WO2020148877A1 - Conductor softening processing device and conductor softening processing method - Google Patents

Conductor softening processing device and conductor softening processing method Download PDF

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Publication number
WO2020148877A1
WO2020148877A1 PCT/JP2019/001340 JP2019001340W WO2020148877A1 WO 2020148877 A1 WO2020148877 A1 WO 2020148877A1 JP 2019001340 W JP2019001340 W JP 2019001340W WO 2020148877 A1 WO2020148877 A1 WO 2020148877A1
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WO
WIPO (PCT)
Prior art keywords
conductor
cavity
cooling water
heater
dissolved oxygen
Prior art date
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PCT/JP2019/001340
Other languages
French (fr)
Japanese (ja)
Inventor
善洋 中澤
春彦 田中
Original Assignee
住友電工ウインテック株式会社
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Filing date
Publication date
Application filed by 住友電工ウインテック株式会社 filed Critical 住友電工ウインテック株式会社
Priority to PCT/JP2019/001340 priority Critical patent/WO2020148877A1/en
Priority to JP2020566060A priority patent/JP7302142B2/en
Priority to CN201980082718.0A priority patent/CN113272462B/en
Publication of WO2020148877A1 publication Critical patent/WO2020148877A1/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/34Methods of heating
    • C21D1/42Induction heating
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous furnaces for strip or wire
    • C21D9/573Continuous furnaces for strip or wire with cooling
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous furnaces for strip or wire
    • C21D9/60Continuous furnaces for strip or wire with induction heating
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B13/00Apparatus or processes specially adapted for manufacturing conductors or cables
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Definitions

  • the present disclosure relates to a conductor softening treatment device and a conductor softening treatment method.
  • Patent Document 1 Japanese Unexamined Patent Publication No. 2016-794366 describes a conductor softening treatment device capable of suppressing oxidation of a conductor.
  • This conductor softening treatment apparatus reduces the amount of oxygen around the conductor to be cooled from the heated state by immersing the conductor after heating in cooling water in which the dissolved oxygen amount is within a predetermined setting range, and Inhibits oxidation.
  • a conductor softening treatment apparatus is a conductor softening treatment apparatus that continuously heats and cools a linear conductor, and a feeding mechanism that continuously conveys the conductor in its axial direction, A heater for heating the conductor conveyed by the feeding mechanism, a cooling tank for storing cooling water in which the conductor heated by the heater is immersed, and a dissolved oxygen amount of the cooling water stored in the cooling tank are set in advance. And a carrier pipe having a dissolved oxygen amount adjusting mechanism for maintaining the temperature within a predetermined set range, wherein the heater extends in the conductor transport direction and a cavity for transporting the conductor is formed therein, and the transport pipe. A plurality of conductive lines embedded along the direction in the carrier pipe and wired so that the magnetic field is strengthened at the center of the plane of the cavity perpendicular to the carrier direction.
  • a conductor softening treatment method is a conductor softening treatment method of continuously heating and cooling a linear conductor, wherein the conductor softening treatment device is used and the conductor is Direction, the step of continuously conveying the conductor, the step of heating the conductor to be conveyed, the step of cooling the heated conductor by immersion in cooling water, and the amount of dissolved oxygen in the cooling water set in advance. Maintaining within the range.
  • FIG. 1 is a schematic diagram showing the configuration of a conductor softening treatment apparatus according to an embodiment of the present invention.
  • FIG. 2 is a schematic cross-sectional view taken along line AA of the heater of the conductor softening treatment device shown in FIG.
  • FIG. 3 is a schematic cross-sectional view showing a state where the magnetic body of the heater shown in FIG. 2 is divided.
  • Patent Document 1 describes, as a heater for heating a conductor, a configuration in which a conductor is inserted into a tubular member made of transparent glass or the like and heated by an induction heating coil arranged outside the tubular member.
  • a heater for heating a conductor a configuration in which a conductor is inserted into a tubular member made of transparent glass or the like and heated by an induction heating coil arranged outside the tubular member.
  • it is effective to bring the coil close to the conductor.
  • the present disclosure has been made based on the above circumstances, and a conductor softening treatment device having a heater capable of enhancing the heating efficiency of a conductor while suppressing damage to the device and a conductor using the conductor softening treatment device. It is intended to provide a softening treatment method.
  • the heater of the conductor softening treatment device of the present disclosure can improve the heating efficiency of the conductor while suppressing damage to the device. Therefore, the conductor softening treatment method using the conductor softening treatment device of the present disclosure can improve the energy efficiency of the conductor softening treatment device while suppressing damage to the conductor softening treatment device, and thus is excellent in manufacturing efficiency.
  • a conductor softening treatment apparatus is a conductor softening treatment apparatus that continuously heats and cools a linear conductor, and a feeding mechanism that continuously conveys the conductor in its axial direction, A heater for heating the conductor conveyed by the feeding mechanism, a cooling tank for storing cooling water in which the conductor heated by the heater is immersed, and a dissolved oxygen amount of the cooling water stored in the cooling tank are set in advance. And a carrier pipe having a dissolved oxygen amount adjusting mechanism for maintaining the temperature within a predetermined set range, wherein the heater extends in the conductor transport direction and a cavity for transporting the conductor is formed therein, and the transport pipe. A plurality of conductive lines embedded along the direction in the carrier pipe and wired so that the magnetic field is strengthened at the center of the plane of the cavity perpendicular to the carrier direction.
  • the conductor softening treatment device reduces the amount of oxygen around the conductor to be cooled from the heated state by immersing the conductor after heating in the cooling water in which the dissolved oxygen amount is within a predetermined setting range. Oxidation can be suppressed. Further, in the heater of the conductor softening processing apparatus, a cavity for carrying the conductor is formed inside the carrying pipe, and a conductive wire for generating a magnetic field for heating the conductor is embedded in the carrying pipe along the carrying direction of the conductor. Has been done. Therefore, even if the heater of the conductor softening apparatus is configured to bring the conductive wire closer to the conductor to improve the heating efficiency, it is not necessary to reduce the wall thickness of the carrier pipe, so that damage to the carrier pipe is suppressed. Therefore, the conductor softening treatment can improve the heating efficiency of the conductor while suppressing damage to the device.
  • the main component of the above-mentioned carrier pipe is heat-resistant resin.
  • the main component of the above-mentioned carrier pipe is heat-resistant resin.
  • the heater may be embedded in the transfer pipe along the transfer direction and may have a heat shield plate surrounding the cavity. In this way, the heater is embedded in the transfer pipe along the transfer direction and has the heat shield plate surrounding the cavity, whereby the heating efficiency of the conductor can be further increased.
  • the average thickness of the heat shield plate is preferably 0.5 mm or more and 5 mm or less. In this way, by setting the average thickness of the heat shield plate within the above range, it is possible to enhance the heat shield effect while maintaining the heating efficiency of the conductor by the conductive wire.
  • the heater is preferably embedded in the transfer tube along the transfer direction and has a magnetic body surrounding the cavity.
  • the heater is embedded in the transfer tube along the transfer direction and has the magnetic body surrounding the cavity, so that the magnetic field of the cavity is further increased, and thus the heating efficiency of the conductor is further increased. be able to.
  • the distance between magnetic bodies in the magnetic flux direction at the center of the cavity in a plane perpendicular to the transport direction is preferably shorter than the distance between magnetic bodies in the direction orthogonal to the magnetic flux direction.
  • the carrier pipe is configured to be separable so as to open the cavity.
  • the transfer pipe by configuring the transfer pipe so that it can be divided so as to open the cavity, it is possible to facilitate insertion of the conductor into the cavity, and it is possible to facilitate confirmation of the inside of the cavity and cleaning.
  • the conductive wires be covered with insulation.
  • an electrical short circuit may occur between a plurality of conductive wires due to water ingress into the carrier tube. Can be deterred. Therefore, damage to the conductor softening device can be further suppressed.
  • the length of the cavity is preferably 50 mm or more and 1500 mm or less.
  • a conductor softening treatment method is a conductor softening treatment method of continuously heating and cooling a linear conductor, wherein the conductor softening treatment device is used and the conductor is Direction, the step of continuously conveying the conductor, the step of heating the conductor to be conveyed, the step of cooling the heated conductor by immersion in cooling water, and the amount of dissolved oxygen in the cooling water set in advance. Maintaining within the range.
  • the conductor softening treatment method uses the conductor softening treatment device of the present invention, the energy efficiency of the conductor softening treatment device can be enhanced while suppressing damage to the conductor softening treatment device. Therefore, the conductor softening method is excellent in manufacturing efficiency.
  • the “dissolved oxygen amount” is a value measured according to JIS-K-0101:1998.
  • the "main component” means a component having the largest content, for example, a component having a content of 50% by mass or more.
  • the “average thickness” refers to the average value of the thickness measured at any 10 points.
  • the conductor softening treatment device shown in FIG. 1 continuously heats and cools the linear conductor C.
  • This conductor softening apparatus includes a feeding mechanism 1 that continuously conveys the conductor C in the axial direction thereof, a heater 2 that heats the conductor C that is conveyed by the feeding mechanism 1, and a conductor C that is heated by the heater 2.
  • the cooling tank 3 that stores the cooling water W in which the water is immersed, the dissolved oxygen amount adjusting mechanism 4 that maintains the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 within a predetermined setting range, and the conductor C
  • An air blower 5 is provided for blowing air to remove water adhering to the surface.
  • the conductor C to be softened in the conductor softening device is not particularly limited, but for example, copper wire, copper alloy wire, tin-plated copper wire, aluminum wire, aluminum alloy wire, steel core aluminum wire, copper fly wire, nickel.
  • Examples of the copper wire include a plated copper wire, a silver-plated copper wire, and a copper-clad aluminum wire, and typically a copper wire.
  • the average cross-sectional area of the conductor C is not particularly limited, but is, for example, 0.01 mm 2 or more and 10 mm 2 or less.
  • the cross-sectional shape of the conductor C is not particularly limited, and may be circular or rectangular, for example.
  • the feeding mechanism 1 includes a plurality of guide sheaves (pulleys) on which the conductor C is bridged, and is configured to convey the conductor C in a constant direction indicated by an arrow D.
  • the feed mechanism 1 of FIG. 1 is configured by three guide sheaves, a first guide sheave 11, a second guide sheave 12, and a third guide sheave 13 from the upstream side in the transport direction.
  • the first guide sheave 11 on the upstream side and the third guide sheave 13 on the downstream side are arranged above the cooling tank 3, and the second guide sheave 12 in the middle is arranged in the cooling tank 3.
  • the mechanism 1 conveys the conductor C so as to pass through the cooling water W stored in the cooling tank 3.
  • the feed mechanism 1 conveys the conductor C so as to enter the cooling water W stored in the cooling tank 3 downward in the vertical direction.
  • the feeding speed of the conductor C by the feeding mechanism 1 is not particularly limited, but is, for example, 1 m/min or more and 1000 m/min or less, typically 5 m/min or more and 100 m/min or less.
  • the heater 2 includes a transport pipe 21 extending in the transport direction of the conductor C, a plurality of conductive wires 22 embedded in the transport pipe 21 along the transport direction, and a heat shield plate 23. And a magnetic body 24.
  • the carrier pipe 21 has a cavity 21a for carrying the conductor C formed therein.
  • the conductor C is heated and then cooled by the cooling water W.
  • the cooling water W takes away the heat of the conductor C and becomes steam.
  • the water vapor thus generated in the cavity 21a rises in the cavity 21a and pushes out the oxygen-containing air present in the cavity 21a.
  • the supply of oxygen to the conductor C in a heated state is cut off, and the oxidation of the conductor C is suppressed.
  • the cross-sectional shape of the cavity 21a formed inside the carrier pipe 21 is not particularly limited, but may be, for example, a square shape or a circular shape as shown in FIG.
  • the cavity 21a is arranged so that the center M of the cross section of the transfer tube 21, that is, the center M of the cross section of the cavity 21a (the surface perpendicular to the transfer direction) coincides with the center of the cross section of the transfer tube 21.
  • the cross-section of the carrier pipe 21 and the cross-section of the cavity 21a may have similar shapes, but may have different shapes.
  • the cross section of the cavity 21a is sized so as to include at least the maximum cross section of the conductor C.
  • the lower limit of the ratio of the cross-sectional area of the cavity 21a to the maximum cross-sectional area of the conductor C is preferably 2 times and more preferably 4 times.
  • the upper limit of the cross-sectional area ratio is preferably 20 times, more preferably 10 times. If the ratio of the above-mentioned cross-sectional areas is less than the above lower limit, the conductor C may come into contact with the inner wall of the cavity 21a, resulting in damage to the conductor C or uneven softening treatment.
  • the cavity 21a may be composed of a heat shield plate 23 or the like in which a part or all of the inner wall is buried in the carrier pipe 21 as shown in FIG. 2, for example. It refers to the area of the space surrounded by the inner wall regardless of its constituent elements.
  • the inter-magnetic body distance (T1 in FIG. 2) in the magnetic flux direction (S direction in FIG. 2, which will be described later in detail) at the center of the cavity 21a in the plane perpendicular to the transport direction is a direction orthogonal to the magnetic flux direction S. It is preferable to be shorter than the inter-magnetic substance distance (T2 in FIG. 2).
  • T1 in the magnetic flux direction S at the center M of the cavity 21a in the plane perpendicular to the transport direction shorter than the inter-magnetic body distance T2 in the direction orthogonal to the magnetic flux direction S, Since the magnetic field in 21a is further enhanced, the heating efficiency of the conductor C can be further enhanced.
  • the length of the cavity 21a (the length of the carrier pipe 21 in which the cavity 21a is formed) is preferably such that at least the portion of the conductor C that is easily oxidized, that is, the portion in the heated state, can be surrounded by the cavity 21a. .. That is, at least the lower end of the cavity 21a is immersed in the cooling water W, and the upper end is arranged at a height higher than the upper end of the conductive wire 22 described later.
  • the lower limit of the length of the cavity 21a is preferably 50 mm, more preferably 100 mm.
  • the upper limit of the length of the cavity 21a is preferably 1500 mm, more preferably 1000 mm. If the length of the cavity 21a is less than the above lower limit, the oxygen amount in the atmosphere of the conductor C at the position where the conductor C is in a heated state may not be sufficiently reduced. On the contrary, if the length of the cavity 21a exceeds the upper limit, the conductor softening device may unnecessarily increase in size.
  • the lower end of the cavity 21a (lower end of the heater 2) is configured to be located inside the cooling water W stored in the cooling tank 3.
  • the lower end of the cavity 21 a is located inside the cooling water W by extending only the transport pipe 21 without including the conductive wire 22, the heat shield plate 23 and the magnetic body 24.
  • the configuration of the lower end of the cavity 21a is not limited to this, and may have another configuration.
  • a configuration in which only the conductive wire 22 is not included and the lower end of the cavity 21a is located in the cooling water W by extending the transport pipe 21, the heat shield plate 23, and the magnetic body 24 downward, and the like are given. be able to.
  • the lower end of the conductive wire 22 may be located in the cooling water W, but from the viewpoint of heating efficiency, the lower end of the conductive wire 22 is preferably located above the liquid surface of the cooling water W.
  • the lower limit of the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W described later is preferably 0.01 m, and more preferably 0.05 m.
  • the upper limit of the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W is preferably 1 m, more preferably 0.7 m.
  • the conductor C Even after the conductor C is conveyed below the lower end of the conductive wire 22, the temperature is maintained to some extent and the annealing effect continues. Then, the conductor C is conveyed to below the liquid surface of the cooling water W, and is rapidly cooled. Therefore, if the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W is less than the above lower limit, the continuous annealing effect is reduced, and the heating efficiency may be reduced. On the contrary, if the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W exceeds the upper limit, the conductor softening treatment device may unnecessarily increase in size.
  • the lower limit of the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W is preferably 0.01 m, more preferably 0.03 m.
  • the upper limit of the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W is preferably 0.15 m, more preferably 0.1 m.
  • the upper end of the cavity 21a is arranged at a height higher than the upper end of the conductive wire 22.
  • the lower limit of the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is preferably 0.01 m, more preferably 0.03 m.
  • the upper limit of the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is preferably 0.15 m, more preferably 0.1 m. If the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is less than the above lower limit, the oxygen amount in the atmosphere of the conductor C at the position where the conductor C is heated may not be sufficiently reduced. On the contrary, if the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 exceeds the above upper limit, the conductor softening treatment device may unnecessarily increase in size.
  • Heat-resistant resin is preferable as the main component of the carrier pipe 21.
  • the heat-resistant resin having no conductivity as the main component of the carrier pipe 21.
  • the heater 2 can easily withstand the heat from the conductor C which becomes hot.
  • heat-resistant resin examples include known engineering plastics such as polycarbonate, polybutylene terephthalate, nylon 66, modified polyphenyl ether, polyphenylene sulfide, polyether ether ketone, polytetrafluoroethylene, polyetherimide, polyamideimide, and polyimide. be able to.
  • the lower limit of the continuous use temperature (UL) of the heat resistant resin is preferably 120°C, more preferably 200°C. If the UL of the heat-resistant resin is less than the above lower limit, the heat resistance of the transport pipe 21 may be insufficient.
  • the upper limit of the continuous use temperature (UL) of the heat resistant resin is not particularly limited, and the higher the better.
  • the “continuous use temperature” is a temperature specified in UL standard UL746B.
  • the lower limit of the toughness of the heat-resistant resin is preferably 1kJ / m 2, 3kJ / m 2 is more preferable. If the toughness of the heat-resistant resin is less than the above lower limit, the effect of suppressing damage to the transport pipe 21 may be insufficient.
  • the upper limit of the toughness of the heat resistant resin is not particularly limited, and the higher the better.
  • the "toughness" means a numerical value obtained based on the method for obtaining the Charpy impact property described in JIS-K-7111-1:2012.
  • the thickness of the carrier tube 21 can be appropriately determined within a range in which the heater 2 does not become excessively large while maintaining the strength of the heater 2.
  • the plurality of conductive lines 22 generate a magnetic field whose magnetic flux density changes by passing an alternating current. An eddy current is generated in the conductor C due to this change in the magnetic field, and the conductor C itself generates heat due to the Joule loss.
  • the heating temperature of the conductor C by the plurality of conductive wires 22 is selected according to the material of the conductor C and the like, but is, for example, 300° C. or more and 500° C. or less.
