Patent Application
20230272504
The present invention relates to a molten metal mixing system in which a 1st melt raw material is melted in a 1st melting apparatus to produce a 1st molten metal, whereas a 2nd melt raw material is melted in a 2nd melting apparatus to produce a 2nd molten metal, and then the 1st and 2nd molten metals are mixed.
Iron has hitherto been a common material for molten metal. Recently, however, vehicles have been under body weight saving for the purpose of improved fuel efficiency, and the rate of non-ferrous metals having relatively lower specific gravities, such as aluminum materials and aluminum alloy materials, used in vehicle bodies has been growing. This leads to increasing resource value of non-ferrous metals, and increasing concerns for effective use of such precious non-ferrous metals. Based on such concerns, a method is demanded of mixing used non-ferrous metals to fresh non-ferrous metals (fresh material) to reduce the amount of fresh non-ferrous metals to be used.
The used non-ferrous metals as mentioned above may include, for example, scrap materials, such as return scrap, briquette material, and machining chips. Among the scrap materials, return scrap, which may be, for example, unnecessary portions generated during casting or during processing following casting of non-ferrous metals, followed by pulverization in a pulverizer, has properties similar to those of fresh material, and is thus convenient for melting with fresh material into molten metal. Briquette material may be, for example, cutting wastes, machining chips, and the like, generated in processing non-ferrous metals and compressed into lumps.
As such, there are a wide variety of used non-ferrous metals, among which some are easy to recycle while some others are difficult to recycle. Specifically, return scrap is relatively easy to recycle as discussed above, while briquette material and machining chips tend to be difficult to recycle. The reasons are as follows.
In general, briquette material, which is made by compressing cutting wastes, machining chips, and the like, generated in processing non-ferrous metals, into lumps as discussed above, contains oil and water, and thus cannot be made into molten metal of high quality, if melted as it is. Accordingly, for recycling, briquette material is preferably pretreated by drying or otherwise for removing oil and water contained therein through evaporation, but is yet hard to be melted into molten metal in the manner similar to that for fresh material. Further, briquette material has a lower specific gravity and a larger surface area, and thus easily floats on the surface of the molten metal and is partly prone to oxidization during melting.
Similarly, machining chips also have a lower specific gravity and a larger surface area, and thus easily float on the surface of the molten metal and are partly prone to oxidization during melting. For example, aluminum materials and aluminum alloys easily turn into oxides, like aluminum oxide (Al2O3). In particular, having a larger surface area, machining chips tend to have more oxide per unit weight. This results in the entire machining chips including the oxides to have an elevated melting point by the impact of the oxides, and become hard to melt. For example, aluminum oxide has a melting point of 2072° C., and is thus very hard to melt.
As such, briquette material and machining chips, having the properties discussed above, tend to be hard to recycle as resources.
Here, a prior art publication related to the present invention is presented. Specifically, prior art related to the present invention includes, e.g., Patent Publication 1 to be mentioned below. The invention disclosed in Patent Publication 1 is use of a connecting pipe having a siphon effect, in transferring molten metal in a melt holding furnace for feeding, into a melt holding furnace for casting.
Patent Publication 1, however, merely discloses transfer of molten metal in a holding furnace into another, adjacent holding furnace, rather than a system for mixing two or more series of molten metal.
Patent Publication 1: JP 5237752 B
For recycling oxidizable briquette material or machining chips as discussed above, machining aluminum chips, for example, contaminated with water or oil, e.g., cutting oil, are first subjected to removal of water or dissolution of oil in a cleaning solution, or to calcination in a rotary kiln without oxidizing aluminum to evaporate oil or water. After that, the machining chips are introduced into a melting furnace to produce aluminum molten metal. Alternatively, machining chips may be made into briquette material without removing oil and water therefrom, and the resulting briquette material is dried after recovery of cutting oil therefrom. After that, the dried briquette material is introduced into a melting furnace to produce aluminum molten metal. Further, it is relatively common to mix this aluminum molten metal with a separate molten metal of fresh aluminum material, aluminum alloy material, or the like, or with a separate molten metal of fresh aluminum material, aluminum alloy material, or the like and return scrap thereof. Such a molten metal of briquette material or machining chips melted in a separate step is often transferred manually from a melting furnace to a holding furnace using a pail or a ladle.
