Patent Application
20240002974
The present disclosure relates to a reduction method for a high-melting-point metal oxide, and specifically, to a reduction method and system for a metal oxide in which an operation is enabled in an atmosphere without using an existing production process in an inert gas atmosphere and the efficiency thereof can be maximized and the easy commercialization thereof is provided using an eco-friendly method.
When a metal typically known in the art is referred to as any metal “M”, the metal M may be obtained by reducing a raw material such as an oxide or halide. Among the methods for producing the desired metal M, the relatively well-known and most widely used method in the art is a so-called Kroll process.
Typically, the Kroll process may be summarized as a process in which molten magnesium is used as a reducing agent and a chloride of the desired metal M, such as titanium chloride or zirconium chloride, is input thereto to reduce titanium or zirconium. In this regard, more details of the Kroll process may be found in U.S. Pat. No. 5,035,404.
Since this Kroll process is a process using chloride as a raw material, chlorine gas and magnesium chloride are produced as by-products during the process. Among these by-products, the chlorine gas is regarded as a representative matter of the Kroll process as an environmental matter that causes fatal matters to the a human body, and in the case of magnesium chloride, it causes a matter in the process of quickly corroding a reaction vessel, which is called an cell, a melting furnace, or a crucible.
As such, the Kroll process requires an additional device to resolve environmentally acceptable regulations, and is accompanied by frequent replacement of the reaction vessel, resulting in high cost for operating the process.
On the other hand, in the Kroll process, the obtained metal is produced in the form of a sponge including a large number of pores, so that it is very difficult to control oxygen that may present in the metal. In other words, the Kroll process has limitations in obtaining high-purity metals.
An electrolytic refining process is being researched to replace these existing processes, the process has the advantage of being simpler than an existing process without generating chlorine gas by directly reducing the metal oxide, but has a matter in that the form of recovered metal is limited to powder and a particle size of the powder is also limited, making it difficult to control an oxygen concentration in the metal after the process. In order to overcome this, although the specific surface area of the recovered metal must be lowered by producing an ingot using a process such as vacuum arc melting while the recovered metal powder produced by a refining process is not exposed to the atmosphere, in this case, large-scale industrial facilities are difficult and realistic difficulties are present in terms of cost.
On the other hand, the present inventors proposed that, a liquid copper-aided electrolysis (LCE) process (see Patent Documents 1 to 3) to solve the matters of the preceding process involves a method of producing a target metal as an alloy through an electrolytic reduction process using a reducing agent, and then refining a high-purity target metal through electrolytic refining. However, even in this electrolytic reduction process, a chlorine-based flux with a high volatilization rate is used, causing rapid corrosion of equipment and matters in terms of cost, and generation of chlorine gas, which requires operation in a closed system in an argon gas atmosphere.
(Non-Patent Document 1) Antoine Allanore, Journal of The Electrochemical Society, 162 (1) (2015) E13-E22
The present disclosure has been proposed to solve the matters of the prior art as described above, and the present disclosure is for the purposed of reducing a high-melting point metal oxide in an environmentally friendly and highly-efficient atmospheric environment using a fluoride-based flux to produce a high-grade alloy metal. The present disclosure is for the purpose of providing a method and system for doing so.
The present disclosure is characterized by producing a liquid metal alloy of metal M1 and metal M2 forming an eutectic phase with each other. Since a melting point of metal M1 is lowered by a eutectic reaction, reduction may be effectively performed at a relatively low temperature, which may significantly save energy and lead to cost reduction. In addition, the present disclosure is obtained in a liquid alloy state (liquid metal alloy of M1 and M2) by the eutectic reaction, so that the metal alloy itself may be used as a final product. In addition, the metal M1 may be obtained by electrorefining of the obtained metal alloy. The liquid alloy thus obtained may be thoroughly separated from an environment in which oxygen may present, and thus contamination by oxygen may be significantly prevented. That is, it is possible to obtain a high-purity metal alloy and metal M1 according to the above aspects.
The present disclosure is directed to providing an alloy metal reduction method that may increase a high-grade production rate of final products compared to the related art and has high energy efficiency and is advantageous for commercialization.
According to the present disclosure, a method of reducing metal M1 from a metal oxide is provided.
