WO2021149223A1 - Heat exchanger and refrigeration cycle apparatus - Google Patents

Heat exchanger and refrigeration cycle apparatus Download PDF

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Publication number
WO2021149223A1
WO2021149223A1 PCT/JP2020/002321 JP2020002321W WO2021149223A1 WO 2021149223 A1 WO2021149223 A1 WO 2021149223A1 JP 2020002321 W JP2020002321 W JP 2020002321W WO 2021149223 A1 WO2021149223 A1 WO 2021149223A1
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WO
WIPO (PCT)
Prior art keywords
flow path
plate
refrigerant
shaped member
heat transfer
Prior art date
Application number
PCT/JP2020/002321
Other languages
French (fr)
Japanese (ja)
Inventor
篤史 ▲高▼橋
前田 剛志
真哉 東井上
Original Assignee
三菱電機株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 三菱電機株式会社 filed Critical 三菱電機株式会社
Priority to PCT/JP2020/002321 priority Critical patent/WO2021149223A1/en
Priority to EP20915558.9A priority patent/EP4095476B1/en
Priority to JP2021572221A priority patent/JP7278430B2/en
Priority to TW109115172A priority patent/TWI768340B/en
Publication of WO2021149223A1 publication Critical patent/WO2021149223A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0278Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of stacked distribution plates or perforated plates arranged over end plates
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0202Header boxes having their inner space divided by partitions
    • F28F9/0204Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0219Arrangements for sealing end plates into casing or header box; Header box sub-elements
    • F28F9/0221Header boxes or end plates formed by stacked elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles

Definitions

  • the present disclosure relates to a heat exchanger and a refrigeration cycle device equipped with the heat exchanger.
  • the heat transfer tubes used in heat exchangers for air conditioners have been made thinner.
  • the number of heat exchanger passes is increased compared to conventional heat exchangers in order to suppress an increase in refrigerant pressure loss.
  • the heat exchanger is provided with a multi-branch refrigerant distributor (see, for example, Patent Document 1).
  • a multi-branch refrigerant distributor see, for example, Patent Document 1.
  • a compact refrigerant distributor that secures a large area but does not hinder the installation space of the heat exchanger is required.
  • the heat exchanger of Patent Document 1 has a plurality of heat transfer tubes arranged side by side, a header collecting pipe which is a refrigerant collecting pipe which is connected to one end of the heat transfer pipe and extends in the vertical direction, and a heat transfer pipe. It has multiple fins joined to.
  • the internal space of the header collecting pipe is divided into a first space on the side where one end of the heat transfer tube is connected by a partition plate and a second space on the side opposite to the first space side with respect to the partition plate. It is partitioned. Further, at the upper end and the lower end of the partition plate, a communication passage for communicating the first space and the second space is provided.
  • the heat exchanger of Patent Document 1 has such a configuration, so that the refrigerant is looped between the first space and the second space.
  • the heat exchanger of Patent Document 1 is said to be able to suppress the drift of the refrigerant to a small value by looping the refrigerant between the first space and the second space.
  • a first space forming a flow path through which the gas-liquid two-phase refrigerant flows upward and a second space forming a circulation flow path for returning the refrigerant from the upper part to the lower part are transmitted. It is located in the extending direction of the conduit of the heat pipe. Since the refrigerant distributor described in Patent Document 1 is enlarged in the extending direction of the heat transfer tube line due to the configuration, the length of the heat transfer tube in the extension direction of the heat transfer tube is reduced due to the structural contract, and the heat transfer tube is transmitted. The heat area becomes small. Therefore, the heat exchanger of Patent Document 1 may have lower heat exchange performance than the conventional heat exchanger.
  • the present disclosure is for solving the above-mentioned problems, and provides a compact refrigerant distributor without increasing the size in the extending direction of the heat transfer pipe while ensuring a wide heat transfer area of the heat transfer pipe. It is an object of the present invention to provide a heat exchanger and a refrigeration cycle device provided.
  • the heat exchanger is a plurality of heat transfer tubes arranged at intervals in the first direction, and includes a plurality of heat transfer tubes for flowing a refrigerant in a second direction intersecting the first direction, and a first.
  • a refrigerant distributor extending in one direction and connected to one end of each of the plurality of heat transfer tubes to distribute the refrigerant to the plurality of heat transfer tubes is provided, and the refrigerant distributor includes a first flow path and a second flow path through which the refrigerant flows.
  • the flow path is formed inside, and the first flow path is formed so as to extend in the first direction, and is an inflow pipe that communicates with a plurality of heat transfer tubes and allows the refrigerant to flow into the inside of the refrigerant distributor.
  • the second flow path is formed so as to extend in the first direction and both ends are connected to the first flow path, and intersect the planes parallel to the first direction and the second direction.
  • the direction is defined as the third direction, it is formed so as to be located in the third direction with respect to the first flow path.
  • the refrigeration cycle device according to the present disclosure is provided with the heat exchanger according to the present disclosure.
  • the heat exchanger has a refrigerant distributor in which a first flow path and a second flow path through which the refrigerant flows are formed.
  • the second flow path is formed so as to extend in the first direction and connect both ends to the first flow path.
  • the second flow path is formed so as to be located in the third direction with respect to the first flow path when the direction intersecting the first direction and the plane parallel to the second direction is defined as the third direction.
  • the heat exchanger can suppress the increase in size of the refrigerant distributor in the second direction in which the refrigerant flows, and the heat exchanger is enlarged in the direction in which the conduit of the heat transfer tube extends within the range of the structural contract. be able to. Therefore, in the heat exchanger 100 of the present disclosure, the heat transfer area of the heat transfer tube can be secured widely, and the refrigerant distributor can be made compact without increasing in size in the extending direction of the heat transfer tube line.
  • FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the first embodiment.
  • FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of a refrigerant distributor constituting the heat exchanger according to the second embodiment.
  • FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the third embodiment.
  • FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the fourth embodiment.
  • FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the fifth embodiment.
  • FIG. 5 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor of the modified example constituting the heat exchanger according to the fifth embodiment.
  • FIG. 5 is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 5.
  • FIG. 1 is a refrigerant circuit diagram showing a configuration of a refrigeration cycle device 200 including the heat exchanger 100 according to the first embodiment.
  • the arrow indicated by the dotted line indicates the direction in which the refrigerant flows in the refrigerant circuit 110 during the cooling operation
  • the arrow indicated by the solid line indicates the direction in which the refrigerant flows during the heating operation. ..
  • the refrigeration cycle apparatus 200 provided with the heat exchanger 100 which will be described later, will be described with reference to FIG.
  • the air conditioner is exemplified as the refrigerating cycle device 200, but the refrigerating cycle device 200 is used for refrigerating, for example, a refrigerator or a freezer, a vending machine, an air conditioner, a refrigerating device, a water heater, and the like. Used for applications or air conditioning applications.
  • the illustrated refrigerant circuit 110 is an example, and the configuration of circuit elements and the like is not limited to the contents described in the embodiment, and can be appropriately changed within the scope of the technique according to the embodiment. ..
  • the refrigerating cycle device 200 has a refrigerant circuit 110 in which a compressor 101, a flow path switching device 102, an indoor heat exchanger 103, a decompression device 104, and an outdoor heat exchanger 105 are cyclically connected via a refrigerant pipe. ..
  • the refrigeration cycle device 200 has an outdoor unit 106 and an indoor unit 107.
  • the outdoor unit 106 includes a compressor 101, a flow path switching device 102, an outdoor heat exchanger 105 and a decompression device 104, and an outdoor blower 108 that supplies outdoor air to the outdoor heat exchanger 105.
  • the indoor unit 107 includes an indoor heat exchanger 103 and an indoor blower 109 that supplies air to the indoor heat exchanger 103.
  • the outdoor unit 106 and the indoor unit 107 are connected via two extension pipes 111 and 112 which are a part of the refrigerant pipe.
  • the compressor 101 is a fluid machine that compresses and discharges the sucked refrigerant.
  • the flow path switching device 102 is, for example, a four-way valve, and is a device that switches the flow path of the refrigerant between the cooling operation and the heating operation by controlling the control device (not shown).
  • the refrigerant is the first heat exchange fluid.
  • the indoor heat exchanger 103 is a heat exchanger that exchanges heat between the refrigerant circulating inside and the indoor air supplied by the indoor blower 109.
  • the indoor heat exchanger 103 functions as a condenser during the heating operation and as an evaporator during the cooling operation.
  • the pressure reducing device 104 is, for example, an expansion valve, which is a device for reducing the pressure of the refrigerant.
  • an electronic expansion valve whose opening degree is adjusted by the control of the control device can be used.
  • the outdoor heat exchanger 105 is a heat exchanger that exchanges heat between the refrigerant circulating inside and the air supplied by the outdoor blower 108.
  • the outdoor heat exchanger 105 functions as an evaporator during the heating operation and as a condenser during the cooling operation.
  • the air supplied by the outdoor blower 108 is an example of a second heat exchange fluid.
  • a heat exchanger 100 which will be described later, is used for at least one of the outdoor heat exchanger 105 and the indoor heat exchanger 103. It is desirable that the refrigerant distributor 150 connected to the heat exchanger 100 is arranged at a position in the heat exchanger 100 where the amount of the liquid phase refrigerant is larger. Specifically, the refrigerant distributor 150 is arranged on the inlet side of the heat exchanger 100 that functions as an evaporator, that is, on the outlet side of the heat exchanger 100 that functions as a condenser in the flow of the refrigerant in the refrigerant circuit 110. Is desirable. In FIG. 1, the refrigerant distributor 150 is used in both the indoor heat exchanger 103 and the outdoor heat exchanger 105, but either the indoor heat exchanger 103 or the outdoor heat exchanger 105. It may be used only for one of the heat exchangers 100.
  • the low-pressure gas-liquid two-phase refrigerant flows into the outdoor heat exchanger 105 and evaporates by heat exchange with the air supplied by the outdoor blower 108.
  • the evaporated refrigerant becomes a low-pressure gas state and is sucked into the compressor 101.
  • frost adheres to the outdoor heat exchanger 105.
  • the refrigerant flowing through the refrigerant circuit 110 flows in the opposite direction to that during the heating operation. That is, during the cooling operation of the refrigeration cycle device 200, the high-pressure and high-temperature gas-state refrigerant discharged from the compressor 101 flows into the outdoor heat exchanger 105 via the flow path switching device 102 and is supplied by the outdoor blower 108. It exchanges heat with the air and condenses.
  • the condensed refrigerant is in a high-pressure liquid state, flows out of the outdoor heat exchanger 105, and is in a low-pressure gas-liquid two-phase state by the decompression device 104.
  • the low-pressure gas-liquid two-phase refrigerant flows into the indoor heat exchanger 103 and evaporates by heat exchange with the air supplied by the indoor blower 109.
  • the evaporated refrigerant becomes a low-pressure gas state and is sucked into the compressor 101.
  • FIG. 2 is a side view conceptually showing the main configuration of the heat exchanger 100 according to the first embodiment.
  • FIG. 3 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the first embodiment.
  • the heat exchanger 100 according to the first embodiment will be described with reference to FIGS. 2 to 3.
  • the arrow F indicated by hatching indicates the direction of the refrigerant flowing through the first flow path portion 15 of the refrigerant distributor 150.
  • the refrigerant distributor 150 is connected to the end of the heat transfer tube 70 which is the inlet side of the refrigerant when the heat exchanger 100 operates as an evaporator. There is.
  • the heat exchanger 100 includes a plurality of heat transfer tubes 70 through which refrigerant is circulated, and a refrigerant distributor 150 connected to one end of each of the plurality of heat transfer tubes 70 in the extending direction. Have. Further, the heat exchanger 100 has a refrigerant inflow pipe 60 attached to the lower part of the refrigerant distributor 150.
  • the plurality of heat transfer tubes 70 are arranged at intervals in the first direction (Z-axis direction), and the refrigerant flows in the second direction (X-axis direction) intersecting the first direction (Z-axis direction). ..
  • the plurality of heat transfer tubes 70 are flat tubes. Although the heat transfer tube 70 is described as a flat tube, the heat transfer tube 70 is not limited to the flat tube, and may be, for example, a circular tube.
  • the arrangement direction of the plurality of heat transfer tubes 70 and the extension direction of the refrigerant distributor 150 are defined as the first direction (Z-axis direction). That is, the first direction is the direction in which the plurality of heat transfer tubes 70 are lined up.
  • the arrangement direction of the plurality of heat transfer tubes 70, which is the first direction (Z-axis direction) is the vertical direction.
  • the vertical direction is, for example, the vertical direction.
  • the arrangement direction of the plurality of heat transfer tubes 70, which is the first direction (Z-axis direction) is not limited to the vertical direction and the vertical direction, and may be a direction inclined with respect to the vertical direction, and is horizontal. It may be a direction.
  • the extension direction of the pipeline of the heat transfer tube 70 is defined as the second direction (X-axis direction).
  • the conduit of the heat transfer tube 70 is a refrigerant passage 72, which will be described later (see FIG. 4). Therefore, the second direction (X-axis direction) is also the flow direction of the refrigerant flowing through the conduit of the heat transfer tube 70.
  • the extension direction of the pipe lines of the plurality of heat transfer tubes 70 which is the second direction (X-axis direction)
  • the extension direction of the conduits of the plurality of heat transfer tubes 70 in the second direction (X-axis direction) is not limited to the horizontal direction, and may be a direction inclined with respect to the horizontal direction, and is vertical. It may be in the vertical direction including the direction.
  • a gap 71 that serves as an air flow path is formed between two adjacent heat transfer tubes 70 among the plurality of heat transfer tubes 70.
  • heat transfer fins 75 may be provided between two adjacent heat transfer tubes 70.
  • the heat exchanger 100 has a heat transfer fin 75 which is a heat transfer promoting member in a part thereof, and has a region in which the heat transfer tubes 70 adjacent to each other are not connected to each other by the heat transfer promoting member. You may.
  • the heat transfer promoting member is a member that promotes heat transfer, and is, for example, a plate fin such as a heat transfer fin 75, a corrugated fin, or the like. Therefore, the outdoor heat exchanger 105 may be configured as a so-called finless heat exchanger.
  • the heat exchanger 100 When the heat exchanger 100 functions as an evaporator of the refrigeration cycle device 200, the refrigerant flows from one end to the other end in the extension direction in each of the plurality of heat transfer tubes 70. Further, when the heat exchanger 100 functions as a condenser of the refrigeration cycle device 200, in each of the plurality of heat transfer tubes 70, the refrigerant flows from the other end in the extension direction toward one end in the inner pipeline of the heat transfer tube 70. ..
  • FIG. 4 is a cross-sectional view showing the configuration of the heat transfer tube 70 constituting the heat exchanger 100 according to the first embodiment.
  • FIG. 4 shows a cross section perpendicular to the extending direction of the heat transfer tube 70.
  • the heat transfer tube 70 has a unidirectionally flat cross-sectional shape such as an oval shape.
  • the heat transfer tube 70 has a first side end portion 70a and a second side end portion 70b, and a pair of flat surfaces 70c and flat surfaces 70d.
  • first side end portion 70a is connected to one end portion of the flat surface 70c and one end portion of the flat surface 70d.
  • the second side end 70b is connected to the other end of the flat surface 70c and the other end of the flat surface 70d.
  • the first side end portion 70a is a side end portion arranged on the windward side, that is, on the front edge side in the flow of air passing through the heat exchanger.
  • the second side end portion 70b is a side end portion arranged on the leeward side, that is, the trailing edge side in the flow of air passing through the heat exchanger.
  • the direction perpendicular to the extending direction of the heat transfer tube 70 and along the flat surface 70c and the flat surface 70d may be referred to as a major axis direction of the heat transfer tube 70.
  • the heat transfer tube 70 is formed with a plurality of refrigerant passages 72 arranged between the first side end portion 70a and the second side end portion 70b along the long axis direction.
  • the heat transfer tube 70 is a flat perforated tube in which a plurality of refrigerant passages 72 through which the refrigerant flows are arranged in the air flow direction.
  • Each of the plurality of refrigerant passages 72 is formed so as to extend in parallel with the extending direction of the heat transfer tube 70.
  • the refrigerant distributor 150 has a main body 151 extending in the first direction (Z-axis direction).
  • the main body 151 of the refrigerant distributor 150 is connected to one end of each of the plurality of heat transfer tubes 70.
  • the refrigerant distributor 150 distributes the refrigerant to each of the plurality of heat transfer tubes 70 connected to the main body 151.
  • the main body 151 of the refrigerant distributor 150 is formed so as to extend in the vertical direction along the arrangement direction of the plurality of heat transfer tubes 70.
  • the main body 151 extends in the first direction, and a distribution flow path for distributing the refrigerant to each heat transfer tube 70 is formed inside.