During transfer of the molten metal or upon pouring the melt into a holding furnace, the molten metal is brought into contact with air and oxidized. As a result, the molten metal being transferred may be contaminated with the oxides, which disadvantageously degrades the quality of the molten metal.
For mixing a molten metal of used non-ferrous metals (briquette material or machining chips) with a molten metal of fresh non-ferrous metals (fresh material), or mixing a molten metal of used non-ferrous metals (briquette material or machining chips) with a molten metal of fresh non-ferrous metals (fresh material) and return scrap thereof, it is required to introduce the non-ferrous metals and the return scrap into a melting furnace at predetermined weights. For example, assume that 150 kg per hour of a molten metal of used non-ferrous metals (briquette material or machining chips) and 150 kg per hour of a molten metal of fresh non-ferrous metals (fresh material), i.e., a total of 300 kg per hour of molten metal, is required. This requires that 150 kg per hour of used non-ferrous metals (briquet material or machining chips) in the form of solid feedstock and 150 kg per hour of fresh non-ferrous metals (fresh material) in the form of solid feedstock be introduced into a melting furnace equipped with melting devices, such as burners or heaters. Even when flame from the melting devices, such as burners or heaters, is uniformly brought into direct contact with each type of the non-ferrous metals, the melting rate differs between the used non-ferrous metals (briquette material or machining chips) and the fresh non-ferrous metals (fresh material). In addition, in a tower-type melting furnace, the melting rate also differs between the non-ferrous metals in direct contact with the flame from the melting devices, such as burners or heaters, and those not in direct contact therewith. This is because the machining chips tend to burn instantaneously upon direct contact with the flame, resulting in oxides rather than melting, whereas the briquette material in direct contact with the flame tends to convert into oxides rather than melting. On the other hand, the return scrap, as discussed above, has properties similar to those of fresh material, and is thus convenient for melting with fresh material into molten metal, where the melting rate of the return scrap may be taken as approximating that of the fresh non-ferrous metals (fresh material). In this way, introduction of the solid feedstock not only causes difference in melting rate to result in inhomogeneous and uneven molten metal, but also causes possible failure to achieve the predetermined weight proportions (in the above-mentioned case, molten metal weight of used non-ferrous metals (briquette material or machining chips):molten metal weight of fresh non-ferrous metals (fresh material)=150 kg:150 kg=1:1).
Moreover, in mixing a molten metal of used non-ferrous metals (briquette material or machining chips) and a molten metal of fresh non-ferrous metals (fresh material), or mixing a molten metal of used non-ferrous metals (briquette material or machining chips) and a molten metal of fresh no-ferrous metals (fresh material) and return scrap thereof, the timing of introduction differs between the molten metals. As such, it is realistically difficult to achieve the desired mixing ratio (weight proportions) between the molten metal amount of the used non-ferrous metals (briquette material or machining chips) and a molten metal amount of the fresh non-ferrous metals (fresh material), or to achieve the desired mixing ratio (weight proportions) between the molten metal amount of the used non-ferrous metals (briquette material or machining chips) and a molten metal amount of the fresh non-ferrous metals (fresh material) and return scrap thereof, as the melting rate differs between the used non-ferrous metals (briquette material or machining chips) and the fresh non-ferrous metals (fresh material) and return scrap thereof, as mentioned above. For example, for mixing an amount of molten metal of the used non-ferrous metals (briquette material or machining chips) and an amount of molten metal of the fresh non-ferrous metals (fresh material) at a predetermined mixing ratio (weight proportions), in some conventional cases, the amount of molten metal of the fresh non-ferrous metals (fresh material), which has a higher melting rate, was first introduced at the predetermined mixing proportion (weight proportion), and then the amount of molten metal of the used non-ferrous metals (briquette material or machining chips), which has a lower melting rate and melts at a lower rate compared to the fresh non-ferrous metals (fresh material), was introduced at the predetermined mixing proportion (weight proportion). Such mixing by introductions at different timings tends to result in mainly a molten metal of higher quality being first transferred to the holding furnace, as the fresh non-ferrous metals (fresh material) and the return scrap thereof having a higher melting rate melt faster. After that, the molten metal resulting from melting of the used non-ferrous metals (briquette material or machining chips) having a lower melting rate is mixed, so that a molten metal of lower quality is transferred to the holding furnace. This results in that the molten metal first transferred to the holding furnace is processed in the subsequent casting process into products of higher quality (strength or the like), whereas the molten metal later transferred to the holding furnace and contaminated with the molten metal resulting from melting of the used non-ferrous metals (briquette material or machining chips) is processed in the subsequent casting process into products of probably lower quality (strength or the like). In this way, not only the quality characteristics of the molten metals, but also the quality (strength or the like) of the products from the subsequent casting process could be adversely affected.