According to the present disclosure, the method of reducing the metal M1 from the metal oxide includes:
In the method of reducing the metal M1 from the metal oxide, the molten salt of the fluoride-based flux may be smaller than a density of the eutectic composition of the metal M2 and the metal M3 and the metal oxide.
According to the present disclosure, a molten salt of the fluoride-based flux has a volatilization rate of 10% by weight or less, specifically 5% by weight or less, and more specifically 2% by weight or less for 10 hours at 1,600 ° C.
According to the present disclosure, the fluoride-based flux may be one or more selected from the group consisting of MgF2, CaF2, SrF2, and BaF2, and specifically may be CaF2.
According to the present disclosure, the metal M1 may be one or more selected from the group consisting of Ti, Zr, Hf, W, Fe, Ni, Zn, Co, Mn, Cr, Ta, Ga, Nb, Sn, Ag, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Ac, Th, Pa, U, Np, Pu, Am, Cm, Bk, Cf, Es, Fm, Md, and No.
According to the present disclosure, the metal M2 may be one or more selected from the group consisting of Cu, Ni, Sn, Zn, Pb, Bi, Cd, and alloys thereof, and specifically may be Cu.
According to the present disclosure, the metal M3 may be one or more selected from the group consisting of Ca, Mg, Al, and alloys thereof, and specifically may be Mg.
According to the present disclosure, the metal oxide may include one or more selected from the group consisting of M1xOz and M1xM3yOz, where x and y are real numbers of 1 to 3, respectively, and z is a real number of 1 to 4.
According to the present disclosure, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed in air or in fluoride.
According to the present disclosure, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed in a range of 900 to 1,600° C.
According to the present disclosure, a method of reducing the metal M1 from the metal oxide may further include forming slags of the molten salt and a by-product generated in a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition by adding a slag-forming additive, and specifically the slag-forming additive may include one or more selected from the group consisting of MgO, CaO, FeO, BaO, SiO2, and Al2O3.
According to the present disclosure, the method includes: forming a layer in which the liquid metal alloy is positioned at a bottom of the cell and separated from the eutectic composition, and continuously obtaining the liquid metal alloy through a lower portion of the cell; and
According to the present disclosure, the method may further include electrorefining the liquid metal alloy to produce the metal M1.
A metal alloy or metal according to the present disclosure may be one obtained by any method disclosed herein or a combination thereof, and may be a metal alloy having a residual content of 0.1% by weight or less, specifically 0.01% by weight or less, and more specifically 0.001% by weight or less, and an oxygen content of 1,800 ppm or less, specifically 1,500 ppm or less, and more specifically 1,200 ppm or less.
A system for reducing metal M1 from a metal oxide according to the present disclosure may include:
The present disclosure provides a system optimized for obtaining the desired metal from a metal oxide without using a metal chloride or chloride at all as a flux, and a method for producing this metal. Therefore, the present disclosure may solve the above-mentioned environmental matters of a Kroll process and cost matters due to corrosion of a cell.
The present disclosure is characterized by producing a liquid metal alloy of metal M1 and metal M2 forming an eutectic phase with each other. Since a melting point of metal M1 is lowered by a eutectic reaction, reduction may be effectively performed at a relatively low temperature, which may significantly save energy and lead to cost reduction.
The present disclosure is obtained in a liquid alloy state (liquid metal alloy of metal M1 and metal M2) by the eutectic reaction, so that the metal alloy itself may be used as a final product. In addition, the metal M1 may be obtained by electrorefining of the obtained metal alloy. The liquid alloy thus obtained may be thoroughly separated from an environment in which oxygen may present, and thus contamination by oxygen may be significantly prevented. That is, it is possible to obtain a high-purity metal alloy and metal M1 according to the above aspects.
In addition, according to the present disclosure, it is easy to adjust the ratio of the target alloy, and a high-purity metal may be produced through an electrorefining technique using a finally produced alloy metal.
In the present disclosure, a recovery rate of high-grade metal M1 is high, and the separation of a final product and a reaction product is easy, so that continuous operation is possible.