  • the number of the conductive wires 22 is not particularly limited, but it is preferable that the number of the conductive wires 22 is 2 or 4 so that the magnetic field can be easily strengthened.
  • the conductive wires 22 are arranged at point symmetric positions with the center M of the cavity 21a as the center.
  • the conductive wires 22 are arranged on each side of the magnetic flux direction S such that two conductive wires 22 are point-symmetrical along the magnetic flux direction S about the center M of the cavity 21a. Good to do.
  • the case where two conductive wires 22 are arranged as shown in FIG. 2 will be described as an example, but the number and the position of the conductive wires 22 are not limited, and the number and the arrangement of the conductive wires 22 are not limited. The same applies when the installation positions are different.
  • the two conductive wires 22 are laid out so that the magnetic field is strengthened at the center M of the cavity 21a in the plane perpendicular to the above-mentioned transport direction. That is, since the voltage applied to the conductive wire 22 is an alternating current, when the alternating voltage becomes positive, the conductive wire 22 below the center M of the cavity 21a in FIG. It is preferable that the conductive wire 22 that is wired so as to flow and that is located above the center M of the cavity 21a be such that a downward current flows from above the paper surface. With such wiring, the magnetic flux of the two conductive wires 22 tends to strengthen the magnetic flux in the magnetic flux direction S when the AC voltage becomes positive, so that the magnetic field strengthens at the center M of the cavity 21a.
  • the magnetic flux direction S is set from the right to the left in FIG. 2, but it may be set from the left to the right.
  • the conductive wire 22 below the center M of the cavity 21a is wired so that a downward current flows from above the paper surface, and the conductive wire 22 above the center M of the cavity 21a. Is wired so that an upward current flows from the bottom of the paper.
  • the conductive wire 22 preferably has a conductor portion 22a through which electricity flows and a covering portion 22b that covers the periphery of the conductor portion 22a. That is, it is preferable that the conductive wire 22 is covered with insulation.
  • the covering portion 22b can be formed of, for example, a heat-resistant resin tube or the like.
  • the plurality of conductive wires 22 have the same length.
  • the length of the conductive wire 22 is determined so that the conductor C can be sufficiently heated, and the specific length is, for example, 10 cm or more and 200 cm or less.
  • the conductor portion 22a of the conductive wire 22 is preferably tubular so that cooling water can pass through it in order to prevent it from becoming too hot.
  • the thickness of the conductor portion 22a is appropriately determined so that the conductor 22a does not become too thin and the pressure loss of the cooling water does not increase, and that the conductor 22a does not become too thick and the heating efficiency decreases.
  • the average thickness of the covering portion 22b is appropriately determined so as to ensure the insulation between the conductor portion 22a and the outside.
  • the heat shield plate 23 surrounds the cavity 21a. By disposing the heat shield plate 23 so as to surround the cavity 21a in this manner, it is possible to prevent heat from diffusing from the cavity 21a to the outside and to improve the heating efficiency of the conductor C.
  • the heat shield plate 23 is preferably located closer to the cavity 21a, more preferably closer to the cavity 21a than the conductive wire 22, and as shown in FIG. It is more preferable to set the position to form the side wall of the cavity 21a.
  • the heat shield plate 23 has an insulating property. As a result, the heat shield plate 23 also functions as an insulating plate for the buried conductive wire 22, and can prevent an electrical short circuit from occurring between the plurality of conductive wires 22. Therefore, damage to the conductor softening device is further suppressed.
  • the lower limit of the average thickness of the heat shield plate 23 is preferably 0.5 mm, more preferably 0.7 mm.
  • the upper limit of the average thickness of the heat shield plate 23 is preferably 5 mm, more preferably 3 mm. If the average thickness of the heat shield plate 23 is less than the above lower limit, the heat shield effect may be insufficient. On the contrary, if the average thickness of the heat shield plate 23 exceeds the upper limit, the heating efficiency of the conductor C may not be sufficiently improved.
  • the lower limit of the continuous use temperature (UL) of the heat shield plate 23 is preferably 350°C, more preferably 500°C. If the UL of the heat shield plate 23 is less than the above lower limit, the heat shield effect may be insufficient. On the other hand, the upper limit of the continuous use temperature (UL) of the heat shield plate 23 is not particularly limited, and the higher the better.
  • the toughness of the lower limit of the heat shield plate 23 is preferably 0.5kJ / m 2, 1kJ / m 2 is more preferable. If the toughness of the heat shield plate 23 is less than the above lower limit, the heat shield plate 23 may be easily damaged. On the other hand, the upper limit of the toughness of the heat shield plate 23 is not particularly limited, and the higher the better.
  • the magnetic body 24 surrounds the cavity 21a.
  • the magnetic body 24 strengthens the magnetic field induced by the conductive wire 22 and promotes heating of the conductor C.
  • the cavity 21a is surrounded by a total of four magnetic bodies 24, that is, a pair of magnetic bodies 24 parallel to the magnetic flux direction S and a pair of magnetic bodies 24 perpendicular to the magnetic flux direction. There is.
  • the material of the magnetic body 24 is not particularly limited, and a known material such as ferrite can be used.
  • each cross section of the magnetic body 24 is not particularly limited, but can be, for example, a square shape (square shape or rectangular shape).
  • the overall size of the cross section of the magnetic body 24 (the total size of the four magnetic bodies 24 in FIG. 2) is appropriately determined according to the material and the like of the conductor C so that the conductor C can be sufficiently heated.
  • the magnetic body 24 is preferably arranged so that the conductor 22 is located in the space surrounded by the four magnetic bodies 24, as shown in FIG. By disposing the magnetic body 24 in this way, the conductive wire 22 can be brought close to the cavity 21a while maintaining the effect of improving the heating efficiency of the conductor C by the magnetic body 24, so that the heating efficiency of the conductor C is further increased.
  • the carrier pipe 21 is dividable so as to open the cavity 21a. By this division, a part of the cavity 21a is opened to the outside along the carrying direction. By configuring the transport pipe 21 so that it can be divided so as to open the cavity 21a, it is possible to facilitate the insertion of the conductor C into the cavity 21a, and also to facilitate confirmation of the state inside the cavity 21a and cleaning.
  • the width of the opened portion of the cavity 21a (the length in the direction perpendicular to the transport direction) is set to a size that allows at least the conductor C to be taken in and out of the cavity 21a, and in consideration of maintenance such as cleaning inside the cavity 21a.
  • the maximum width of the cavity 21a is preferable.
  • the carrier tube 21 is divided into the postures as shown in FIG.
  • the transport line is a polygonal line that includes one of the inner wall surfaces of the cavity 21a orthogonal to the magnetic flux direction S and does not include the plurality of conductive lines 22. It may be divided into two parts that are cut along the direction.
  • the method of opening and closing the dividable carrier pipe 21 is not particularly limited as long as airtightness can be ensured in the closed state, but for example, a method of using a sealing material made of heat-resistant rubber or the like, or a main body portion and a dividing portion. There may be mentioned a method of providing an engaging mechanism in the.
  • the cooling tank 3 is a water tank having an open upper portion for storing the cooling water W.
  • the cooling tank 3 has an upper part sealed by a lid 31 having a hole formed through the heater 2.
  • the cooling tank 3 also has an overflow mechanism 32 that keeps the water level of the cooling water W within a predetermined range.
  • the capacity of the cooling tank 3 is not particularly limited, and is selected according to the size of the second guide sheave 12 and the like.
  • a material forming the cooling tank 3 for example, one kind or a combination of plural kinds of metal, resin, glass and the like is used.
  • the cooling water W is stored in the cooling tank 3 so as to immerse the lower end of the heater 2 (the lower end of the cavity 21a).
  • the immersion depth of the conductor C in the cooling tank 3, that is, the vertical distance from the liquid surface of the cooling water W to the lower end of the second guide sheave 12 in the cooling tank 3 depends on the cross-sectional area of the conductor C and the transport speed. The depth is set so that C can be sufficiently cooled.
  • the lid 31 restricts the entry and exit of air to and from the cooling tank 3, but is not airtight enough to make the pressure in the cooling tank 3 different from the atmospheric pressure.
  • a material for forming the lid 31 for example, one kind or a combination of plural kinds of metal, resin, glass and the like is used.
  • the overflow mechanism 32 causes the cooling water W to overflow so that the water level in the cooling tank 3 does not exceed a certain height.
  • the conductor softening treatment device when oxygen in the atmosphere is dissolved in the cooling water W in the cooling tank 3 and the dissolved oxygen amount rises, a new cooling with a small dissolved oxygen amount is performed in the cooling tank 3 from the dissolved oxygen amount adjusting mechanism 4 described later. Water W is supplied.
  • the conductor softening treatment device has the overflow mechanism 32, so that when the new cooling water W is supplied, the old cooling water W is preferentially overflowed, so that the dissolved oxygen of the cooling water W in the cooling tank 3 is dissolved.
  • the amount can be kept within the set range.
  • the overflow mechanism 32 a pipe or the like that opens to the side wall of the cooling tank 3 is used. As shown in FIG. 1, the overflow mechanism 32 may have a trap 32a that isolates the internal space of the cooling tank 3 from the outside by the overflowed cooling water W.
  • the dissolved oxygen amount adjusting mechanism 4 includes a supply unit 41 that supplies new cooling water W to the cooling tank 3, and a dissolved oxygen amount detection unit 42 that measures the dissolved oxygen amount of the cooling water W stored in the cooling tank 3.
  • a control unit 43 that controls the cooling water supply amount of the supply unit 41 based on the detection value of the dissolved oxygen amount detection unit 42, and a deoxidation unit 44 that reduces the dissolved oxygen amount of the cooling water W supplied by the supply unit 41.
  • the dissolved oxygen amount detection unit 42 detects the dissolved oxygen amount of the cooling water W stored in the cooling tank 3, and the detected value indicates the upper limit value of the preset range. When it exceeds, new cooling water W with the amount of dissolved oxygen reduced by the deoxidizing unit 44 is supplied from the supply unit 41 to the cooling tank 3. Further, the dissolved oxygen amount adjusting mechanism 4 stops the supply of the new cooling water W from the supply unit 41 to the cooling tank 3 when the detected value of the dissolved oxygen amount detection unit 42 becomes less than the lower limit value of the above setting range. .. As a result, the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 is maintained within the above set range. Further, the supply amount of the cooling water W may be adjusted so that the detection value of the dissolved oxygen amount detection unit 42 becomes a representative value within the above setting range.
  • the lower limit value of the above-mentioned set range of the dissolved oxygen amount of the cooling water W in the cooling tank 3 is preferably 0.1 mg/L, more preferably 0.3 mg/L.
  • the upper limit of the above setting range is preferably 6 mg/L, more preferably 3 mg/L, further preferably 2 mg/L, particularly preferably 1 mg/L.
  • a large equipment cost and running cost are required, which may be uneconomical and may result in halfway oxidation.
  • the adhesion of the surface of the conductor C may be lowered due to the formation of the coating film.
  • the dissolved oxygen amount of the cooling water W in the cooling tank 3 is preferably maintained at a value lower than the dissolved oxygen amount of water in the air-opened state, but the smaller it is, the closer the conductor C surface adheres after the softening treatment. It is not possible to improve the sex. Therefore, by maintaining the dissolved oxygen amount of the cooling water W in the cooling tank 3 within the above-mentioned preferable range, the adhesion of the surface of the conductor C after the softening treatment can be maximized.
  • the lower limit value of the above setting range may be 0 mg/L if there is no problem in operation and control.
  • the dissolved oxygen amount of the cooling water W in the cooling tank 3 need only be a preset value (corresponding to the upper limit of the above setting range) or less.
  • the lower limit value of the setting range may be the same as the upper limit value. That is, the dissolved oxygen amount of the cooling water W in the cooling tank 3 may be adjusted by the dissolved oxygen amount adjusting mechanism 4 so that the difference from the set value becomes as small as possible.
  • the supply unit 41 is formed from a pipe that supplies new cooling water W to the cooling tank 3, and has a regulating valve 45 that adjusts the flow rate of the cooling water W supplied to the cooling tank 3.
  • the position inside the cooling tank 3 where the supply unit 41 supplies the cooling water W is preferably a position away from the overflow mechanism 32 of the cooling tank 3.
  • the supply unit 41 supplies new cooling water W through a pipe that opens into the cooling water W stored in the cooling tank 3.
  • the new cooling water W By supplying the new cooling water W to the inside of the cooling tank 3 in this manner, it is possible to prevent the oxygen existing in the space above the liquid surface from dissolving into the cooling water W due to the stirring of the liquid surface of the cooling water W.
  • the dissolved oxygen amount detection unit 42 detects the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 and sends it as a detection signal to the control unit 43.
  • the dissolved oxygen amount detection unit 42 for example, an automatic dissolved oxygen measuring device based on JIS-K-0803:1995 can be used.
  • the disposing position of the dissolved oxygen amount detection unit 42 it is preferable to avoid a position where the amount of dissolved oxygen may be smaller than that of other portions by supplying new cooling water W from the supply unit 41, and to suppress the oxidation of the conductor C. It is more preferable that the position where the dissolved oxygen amount of the cooling water W contributing to the measurement can be measured, that is, the vicinity of the position where the conductor C enters the cooling water W.
  • Control unit 43 adjusts the opening degree of the adjustment valve 45 of the supply unit 41 so as to maintain the detected value of the dissolved oxygen amount detection unit 42 within a predetermined setting range.
  • the supply amount of new cooling water W is controlled.
  • the control unit 43 can be composed of, for example, a general-purpose computer, a PID controller, a sequencer, or the like.
  • a control method for example, PID control, proportional control, on/off control, fuzzy (membership function) control, or the like can be applied.
  • the deoxidizing unit 44 is configured by, for example, a chemical deoxidizer, a heating deoxidizer, a vacuum deoxidizer, a reverse osmosis membrane deoxidizer, a nitrogen deoxidizer, and the like.
  • the above chemical deoxidizer removes oxygen by a chemical reaction by adding a deoxidizer to the makeup water.
  • oxygen scavenger include hydrazine, sodium sulfite, and natural organic compounds.
  • the above-mentioned heated deoxidizer removes dissolved oxygen by heating make-up water to boil.
  • Examples of the method of boiling the makeup water include a method of heating the makeup water with a heater and a method of introducing steam into the makeup water.
  • the vacuum deoxidizer removes dissolved oxygen by decompressing the makeup water.
  • Make-up water may be sprayed to promote degassing of dissolved oxygen.
  • the above reverse osmosis membrane deoxidizer obtains water with a small amount of dissolved oxygen by filtering water using a reverse osmosis membrane that blocks the permeation of oxygen.
  • the above-mentioned nitrogen deoxidizer makes nitrogen gas vapor-liquid contact with the makeup water, and moves the dissolved oxygen in the makeup water to the nitrogen gas side due to the difference in partial pressure.
  • the lower limit of the dissolved oxygen amount of the new cooling water W obtained by removing oxygen from the makeup water by the deoxidizing unit 44 as described above is preferably 0.05 mg/L, more preferably 0.1 mg/L.
  • the upper limit of the dissolved oxygen amount of the new cooling water W is preferably 2 mg/L, more preferably 1 mg/L. In order to prevent the amount of dissolved oxygen in the new cooling water W from falling below the lower limit, a large equipment cost and running cost are required, which may be uneconomical. On the contrary, if the amount of dissolved oxygen in the new cooling water W exceeds the upper limit, the amount of dissolved oxygen in the cooling water W in the cooling tank 3 may not be sufficiently reduced.
  • the air blow 5 is a non-contact wiper that blows off air onto the surface of the conductor C coming out of the cooling tank 3 to wipe off water droplets adhering to the surface of the conductor C.
  • this air blow 5 it is preferable to set the blowing direction and the distance from the lid 31 so that the air blown on the surface of the conductor C does not easily enter the inside of the cooling tank 3 through the hole of the lid 31.
  • the conductor softening treatment apparatus reduces the amount of oxygen around the conductor C cooled from the heated state by immersing the conductor C after heating in the cooling water W in which the dissolved oxygen amount is within a predetermined setting range.
  • the oxidation of the conductor C can be suppressed.
  • a cavity 21a for transporting the conductor C is formed inside the transport pipe 21, and a conductive wire 22 for generating a magnetic field for heating the conductor C is further provided in the transport direction of the conductor C. Is embedded in the carrier pipe 21 along the.
  • the conductor softening treatment can improve the heating efficiency of the conductor C while suppressing damage to the device.
  • a conductor softening treatment method according to an aspect of the present invention is a conductor softening treatment method of continuously heating and cooling a linear conductor C.
  • the conductor softening method is performed by using the conductor softening device shown in FIG.
  • the conductor softening treatment method includes a step of continuously transporting the conductor C in the axial direction thereof, a step of heating the transported conductor C, and a step of cooling the heated conductor C by immersion in cooling water W. , Maintaining the dissolved oxygen amount of the cooling water W within a predetermined set range.
  • the carrying step can be performed using the feeding mechanism 1 of the conductor softening device of FIG. Therefore, the transport conditions such as the transport speed are the same as those described for the conductor softening device in FIG.
  • the conductor C is a rectangular conductor having a rectangular cross section
  • the conductor C may be conveyed so that the long side of the cross section of the conductor C is perpendicular to the magnetic flux direction S. By carrying in this manner, the conductor C can be efficiently heated.
  • the heating step can be performed using the heater 2 of the conductor softening device of FIG. Therefore, the heating conditions are the same as those described for the conductor softening device in FIG.
  • the cooling step can be performed by immersing the conductor C in the cooling water W stored in the cooling tank 3 of the conductor softening device of FIG.
  • the maintaining step can be performed using the dissolved oxygen amount adjusting mechanism 4 of the conductor softening device of FIG. Therefore, the conditions and the like of the cooling water W are the same as those described for the conductor softening device of FIG.
  • the conductor softening treatment method uses the conductor softening treatment device of the present invention, it is possible to enhance the energy efficiency of the conductor softening treatment device while suppressing damage to the conductor softening treatment device. Therefore, the conductor softening method is excellent in manufacturing efficiency.
  • the insulated wire includes a step of softening the conductor by the conductor softening treatment method, a step of applying an insulating coating (varnish) on the surface of the softened conductor, and a step of baking the insulating coating applied on the surface of the conductor by heating. It is manufactured by the method of preparing.