  • the main body 151 of the refrigerant distributor 150 is formed with a refrigerant inflow port 18 into which the refrigerant inflow pipe 60 is inserted and a plurality of insertion holes 31 into which each of the plurality of heat transfer pipes 70 is inserted.
  • the refrigerant inflow port 18 is formed on one end 151a side of the main body 151 in the first direction.
  • the plurality of insertion holes 31 are formed on the side surface of the main body 151 on the side connected to the plurality of heat transfer tubes 70.
  • Each of the plurality of insertion holes 31 is formed so as to correspond to each of the plurality of heat transfer tubes 70 so as to be spaced apart from each other along the first direction (Z-axis direction).
  • the main body 151 of the refrigerant distributor 150 has a first plate-shaped member 10, a second plate-shaped member 20, and a third plate-shaped member 30.
  • the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are all formed by using a metal flat plate and have a strip-like shape long in one direction.
  • the contours of the outer edges of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 have the same shape as each other.
  • Each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 has a plate thickness direction parallel to the extension direction of the pipe line of the heat transfer tube 70, that is, each plate surface. Is arranged so as to be perpendicular to the extending direction of the conduit of the heat transfer tube 70.
  • the main body 151 of the refrigerant distributor 150 has a configuration in which the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are laminated in this order from the farthest distance from the heat transfer tube 70. ing.
  • the first plate-shaped member 10 is arranged at the position farthest from the heat transfer tube 70 in the main body 151, and the third plate-shaped member 30 is arranged at the position closest to the heat transfer tube 70 in the main body 151. Has been done.
  • the second plate-shaped member 20 is arranged between the first plate-shaped member 10 and the heat transfer tube 70, and is adjacent to the first plate-shaped member 10 and the third plate-shaped member 30.
  • the third plate-shaped member 30 is arranged between the second plate-shaped member 20 and the heat transfer tube 70, and is adjacent to the second plate-shaped member 20.
  • One end of each of the plurality of heat transfer tubes 70 is connected to the third plate-shaped member 30.
  • the adjacent members of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are joined by brazing.
  • the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are arranged so that their respective longitudinal directions are along the first direction (Z-axis direction).
  • FIG. 5 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment.
  • the plate thickness direction of each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 is the vertical direction of FIG. 5, and is the extending direction of the conduit of the heat transfer tube 70.
  • the lateral direction of each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 is the left-right direction in FIG. 5, and the major axis direction of the heat transfer tube 70.
  • the configuration of the main body 151 of the refrigerant distributor 150 will be further described with reference to FIGS. 3 and 5.
  • the first plate-shaped member 10 has a first flow path portion 15 that bulges in a direction away from the heat transfer tube 70.
  • the first flow path portion 15 is formed in a tubular shape, and a space is formed inside the bulge.
  • the first plate-shaped member 10 and the first flow path portion 15 are integrally formed in the refrigerant distributor 150, they may be formed separately.
  • the first flow path portion 15 extends from one end in the longitudinal direction to the other end in the longitudinal direction of the first plate-shaped member 10 along the longitudinal direction of the first plate-shaped member 10.
  • the first flow path portion 15 is formed in a semi-cylindrical shape. Both ends of the first flow path portion 15 in the stretching direction are closed.
  • the first flow path portion 15 has a semicircular, semi-elliptical or semi-oval cross-sectional shape in a cross section perpendicular to the first direction (Z-axis direction).
  • the cross-sectional shape of the first flow path portion 15 is not limited to a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape, and may be, for example, a rectangular shape.
  • the first plate-shaped member 10 has a flat plate portion 11a and a flat plate portion 11b formed in a flat plate shape on both sides of the first flow path portion 15. Both the flat plate portion 11a and the flat plate portion 11b extend from one end in the longitudinal direction to the other end in the longitudinal direction of the first plate-shaped member 10 along the longitudinal direction of the first plate-shaped member 10.
  • the first flow path portion 15 is formed between the flat plate portion 11a and the flat plate portion 11b, and is opposite to the side on which the heat transfer tube 70 is arranged with respect to the flat plate portion 11a and the flat plate portion 11b. It is formed so as to bulge in the direction.
  • the first flow path portion 15 is open on the arrangement side of the heat transfer tube 70.
  • the flat plate portion 11a and the flat plate portion 11b may be collectively referred to as the flat plate portion 11.
  • a main flow path 15a extending in the vertical direction along the longitudinal direction of the first plate-shaped member 10 is formed.
  • the main flow path 15a is the first flow path of the refrigerant distributor 150.
  • the main flow path 15a which is the first flow path, is connected to the refrigerant inflow pipe 60 connected to the refrigerant inflow port 18 and is formed so as to extend in the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. Has been done.
  • the main flow path 15a which is the first flow path, extends so as to intersect with each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the first plate-shaped member 10.
  • the main flow path 15a which is the first flow path, communicates with the conduits of the plurality of heat transfer tubes 70 via the distribution hole portion 26 formed in the second plate-shaped member 20 which will be described later.
  • the main flow path 15a has a semicircular, semi-elliptical or semi-oval cross-sectional shape in a cross section perpendicular to the first direction (Z-axis direction). That is, the main flow path 15a is a space formed in a semi-cylindrical shape, a semi-elliptical cylinder shape, or a semi-long cylindrical shape.
  • the cross-sectional shape of the main flow path 15a is not limited to a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape, and may be, for example, a rectangular shape.
  • the main flow path 15a which is the first flow path, is formed so as to extend in the first direction (Z-axis direction), communicates with the plurality of heat transfer tubes 70, and is in the first direction.
  • the lower end portion 15a2 it is connected to a refrigerant inflow pipe 60 that allows the refrigerant to flow into the refrigerant distributor 150.
  • the gas-liquid two-phase refrigerant flowing into the main flow path 15a through the refrigerant inflow pipe 60 flows upward in the main flow path 15a so as to go from one end 151a of the main body 151 to the other end 151b. It is distributed to each heat transfer tube 70.
  • a refrigerant inflow pipe 60 is connected to the lower end of the first flow path portion 15.
  • the main flow path 15a and the internal space of the refrigerant inflow pipe 60 communicate with each other.
  • the refrigerant inflow pipe 60 causes a gas-liquid two-phase refrigerant to flow into the main flow path 15a when the heat exchanger 100 functions as an evaporator.
  • the connection position between the refrigerant inflow pipe 60 and the first flow path portion 15 is the refrigerant inflow port 18 through which the refrigerant flows into the refrigerant distributor 150.
  • the heat exchanger 100 functions as a condenser
  • the liquid refrigerant flows downward in the main flow path 15a and flows out through the refrigerant inflow pipe 60.
  • the second plate-shaped member 20 is formed with a sub-flow path 25 and a distribution hole portion 26.
  • the third direction includes the Y-axis direction.
  • the distribution hole portion 26 is formed near the center of the second plate-shaped member 20, and the auxiliary flow path 25 is formed near the end of the second plate-shaped member 20. .. That is, in the third direction (Y-axis direction), the distribution hole portion 26 is formed near the center of the second plate-shaped member 20, and the auxiliary flow paths 25 are formed on both sides of the distribution hole portion 26, respectively. ..
  • the formation positions of the sub-flow path 25 and the distribution hole portion 26 in the second plate-shaped member 20 are not limited to the above positions.
  • the sub-flow paths 25 formed on both sides of the distribution hole portion 26 may be formed so that at least one end portion in the first direction communicates with each other.
  • the auxiliary flow path 25 is formed so as to extend in the first direction (Z-axis direction) in the second plate-shaped member 20. That is, the sub-channel 25 is formed by extending in the vertical direction along the longitudinal direction of the second plate-shaped member 20.
  • the sub-flow path 25 is the second flow path of the refrigerant distributor 150.
  • the sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that both ends are connected to the main flow path 15a, which is the first flow path.
  • the sub-flow path 25 communicates the upper end portion 15a1 and the lower end portion 15a2 of the main flow path 15a, and returns the refrigerant that has reached the upper end portion 15a1 of the main flow path 15a to the lower end portion 15a2 in which the refrigerant inlet 18 is formed. It forms a flow path for the refrigerant.
  • the main body 151 of the refrigerant distributor 150 forms a refrigerant circulation flow path by the main flow path 15a and the sub flow path 25.
  • the main body 151 of the refrigerant distributor 150 has a main flow path 15a and a sub flow path 25 through which the refrigerant flows.
  • the main flow path 15a is the first flow path
  • the sub-flow path 25 is the second flow path.
  • the sub-flow path 25, which is the second flow path is formed so as to be located in the third direction with respect to the main flow path 15a, which is the first flow path. That is, the main flow path 15a and the sub-flow path 25 are formed so as to be located on the upstream side and the downstream side in the ventilation direction of the wind formed by the outdoor blower 108 or the indoor blower 109 shown in FIG.
  • the sub-flow path 25 has a central portion 25a, an inlet portion 25b, and an outlet portion 25c.
  • the central portion 25a forms a flow path extending in the first direction (Z-axis direction).
  • the inlet portion 25b is formed at one end portion 25a1 of the central portion 25a in the first direction (Z-axis direction).
  • the outlet portion 25c is formed at the other end portion 25a2 of the central portion 25a in the first direction (Z-axis direction).
  • the inlet portion 25b and the outlet portion 25c are formed as flow paths extending in the third direction (Y-axis direction) in the main body 151 of the refrigerant distributor 150.
  • the central portion 25a of the auxiliary flow path 25 has a flat plate portion 11 and a third plate shape of the first plate-shaped member 10 in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. It is sandwiched between the flat plate portion 34 of the member 30 and the flat plate portion 34.
  • Both ends of the subchannel 25 are composed of an inlet portion 25b and an outlet portion 25c.
  • the inlet portion 25b and the outlet portion 25c are flat plates of the first flow path portion 15 and the third plate-shaped member 30 in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. It is sandwiched between the portion 34 and the portion 34. Therefore, the inlet portion 25b and the outlet portion 25c communicate with the main flow path 15a, which is the first flow path formed by the first flow path portion 15.
  • the central portion 25a of the sub-flow path 25 does not communicate with the main flow path 15a, which is the first flow path.
  • the sub-flow path 25, which is the second flow path has an inlet portion 25b and an outlet portion 25c so that both ends are connected to the main flow path 15a, which is the first flow path. It is formed. More specifically, the sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that the inlet portion 25b communicates with the upper end portion 15a1 of the main flow path 15a. The sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that the outlet portion 25c communicates with the lower end portion 15a2 of the main flow path 15a.
  • the sub-flow path 25, which is the second flow path does not communicate with the insertion hole 31 of the third plate-shaped member 30, which will be described later.
  • the second plate-shaped member 20 is formed with a plurality of distribution hole portions 26 each having a circular opening shape.
  • the plurality of distribution holes 26 form a flow path between the main flow path 15a and the heat transfer tube 70, and distribute the refrigerant to each heat transfer tube 70.
  • Each of the plurality of distribution hole portions 26 is a through hole that penetrates the second plate-shaped member 20 in the plate thickness direction of the second plate-shaped member 20.
  • the plurality of distribution hole portions 26 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the second plate-shaped member 20.
  • Each of the plurality of distribution hole portions 26 forms a through hole penetrating the second plate-shaped member 20, and is provided corresponding to each of the plurality of heat transfer tubes 70.
  • the opening shape of the distribution hole portion 26 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape.
  • the flow path cross-sectional areas of the plurality of distribution hole portions 26 are the same size. However, the flow path cross-sectional areas of the plurality of distribution hole portions 26 are not limited to those having the same size, and may be formed to have different sizes.
  • a plurality of distribution hole portions 26 are formed in the second plate-shaped member 20, but the distribution hole portion 26 is 1 in the second plate-shaped member 20. Only one may be formed. In this case, the distribution hole portion 26 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
  • Each of the plurality of distribution hole portions 26 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the second plate-shaped member 20. Further, each of the plurality of distribution hole portions 26 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30, which will be described later, when viewed in the plate thickness direction of the second plate-shaped member 20. There is. Further, each of the plurality of distribution hole portions 26 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the second plate-shaped member 20.
  • the distribution hole portion 26 is located between the heat transfer tube 70 and the main flow path 15a which is the first flow path. positioned. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of distribution holes 26.
  • the second plate-shaped member 20 has a flat plate-shaped closing portion 24.
  • a part of the closing portion 24 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the second plate-shaped member 20.
  • the closing portion 24 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the distribution hole portion 26.
  • the third plate-shaped member 30 is formed with a plurality of insertion holes 31 into which one ends of the plurality of heat transfer tubes 70 are inserted.
  • Each of the plurality of insertion holes 31 is a through hole that penetrates the third plate-shaped member 30 in the plate thickness direction of the third plate-shaped member 30.
  • the plurality of insertion holes 31 are arranged in parallel in the vertical direction along the longitudinal direction of the third plate-shaped member 30.
  • the plurality of insertion holes 31 are provided independently of each other corresponding to each of the plurality of heat transfer tubes 70.
  • the insertion hole 31 has a flat opening shape similar to the outer peripheral shape of the heat transfer tube 70.
  • the open end of the insertion hole 31 is joined to the outer peripheral surface of the heat transfer tube 70 over the entire circumference by brazing.
  • the third plate-shaped member 30 has a flat plate-shaped flat plate portion 34.
  • the flat plate portion 34 corresponds to a portion of the third plate-shaped member 30 that overlaps with the sub-flow path 25 of the second plate-shaped member 20 when viewed in the plate thickness direction of the third plate-shaped member 30.
  • the sub-flow path 25, which is the second flow path, is blocked by the flat plate portion 34 and the flat plate portion 11 in the second direction (X-axis direction).
  • the main body 151 of the refrigerant distributor 150 has a main flow path 15a and a second flow, which are the first flow paths, in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. Both ends of the sub-flow path 25, which is a road, overlap each other. Further, the main body 151 of the refrigerant distributor 150 includes the main flow path 15a, which is the first flow path, in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. The distribution hole portion 26 and the insertion hole 31 are formed so as to overlap each other.
  • FIG. 6 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment.
  • the operation of the refrigerant distributor 150 according to the first embodiment will be described by exemplifying the operation when the heat exchanger 100 functions as the evaporator of the refrigeration cycle device 200.
  • the refrigerant flowing into the refrigerant distributor 150 is a gas-liquid two-phase flow.
  • the gas-liquid two-phase refrigerant flows into the main body 151 from the refrigerant inflow pipe 60 shown in FIGS. 2 and 6, and forms a main flow path 15a formed in the first plate-shaped member 10 as shown by the arrow UF in FIG. It flows vertically upward from one end 151a toward the other end 151b.
  • the vertically rising and flowing refrigerant passes through the distribution hole 26 of the second plate-shaped member 20 and is distributed to each heat transfer tube 70 through the insertion hole 31 formed in the third plate-shaped member 30.
  • the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 25b provided in the second plate-shaped member 20 communicating with the upper end portion 15a1 of the main flow path 15a.
  • the refrigerant flows from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path, toward the outside, which is the third direction.
  • the refrigerant flowing in from the inlet portion 25b of the sub-channel 25 flows downward along the central portion 25a of the sub-channel 25 formed in the second plate-shaped member 20. ..
  • the refrigerant that has reached the lower end of the central portion 25a of the sub-flow path 25 flows out to the main flow path 15a from the outlet portion 25c that communicates with the lower end portion 15a2 of the main flow path 15a.
  • the refrigerant flows inward in the third direction from the sub-flow path 25 which is the second flow path toward the main flow path 15a which is the first flow path.
  • the refrigerant flowing out from the outlet portion 25c to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
  • FIG. 7 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment.
  • the horizontal axis represents the refrigerant flow rate [kg / h]
  • the vertical axis represents the distance [m] from the refrigerant inflow port 18 in the first direction in which the heat transfer tubes 70 are arranged.
  • the dotted line A shows the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided
  • the solid line B shows the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided.
  • the alternate long and short dash line C shows a case where the flow rate of the refrigerant flowing through the main flow path 15a is constant in the vertical direction.
  • the inflow amount of the refrigerant flowing into the heat transfer tubes 70 arranged in the first direction is constant. Therefore, it is desirable that the flow rate of the refrigerant in the main flow path 15a is close to the flow rate of the refrigerant indicated by the alternate long and short dash line C.
  • the liquid refrigerant staying in the upper part of the main flow path 15a is transferred to the lower part of the main flow path 15a via the sub-flow path 25. return. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases.
  • the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a. Therefore, as shown by the solid line B, the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
  • the heat exchanger 100 has a refrigerant distributor 150 in which a main flow path 15a through which the refrigerant flows and a sub-flow path 25 are formed therein.
  • the sub-flow path 25, which is the second flow path extends in the first direction (Z-axis direction) and is formed so that both ends are connected to the main flow path 15a, which is the first flow path.