Hereinafter, the intention, operation, and effect of the present disclosure will be described in detail through the embodiments of the present disclosure and specific descriptions, and examples to aid understanding and practice thereof, However, the following description and embodiments are presented as examples to aid understanding of the present disclosure as described above, and the scope of the invention disclosure is not limited or limited thereto.
Prior to the detailed description of the present disclosure, the terms or words used in the specification and claims should not be interpreted as limiting in a sense in the related art or a preliminary sense, and the inventor should be interpreted in a sense and a concept that are consistent with the technical concept of the present disclosure given the principle that the concepts of the terms may be appropriately defined in order to explain its own invention in its best mode.
Accordingly, it should be understood that the configuration of the embodiments described herein are only preferred embodiments of the present disclosure and are not intended to vary all of the spirit of the invention, and that there may be various equivalents and modifications that may be substituted for them at the time of this application.
In this specification, the singular expression includes the plural expression unless the context clearly dictates otherwise. In this specification, the terms “comprises,” “includes,” or “has” and the like are intended to designate the presence of the features, numbers, steps, components, or combinations thereof that are implemented, and are not to be understood as precluding the possibility of the presence or addition of one or more other features or numbers, steps, components or combinations thereof.
As used herein, the term “loading” may be used interchangeably with “put”, “introduction”, “inflow”, and “injection” in this specification, and may be understood to mean bringing or putting any material, such as a raw material, into a place where it is needed.
Hereinafter, the present disclosure will be described in detail in the order of reduction method of metal M1, a reduction system, and examples.
A method of reducing metal M1 from a metal oxide according to the present disclosure may include:
In the method of the present disclosure, the molten salt of the fluoride-based flux may be smaller than a density of the eutectic composition of the metal M2 and the metal M3 and the metal oxide.
In the method of the present disclosure, a molten salt of the fluoride-based flux has a volatilization rate of 10% by weight or less, specifically 5% by weight or less, and more specifically 2% by weight or less for 10 hours at 1,600° C.
By using the molten salt of the fluoride-based flux, there is an environmental advantage in that toxic chlorine gas is not generated, and since its volatilization rate is low, loss of the flux during the process is small, and it is advantageous in terns of maintenance cost. In particular, when compared with a chloride-based flux, such as CaCl2, which has a volatilization rate of about 74% by weight (
In the method of the present disclosure, the fluoride-based flux may be a fluoride-based flux of one or more metals selected from the group of alkali metals and alkaline earth metals, and determined by considering the relative density difference, a volatilization rate, convenience and safety of operation, and the like according to the target metal M1 and the reducing agent used. The fluoride-based flux may, for example, be one or more selected from the group consisting of MgF2, CaF2, SrF2, and BaF2, and specifically may be CaF2.
In the method of the present disclosure, by using an eutectic composition of metal M2 and metal M3 and a fluoride-based flux molten salt having a density lower than that of the metal oxide, In the step in which the metal oxide reacts with the eutectic composition to reduce the metal M1 and form a liquid metal alloy between the reduced metal M1 and the metal M2, and since the molten salt of the fluoride-based flux is positioned at the top of the cell, the eutectic composition and the metal oxide may not be exposed to an external environment, and inflow of oxygen from the outside may be prevented. Accordingly, a reduction process of the metal M1 is possible even in a normal air atmosphere other than an inert gas atmosphere.
In addition, by using a fluoride-based flux with a low volatilization rate, it is advantageous for large-scale industrialization because it allows harmful gases to be disloaded in an acceptable amount even in a normal air atmosphere, thereby increasing the convenience and safety of operation, and significantly lowering a degree of corrosion of equipment than used fluxes in the related art.
The metal M1 is not particularly limited, but specifically may be one selected from the group consisting of Ti, Zr, Hf, W, Fe, Ni, Zn, Co, Mn, Cr, Ta, Ga, Nb, Sn, Ag, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Ac, Th, Pa, U, Np, Pu, Am, Cm, Bk, Cf, Es, Fm, Md, and No, more specifically, one selected from the group consisting of Ti, Zr, W, Fe, Ni, Zn, Co, Mn, Cr, Ta, Er, and No, and even more specifically, one selected from the group consisting of Ti, Zr, W, Fe, Ni, Zn, Co, Mn, and Cr, and in particular, Ti, Zr, or W.