In the above description, aluminum material and aluminum alloy materials, which are non-ferrous metals with increasing popularity, have mainly been discussed, but similar problems reside also in iron or the like, which have been commonly used in molten metals.
It is therefore a primary object of the present invention to provide a molten metal mixing system capable of controlling generation of oxides in the course of mixing a 1st molten metal obtained by melting a 1st melt raw material and a 2nd molten metal obtained by melting a 2nd melt raw material, to thereby produce a homogeneous molten metal not contaminated with oxides (or contaminated little with oxides). It is a secondary object of the present invention to provide a molten metal mixing system capable of mixing the 1st molten metal and the 2nd molten metal at predetermined weight proportions.
The above-mentioned problems may be solved by the present invention discussed below, i.e., a molten metal mixing system, including:
According to the molten metal mixing system of the present invention, generation of oxides is controlled in the course of mixing a 1st molten metal obtained by melting a 1st melt raw material and a 2nd molten metal obtained by melting a 2nd melt raw material, to thereby produce a homogeneous molten metal not contaminated with oxides (or contaminated little with oxides). Further, the 1st molten metal and the 2nd molten metal may be mixed at predetermined weight proportions, as the two components are mixed in the form of molten metals.
Preferred embodiments of the molten metal mixing system according to the present invention will now be explained with reference to the drawings. The descriptions below and the drawings merely show some embodiments of the present invention, which should not be interpreted as limiting the present invention.
A first embodiment of the molten metal mixing system according to the present invention is shown in
<1st Melting Apparatus 10>
The 1st melting apparatus 10 includes a 1st introduction chamber 11, into which the 1st melt raw material is introduced, a 1st melting chamber 12, in which the 1st melt raw material is received from the 1st introduction chamber 11 and melted into a 1st molten metal, and a 1st retention chamber 13, in which the 1st molten metal is received from the 1st melting chamber 12 and temporarily retained therein until feeding to external apparatus, such as casting apparatus or die-casting machine.
The 1st introduction chamber 11 and the 1st melting chamber 12 are connected with an 11th transfer line W11. This 11th transfer line W11 may be, for example, in the form of a hollow pipe. In the following, an embodiment is described in which the 11th transfer line W11 is a pipe, which is designated as pipe W11.
Further, as will be discussed in detail later, according to the first embodiment, in addition to the 1st melt raw material, the 2nd molten metal is also introduced into the 1st introduction chamber 11, which is also a molten-metal-receiving chamber. Thus, in the 1st introduction chamber 11, the 1st melt raw material is mixed in the 2nd molten metal in the form of liquid. The 2nd molten metal and the 1st melt raw material in the 1st introduction chamber 11 then flow into the 1st melting chamber 12 through the interior space of the pipe W11.