  • the sub-flow path 25, which is the second flow path is the third direction when the direction intersecting the plane P parallel to the first direction (Z-axis direction) and the second direction (X-axis direction) is defined as the third direction. It is formed so as to be located in the third direction with respect to the main flow path 15a which is one flow path.
  • the heat exchanger 100 can suppress the increase in size of the refrigerant distributor 150 in the second direction in which the refrigerant flows, and extends the heat exchanger 100 through the conduit of the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
  • the heat exchanger 100 secures a wider heat transfer area of the heat transfer tube 70 as compared with a heat exchanger having a first flow path and a second flow path in the extending direction of the line of the heat transfer tube 70. Can be done. Therefore, the heat exchanger 100 can improve the heat exchange performance as compared with the heat exchanger having the first flow path and the second flow path in the extending direction of the conduit of the heat transfer tube 70. Therefore, the heat exchanger 100 can improve the suppression of the uneven flow of the refrigerant distribution with respect to the change in the refrigerant flow rate or the dryness depending on the operating state of the air conditioner, and has a distribution robustness that widens the range corresponding to the refrigerant flow rate and the like. Can be improved.
  • the heat exchanger 100 has a sub-flow path 25 so that the refrigerant can be transferred from the upper part of the main flow path 15a to the lower part of the main flow path 15a in a state where the liquid refrigerant stays in the upper part of the main flow path 15a depending on the operating state of the air conditioner.
  • the heat exchanger 100 provided with the refrigerant distributor 150 having the auxiliary flow path 25 transfers the refrigerant to each heat transfer tube 70 as compared with the heat exchanger provided with the refrigerant distributor having no auxiliary flow path 25. It can be evenly distributed.
  • the heat exchanger 100 can improve the heat exchange performance as compared with the heat exchanger provided with the refrigerant distributor which does not have the auxiliary flow path 25.
  • both ends of the main flow path 15a and the sub-flow path 25 overlap in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30.
  • the main flow path 15a, the distribution hole portion 26, and the insertion hole 31 are formed so as to overlap each other. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
  • both ends of the sub-flow path 25 which is the second flow path flow out the refrigerant to the inlet portion 25b where the refrigerant flows in from the main flow path 15a which is the first flow path and the main flow path 15a which is the first flow path. It is composed of an outlet portion 25c and an outlet portion 25c.
  • the inlet portion 25b and the outlet portion 25c are formed so as to extend in the third direction. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
  • the sub-flow path 25, which is the second flow path, is formed on both sides of the distribution hole portion 26 in the third direction. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
  • a plurality of distribution hole portions 26 are formed along the first direction (Z-axis direction).
  • Each of the plurality of distribution hole portions 26 functions as a throttle hole having a high flow resistance in the refrigerant flow path between the main flow path 15a which is the first flow path and each of the plurality of heat transfer tubes 70.
  • each distribution hole 26 functions as a throttle hole, so that the pressure in the main flow path 15a rises, and the pressure in the main flow path 15a and the pressure in the plurality of insertion holes 31 are respectively. The pressure difference between the pressure and the pressure increases.
  • the pressure difference between the pressure of the main flow path 15a and the pressure of the upper insertion hole 31 and the pressure difference between the pressure of the main flow path 15a and the pressure of the lower insertion hole 31 become more uniform.
  • the refrigerant in the main flow path 15a is evenly distributed to each insertion hole 31, and as a result, is evenly distributed to each heat transfer tube 70.
  • FIG. 8 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the second embodiment.
  • FIG. 9 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment.
  • the components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted.
  • the heat exchanger 100 according to the second embodiment is different from the heat exchanger 100 according to the first embodiment in that the refrigerant distributor 150 further includes the fourth plate-shaped member 40 and the fifth plate-shaped member 50.
  • the main body 151 of the refrigerant distributor 150 has a first plate-shaped member 10, a second plate-shaped member 20, a third plate-shaped member 30, a fourth plate-shaped member 40, and a fifth plate-shaped member 50.
  • Both the fourth plate-shaped member 40 and the fifth plate-shaped member 50 are formed by using a metal flat plate and have a strip-like shape long in one direction.
  • the contours of the outer edges of the first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 have the same shape as each other. There is.
  • the first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 have their respective plate thickness directions extending in the conduit of the heat transfer tube 70. It is arranged so as to be parallel to the direction. That is, the plate surfaces of the first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 are the conduits of the heat transfer tube 70. It is arranged so as to be perpendicular to the stretching direction.
  • the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 are from the heat transfer tube 70. It has a structure in which the layers are stacked in this order from the farthest distance.
  • the first plate-shaped member 10 is arranged at the position farthest from the heat transfer tube 70 in the main body 151, and the third plate-shaped member 30 is arranged at the position closest to the heat transfer tube 70 in the main body 151. Has been done.
  • the fourth plate-shaped member 40 is arranged between the first plate-shaped member 10 and the second plate-shaped member 20, and the plate surface of the fourth plate-shaped member 40 is the first plate-shaped member 10 and the second plate-shaped member 20. Adjacent to the plate surface of the plate-shaped member 20.
  • the fifth plate-shaped member 50 is arranged between the second plate-shaped member 20 and the third plate-shaped member 30, and the plate surface of the fifth plate-shaped member 50 is the second plate-shaped member 20 and the third plate-shaped member 20. Adjacent to the plate surface of the plate-shaped member 30.
  • the adjacent members of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 are joined by brazing.
  • the longitudinal direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 is in the first direction (Z-axis direction). It is arranged along the line.
  • the fourth plate-shaped member 40 has a communication hole 45 located between the main flow path 15a, which is the first flow path, and both ends of the sub-flow path 25, and the main flow path 15a, which is the first flow path, and the second distribution.
  • a second distribution hole 46 located between the hole 46 is formed.
  • the communication hole 45 and the second distribution hole 46 are through holes.
  • Two communication holes 45 are formed in the fourth plate-shaped member 40 on one end 151a side and two on the other end 151b side.
  • the communication hole 45 formed on the one end 151a side serves as an outlet when the refrigerant flows out from the sub flow path 25 to the main flow path 15a.
  • the communication hole 45 formed on the other end 151b side serves as an inlet when the refrigerant flows from the main flow path 15a into the sub-flow path 25.
  • the communication hole 45 is shown as a through hole forming a rectangular opening in FIG. 8, but the opening shape of the communication hole 45 is not limited to a rectangular shape.
  • the communication hole 45 is formed with the main flow path 15a and the inlet portion in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30. It is formed so as to be located between 25b. Further, the communication hole 45 is formed with the main flow path 15a in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30. It is formed so as to be located between the outlet portion 25c and the outlet portion 25c.
  • the communication hole 45 communicates with the main flow path 15a which is the first flow path and the sub flow path 25 which is the second flow path, and the main flow path 15a which is the first flow path and the sub flow path which is the second flow path. It serves as a flow path connecting the flow path 25.
  • the fourth plate-shaped member 40 is formed with a plurality of second distribution hole portions 46 each having a circular opening shape.
  • the second distribution hole portion 46 is formed near the center of the fourth plate-shaped member 40 in the third direction (Y-axis direction).
  • the plurality of second distribution hole portions 46 include the main flow path 15a and the heat transfer tube together with the distribution hole portion 26 formed in the second plate-shaped member 20 and the third distribution hole portion 51 formed in the fifth plate-shaped member 50 described later.
  • a flow path is formed between the heat transfer tubes 70 and the refrigerant is distributed to each heat transfer tube 70.
  • Each of the plurality of second distribution hole portions 46 is a through hole that penetrates the fourth plate-shaped member 40 in the plate thickness direction of the fourth plate-shaped member 40.
  • the plurality of second distribution hole portions 46 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the fourth plate-shaped member 40.
  • Each of the plurality of second distribution hole portions 46 forms a through hole penetrating the fourth plate-shaped member 40, and is provided corresponding to each of the plurality of heat transfer tubes 70.
  • each of the plurality of second distribution hole portions 46 is provided corresponding to each of the distribution hole portions 26 formed in the second plate-shaped member 20.
  • each of the plurality of second distribution hole portions 46 is provided corresponding to each of the third distribution hole portions 51 formed in the fifth plate-shaped member 50, which will be described later.
  • the opening shape of the second distribution hole portion 46 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape.
  • the flow path cross-sectional areas of the plurality of second distribution hole portions 46 are the same size. However, the flow path cross-sectional areas of the plurality of second distribution holes 46 are not limited to those having the same size, and may be formed to have different sizes.
  • a plurality of second distribution hole portions 46 are formed in the fourth plate-shaped member 40, but the second distribution hole portion 46 has a fourth plate shape. Only one may be formed on the member 40. In this case, the second distribution hole portion 46 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
  • Each of the plurality of second distribution hole portions 46 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fourth plate-shaped member 40. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the distribution hole portions 26 of the second plate-shaped member 20 when viewed in the plate thickness direction of the fourth plate-shaped member 40. .. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the third distribution hole portions 51 of the fifth plate-shaped member 50 when viewed in the plate thickness direction of the fourth plate-shaped member 40. ing.
  • each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30 when viewed in the plate thickness direction of the fourth plate-shaped member 40. There is. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the fourth plate-shaped member 40.
  • the second distribution hole portion 46 is transmitted. It is located between the heat pipe 70 and the main flow path 15a, which is the first flow path. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of second distribution hole portions 46.
  • the fourth plate-shaped member 40 has a flat plate-shaped closing portion 44.
  • a part of the closing portion 44 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fourth plate-shaped member 40.
  • the closing portion 44 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the second distribution hole portion 46.
  • the closing portion 44 covers a part of the sub-flow path 25 from the arrangement side of the first plate-shaped member 10.
  • the closing portion 44 covers at least the central portion 25a of the sub-flow path 25 from the arrangement side of the first plate-shaped member 10.
  • the closing portion 44 forms a part of the pipeline forming the sub-flow path 25.
  • the fifth plate-shaped member 50 is formed with a third distribution hole 51 located between the distribution hole 26 and the insertion hole 31.
  • the third distribution hole portion 51 is a through hole.
  • the fifth plate-shaped member 50 is formed with a plurality of third distribution holes 51 each having a circular opening shape.
  • the third distribution hole portion 51 is formed near the center of the fifth plate-shaped member 50 in the third direction (Y-axis direction).
  • the plurality of third distribution hole portions 51 include the main flow path 15a and the heat transfer tube 70 together with the distribution hole portion 26 formed in the second plate-shaped member 20 and the second distribution hole portion 46 formed in the fourth plate-shaped member 40.
  • a flow path is formed between the heat transfer tubes 70 to distribute the refrigerant to each heat transfer tube 70.
  • Each of the plurality of third distribution hole portions 51 is a through hole that penetrates the fifth plate-shaped member 50 in the plate thickness direction of the fifth plate-shaped member 50.
  • the plurality of third distribution hole portions 51 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the fifth plate-shaped member 50.
  • Each of the plurality of third distribution hole portions 51 forms a through hole penetrating the fifth plate-shaped member 50, and is provided corresponding to each of the plurality of heat transfer tubes 70.
  • each of the plurality of third distribution hole portions 51 is provided corresponding to each of the distribution hole portions 26 formed in the second plate-shaped member 20.
  • each of the plurality of third distribution hole portions 51 is provided corresponding to each of the second distribution hole portions 46 formed in the fourth plate-shaped member 40.
  • the opening shape of the third distribution hole 51 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape.
  • the flow path cross-sectional areas of the plurality of third distribution holes 51 are the same size. However, the flow path cross-sectional areas of the plurality of third distribution holes 51 are not limited to those having the same size, and may be formed to have different sizes.
  • a plurality of third distribution hole portions 51 are formed in the fifth plate-shaped member 50, but the third distribution hole portion 51 has a fifth plate shape. Only one may be formed on the member 50. In this case, the third distribution hole 51 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
  • Each of the plurality of third distribution hole portions 51 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fifth plate-shaped member 50. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the distribution hole portions 26 of the second plate-shaped member 20 when viewed in the plate thickness direction of the fifth plate-shaped member 50. .. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the second distribution hole portions 46 of the fourth plate-shaped member 40 when viewed in the plate thickness direction of the fifth plate-shaped member 50. ing.
  • each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30 when viewed in the plate thickness direction of the fifth plate-shaped member 50. There is. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the fifth plate-shaped member 50.
  • the third distribution hole portion 51 is transmitted. It is located between the heat pipe 70 and the main flow path 15a, which is the first flow path. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of third distribution hole portions 51.
  • the fifth plate-shaped member 50 has a flat plate-shaped closing portion 53.
  • a part of the closing portion 53 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fifth plate-shaped member 50.
  • the closing portion 53 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the third distribution hole portion 51.
  • the closing portion 53 covers a part of the sub-flow path 25 from the arrangement side of the third plate-shaped member 30.
  • the closing portion 53 covers at least the central portion 25a of the sub-flow path 25 from the arrangement side of the third plate-shaped member 30.
  • the closing portion 53 forms a part of the pipeline forming the sub-flow path 25.
  • FIG. 10 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment.
  • the refrigerant flowing into the refrigerant distributor 150 is a gas-liquid two-phase flow.
  • the gas-liquid two-phase refrigerant flows into the main body 151 from the refrigerant inflow pipe 60, and as shown by the arrow UF in FIG. 10, the main flow path 15a formed in the first plate-shaped member 10 is formed from one end 151a to the other. Flows vertically upward toward the end 151b of.
  • a part of the refrigerant that rises vertically and flows is the second distribution hole portion 46 of the fourth plate-shaped member 40, the distribution hole portion 26 of the second plate-shaped member 20, and the third distribution hole portion of the fifth plate-shaped member 50. It passes through 51 in this order and is distributed to each heat transfer tube 70 through an insertion hole 31 formed in the third plate-shaped member 30.
  • the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 25b provided in the second plate-shaped member 20 through the communication hole 45 communicating with the upper end portion 15a1 of the main flow path 15a.
  • the refrigerant flows from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path, toward the outside, which is the third direction.
  • the refrigerant flowing in from the inlet portion 25b of the sub-channel 25 flows downward along the central portion 25a of the sub-channel 25 formed in the second plate-shaped member 20. ..
  • the refrigerant that has reached the lower end of the central portion 25a of the sub-flow path 25 flows out from the outlet portion 25c to the main flow path 15a through the communication hole 45 that communicates with the lower end portion 15a2 of the main flow path 15a.
  • the refrigerant flows inward in the third direction from the sub-flow path 25 which is the second flow path toward the main flow path 15a which is the first flow path.
  • the refrigerant flowing out from the outlet portion 25c to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
  • FIG. 11 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment.
  • the horizontal axis represents the refrigerant flow rate [kg / h]
  • the vertical axis represents the distance [m] from the refrigerant inlet 18 in the first direction in which the heat transfer tubes 70 are arranged.
  • the liquid refrigerant staying in the upper part of the main flow path 15a passes through the main flow path 25. Return to the bottom of 15a. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases. Further, as shown by the arrow MD between the dotted line A and the solid line B, the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a.
  • the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
  • the refrigerant distributor 150 has a fourth plate-shaped member 40 and a fifth plate-shaped member 50.
  • the fourth plate-shaped member 40 is divided into a communication hole 45 located between the main flow path 15a, which is the first flow path, and both ends of the sub-flow path 25, and the main flow path 15a, which is the first flow path.
  • a second distribution hole 46 located between the hole 26 is formed.
  • the fifth plate-shaped member 50 is formed with a third distribution hole portion 51 located between the distribution hole portion 26 and the insertion hole 31.
  • the main body 151 of the refrigerant distributor 150 has the above-mentioned penetration of the fourth plate-shaped member 40 and the fifth plate-shaped member 50, so that the refrigerant flows between the main flow path 15a and the sub-flow path 25 and the mainstream. It does not interfere with the flow of the refrigerant from the passage 15a to the heat transfer tube 70. Further, the main body 151 of the refrigerant distributor 150 can form a conduit for the sub-flow path 25 by the closing portion 44 of the fourth plate-shaped member 40 and the closing portion 53 of the fifth plate-shaped member 50. That is, the main body 151 of the refrigerant distributor 150 does not require the flat plate portion 11 of the first plate-shaped member 10 and the flat plate portion 34 of the third plate-shaped member 30 in order to form the conduit of the sub-flow path 25.
  • the second plate-shaped member 20 has a side flow so as to overlap the main flow path 15a of the first plate-shaped member 10 and the insertion hole 31 of the third plate-shaped member 30 when viewed in the stacking direction of each plate-shaped member.
  • the road 25 can be formed.
  • the main body 151 of the refrigerant distributor 150 can increase the width of the sub-flow path 25 formed in the second plate-shaped member 20 in the third direction (Y-axis direction), and the sub-flow path 25 can be increased.
  • the volume of the can be increased.