In the method of the present disclosure, the metal M2 is not limited as long as it may form an eutectic phase with the metal M1, for example, the metal M2 may be one or more selected from the group consisting of Cu, Ni, Sn, Zn, Pb, Bi, Cd, and alloys thereof, and specifically, Cu.
In the method of the present disclosure, a reducing agent including the metal M3 is not limited as long as it may reduce the metal oxide including the metal M1, for example, the metal M3 may be one or more selected from the group consisting of Ca, Mg, Al, and alloys thereof. Specifically, the metal M3 may be Mg.
In the method of the present disclosure, the metal oxide may include one or more selected from the group consisting of M1xOz and M1xM3yOz, where x and y are real numbers of 1 to 3, respectively, and z is a real number of 1 to 4.
Non-limiting examples of the above metal oxides for ease of understanding may include one selected from the group consisting of ZrO2, TiO2, MgTiO3, HfO2, Nb2O5, Dy2O3, Tb4O7, WO3, Co3O4, MnO, Cr2O3, MgO, CaO, Al2O3, Ta2O5, Ga2O3, Pb3O4, SnO, NbO, and Ag2O, or a combination of two or more of these.
When a composite oxide (M1xM3yOz) of the metal M1 and the metal M3 is used as the metal oxide, a process of reducing the metal M1 by reacting with the eutectic composition of the metal M2 and the metal M3 may be faster. According to the findings of the present disclosure, in the case of using the complex oxide (M1xM3yOz), the time required for reduction may be reduced by at least ⅓ to 1/10 compared to the case of using M1xOz . That is, when the composite oxide of the metal M1 and the metal M3 is used as the metal oxide, a reaction rate between the metal oxide and the eutectic composition may be faster than when only the oxide of the metal M1 is used. In addition, in the case of using M1xM3yOz, there is an advantage in that a ratio of M1 and M2 in the liquid metal alloy produced according to the present disclosure may be more widely adjusted. Moreover, when M1xM3yOz is used, a required amount of M3 used as a reducing agent is significantly reduced compared to the case of using M1xOz . For example, when Ti is used as the metal M1 and Ca is used as the metal M3. oxide of the metal M1 may be TiO2, and the composite oxide of the metal M1 and the metal M3 may be CaTiO3.
Unlike the Kroll process in the related art, the method according to the present disclosure is different in that it uses a metal oxide instead of a metal chloride as a raw material. A raw material usually found in nature includes an oxide of the metal M1, and a pre-treatment process of substituting the metal oxide with a chloride is involved in order to use the oxide in the Kroll process. When such a pre-treatment process is performed, it itself causes an increase in process cost. Moreover, hydrochloric acid is used in the pre-treatment process of replacing metal oxide with chloride, and this process promotes corrosion of manufacturing equipment due to strong acidity, and toxic chlorine gas may be generated during the process, which may cause environmental matters. Since the method according to the present disclosure does not require a pre-treatment process for substituting the metal oxide with chloride, process cost is lower than that of the Kroll process and there are advantages in not causing environmental matters.
In the method of the present disclosure, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed in air or in fluoride. Since a density of the molten salt of the fluoride-based flux is lower than that of the eutectic composition and the metal oxide, the molten salt of the fluoride-based flux is positioned at the top of the cell, and the eutectic composition and the input metal oxide are positioned below the molten salt of the fluoride-based flux. Due to this, since the eutectic composition and the introduced metal oxide can present in a state that is not exposed to an external environment due to the molten salt of the fluoride-based flux and the cell, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed even in a normal atmosphere other than an inert gas atmosphere. Moreover, since a volatilization rate of the molten salt of the fluoride-based flux is relatively low, even when the process is performed in an atmospheric atmosphere, the generation of toxic gases is reduced, and the corrosion of equipment used in the process is significantly reduced, a harmful environment is not created for operators, and large-scale industrialization can be achieved.