  • the softening treatment step is performed according to the conductor softening treatment method described above.
  • the conductor C is penetrated through a coating tank that stores the insulating coating material, and the insulating coating material attached to the surface of the conductor C is adjusted to have a constant thickness by a die.
  • the main component of the insulating paint may be a resin having high insulation and heat resistance, and examples thereof include polyamide, polyimide, polyamideimide, polyesterimide, and the like.
  • the insulating paint may contain a solvent such as N-methyl-2-pyrrolidone or cresol.
  • a known die having an inner surface formed into a conical surface and having the effect of automatically aligning the conductor C by the wedge film effect and making the film thickness constant in the circumferential direction is used.
  • the insulating coating material is cured by heating the conductor whose surface is coated with the insulating coating material.
  • the insulating paint contains a solvent
  • the solvent is volatilized at a temperature lower than the curing temperature of the resin component, and then the temperature is raised to a temperature at which the resin component is cured, thereby forming an insulating coating without bubbles. it can.
  • the heating method for example, induction heating that heats the conductor by electromagnetic induction, radiant heating that heats the insulating paint by radiant heat of the heater, hot air heating that circulates hot air to heat the insulating paint, and the like can be adopted.
  • the conductor C is softened by the conductor softening treatment method and then the insulating coating is formed. Therefore, the conductor C is not oxidized and an insulated wire having high flexibility and conductivity can be manufactured. ..
  • the heater has the heat shield plate surrounding the cavity, but the heat shield plate may not surround the cavity.
  • the heat shield plate may not surround the cavity.
  • a certain effect can be obtained for improving the heating efficiency.
  • a configuration in which the heat shield plate is omitted is also intended by the present invention.
  • the carrier tube may be composed of only the magnetic body.
  • the conductor softening treatment device As the conductor softening treatment device, the case where the heat shield plate, the magnetic body, and the conductive wire are independently embedded in the carrier pipe has been described.
  • the conductive wire is embedded in the heat shield plate and the magnetic body. It is also possible to have a different configuration.
  • the conductor softening treatment device As the conductor softening treatment device, the case where the carrier pipe is configured to be divisible so as to open the cavity formed inside has been described, but the structure that the carrier pipe is divisible is not essential.
  • a conductor softening treatment device composed of an indivisible carrier pipe is also intended by the present invention.
  • the conductive wire is covered with insulation, but this is not an indispensable constituent requirement, and the conductive wire may not be covered with insulation.
  • insulation may be achieved by the heat shield plate.
  • the supply unit may be omitted in the conductor softening device. If the cooling tank is sufficiently large, the amount of dissolved oxygen in the cooling water in the cooling tank can be kept low for a certain period of time without supplying new cooling water from the supply unit.
  • the overflow mechanism may be omitted in the conductor softening device. If there is no excess supply of new cooling water, it is not necessary to discharge the cooling water from the cooling tank.Even when the cooling water is discharged from the cooling tank, a discharge passage is formed at the bottom of the cooling tank or a suction pump is used. Other means such as drawing out the cooling water may be used.
  • a deoxidizing unit may be provided in the cooling tank as a dissolved oxygen amount adjusting mechanism in place of the supplying unit.
  • a device for supplying an oxygen scavenger or a device for supplying nitrogen gas to the cooling tank, the amount of dissolved oxygen in the cooling water stored in the cooling tank can be kept low.
  • the dissolved oxygen amount adjusting mechanism may be not only automatically controlled by the control unit but also operated by an operator.
  • the amount of dissolved oxygen can be kept low for a certain period of time by previously adding an excess amount of oxygen scavenger to the cooling tank.
  • the cooling tank lid may be omitted.
  • the shape of the cooling tank may be designed so that the area of the liquid surface is small.
  • air blow may be omitted in the conductor softening processing device.
  • the heater uses a glass tube that extends in the conductor transport direction and has a cavity for transporting the conductor, and the heater faces the outside of the glass tube with the cavity therebetween.
  • the structure is such that two conductive wires are arranged.
  • the heater was configured to have no magnetic substance, and the length of the conductive wire (length in the carrying direction of the conductor) was 10 cm. Further, the conductive wire is wired so that the magnetic field is strengthened at the center of the plane of the cavity which is perpendicular to the transport direction.
  • the conductor is a rectangular copper wire (rectangular shape whose cross section has an area equivalent to a circle with a diameter of 3 mm), and the conductor transport speed was set to 15 m/min.
  • the amount of power supplied was adjusted so that the heating rate by the heater was 100° C./second, and the conductor was heated to 300° C.
  • the heating efficiency at this time is shown in Table 1.
  • the heater has a pair of magnetic bodies. No. In No. 2, except for the structure of this heater, The configuration is the same as that of 1.
  • the pair of magnetic bodies were arranged on the opposite sides of the cavities with the conductive wires sandwiched therebetween. That is, the magnetic flux direction is open (the magnetic substance distance T1 is infinite), and the magnetic substance distance T1 in the magnetic flux direction at the center of the cavity is longer than the magnetic substance distance T2 in the direction orthogonal to the magnetic flux direction.
  • the heater uses a carrier pipe that extends in the conductor carrying direction and has a cavity for carrying the conductor therein, and two conductive wires and four magnetic bodies are provided in the carrier pipe. It was configured to be embedded as shown in FIG. The distance T1 between magnetic bodies in the magnetic flux direction at the center of the cavity is made shorter than the distance T2 between magnetic bodies in the direction orthogonal to the magnetic flux direction.
  • the carrier tube was made of a heat-resistant resin as a main component, and the conductive wire had a length of 10 cm.
  • heating efficiency means the value obtained by multiplying the temperature rise of the conductor by the specific heat per unit length of the conductor, divided by the input power amount.
  • the heater has a magnetic body No. 2 and No.
  • the conductor softening treatment device of No. 3 has No.
  • the heating efficiency is higher than that of the conductor softening treatment device of No. 1. From this, it can be said that the heating efficiency of the conductor can be further increased by using the heater having the magnetic material.
  • the distance T1 between magnetic bodies in the magnetic flux direction at the center of the cavity is shorter than the distance T2 between magnetic bodies in the direction orthogonal to the magnetic flux direction.
  • the conductor softening treatment apparatus of No. 3 has No. 1 in which T1 is longer than T2.
  • the heating efficiency is higher than that of the second conductor softening treatment device. Therefore, the heating efficiency of the conductor is further improved by making the distance between magnetic bodies in the magnetic flux direction at the center of the cavity in the plane perpendicular to the transport direction shorter than the distance between magnetic bodies in the direction orthogonal to the magnetic flux direction. It can be said that you can.

Abstract

A conductor softening processing device according to one aspect of the present invention continuously heats and cools a wire-shaped conductor, and comprises: a conveyance mechanism that continuously conveys the conductor in the axial direction thereof; a heater that heats the conductor conveyed by the conveyance mechanism; a cooling tank that stores a cooling water, in which the conductor that was heated by the heater is submerged; and a dissolved oxygen quantity regulation mechanism that keeps the quantity of dissolved oxygen in the cooling water stored in the cooling tank within a predetermined set range, wherein the heater has a conveyance pipe that extends in the conveyance direction of the conductor and has a cavity formed in an interior section thereof, said cavity being for conveying the conductor, and a plurality of conductive wires that are embedded within the conveyance pipe along the conveyance direction and are wired such that a magnetic field becomes stronger at the center of a plane that is perpendicular to the conveyance direction in the cavity.

Description

導体軟化処理装置及び導体軟化処理方法Conductor softening treatment device and conductor softening treatment method
 本開示は、導体軟化処理装置及び導体軟化処理方法に関する。 The present disclosure relates to a conductor softening treatment device and a conductor softening treatment method.
 特許文献1(特開2016-79436号公報)には、導体の酸化を抑制できる導体軟化処理装置が記載されている。この導体軟化処理装置は、溶存酸素量が予め定められる設定範囲内の冷却水に加熱後の導体を浸漬することによって、加熱状態から冷却される導体の周囲の酸素量を低減して、導体の酸化を抑制する。 Patent Document 1 (Japanese Unexamined Patent Publication No. 2016-79436) describes a conductor softening treatment device capable of suppressing oxidation of a conductor. This conductor softening treatment apparatus reduces the amount of oxygen around the conductor to be cooled from the heated state by immersing the conductor after heating in cooling water in which the dissolved oxygen amount is within a predetermined setting range, and Inhibits oxidation.
特開2016-79436号公報JP, 2016-79436, A
 本発明の一態様に係る導体軟化処理装置は、線状の導体を連続的に加熱及び冷却する導体軟化処理装置であって、上記導体をその軸方向に連続的に搬送する送り機構と、上記送り機構により搬送される上記導体を加熱するヒーターと、上記ヒーターにより加熱された上記導体を浸漬する冷却水を貯留する冷却槽と、上記冷却槽に貯留されている冷却水の溶存酸素量を予め定められる設定範囲内に維持する溶存酸素量調節機構とを備え、上記ヒーターが、導体の搬送方向に延び、上記導体を搬送するための空洞がその内部に形成されている搬送管と、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞の上記搬送方向に垂直な面内の中心で磁場が強まるように配線される複数の導電線とを有する。 A conductor softening treatment apparatus according to an aspect of the present invention is a conductor softening treatment apparatus that continuously heats and cools a linear conductor, and a feeding mechanism that continuously conveys the conductor in its axial direction, A heater for heating the conductor conveyed by the feeding mechanism, a cooling tank for storing cooling water in which the conductor heated by the heater is immersed, and a dissolved oxygen amount of the cooling water stored in the cooling tank are set in advance. And a carrier pipe having a dissolved oxygen amount adjusting mechanism for maintaining the temperature within a predetermined set range, wherein the heater extends in the conductor transport direction and a cavity for transporting the conductor is formed therein, and the transport pipe. A plurality of conductive lines embedded along the direction in the carrier pipe and wired so that the magnetic field is strengthened at the center of the plane of the cavity perpendicular to the carrier direction.
 本発明の別の一態様に係る導体軟化処理方法は、線状の導体を連続的に加熱及び冷却する導体軟化処理方法であって、本発明の導体軟化処理装置を用い、上記導体をその軸方向に連続的に搬送する工程と、搬送される上記導体を加熱する工程と、加熱された上記導体を冷却水への浸漬により冷却する工程と、上記冷却水の溶存酸素量を予め定められる設定範囲内に維持する工程とを備える。 A conductor softening treatment method according to another aspect of the present invention is a conductor softening treatment method of continuously heating and cooling a linear conductor, wherein the conductor softening treatment device is used and the conductor is Direction, the step of continuously conveying the conductor, the step of heating the conductor to be conveyed, the step of cooling the heated conductor by immersion in cooling water, and the amount of dissolved oxygen in the cooling water set in advance. Maintaining within the range.
図1は、本発明の一実施形態に係る導体軟化処理装置の構成を示す模式図である。FIG. 1 is a schematic diagram showing the configuration of a conductor softening treatment apparatus according to an embodiment of the present invention. 図2は、図1に示す導体軟化処理装置のヒーターのA-A線での模式的断面図である。FIG. 2 is a schematic cross-sectional view taken along line AA of the heater of the conductor softening treatment device shown in FIG. 図3は、図2に示すヒーターの磁性体を分割した状態を示す模式的断面図である。FIG. 3 is a schematic cross-sectional view showing a state where the magnetic body of the heater shown in FIG. 2 is divided.
[本開示が解決しようとする課題]
 特許文献1には、導体を加熱するヒーターとして、透明ガラス等により構成される管状部材に導体を挿通し、管状部材の外側に配置される誘導加熱コイルにより加熱する構成が記載されている。このような構成において加熱効率を高めるには、コイルを導体に近づける方法が有効である。しかしながら、コイルを導体に近づけるためには管状部材を細くする必要がある。このため、管状部材が破損し易い、管状部材に導体を挿通し難い、管内部の状態確認や清掃が困難となるといった弊害が生じ易い。従って、上記従来のヒーターの構成では管状部材を細くしてコイルを導体に近づけることには限度があり、加熱効率を高めることが難しい。
[Problems to be solved by the present disclosure]
Patent Document 1 describes, as a heater for heating a conductor, a configuration in which a conductor is inserted into a tubular member made of transparent glass or the like and heated by an induction heating coil arranged outside the tubular member. In order to improve the heating efficiency in such a configuration, it is effective to bring the coil close to the conductor. However, it is necessary to make the tubular member thinner in order to bring the coil closer to the conductor. For this reason, the tubular member is likely to be damaged, it is difficult to insert the conductor into the tubular member, and it is difficult to check the state of the inside of the tube and to clean the tubular member. Therefore, in the above-mentioned conventional heater configuration, there is a limit to making the tubular member thin and bringing the coil close to the conductor, and it is difficult to improve heating efficiency.
 本開示は、上述のような事情に基づいてなされたものであり、装置の破損を抑止しつつ、導体の加熱効率を高められるヒーターを有する導体軟化処理装置及びこの導体軟化処理装置を用いた導体軟化処理方法の提供を目的とする。 The present disclosure has been made based on the above circumstances, and a conductor softening treatment device having a heater capable of enhancing the heating efficiency of a conductor while suppressing damage to the device and a conductor using the conductor softening treatment device. It is intended to provide a softening treatment method.
[本開示の効果]
 本開示の導体軟化処理装置のヒーターは、装置の破損を抑止しつつ、導体の加熱効率を高められる。従って、本開示の導体軟化処理装置を用いた導体軟化処理方法は、導体軟化処理装置の破損を抑止しつつ導体軟化処理装置のエネルギー効率を高められるので、製造効率に優れる。
[Effect of the present disclosure]
The heater of the conductor softening treatment device of the present disclosure can improve the heating efficiency of the conductor while suppressing damage to the device. Therefore, the conductor softening treatment method using the conductor softening treatment device of the present disclosure can improve the energy efficiency of the conductor softening treatment device while suppressing damage to the conductor softening treatment device, and thus is excellent in manufacturing efficiency.
[本発明の実施形態の説明]
 本発明の一態様に係る導体軟化処理装置は、線状の導体を連続的に加熱及び冷却する導体軟化処理装置であって、上記導体をその軸方向に連続的に搬送する送り機構と、上記送り機構により搬送される上記導体を加熱するヒーターと、上記ヒーターにより加熱された上記導体を浸漬する冷却水を貯留する冷却槽と、上記冷却槽に貯留されている冷却水の溶存酸素量を予め定められる設定範囲内に維持する溶存酸素量調節機構とを備え、上記ヒーターが、導体の搬送方向に延び、上記導体を搬送するための空洞がその内部に形成されている搬送管と、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞の上記搬送方向に垂直な面内の中心で磁場が強まるように配線される複数の導電線とを有する。
[Description of Embodiments of the Present Invention]
A conductor softening treatment apparatus according to an aspect of the present invention is a conductor softening treatment apparatus that continuously heats and cools a linear conductor, and a feeding mechanism that continuously conveys the conductor in its axial direction, A heater for heating the conductor conveyed by the feeding mechanism, a cooling tank for storing cooling water in which the conductor heated by the heater is immersed, and a dissolved oxygen amount of the cooling water stored in the cooling tank are set in advance. And a carrier pipe having a dissolved oxygen amount adjusting mechanism for maintaining the temperature within a predetermined set range, wherein the heater extends in the conductor transport direction and a cavity for transporting the conductor is formed therein, and the transport pipe. A plurality of conductive lines embedded along the direction in the carrier pipe and wired so that the magnetic field is strengthened at the center of the plane of the cavity perpendicular to the carrier direction.
 当該導体軟化処理装置は、溶存酸素量が予め定められる設定範囲内の冷却水に加熱後の導体を浸漬することによって、加熱状態から冷却される導体の周囲の酸素量を低減して、導体の酸化を抑制することができる。また、当該導体軟化処理装置のヒーターでは、導体を搬送するための空洞が搬送管の内部に形成され、さらに導体を加熱する磁場を発生する導電線が導体の搬送方向に沿って搬送管内に埋設されている。このため、当該導体軟化処理装置のヒーターは、導電線を導体に近づけて加熱効率を向上した構成としても搬送管の肉厚を薄くする必要がないので、搬送管の破損が抑止される。従って、当該導体軟化処理は、装置の破損を抑止しつつ、導体の加熱効率を高められる。 The conductor softening treatment device reduces the amount of oxygen around the conductor to be cooled from the heated state by immersing the conductor after heating in the cooling water in which the dissolved oxygen amount is within a predetermined setting range. Oxidation can be suppressed. Further, in the heater of the conductor softening processing apparatus, a cavity for carrying the conductor is formed inside the carrying pipe, and a conductive wire for generating a magnetic field for heating the conductor is embedded in the carrying pipe along the carrying direction of the conductor. Has been done. Therefore, even if the heater of the conductor softening apparatus is configured to bring the conductive wire closer to the conductor to improve the heating efficiency, it is not necessary to reduce the wall thickness of the carrier pipe, so that damage to the carrier pipe is suppressed. Therefore, the conductor softening treatment can improve the heating efficiency of the conductor while suppressing damage to the device.
 上記搬送管の主成分が耐熱樹脂であるとよい。このように上記搬送管の主成分を導電性を有さない耐熱樹脂とすることで、導体の加熱効率を維持しつつ、搬送管の破損抑止効果を高めることができる。また、搬送管の耐熱効果をさらに高められるので、ヒーターを高温となる導体からの熱に容易に耐え得るようにできる。 ㆍIt is recommended that the main component of the above-mentioned carrier pipe is heat-resistant resin. In this way, by using a heat-resistant resin having no conductivity as the main component of the carrier pipe, it is possible to enhance the effect of suppressing damage to the carrier pipe while maintaining the heating efficiency of the conductor. Further, since the heat resistance effect of the carrier pipe can be further enhanced, the heater can easily withstand the heat from the conductor which becomes hot.
 上記ヒーターが、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む遮熱板を有するとよい。このように上記ヒーターを、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む遮熱板を有する構成とすることで、導体の加熱効率をさらに高めることができる。 The heater may be embedded in the transfer pipe along the transfer direction and may have a heat shield plate surrounding the cavity. In this way, the heater is embedded in the transfer pipe along the transfer direction and has the heat shield plate surrounding the cavity, whereby the heating efficiency of the conductor can be further increased.