  • the refrigerant distributor 150 of the heat exchanger 100 can circulate a large amount of refrigerant staying in the upper part when the pressure loss on the sub-flow path 25 side is small and the circulation flow rate is high, and suppresses the refrigerant drift.
  • the performance of the heat exchanger 100 can be improved.
  • FIG. 12 is an exploded perspective view conceptually showing the main configuration of the heat exchanger 100 according to the third embodiment.
  • FIG. 13 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment.
  • FIG. 14 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment.
  • the components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted.
  • the heat exchanger 100 according to the third embodiment is different from the outlet portion 25c of the heat exchanger 100 according to the first embodiment in that the angle of the pipe axis of the outlet portion 25c1 is specified.
  • the subchannel 25 has a central portion 25a, an inlet portion 25b, and an outlet portion 25c1.
  • the central portion 25a forms a flow path extending in the first direction (Z-axis direction).
  • the outlet portion 25c1 is formed at the other end portion 25a2 of the central portion 25a in the first direction (Z-axis direction).
  • the pipe axis TA of the outlet portion 25c1 is inclined with respect to the first direction (Z-axis direction) and the third direction (Y-axis direction) so as to approach the diagonal DL of the second plate-shaped member 20. Therefore, as shown by the arrows IF and UF in FIG. 14, the outlet portion 25c1 has a vector component in which the direction in which the refrigerant flowing out from the outlet portion 25c1 flows has a vector component in the direction in which the refrigerant flowing out from the refrigerant inflow pipe 60 flows. It is formed so as to be inclined with respect to the first direction and the third direction. That is, the refrigerant flowing out from the outlet portion 25c1 is directed in the direction along the flow of the refrigerant flowing through the main flow path 15a.
  • the outlet angle ⁇ which is the angle between the pipe axis TA direction of the outlet portion 25c1 and the gravity direction GD, is formed to be an angle of 90 degrees or more.
  • FIG. 15 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment.
  • the horizontal axis represents the refrigerant flow rate [kg / h]
  • the vertical axis represents the distance [m] from the refrigerant inflow port 18 in the first direction in which the heat transfer tubes 70 are arranged.
  • the liquid refrigerant staying in the upper part of the main flow path 15a passes through the main flow path 25. Return to the bottom of 15a. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases. Further, as shown by the arrow MD between the dotted line A and the solid line B, the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a.
  • the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
  • the outlet portion 25c1 has a vector component in the direction in which the refrigerant flowing out from the outlet portion 25c1 flows in the direction in which the refrigerant flows out from the refrigerant inflow pipe 60. It is formed so as to be inclined with respect to the first direction and the third direction.
  • the direction of the outlet portion 25c1 of the sub-flow path 25 formed in the second plate-shaped member 20 is the vertical ascending direction, and the flow vector of the refrigerant when merging from the sub-flow path 25 to the main flow path 15a is upward. , The upward inertial force of the refrigerant increases.
  • the refrigerant distributor 150 of the heat exchanger 100 promotes the circulation of the refrigerant in the main flow path 15a and the sub-flow path 25. Then, the refrigerant distributor 150 of the heat exchanger 100 can circulate a large amount of refrigerant staying in the upper part of the main flow path 15a, and can suppress the drift of the refrigerant.
  • FIG. 16 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the fourth embodiment.
  • FIG. 17 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the fourth embodiment.
  • FIG. 18 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the fourth embodiment.
  • the components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted.
  • the heat exchanger 100 according to the fourth embodiment is different from the heat exchanger 100 according to the first embodiment in that the configuration of the main flow path 15a, which is the first flow path, is further specified.
  • the first flow path portion 15 forms the main flow path 15a, which is the first flow path, inside.
  • the main flow path 15a which is the first flow path
  • the main flow path 15a is cut off from one lower end portion 15a2 on the side communicating with the refrigerant inflow pipe 60 toward the other upper end portion 15a1. It is formed so that the area is small.
  • the first direction Z-axis direction
  • the main flow path 15a is formed so that the cross-sectional area of the flow path decreases as it goes upward.
  • the first flow path portion 15 has a rectangular cross-sectional shape.
  • the cross-sectional shape of the first flow path portion 15 is not limited to a rectangle, and may be, for example, a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape.
  • the first flow path portion 15 extends from one end portion 151a of the main body portion to the other end portion 151b along the longitudinal direction of the first plate-shaped member 10. Both ends of the first flow path portion 15 in the stretching direction are closed.
  • the first flow path portion 15 has a side wall 15b formed in a trapezoidal shape when viewed in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30.
  • the first flow path portion 15 is formed in a square columnar shape having a side wall 15b.
  • the first flow path portion 15 is formed so as to taper from the lower end portion 15a2 on the refrigerant inflow port 18 side toward the other upper end portion 15a1 in the longitudinal direction of the first plate-shaped member 10.
  • the first flow path portion 15 is not limited to the one formed in a square columnar shape having the side wall 15b, and may have another shape such as a truncated cone shape or a truncated cone shape. May be good.
  • the main flow path 15a which is the first flow path, is formed so that the cross-sectional area of the flow path decreases from one lower end portion 15a2 on the side communicating with the refrigerant inflow pipe 60 toward the other upper end portion 15a1.
  • the flow path cross-sectional area of the main flow path 15a is formed to be smaller toward the upper vertical direction, so that the refrigerant distributor 150 of the heat exchanger 100 is formed in the main flow path 15a.
  • the flow velocity of the refrigerant can be increased.
  • the refrigerant distributor 150 of the heat exchanger 100 can reach the uppermost part of the main flow path 15a and suppress the drift of the refrigerant. can do.
  • FIG. 19 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the fifth embodiment.
  • FIG. 20 is a side view conceptually showing the inside of the refrigerant distributor 150 shown in FIG.
  • FIG. 21 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the fifth embodiment.
  • the components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted.
  • the refrigerant distributors 150 of the first to fourth embodiments are configured by laminating the first plate-shaped members 10 to the fifth plate-shaped members 50 and the like.
  • the main body 151 of the refrigerant distributor 150 of the fifth embodiment is configured by using a tubular member.
  • the refrigerant distributor 150 main body 151 extends in the first direction (Z-axis direction) and is connected to one end of each of the plurality of heat transfer tubes 70 to distribute the refrigerant to the plurality of heat transfer tubes 70.
  • the main body 151 of the refrigerant distributor 150 has a tubular portion 90 extending in the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. Further, in the hollow portion 95 in the tubular portion 90, the main body 151 of the refrigerant distributor 150 separates the main flow path 15a and the sub flow path 25 in the third direction, and inlets that are through holes at both ends in the first direction. It has a wall portion 91 in which a portion 92a and an outlet portion 92b are formed. Further, the main body 151 of the refrigerant distributor 150 has a lid portion 94 that closes both ends of the tubular portion 90, respectively.
  • the tubular portion 90 is formed in a hollow cylindrical shape extending in the arrangement direction of the heat transfer tubes 70.
  • the tubular portion 90 is not limited to a cylindrical shape, and may be tubular, and may be formed in a rectangular parallelepiped box shape, for example.
  • the tubular portion 90 has a first tubular portion 90a connected to the refrigerant inflow pipe 60 and a second tubular portion 90b connected to the heat transfer pipe 70.
  • the first tubular portion 90a and the second tubular portion 90b are formed in a semicircular shape in a cross section perpendicular to the first direction (Z-axis direction).
  • the tubular portion 90 does not have a structure in which the first tubular portion 90a and the second tubular portion 90b are divided, but the first tubular portion 90a and the second tubular portion 90b are integrally lightly formed. It may have a structure.
  • the wall portion 91 has a strip-like shape that is long in one direction.
  • the wall portion 91 is a plate-shaped portion extending in the arrangement direction of the plurality of heat transfer tubes 70, and the longitudinal direction of the wall portion 91 is the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. .. Further, the lateral direction of the wall portion 91 is the second direction (X-axis direction), which is the extending direction of the pipe line of the heat transfer tube 70. Further, the plate thickness direction of the wall portion 91 is the major axis direction of the heat transfer tube 70.
  • the wall portion 91 forms a plate surface extending in the first direction (Z-axis direction) and the second direction (X-axis direction).
  • the wall portion 91 forms an outlet portion 92b at one end 91b on the side to which the refrigerant inflow pipe 60 is connected. Further, the wall portion 91 forms an inlet portion 92a at the other end portion 91a.
  • the inlet portion 92a and the outlet portion 92b are through holes that penetrate the wall portion 91 in the plate thickness direction of the wall portion 91. In the main body 151, the direction of the flow path formed by the inlet portion 92a and the outlet portion 92b is the third direction.
  • the wall portion 91 is further formed with a plurality of insertion holes 93 into which one ends of the plurality of heat transfer tubes 70 are inserted.
  • Each of the plurality of insertion holes 93 is a through hole that penetrates the wall portion 91 in the plate thickness direction of the wall portion 91. Further, each of the plurality of insertion holes 93 is also a notch portion cut out from the edge portion 91e extending in the first direction (Z-axis direction) toward the opposite edge portion 91d.
  • the plurality of insertion holes 93 are arranged in parallel in the vertical direction along the longitudinal direction of the wall portion 91.
  • the plurality of insertion holes 93 are provided independently of each other corresponding to each of the plurality of heat transfer tubes 70.
  • the insertion hole 93 has a flat opening shape similar to the outer peripheral shape of the heat transfer tube 70.
  • the open end of the insertion hole 93 is joined to the outer peripheral surface of the heat transfer tube 70 over the entire circumference by brazing.
  • the lid portion 94 closes both ends of the tubular portion 90 in the extending direction.
  • the lid portion 94 may be a plate-shaped member as long as it closes both ends of the tubular portion 90 in the extending direction, or may be a member that covers the end portions of the tubular portion 90.
  • the hollow portion 95 in the tubular portion 90 is formed by the tubular portion 90 and the lid portion 94 that closes both ends of the tubular portion 90. Further, as shown in FIG. 21, the hollow portion 95 in the tubular portion 90 is separated into two spaces, a first space S1 and a second space S2, by a wall portion 91. The first space S1 and the second space S2 communicate with each other via the inlet portion 92a and the outlet portion 92b.
  • the main body 151 of the refrigerant distributor 150 has a first space S1 as a main flow path 15a.
  • the main flow path 15a is a flow path in which the refrigerant flows from one end 151a on the side to which the refrigerant inflow pipe 60 of the main body 151 is connected to the other end 151b.
  • the main flow path 15a is a flow path through which the refrigerant rises.
  • the main flow path 15a which is the first flow path, is formed so as to extend in the first direction, communicates with a plurality of heat transfer tubes 70, and has a refrigerant in the refrigerant distributor 150 at the lower end portion 15a2 in the first direction. Is connected to the refrigerant inflow pipe 60.
  • the main body 151 of the refrigerant distributor 150 includes a second space S2, an inlet portion 92a, and an outlet portion 92b as a sub-flow path 25.
  • the sub-flow path 25 is a flow path through which the refrigerant flows from the other end 151b to one end 151a on the side to which the refrigerant inflow pipe 60 of the main body 151 is connected.
  • the sub-flow path 25 is a flow path through which the refrigerant drops.
  • the sub-flow path 25, which is the second flow path, extends in the first direction and is formed so that both ends of the inlet portion 92a and the outlet portion 92b are connected to the main flow path 15a, which is the first flow path.
  • the sub-flow path 25, which is the second flow path, is formed so as to be located in the third direction with respect to the main flow path 15a, which is the first flow path. That is, the main flow path 15a and the sub-flow path 25 are formed so as to be located on the upstream side and the downstream side in the ventilation direction of the wind formed by the outdoor blower 108 or the indoor blower 109 shown in FIG.
  • the main body 151 of the refrigerant distributor 150 has a main flow path 15a, which is a first flow path through which the refrigerant flows, and a sub flow path 25, which is a second flow path, formed therein.
  • the main body 151 of the refrigerant distributor 150 forms a flow path through which the refrigerant circulates by the main flow path 15a and the sub flow path 25.
  • FIG. 22 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor of the modified example constituting the heat exchanger according to the fifth embodiment.
  • the tubular portion 90 is not limited to the cylindrical shape as shown in FIG. 21.
  • the tubular portion 90 may be tubular, and may be formed in a semi-cylindrical shape as shown in FIG. 22, for example.
  • FIG. 23 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the fifth embodiment. Similar to the first embodiment, the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 92a provided in the second plate-shaped member 20 communicating with the upper end portion 15a1 of the main flow path 15a. At this time, as shown by the arrow OF, the refrigerant flows in the third direction from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path. Then, as shown by the arrow DF, the refrigerant flowing in from the inlet portion 92a of the sub-flow path 25 flows downward along the sub-flow path 25 formed in the second plate-shaped member 20 in the direction of gravity.
  • the refrigerant that has reached the lower end of the sub-flow path 25 flows out to the main flow path 15a from the outlet portion 92b that communicates with the lower end portion 15a2 of the main flow path 15a.
  • the refrigerant flows in the third direction from the sub-flow path 25, which is the second flow path, toward the main flow path 15a, which is the first flow path.
  • the refrigerant flowing out from the outlet portion 92b to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
  • the refrigerant distributor 150 separates the tubular portion 90, the lid portion 94, the main flow path 15a which is the first flow path, and the sub flow path 25 which is the second flow path in the third direction, and both ends in the first direction.
  • the portion has a wall portion 91 in which an inlet portion 92a and an outlet portion 92b, which are through holes, are formed.
  • the plurality of heat transfer tubes 70 are connected to the wall portion 91 so as to communicate with the main flow path 15a which is the first flow path and the sub flow path 25 which is the second flow path.
  • the main body 151 of the heat exchanger 100 is a tubular body such as a circular pipe, it is possible to suppress an increase in the size of the refrigerant distributor 150 in the second direction in which the refrigerant flows, and the range of structural contracts can be concluded.
  • the heat exchanger 100 can be enlarged in the second direction in which the conduit of the heat transfer tube 70 extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
  • the refrigeration cycle device 200 includes the heat exchanger 100 according to any one of the first to fifth embodiments. Therefore, the refrigeration cycle device 200 can obtain the same effect as that of any one of the first to fifth embodiments.
  • each of the above embodiments 1 to 5 can be implemented in combination with each other.
  • the configuration shown in the above embodiment is an example, and can be combined with another known technique, and a part of the configuration is omitted or changed without departing from the gist. It is also possible.
  • the refrigerant distributors 150 and the like according to the first to fifth embodiments may be of a vertical type in which the main body 151 extends in the vertical direction or a horizontal type in which the main body 151 extends in the horizontal direction.
  • the refrigerant distributor 150 and the like according to the first to fifth embodiments may have a configuration in which the main body 151 is tilted with respect to the vertical direction.

Abstract

A heat exchanger comprising: a plurality of heat transfer tubes positioned so as to leave gaps between each other in a first direction, the plurality of heat transfer tubes channeling a refrigerant in a second direction that intersects the first direction; and a refrigerant distributor extending in the first direction, the refrigerant distributor being connected to one end of each of the plurality of heat transfer tubes and distributing the refrigerant to the plurality of heat transfer tubes. The refrigerant distributor has formed in the interior thereof a first channel and a second channel in which the refrigerant flows. The first channel is formed so as to extend in the first direction. The first channel connects to an inflow tube, which communicates with the plurality of heat transfer tubes and causes the refrigerant to flow into the interior of the refrigerant distributor. The second channel is formed so as to extend in the first direction and so that both end sections connect to the first channel, and is formed so as to be located in a third direction relative to the first channel, where the third direction is defined as a direction that intersects a plane parallel to the first direction and the second direction.

Description

熱交換器及び冷凍サイクル装置Heat exchanger and refrigeration cycle equipment
 本開示は、熱交換器及び当該熱交換器を備えた冷凍サイクル装置に関するものである。 The present disclosure relates to a heat exchanger and a refrigeration cycle device equipped with the heat exchanger.
 近年、冷媒量の削減あるいは熱交換器の高性能化のため、空調機用の熱交換器に用いられる伝熱管の細管化が進められている。熱交換器は、伝熱管の細管化が進む中で、冷媒の圧力損失の増加を抑制するために、従来の熱交換器と比較して熱交換器のパス数(分岐数)が増加されている。そのため、熱交換器には、多分岐の冷媒分配器が設けられている(例えば、特許文献1参照)。熱交換器の性能と、使用する冷媒量の削減との両立には、各パスへの冷媒の偏流を抑制し、分配流路の省容積化によって使用する冷媒量を削減し、かつ、伝熱面積を広く確保しつつも熱交換器の設置スペースを阻害しないコンパクトな冷媒分配器が求められる。 In recent years, in order to reduce the amount of refrigerant or improve the performance of heat exchangers, the heat transfer tubes used in heat exchangers for air conditioners have been made thinner. As heat exchangers are becoming thinner, the number of heat exchanger passes (number of branches) is increased compared to conventional heat exchangers in order to suppress an increase in refrigerant pressure loss. There is. Therefore, the heat exchanger is provided with a multi-branch refrigerant distributor (see, for example, Patent Document 1). In order to achieve both the performance of the heat exchanger and the reduction of the amount of refrigerant used, it is possible to suppress the drift of the refrigerant to each path, reduce the amount of refrigerant used by reducing the volume of the distribution flow path, and transfer heat. A compact refrigerant distributor that secures a large area but does not hinder the installation space of the heat exchanger is required.