In the method of the present disclosure, a method of reducing the metal M1 may be performed at least a temperature at which the fluoride-based flux can be melted, the eutectic composition can be produced, and a process of reducing metal M1 by reacting the metal oxide with the eutectic composition can be performed. For example, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed at 900° C. or more. In addition, he method can be performed at a temperature below which the molten salt of the fluoride-based flux does not evaporate excessively, and considering the energy efficiency according to the heating of the furnace, the method may be performed at 1800° C. or less, 1700° C. or less, 1600° C. or less, or 1600° C. or less. Accordingly, a process of reducing the metal M1 by reacting the metal oxide with the eutectic composition may be performed in the range of 900 to 1600° C.
As an example, when the metal M1 is Ti, the metal oxide (M1xOz ) is TiO2, the metal M2 is Cu, and the metal M3 is Ca, the metal Ti is reduced according to the following Scheme 1-1 and Scheme 1-2, and a metal M3 oxide (M3aOb) can then be separated while the liquid metal alloy CuTi is obtained. Here, a and b are a real number from 1 to 3, respectively.
2Ca+TiO2->Ti+2CaO [Scheme 1-1]
Ti+Cu+2CaO->CuTi (Alloy)+2CaO (separation) [Scheme 1-2]
As another example, when the metal M1 is Ti, the metal oxide (M1xM3yOz) is CaTiO3, the metal M2 is Cu, and the metal M3 is Ca, the metal Ti is reduced according to the following Scheme 1-1 and Scheme 1-2, and a metal M3 oxide (M3aOb) can then be separated while the liquid metal alloy CuTi is obtained.
2Ca+CaTiO3->Ti+3CaO [Scheme 2-1]
Ti+Cu+3CaO->CuTi (alloy)+3CaO (separation) [Scheme 2-2]
The metal M3 oxide (M3aOb) produced according to the above reaction is a kind of by-product, and it is necessary to continuously remove the by-products in order to enable a continuous process. The by-products may not be completely soluble in the molten salt and it may not be easy to remove the by-products or run the process continuously. The method of the present disclosure may further include forming slags of by-products generated in the process of reducing the metal M1 by reacting the metal oxide with the eutectic composition and the molten salt of the fluoride-based flux by putting a slag-forming additive. When slags are formed, viscosity is relatively reduced compared to the case where by-products and the molten salt of the fluoride-based flux are present, fluidity is increased, continuous removal of slags including by-products is possible, and furthermore, a continuous process can be made possible.
Examples of the slag-forming additive to achieve the above effect may include one or more selected from the group consisting of MgO, CaO, FeO, BaO, SiO2, and Al2O3, but are not limited thereto.
A method of reducing metal M1 from a metal oxide according to the present disclosure may further include forming a layer in which the liquid metal alloy is positioned at a bottom of the cell and separated from the eutectic composition, and continuously obtaining the liquid metal alloy through a lower portion of the cell; and forming a distinct layer on top of the eutectic composition using the slags, and continuously removing the slags through a top of the cell. By forming a layer in which the liquid metal alloy is positioned at a bottom of the cell and separated from the eutectic composition, a liquid metal alloy may be continuously tapped from a lower portion of the cell. In addition, input of the slag-forming additive causes the slag to form as a distinct layer on an upper portion of the eutectic composition, and the slag is continuously removed through the upper portion of the cell, so that by-products generated in the reduction process of metal oxides can be continuously removed. Accordingly, by continuously removing the reaction product formed when the metal oxide is input to the eutectic composition from the cell, after inputting an amount of the metal oxide, the liquid metal alloy of the metal M1 and the metal M2 may be obtained without interruption of the process by continuously inputting the metal oxide rather than all reactions being terminated. At this time, a method known to those skilled in the art may be used for continuously obtaining a liquid metal alloy through the lower portion of the cell or continuously removing slags through the upper portion of the cell.
After the slags are removed through removing the slags and the fluoride-based flux through the upper portion of the cell, the fluoride-based flux is supplemented during a process operation to maintain the balance of a reaction system and enable a continuous process. At this time, the fluoride-based flux may be continuously separated from the removed slags, and the separated fluoride-based flux may be input into the cell again.
