 12503 ⁇ 4 or more. On the other hand, at 1500 ° C or higher, high temperature flux evaporation cannot be ignored. In other words, the lower the hot metal temperature, the better to suppress the evaporation of the sulfur-containing flux and perform the copper removal reaction efficiently. Therefore, the hot metal temperature should be 1350T or less for efficient copper removal reaction. Is desirable.
- the carbon concentration in the hot metal before the copper removal treatment is preferably 2% by mass or more.
- the reaction in which the copper in the hot metal becomes copper sulfide proceeds more thermodynamically as the carbon concentration in the hot metal becomes higher.
- the carbon concentration in the hot metal before the copper removal treatment is less than 2% by mass, the liquidus temperature of the hot metal rises, and adhesion of the hot metal to the vessel wall becomes a problem. It should be noted that there is no problem even if carbon is contained up to the saturation concentration.
- the copper concentration in the hot metal before the copper removal treatment is 0.1 mass. / 0 to 1.0% by mass is preferable.
- the copper concentration in the hot metal before copper removal treatment exceeds 1.0% by mass, the amount of sulfur-containing flux required for copper removal becomes excessive, and the practical load is large. On the other hand, if it is less than 0.1% by mass, no copper removal treatment should be performed. However, it can be applied to high-grade steel by, for example, diluting with hot metal having a low copper content.
- the sulfur concentration of the hot metal before the copper removal treatment is preferably 0.01% by mass or more, more preferably 0.05% by mass or more.
- the hot metal sulfur concentration before copper removal treatment is 0.01 mass. If it is less than / o, the amount of sulfur dissolved in the hot metal containing sulfur will be excessive, and the utilization efficiency of the sulfur containing flux will be low, which is not economical.
- the upper limit of the sulfur concentration does not need to be specified, but if it is too high, desulfurization treatment will be hindered, so it is desirable to set it to 0.5 mass% or less.
- the silicon concentration is 0.5 mass. /.
- the manganese concentration is preferably 0.5% by mass or less.
- blast furnace hot metal hot metal produced from a blast furnace
- steelmaking iron produced by carburizing and melting copper-containing steel scrap
- the copper contained in may be removed using a sulfur-containing flats.
- the composition of copper-containing scrap iron is 0.1 mass in copper concentration in the hot metal obtained. Anything over / o is acceptable. Since dilution with blast furnace hot metal is possible, the upper limit of the copper concentration of hot metal from the scrap iron is allowed to be around 1.0% by mass. The copper concentration of lower scrap iron is generally within the above range.
- Processes for producing hot metal by carburizing and dissolving copper-containing copper scrap include a method using an electric furnace, a method using a converter, a method using a vertical furnace, etc. A method using a vertical furnace in which a bed is formed is preferable.
- the vertical furnace with a charcoal bed formed inside is a vertical furnace in which copper-containing steel scraps and coatas are added from the upper part of the vertical furnace and, if necessary, fluxes. Air, oxygen-enriched air, oxygen gas, etc. are preferably blown as hot air from the tuyere provided at the lower part of the furnace to burn the coke, and the copper-containing steel scraps and the iron making agent are put into the furnace by the combustion heat of coatus
- This is a device that takes out molten iron and liquid slag from the tap at the bottom of the furnace.
- the hot metal taken out from the hot water outlet at the bottom of the furnace flows through a refractory bed that is installed in the casthouse in front of the furnace, and hot metal is placed below the tip of the bed.
- a hot metal holding container such as a transfer ladle
- a vertical furnace with a charcoal bed inside only the coke is packed in the range from the furnace bottom to a certain height above the tuyere, and this is burned and the copper charged into the upper part of the coatus is charged. Contains steel scrap.
- the coke packed at the bottom of the furnace is called the “charcoal bed”, and this charcoal bed burns and wears out.
- the coke is charged from the top of the furnace body.
- Molten iron which is produced by melting copper-containing steel scraps, flows down the gaps in the coatus and is carburized by the coke to produce hot metal.
- a vertical furnace with a charcoal bed inside is more energy efficient than an electric furnace.