 特許文献1の熱交換器は、互いに並んで配置された複数の伝熱管と、伝熱管の一端が接続されており、鉛直方向に沿って延びた冷媒分配器であるヘッダ集合管と、伝熱管に接合された複数のフィンとを備えている。このヘッダ集合管の内部空間は、仕切板によって伝熱管の一端が接続されている側の第1空間と、仕切板に対して第1空間側とは反対側の空間である第2空間とに仕切られている。また、仕切板の上端と下端とには、第1空間と第2空間とを連通させる連通路が設けられている。特許文献1の熱交換器は、当該構成を有することで、第1空間と第2空間との間で冷媒をループさせている。そして、特許文献1の熱交換器は、第1空間と第2空間との間で冷媒をループさせることで、冷媒の偏流を小さく抑えることが可能になるとされている。 The heat exchanger of Patent Document 1 has a plurality of heat transfer tubes arranged side by side, a header collecting pipe which is a refrigerant collecting pipe which is connected to one end of the heat transfer pipe and extends in the vertical direction, and a heat transfer pipe. It has multiple fins joined to. The internal space of the header collecting pipe is divided into a first space on the side where one end of the heat transfer tube is connected by a partition plate and a second space on the side opposite to the first space side with respect to the partition plate. It is partitioned. Further, at the upper end and the lower end of the partition plate, a communication passage for communicating the first space and the second space is provided. The heat exchanger of Patent Document 1 has such a configuration, so that the refrigerant is looped between the first space and the second space. The heat exchanger of Patent Document 1 is said to be able to suppress the drift of the refrigerant to a small value by looping the refrigerant between the first space and the second space.
特開2015-68622号公報JP-A-2015-68622
 しかしながら、特許文献1の熱交換器は、気液二相冷媒が上向きに流れる流路を形成する第1空間と、上部から下部へ冷媒を戻す循環流路を形成する第2空間とが、伝熱管の管路の延伸方向に位置している。特許文献1に記載の冷媒分配器は、当該構成により伝熱管の管路の延伸方向に大型化するため、構造成約上、伝熱管は管路の延伸方向の長さが小さくなり伝熱管の伝熱面積が小さくなってしまう。そのため、特許文献1の熱交換器は、従来の熱交換器と比較して熱交換性能が低下する恐れがある。 However, in the heat exchanger of Patent Document 1, a first space forming a flow path through which the gas-liquid two-phase refrigerant flows upward and a second space forming a circulation flow path for returning the refrigerant from the upper part to the lower part are transmitted. It is located in the extending direction of the conduit of the heat pipe. Since the refrigerant distributor described in Patent Document 1 is enlarged in the extending direction of the heat transfer tube line due to the configuration, the length of the heat transfer tube in the extension direction of the heat transfer tube is reduced due to the structural contract, and the heat transfer tube is transmitted. The heat area becomes small. Therefore, the heat exchanger of Patent Document 1 may have lower heat exchange performance than the conventional heat exchanger.
 本開示は、上述のような課題を解決するためのものであり、伝熱管の伝熱面積を広く確保しつつ、伝熱管の管路の延伸方向に大型化せずにコンパクトな冷媒分配器を備えた熱交換器及び冷凍サイクル装置を提供することを目的とする。 The present disclosure is for solving the above-mentioned problems, and provides a compact refrigerant distributor without increasing the size in the extending direction of the heat transfer pipe while ensuring a wide heat transfer area of the heat transfer pipe. It is an object of the present invention to provide a heat exchanger and a refrigeration cycle device provided.
 本開示に係る熱交換器は、第1方向に互いに間隔をあけて配置された複数の伝熱管であって、第1方向と交差する第2方向に冷媒を流通させる複数の伝熱管と、第1方向に延伸し、複数の伝熱管のそれぞれの一端に接続されて複数の伝熱管に冷媒を分配する冷媒分配器と、を備え、冷媒分配器は、冷媒が流れる第1流路及び第2流路が内部に形成されており、第1流路は、第1方向に延伸するように形成されており、複数の伝熱管と連通すると共に、冷媒分配器の内部に冷媒を流入させる流入管と接続しており、第2流路は、第1方向に延伸し、両端部が第1流路と接続するように形成されており、第1方向及び第2方向に平行な面に交差する方向を第3方向と定義した場合に、第1流路に対して第3方向に位置するように形成されている。 The heat exchanger according to the present disclosure is a plurality of heat transfer tubes arranged at intervals in the first direction, and includes a plurality of heat transfer tubes for flowing a refrigerant in a second direction intersecting the first direction, and a first. A refrigerant distributor extending in one direction and connected to one end of each of the plurality of heat transfer tubes to distribute the refrigerant to the plurality of heat transfer tubes is provided, and the refrigerant distributor includes a first flow path and a second flow path through which the refrigerant flows. The flow path is formed inside, and the first flow path is formed so as to extend in the first direction, and is an inflow pipe that communicates with a plurality of heat transfer tubes and allows the refrigerant to flow into the inside of the refrigerant distributor. The second flow path is formed so as to extend in the first direction and both ends are connected to the first flow path, and intersect the planes parallel to the first direction and the second direction. When the direction is defined as the third direction, it is formed so as to be located in the third direction with respect to the first flow path.
 本開示に係る冷凍サイクル装置は、本開示に係る熱交換器を備えたものである。 The refrigeration cycle device according to the present disclosure is provided with the heat exchanger according to the present disclosure.
 本開示によれば、熱交換器は、冷媒が流れる第1流路及び第2流路が内部に形成された冷媒分配器を有する。第2流路は、第1方向に延伸し、両端部が第1流路と接続するように形成されている。この第2流路は、第1方向及び第2方向に平行な面に交差する方向を第3方向と定義した場合に、第1流路に対して第3方向に位置するように形成されている。そのため、熱交換器は、冷媒を流通させる第2方向への冷媒分配器の大型化を抑制することができ、構造成約の範囲内で熱交換器を伝熱管の管路の延びる方向へ大きくすることができる。そのため、本開示の熱交換器100は、伝熱管の伝熱面積を広く確保しつつ、冷媒分配器を伝熱管の管路の延伸方向に大型化せずにコンパクトにすることができる。 According to the present disclosure, the heat exchanger has a refrigerant distributor in which a first flow path and a second flow path through which the refrigerant flows are formed. The second flow path is formed so as to extend in the first direction and connect both ends to the first flow path. The second flow path is formed so as to be located in the third direction with respect to the first flow path when the direction intersecting the first direction and the plane parallel to the second direction is defined as the third direction. There is. Therefore, the heat exchanger can suppress the increase in size of the refrigerant distributor in the second direction in which the refrigerant flows, and the heat exchanger is enlarged in the direction in which the conduit of the heat transfer tube extends within the range of the structural contract. be able to. Therefore, in the heat exchanger 100 of the present disclosure, the heat transfer area of the heat transfer tube can be secured widely, and the refrigerant distributor can be made compact without increasing in size in the extending direction of the heat transfer tube line.
実施の形態1に係る熱交換器を備えた冷凍サイクル装置の構成を示す冷媒回路図である。It is a refrigerant circuit diagram which shows the structure of the refrigerating cycle apparatus provided with the heat exchanger according to Embodiment 1. FIG. 実施の形態1に係る熱交換器の要部構成を概念的に示す側面図である。It is a side view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 1. FIG. 実施の形態1に係る熱交換器の要部構成を概念的に示す分解斜視図である。It is an exploded perspective view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 1. FIG. 実施の形態1に係る熱交換器を構成する伝熱管の構成を示す断面図である。It is sectional drawing which shows the structure of the heat transfer tube which comprises the heat exchanger which concerns on Embodiment 1. FIG. 実施の形態1に係る熱交換器を構成する冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the first embodiment. 実施の形態1に係る熱交換器を構成する冷媒分配器内の冷媒の流れを示した概念図である。It is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 1. FIG. 実施の形態1に係る熱交換器を構成する冷媒分配器内の冷媒の流量分布を表した図である。It is a figure which showed the flow rate distribution of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 1. FIG. 実施の形態2に係る熱交換器の要部構成を概念的に示す分解斜視図である。It is an exploded perspective view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 2. FIG. 実施の形態2に係る熱交換器を構成する冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of a refrigerant distributor constituting the heat exchanger according to the second embodiment. 実施の形態2に係る熱交換器を構成する冷媒分配器内の冷媒の流れを示した概念図である。It is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 2. FIG. 実施の形態2に係る熱交換器を構成する冷媒分配器内の冷媒の流量分布を表した図である。It is a figure which showed the flow rate distribution of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 2. FIG. 実施の形態3に係る熱交換器の要部構成を概念的に示す分解斜視図である。It is an exploded perspective view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 3. FIG. 実施の形態3に係る熱交換器を構成する冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the third embodiment. 実施の形態3に係る熱交換器を構成する冷媒分配器内の冷媒の流れを示した概念図である。It is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 3. FIG. 実施の形態3に係る熱交換器を構成する冷媒分配器内の冷媒の流量分布を表した図である。It is a figure which showed the flow rate distribution of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 3. FIG. 実施の形態4に係る熱交換器の要部構成を概念的に示す分解斜視図である。It is an exploded perspective view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 4. FIG. 実施の形態4に係る熱交換器を構成する冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the fourth embodiment. 実施の形態4に係る熱交換器を構成する冷媒分配器内の冷媒の流れを示した概念図である。It is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 4. FIG. 実施の形態5に係る熱交換器の要部構成を概念的に示す分解斜視図である。It is an exploded perspective view which conceptually shows the main part structure of the heat exchanger which concerns on Embodiment 5. 図19に示す冷媒分配器の内部を概念的に示す側面図である。It is a side view which conceptually shows the inside of the refrigerant distributor shown in FIG. 実施の形態5に係る熱交換器を構成する冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing a communication position between a first flow path and a second flow path of the refrigerant distributor constituting the heat exchanger according to the fifth embodiment. 実施の形態5に係る熱交換器を構成する変形例の冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。FIG. 5 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor of the modified example constituting the heat exchanger according to the fifth embodiment. 実施の形態5に係る熱交換器を構成する冷媒分配器内の冷媒の流れを示した概念図である。It is a conceptual diagram which showed the flow of the refrigerant in the refrigerant distributor which comprises the heat exchanger which concerns on Embodiment 5. FIG.
 以下、実施の形態1に係る熱交換器100及び冷凍サイクル装置200について図面等を参照しながら説明する。なお、図1を含む以下の図面では、各構成部材の相対的な寸法の関係及び形状等が実際のものとは異なる場合がある。また、以下の図面において、同一の符号を付したものは、同一又はこれに相当するものであり、このことは明細書の全文において共通することとする。また、理解を容易にするために方向を表す用語(例えば「上」、「下」、「右」、「左」、「前」及び「後」等)を適宜用いるが、それらの表記は、説明の便宜上、そのように記載しているだけであって、装置あるいは部品の配置及び向きを限定するものではない。明細書中において、各構成部材同士の位置関係、各構成部材の延伸方向、及び各構成部材の配列方向は、原則として、室外熱交換器105が使用可能な状態に設置されたときのものである。 Hereinafter, the heat exchanger 100 and the refrigeration cycle device 200 according to the first embodiment will be described with reference to the drawings and the like. In the following drawings including FIG. 1, the relative dimensional relationships and shapes of the constituent members may differ from the actual ones. Further, in the following drawings, those having the same reference numerals are the same or equivalent thereof, and this shall be common to the entire text of the specification. In addition, terms that indicate directions (for example, "top", "bottom", "right", "left", "front", "rear", etc.) are used as appropriate for ease of understanding. For convenience of explanation, it is described as such, and does not limit the arrangement and orientation of the device or component. In the specification, the positional relationship between each component, the extension direction of each component, and the arrangement direction of each component are, in principle, those when the outdoor heat exchanger 105 is installed in a usable state. be.
実施の形態1.
[冷凍サイクル装置200]
 図1は、実施の形態1に係る熱交換器100を備えた冷凍サイクル装置200の構成を示す冷媒回路図である。なお、図1において、点線で示す矢印は、冷媒回路110において、冷房運転時における冷媒の流れる方向を示すものであり、実線で示す矢印は、暖房運転時における冷媒の流れる方向を示すものである。まず、図1を用いて後述する熱交換器100を備えた冷凍サイクル装置200について説明する。
Embodiment 1.
[Refrigeration Cycle Device 200]
FIG. 1 is a refrigerant circuit diagram showing a configuration of a refrigeration cycle device 200 including the heat exchanger 100 according to the first embodiment. In FIG. 1, the arrow indicated by the dotted line indicates the direction in which the refrigerant flows in the refrigerant circuit 110 during the cooling operation, and the arrow indicated by the solid line indicates the direction in which the refrigerant flows during the heating operation. .. First, the refrigeration cycle apparatus 200 provided with the heat exchanger 100, which will be described later, will be described with reference to FIG.
 本実施の形態では、冷凍サイクル装置200として空気調和装置を例示しているが、冷凍サイクル装置200は、例えば、冷蔵庫あるいは冷凍庫、自動販売機、空気調和装置、冷凍装置、給湯器などの、冷凍用途または空調用途に使用される。なお、図示した冷媒回路110は一例であって、回路要素の構成等について実施の形態で説明した内容に限定されるものではなく、実施の形態に係る技術の範囲内で適宜変更が可能である。 In the present embodiment, the air conditioner is exemplified as the refrigerating cycle device 200, but the refrigerating cycle device 200 is used for refrigerating, for example, a refrigerator or a freezer, a vending machine, an air conditioner, a refrigerating device, a water heater, and the like. Used for applications or air conditioning applications. The illustrated refrigerant circuit 110 is an example, and the configuration of circuit elements and the like is not limited to the contents described in the embodiment, and can be appropriately changed within the scope of the technique according to the embodiment. ..
 冷凍サイクル装置200は、圧縮機101、流路切替装置102、室内熱交換器103、減圧装置104及び室外熱交換器105が冷媒配管を介して環状に接続された冷媒回路110を有している。冷凍サイクル装置200は、室外機106及び室内機107を有している。室外機106には、圧縮機101、流路切替装置102、室外熱交換器105及び減圧装置104と、室外熱交換器105に室外空気を供給する室外送風機108と、が収容されている。室内機107には、室内熱交換器103と、室内熱交換器103に空気を供給する室内送風機109と、が収容されている。室外機106と室内機107との間は、冷媒配管の一部である2本の延長配管111及び延長配管112を介して接続されている。 The refrigerating cycle device 200 has a refrigerant circuit 110 in which a compressor 101, a flow path switching device 102, an indoor heat exchanger 103, a decompression device 104, and an outdoor heat exchanger 105 are cyclically connected via a refrigerant pipe. .. The refrigeration cycle device 200 has an outdoor unit 106 and an indoor unit 107. The outdoor unit 106 includes a compressor 101, a flow path switching device 102, an outdoor heat exchanger 105 and a decompression device 104, and an outdoor blower 108 that supplies outdoor air to the outdoor heat exchanger 105. The indoor unit 107 includes an indoor heat exchanger 103 and an indoor blower 109 that supplies air to the indoor heat exchanger 103. The outdoor unit 106 and the indoor unit 107 are connected via two extension pipes 111 and 112 which are a part of the refrigerant pipe.
 圧縮機101は、吸入した冷媒を圧縮して吐出する流体機械である。流路切替装置102は、例えば四方弁であり、制御装置(図示は省略)の制御により、冷房運転時と暖房運転時とで冷媒の流路を切り替える装置である。冷媒は、第1の熱交換流体である。 The compressor 101 is a fluid machine that compresses and discharges the sucked refrigerant. The flow path switching device 102 is, for example, a four-way valve, and is a device that switches the flow path of the refrigerant between the cooling operation and the heating operation by controlling the control device (not shown). The refrigerant is the first heat exchange fluid.
 室内熱交換器103は、内部を流通する冷媒と、室内送風機109により供給される室内空気と、の熱交換を行う熱交換器である。室内熱交換器103は、暖房運転時には凝縮器として機能し、冷房運転時には蒸発器として機能する。 The indoor heat exchanger 103 is a heat exchanger that exchanges heat between the refrigerant circulating inside and the indoor air supplied by the indoor blower 109. The indoor heat exchanger 103 functions as a condenser during the heating operation and as an evaporator during the cooling operation.