Cooling for solidification of the obtained liquid metal alloy may be performed. Since the liquid metal alloy is in a state in which the metal M1 and the metal M2 are homogeneously mixed, the structure of the alloy obtained after solidification is greatly affected by a cooling rate of the liquid metal alloy. The cooling rate can stably form an intermetallic compound phase, in the temperature range in which the process according to the present disclosure is performed, it may be slowly cooled to room temperature at a rate of 20° C./min, so that a tissue structure in which the intermetallic compound phases of M1 and M2 are continuously connected to each other can be produced. When the cooling rate is excessively fast outside a suggested range, a structure in which a large amount of fine intermetallic compound particles are dispersed and incorporated into the metal M1 matrix is obtained, and thus there is a risk that a continuous and rapid mass transfer path of metal M1 may not be formed. When the cooling is excessively slow, the microstructural benefit is negligible, but as the time required for the process becomes excessively long, the cooling rate may be substantially 1° C./min or more, and more substantially 5° C./min or more.
The method according to the present disclosure may further include obtaining an alloy including the metal M1 and the metal M2, and then electrolytically refining the obtained alloy including the metal M1 and the metal M2 to obtain the metal M1.
Obtaining the metal M1 by performing the electrorefining may be solidifying the obtained liquid metal alloy to obtain a solid alloy, electrolytically refining the solid alloy, and recovering the metal M1 from the alloy.
In some cases, prior to electrorefining the solidified alloy, the flux that may remain in the liquid metal alloy may be removed, this can be achieved, for example, by heat treating the liquid metal alloy in a vacuum or inert gas atmosphere to cause the flux to distill off A distillation temperature (heat treatment temperature) is not particularly limited as long as the temperature is higher than a boiling point of the flux used in the system of the present disclosure, for example, the temperature may be 2,500° C. or more, and reduced pressure may be performed to lower the distillation temperature and increase efficiency. In order to effectively prevent the liquid metal alloy from being oxidized again, it may be advantageous to perform the distillation in a vacuum atmosphere and under an inert gas.
The present disclosure provides a metal alloy of the metal M1 and the metal M2 obtained by any method or combination thereof described in the specification of the present disclosure. For example, the metal alloy of the metal M1 and the metal M2 can be obtained by a method of reducing metal M1 from a metal oxide, including: forming a molten salt of a fluoride-based flux in an cell; putting, into the cell, a reducing agent including a metal M2 forming an eutectic phase with the metal M1, and a metal M3 to produce an eutectic composition of the metal M2 and the metal M3; and reducing the metal M1 by reacting the metal oxide with the eutectic composition and forming a liquid metal alloy with the reduced metal M1 and M2. For example, the metal alloy of the metal M1 and the metal M2 may be made in an atmosphere or obtained from a process performed in a range of 900 to 1600° C. For example, the metal alloy of the metal M1 and the metal M2 may be obtained by a method including forming slags of the molten salt and a by-product generated in a process of reducing the metal M1 by adding a slag-forming additive to react the metal oxide with the eutectic composition. In addition, the metal alloy of the metal M1 and the metal M2 of the present disclosure may be obtained by any method or a combination thereof described in the specification of the present disclosure.
In one embodiment, the metal alloy of the metal M1 and the metal M2 is a high-grade metal alloy with a residual content of 0.1% by weight or less, specifically 0.01% by weight or less, and more specifically 0.001% by weight or less, based on a total weight of the metal alloy. In addition, the metal alloy of the metal M1 and the metal M2 is a high-grade metal alloy with an oxygen content of 1,800 ppm or less, specifically 1,500 ppm or less, and more specifically 1,200 ppm or less.
In addition, in a liquid alloy (M1 and M2 are liquid metal alloys) obtained according to the method of the present disclosure, the metal alloy itself may be used as a final product. M1 is often used industrially in the form of an alloy, and when M1 can be produced with only a single metal, as in the Kroll process in the related art, a post-processing process for forming an alloy with another metal may be required. However, the present disclosure has high process efficiency in that a final product may be obtained in the form of a metal alloy of M1 and M2 simultaneously with reduction without such a post-treatment process. Moreover, the reduced metal produced through the Kroll process in the related art has a low production of high grade (grade 1) metal having a low oxygen content and a relatively high residual oxygen content. Therefore, even when a metal alloy is produced using the reduced metal produced by the Kroll process, there is a limit in that the residual oxygen content is high. On the other hand, most of the metal alloys produced according to the present disclosure have a very low oxygen content and are of high quality grade. For example, when M1 is Ti, the method according to the present disclosure yields a high-grade metal as high as 98% or more, but it is known that the crawl process in the related art yields less than 50% of high-grade metal, and through this, superiority of the present disclosure can be more clearly understood.
