MOLTEN METAL MIXING SYSTEM
20230272504 · 2023-08-31
Assignee
Inventors
Cpc classification
B22D35/00
PERFORMING OPERATIONS; TRANSPORTING
Y02P10/20
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
C22B7/00
CHEMISTRY; METALLURGY
C22B21/0092
CHEMISTRY; METALLURGY
C22B7/003
CHEMISTRY; METALLURGY
International classification
C22B7/00
CHEMISTRY; METALLURGY
Abstract
A molten metal mixing system capable of controlling generation of oxides in mixing of molten metals to. The system includes 1st/2nd apparatus for melting 1st/2nd raw materials into 1st/2nd molten metals, and a pipe connecting the 1st and 2nd apparatus. The 2nd molten metal produced in the 2nd apparatus is transferred through the pipe to the 1st apparatus to mix with the 1st raw material and/or the 1st molten metal. The 2nd apparatus has a tapping chamber for retaining the 2nd molten metal to be transferred to the 1st apparatus. The 1st apparatus has a receiving chamber for retaining the 2nd molten metal transferred from the 2nd apparatus. When part of the 2nd molten metal is discharged out of the receiving chamber to lower the surface of the molten metal, the 2nd molten metal in the tapping chamber is transferred through the pipe into the receiving chamber by siphon principle.
Claims
1. A molten metal mixing system, comprising: 1st melting apparatus for melting a 1st melt raw material to produce a 1st molten metal, 2nd melting apparatus for melting a 2nd melt raw material to produce a 2nd molten metal, and a connecting pipe connecting the 1st melting apparatus and the 2nd melting apparatus, wherein the system is configured to transfer the 2nd molten metal produced in the 2nd melting apparatus through interior space of the connecting pipe to the 1st melting apparatus to mix with at least one of the 1st melt raw material and the 1st molten metal in the 1st melting apparatus, wherein the 2nd melting apparatus has a molten-metal-tapping chamber for retaining therein the 2nd molten metal to be transferred to the 1st melting apparatus, wherein the 1st melting apparatus has a molten-metal-receiving chamber for retaining therein the 2nd molten metal received from the 2nd melting apparatus, and wherein the system is configured that, when part of the 2nd molten metal retained in the molten-metal-receiving chamber is discharged out of the molten-metal-receiving chamber to lower a surface of a molten metal in the molten-metal-receiving chamber, the 2nd molten metal in the molten-metal-tapping chamber is transferred through the connecting pipe into the molten-metal-receiving chamber by siphon principle.
2. The molten metal mixing system according to claim 1, wherein the 1st melting apparatus including: an introduction chamber into which the 1st melt raw material is introduced, and a melting chamber in which the 1st melt raw material is received from the introduction chamber, and the 1st melt raw material thus received is melted to produce the 1st molten metal, wherein the system is configured to use the introduction chamber as the molten-metal-receiving chamber to mix the 1st melt raw material and the 2nd molten metal in the introduction chamber.
3. The molten metal mixing system according to claim 1, wherein the 1st melting apparatus including: a melting chamber for melting the 1st melt raw material to produce the 1st molten metal, and a retention chamber in which the 1st molten metal is received from the melting chamber and retained, wherein the system is configured to use the retention chamber as the molten-metal-receiving chamber to mix the 1st molten metal and the 2nd molten metal in the retention chamber.
4. The molten metal mixing system according to any one of claim 1, wherein the 1st melt raw material comprises at least one of fresh non-ferrous metals and return scrap, and wherein the 2nd melt raw material comprises at least one of briquette material and machining chips.
5. The molten metal mixing system according to claim 2, wherein the 1st melting apparatus including: a melting chamber for melting the 1st melt raw material to produce the 1st molten metal, and a retention chamber in which the 1st molten metal is received from the melting chamber and retained, wherein the system is configured to use the retention chamber as the molten-metal-receiving chamber to mix the 1st molten metal and the 2nd molten metal in the retention chamber.
6. The molten metal mixing system according to any one of claim 2, wherein the 1st melt raw material comprises at least one of fresh non-ferrous metals and return scrap, and wherein the 2nd melt raw material comprises at least one of briquette material and machining chips.