 上記遮熱板の平均厚さとしては、0.5mm以上5mm以下が好ましい。このように上記遮熱板の平均厚さを上記範囲内とすることで、導電線による導体の加熱効率を維持しつつ、遮熱効果を高めることができる。 The average thickness of the heat shield plate is preferably 0.5 mm or more and 5 mm or less. In this way, by setting the average thickness of the heat shield plate within the above range, it is possible to enhance the heat shield effect while maintaining the heating efficiency of the conductor by the conductive wire.
 上記ヒーターが、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む磁性体を有するとよい。このように上記ヒーターを、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む磁性体を有する構成とすることで、空洞の磁場がより高められるので、導体の加熱効率をさらに高めることができる。 The heater is preferably embedded in the transfer tube along the transfer direction and has a magnetic body surrounding the cavity. In this way, the heater is embedded in the transfer tube along the transfer direction and has the magnetic body surrounding the cavity, so that the magnetic field of the cavity is further increased, and thus the heating efficiency of the conductor is further increased. be able to.
 上記搬送方向に垂直な面内での上記空洞の中心における磁束方向の磁性体間距離が、上記磁束方向と直交する方向の磁性体間距離より短いとよい。このように上記搬送方向に垂直な面内での上記空洞の中心における磁束方向の磁性体間距離を、上記磁束方向と直交する方向の磁性体間距離より短くすることで、上記空洞内の磁場がより高められるので、導体の加熱効率をさらに高めることができる。 The distance between magnetic bodies in the magnetic flux direction at the center of the cavity in a plane perpendicular to the transport direction is preferably shorter than the distance between magnetic bodies in the direction orthogonal to the magnetic flux direction. Thus, by making the distance between magnetic bodies in the magnetic flux direction at the center of the cavity in the plane perpendicular to the transport direction shorter than the distance between magnetic bodies in the direction orthogonal to the magnetic flux direction, the magnetic field in the cavity is reduced. Is further increased, the heating efficiency of the conductor can be further increased.
 上記搬送管が、上記空洞を開放するように分割可能に構成されるとよい。このように上記搬送管を、上記空洞を開放するように分割可能に構成することで、上記空洞への導体の挿通を容易化できるほか、上記空洞内の状態確認や清掃を容易化できる。 ㆍIt is preferable that the carrier pipe is configured to be separable so as to open the cavity. In this way, by configuring the transfer pipe so that it can be divided so as to open the cavity, it is possible to facilitate insertion of the conductor into the cavity, and it is possible to facilitate confirmation of the inside of the cavity and cleaning.
 上記導電線が絶縁被覆されているとよい。このように上記導電線を絶縁被覆することで、上記磁性体を分割可能な構成とした場合においても搬送管内部への水の浸入等により複数の導電線間で電気的な短絡が生じることを抑止できる。従って、当該導体軟化処理装置の破損をさらに抑止できる。  It is recommended that the conductive wires be covered with insulation. By insulatingly coating the conductive wires in this manner, even when the magnetic body is configured to be dividable, an electrical short circuit may occur between a plurality of conductive wires due to water ingress into the carrier tube. Can be deterred. Therefore, damage to the conductor softening device can be further suppressed.
 上記空洞の長さとしては、50mm以上1500mm以下が好ましい。上記空洞の長さを上記範囲内とすることで、当該導体軟化処理装置の大型化を抑止しつつ、導体の周囲の酸素量を低減して、導体の酸化抑制効果を高められる。 The length of the cavity is preferably 50 mm or more and 1500 mm or less. By setting the length of the cavity within the above range, it is possible to suppress an increase in the size of the conductor softening treatment device, reduce the amount of oxygen around the conductor, and enhance the effect of suppressing the oxidation of the conductor.
 本発明の別の一態様に係る導体軟化処理方法は、線状の導体を連続的に加熱及び冷却する導体軟化処理方法であって、本発明の導体軟化処理装置を用い、上記導体をその軸方向に連続的に搬送する工程と、搬送される上記導体を加熱する工程と、加熱された上記導体を冷却水への浸漬により冷却する工程と、上記冷却水の溶存酸素量を予め定められる設定範囲内に維持する工程とを備える。 A conductor softening treatment method according to another aspect of the present invention is a conductor softening treatment method of continuously heating and cooling a linear conductor, wherein the conductor softening treatment device is used and the conductor is Direction, the step of continuously conveying the conductor, the step of heating the conductor to be conveyed, the step of cooling the heated conductor by immersion in cooling water, and the amount of dissolved oxygen in the cooling water set in advance. Maintaining within the range.
 当該導体軟化処理方法は、本発明の導体軟化処理装置を用いるので、導体軟化処理装置の破損を抑止しつつ導体軟化処理装置のエネルギー効率を高められる。従って、当該導体軟化処理方法は、製造効率に優れる。 Since the conductor softening treatment method uses the conductor softening treatment device of the present invention, the energy efficiency of the conductor softening treatment device can be enhanced while suppressing damage to the conductor softening treatment device. Therefore, the conductor softening method is excellent in manufacturing efficiency.
 ここで、「溶存酸素量」とは、JIS-K-0101:1998に準拠して測定される値である。「主成分」とは、最も含有量が多い成分をいい、例えば含有量が50質量%以上の成分をいう。また、「平均厚さ」とは、任意の10点で測定される厚さの平均値を指す。 Here, the “dissolved oxygen amount” is a value measured according to JIS-K-0101:1998. The "main component" means a component having the largest content, for example, a component having a content of 50% by mass or more. Further, the “average thickness” refers to the average value of the thickness measured at any 10 points.
[本発明の実施形態の詳細]
 以下、本発明に係る導体軟化処理装置及び導体軟化処理方法の実施形態について図面を参照しつつ詳説する。
[Details of the embodiment of the present invention]
Hereinafter, embodiments of a conductor softening treatment apparatus and a conductor softening treatment method according to the present invention will be described in detail with reference to the drawings.
〔導体軟化処理装置〕
 図1に示す導体軟化処理装置は、線状の導体Cを連続的に加熱及び冷却する。この導体軟化処理装置は、導体Cをその軸方向に連続的に搬送する送り機構1と、この送り機構1により搬送される導体Cを加熱するヒーター2と、このヒーター2により加熱された導体Cを浸漬する冷却水Wを貯留する冷却槽3と、冷却槽3に貯留されている冷却水Wの溶存酸素量を予め定められる設定範囲内に維持する溶存酸素量調節機構4と、導体Cにエアーを吹き付けて表面に付着している水分を除去するエアーブロー5とを備える。
[Conductor softening device]
The conductor softening treatment device shown in FIG. 1 continuously heats and cools the linear conductor C. This conductor softening apparatus includes a feeding mechanism 1 that continuously conveys the conductor C in the axial direction thereof, a heater 2 that heats the conductor C that is conveyed by the feeding mechanism 1, and a conductor C that is heated by the heater 2. The cooling tank 3 that stores the cooling water W in which the water is immersed, the dissolved oxygen amount adjusting mechanism 4 that maintains the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 within a predetermined setting range, and the conductor C An air blower 5 is provided for blowing air to remove water adhering to the surface.
<導体>
 当該導体軟化処理装置において軟化処理される導体Cとしては、特に限定されないが、例えば銅線、銅合金線、錫めっき銅線、アルミニウム線、アルミニウム合金線、鋼心アルミニウム線、カッパーフライ線、ニッケルめっき銅線、銀めっき銅線、銅覆アルミニウム線等が挙げられ、典型的には銅線とされる。導体Cの平均断面積としては、特に限定されないが、例えば0.01mm以上10mm以下とされる。また、導体Cの断面形状としては、特に限定されず、例えば円形状や長方形状とされる。
<conductor>
The conductor C to be softened in the conductor softening device is not particularly limited, but for example, copper wire, copper alloy wire, tin-plated copper wire, aluminum wire, aluminum alloy wire, steel core aluminum wire, copper fly wire, nickel. Examples of the copper wire include a plated copper wire, a silver-plated copper wire, and a copper-clad aluminum wire, and typically a copper wire. The average cross-sectional area of the conductor C is not particularly limited, but is, for example, 0.01 mm 2 or more and 10 mm 2 or less. Moreover, the cross-sectional shape of the conductor C is not particularly limited, and may be circular or rectangular, for example.
<送り機構>
 送り機構1は、導体Cが架け渡される複数のガイドシーブ(プーリー)を含み、導体Cを矢印Dで示す一定の方向に搬送するよう構成される。図1の送り機構1では、搬送方向の上流側から第1ガイドシーブ11、第2ガイドシーブ12及び第3ガイドシーブ13の3つのガイドシーブにより構成されている。上流側の第1ガイドシーブ11及び下流側の第3ガイドシーブ13が冷却槽3の上方に配設され、中間の第2ガイドシーブ12が冷却槽3の中に配設されることにより、送り機構1は、冷却槽3に貯留されている冷却水Wの中を通過させるよう導体Cを搬送する。好ましくは、送り機構1は、冷却槽3に貯留されている冷却水Wに鉛直方向下向きに進入するよう導体Cを搬送する。
<Feeding mechanism>
The feeding mechanism 1 includes a plurality of guide sheaves (pulleys) on which the conductor C is bridged, and is configured to convey the conductor C in a constant direction indicated by an arrow D. The feed mechanism 1 of FIG. 1 is configured by three guide sheaves, a first guide sheave 11, a second guide sheave 12, and a third guide sheave 13 from the upstream side in the transport direction. The first guide sheave 11 on the upstream side and the third guide sheave 13 on the downstream side are arranged above the cooling tank 3, and the second guide sheave 12 in the middle is arranged in the cooling tank 3. The mechanism 1 conveys the conductor C so as to pass through the cooling water W stored in the cooling tank 3. Preferably, the feed mechanism 1 conveys the conductor C so as to enter the cooling water W stored in the cooling tank 3 downward in the vertical direction.
 送り機構1による導体Cの搬送速度としては、特に限定されないが、例えば1m/min以上1000m/min以下、典型的には5m/min以上100m/min以下とされる。 The feeding speed of the conductor C by the feeding mechanism 1 is not particularly limited, but is, for example, 1 m/min or more and 1000 m/min or less, typically 5 m/min or more and 100 m/min or less.
<ヒーター>
 ヒーター2は、図1から図3に示すように、導体Cの搬送方向に延びる搬送管21と、上記搬送方向に沿って搬送管21内に埋設される複数の導電線22、遮熱板23及び磁性体24とを有する。
<Heater>
As shown in FIGS. 1 to 3, the heater 2 includes a transport pipe 21 extending in the transport direction of the conductor C, a plurality of conductive wires 22 embedded in the transport pipe 21 along the transport direction, and a heat shield plate 23. And a magnetic body 24.
(搬送管)
 搬送管21は、導体Cを搬送するための空洞21aがその内部に形成されている。この空洞21aの中で、導体Cは加熱された後、冷却水Wによって冷却される。加熱状態の導体Cが冷却水Wに浸漬されると、冷却水Wが導体Cの熱を奪い取って水蒸気となる。このようにして空洞21aの中で発生した水蒸気は、空洞21a内を上昇し、空洞21a内に存在する酸素を含む空気を押し出す。これにより、加熱状態の導体Cへの酸素の供給が遮断され、導体Cの酸化が抑制される。
(Conveyor tube)
The carrier pipe 21 has a cavity 21a for carrying the conductor C formed therein. In the cavity 21a, the conductor C is heated and then cooled by the cooling water W. When the conductor C in the heated state is immersed in the cooling water W, the cooling water W takes away the heat of the conductor C and becomes steam. The water vapor thus generated in the cavity 21a rises in the cavity 21a and pushes out the oxygen-containing air present in the cavity 21a. As a result, the supply of oxygen to the conductor C in a heated state is cut off, and the oxidation of the conductor C is suppressed.
 搬送管21の内部に形成される空洞21aの横断面形状は、特に限定されないが、例えば図2に示すような方形状や円形状とすることができる。また、空洞21aは、搬送管21の横断面の略中央、つまり空洞21aの横断面(上記搬送方向に垂直な面)の中心Mが搬送管21の横断面の中心と一致するように配設されることが好ましい。なお、搬送管21の横断面と空洞21aの横断面とは相似形であってもよいが、異なる形状であってもよい。 The cross-sectional shape of the cavity 21a formed inside the carrier pipe 21 is not particularly limited, but may be, for example, a square shape or a circular shape as shown in FIG. The cavity 21a is arranged so that the center M of the cross section of the transfer tube 21, that is, the center M of the cross section of the cavity 21a (the surface perpendicular to the transfer direction) coincides with the center of the cross section of the transfer tube 21. Preferably. The cross-section of the carrier pipe 21 and the cross-section of the cavity 21a may have similar shapes, but may have different shapes.
 空洞21aはその内側を導体Cが搬送されるので、空洞21aの横断面は、少なくとも導体Cの最大横断面が包含できる大きさとされる。導体Cの最大横断面積に対する空洞21aの横断面積の比の下限としては、2倍が好ましく、4倍がより好ましい。一方、上記横断面積の比の上限としては、20倍が好ましく、10倍がより好ましい。上記横断面積の比が上記下限未満であると、導体Cが空洞21aの内壁に接触することにより導体Cが損傷したり軟化処理が不均一となったりするおそれがある。逆に、上記横断面積の比が上記上限を超えると、搬送管21内に埋設される複数の導電線22を導体Cに近接配置することが難しくなるため、導体Cの加熱効率が十分に高められないおそれがあるほか、水蒸気による酸素の排除が不十分となるおそれがある。なお、空洞21aは、例えば図2に示すように、その内壁の一部又は全部が搬送管21に埋設される遮熱板23等で構成されることがあるが、空洞21aの横断面積は、その構成要素に関わらず内壁で囲まれる空間の面積を指す。 Since the conductor C is transported inside the cavity 21a, the cross section of the cavity 21a is sized so as to include at least the maximum cross section of the conductor C. The lower limit of the ratio of the cross-sectional area of the cavity 21a to the maximum cross-sectional area of the conductor C is preferably 2 times and more preferably 4 times. On the other hand, the upper limit of the cross-sectional area ratio is preferably 20 times, more preferably 10 times. If the ratio of the above-mentioned cross-sectional areas is less than the above lower limit, the conductor C may come into contact with the inner wall of the cavity 21a, resulting in damage to the conductor C or uneven softening treatment. On the contrary, if the ratio of the cross-sectional area exceeds the upper limit, it becomes difficult to dispose the plurality of conductive wires 22 embedded in the carrier pipe 21 close to the conductor C, so that the heating efficiency of the conductor C is sufficiently increased. In addition, there is a risk that oxygen will not be removed sufficiently by water vapor. The cavity 21a may be composed of a heat shield plate 23 or the like in which a part or all of the inner wall is buried in the carrier pipe 21 as shown in FIG. 2, for example. It refers to the area of the space surrounded by the inner wall regardless of its constituent elements.
 上記搬送方向に垂直な面内での空洞21aの中心における磁束方向(図2のS方向で、詳細は後述する)の磁性体間距離(図2のT1)は、磁束方向Sと直交する方向の磁性体間距離(図2のT2)より短いことが好ましい。このように上記搬送方向に垂直な面内での空洞21aの中心Mにおける磁束方向Sの磁性体間距離T1を、磁束方向Sと直交する方向の磁性体間距離T2より短くすることで、空洞21a内の磁場がより高められるので、導体Cの加熱効率をさらに高めることができる。 The inter-magnetic body distance (T1 in FIG. 2) in the magnetic flux direction (S direction in FIG. 2, which will be described later in detail) at the center of the cavity 21a in the plane perpendicular to the transport direction is a direction orthogonal to the magnetic flux direction S. It is preferable to be shorter than the inter-magnetic substance distance (T2 in FIG. 2). As described above, by making the inter-magnetic-body distance T1 in the magnetic flux direction S at the center M of the cavity 21a in the plane perpendicular to the transport direction shorter than the inter-magnetic body distance T2 in the direction orthogonal to the magnetic flux direction S, Since the magnetic field in 21a is further enhanced, the heating efficiency of the conductor C can be further enhanced.
 空洞21aの長さ(空洞21aが形成されている搬送管21の長さ)としては、少なくとも導体Cの酸化し易い部分、つまり加熱状態である部分を空洞21aが取り囲むことができる長さとするとよい。つまり、空洞21aは、少なくとも下端が冷却水Wに浸漬され、上端は後述する導電線22の上端以上の高さに配置される。 The length of the cavity 21a (the length of the carrier pipe 21 in which the cavity 21a is formed) is preferably such that at least the portion of the conductor C that is easily oxidized, that is, the portion in the heated state, can be surrounded by the cavity 21a. .. That is, at least the lower end of the cavity 21a is immersed in the cooling water W, and the upper end is arranged at a height higher than the upper end of the conductive wire 22 described later.
 空洞21aの長さの下限としては、50mmが好ましく、100mmがより好ましい。一方、空洞21aの長さの上限としては、1500mmが好ましく、1000mmがより好ましい。空洞21aの長さが上記下限未満であると、導体Cが加熱状態となる位置における導体Cの雰囲気の酸素量を十分に低減できないおそれがある。逆に、空洞21aの長さが上記上限を超えると、当該導体軟化処理装置が不必要に大型化するおそれがある。 The lower limit of the length of the cavity 21a is preferably 50 mm, more preferably 100 mm. On the other hand, the upper limit of the length of the cavity 21a is preferably 1500 mm, more preferably 1000 mm. If the length of the cavity 21a is less than the above lower limit, the oxygen amount in the atmosphere of the conductor C at the position where the conductor C is in a heated state may not be sufficiently reduced. On the contrary, if the length of the cavity 21a exceeds the upper limit, the conductor softening device may unnecessarily increase in size.