A system for reducing metal M1 from a metal oxide according to the present disclosure may include:
In one embodiment, the cell may be an electrolytic reduction cell or the like, a high-frequency melting furnace may be used to achieve a desired temperature range, or an electric furnace may be used depending on a target metal alloy, but is not limited thereto. Considering a reaction temperature range, reactivity, and the like, all cells and furnaces that are easy for a person skilled in the art may be used.
In one embodiment, a mass ratio of the molten salt of the fluoride-based flux to the reaction by-product may be 5:1 to 2:1, preferably 3:1, but is not limited thereto, for smooth separation of the liquid metal alloy and the reaction by-product.
In one embodiment, the flux may further include an oxide of one or two or more metals selected from an alkali metal and an alkaline earth metal group as a reactive additive. A content of the reactive additive may be 0.1 to 25% by weight based on a total weight of the flux. The reactive additive may include, but are not limited to, LiO, NaO, SrO, CsO, KO, CaO, BaO, or mixtures thereof. The reactive additive contained in the flux may enable easier reduction of a metal oxide contained in a raw material module.
In one embodiment, a cell similar to that of
Hereinafter, examples will be described in detail, through which the action and effect of the present disclosure will be demonstrated. However, the following examples are only presented as examples of the invention disclosure, and the scope of the invention disclosure is not determined thereby.
A system as shown in
52.8 g and 72.3 g of Cu(s) and Ca(s) were weighed, input into an cell, and melted to produce an eutectic composition (
72.1 g of TiO2 (average particle size of 100 μm) as a metal oxide was weighed and reacted for 10 hours (
In order to remove by-products, 200 g of Al2O3 powder and 100 g of CaO as slag-forming additives were input to slags (
A system as shown in
60 g and 65.5 g of Cu(s) and Ca(s) were weighed, input into a cell, and melted to produce an eutectic composition (
111 g of CaTiO3 as a metal oxide was weighed and reacted for 2 hours (
In order to remove by-products, 200 g of Al2O3 powder and 100 g of CaO as slag-forming additives were input to slags (
A volatilization rate of a fluoride-based flux and a chloride-based flux were measured. 500 g of each flux (weight before loading) was weighed and input into a crucible, and weight (weight after loading) of the flux after loading the crucible to a melting furnace and leaving the flux at 1,600° C. for 10 hours was measured. The volatilization rate was evaluated using the following method.
Volatilization rate: (weight before loading−weight after loading)/(weight before loading)×100%
As a result, it was confirmed that CaF2 used as the fluoride-based flux showed a low volatilization rate of 1.8% by weight, but CaCl2, a chloride-based flux, showed a high volatilization rate of about 74% by weight (
Regarding a volatilization rate of CaF2, a fluoride-based flux, and a volatilization rate of CaCl2, a chloride-based flux, measured in each temperature range, it may be seen that a vapor pressure of the fluoride-based flux is remarkably low based on a process temperature at which this process is performed (
From this, it is preferable to use a fluoride-based flux having a low volatilization rate for an efficient process as described above.
The properties of the alloys obtained in Examples 1 and 2 were evaluated using the following method.
Recovery rate: 100−{(1st weight−2nd weight)/2nd weight×100%}
From the results of Table 1, it may be seen that the alloys of Examples produced according to the present disclosure showed a high recovery rate, and that a high-purity alloy was obtained that was substantially free of metal or oxygen used as a reducing agent. That is, it was confirmed that, unlike a presenting process, which was possible only in an inert gas atmosphere as above, even though the process proceeded in an air atmosphere, the recovery rate of the target metal was better and the oxygen content was significantly lower.
Although the present disclosure has been described with reference to embodiments, those skilled in the art will be able to make various applications and modifications within the scope of the present disclosure based on the above information.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2020-0154083 | Nov 2020 | KR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2021/003849 | 3/29/2021 | WO |