- the sulfur concentration in the hot metal is generally higher than that in the blast furnace hot metal. Taking advantage of this high sulfur concentration, copper removal with a sulfur-containing flux can be made much more advantageous. That is, since the sulfur concentration in the hot metal is high, the sulfur-containing flux force requires less movement of sulfur into the hot metal, and the utilization efficiency of the sulfur-containing flux can be significantly increased.
- the sulfur concentration in the blast furnace hot metal is generally 0.04 mass, except in the very early stage of power operation, which depends on the raw material, and at the start-up after a wind break. / 0 or less.
- the copper removal treatment may be carried out by supplying the sulfur-containing flux by adding it to the hot metal flowing through the iron bed, blowing it with the gas, or blowing it with the gas.
- the sulfur-containing flux supplied to the hot metal flowing through the hot metal is not only decopperized during the period when the hot metal flows through the hot metal, but also vigorously stirred with the hot metal by dropping from the hot metal into the hot metal holding container.
- the copper removal treatment of the hot metal is efficiently performed.
- the copper removal reaction is further promoted by previously placing a sulfur-containing flux separately in the hot metal holding container.
- the copper removal treatment can be further performed by using the above-described method, for example, a mechanical stirring type refiner or a flux blowing method. .
- the copper concentration in the hot metal after copper removal may be set according to the purpose of use of the steel, but is usually about 0.25% by mass or less. Gudesulfurization treatment>
- the desulfurization treatment is performed by applying a desulfurizing agent to the hot metal. Specific methods include a method using a known mechanical stirring type refinery device, a method by blowing powder from a lance, and a method using a converter. It can be either.
- the generated slag may be removed, and then the desulfurization process may be performed with the same mechanical stirring type refinement apparatus.
- the extremely high stirring effect by mechanical stirring can be used for both copper removal and desulfurization.
- the desulfurizing agent examples include a desulfurizing agent mainly composed of CaO, a desulfurizing agent mainly composed of calcium carbide, Various desulfurization agents such as a desulfurization agent mainly composed of soda ash and metallic Mg can be used.
- the blast furnace hot metal may be additionally mixed with the hot metal subjected to the decoppering treatment, and then the mixed hot metal may be desulfurized. Furthermore, the blast furnace hot metal may be mixed with the hot metal after the desulfurization treatment.
- the sulfur-containing flux subjected to the decopperization treatment is removed from the reaction vessel. If the desulfurization treatment is performed without removing the sulfur-containing flux, the copper sulfide (Cu 2 S) in the sulfur-containing flux may be decomposed and returned to the hot metal, which may increase the copper concentration in the hot metal.
- the slag removal work is owned by each steelworks using any method such as a method using a known slag dragger, a method using a slag suction machine, or a method of discharging the slag in the container by tilting the hot metal container. Select the one that is appropriate for the equipment situation.
- the concentration of sulfur in the hot metal after desulfurization may be set according to the purpose of use of the steel, but is usually about 0.25% by mass or less.
- the copper in the hot metal brought from the steel scrap is separated and removed into the sulfur-containing flux.
- copper that has been difficult to separate by the method of separating and removing by magnetic separation or the like can be separated efficiently.
- the removal of sulfur in the hot metal brought from the sulfur-containing flux is performed, so that it is possible to efficiently obtain a low level of copper-containing steel scrap, copper and sulfur, and hot metal. it can.
- Test No. 1 and Test No. 3 it was found that by desulfurization treatment, it was finally possible to obtain hot metal with low copper and sulfur concentrations, and it could be used without any problem as hot metal for high-grade steel.
- test was conducted to perform decopperization and desulfurization after decopperization (tests ⁇ ⁇ 4 to 15).
- the copper removal treatment was performed by charging a hot metal for steelmaking in a pan-shaped reaction vessel and adding a hopper force for supplying a fermenting agent provided on the pan to remove copper.
- Hot metal ton as flux for copper removal 40 kg of iron-sulfur alloy (ferrosulfur, sulfur content: 48 mass%) and 30 kg of soda ash (Na 2 C0 3 ) per ton of hot metal were used.
- As the flux for copper removal 53 kg of iron-sulfur alloy (fluorosulfur, sulfur content: 36 mass%) per molten iron and 30 kg of soda ash (Na 2 C0 3 per ton of molten iron) ) was used.