The 1st melt raw material flown into the 1st melting chamber 12 is heated with an immersion burner 7 installed inside the 1st melting chamber 12 to melt into the 1st molten metal. The immersion burner 7 is configured to extend through a side wall of the 1st melting chamber 12 into the inside thereof, and arranged below the surface of the molten metal retained in the 1st melting chamber 12. The immersion burner 7 is a so-called horizontal immersion burner. The immersion burner 7 has, for example, a double pipe structure inside. Specifically, hot air introduced into the immersion burner 7 from its base end portion flows along the exterior wall of the immersion burner 7 toward the tip end portion of the immersion burner 7. In the course of this travelling of the hot air, the exterior wall of the immersion burner 7 is heated, which in turn heats the molten metal and the 1st melt raw material in contact therewith. The hot air, upon thus reaching the tip end portion of the immersion burner 7, reverses its flowing direction to flow back toward the base end portion of the immersion burner 7 through the interior space of a discharge pipe arranged along the center of the immersion burner 7, and then discharged out of the immersion burner 7. With the immersion burner 7 of such a structure, heating with higher energy efficiency is realized. An embodiment with the horizontal immersion burner has been described, but the immersion burner 7 may alternatively extend through the ceiling of the 1st melting chamber 12 into the inside thereof, and arranged below the surface of the molten metal retained in the 1st melting chamber 12. The immersion burner 7 may be a so-called vertical immersion burner. Note that the immersion burner may be replaced with an immersion heater.
In this way, the 1st molten metal is produced from the 1st melt raw material in the 1st melting chamber 12. Since the 2nd molten metal is also flown from the 1st introduction chamber 11 into the 1st melting chamber 12 as discussed above, the 1st molten metal and the 2nd molten metal are mixed in the 1st melting chamber 12 to produce a mixed molten metal.
The 1st melting chamber 12 and the 1st retention chamber 13 are connected with a 12th transfer line W12. This 12th transfer line W12 may be, for example, in the form of a hollow pipe. In the following description, an embodiment is explained in which the 12th transfer line W12 is a pipe, which is designated as pipe W12.
The mixed molten metal produced in the 1st melting chamber 12 flows into the 1st retention chamber 13 through the interior space of the pipe W12. In this way, the mixed molten metal is retained in the 1st retention chamber 13. This mixed molten metal is supplied, for example, in batches or continuously to a casting apparatus or a die-casting machine or the like in the subsequent stage.
As shown in the first sectional view of
Further, as shown in
The 1st introduction chamber 11, the 1st melting chamber 12, and the 1st retention chamber 13 are connected with the pipes W11 and W12, respectively, and the air pressures in the respective chambers 11, 12, and 13 are approximately the same, so that the surface levels of the molten metal in the respective chambers 11, 12, and 13 are generally the same.
From this state, when part of the mixed molten metal in the 1st retention chamber 13 is discharged out of the 1st melting apparatus 10, the surface level of the mixed molten metal in the 1st retention chamber 13 is lowered. Then, for compensating for this fall of the surface level of the molten metal in the 1st retention chamber 13, the 2nd molten metal is automatically transferred from the 2nd melting apparatus 1 into the 1st introduction chamber 11 (molten-metal-receiving chamber). The 2nd molten metal transferred into the 1st introduction chamber 11 (molten-metal-receiving chamber) is mixed with the 1st molten metal produced from the 1st melt raw material in the 1st melting chamber 12 into the mixed molten metal, with which the 1st retention chamber 13 is replenished. As a result, the previous surface levels of the molten metal in the chambers 11, 12, and 13 are recovered.
<2nd Melting Apparatus 1>
The 2nd melting apparatus 1 includes a 2nd introduction chamber 2, into which the 2nd melt raw material is introduced, a 2nd melting chamber 4, in which the 2nd melt raw material is received from the 2nd introduction chamber 2 and melted into a 2nd molten metal, a removal chamber 5, in which the 2nd molten metal is received from the 2nd melting chamber 4, and residual impurities, such as lumps, in the 2nd molten metal are removed by causing the impurities to float or sediment to obtain a clean 2nd molten metal, and a 2nd retention chamber 6, in which the 2nd molten metal deprived of the impurities is received and temporarily retained therein until feeding to the 1st melting apparatus 10.