7. The molten metal mixing system according to any one of claim 3, wherein the 1st melt raw material comprises at least one of fresh non-ferrous metals and return scrap, and wherein the 2nd melt raw material comprises at least one of briquette material and machining chips.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
[0032]
[0033]
EMBODIMENTS FOR CARRYING OUT THE INVENTION
[0034] 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.
First Embodiment
[0035] A first embodiment of the molten metal mixing system according to the present invention is shown in
[0036] <1st Melting Apparatus 10>
[0037] 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.
[0038] 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.
[0039] 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.
[0040] 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.
[0041] 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.
[0042] 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.
[0043] 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.
[0044] As shown in the first sectional view of
[0045] Further, as shown in
[0046] 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.
[0047] 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.
[0048] <2nd Melting Apparatus 1>
[0049] 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.
[0050] 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.
[0051] 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.
[0052] 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.
[0053] 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.
[0054] The 2nd molten metal in the 2nd melting chamber 4 flows through the interior space of the pipe W2 into the removal chamber 5.
[0055] 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.
[0056] 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.
[0057] 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.
[0058]
[0059] In particular, it is preferred that, as shown in
[0060] Further, as shown in
[0061] <Connecting Pipe W20>
[0062] 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.
[0063] 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 (Si.sub.3N.sub.4) ceramics, a refractory material containing silicon carbide (SiC) and silicon nitride (Si.sub.3N.sub.4) 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 (Al.sub.2O.sub.3) and silicon dioxide (SiO.sub.2), 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 (Al.sub.2O.sub.3) and silicon dioxide (SiO.sub.2) 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.
[0064] 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.
[0065] 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.
[0066] 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.
[0067] <1st Melt Raw Material and 2nd Melt Raw Material>
[0068] 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.
[0069] 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.
Second Embodiment
[0070] A second embodiment is shown in
Third Embodiment
[0071] A third embodiment is shown in
Fourth Embodiment
[0072] A fourth embodiment is shown in
Fifth Embodiment
[0073] A fifth embodiment is shown in
Sixth Embodiment
[0074] A sixth embodiment is shown in
[0075] <Miscellaneous>
[0076] 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.
Effects of Embodiments
[0077] 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.
[0078] 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.
[0079] 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.
DESCRIPTION OF REFERENCE NUMERALS
[0080] 1: 2nd melting apparatus [0081] 2: 2nd introduction chamber [0082] 2a: top opening of 2nd introduction chamber [0083] 2L: 2nd introduction chamber lid [0084] 3: circulation chamber [0085] 3a: top opening of circulation chamber [0086] 3L: circulation chamber lid [0087] 4: 2nd melting chamber [0088] 4a: top opening of 2nd melting chamber [0089] 4L: 2nd melting chamber lid [0090] 5: removal chamber [0091] 5a: top opening of removal chamber [0092] 5L: removal chamber lid [0093] 6: 2nd retention chamber [0094] 6a: top opening of 2nd retention chamber [0095] 6L: 2nd retention chamber lid [0096] 7: burner (immersion burner/heater) [0097] 10: 1st melting apparatus [0098] 11: 1st introduction chamber [0099] 11a: top opening of 1st introduction chamber [0100] 11L: 1st introduction chamber lid [0101] 12: 1st melting chamber [0102] 12a: top opening of 1st melting chamber [0103] 12L: 1st melting chamber lid [0104] 13: 1st retention chamber [0105] 13a: top opening of 1st retention chamber [0106] 13L: 1st retention chamber lid [0107] 14: circulation chamber [0108] W1: 1st transfer line [0109] W2: 2nd transfer line [0110] W3: 3rd transfer line [0111] W4: 4th transfer line [0112] W4′: 4′th transfer line [0113] W5: 5th transfer line [0114] W6: 6th transfer line [0115] W11: 11th transfer line [0116] W12: 12th transfer line [0117] W13: 13th transfer line [0118] W14: 14th transfer line [0119] W20: connecting pipe