- the hot metal temperature is 1200 or more and 1500 ⁇ : or less, and the carbon concentration is 2 mass. /.
- the concentration of copper in the hot metal was 0.4 or more, and it was confirmed that the copper removal was performed well. Meanwhile, test ⁇ .10 ⁇ 1 In No.
- the copper removal rate ⁇ (copper concentration in hot metal before treatment, copper concentration in hot metal after treatment) X 100Z in hot metal before treatment Copper concentration) was less than 40%.
- Test Nos. 13 and 14 satisfy the preferable conditions of a sulfur concentration of 0.01% by mass or more, but since the more preferable 0.05% by mass or more is not satisfied, the copper removal rate is nearly 40% (however, Less than 40%).
- the temperature of the steelmaking steel produced in the vertical furnace was 1400 ° C, the carbon concentration was 4.0% by mass, the copper concentration was 0.30% by mass, and the sulfur concentration was 0.11% by mass.
- a flux for removing copper was added from a hopper for supplying a fertilizer on the pan.
- As the flux for copper removal iron-sulfur alloy (ferrosulfur, sulfur content: 48% by mass) and soda ash (Na 2 C0 3 ) were used.
- the method of stirring the hot metal in the pan is to immerse the impeller covered with refractory in the hot metal and rotate the impeller. The method of stirring was used. Table 3 lists the test conditions and test results.
- the hot metal components before copper removal treatment are 4.5 to 4.7% by mass of carbon, 0.20% by mass of silicon, 0.15% by mass of manganese and 0.1% by mass of phosphorus. The test was conducted by adjusting to 0. 05% by mass. Table 3
- Figure 1 shows the relationship between the hot metal temperature before the copper removal treatment and the copper removal rate.
- the hot metal temperature was 1250-1500
- the lower the hot metal temperature the higher the copper removal rate.
- the copper removal rate decreased to 33.3%. This is thought to be due to the fact that the reactivity of the flux for copper removal has deteriorated due to low temperatures. From these results, it was found that a high copper removal rate exceeding 50% can be obtained by setting the hot metal temperature in the range of 1250 to 1350.
- a copper removal test was conducted on a hot metal for steelmaking contained in a pan-shaped reaction vessel (test No. 23- 29).
- test No. 23- 29 An injection lance coated with a refractory was immersed in the hot metal in the pan, and a part or all of the flux for removing copper was blown into the hot metal through the injection lance using nitrogen gas as a transport gas.
- the top plate was added from the hopper for supplying the fertilizer on the pan.
- Iron-sulfur alloy (ferrosulfur, sulfur content: 48% by mass) and soda ash (Na 2 C0 3 ) were used for the flux for removing copper.
- Table 4 lists the test conditions and test results.
- the hot metal component before the copper removal treatment is 4.5 to 4.7 masses of carbon. / 0 , silicon (0.20% by mass), mangan (0.15% by mass) and phosphorus (0.05% by mass) were prepared, and the hot metal temperature was 1400 ° C.
- the immersion depth of the injection lance if the bath depth of the hot metal is H (m) and the distance to the tip of the hot metal bath is L (m), L / H should be 0.3 or more.
- the blown flux can contribute to the copper removal reaction.
- Any injection lance may be used as long as it can withstand the process of immersing in hot metal and blowing flux. Further, the relationship between the flow rate of the conveying gas and the flux blowing speed has no effect on the metallurgical properties as long as flux clogging does not occur in the induction lance.
- Ar gas may be used as long as it is an inert gas. Table 4
- the copper in the hot metal brought from the steel scrap is separated and removed into the sulfur-containing flux, so that the steel scrap is physically decomposed. Copper that was difficult to separate by the method of separation and removal by magnetic separation can be separated efficiently.
- the removal of sulfur in the hot metal, which is brought about by the sulfur-containing flux force, is performed after the copper removal treatment, the hot metal containing less copper and sulfur can be efficiently obtained from the copper-containing copper scrap.