 減圧装置104は、例えば膨張弁であり、冷媒を減圧させる装置である。減圧装置104としては、制御装置の制御により開度が調節される電子膨張弁を用いることができる。 The pressure reducing device 104 is, for example, an expansion valve, which is a device for reducing the pressure of the refrigerant. As the pressure reducing device 104, an electronic expansion valve whose opening degree is adjusted by the control of the control device can be used.
 室外熱交換器105は、内部を流通する冷媒と、室外送風機108により供給される空気と、の熱交換を行う熱交換器である。室外熱交換器105は、暖房運転時には蒸発器として機能し、冷房運転時には凝縮器として機能する。室外送風機108により供給される空気は、第2の熱交換流体の一例である。 The outdoor heat exchanger 105 is a heat exchanger that exchanges heat between the refrigerant circulating inside and the air supplied by the outdoor blower 108. The outdoor heat exchanger 105 functions as an evaporator during the heating operation and as a condenser during the cooling operation. The air supplied by the outdoor blower 108 is an example of a second heat exchange fluid.
 室外熱交換器105及び室内熱交換器103の少なくとも一方には、後述する熱交換器100が用いられている。熱交換器100に接続される冷媒分配器150は、熱交換器100において液相冷媒がより多くなる位置に配置されるのが望ましい。具体的には、冷媒分配器150は、冷媒回路110での冷媒の流れにおいて、蒸発器として機能する熱交換器100の入口側、すなわち凝縮器として機能する熱交換器100の出口側に配置されるのが望ましい。なお、図1において冷媒分配器150は、室内熱交換器103と室外熱交換器105との両方の熱交換器100に用いられているが、室内熱交換器103又は室外熱交換器105のいずれか一方の熱交換器100にのみ用いられてもよい。 A heat exchanger 100, which will be described later, is used for at least one of the outdoor heat exchanger 105 and the indoor heat exchanger 103. It is desirable that the refrigerant distributor 150 connected to the heat exchanger 100 is arranged at a position in the heat exchanger 100 where the amount of the liquid phase refrigerant is larger. Specifically, the refrigerant distributor 150 is arranged on the inlet side of the heat exchanger 100 that functions as an evaporator, that is, on the outlet side of the heat exchanger 100 that functions as a condenser in the flow of the refrigerant in the refrigerant circuit 110. Is desirable. In FIG. 1, the refrigerant distributor 150 is used in both the indoor heat exchanger 103 and the outdoor heat exchanger 105, but either the indoor heat exchanger 103 or the outdoor heat exchanger 105. It may be used only for one of the heat exchangers 100.
[冷凍サイクル装置200の動作]
 次に、図1を用いて冷凍サイクル装置200の動作の一例について説明する。冷凍サイクル装置200の暖房運転時には、圧縮機101から吐出される高圧高温のガス状態の冷媒は、流路切替装置102を介して室内熱交換器103に流入し、室内送風機109によって供給される空気と熱交換を行い凝縮する。凝縮した冷媒は、高圧の液状態となり、室内熱交換器103から流出し、減圧装置104によって、低圧の気液二相状態となる。低圧の気液二相状態の冷媒は、室外熱交換器105に流入し、室外送風機108によって供給される空気との熱交換によって蒸発する。蒸発した冷媒は、低圧のガス状態となり、圧縮機101に吸入される。なお、暖房運転時において、室外熱交換器105の圧力飽和温度が室外空気の露点温度以下で水の凝固点以下の場合、室外熱交換器105に霜が付着する。
[Operation of refrigeration cycle device 200]
Next, an example of the operation of the refrigeration cycle apparatus 200 will be described with reference to FIG. During the heating operation of the refrigeration cycle device 200, the high-pressure and high-temperature gas-state refrigerant discharged from the compressor 101 flows into the indoor heat exchanger 103 via the flow path switching device 102, and the air supplied by the indoor blower 109. Heat exchange with and condenses. The condensed refrigerant is in a high-pressure liquid state, flows out of the indoor heat exchanger 103, and is in a low-pressure gas-liquid two-phase state by the decompression device 104. The low-pressure gas-liquid two-phase refrigerant flows into the outdoor heat exchanger 105 and evaporates by heat exchange with the air supplied by the outdoor blower 108. The evaporated refrigerant becomes a low-pressure gas state and is sucked into the compressor 101. During the heating operation, if the pressure saturation temperature of the outdoor heat exchanger 105 is equal to or lower than the dew point temperature of the outdoor air and lower than the freezing point of water, frost adheres to the outdoor heat exchanger 105.
 冷凍サイクル装置200の冷房運転時には、冷媒回路110を流れる冷媒は暖房運転時とは逆方向に流れる。すなわち、冷凍サイクル装置200の冷房運転時には、圧縮機101から吐出される高圧高温のガス状態の冷媒は、流路切替装置102を介して室外熱交換器105に流入し、室外送風機108によって供給される空気と熱交換を行い凝縮する。凝縮した冷媒は、高圧の液状態となり、室外熱交換器105から流出し、減圧装置104によって、低圧の気液二相状態となる。低圧の気液二相状態の冷媒は、室内熱交換器103に流入し、室内送風機109によって供給される空気との熱交換によって蒸発する。蒸発した冷媒は、低圧のガス状態となり、圧縮機101に吸入される。 During the cooling operation of the refrigeration cycle device 200, the refrigerant flowing through the refrigerant circuit 110 flows in the opposite direction to that during the heating operation. That is, during the cooling operation of the refrigeration cycle device 200, the high-pressure and high-temperature gas-state refrigerant discharged from the compressor 101 flows into the outdoor heat exchanger 105 via the flow path switching device 102 and is supplied by the outdoor blower 108. It exchanges heat with the air and condenses. The condensed refrigerant is in a high-pressure liquid state, flows out of the outdoor heat exchanger 105, and is in a low-pressure gas-liquid two-phase state by the decompression device 104. The low-pressure gas-liquid two-phase refrigerant flows into the indoor heat exchanger 103 and evaporates by heat exchange with the air supplied by the indoor blower 109. The evaporated refrigerant becomes a low-pressure gas state and is sucked into the compressor 101.
[室外熱交換器105]
 図2は、実施の形態1に係る熱交換器100の要部構成を概念的に示す側面図である。図3は、実施の形態1に係る熱交換器100の要部構成を概念的に示す分解斜視図である。図2~図3を用いて、実施の形態1に係る熱交換器100について説明する。図2において、ハッチングで示した矢印Fは、冷媒分配器150の第1流路部15を流れる冷媒の方向を示すものである。冷媒分配器150が冷凍サイクル装置200に適用される場合、冷媒分配器150は、熱交換器100が蒸発器として運転する場合に、冷媒の入口側となる伝熱管70の端部に接続されている。
[Outdoor heat exchanger 105]
FIG. 2 is a side view conceptually showing the main configuration of the heat exchanger 100 according to the first embodiment. FIG. 3 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the first embodiment. The heat exchanger 100 according to the first embodiment will be described with reference to FIGS. 2 to 3. In FIG. 2, the arrow F indicated by hatching indicates the direction of the refrigerant flowing through the first flow path portion 15 of the refrigerant distributor 150. When the refrigerant distributor 150 is applied to the refrigeration cycle device 200, the refrigerant distributor 150 is connected to the end of the heat transfer tube 70 which is the inlet side of the refrigerant when the heat exchanger 100 operates as an evaporator. There is.
 図2に示すように、熱交換器100は、冷媒を流通させる複数の伝熱管70と、複数の伝熱管70のそれぞれの管路の延伸方向の一端に接続された冷媒分配器150と、を有する。また、熱交換器100は、冷媒分配器150の下部に取り付けられた冷媒流入管60を有している。 As shown in FIG. 2, the heat exchanger 100 includes a plurality of heat transfer tubes 70 through which refrigerant is circulated, and a refrigerant distributor 150 connected to one end of each of the plurality of heat transfer tubes 70 in the extending direction. Have. Further, the heat exchanger 100 has a refrigerant inflow pipe 60 attached to the lower part of the refrigerant distributor 150.
 複数の伝熱管70は、第1方向(Z軸方向)に互いに間隔をあけて配置されており、第1方向(Z軸方向)と交差する第2方向(X軸方向)に冷媒を流通させる。複数の伝熱管70は、扁平管である。なお、伝熱管70は、扁平管として説明しているが、伝熱管70は扁平管に限定されるものではなく、例えば円管であってもよい。 The plurality of heat transfer tubes 70 are arranged at intervals in the first direction (Z-axis direction), and the refrigerant flows in the second direction (X-axis direction) intersecting the first direction (Z-axis direction). .. The plurality of heat transfer tubes 70 are flat tubes. Although the heat transfer tube 70 is described as a flat tube, the heat transfer tube 70 is not limited to the flat tube, and may be, for example, a circular tube.
 熱交換器100において、複数の伝熱管70の配列方向と冷媒分配器150の延伸方向とを第1方向(Z軸方向)と規定する。すなわち、第1方向は、複数の伝熱管70が並ぶ方向である。熱交換器100は、第1方向(Z軸方向)である複数の伝熱管70の配列方向を上下方向としている。上下方向は、例えば鉛直方向である。ただし、第1方向(Z軸方向)である複数の伝熱管70の配列方向は、上下方向及び鉛直方向に限定されるものではなく、鉛直方向に対して傾いた方向であってもよく、水平方向であってもよい。 In the heat exchanger 100, the arrangement direction of the plurality of heat transfer tubes 70 and the extension direction of the refrigerant distributor 150 are defined as the first direction (Z-axis direction). That is, the first direction is the direction in which the plurality of heat transfer tubes 70 are lined up. In the heat exchanger 100, the arrangement direction of the plurality of heat transfer tubes 70, which is the first direction (Z-axis direction), is the vertical direction. The vertical direction is, for example, the vertical direction. However, the arrangement direction of the plurality of heat transfer tubes 70, which is the first direction (Z-axis direction), is not limited to the vertical direction and the vertical direction, and may be a direction inclined with respect to the vertical direction, and is horizontal. It may be a direction.
 熱交換器100において、伝熱管70の管路の延伸方向を第2方向(X軸方向)と規定する。なお、伝熱管70の管路は、後述する冷媒通路72である(図4参照)。そのため、第2方向(X軸方向)は、伝熱管70の管路を流れる冷媒の流通方向でもある。熱交換器100は、第2方向(X軸方向)である複数の伝熱管70の管路の延伸方向を水平方向としている。ただし、第2方向(X軸方向)である複数の伝熱管70の管路の延伸方向は、水平方向に限定されるものではなく、水平方向に対して傾いた方向であってもよく、鉛直方向を含む上下方向であってもよい。 In the heat exchanger 100, the extension direction of the pipeline of the heat transfer tube 70 is defined as the second direction (X-axis direction). The conduit of the heat transfer tube 70 is a refrigerant passage 72, which will be described later (see FIG. 4). Therefore, the second direction (X-axis direction) is also the flow direction of the refrigerant flowing through the conduit of the heat transfer tube 70. In the heat exchanger 100, the extension direction of the pipe lines of the plurality of heat transfer tubes 70, which is the second direction (X-axis direction), is the horizontal direction. However, the extension direction of the conduits of the plurality of heat transfer tubes 70 in the second direction (X-axis direction) is not limited to the horizontal direction, and may be a direction inclined with respect to the horizontal direction, and is vertical. It may be in the vertical direction including the direction.
 複数の伝熱管70のうち隣り合う2つの伝熱管70の間には、空気の流路となる隙間71が形成されている。隣り合う2つの伝熱管70の間には、図2に示すように、伝熱フィン75が設けられていてもよい。また、熱交換器100は、一部に伝熱促進部材である伝熱フィン75を有し、一部に隣り合う伝熱管70同士が伝熱促進部材によって接続されていない領域を有するものであってもよい。 A gap 71 that serves as an air flow path is formed between two adjacent heat transfer tubes 70 among the plurality of heat transfer tubes 70. As shown in FIG. 2, heat transfer fins 75 may be provided between two adjacent heat transfer tubes 70. Further, the heat exchanger 100 has a heat transfer fin 75 which is a heat transfer promoting member in a part thereof, and has a region in which the heat transfer tubes 70 adjacent to each other are not connected to each other by the heat transfer promoting member. You may.
 なお、複数の伝熱管70の中で隣り合う伝熱管70は、伝熱フィン75を有さず、互いの伝熱管70同士が伝熱促進部材によって接続されていなくてもよい。伝熱促進部材とは、伝熱を促進する部材であって、例えば、伝熱フィン75のようなプレートフィン、あるいは、コルゲートフィン等である。したがって、室外熱交換器105は、所謂フィンレス熱交換器として構成されてもよい。 Note that the heat transfer tubes 70 adjacent to each other among the plurality of heat transfer tubes 70 do not have the heat transfer fins 75, and the heat transfer tubes 70 may not be connected to each other by the heat transfer promotion member. The heat transfer promoting member is a member that promotes heat transfer, and is, for example, a plate fin such as a heat transfer fin 75, a corrugated fin, or the like. Therefore, the outdoor heat exchanger 105 may be configured as a so-called finless heat exchanger.
 熱交換器100が冷凍サイクル装置200の蒸発器として機能する場合、複数の伝熱管70のそれぞれでは、伝熱管70の内部の管路を延伸方向の一端から他端に向かって冷媒が流れる。また、熱交換器100が冷凍サイクル装置200の凝縮器として機能する場合、複数の伝熱管70のそれぞれでは、伝熱管70の内部の管路を延伸方向の他端から一端に向かって冷媒が流れる。 When the heat exchanger 100 functions as an evaporator of the refrigeration cycle device 200, the refrigerant flows from one end to the other end in the extension direction in each of the plurality of heat transfer tubes 70. Further, when the heat exchanger 100 functions as a condenser of the refrigeration cycle device 200, in each of the plurality of heat transfer tubes 70, the refrigerant flows from the other end in the extension direction toward one end in the inner pipeline of the heat transfer tube 70. ..
(伝熱管70)
 図4は、実施の形態1に係る熱交換器100を構成する伝熱管70の構成を示す断面図である。図4は、伝熱管70の延伸方向と垂直な断面を示している。図4に示すように、伝熱管70は、長円形状等の一方向に扁平な断面形状を有している。
(Heat transfer tube 70)
FIG. 4 is a cross-sectional view showing the configuration of the heat transfer tube 70 constituting the heat exchanger 100 according to the first embodiment. FIG. 4 shows a cross section perpendicular to the extending direction of the heat transfer tube 70. As shown in FIG. 4, the heat transfer tube 70 has a unidirectionally flat cross-sectional shape such as an oval shape.
 伝熱管70は、第1側端部70a及び第2側端部70bと一対の平坦面70c及び平坦面70dとを有している。図4に示す断面において、第1側端部70aは、平坦面70cの一方の端部と平坦面70dの一方の端部とに接続されている。同断面において、第2側端部70bは、平坦面70cの他方の端部と平坦面70dの他方の端部とに接続されている。 The heat transfer tube 70 has a first side end portion 70a and a second side end portion 70b, and a pair of flat surfaces 70c and flat surfaces 70d. In the cross section shown in FIG. 4, the first side end portion 70a is connected to one end portion of the flat surface 70c and one end portion of the flat surface 70d. In the same cross section, the second side end 70b is connected to the other end of the flat surface 70c and the other end of the flat surface 70d.
 第1側端部70aは、熱交換器を通過する空気の流れにおいて風上側、すなわち前縁側に配置される側端部である。第2側端部70bは、熱交換器を通過する空気の流れにおいて風下側、すなわち後縁側に配置される側端部である。以下、伝熱管70の延伸方向と垂直であってかつ平坦面70c及び平坦面70dに沿う方向を、伝熱管70の長軸方向という場合がある。 The first side end portion 70a is a side end portion arranged on the windward side, that is, on the front edge side in the flow of air passing through the heat exchanger. The second side end portion 70b is a side end portion arranged on the leeward side, that is, the trailing edge side in the flow of air passing through the heat exchanger. Hereinafter, the direction perpendicular to the extending direction of the heat transfer tube 70 and along the flat surface 70c and the flat surface 70d may be referred to as a major axis direction of the heat transfer tube 70.
 伝熱管70には、長軸方向に沿って第1側端部70aと第2側端部70bとの間に配列した複数の冷媒通路72が形成されている。伝熱管70は、冷媒の流れる冷媒通路72が空気の流れ方向に複数配列された扁平多孔管である。複数の冷媒通路72のそれぞれは、伝熱管70の延伸方向と平行に延びるように形成されている。 The heat transfer tube 70 is formed with a plurality of refrigerant passages 72 arranged between the first side end portion 70a and the second side end portion 70b along the long axis direction. The heat transfer tube 70 is a flat perforated tube in which a plurality of refrigerant passages 72 through which the refrigerant flows are arranged in the air flow direction. Each of the plurality of refrigerant passages 72 is formed so as to extend in parallel with the extending direction of the heat transfer tube 70.