 上述のように空洞21aの下端(ヒーター2の下端)は、冷却槽3に貯留されている冷却水W内に位置するように構成される。空洞21aの下端の構成としては、図1では、導電線22、遮熱板23及び磁性体24を含まず搬送管21のみを下方に延長することによって空洞21aの下端を冷却水W内に位置させる構成であるが、空洞21aの下端の構成はこれに限定されるものではなく、他の構成であってもよい。この他の構成としては、例えば導電線22のみを含まず搬送管21、遮熱板23及び磁性体24を下方に延長することによって空洞21aの下端を冷却水W内に位置させる構成などを挙げることができる。導電線22の下端を冷却水W内に位置させることもできるが、加熱効率の観点から導電線22の下端は冷却水Wの液面より上に位置することが好ましい。 As described above, the lower end of the cavity 21a (lower end of the heater 2) is configured to be located inside the cooling water W stored in the cooling tank 3. As the configuration of the lower end of the cavity 21 a, in FIG. 1, the lower end of the cavity 21 a is located inside the cooling water W by extending only the transport pipe 21 without including the conductive wire 22, the heat shield plate 23 and the magnetic body 24. However, the configuration of the lower end of the cavity 21a is not limited to this, and may have another configuration. As another configuration, for example, a configuration in which only the conductive wire 22 is not included and the lower end of the cavity 21a is located in the cooling water W by extending the transport pipe 21, the heat shield plate 23, and the magnetic body 24 downward, and the like are given. be able to. The lower end of the conductive wire 22 may be located in the cooling water W, but from the viewpoint of heating efficiency, the lower end of the conductive wire 22 is preferably located above the liquid surface of the cooling water W.
 上述の下端の構成としては、図1に示すように、導電線22、遮熱板23及び磁性体24を含まず搬送管21のみを下方に延長し、空洞21aの下端を冷却水W内に位置させる構成が好ましい。このような構成とする場合において、後述する導電線22の下端と冷却水Wの液面との距離の下限としては、0.01mが好ましく、0.05mがより好ましい。一方、導電線22の下端と冷却水Wの液面との距離の上限としては、1mが好ましく、0.7mがより好ましい。導体Cは、導電線22の下端より下方へ搬送された後も、ある程度温度が保たれ、焼鈍効果が持続する。その後、導体Cは、冷却水Wの液面下まで搬送され、急激に冷却される。このため、導電線22の下端と冷却水Wの液面との距離が上記下限未満であると、持続する焼鈍効果が減少し、加熱効率が低下するおそれがある。逆に、導電線22の下端と冷却水Wの液面との距離が上記上限を超えると、当該導体軟化処理装置が不必要に大型化するおそれがある。 As the configuration of the lower end described above, as shown in FIG. 1, only the carrier pipe 21 is extended downward without including the conductive wire 22, the heat shield plate 23, and the magnetic body 24, and the lower end of the cavity 21 a is placed in the cooling water W. Positioned configurations are preferred. In such a configuration, the lower limit of the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W described later is preferably 0.01 m, and more preferably 0.05 m. On the other hand, the upper limit of the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W is preferably 1 m, more preferably 0.7 m. Even after the conductor C is conveyed below the lower end of the conductive wire 22, the temperature is maintained to some extent and the annealing effect continues. Then, the conductor C is conveyed to below the liquid surface of the cooling water W, and is rapidly cooled. Therefore, if the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W is less than the above lower limit, the continuous annealing effect is reduced, and the heating efficiency may be reduced. On the contrary, if the distance between the lower end of the conductive wire 22 and the liquid surface of the cooling water W exceeds the upper limit, the conductor softening treatment device may unnecessarily increase in size.
 空洞21aの下端が冷却水Wに浸漬する部分の長さの下限としては、0.01mが好ましく、0.03mがより好ましい。一方、空洞21aの下端が冷却水Wに浸漬する部分の長さの上限としては、0.15mが好ましく、0.1mがより好ましい。空洞21aの下端が冷却水Wに浸漬する部分の長さが上記下限未満であると、導体Cの冷却水Wによる冷却により発生した水蒸気が空洞21aの外部に漏れ易くなり、導体Cの雰囲気の酸素量を十分に低減できないおそれがある。逆に、空洞21aの下端が冷却水Wに浸漬する部分の長さが上記上限を超えると、当該導体軟化処理装置が不必要に大型化するおそれがある。 The lower limit of the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W is preferably 0.01 m, more preferably 0.03 m. On the other hand, the upper limit of the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W is preferably 0.15 m, more preferably 0.1 m. When the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W is less than the above lower limit, water vapor generated by cooling the conductor C with the cooling water W easily leaks to the outside of the cavity 21a, and The amount of oxygen may not be reduced sufficiently. On the contrary, if the length of the portion where the lower end of the cavity 21a is immersed in the cooling water W exceeds the upper limit, the conductor softening treatment device may unnecessarily increase in size.
 上述のように空洞21aの上端は導電線22の上端以上の高さに配置される。空洞21aの上端と導電線22の上端との差の下限としては、0.01mが好ましく、0.03mがより好ましい。一方、空洞21aの上端と導電線22の上端との差の上限としては、0.15mが好ましく、0.1mがより好ましい。空洞21aの上端と導電線22の上端との差が上記下限未満であると、導体Cが加熱状態となる位置における導体Cの雰囲気の酸素量を十分に低減できないおそれがある。逆に、空洞21aの上端と導電線22の上端との差が上記上限を超えると、当該導体軟化処理装置が不必要に大型化するおそれがある。 As described above, the upper end of the cavity 21a is arranged at a height higher than the upper end of the conductive wire 22. The lower limit of the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is preferably 0.01 m, more preferably 0.03 m. On the other hand, the upper limit of the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is preferably 0.15 m, more preferably 0.1 m. If the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 is less than the above lower limit, the oxygen amount in the atmosphere of the conductor C at the position where the conductor C is heated may not be sufficiently reduced. On the contrary, if the difference between the upper end of the cavity 21a and the upper end of the conductive wire 22 exceeds the above upper limit, the conductor softening treatment device may unnecessarily increase in size.
 搬送管21の主成分としては、耐熱樹脂が好ましい。このように搬送管21の主成分を導電性を有さない耐熱樹脂とすることで、導体Cの加熱効率を維持しつつ、搬送管21の破損抑止効果を高めることができる。また、搬送管21の耐熱効果をさらに高められるので、ヒーター2を高温となる導体Cからの熱に容易に耐え得るようにできる。 Heat-resistant resin is preferable as the main component of the carrier pipe 21. In this way, by using the heat-resistant resin having no conductivity as the main component of the carrier pipe 21, it is possible to enhance the damage suppressing effect of the carrier pipe 21 while maintaining the heating efficiency of the conductor C. Further, since the heat resistance effect of the carrier pipe 21 can be further enhanced, the heater 2 can easily withstand the heat from the conductor C which becomes hot.
 上記耐熱樹脂としては、公知のエンジニアリングプラスチック、例えばポリカーボネート、ポリブチレンテレフタレート、ナイロン66、変性ポリフェニルエーテル、ポリフェニレンサルファイド、ポリエーテルエーテルケトン、ポリテトラフルオロエチレン、ポリエーテルイミド、ポリアミドイミド、ポリイミド等を挙げることができる。 Examples of the heat-resistant resin include known engineering plastics such as polycarbonate, polybutylene terephthalate, nylon 66, modified polyphenyl ether, polyphenylene sulfide, polyether ether ketone, polytetrafluoroethylene, polyetherimide, polyamideimide, and polyimide. be able to.
 上記耐熱樹脂の連続使用温度(UL)の下限としては、120℃が好ましく、200℃がより好ましい。上記耐熱樹脂のULが上記下限未満であると、搬送管21の耐熱が不十分となるおそれがある。一方、上記耐熱樹脂の連続使用温度(UL)の上限は、特に限定されず、高いほどよい。なお、「連続使用温度」とは、UL規格のUL746Bに規定される温度である。 The lower limit of the continuous use temperature (UL) of the heat resistant resin is preferably 120°C, more preferably 200°C. If the UL of the heat-resistant resin is less than the above lower limit, the heat resistance of the transport pipe 21 may be insufficient. On the other hand, the upper limit of the continuous use temperature (UL) of the heat resistant resin is not particularly limited, and the higher the better. The “continuous use temperature” is a temperature specified in UL standard UL746B.
 上記耐熱樹脂の靭性の下限としては、1kJ/mが好ましく、3kJ/mがより好ましい。上記耐熱樹脂の靭性が上記下限未満であると、搬送管21の破損抑止効果が不足するおそれがある。一方、上記耐熱樹脂の靭性の上限としては、特に限定されず、高いほどよい。ここで、「靭性」とは、JIS-K-7111-1:2012に記載のシャルピー衝撃特性の求め方に基づいて求められる数値をいう。 The lower limit of the toughness of the heat-resistant resin is preferably 1kJ / m 2, 3kJ / m 2 is more preferable. If the toughness of the heat-resistant resin is less than the above lower limit, the effect of suppressing damage to the transport pipe 21 may be insufficient. On the other hand, the upper limit of the toughness of the heat resistant resin is not particularly limited, and the higher the better. Here, the "toughness" means a numerical value obtained based on the method for obtaining the Charpy impact property described in JIS-K-7111-1:2012.
 なお、搬送管21の厚さは、ヒーター2の強度を維持しつつ、ヒーター2が過度に大きくならない範囲で適宜決定できる。 Note that the thickness of the carrier tube 21 can be appropriately determined within a range in which the heater 2 does not become excessively large while maintaining the strength of the heater 2.
(導電線)
 複数の導電線22は、交流を流すことで磁束密度の変化する磁場を発生させる。この磁場の変化により導体C内に渦電流が発生し、そのジュール損によって導体C自体が発熱する。複数の導電線22による導体Cの加熱温度としては、導体Cの材質等に応じて選択されるが、例えば300℃以上500℃以下とされる。
(Conductive wire)
The plurality of conductive lines 22 generate a magnetic field whose magnetic flux density changes by passing an alternating current. An eddy current is generated in the conductor C due to this change in the magnetic field, and the conductor C itself generates heat due to the Joule loss. The heating temperature of the conductor C by the plurality of conductive wires 22 is selected according to the material of the conductor C and the like, but is, for example, 300° C. or more and 500° C. or less.
 導電線22の本数は、特に限定されないが、磁場を強め易い2本又は4本とすることが好ましい。導電線22の本数を2本とする場合、図2に示すように、導電線22は空洞21aの中心Mを中心として点対称位置に配設するとよい。また、導電線22の本数を4本とする場合、導電線22は、磁束方向Sの両側に2本ずつ磁束方向Sに沿って空洞21aの中心Mを中心として点対称となるように配設するとよい。以下、図2のように2本の導電線22が配設されている場合を例に説明するが、導電線22の本数や配設位置を限定するものではなく、導電線22の本数や配設位置が異なる場合であっても同様である。 The number of the conductive wires 22 is not particularly limited, but it is preferable that the number of the conductive wires 22 is 2 or 4 so that the magnetic field can be easily strengthened. When the number of the conductive wires 22 is two, as shown in FIG. 2, it is preferable that the conductive wires 22 are arranged at point symmetric positions with the center M of the cavity 21a as the center. Further, when the number of the conductive wires 22 is four, the conductive wires 22 are arranged on each side of the magnetic flux direction S such that two conductive wires 22 are point-symmetrical along the magnetic flux direction S about the center M of the cavity 21a. Good to do. Hereinafter, the case where two conductive wires 22 are arranged as shown in FIG. 2 will be described as an example, but the number and the position of the conductive wires 22 are not limited, and the number and the arrangement of the conductive wires 22 are not limited. The same applies when the installation positions are different.
 2本の導電線22は、空洞21aの上記搬送方向に垂直な面内の中心Mで磁場が強まるように配線されている。つまり、導電線22に加わる電圧は交流であるので、この交流電圧が正となった場合において、図2で空洞21aの中心Mの下側にある導電線22は紙面の下から上向きの電流が流れるように配線され、空洞21aの中心Mの上側にある導電線22は紙面の上から下向きの電流が流れるように配線されるとよい。このように配線を行うと、交流電圧が正となった場合に2本の導電線22の磁束が磁束方向Sの磁束を強める向きとなるので、空洞21aの中心Mで磁場が強まる。なお、上述の例では磁束方向Sを図2の右から左へ向かう向きに取ったが、逆に左から右へ向かう向きに取ることもできる。この場合は、上述とは逆に、空洞21aの中心Mの下側にある導電線22は紙面の上から下向きの電流が流れるように配線され、空洞21aの中心Mの上側にある導電線22は紙面の下から上向きの電流が流れるように配線される。 The two conductive wires 22 are laid out so that the magnetic field is strengthened at the center M of the cavity 21a in the plane perpendicular to the above-mentioned transport direction. That is, since the voltage applied to the conductive wire 22 is an alternating current, when the alternating voltage becomes positive, the conductive wire 22 below the center M of the cavity 21a in FIG. It is preferable that the conductive wire 22 that is wired so as to flow and that is located above the center M of the cavity 21a be such that a downward current flows from above the paper surface. With such wiring, the magnetic flux of the two conductive wires 22 tends to strengthen the magnetic flux in the magnetic flux direction S when the AC voltage becomes positive, so that the magnetic field strengthens at the center M of the cavity 21a. In the above example, the magnetic flux direction S is set from the right to the left in FIG. 2, but it may be set from the left to the right. In this case, contrary to the above, the conductive wire 22 below the center M of the cavity 21a is wired so that a downward current flows from above the paper surface, and the conductive wire 22 above the center M of the cavity 21a. Is wired so that an upward current flows from the bottom of the paper.
 導電線22は、電気の流れる導体部22aと、導体部22aの周囲を被覆する被覆部22bとを有することが好ましい。つまり、導電線22は絶縁被覆されていることが好ましい。このように導電線22を絶縁被覆することで、搬送管21を分割可能な構成とした場合においても搬送管21内部への水の浸入等により複数の導電線間で電気的な短絡が生じることを抑止できる。従って、当該導体軟化処理装置の破損をさらに抑止できる。なお、被覆部22bは、例えば耐熱性の樹脂チューブ等により構成することができる。 The conductive wire 22 preferably has a conductor portion 22a through which electricity flows and a covering portion 22b that covers the periphery of the conductor portion 22a. That is, it is preferable that the conductive wire 22 is covered with insulation. By insulatingly coating the conductive wires 22 in this way, even when the transport pipe 21 is configured to be dividable, an electrical short circuit may occur between a plurality of conductive wires due to infiltration of water into the transport pipe 21 or the like. Can be suppressed. Therefore, damage to the conductor softening device can be further suppressed. The covering portion 22b can be formed of, for example, a heat-resistant resin tube or the like.
 導体Cの加熱の均一性の観点から、複数の導電線22は、同じ長さとすることが好ましい。導電線22の長さは、導体Cが十分加熱可能なように決定されるが、具体的な長さとしては、例えば10cm以上200cm以下とされる。 From the viewpoint of heating uniformity of the conductor C, it is preferable that the plurality of conductive wires 22 have the same length. The length of the conductive wire 22 is determined so that the conductor C can be sufficiently heated, and the specific length is, for example, 10 cm or more and 200 cm or less.
 導電線22の導体部22aは、熱くなり過ぎないようにするため、その内部に冷却水を通水可能な管状とするとよい。このように導体部22aを管状とする場合、導体部22aの太さは、細くなり過ぎて冷却水の圧損が増大しないように、また太くなり過ぎて加熱効率が低下しないように、適宜決定される。また、被覆部22bの平均厚さは導体部22aと外部との絶縁性が担保されるように適宜決定される。 The conductor portion 22a of the conductive wire 22 is preferably tubular so that cooling water can pass through it in order to prevent it from becoming too hot. When the conductor portion 22a is tubular as described above, the thickness of the conductor portion 22a is appropriately determined so that the conductor 22a does not become too thin and the pressure loss of the cooling water does not increase, and that the conductor 22a does not become too thick and the heating efficiency decreases. It Further, the average thickness of the covering portion 22b is appropriately determined so as to ensure the insulation between the conductor portion 22a and the outside.
(遮熱板)
 遮熱板23は、空洞21aを取り囲む。このように遮熱板23を、空洞21aを取り囲むように配設することで、空洞21aから外部へ熱が拡散することを抑止し、導体Cの加熱効率を高めることができる。
(Heat shield plate)
The heat shield plate 23 surrounds the cavity 21a. By disposing the heat shield plate 23 so as to surround the cavity 21a in this manner, it is possible to prevent heat from diffusing from the cavity 21a to the outside and to improve the heating efficiency of the conductor C.
 遮熱板23の配設位置としては、加熱効率の向上効果の観点から、空洞21aに近いほど好ましく、導電線22より空洞21aに近い位置とすることがより好ましく、図2に示すように、空洞21aの側壁を構成する位置とすることがさらに好ましい。 From the viewpoint of improving the heating efficiency, the heat shield plate 23 is preferably located closer to the cavity 21a, more preferably closer to the cavity 21a than the conductive wire 22, and as shown in FIG. It is more preferable to set the position to form the side wall of the cavity 21a.
 遮熱板23は絶縁性を有する。これにより、遮熱板23は、埋設されている導電線22に対し絶縁板としても機能し、複数の導電線22間で電気的な短絡が生じることを抑止できる。従って、当該導体軟化処理装置の破損がさらに抑止される。 The heat shield plate 23 has an insulating property. As a result, the heat shield plate 23 also functions as an insulating plate for the buried conductive wire 22, and can prevent an electrical short circuit from occurring between the plurality of conductive wires 22. Therefore, damage to the conductor softening device is further suppressed.
 遮熱板23の平均厚さの下限としては、0.5mmが好ましく、0.7mmがより好ましい。一方、遮熱板23の平均厚さの上限としては、5mmが好ましく、3mmがより好ましい。遮熱板23の平均厚さが上記下限未満であると、遮熱効果が不足するおそれがある。逆に、遮熱板23の平均厚さが上記上限を超えると、導体Cの加熱効率を十分に高められないおそれがある。 The lower limit of the average thickness of the heat shield plate 23 is preferably 0.5 mm, more preferably 0.7 mm. On the other hand, the upper limit of the average thickness of the heat shield plate 23 is preferably 5 mm, more preferably 3 mm. If the average thickness of the heat shield plate 23 is less than the above lower limit, the heat shield effect may be insufficient. On the contrary, if the average thickness of the heat shield plate 23 exceeds the upper limit, the heating efficiency of the conductor C may not be sufficiently improved.
 遮熱板23の連続使用温度(UL)の下限としては、350℃が好ましく、500℃がより好ましい。遮熱板23のULが上記下限未満であると、遮熱効果が不足するおそれがある。一方、遮熱板23の連続使用温度(UL)の上限は、特に限定されず、高いほどよい。 The lower limit of the continuous use temperature (UL) of the heat shield plate 23 is preferably 350°C, more preferably 500°C. If the UL of the heat shield plate 23 is less than the above lower limit, the heat shield effect may be insufficient. On the other hand, the upper limit of the continuous use temperature (UL) of the heat shield plate 23 is not particularly limited, and the higher the better.