- copper-containing steel scrap can be used as an iron source for high-grade copper, and the use of lower-grade copper scrap is promoted.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/920,741 US20110000340A1 (en) | 2008-03-05 | 2009-03-03 | Method for removing copper in steel scraps |
KR1020107019379A KR101276921B1 (ko) | 2008-03-05 | 2009-03-03 | 강 스크랩 중의 구리 제거방법 |
CN200980107370.2A CN101960023B (zh) | 2008-03-05 | 2009-03-03 | 去除钢屑中的铜的方法 |
CA 2715322 CA2715322C (en) | 2008-03-05 | 2009-03-03 | Method for removing copper in steel scraps |
KR1020137009853A KR20130045955A (ko) | 2008-03-05 | 2009-03-03 | 강 스크랩 중의 구리 제거방법 |
MX2010009609A MX2010009609A (es) | 2008-03-05 | 2009-03-03 | Proceso para remover cobre contenido en chatarras de acero. |
EP20090717326 EP2248916B1 (en) | 2008-03-05 | 2009-03-03 | Process for removal of copper contained in steel scraps |
BRPI0909687A BRPI0909687A2 (pt) | 2008-03-05 | 2009-03-03 | método para remover cobre em fragmentos de aço |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008-054635 | 2008-03-05 | ||
JP2008054635 | 2008-03-05 | ||
JP2008-284935 | 2008-11-06 | ||
JP2008284935 | 2008-11-06 | ||
JP2009006297A JP5402005B2 (ja) | 2008-03-05 | 2009-01-15 | 鋼屑中の銅の除去方法 |
JP2009-006297 | 2009-01-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2009110627A1 true WO2009110627A1 (ja) | 2009-09-11 |
Family
ID=41056175
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2009/054370 WO2009110627A1 (ja) | 2008-03-05 | 2009-03-03 | 鋼屑中の銅の除去方法 |
Country Status (10)
Country | Link |
---|---|
US (1) | US20110000340A1 (ja) |
EP (1) | EP2248916B1 (ja) |
JP (1) | JP5402005B2 (ja) |
KR (2) | KR20130045955A (ja) |
CN (1) | CN101960023B (ja) |
BR (1) | BRPI0909687A2 (ja) |
CA (1) | CA2715322C (ja) |
MX (1) | MX2010009609A (ja) |
TW (1) | TWI409338B (ja) |
WO (1) | WO2009110627A1 (ja) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011084811A (ja) * | 2009-09-15 | 2011-04-28 | Jfe Steel Corp | 溶銑の製造方法 |
JP2011195887A (ja) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | 鋼屑中の銅の除去方法及び鋼屑を鉄源とした溶鋼の製造方法 |
JP2011195886A (ja) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | 鋼屑中の銅の除去方法 |
KR101462168B1 (ko) * | 2012-12-26 | 2014-11-14 | 주식회사 포스코 | 용철 처리장치 및 그 처리방법 |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101321086B1 (ko) * | 2010-12-22 | 2013-10-23 | 주식회사 포스코 | 용선 정련 방법 |
JP5724861B2 (ja) * | 2011-12-09 | 2015-05-27 | 新日鐵住金株式会社 | 鉄スクラップからの銅の硫化除去方法 |
JP6065538B2 (ja) * | 2012-11-20 | 2017-01-25 | Jfeスチール株式会社 | 溶銑の脱銅処理方法 |
CN107130082B (zh) * | 2017-04-26 | 2019-05-07 | 湖南工业大学 | 一种高铜铁料中铜元素有效分离的方法 |
CN107151736A (zh) * | 2017-06-21 | 2017-09-12 | 江苏省冶金设计院有限公司 | 一种制备脱铜铁水的***及方法 |
CN110793880A (zh) * | 2019-09-30 | 2020-02-14 | 鞍钢股份有限公司 | 一种冶金还原矿料过程模拟装置及方法 |
CN110565120B (zh) * | 2019-10-18 | 2021-09-07 | 东北大学 | 一种在含铜铁液中脱除并回收铜的方法 |
MX2023008678A (es) * | 2021-01-26 | 2023-08-02 | Nucor Corp | Metodo y sistema para reducir el contenido de metal no ferroso de la chatarra de acero. |