(冷媒分配器150)
 図2及び図3に戻り、冷媒分配器150について説明する。冷媒分配器150は、第1方向(Z軸方向)に延伸する本体151を有する。冷媒分配器150の本体151は、複数の伝熱管70のそれぞれの一端に接続されている。冷媒分配器150は、本体151に接続された複数の伝熱管70のそれぞれに冷媒を分配する。
(Refrigerant distributor 150)
Returning to FIGS. 2 and 3, the refrigerant distributor 150 will be described. The refrigerant distributor 150 has a main body 151 extending in the first direction (Z-axis direction). The main body 151 of the refrigerant distributor 150 is connected to one end of each of the plurality of heat transfer tubes 70. The refrigerant distributor 150 distributes the refrigerant to each of the plurality of heat transfer tubes 70 connected to the main body 151.
 冷媒分配器150の本体151は、複数の伝熱管70の配列方向に沿って上下方向に延伸するように形成されている。本体151は、第1方向に延伸しており、各伝熱管70に冷媒を分配する分配流路が内部に形成されている。冷媒分配器150の本体151には、冷媒流入管60が挿入される冷媒流入口18と、複数の伝熱管70のそれぞれが挿入される複数の挿入孔31とが形成されている。 The main body 151 of the refrigerant distributor 150 is formed so as to extend in the vertical direction along the arrangement direction of the plurality of heat transfer tubes 70. The main body 151 extends in the first direction, and a distribution flow path for distributing the refrigerant to each heat transfer tube 70 is formed inside. The main body 151 of the refrigerant distributor 150 is formed with a refrigerant inflow port 18 into which the refrigerant inflow pipe 60 is inserted and a plurality of insertion holes 31 into which each of the plurality of heat transfer pipes 70 is inserted.
 冷媒流入口18は、第1方向において本体151の一方の端部151a側に形成されている。複数の挿入孔31は、複数の伝熱管70と接続される側の本体151の側面に形成されている。複数の挿入孔31のそれぞれは、複数の伝熱管70のそれぞれと対応するように、第1方向(Z軸方向)に沿って互いに間隔をあけて形成されている。 The refrigerant inflow port 18 is formed on one end 151a side of the main body 151 in the first direction. The plurality of insertion holes 31 are formed on the side surface of the main body 151 on the side connected to the plurality of heat transfer tubes 70. Each of the plurality of insertion holes 31 is formed so as to correspond to each of the plurality of heat transfer tubes 70 so as to be spaced apart from each other along the first direction (Z-axis direction).
 冷媒分配器150の本体151は、第1板状部材10、第2板状部材20及び第3板状部材30を有している。第1板状部材10、第2板状部材20及び第3板状部材30はいずれも、金属平板を用いて形成され、一方向に長い帯状の形状を有している。第1板状部材10、第2板状部材20及び第3板状部材30のそれぞれの外縁の輪郭は、互いに同一の形状を有している。第1板状部材10、第2板状部材20及び第3板状部材30は、それぞれの板厚方向が伝熱管70の管路の延伸方向と平行になるように、すなわち、それぞれの板面が伝熱管70の管路の延伸方向と垂直になるように配置されている。 The main body 151 of the refrigerant distributor 150 has a first plate-shaped member 10, a second plate-shaped member 20, and a third plate-shaped member 30. The first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are all formed by using a metal flat plate and have a strip-like shape long in one direction. The contours of the outer edges of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 have the same shape as each other. Each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 has a plate thickness direction parallel to the extension direction of the pipe line of the heat transfer tube 70, that is, each plate surface. Is arranged so as to be perpendicular to the extending direction of the conduit of the heat transfer tube 70.
 冷媒分配器150の本体151は、第1板状部材10、第2板状部材20及び第3板状部材30が、伝熱管70からの距離が遠い方からこの順に積層された構成を有している。第1板状部材10は、本体151において伝熱管70からの距離が最も遠い位置に配置されており、第3板状部材30は、本体151において伝熱管70からの距離が最も近い位置に配置されている。 The main body 151 of the refrigerant distributor 150 has a configuration in which the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are laminated in this order from the farthest distance from the heat transfer tube 70. ing. The first plate-shaped member 10 is arranged at the position farthest from the heat transfer tube 70 in the main body 151, and the third plate-shaped member 30 is arranged at the position closest to the heat transfer tube 70 in the main body 151. Has been done.
 第2板状部材20は、第1板状部材10と伝熱管70との間に配置されており、第1板状部材10及び第3板状部材30と隣接している。第3板状部材30は、第2板状部材20と伝熱管70との間に配置されており、第2板状部材20と隣接している。第3板状部材30には、複数の伝熱管70のそれぞれの一端が接続されている。 The second plate-shaped member 20 is arranged between the first plate-shaped member 10 and the heat transfer tube 70, and is adjacent to the first plate-shaped member 10 and the third plate-shaped member 30. The third plate-shaped member 30 is arranged between the second plate-shaped member 20 and the heat transfer tube 70, and is adjacent to the second plate-shaped member 20. One end of each of the plurality of heat transfer tubes 70 is connected to the third plate-shaped member 30.
 第1板状部材10、第2板状部材20及び第3板状部材30のうち隣接する部材同士は、ろう付けによって接合されている。第1板状部材10、第2板状部材20及び第3板状部材30は、それぞれの長手方向が第1方向(Z軸方向)に沿うように配置されている。 The adjacent members of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are joined by brazing. The first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 are arranged so that their respective longitudinal directions are along the first direction (Z-axis direction).
 図5は、実施の形態1に係る熱交換器100を構成する冷媒分配器150の第1流路と第2流路との連通位置を概念的に示した断面図である。第1板状部材10、第2板状部材20及び第3板状部材30のそれぞれの板厚方向は、図5の上下方向であり、伝熱管70の管路の延伸方向である。第1板状部材10、第2板状部材20及び第3板状部材30のそれぞれの短手方向は、図5の左右方向であり、伝熱管70の長軸方向である。図3及び図5を用いて、冷媒分配器150の本体151の構成について更に説明する。 FIG. 5 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment. The plate thickness direction of each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 is the vertical direction of FIG. 5, and is the extending direction of the conduit of the heat transfer tube 70. The lateral direction of each of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30 is the left-right direction in FIG. 5, and the major axis direction of the heat transfer tube 70. The configuration of the main body 151 of the refrigerant distributor 150 will be further described with reference to FIGS. 3 and 5.
 図3及び図5に示すように、第1板状部材10は、伝熱管70から離れる方向に膨出した第1流路部15を有している。第1流路部15は、筒状に形成されており、膨出した内部に空間が形成されている。冷媒分配器150は、第1板状部材10と第1流路部15とが一体に形成されているが別体で形成されてもよい。 As shown in FIGS. 3 and 5, the first plate-shaped member 10 has a first flow path portion 15 that bulges in a direction away from the heat transfer tube 70. The first flow path portion 15 is formed in a tubular shape, and a space is formed inside the bulge. Although the first plate-shaped member 10 and the first flow path portion 15 are integrally formed in the refrigerant distributor 150, they may be formed separately.
 第1流路部15は、第1板状部材10の長手方向に沿って、第1板状部材10の長手方向一端から長手方向他端まで延伸している。第1流路部15は、半円筒形状に形成されている。第1流路部15の延伸方向の両端は閉塞されている。第1流路部15は、第1方向(Z軸方向)に対する垂直な断面において、半円状、半楕円状又は半長円状の断面形状を有している。ただし、第1流路部15の断面形状は、半円状、半楕円状又は半長円状に限定されるものはなく、例えば、矩形状であってもよい。 The first flow path portion 15 extends from one end in the longitudinal direction to the other end in the longitudinal direction of the first plate-shaped member 10 along the longitudinal direction of the first plate-shaped member 10. The first flow path portion 15 is formed in a semi-cylindrical shape. Both ends of the first flow path portion 15 in the stretching direction are closed. The first flow path portion 15 has a semicircular, semi-elliptical or semi-oval cross-sectional shape in a cross section perpendicular to the first direction (Z-axis direction). However, the cross-sectional shape of the first flow path portion 15 is not limited to a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape, and may be, for example, a rectangular shape.
 また、第1板状部材10は、第1流路部15を挟んだ両側に、平板状に形成された平板部11a及び平板部11bを有している。平板部11a及び平板部11bはいずれも、第1板状部材10の長手方向に沿って、第1板状部材10の長手方向一端から長手方向他端まで延伸している。換言すれば、第1流路部15は、平板部11aと平板部11bとの間に形成されており、平板部11a及び平板部11bに対して伝熱管70が配置されている側とは反対方向に膨出するように形成されている。そして、第1流路部15は、伝熱管70の配置側が開口している。なお、以下の説明では平板部11a及び平板部11bの総称を平板部11とする場合がある。 Further, the first plate-shaped member 10 has a flat plate portion 11a and a flat plate portion 11b formed in a flat plate shape on both sides of the first flow path portion 15. Both the flat plate portion 11a and the flat plate portion 11b extend from one end in the longitudinal direction to the other end in the longitudinal direction of the first plate-shaped member 10 along the longitudinal direction of the first plate-shaped member 10. In other words, the first flow path portion 15 is formed between the flat plate portion 11a and the flat plate portion 11b, and is opposite to the side on which the heat transfer tube 70 is arranged with respect to the flat plate portion 11a and the flat plate portion 11b. It is formed so as to bulge in the direction. The first flow path portion 15 is open on the arrangement side of the heat transfer tube 70. In the following description, the flat plate portion 11a and the flat plate portion 11b may be collectively referred to as the flat plate portion 11.
 第1流路部15の内側には、第1板状部材10の長手方向に沿って上下方向に延伸した主流路15aが形成されている。主流路15aは、冷媒分配器150の第1流路である。第1流路である主流路15aは、冷媒流入口18に接続された冷媒流入管60と接続し、複数の伝熱管70の配列方向である第1方向(Z軸方向)に延びるように形成されている。 Inside the first flow path portion 15, a main flow path 15a extending in the vertical direction along the longitudinal direction of the first plate-shaped member 10 is formed. The main flow path 15a is the first flow path of the refrigerant distributor 150. The main flow path 15a, which is the first flow path, is connected to the refrigerant inflow pipe 60 connected to the refrigerant inflow port 18 and is formed so as to extend in the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. Has been done.
 第1流路である主流路15aは、第1板状部材10の板厚方向に見たとき、複数の伝熱管70のそれぞれと交差して延伸している。そして、第1流路である主流路15aは、第2板状部材20に形成された後述する分配孔部26を介して複数の伝熱管70の管路と連通している。 The main flow path 15a, which is the first flow path, extends so as to intersect with each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the first plate-shaped member 10. The main flow path 15a, which is the first flow path, communicates with the conduits of the plurality of heat transfer tubes 70 via the distribution hole portion 26 formed in the second plate-shaped member 20 which will be described later.
 主流路15aは、第1方向(Z軸方向)に対する垂直な断面において、半円状、半楕円状又は半長円状の断面形状を有している。すなわち、主流路15aは、半円筒状、半楕円筒状又は半長円筒状に形成された空間である。ただし、主流路15aの断面形状は、半円状、半楕円状又は半長円状に限定されるものはなく、例えば、矩形状であってもよい。 The main flow path 15a has a semicircular, semi-elliptical or semi-oval cross-sectional shape in a cross section perpendicular to the first direction (Z-axis direction). That is, the main flow path 15a is a space formed in a semi-cylindrical shape, a semi-elliptical cylinder shape, or a semi-long cylindrical shape. However, the cross-sectional shape of the main flow path 15a is not limited to a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape, and may be, for example, a rectangular shape.
 上記に説明したように、第1流路である主流路15aは、第1方向(Z軸方向)に延伸するように形成されており、複数の伝熱管70と連通すると共に、第1方向の下端部15a2において、冷媒分配器150内に冷媒を流入させる冷媒流入管60と接続している。そして、冷媒流入管60を介して主流路15aに流入する気液二相冷媒は、本体151の一方の端部151aから他方の端部151bに向かうように、主流路15aを上向きに流れて、各伝熱管70に分配される。 As described above, the main flow path 15a, which is the first flow path, is formed so as to extend in the first direction (Z-axis direction), communicates with the plurality of heat transfer tubes 70, and is in the first direction. At the lower end portion 15a2, it is connected to a refrigerant inflow pipe 60 that allows the refrigerant to flow into the refrigerant distributor 150. Then, the gas-liquid two-phase refrigerant flowing into the main flow path 15a through the refrigerant inflow pipe 60 flows upward in the main flow path 15a so as to go from one end 151a of the main body 151 to the other end 151b. It is distributed to each heat transfer tube 70.
 第1流路部15の下端部には、冷媒流入管60が接続されている。そして、主流路15aと、冷媒流入管60の内部空間とが連通している。冷媒流入管60は、熱交換器100が蒸発器として機能する際、主流路15aに気液二相冷媒を流入させる。冷媒流入管60と第1流路部15との接続位置が、冷媒分配器150に冷媒が流入する冷媒流入口18となる。なお、熱交換器100が凝縮器として機能する際には、液冷媒が主流路15aを下向きに流れて冷媒流入管60を介して流出する。 A refrigerant inflow pipe 60 is connected to the lower end of the first flow path portion 15. The main flow path 15a and the internal space of the refrigerant inflow pipe 60 communicate with each other. The refrigerant inflow pipe 60 causes a gas-liquid two-phase refrigerant to flow into the main flow path 15a when the heat exchanger 100 functions as an evaporator. The connection position between the refrigerant inflow pipe 60 and the first flow path portion 15 is the refrigerant inflow port 18 through which the refrigerant flows into the refrigerant distributor 150. When the heat exchanger 100 functions as a condenser, the liquid refrigerant flows downward in the main flow path 15a and flows out through the refrigerant inflow pipe 60.
 第2板状部材20には、副流路25及び分配孔部26が形成されている。ここで、第1方向(Z軸方向)及び第2方向(X軸方向)に平行な面Pに交差する方向を第3方向と定義する。なお、第3方向は、Y軸方向を含んでいる。第3方向(Y軸方向)において、分配孔部26は第2板状部材20の中央付近に形成されており、副流路25は第2板状部材20の端部付近に形成されている。すなわち、第3方向(Y軸方向)において、分配孔部26は第2板状部材20の中央付近に形成されており、副流路25は、分配孔部26の両側にそれぞれ形成されている。なお、第2板状部材20における副流路25及び分配孔部26の形成位置は、上記の位置に限定されるものではない。なお、分配孔部26の両側にそれぞれ形成されている副流路25は、第1方向における少なくとも一方の端部同士が連通するように形成されていてもよい。 The second plate-shaped member 20 is formed with a sub-flow path 25 and a distribution hole portion 26. Here, the direction intersecting the plane P parallel to the first direction (Z-axis direction) and the second direction (X-axis direction) is defined as the third direction. The third direction includes the Y-axis direction. In the third direction (Y-axis direction), the distribution hole portion 26 is formed near the center of the second plate-shaped member 20, and the auxiliary flow path 25 is formed near the end of the second plate-shaped member 20. .. That is, in the third direction (Y-axis direction), the distribution hole portion 26 is formed near the center of the second plate-shaped member 20, and the auxiliary flow paths 25 are formed on both sides of the distribution hole portion 26, respectively. .. The formation positions of the sub-flow path 25 and the distribution hole portion 26 in the second plate-shaped member 20 are not limited to the above positions. The sub-flow paths 25 formed on both sides of the distribution hole portion 26 may be formed so that at least one end portion in the first direction communicates with each other.
 副流路25は、第2板状部材20において第1方向(Z軸方向)に延伸するように形成されている。すなわち、副流路25は、第2板状部材20の長手方向に沿って、上下方向に延伸して形成されている。副流路25は、冷媒分配器150の第2流路である。第2流路である副流路25は、冷媒分配器150の本体151において、両端部が第1流路である主流路15aと接続するように形成されている。副流路25は、主流路15aの上端部15a1と下端部15a2とを連通させ、主流路15aの上端部15a1に到達した冷媒を、冷媒流入口18が形成された下端部15a2に戻すための冷媒の流路を形成している。冷媒分配器150の本体151は、主流路15a及び副流路25によって冷媒の循環流路を形成している。 The auxiliary flow path 25 is formed so as to extend in the first direction (Z-axis direction) in the second plate-shaped member 20. That is, the sub-channel 25 is formed by extending in the vertical direction along the longitudinal direction of the second plate-shaped member 20. The sub-flow path 25 is the second flow path of the refrigerant distributor 150. The sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that both ends are connected to the main flow path 15a, which is the first flow path. The sub-flow path 25 communicates the upper end portion 15a1 and the lower end portion 15a2 of the main flow path 15a, and returns the refrigerant that has reached the upper end portion 15a1 of the main flow path 15a to the lower end portion 15a2 in which the refrigerant inlet 18 is formed. It forms a flow path for the refrigerant. The main body 151 of the refrigerant distributor 150 forms a refrigerant circulation flow path by the main flow path 15a and the sub flow path 25.