 遮熱板23の靭性の下限としては、0.5kJ/mが好ましく、1kJ/mがより好ましい。遮熱板23の靭性が上記下限未満であると、遮熱板23が破損し易くなるおそれがある。一方、遮熱板23の靭性の上限としては、特に限定されず、高いほどよい。 The toughness of the lower limit of the heat shield plate 23 is preferably 0.5kJ / m 2, 1kJ / m 2 is more preferable. If the toughness of the heat shield plate 23 is less than the above lower limit, the heat shield plate 23 may be easily damaged. On the other hand, the upper limit of the toughness of the heat shield plate 23 is not particularly limited, and the higher the better.
(磁性体)
 磁性体24は、空洞21aを取り囲む。磁性体24は、導電線22により誘起される磁場を強め、導体Cの加熱を促進する。具体的には、図2に示すように、磁束方向Sに平行な1対の磁性体24及び磁束方向に垂直な1対の磁性体24の合計4つの磁性体24により空洞21aが取り囲まれている。このようにヒーター2を、空洞21aを取り囲む磁性体24を有する構成とすることで、空洞21aの磁場がより高められるので、導体Cの加熱効率をさらに高めることができる。
(Magnetic material)
The magnetic body 24 surrounds the cavity 21a. The magnetic body 24 strengthens the magnetic field induced by the conductive wire 22 and promotes heating of the conductor C. Specifically, as shown in FIG. 2, the cavity 21a is surrounded by a total of four magnetic bodies 24, that is, a pair of magnetic bodies 24 parallel to the magnetic flux direction S and a pair of magnetic bodies 24 perpendicular to the magnetic flux direction. There is. By thus configuring the heater 2 to have the magnetic body 24 that surrounds the cavity 21a, the magnetic field of the cavity 21a can be further enhanced, so that the heating efficiency of the conductor C can be further enhanced.
 磁性体24の材料としては、特に限定されず、公知のフェライト等の材料を用いることができる。 The material of the magnetic body 24 is not particularly limited, and a known material such as ferrite can be used.
 磁性体24の個々の横断面形状は、特に限定されないが、例えば方形状(正方形状又は長方形状)などとできる。磁性体24の横断面の全体の大きさ(図2では4つの磁性体24を合計した大きさ)は、導体Cを十分に加熱できるように導体Cの材質等に応じて適宜決定される。 The shape of each cross section of the magnetic body 24 is not particularly limited, but can be, for example, a square shape (square shape or rectangular shape). The overall size of the cross section of the magnetic body 24 (the total size of the four magnetic bodies 24 in FIG. 2) is appropriately determined according to the material and the like of the conductor C so that the conductor C can be sufficiently heated.
 磁性体24は、図2に示すように、4つの磁性体24で取り囲まれる空間内に導電体22が位置するように配設することが好ましい。このように磁性体24を配設することで、磁性体24による導体Cの加熱効率向上効果を維持しつつ、導電線22を空洞21aに近づけられるので、導体Cの加熱効率がさらに高まる。 The magnetic body 24 is preferably arranged so that the conductor 22 is located in the space surrounded by the four magnetic bodies 24, as shown in FIG. By disposing the magnetic body 24 in this way, the conductive wire 22 can be brought close to the cavity 21a while maintaining the effect of improving the heating efficiency of the conductor C by the magnetic body 24, so that the heating efficiency of the conductor C is further increased.
(搬送管の分割)
 搬送管21は、空洞21aを開放するように分割可能に構成される。この分割により、空洞21aの一部が、上記搬送方向に沿って外部へ開放される。このように搬送管21を、空洞21aを開放するように分割可能に構成することで、空洞21aへの導体Cの挿通を容易化できるほか、空洞21a内の状態確認や清掃を容易化できる。
(Division of carrier pipe)
The carrier pipe 21 is dividable so as to open the cavity 21a. By this division, a part of the cavity 21a is opened to the outside along the carrying direction. By configuring the transport pipe 21 so that it can be divided so as to open the cavity 21a, it is possible to facilitate the insertion of the conductor C into the cavity 21a, and also to facilitate confirmation of the state inside the cavity 21a and cleaning.
 空洞21aの開放される部分の幅(上記搬送方向に垂直な方向の長さ)は、少なくとも導体Cを空洞21aに出し入れ可能な大きさとされ、空洞21a内の清掃等のメインテナンス性を考慮すれば空洞21aの最大幅とすることが好ましい。例えば、横断面が図2に示すような方形状の空洞21aを有する搬送管21であれば、図3に示すような姿勢に分割されることが好ましい。具体的には、上記搬送方向に垂直な面において、磁束方向Sと直交する空洞21aの内壁面の1つを含み、かつ複数の導電線22を含まない位置を通るような折れ線で、上記搬送方向に沿って切断される2つの部分に分割するとよい。 The width of the opened portion of the cavity 21a (the length in the direction perpendicular to the transport direction) is set to a size that allows at least the conductor C to be taken in and out of the cavity 21a, and in consideration of maintenance such as cleaning inside the cavity 21a. The maximum width of the cavity 21a is preferable. For example, in the case of the carrier tube 21 having a rectangular cavity 21a whose cross section is as shown in FIG. 2, it is preferable that the carrier tube 21 is divided into the postures as shown in FIG. Specifically, in the plane perpendicular to the transport direction, the transport line is a polygonal line that includes one of the inner wall surfaces of the cavity 21a orthogonal to the magnetic flux direction S and does not include the plurality of conductive lines 22. It may be divided into two parts that are cut along the direction.
 分割可能に構成される搬送管21の開閉方法は、閉じた状態で気密性を確保できる限り特に限定されないが、例えば耐熱ゴム等を材料とするシール材を用いる方法や、本体部と分割部とに係合機構を設ける方法などを挙げることができる。 The method of opening and closing the dividable carrier pipe 21 is not particularly limited as long as airtightness can be ensured in the closed state, but for example, a method of using a sealing material made of heat-resistant rubber or the like, or a main body portion and a dividing portion. There may be mentioned a method of providing an engaging mechanism in the.
<冷却槽>
 冷却槽3は、冷却水Wを貯留する上部が開放した水槽である。この冷却槽3は、ヒーター2に貫通される穴が形成された蓋体31により上部が封止されている。また、冷却槽3は、冷却水Wの水位を予定範囲に保つオーバーフロー機構32を有する。
<Cooling tank>
The cooling tank 3 is a water tank having an open upper portion for storing the cooling water W. The cooling tank 3 has an upper part sealed by a lid 31 having a hole formed through the heater 2. The cooling tank 3 also has an overflow mechanism 32 that keeps the water level of the cooling water W within a predetermined range.
 この冷却槽3の容量としては、特に限定されず、第2ガイドシーブ12の大きさ等に応じて選択される。冷却槽3を構成する材料としては、例えば金属、樹脂、ガラス等の一種又は複数種の組合せが用いられる。 The capacity of the cooling tank 3 is not particularly limited, and is selected according to the size of the second guide sheave 12 and the like. As a material forming the cooling tank 3, for example, one kind or a combination of plural kinds of metal, resin, glass and the like is used.
(冷却水)
 冷却水Wは、冷却槽3内にヒーター2の下端(空洞21aの下端)を浸漬するよう貯留される。
(Cooling water)
The cooling water W is stored in the cooling tank 3 so as to immerse the lower end of the heater 2 (the lower end of the cavity 21a).
 冷却槽3における導体Cの浸漬深さ、つまり冷却水Wの液面から冷却槽3内の第2ガイドシーブ12の下端までの垂直距離としては、導体Cの横断面積や搬送速度に応じて導体Cを十分に冷却できる深さとされる。 The immersion depth of the conductor C in the cooling tank 3, that is, the vertical distance from the liquid surface of the cooling water W to the lower end of the second guide sheave 12 in the cooling tank 3 depends on the cross-sectional area of the conductor C and the transport speed. The depth is set so that C can be sufficiently cooled.
(蓋体)
 蓋体31は、冷却槽3への空気の出入りを制限するが、冷却槽3内の圧力を大気圧と異ならせるほどの気密性は有しない。この蓋体31を構成する材料としては、例えば金属、樹脂、ガラス等の一種又は複数種の組合せが用いられる。
(Lid)
The lid 31 restricts the entry and exit of air to and from the cooling tank 3, but is not airtight enough to make the pressure in the cooling tank 3 different from the atmospheric pressure. As a material for forming the lid 31, for example, one kind or a combination of plural kinds of metal, resin, glass and the like is used.
(オーバーフロー機構)
 オーバーフロー機構32は、冷却槽3の水位が一定の高さ以上とならないよう、冷却水Wをオーバーフローさせる。当該導体軟化処理装置では、冷却槽3内の冷却水Wに雰囲気中の酸素が溶け込んで溶存酸素量が上昇すると、冷却槽3に後述する溶存酸素量調節機構4から溶存酸素量の小さい新しい冷却水Wが供給される。当該導体軟化処理装置は、このオーバーフロー機構32を有することにより、新しい冷却水Wが供給された際、古い冷却水Wを優先的にオーバーフローさせることで、冷却槽3内の冷却水Wの溶存酸素量を設定範囲内に維持することができる。
(Overflow mechanism)
The overflow mechanism 32 causes the cooling water W to overflow so that the water level in the cooling tank 3 does not exceed a certain height. In the conductor softening treatment device, when oxygen in the atmosphere is dissolved in the cooling water W in the cooling tank 3 and the dissolved oxygen amount rises, a new cooling with a small dissolved oxygen amount is performed in the cooling tank 3 from the dissolved oxygen amount adjusting mechanism 4 described later. Water W is supplied. The conductor softening treatment device has the overflow mechanism 32, so that when the new cooling water W is supplied, the old cooling water W is preferentially overflowed, so that the dissolved oxygen of the cooling water W in the cooling tank 3 is dissolved. The amount can be kept within the set range.
 このオーバーフロー機構32としては、冷却槽3の側壁に開口するパイプ等が用いられる。オーバーフロー機構32は、図1に示すように、冷却槽3の内部空間と外部との間をオーバーフローした冷却水Wによって隔離するトラップ32aを有してもよい。 As this overflow mechanism 32, a pipe or the like that opens to the side wall of the cooling tank 3 is used. As shown in FIG. 1, the overflow mechanism 32 may have a trap 32a that isolates the internal space of the cooling tank 3 from the outside by the overflowed cooling water W.
<溶存酸素量調節機構>
 溶存酸素量調節機構4は、冷却槽3に新しい冷却水Wを供給する供給部41と、冷却槽3に貯留されている冷却水Wの溶存酸素量を測定する溶存酸素量検出部42と、この溶存酸素量検出部42の検出値に基づいて供給部41の冷却水供給量を制御する制御部43と、供給部41が供給する冷却水Wの溶存酸素量を低減する脱酸素部44とを有する。
<Dissolved oxygen control mechanism>
The dissolved oxygen amount adjusting mechanism 4 includes a supply unit 41 that supplies new cooling water W to the cooling tank 3, and a dissolved oxygen amount detection unit 42 that measures the dissolved oxygen amount of the cooling water W stored in the cooling tank 3. A control unit 43 that controls the cooling water supply amount of the supply unit 41 based on the detection value of the dissolved oxygen amount detection unit 42, and a deoxidation unit 44 that reduces the dissolved oxygen amount of the cooling water W supplied by the supply unit 41. Have.
 この溶存酸素量調節機構4は、例えば溶存酸素量検出部42が冷却槽3に貯留されている冷却水Wの溶存酸素量を検出し、その検出値が予め設定される設定範囲の上限値を超えたとき、脱酸素部44により溶存酸素量を低減した新しい冷却水Wが供給部41から冷却槽3へ供給される。また、溶存酸素量調節機構4は、溶存酸素量検出部42の検出値が上記設定範囲の下限値未満となったとき、供給部41から冷却槽3への新しい冷却水Wの供給を停止する。これにより、冷却槽3に貯留されている冷却水Wの溶存酸素量は上記設定範囲内に維持される。また、溶存酸素量検出部42の検出値が上記設定範囲内の代表値となるよう、冷却水Wの供給量を調整してもよい。 In this dissolved oxygen amount adjusting mechanism 4, for example, the dissolved oxygen amount detection unit 42 detects the dissolved oxygen amount of the cooling water W stored in the cooling tank 3, and the detected value indicates the upper limit value of the preset range. When it exceeds, new cooling water W with the amount of dissolved oxygen reduced by the deoxidizing unit 44 is supplied from the supply unit 41 to the cooling tank 3. Further, the dissolved oxygen amount adjusting mechanism 4 stops the supply of the new cooling water W from the supply unit 41 to the cooling tank 3 when the detected value of the dissolved oxygen amount detection unit 42 becomes less than the lower limit value of the above setting range. .. As a result, the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 is maintained within the above set range. Further, the supply amount of the cooling water W may be adjusted so that the detection value of the dissolved oxygen amount detection unit 42 becomes a representative value within the above setting range.
 冷却槽3内の冷却水Wの溶存酸素量の上記設定範囲の下限値としては、0.1mg/Lが好ましく、0.3mg/Lがより好ましい。一方、上記設定範囲の上限値としては、6mg/Lが好ましく、3mg/Lがより好ましく、2mg/Lがさらに好ましく、1mg/Lが特に好ましい。冷却槽3内の冷却水Wの溶存酸素量を上記設定範囲の下限値に満たないようにするためには、大きな設備コスト及びランニングコストが必要となり、不経済となるおそれや、中途半端に酸化被膜が形成されることにより導体Cの表面の密着性が低くなるおそれがある。逆に、冷却槽3内の冷却水Wの溶存酸素量が上記上限を超えると、導体Cの酸化を十分に抑制できないおそれがある。つまり、冷却槽3内の冷却水Wの溶存酸素量は、大気開放状態の水の溶存酸素量より低い値に維持されることが好ましいが、小さければ小さいほど軟化処理後の導体C表面の密着性を向上できるというわけではない。従って、冷却槽3内の冷却水Wの溶存酸素量を上述の好ましい範囲内に維持することで軟化処理後の導体Cの表面の密着性を最大化することができる。なお、オペレーション及び制御上の問題がなければ、上記設定範囲の下限値は0mg/Lであってもよい。この場合、冷却槽3内の冷却水Wの溶存酸素量は、予め設定される設定値(上記設定範囲の上限に相当)以下でありさえすればよい。また、上記設定範囲の下限値は上限値と同じであってもよい。つまり、冷却槽3内の冷却水Wの溶存酸素量は、溶存酸素量調節機構4によって、設定値からの差が極力小さくなるよう調節されてもよい。 The lower limit value of the above-mentioned set range of the dissolved oxygen amount of the cooling water W in the cooling tank 3 is preferably 0.1 mg/L, more preferably 0.3 mg/L. On the other hand, the upper limit of the above setting range is preferably 6 mg/L, more preferably 3 mg/L, further preferably 2 mg/L, particularly preferably 1 mg/L. In order to prevent the amount of dissolved oxygen in the cooling water W in the cooling tank 3 from falling below the lower limit value of the above setting range, a large equipment cost and running cost are required, which may be uneconomical and may result in halfway oxidation. The adhesion of the surface of the conductor C may be lowered due to the formation of the coating film. On the contrary, if the amount of dissolved oxygen in the cooling water W in the cooling tank 3 exceeds the above upper limit, the oxidation of the conductor C may not be sufficiently suppressed. That is, the dissolved oxygen amount of the cooling water W in the cooling tank 3 is preferably maintained at a value lower than the dissolved oxygen amount of water in the air-opened state, but the smaller it is, the closer the conductor C surface adheres after the softening treatment. It is not possible to improve the sex. Therefore, by maintaining the dissolved oxygen amount of the cooling water W in the cooling tank 3 within the above-mentioned preferable range, the adhesion of the surface of the conductor C after the softening treatment can be maximized. The lower limit value of the above setting range may be 0 mg/L if there is no problem in operation and control. In this case, the dissolved oxygen amount of the cooling water W in the cooling tank 3 need only be a preset value (corresponding to the upper limit of the above setting range) or less. Further, the lower limit value of the setting range may be the same as the upper limit value. That is, the dissolved oxygen amount of the cooling water W in the cooling tank 3 may be adjusted by the dissolved oxygen amount adjusting mechanism 4 so that the difference from the set value becomes as small as possible.
(供給部)
 供給部41は、冷却槽3に新たな冷却水Wを供給する配管から形成され、冷却槽3に供給される冷却水Wの流量を調整する調整弁45を有する。
(Supply Department)
The supply unit 41 is formed from a pipe that supplies new cooling water W to the cooling tank 3, and has a regulating valve 45 that adjusts the flow rate of the cooling water W supplied to the cooling tank 3.
 供給部41が冷却水Wを供給する冷却槽3内の位置は、冷却槽3のオーバーフロー機構32から離れた位置とすることが好ましい。この配置により、供給部41から溶存酸素量が小さい新しい冷却水Wを供給することで、溶存酸素量が増加した古い冷却水Wがオーバーフローし、冷却槽3内の冷却水W全体として、溶存酸素量を減少させられる。 The position inside the cooling tank 3 where the supply unit 41 supplies the cooling water W is preferably a position away from the overflow mechanism 32 of the cooling tank 3. With this arrangement, by supplying new cooling water W having a small dissolved oxygen amount from the supply unit 41, old cooling water W having an increased dissolved oxygen amount overflows, and the entire cooling water W in the cooling tank 3 is dissolved oxygen. The amount can be reduced.
 さらに、供給部41は、冷却槽3に貯留する冷却水Wの中に開口する配管を介して新しい冷却水Wを供給することが好ましい。このように新しい冷却水Wを冷却槽3の内部に供給することにより、冷却水Wの液面の撹拌により液面上の空間に存在する酸素が冷却水Wに溶け込むことを防止できる。 Furthermore, it is preferable that the supply unit 41 supplies new cooling water W through a pipe that opens into the cooling water W stored in the cooling tank 3. By supplying the new cooling water W to the inside of the cooling tank 3 in this manner, it is possible to prevent the oxygen existing in the space above the liquid surface from dissolving into the cooling water W due to the stirring of the liquid surface of the cooling water W.