CN115369258A (zh) * | 2022-08-04 | 2022-11-22 | 江苏鑫瑞崚新材料科技有限公司 | 一种低银低硫超高纯铜提纯真空熔炼工艺 |
CN116287549A (zh) * | 2023-03-21 | 2023-06-23 | 武汉科技大学 | 真空处理低碳低硫钢同时脱除残留元素锡和锑的方法 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63192812A (ja) * | 1987-02-05 | 1988-08-10 | Sumitomo Metal Ind Ltd | 溶銑の脱Cu方法 |
JPH04198431A (ja) | 1990-11-29 | 1992-07-17 | Nippon Steel Corp | 鋼鉄中の銅の除去方法 |
JPH07316618A (ja) * | 1994-05-17 | 1995-12-05 | Nkk Corp | 溶融還元溶銑の予備精錬方法 |
JPH09143586A (ja) * | 1995-11-28 | 1997-06-03 | Ryokichi Shinpo | 溶鉄中の銅の除去方法 |
JP2007002305A (ja) * | 2005-06-24 | 2007-01-11 | Nippon Chutetsukan Kk | キュポラによる溶銑の溶製方法 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2403419A (en) * | 1943-04-15 | 1946-07-02 | Revere Copper & Brass Inc | Method of recovering the constituents of scrap bi-metal |
US2512578A (en) * | 1949-05-26 | 1950-06-20 | Jordan James Fernando | Method of desulfurizing and decopperizing ferrous metal |
SU1227689A1 (ru) * | 1984-07-03 | 1986-04-30 | Магнитогорский горно-металлургический институт им.Г.И.Носова | Способ удалени меди из расплава чугуна |
JPS61119612A (ja) * | 1984-11-14 | 1986-06-06 | Sumitomo Metal Ind Ltd | 溶鉄の脱銅及び/又は脱錫方法 |
JPS61266515A (ja) * | 1985-05-21 | 1986-11-26 | Masanori Tokuda | 含銅溶鉄より低銅鋼を製造する方法 |
US4925488A (en) * | 1987-07-30 | 1990-05-15 | Milton Blander | Removal of copper from ferrous scrap |
-
2009
- 2009-01-15 JP JP2009006297A patent/JP5402005B2/ja active Active
- 2009-03-03 KR KR1020137009853A patent/KR20130045955A/ko not_active Application Discontinuation
- 2009-03-03 EP EP20090717326 patent/EP2248916B1/en active Active
- 2009-03-03 US US12/920,741 patent/US20110000340A1/en not_active Abandoned
- 2009-03-03 BR BRPI0909687A patent/BRPI0909687A2/pt not_active Application Discontinuation
- 2009-03-03 WO PCT/JP2009/054370 patent/WO2009110627A1/ja active Application Filing
- 2009-03-03 KR KR1020107019379A patent/KR101276921B1/ko active IP Right Grant
- 2009-03-03 CA CA 2715322 patent/CA2715322C/en active Active
- 2009-03-03 MX MX2010009609A patent/MX2010009609A/es not_active Application Discontinuation
- 2009-03-03 CN CN200980107370.2A patent/CN101960023B/zh active Active
- 2009-03-05 TW TW98107087A patent/TWI409338B/zh active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63192812A (ja) * | 1987-02-05 | 1988-08-10 | Sumitomo Metal Ind Ltd | 溶銑の脱Cu方法 |
JPH04198431A (ja) | 1990-11-29 | 1992-07-17 | Nippon Steel Corp | 鋼鉄中の銅の除去方法 |
JPH07316618A (ja) * | 1994-05-17 | 1995-12-05 | Nkk Corp | 溶融還元溶銑の予備精錬方法 |
JPH09143586A (ja) * | 1995-11-28 | 1997-06-03 | Ryokichi Shinpo | 溶鉄中の銅の除去方法 |
JP2007002305A (ja) * | 2005-06-24 | 2007-01-11 | Nippon Chutetsukan Kk | キュポラによる溶銑の溶製方法 |
Non-Patent Citations (5)
Title |
---|
CHAOWANG, TETSU-TO-HAGANE, vol. 77, no. 4, 1991, pages 504 |
HIROKAZU SHIRAKAWA ET AL.: "Yoyu Flux ni yoru Yosen no Datsudo", JOURNAL OF THE IRON & STEEL INSTITUTE OF JAP, vol. 72, no. 12, September 1986 (1986-09-01), pages S961 * |