The 2nd introduction chamber 2 and a circulation chamber 3 are connected with a 4′th transfer line W4′. This 4′th transfer line W4′ may be, for example, in the form of a hollow pipe. A pipe acting as the 4′th transfer line W4′ is designated as pipe W4′. The circulation chamber 3 and the 2nd melting chamber 4 are connected with a 5th transfer line W5. This 5th transfer line W5 may be, for example, in the form of a hollow pipe. A pipe acting as the 5th transfer line W5 is designated as pipe W5. The 2nd introduction chamber 2 and the 2nd melting chamber 4 are connected with a 1st transfer line W1. This 1st transfer line W1 may be, for example, in the form of a hollow pipe. A pipe acting as the 1st transfer line W1 is designated as pipe W1. For example, by means of rotation (clockwise rotation) of an impeller installed in the circulation chamber 3 for circulating molten metal, the 2nd molten metal and the 2nd melt raw material in the 2nd melting chamber 4 may be circulated through the pipe W1, the 2nd introduction chamber 2, the pipe W4′, the circulation chamber 3, and the pipe W5 back to the 2nd melting chamber 4. In particular, when a fresh 2nd melt raw material is introduced into the 2nd introduction chamber 2, the temperature of the molten metal is lowered, so that it is preferred, by means of the rotation (counterclockwise rotation) of the impeller installed in the circulation chamber 3 for circulating molten metal, to circulate the 2nd molten metal and the 2nd melt raw material through the pipe W1, the 2nd melting chamber 4, the pipe W5, the circulation chamber 3, and the pipe W4′ back to the 2nd introduction chamber 2, to thereby promote melting of the freshly introduced 2nd melt raw material into molten metal in the 2nd melting chamber 4, and to keep the temperature of the molten metal from lowering.
The 2nd molten metal and the 2nd melt raw material flown into the 2nd melting chamber 4 are heated with an immersion burner 7 installed inside the 2nd melting chamber 4, where the 2nd melt raw material melts into 2nd molten metal. The immersion burner 7 is configured to extend through a side wall of the 2nd melting chamber 4 into the inside thereof, and arranged below the surface of the molten metal retained in the 2nd melting chamber 4. This immersion burner 7 is a so-called horizontal immersion burner. The inside of this immersion burner 7 is as discussed above. Further, the immersion burner 7 has been discussed as a horizontal immersion burner, but may alternatively extend through the ceiling of the 2nd melting chamber 4 into the inside thereof, and arranged below the surface of the molten metal retained in the 2nd melting chamber 4. The immersion burner 7 may be a so-called vertical immersion burner. Note that the immersion burner may be replaced with an immersion heater.
As discussed above, in the 2nd melting chamber 4, the 2nd melt raw material is made into the 2nd molten metal. The 2nd molten metal and the 2nd melt raw material are flown from the 2nd introduction chamber 2 through the pipe W4′ into the circulation chamber 3, and then from the circulation chamber 3 through the pipe W5 back into the 2nd melting chamber 4, so that a mixture of the 2nd molten metal and the 2nd melt raw material is contained in the 2nd melting chamber 4. According to the first embodiment, the 2nd melting chamber 4 is composed of two chambers, which are connected with a 6th transfer line W6. This 6th transfer line W6 may be, for example, in the form of a hollow pipe. A pipe acting as the 6th transfer line W6 is designated as pipe W6. This structure aims to sufficiently melt the 2nd melt raw material in the 2nd melting chamber 4 located closer to the 2nd introduction chamber, and then flow the resulting molten metal into the 2nd melting chamber 4 located closer to the removal chamber 5. Note that the 2nd melting chamber 4 is not limited to being composed of two chambers as in the first embodiment, and may be composed of three or more chambers, or may be composed of one chamber as in the sixth embodiment as will be discussed later.
The 2nd melting chamber 4 and the removal chamber 5 is connected with a 2nd transfer line W2. This 2nd transfer line W2 may be, for example, in the form of a hollow pipe. A pipe acting as the 2nd transfer line W2 is designated as pipe W2.