(溶存酸素量検出部)
 溶存酸素量検出部42は、冷却槽3内に貯留されている冷却水Wの溶存酸素量を検出し、検出信号として制御部43に送信する。この溶存酸素量検出部42としては、例えばJIS-K-0803:1995に準拠した溶存酸素自動計測器を用いることができる。
(Dissolved oxygen amount detector)
The dissolved oxygen amount detection unit 42 detects the dissolved oxygen amount of the cooling water W stored in the cooling tank 3 and sends it as a detection signal to the control unit 43. As the dissolved oxygen amount detection unit 42, for example, an automatic dissolved oxygen measuring device based on JIS-K-0803:1995 can be used.
 溶存酸素量検出部42の配設位置としては、供給部41から新しい冷却水Wが供給されることにより他の部分より溶存酸素量が小さくなり得る位置を避けることが好ましく、導体Cの酸化抑制に寄与する冷却水Wの溶存酸素量を測定できる位置、つまり導体Cが冷却水Wに進入する位置の近傍がより好ましい。 As the disposing position of the dissolved oxygen amount detection unit 42, it is preferable to avoid a position where the amount of dissolved oxygen may be smaller than that of other portions by supplying new cooling water W from the supply unit 41, and to suppress the oxidation of the conductor C. It is more preferable that the position where the dissolved oxygen amount of the cooling water W contributing to the measurement can be measured, that is, the vicinity of the position where the conductor C enters the cooling water W.
(制御部)
 制御部43は、溶存酸素量検出部42の検出値を予め定められる設定範囲内に維持するよう供給部41の調整弁45の開度を調節することにより、供給部41の冷却槽3への新しい冷却水Wの供給量を制御する。
(Control unit)
The control unit 43 adjusts the opening degree of the adjustment valve 45 of the supply unit 41 so as to maintain the detected value of the dissolved oxygen amount detection unit 42 within a predetermined setting range. The supply amount of new cooling water W is controlled.
 制御部43は、例えば汎用コンピューター、PIDコントローラー、シーケンサー等で構成することができる。また、その制御方法としては、例えばPID制御、比例制御、オンオフ制御、ファジィ(メンバーシップ関数)制御等が適用できる。 The control unit 43 can be composed of, for example, a general-purpose computer, a PID controller, a sequencer, or the like. As the control method, for example, PID control, proportional control, on/off control, fuzzy (membership function) control, or the like can be applied.
(脱酸素部)
 脱酸素部44は、例えば化学的脱酸素器、加熱脱酸素器、真空脱酸素器、逆浸透膜脱酸素器、窒素脱酸素器等によって構成される。
(Deoxidizer part)
The deoxidizing unit 44 is configured by, for example, a chemical deoxidizer, a heating deoxidizer, a vacuum deoxidizer, a reverse osmosis membrane deoxidizer, a nitrogen deoxidizer, and the like.
 上記化学的脱酸素器は、補給水に脱酸素剤を添加することで、化学反応により酸素を除去するものである。上記脱酸素剤としては、例えばヒドラジン、亜硫酸ナトリウム、天然有機化合物等が挙げられる。 The above chemical deoxidizer removes oxygen by a chemical reaction by adding a deoxidizer to the makeup water. Examples of the oxygen scavenger include hydrazine, sodium sulfite, and natural organic compounds.
 上記加熱脱酸素器は、補給水を加熱して沸騰させることによって溶存酸素を除去するものである。補給水を沸騰させる方法としては、補給水をヒーターで加熱する方法や補給水に蒸気を導入する方法等が挙げられる。 The above-mentioned heated deoxidizer removes dissolved oxygen by heating make-up water to boil. Examples of the method of boiling the makeup water include a method of heating the makeup water with a heater and a method of introducing steam into the makeup water.
 上記真空脱酸素器は、補給水を減圧することによって溶存酸素を除去するものである。溶存酸素の脱気を促進するため、補給水を噴霧してもよい。 The vacuum deoxidizer removes dissolved oxygen by decompressing the makeup water. Make-up water may be sprayed to promote degassing of dissolved oxygen.
 上記逆浸透膜脱酸素器は、酸素の透過を阻止する逆浸透膜を用いて、水を濾過することで溶存酸素量の小さい水を得るものである。 The above reverse osmosis membrane deoxidizer obtains water with a small amount of dissolved oxygen by filtering water using a reverse osmosis membrane that blocks the permeation of oxygen.
 上記窒素脱酸素器は、補給水に窒素ガスを気液接触させ、補給水中の溶存酸素を分圧の差により窒素ガス側に移動させるものである。 The above-mentioned nitrogen deoxidizer makes nitrogen gas vapor-liquid contact with the makeup water, and moves the dissolved oxygen in the makeup water to the nitrogen gas side due to the difference in partial pressure.
 以上のような脱酸素部44により補給水から酸素を除去して得られる新しい冷却水Wの溶存酸素量の下限としては、0.05mg/Lが好ましく、0.1mg/Lがより好ましい。一方、上記新しい冷却水Wの溶存酸素量の上限としては、2mg/Lが好ましく、1mg/Lがより好ましい。上記新しい冷却水Wの溶存酸素量を上記下限に満たないようにするためには、大きな設備コスト及びランニングコストが必要となり、不経済となるおそれがある。逆に、上記新しい冷却水Wの溶存酸素量が上記上限を超えると、冷却槽3内の冷却水Wの溶存酸素量を十分低減することができないおそれがある。 The lower limit of the dissolved oxygen amount of the new cooling water W obtained by removing oxygen from the makeup water by the deoxidizing unit 44 as described above is preferably 0.05 mg/L, more preferably 0.1 mg/L. On the other hand, the upper limit of the dissolved oxygen amount of the new cooling water W is preferably 2 mg/L, more preferably 1 mg/L. In order to prevent the amount of dissolved oxygen in the new cooling water W from falling below the lower limit, a large equipment cost and running cost are required, which may be uneconomical. On the contrary, if the amount of dissolved oxygen in the new cooling water W exceeds the upper limit, the amount of dissolved oxygen in the cooling water W in the cooling tank 3 may not be sufficiently reduced.
<エアーブロー>
 エアーブロー5は、冷却槽3から出てきた導体Cの表面に空気を吹き付けることにより、導体Cの表面に付着した水滴を払い落とす非接触式のワイパーである。このエアーブロー5は、導体Cの表面に吹き付けた空気が蓋体31の穴から冷却槽3の内部に入り込み易くならないよう、吹き付け方向や蓋体31からの離間距離を設定することが好ましい。
<Air blow>
The air blow 5 is a non-contact wiper that blows off air onto the surface of the conductor C coming out of the cooling tank 3 to wipe off water droplets adhering to the surface of the conductor C. In this air blow 5, it is preferable to set the blowing direction and the distance from the lid 31 so that the air blown on the surface of the conductor C does not easily enter the inside of the cooling tank 3 through the hole of the lid 31.
<利点>
 当該導体軟化処理装置は、溶存酸素量が予め定められる設定範囲内の冷却水Wに加熱後の導体Cを浸漬することによって、加熱状態から冷却される導体Cの周囲の酸素量を低減して、導体Cの酸化を抑制することができる。また、当該導体軟化処理装置のヒーター2では、導体Cを搬送するための空洞21aが搬送管21の内部に形成され、さらに導体Cを加熱する磁場を発生する導電線22が導体Cの搬送方向に沿って搬送管21内に埋設されている。このため、当該導体軟化処理装置のヒーター2は、導電線22を導体Cに近づけて加熱効率を向上した構成としても搬送管21の肉厚を薄くする必要がないので、搬送管21の破損が抑止される。従って、当該導体軟化処理は、装置の破損を抑止しつつ、導体Cの加熱効率を高められる。
<Advantages>
The conductor softening treatment apparatus reduces the amount of oxygen around the conductor C cooled from the heated state by immersing the conductor C after heating in the cooling water W in which the dissolved oxygen amount is within a predetermined setting range. The oxidation of the conductor C can be suppressed. Further, in the heater 2 of the conductor softening processing apparatus, a cavity 21a for transporting the conductor C is formed inside the transport pipe 21, and a conductive wire 22 for generating a magnetic field for heating the conductor C is further provided in the transport direction of the conductor C. Is embedded in the carrier pipe 21 along the. For this reason, in the heater 2 of the conductor softening treatment device, even if the conductive wire 22 is brought close to the conductor C to improve the heating efficiency, it is not necessary to reduce the wall thickness of the carrier pipe 21, so that the carrier pipe 21 is not damaged. Be deterred. Therefore, the conductor softening treatment can improve the heating efficiency of the conductor C while suppressing damage to the device.
[導体軟化処理方法]
 本発明の一態様に係る導体軟化処理方法は、線状の導体Cを連続的に加熱及び冷却する導体軟化処理方法である。当該導体軟化処理方法は、図1の当該導体軟化装置を用いて行う。
[Conductor softening method]
A conductor softening treatment method according to an aspect of the present invention is a conductor softening treatment method of continuously heating and cooling a linear conductor C. The conductor softening method is performed by using the conductor softening device shown in FIG.
 当該導体軟化処理方法は、導体Cをその軸方向に連続的に搬送する工程と、搬送される導体Cを加熱する工程と、加熱された導体Cを冷却水Wへの浸漬により冷却する工程と、冷却水Wの溶存酸素量を予め定められる設定範囲内に維持する工程とを備える。 The conductor softening treatment method includes a step of continuously transporting the conductor C in the axial direction thereof, a step of heating the transported conductor C, and a step of cooling the heated conductor C by immersion in cooling water W. , Maintaining the dissolved oxygen amount of the cooling water W within a predetermined set range.
<搬送工程>
 上記搬送工程は、図1の当該導体軟化装置の送り機構1を用いて行うことができる。従って、搬送速度等の搬送条件は、図1の当該導体軟化装置について説明したものと同様である。
<Conveying process>
The carrying step can be performed using the feeding mechanism 1 of the conductor softening device of FIG. Therefore, the transport conditions such as the transport speed are the same as those described for the conductor softening device in FIG.
 なお、導体Cが断面形状が長方形状である平角導体である場合、導体Cの断面の長辺が磁束方向Sに対して垂直となるように導体Cを搬送するとよい。このように搬送することで、導体Cを効率的に加熱することができる。 If the conductor C is a rectangular conductor having a rectangular cross section, the conductor C may be conveyed so that the long side of the cross section of the conductor C is perpendicular to the magnetic flux direction S. By carrying in this manner, the conductor C can be efficiently heated.
<加熱工程>
 上記加熱工程は、図1の当該導体軟化装置のヒーター2を用いて行うことができる。従って、加熱条件は、図1の当該導体軟化装置について説明したものと同様である。
<Heating process>
The heating step can be performed using the heater 2 of the conductor softening device of FIG. Therefore, the heating conditions are the same as those described for the conductor softening device in FIG.
<冷却工程>
 上記冷却工程は、図1の当該導体軟化装置の冷却槽3に貯留した冷却水Wに導体Cを浸漬することにより行うことができる。
<Cooling process>
The cooling step can be performed by immersing the conductor C in the cooling water W stored in the cooling tank 3 of the conductor softening device of FIG.
<維持工程>
 上記維持工程は、図1の当該導体軟化装置の溶存酸素量調節機構4を用いて行うことができる。従って、冷却水Wの条件等は、図1の当該導体軟化装置について説明したものと同様である。
<Maintenance process>
The maintaining step can be performed using the dissolved oxygen amount adjusting mechanism 4 of the conductor softening device of FIG. Therefore, the conditions and the like of the cooling water W are the same as those described for the conductor softening device of FIG.
<利点>
 当該導体軟化処理方法は、本発明の導体軟化処理装置を用いるので、導体軟化処理装置の破損を抑止しつつ導体軟化処理装置のエネルギー効率を高められる。従って、当該導体軟化処理方法は、製造効率に優れる。
<Advantages>
Since the conductor softening treatment method uses the conductor softening treatment device of the present invention, it is possible to enhance the energy efficiency of the conductor softening treatment device while suppressing damage to the conductor softening treatment device. Therefore, the conductor softening method is excellent in manufacturing efficiency.
〔絶縁電線の製造方法〕
 続いて、当該導体軟方法を用いた絶縁電線の製造方法について説明する。絶縁電線は、当該導体軟化処理方法により導体を軟化処理する工程と、軟化した導体の表面に絶縁塗料(ワニス)を塗布する工程と、加熱により導体の表面に塗布した絶縁塗料を焼き付ける工程とを備える方法により製造される。
[Insulated wire manufacturing method]
Then, the manufacturing method of the insulated wire using the said conductor softening method is demonstrated. The insulated wire includes a step of softening the conductor by the conductor softening treatment method, a step of applying an insulating coating (varnish) on the surface of the softened conductor, and a step of baking the insulating coating applied on the surface of the conductor by heating. It is manufactured by the method of preparing.
<軟化処理工程>
 上記軟化処理工程は、上述の当該導体軟化処理方法に従って行われる。
<Softening process>
The softening treatment step is performed according to the conductor softening treatment method described above.
<塗布工程>
 上記塗布工程では、絶縁塗料を貯留する塗布槽に導体Cを貫通させ、導体Cの表面に付着する絶縁塗料をダイスにより一定の厚さに調整する。
<Coating process>
In the coating step, the conductor C is penetrated through a coating tank that stores the insulating coating material, and the insulating coating material attached to the surface of the conductor C is adjusted to have a constant thickness by a die.
 絶縁塗料の主成分としては、絶縁性及び耐熱性が高い樹脂であればよく、例えばポリアミド、ポリイミド、ポリアミドイミド、ポリエステルイミド等が挙げられる。また絶縁塗料は、例えばN-メチル-2-ピロリドン、クレゾール等の溶剤を含むことができる。 The main component of the insulating paint may be a resin having high insulation and heat resistance, and examples thereof include polyamide, polyimide, polyamideimide, polyesterimide, and the like. The insulating paint may contain a solvent such as N-methyl-2-pyrrolidone or cresol.
 上記ダイスとしては、内面が円錐面状に形成され、楔膜効果により導体Cを自動的に調心して、周方向に膜厚を一定にする効果を有する公知のダイスが使用される。 As the die, a known die having an inner surface formed into a conical surface and having the effect of automatically aligning the conductor C by the wedge film effect and making the film thickness constant in the circumferential direction is used.
<焼付工程>
 上記焼付工程では、表面に絶縁塗料が塗布された導体を加熱することにより、絶縁塗料を硬化させる。絶縁塗料が溶剤を含む場合には、まず樹脂成分の硬化温度未満の温度で溶剤を揮発させ、次に樹脂成分を硬化させる温度に昇温することで、気泡のない絶縁被覆を形成することができる。
<Baking process>
In the baking step, the insulating coating material is cured by heating the conductor whose surface is coated with the insulating coating material. When the insulating paint contains a solvent, first, the solvent is volatilized at a temperature lower than the curing temperature of the resin component, and then the temperature is raised to a temperature at which the resin component is cured, thereby forming an insulating coating without bubbles. it can.
 加熱方法としては、例えば電磁誘導により導体を発熱させる誘導加熱、ヒーターの輻射熱で絶縁塗料を加熱する輻射加熱、熱風を循環させて絶縁塗料を加熱する熱風加熱等を採用することができる。 As the heating method, for example, induction heating that heats the conductor by electromagnetic induction, radiant heating that heats the insulating paint by radiant heat of the heater, hot air heating that circulates hot air to heat the insulating paint, and the like can be adopted.
<利点>
 上記絶縁電線の製造方法は、当該導体軟化処理方法により導体Cを軟化させてから絶縁被覆を形成するので、導体Cが酸化せず、柔軟性及び導電率が高い絶縁電線を製造することができる。
<Advantages>
In the above-described method for manufacturing an insulated wire, the conductor C is softened by the conductor softening treatment method and then the insulating coating is formed. Therefore, the conductor C is not oxidized and an insulated wire having high flexibility and conductivity can be manufactured. ..
[その他の実施形態]
 今回開示された実施の形態は全ての点で例示であって制限的なものではないと考えられるべきである。本発明の範囲は、上記実施形態の構成に限定されるものではなく、請求の範囲によって示され、請求の範囲と均等の意味及び範囲内での全ての変更が含まれることが意図される。
[Other Embodiments]
The embodiments disclosed this time are to be considered as illustrative in all points and not restrictive. The scope of the present invention is not limited to the configurations of the above-described embodiments, but is defined by the scope of the claims, and is intended to include meanings equivalent to the scope of the claims and all modifications within the scope.
 上記実施形態では、導体軟化処理装置として、ヒーターが空洞を取り囲む遮熱板を有する構成を説明したが、遮熱板は上記空洞を取り囲まなくともよい。例えば遮熱板が空洞の一部に沿って搬送管内に埋設されていても、加熱効率の向上に対して一定の効果を奏する。さらに、遮熱板を省略した構成も本発明の意図するところである。 In the above embodiment, as the conductor softening treatment device, the heater has the heat shield plate surrounding the cavity, but the heat shield plate may not surround the cavity. For example, even if the heat shield plate is embedded in the transfer pipe along a part of the cavity, a certain effect can be obtained for improving the heating efficiency. Furthermore, a configuration in which the heat shield plate is omitted is also intended by the present invention.
 上記実施形態では、合計4つの磁性体により空洞が取り囲まれている場合を説明したが、空洞を取り囲む磁性体は4つに限定されるものではなく、例えば1つの磁性体で空洞を取り囲んでもよい。このように1つの磁性体で空洞を取り囲む構成とすることで、特に変形に対する強度を向上できるので、搬送管の破損の抑止効果をさらに高めることができる。なお、1つの磁性体で空洞を取り囲む場合、搬送管は磁性体のみで構成されてもよい。 In the above embodiment, the case where the cavity is surrounded by a total of four magnetic bodies has been described, but the number of magnetic bodies surrounding the cavity is not limited to four, and for example, one magnetic body may surround the cavity. .. Since the strength against deformation can be particularly improved by adopting a structure in which the cavity is surrounded by one magnetic body in this way, the effect of suppressing damage to the transport pipe can be further enhanced. When the cavity is surrounded by one magnetic body, the carrier tube may be composed of only the magnetic body.
 上記実施形態では、導体軟化処理装置として、遮熱板、磁性体及び導電線が独立して搬送管に埋設されている場合について説明したが、例えば導電線は遮熱板や磁性体に埋設された構成とすることもできる。 In the above embodiment, as the conductor softening treatment device, the case where the heat shield plate, the magnetic body, and the conductive wire are independently embedded in the carrier pipe has been described. However, for example, the conductive wire is embedded in the heat shield plate and the magnetic body. It is also possible to have a different configuration.