IMAI TADASHI, TETSU-TO-HAGANE, vol. 74, no. 4, 1988, pages 640 |
See also references of EP2248916A4 |
TADASHI IMAI ET AL.: "Na2S-kei Flux to Tanso Howa Yotetsu Kan no Do no Bunpai Heiko", JOURNAL OF THE IRON & STEEL INSTITUTE OF JAP, vol. 74, no. 4, April 1988 (1988-04-01), pages 640 - 647 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011084811A (ja) * | 2009-09-15 | 2011-04-28 | Jfe Steel Corp | 溶銑の製造方法 |
JP2011195887A (ja) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | 鋼屑中の銅の除去方法及び鋼屑を鉄源とした溶鋼の製造方法 |
JP2011195886A (ja) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | 鋼屑中の銅の除去方法 |
KR101462168B1 (ko) * | 2012-12-26 | 2014-11-14 | 주식회사 포스코 | 용철 처리장치 및 그 처리방법 |
Also Published As
Publication number | Publication date |
---|---|
TW200944594A (en) | 2009-11-01 |
US20110000340A1 (en) | 2011-01-06 |
CN101960023A (zh) | 2011-01-26 |
BRPI0909687A2 (pt) | 2015-09-22 |
EP2248916B1 (en) | 2013-10-30 |
KR101276921B1 (ko) | 2013-06-19 |
TWI409338B (zh) | 2013-09-21 |
EP2248916A4 (en) | 2011-01-05 |
JP5402005B2 (ja) | 2014-01-29 |
KR20100105794A (ko) | 2010-09-29 |
CN101960023B (zh) | 2014-06-18 |
CA2715322C (en) | 2013-01-15 |
MX2010009609A (es) | 2010-09-30 |
CA2715322A1 (en) | 2009-09-11 |
JP2010133002A (ja) | 2010-06-17 |
KR20130045955A (ko) | 2013-05-06 |
EP2248916A1 (en) | 2010-11-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5402005B2 (ja) | 鋼屑中の銅の除去方法 | |
JP5909957B2 (ja) | 鉄スクラップを利用した製鋼方法 | |
JP5589688B2 (ja) | 溶銑の製造方法 | |
JP5326590B2 (ja) | 溶銑からの銅及び硫黄の除去方法 | |
JP5625654B2 (ja) | 溶銑の製造方法 | |
JP5493335B2 (ja) | 溶銑の脱銅処理方法 | |
JP5707668B2 (ja) | 溶銑の脱銅処理方法 | |
JP5549198B2 (ja) | 鉄スクラップを利用した製鋼方法 | |
JP6065538B2 (ja) | 溶銑の脱銅処理方法 | |
JP3790414B2 (ja) | 溶銑の精錬方法 | |
JP5581759B2 (ja) | 鋼屑中の銅の除去方法 | |
JP4714655B2 (ja) | 含クロム溶鉄の脱硫方法 | |
JP5326591B2 (ja) | 鋼屑を鉄源とした溶銑の製造方法 | |
JP5581760B2 (ja) | 鋼屑中の銅の除去方法及び鋼屑を鉄源とした溶鋼の製造方法 | |
JP2021134386A (ja) | スラグ還元を伴った冷鉄源の溶解方法 | |
JP5365207B2 (ja) | 鋼屑を鉄源とした溶鋼の製造方法 | |
JP3233304B2 (ja) | Mn鉱石の溶融還元を伴った低Si・低S・高Mn溶銑の製造 | |
JP2011208172A (ja) | 鉄スクラップを鉄源として利用した転炉脱炭精錬方法 | |
SU1027227A1 (ru) | Способ производства стали | |
JP2005200762A (ja) | 溶銑の脱硫方法 | |
JP2018035404A (ja) | 鋳鉄の精錬方法 | |
JP2008214711A (ja) | 含クロム溶鉄の脱硫方法 | |
JP2006097137A (ja) | 溶銑の予備処理方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200980107370.2 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 09717326 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2715322 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 3027/KOLNP/2010 Country of ref document: IN |
|
ENP | Entry into the national phase |
Ref document number: 20107019379 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2009717326 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 12920741 Country of ref document: US Ref document number: MX/A/2010/009609 Country of ref document: MX |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: PI0909687 Country of ref document: BR Kind code of ref document: A2 Effective date: 20100903 |