The 2nd molten metal in the 2nd melting chamber 4 flows through the interior space of the pipe W2 into the removal chamber 5.
In the removal chamber 5, the 2nd molten metal received therein is left to stand to float or sediment impurities, such as lumps, remaining in the molten metal, which is then removed to obtain a clear 2nd molten metal.
The removal chamber 5 and the 2nd retention chamber 6 are connected with a 3rd transfer line W3. This 3rd transfer line W3 may be, for example, in the form of a hollow pipe. A pipe acting as the 3rd transfer line W3 is designated as pipe W3.
The 2nd molten metal cleaned in the removal chamber 5 flows through the interior of the pipe W3 into the second retention chamber 6. It is preferred to install an immersion burner 7 in the removal chamber 5 for keeping the temperature of the 2nd molten metal from lowering. This immersion burner 7 is configured to extend through a side wall of the removal chamber 5 into the inside thereof as illustrated, and arranged below the surface of the molten metal retained in the removal chamber 5. This immersion burner 7 is a so-called horizontal immersion burner. The inside of this immersion burner 7 is as discussed above. Further, the immersion burner 7 has been discussed as a horizontal immersion burner, but may alternatively extend through the ceiling of the removal chamber 5 into the inside thereof, and arranged below the surface of the molten metal retained in the removal chamber 5. The immersion burner 7 may be a so-called vertical immersion burner. Note that the immersion burner may be replaced with an immersion heater.
In particular, it is preferred that, as shown in
Further, as shown in
<Connecting Pipe W20>
The connecting pipe W20 connects the 1st melting apparatus 10 and the 2nd melting apparatus 1. Specifically, this connecting pipe W20 connects the 1st introduction chamber 11 (molten-metal-receiving chamber) of the 1st melting apparatus 10 and the 2nd retention chamber 6 (molten-metal-tapping chamber) of the 2nd melting apparatus 1.
The material of the connecting pipe W20 is not particularly limited, and from the viewpoint of heat resistance and durability, may preferably be, for example, silicon nitride (Si3N4) ceramics, a refractory material containing silicon carbide (SiC) and silicon nitride (Si3N4) components, or a silicon carbide (SiC) refractory material. The connecting pipe W20 may be a single-layered pipe, or a two- or more layered pipe. For example, when the connecting pipe W20 is a three-layered pipe, the first layer located closest to the center (inner layer) may be a cylindrical layer of fine ceramics, the third layer located outermost (outer layer) may be a cylindrical layer of a blanket-like insulating material or the like, mainly composed of aluminum oxide (Al2O3) and silicon dioxide (SiO2), and the second layer located between inner layer and the outer layer (intermediate layer) may be heating means embedded therebetween, such as an electric heater having a hot plate made of aluminum oxide (Al2O3) and silicon dioxide (SiO2) ceramic fibers. In such a three-layered connecting pipe W20, molten metal passes through the hollow (interior space) formed closer to the center than the inner layer. With the three-layered structure, when the outside air temperature is low, the temperature of the molten metal flowing through the interior space lowers and the molten metal solidifies, thereby preventing solidified molten metal from adhering to the inner wall of the connecting pipe W20.
The connecting pipe W20 has a siphon function. Specifically, the system is configured that, with the interior of the connecting pipe W20 filled with liquid (e.g., the 2nd molten metal), when the surface of the 2nd molten metal retained in the 1st introduction chamber 11 of the 1st melting apparatus 10 is lowered, the 2nd molten metal retained in the 2nd retention chamber 6 of the 2nd melting apparatus 1 is automatically transferred through the interior space of the connecting pipe W20 into the 1st introduction chamber 11, by the siphon principle.