 上記実施形態では、導体軟化処理装置として、搬送管が、内部に形成された空洞を開放するように分割可能に構成される場合を説明したが、搬送管が分割可能である構成は必須ではなく、分割できない搬送管で構成される導体軟化処理装置も本発明の意図するところである。 In the above embodiment, as the conductor softening treatment device, the case where the carrier pipe is configured to be divisible so as to open the cavity formed inside has been described, but the structure that the carrier pipe is divisible is not essential. A conductor softening treatment device composed of an indivisible carrier pipe is also intended by the present invention.
 上記実施形態では、導電線が絶縁被覆されている場合を説明したが、これは必須の構成要件ではなく、導電線は絶縁被覆されていなくともよい。例えば導電線が遮熱板内に埋設されている場合においては、遮熱板により絶縁を図ってもよい。 In the above embodiment, the case where the conductive wire is covered with insulation has been described, but this is not an indispensable constituent requirement, and the conductive wire may not be covered with insulation. For example, when the conductive wire is embedded in the heat shield plate, insulation may be achieved by the heat shield plate.
 当該導体軟化処理装置において、供給部を省略してもよい。冷却槽が十分大きければ、供給部から新しい冷却水を供給しなくても冷却槽中の冷却水の溶存酸素量を一定時間低く保つことができる。 The supply unit may be omitted in the conductor softening device. If the cooling tank is sufficiently large, the amount of dissolved oxygen in the cooling water in the cooling tank can be kept low for a certain period of time without supplying new cooling water from the supply unit.
 当該導体軟化処理装置において、オーバーフロー機構を省略してもよい。新しい冷却水を過剰供給しない場合には、冷却槽から冷却水を排出する必要がなく、冷却槽から冷却水を排出する場合にも、冷却槽の下部に排出流路を形成したり、吸引ポンプで冷却水を引き抜いたりする等、他の手段を用いてもよい。 The overflow mechanism may be omitted in the conductor softening device. If there is no excess supply of new cooling water, it is not necessary to discharge the cooling water from the cooling tank.Even when the cooling water is discharged from the cooling tank, a discharge passage is formed at the bottom of the cooling tank or a suction pump is used. Other means such as drawing out the cooling water may be used.
 当該導体軟化処理装置において、供給部に替わる溶存酸素量調整機構として、冷却槽に脱酸素部を設けてもよい。例えば、冷却槽に脱酸素剤を供給する装置や窒素ガスを供給する装置を配設することで、冷却槽に貯留する冷却水の溶存酸素量を低く保つことができる。溶存酸素量調整機構は、制御部によって自動で制御されるものだけでなく、オペレーターが操作するものであってもよい。また、冷却槽に予め脱酸素剤を過剰投入しておくことでも、溶存酸素量を一定時間低く維持することができる。 In the conductor softening treatment device, a deoxidizing unit may be provided in the cooling tank as a dissolved oxygen amount adjusting mechanism in place of the supplying unit. For example, by disposing a device for supplying an oxygen scavenger or a device for supplying nitrogen gas to the cooling tank, the amount of dissolved oxygen in the cooling water stored in the cooling tank can be kept low. The dissolved oxygen amount adjusting mechanism may be not only automatically controlled by the control unit but also operated by an operator. In addition, the amount of dissolved oxygen can be kept low for a certain period of time by previously adding an excess amount of oxygen scavenger to the cooling tank.
 当該導体軟化処理装置において、液面から冷却水に溶け込む酸素量が少ない場合等においては、冷却槽の蓋を省略してもよい。 In the conductor softening treatment device, if the amount of oxygen dissolved in the cooling water from the liquid surface is small, the cooling tank lid may be omitted.
 また、液面から冷却水に溶け込む酸素量を低減するために、冷却槽の形状を液面の面積が小さくなるように設計してもよい。 Also, in order to reduce the amount of oxygen that dissolves in the cooling water from the liquid surface, the shape of the cooling tank may be designed so that the area of the liquid surface is small.
 さらに、当該導体軟化処理装置において、エアーブローを省略してもよい。 Furthermore, air blow may be omitted in the conductor softening processing device.
 以下、実施例に基づき本発明を詳述するが、この実施例の記載に基づいて本発明が限定的に解釈されるものではない。 Hereinafter, the present invention will be described in detail based on examples, but the present invention is not limitedly interpreted based on the description of the examples.
[No.1]
 図1の導体軟化処理装置に準じる構成の装置を用いて、導体としての硬銅線を軟化する試験を行った。
[No. 1]
A test for softening a hard copper wire as a conductor was conducted using an apparatus having a configuration similar to that of the conductor softening treatment apparatus of FIG.
 No.1において、ヒーターは、導体の搬送方向に延び、上記導体を搬送するための空洞がその内部に形成されているガラス管を用い、このガラス管の外部に上記空洞を挟んで対向するように2本の導電線を配置した構成とした。なお、No.1においてヒーターは磁性体を有しない構成とし、導電線の長さ(導体の搬送方向の長さ)は10cmとした。また、導電線は上記空洞の上記搬送方向に垂直な面内の中心で磁場が強まるように配線されている。 No. In 1, the heater uses a glass tube that extends in the conductor transport direction and has a cavity for transporting the conductor, and the heater faces the outside of the glass tube with the cavity therebetween. The structure is such that two conductive wires are arranged. In addition, No. In No. 1, the heater was configured to have no magnetic substance, and the length of the conductive wire (length in the carrying direction of the conductor) was 10 cm. Further, the conductive wire is wired so that the magnetic field is strengthened at the center of the plane of the cavity which is perpendicular to the transport direction.
 導体は平角銅線(横断面が直径3mmの円と同等の面積を有する長方形状)であり、導体の搬送速度は15m/minとした。また、ヒーターによる加熱速度は100℃/秒となるように供給電力量を調整し、導体を300℃まで加熱した。このときの加熱効率を表1に示す。 The conductor is a rectangular copper wire (rectangular shape whose cross section has an area equivalent to a circle with a diameter of 3 mm), and the conductor transport speed was set to 15 m/min. The amount of power supplied was adjusted so that the heating rate by the heater was 100° C./second, and the conductor was heated to 300° C. The heating efficiency at this time is shown in Table 1.
 また、表1に示すように、No.1の装置を用いて10回の導体の軟化処理試験を行ったところ、そのうちの3回においてヒーターの破損が確認された。 Also, as shown in Table 1, No. When the conductor softening treatment test was performed 10 times using the apparatus of No. 1, the breakage of the heater was confirmed in three of them.
[No.2]
 No.2では、ヒーターが一対の磁性体を有する構成とした。No.2では、このヒーターの構成以外は、No.1と同様の構成とした。なお、一対の磁性体は、各導電線を挟んで空洞と反対側にそれぞれ配置した。つまり、磁束方向は開放されており(磁性体間距離T1が無限大)、空洞の中心における磁束方向の磁性体間距離T1が、磁束方向と直交する方向の磁性体間距離T2より長い。
[No. 2]
No. In No. 2, the heater has a pair of magnetic bodies. No. In No. 2, except for the structure of this heater, The configuration is the same as that of 1. The pair of magnetic bodies were arranged on the opposite sides of the cavities with the conductive wires sandwiched therebetween. That is, the magnetic flux direction is open (the magnetic substance distance T1 is infinite), and the magnetic substance distance T1 in the magnetic flux direction at the center of the cavity is longer than the magnetic substance distance T2 in the direction orthogonal to the magnetic flux direction.
 上記導体軟化処理装置を用いて、No.1と同様の条件で導体の加熱を行った。このときの加熱効率を表1に示す。 Using the above conductor softening device, No. The conductor was heated under the same conditions as in 1. The heating efficiency at this time is shown in Table 1.
 また、表1に示すように、No.2の装置を用いて20回の導体の軟化処理試験を行ったところ、そのうちの5回においてヒーターの破損が確認された。 Also, as shown in Table 1, No. When the conductor softening treatment test was performed 20 times using the apparatus of No. 2, the breakage of the heater was confirmed in 5 of them.
[No.3]
 No.3では、ヒーターは、導体の搬送方向に延び、上記導体を搬送するための空洞がその内部に形成されている搬送管を用い、この搬送管内に2本の導電線及び4つの磁性体が、図2に示すように埋設された構成とした。空洞の中心における磁束方向の磁性体間距離T1を、磁束方向と直交する方向の磁性体間距離T2より短くした。なお、搬送管は、耐熱樹脂を主成分とし、導電線の長さは10cmとした。
[No. 3]
No. In 3, the heater uses a carrier pipe that extends in the conductor carrying direction and has a cavity for carrying the conductor therein, and two conductive wires and four magnetic bodies are provided in the carrier pipe. It was configured to be embedded as shown in FIG. The distance T1 between magnetic bodies in the magnetic flux direction at the center of the cavity is made shorter than the distance T2 between magnetic bodies in the direction orthogonal to the magnetic flux direction. The carrier tube was made of a heat-resistant resin as a main component, and the conductive wire had a length of 10 cm.
 上記導体軟化処理装置を用いて、No.1と同様の条件で導体の加熱を行った。このときの加熱効率を表1に示す。 Using the above conductor softening device, No. The conductor was heated under the same conditions as in 1. The heating efficiency at this time is shown in Table 1.
 また、表1に示すように、No.3の装置を用いて35回の導体の軟化処理試験を行ったところ、ヒーターの破損は確認されなかった。 Also, as shown in Table 1, No. When the conductor softening treatment test was performed 35 times using the apparatus of No. 3, no damage to the heater was confirmed.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 表1で、「加熱効率」とは、導体の単位長当たりに対し、導体の温度上昇に比熱を乗じた値を投入電力量で除した値をいう。 In Table 1, "heating efficiency" means the value obtained by multiplying the temperature rise of the conductor by the specific heat per unit length of the conductor, divided by the input power amount.
 表1から、導電線を搬送管内に埋設したヒーターを用いたNo.3の導体軟化処理装置は、導電線が埋設されていないNo.1やNo.2の導体軟化処理装置に比べてヒーターの破損が発生し難いことがわかる。このことから、導電線を導体の搬送方向に沿って搬送管内に埋設することで、搬送管の破損が抑止できるといえる。 From Table 1, No. 1 using a heater in which a conductive wire is embedded in the carrier pipe. The conductor softening treatment device of No. 3 is No. 3 in which the conductive wire is not buried. 1 or No. It can be seen that the heater is less likely to be damaged as compared with the conductor softening treatment device of 2. From this, it can be said that by embedding the conductive wire in the transport pipe along the transport direction of the conductor, damage to the transport pipe can be suppressed.
 また、ヒーターが磁性体を有するNo.2及びNo.3の導体軟化処理装置は、磁性体を有しないNo.1の導体軟化処理装置よりも加熱効率が高い。このことから、磁性体を有するヒーターを用いることで導体の加熱効率をさらに高めることができるといえる。 In addition, the heater has a magnetic body No. 2 and No. The conductor softening treatment device of No. 3 has No. The heating efficiency is higher than that of the conductor softening treatment device of No. 1. From this, it can be said that the heating efficiency of the conductor can be further increased by using the heater having the magnetic material.
 さらに、空洞の中心における磁束方向の磁性体間距離T1を、磁束方向と直交する方向の磁性体間距離T2より短いNo.3の導体軟化処理装置は、上記T1が上記T2より長いNo.2の導体軟化処理装置よりも加熱効率が高い。このことから、搬送方向に垂直な面内での空洞の中心における磁束方向の磁性体間距離を、磁束方向と直交する方向の磁性体間距離より短くすることで、導体の加熱効率をさらに高めることができるといえる。 Further, the distance T1 between magnetic bodies in the magnetic flux direction at the center of the cavity is shorter than the distance T2 between magnetic bodies in the direction orthogonal to the magnetic flux direction. The conductor softening treatment apparatus of No. 3 has No. 1 in which T1 is longer than T2. The heating efficiency is higher than that of the second conductor softening treatment device. Therefore, the heating efficiency of the conductor is further improved by making the distance between magnetic bodies in the magnetic flux direction at the center of the cavity in the plane perpendicular to the transport direction shorter than the distance between magnetic bodies in the direction orthogonal to the magnetic flux direction. It can be said that you can.
1 送り機構
11 第1ガイドシーブ
12 第2ガイドシーブ
13 第3ガイドシーブ
2 ヒーター
21 搬送管
21a 空洞
22 導電線
22a 導体部
22b 被覆部
23 遮熱板
24 磁性体
3 冷却槽
31 蓋体
32 オーバーフロー機構
32a トラップ
4 溶存酸素量調節機構
41 供給部
42 溶存酸素量検出部
43 制御部
44 脱酸素部
45 調整弁
5 エアーブロー
C 導体
M 空洞の中心
W 冷却水
1 Feed Mechanism 11 1st Guide Sheave 12 2nd Guide Sheave 13 3rd Guide Sheave 2 Heater 21 Carrier Pipe 21a Cavity 22 Conductive Wire 22a Conductor 22b Covering Part 23 Heat Shield Plate 24 Magnetic Material 3 Cooling Tank 31 Lid 32 Overflow Mechanism 32a Trap 4 Dissolved oxygen amount adjusting mechanism 41 Supply unit 42 Dissolved oxygen amount detecting unit 43 Control unit 44 Deoxidizing unit 45 Adjustment valve 5 Air blow C Conductor M Center of cavity W Cooling water

Claims (10)

  1.  線状の導体を連続的に加熱及び冷却する導体軟化処理装置であって、
     上記導体をその軸方向に連続的に搬送する送り機構と、
     上記送り機構により搬送される上記導体を加熱するヒーターと、
     上記ヒーターにより加熱された上記導体を浸漬する冷却水を貯留する冷却槽と、
     上記冷却槽に貯留されている冷却水の溶存酸素量を予め定められる設定範囲内に維持する溶存酸素量調節機構とを備え、
     上記ヒーターが、
     導体の搬送方向に延び、上記導体を搬送するための空洞がその内部に形成されている搬送管と、
     上記搬送方向に沿って上記搬送管内に埋設され、上記空洞の上記搬送方向に垂直な面内の中心で磁場が強まるように配線される複数の導電線と
     を有する導体軟化処理装置。
    A conductor softening treatment device for continuously heating and cooling a linear conductor,
    A feed mechanism that continuously conveys the conductor in its axial direction,
    A heater for heating the conductor conveyed by the feeding mechanism,
    A cooling tank that stores cooling water for immersing the conductor heated by the heater,
    With a dissolved oxygen amount adjusting mechanism for maintaining the dissolved oxygen amount of the cooling water stored in the cooling tank within a predetermined setting range,
    The heater is
    A carrier pipe extending in the conductor carrying direction and having a cavity formed therein for carrying the conductor;
    A conductor softening treatment device having a plurality of conductive wires embedded along the carrying direction in the carrying pipe and wired so that a magnetic field is strengthened at the center of a plane of the cavity perpendicular to the carrying direction.
  2.  上記搬送管の主成分が耐熱樹脂である請求項1に記載の導体軟化処理装置。 The conductor softening device according to claim 1, wherein a main component of the carrier pipe is a heat resistant resin.
  3.  上記ヒーターが、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む遮熱板を有する請求項1又は請求項2に記載の導体軟化処理装置。 The conductor softening device according to claim 1 or 2, wherein the heater has a heat shield plate that is embedded in the transfer pipe along the transfer direction and surrounds the cavity.
  4.  上記遮熱板の平均厚さが0.5mm以上5mm以下である請求項3に記載の導体軟化処理装置。 The conductor softening device according to claim 3, wherein the heat shield plate has an average thickness of 0.5 mm or more and 5 mm or less.
  5.  上記ヒーターが、上記搬送方向に沿って上記搬送管内に埋設され、上記空洞を取り囲む磁性体を有する請求項1から請求項4のいずれか1項に記載の導体軟化処理装置。 The conductor softening device according to any one of claims 1 to 4, wherein the heater has a magnetic body embedded in the transport pipe along the transport direction and surrounding the cavity.
  6.  上記搬送方向に垂直な面内での上記空洞の中心における磁束方向の磁性体間距離が、上記磁束方向と直交する方向の磁性体間距離より短い請求項5に記載の導体軟化処理装置。 The conductor softening device according to claim 5, wherein a distance between magnetic bodies in a magnetic flux direction at a center of the cavity in a plane perpendicular to the transport direction is shorter than a distance between magnetic bodies in a direction orthogonal to the magnetic flux direction.
  7.  上記搬送管が、上記空洞を開放するように分割可能に構成される請求項1から請求項6のいずれか1項に記載の導体軟化処理装置。 The conductor softening device according to any one of claims 1 to 6, wherein the carrier pipe is configured to be divisible so as to open the cavity.
  8.  上記導電線が絶縁被覆されている請求項1から請求項7のいずれか1項に記載の導体軟化処理装置。 The conductor softening device according to any one of claims 1 to 7, wherein the conductive wire is insulation-coated.
  9.  上記空洞の長さが50mm以上1500mm以下である請求項1から請求項8のいずれか1項に記載の導体軟化処理装置。 The conductor softening device according to any one of claims 1 to 8, wherein the cavity has a length of 50 mm or more and 1500 mm or less.
  10.  線状の導体を連続的に加熱及び冷却する導体軟化処理方法であって、
     請求項1から請求項9のいずれか1項に記載の導体軟化処理装置を用い、
     上記導体をその軸方向に連続的に搬送する工程と、
     搬送される上記導体を加熱する工程と、
     加熱された上記導体を冷却水への浸漬により冷却する工程と、
     上記冷却水の溶存酸素量を予め定められる設定範囲内に維持する工程と
     を備える導体軟化処理方法。
     
    A conductor softening treatment method of continuously heating and cooling a linear conductor,
    Using the conductor softening apparatus according to any one of claims 1 to 9,
    A step of continuously transporting the conductor in its axial direction,
    Heating the carried conductor,
    A step of cooling the heated conductor by immersion in cooling water,
    A step of maintaining the dissolved oxygen amount of the cooling water within a predetermined set range.
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JP2010244763A (en) * 2009-04-02 2010-10-28 Shimada Phys & Chem Ind Co Ltd High-frequency induction heating apparatus
JP2016079436A (en) * 2014-10-14 2016-05-16 住友電工ウインテック株式会社 Apparatus and method for subjecting conductor to softening treatment

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