The arrangement of the connecting pipe W20 is not particularly limited, and may preferably be such that one end of the connecting pipe W20 is positioned below the surface of the 2nd molten metal retained in the 2nd retention chamber 6 of the 2nd melting apparatus 1, while the other end of the connecting pipe W20 is positioned below the surface of the 2nd molten metal retained in the 1st introduction chamber 11 of the 1st melting apparatus 10. It is particularly preferred to position each end of the connecting pipe W20 in the vicinity of the center of the molten metal, other than the vicinity of the surface of the molten metal in each chamber and the vicinity of each chamber bottom. In the vicinity of the surface of the molten metal, a film of oxide resulting from reaction with oxygen in the air is prone to form, whereas in the vicinity of each chamber bottom, heavy metals contained in the used non-ferrous metals (briquette material, machining chips, or the like), fresh non-ferrous metals (fresh material), or return scrap are sedimented. Thus, such positioning is for the purpose of avoiding contamination of the interior of the connecting pipe W20 with such oxide film or heavy metals entering together with the molten metal. Such positioning is also for the purpose of the siphon principle, with each end of the connecting pipe W20 positioned in the molten metal. Similarly, for practicing the siphon principle, it is preferred to fill also the interior space of the connecting pipe W20 with the molten metal.
In order to keep each end of the connecting pipe W20 below the surface of the molten metal, each chamber is preferably provided with a level sensor for detecting the surface level of the molten metal in the chamber. The system is preferably configured such that, when the level sensor detects the approach of at least one of the ends of the connecting pipe W20 to emerge above the surface of the molten metal, the 1st melt raw material and/or the 2nd melt raw material is additionally introduced to raise the surface level of the molten metal in each chamber. Note that, when the surface level of the molten metal in the 2nd retention chamber 6 (molten-metal-tapping chamber) is lower than the surface level of the molten metal in the 1st introduction chamber 11 (molten-metal-receiving chamber), undesirable backflow of the molten metal occurs. In order to avoid such defect, when the level sensor detects a risk of backflow, the siphon principle is deactivated. Note that the siphon principle is the phenomenon of molten metal retained in one chamber with a higher surface of a molten metal, transferring to another chamber with a lower surface of a molten metal, and the transfer of the molten metal ceases when the surface levels of the molten metal in the two chambers become substantially the same.
<1st Melt Raw Material and 2nd Melt Raw Material>
The 1st melt raw material preferably contains at least one of fresh non-ferrous metals and return scrap. The 2nd melt raw material preferably contains at least one of briquette material and machining chips.
It is particularly preferred to provide the 2nd introduction chamber 2 as a vortex chamber, under which a magnetic stirrer, or a gas injection system disclosed in Japanese Patent Application No. 2019-207478 by the Applicant of the present application is provided. This is for the purpose of generating a vortex in the molten metal in the vortex chamber to draw the briquette material and machining chips, which have a lower specific gravity than that of the molten metal, into the molten metal to reduce the duration of contact with external air, which discourages formation of oxides.
A second embodiment is shown in
A third embodiment is shown in
A fourth embodiment is shown in
A fifth embodiment is shown in
A sixth embodiment is shown in
<Miscellaneous>
In the above description, the immersion burner 7 was taken as an example, but other burners may also be used. Also, the burner may be replaced with a heater.
For transporting molten metal from the 2nd melting apparatus 1 to the 1st melting apparatus 10, it is conceivable to scoop the 2nd molten metal in the 2nd melting apparatus 1 with a ladle, transport the ladle with a forklift, and pour out the molten metal into the 1st melting apparatus 10. However, this may bring the 2nd molten metal into contact with air during the molten metal transportation, to produce a large amount of oxides, leading to deterioration of final product quality. Further, during the transportation, the molten metal may splatter or the exhaust gas from the forklift may permeate the factory, which may deteriorate the working environment of workers.
In the various embodiments, transferring the 2nd molten metal through the connecting pipe W20 may significantly reduce the amount of oxides generated during the transfer, which leads to improvement in final product quality. In addition, deterioration of working environment of workers may be avoided. Further, human intervention is not required in the transfer, which contributes to reduction of labor cost.
Moreover, the 1st molten metal and the 2nd molten metal may be mixed at predetermined weight proportions, as the two components are mixed in the form of molten metals.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2020-189243 | Nov 2020 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2021/028385 | 7/30/2021 | WO |