 冷媒分配器150の本体151は、冷媒が流れる主流路15a及び副流路25が内部に形成されている。上述したように、主流路15aは、第1流路であり、副流路25は、第2流路である。第2流路である副流路25は、第1流路である主流路15aに対して第3方向に位置するように形成されている。すなわち、主流路15a及び副流路25は、図1に示す室外送風機108あるいは室内送風機109によって形成される風の通風方向において上流側と下流側とに位置するように形成されている。 The main body 151 of the refrigerant distributor 150 has a main flow path 15a and a sub flow path 25 through which the refrigerant flows. As described above, the main flow path 15a is the first flow path, and the sub-flow path 25 is the second flow path. The sub-flow path 25, which is the second flow path, is formed so as to be located in the third direction with respect to the main flow path 15a, which is the first flow path. That is, the main flow path 15a and the sub-flow path 25 are formed so as to be located on the upstream side and the downstream side in the ventilation direction of the wind formed by the outdoor blower 108 or the indoor blower 109 shown in FIG.
 副流路25は、中央部25aと、入口部25bと、出口部25cとを有している。中央部25aは、第1方向(Z軸方向)に延びる流路を形成している。入口部25bは、第1方向(Z軸方向)において、中央部25aの一方の端部25a1に形成されている。出口部25cは、第1方向(Z軸方向)において、中央部25aの他方の端部25a2に形成されている。入口部25b及び出口部25cは、冷媒分配器150の本体151において、第3方向(Y軸方向)に延びる流路として形成されている。 The sub-flow path 25 has a central portion 25a, an inlet portion 25b, and an outlet portion 25c. The central portion 25a forms a flow path extending in the first direction (Z-axis direction). The inlet portion 25b is formed at one end portion 25a1 of the central portion 25a in the first direction (Z-axis direction). The outlet portion 25c is formed at the other end portion 25a2 of the central portion 25a in the first direction (Z-axis direction). The inlet portion 25b and the outlet portion 25c are formed as flow paths extending in the third direction (Y-axis direction) in the main body 151 of the refrigerant distributor 150.
 副流路25の中央部25aは、第1板状部材10、第2板状部材20及び第3板状部材30の積層方向において、第1板状部材10の平板部11と第3板状部材30の平板部34との間に挟まれている。 The central portion 25a of the auxiliary flow path 25 has a flat plate portion 11 and a third plate shape of the first plate-shaped member 10 in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. It is sandwiched between the flat plate portion 34 of the member 30 and the flat plate portion 34.
 副流路25の両端部は、入口部25b及び出口部25cから構成されている。この入口部25b及び出口部25cは、第1板状部材10、第2板状部材20及び第3板状部材30の積層方向において、第1流路部15と第3板状部材30の平板部34との間に挟まれている。したがって、入口部25b及び出口部25cは、第1流路部15により形成された第1流路である主流路15aと連通している。これに対して、副流路25の中央部25aは、第1流路である主流路15aと連通していない。 Both ends of the subchannel 25 are composed of an inlet portion 25b and an outlet portion 25c. The inlet portion 25b and the outlet portion 25c are flat plates of the first flow path portion 15 and the third plate-shaped member 30 in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. It is sandwiched between the portion 34 and the portion 34. Therefore, the inlet portion 25b and the outlet portion 25c communicate with the main flow path 15a, which is the first flow path formed by the first flow path portion 15. On the other hand, the central portion 25a of the sub-flow path 25 does not communicate with the main flow path 15a, which is the first flow path.
 冷媒分配器150の本体151において、第2流路である副流路25は、入口部25b及び出口部25cを有することによって、両端部が第1流路である主流路15aと接続するように形成されている。より詳細には、第2流路である副流路25は、冷媒分配器150の本体151において、入口部25bが主流路15aの上端部15a1と連通するように形成されている。第2流路である副流路25は、冷媒分配器150の本体151において、出口部25cが主流路15aの下端部15a2と連通するように形成されている。 In the main body 151 of the refrigerant distributor 150, the sub-flow path 25, which is the second flow path, has an inlet portion 25b and an outlet portion 25c so that both ends are connected to the main flow path 15a, which is the first flow path. It is formed. More specifically, the sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that the inlet portion 25b communicates with the upper end portion 15a1 of the main flow path 15a. The sub-flow path 25, which is the second flow path, is formed in the main body 151 of the refrigerant distributor 150 so that the outlet portion 25c communicates with the lower end portion 15a2 of the main flow path 15a.
 入口部25bは、第1流路である主流路15aから第2流路である副流路25に流入する冷媒が通過する。すなわち、入口部25bは、第1流路である主流路15aから冷媒が流入する。出口部25cは、第2流路である副流路25から第1流路である主流路15aに流入する冷媒が通過する。すなわち、出口部25cは、第1流路である主流路15aに冷媒を流出する。なお、冷媒分配器150の本体151において、第2流路である副流路25は、後述する第3板状部材30の挿入孔31とは連通していない。 The refrigerant flowing from the main flow path 15a, which is the first flow path, to the sub-flow path 25, which is the second flow path, passes through the inlet portion 25b. That is, the refrigerant flows into the inlet portion 25b from the main flow path 15a, which is the first flow path. The refrigerant flowing from the sub-flow path 25, which is the second flow path, to the main flow path 15a, which is the first flow path, passes through the outlet portion 25c. That is, the outlet portion 25c causes the refrigerant to flow out to the main flow path 15a, which is the first flow path. In the main body 151 of the refrigerant distributor 150, the sub-flow path 25, which is the second flow path, does not communicate with the insertion hole 31 of the third plate-shaped member 30, which will be described later.
 第2板状部材20には、それぞれ円形の開口形状を有する複数の分配孔部26が形成されている。複数の分配孔部26は、主流路15aと伝熱管70との間の流路を形成し、各伝熱管70に冷媒を分配する。複数の分配孔部26のそれぞれは、第2板状部材20を第2板状部材20の板厚方向に貫通している貫通孔である。複数の分配孔部26は、第2板状部材20の長手方向となる第1方向(Z軸方向)に沿って配列している。複数の分配孔部26のそれぞれは、第2板状部材20を貫通する貫通孔を形成し、複数の伝熱管70のそれぞれに対応して設けられている。 The second plate-shaped member 20 is formed with a plurality of distribution hole portions 26 each having a circular opening shape. The plurality of distribution holes 26 form a flow path between the main flow path 15a and the heat transfer tube 70, and distribute the refrigerant to each heat transfer tube 70. Each of the plurality of distribution hole portions 26 is a through hole that penetrates the second plate-shaped member 20 in the plate thickness direction of the second plate-shaped member 20. The plurality of distribution hole portions 26 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the second plate-shaped member 20. Each of the plurality of distribution hole portions 26 forms a through hole penetrating the second plate-shaped member 20, and is provided corresponding to each of the plurality of heat transfer tubes 70.
 分配孔部26の開口形状は、円形状であるが、円形状に限定されるものではなく、例えば、半円状、半楕円状、半長円状又は矩形状であってもよい。なお、複数の分配孔部26の流路断面積は、それぞれ同じ大きさである。ただし、複数の分配孔部26の流路断面積は、それぞれ同じ大きさのものに限定されるものではなく、異なる大きさに形成されてもよい。 The opening shape of the distribution hole portion 26 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape. The flow path cross-sectional areas of the plurality of distribution hole portions 26 are the same size. However, the flow path cross-sectional areas of the plurality of distribution hole portions 26 are not limited to those having the same size, and may be formed to have different sizes.
 また、実施の形態1に係る冷媒分配器150の本体151において、第2板状部材20には分配孔部26が複数形成されているが、分配孔部26は第2板状部材20に1つだけ形成されていてもよい。この場合、分配孔部26は、複数の伝熱管70に対応させるために、第1方向(Z軸方向)に延びるように形成されている。 Further, in the main body 151 of the refrigerant distributor 150 according to the first embodiment, a plurality of distribution hole portions 26 are formed in the second plate-shaped member 20, but the distribution hole portion 26 is 1 in the second plate-shaped member 20. Only one may be formed. In this case, the distribution hole portion 26 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
 複数の分配孔部26はいずれも、第2板状部材20の板厚方向に見たとき、第1板状部材10の主流路15aと重なるように形成されている。また、複数の分配孔部26のそれぞれは、第2板状部材20の板厚方向に見たとき、後述する第3板状部材30の複数の挿入孔31のそれぞれと重なるように形成されている。さらに、複数の分配孔部26のそれぞれは、第2板状部材20の板厚方向に見たとき、複数の伝熱管70のそれぞれと重なるように形成されている。したがって、第1板状部材10、第2板状部材20及び第3板状部材30の積層方向において、分配孔部26は、伝熱管70と第1流路である主流路15aとの間に位置している。そして、第1板状部材10の主流路15aと、複数の伝熱管70のそれぞれとは、複数の分配孔部26を介して連通する。 Each of the plurality of distribution hole portions 26 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the second plate-shaped member 20. Further, each of the plurality of distribution hole portions 26 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30, which will be described later, when viewed in the plate thickness direction of the second plate-shaped member 20. There is. Further, each of the plurality of distribution hole portions 26 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the second plate-shaped member 20. Therefore, in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30, the distribution hole portion 26 is located between the heat transfer tube 70 and the main flow path 15a which is the first flow path. positioned. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of distribution holes 26.
 また、第2板状部材20は、平板状の閉塞部24を有している。閉塞部24の一部は、第2板状部材20の板厚方向に見たときに第1板状部材10の主流路15aと重なる。閉塞部24は、主流路15aと複数の伝熱管70のそれぞれとが、分配孔部26を介さずに直接連通するのを防ぐ機能を有している。 Further, the second plate-shaped member 20 has a flat plate-shaped closing portion 24. A part of the closing portion 24 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the second plate-shaped member 20. The closing portion 24 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the distribution hole portion 26.
 第3板状部材30には、複数の伝熱管70の一端がそれぞれ挿入される複数の挿入孔31が形成されている。複数の挿入孔31のそれぞれは、第3板状部材30を第3板状部材30の板厚方向に貫通している貫通孔である。 The third plate-shaped member 30 is formed with a plurality of insertion holes 31 into which one ends of the plurality of heat transfer tubes 70 are inserted. Each of the plurality of insertion holes 31 is a through hole that penetrates the third plate-shaped member 30 in the plate thickness direction of the third plate-shaped member 30.
 複数の挿入孔31は、第3板状部材30の長手方向に沿って上下方向に並列している。複数の挿入孔31は、複数の伝熱管70のそれぞれと対応して互いに独立して設けられている。挿入孔31は、伝熱管70の外周形状と同様に扁平な開口形状を有している。挿入孔31の開口端は、ろう付けにより伝熱管70の外周面と全周にわたって接合されている。 The plurality of insertion holes 31 are arranged in parallel in the vertical direction along the longitudinal direction of the third plate-shaped member 30. The plurality of insertion holes 31 are provided independently of each other corresponding to each of the plurality of heat transfer tubes 70. The insertion hole 31 has a flat opening shape similar to the outer peripheral shape of the heat transfer tube 70. The open end of the insertion hole 31 is joined to the outer peripheral surface of the heat transfer tube 70 over the entire circumference by brazing.
 第3板状部材30は、平板状の平板部34を有している。平板部34は、第3板状部材30のうち、第3板状部材30の板厚方向に見たときに第2板状部材20の副流路25と重なる部分に相当する。第2流路である副流路25は、第2方向(X軸方向)において、平板部34と平板部11とによって閉塞されている。 The third plate-shaped member 30 has a flat plate-shaped flat plate portion 34. The flat plate portion 34 corresponds to a portion of the third plate-shaped member 30 that overlaps with the sub-flow path 25 of the second plate-shaped member 20 when viewed in the plate thickness direction of the third plate-shaped member 30. The sub-flow path 25, which is the second flow path, is blocked by the flat plate portion 34 and the flat plate portion 11 in the second direction (X-axis direction).
 冷媒分配器150の本体151は、第1板状部材10と、第2板状部材20と、第3板状部材30との積層方向において、第1流路である主流路15aと第2流路である副流路25の両端部とが重なる。また、冷媒分配器150の本体151は、第1板状部材10と、第2板状部材20と、第3板状部材30との積層方向において、第1流路である主流路15aと、分配孔部26と、挿入孔31とが重なるように形成されている。 The main body 151 of the refrigerant distributor 150 has a main flow path 15a and a second flow, which are the first flow paths, in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. Both ends of the sub-flow path 25, which is a road, overlap each other. Further, the main body 151 of the refrigerant distributor 150 includes the main flow path 15a, which is the first flow path, in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. The distribution hole portion 26 and the insertion hole 31 are formed so as to overlap each other.
 図6は、実施の形態1に係る熱交換器100を構成する冷媒分配器150内の冷媒の流れを示した概念図である。次に、実施の形態1に係る冷媒分配器150の動作について、熱交換器100が冷凍サイクル装置200の蒸発器として機能する際の動作を例に挙げて説明する。 FIG. 6 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment. Next, the operation of the refrigerant distributor 150 according to the first embodiment will be described by exemplifying the operation when the heat exchanger 100 functions as the evaporator of the refrigeration cycle device 200.
 冷凍サイクル装置200が暖房運転の場合、冷媒分配器150に流入する冷媒は、気液二相流である。気液二相冷媒は、図2及び図6に示す冷媒流入管60から本体151内に流入し、図6の矢印UFで示すように、第1板状部材10に形成された主流路15aを一方の端部151aから他方の端部151bに向かって鉛直上向きに流れる。鉛直に上昇して流れる冷媒は、第2板状部材20の分配孔部26を通り、第3板状部材30に形成された挿入孔31を通って各伝熱管70に分配される。 When the refrigeration cycle device 200 is in the heating operation, the refrigerant flowing into the refrigerant distributor 150 is a gas-liquid two-phase flow. The gas-liquid two-phase refrigerant flows into the main body 151 from the refrigerant inflow pipe 60 shown in FIGS. 2 and 6, and forms a main flow path 15a formed in the first plate-shaped member 10 as shown by the arrow UF in FIG. It flows vertically upward from one end 151a toward the other end 151b. The vertically rising and flowing refrigerant passes through the distribution hole 26 of the second plate-shaped member 20 and is distributed to each heat transfer tube 70 through the insertion hole 31 formed in the third plate-shaped member 30.
 また、主流路15aの上部に滞留した冷媒は、主流路15aの上端部15a1と連通した第2板状部材20に設けられた入口部25bへ流入する。この際、冷媒は、矢印OFで示すように、第1流路である主流路15aから第2流路である副流路25に向かって、第3方向となる外側に向かって流れる。そして、副流路25の入口部25bから流入した冷媒は、矢印DFで示すように、第2板状部材20に形成された副流路25の中央部25aを重力方向に沿って下向きに流れる。 Further, the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 25b provided in the second plate-shaped member 20 communicating with the upper end portion 15a1 of the main flow path 15a. At this time, as shown by the arrow OF, the refrigerant flows from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path, toward the outside, which is the third direction. Then, as shown by the arrow DF, the refrigerant flowing in from the inlet portion 25b of the sub-channel 25 flows downward along the central portion 25a of the sub-channel 25 formed in the second plate-shaped member 20. ..
 副流路25の中央部25aの下端に到達した冷媒は、主流路15aの下端部15a2と連通した出口部25cから主流路15aへ流出する。この際、冷媒は、矢印IFで示すように、第2流路である副流路25から第1流路である主流路15aに向かって、第3方向となる内側に向かって流れる。そして、出口部25cから主流路15aへ流出した冷媒は、冷媒流入管60から本体151内に流入した冷媒と共に、主流路15aを鉛直に上昇し、各伝熱管70に分配される。 The refrigerant that has reached the lower end of the central portion 25a of the sub-flow path 25 flows out to the main flow path 15a from the outlet portion 25c that communicates with the lower end portion 15a2 of the main flow path 15a. At this time, as shown by the arrow IF, the refrigerant flows inward in the third direction from the sub-flow path 25 which is the second flow path toward the main flow path 15a which is the first flow path. Then, the refrigerant flowing out from the outlet portion 25c to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
 図7は、実施の形態1に係る熱交換器100を構成する冷媒分配器150内の冷媒の流量分布を表した図である。図7において、横軸は、冷媒流量[kg/h]を表し、縦軸は、伝熱管70が配列する第1方向において、冷媒流入口18からの距離[m]を表している。 FIG. 7 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the first embodiment. In FIG. 7, the horizontal axis represents the refrigerant flow rate [kg / h], and the vertical axis represents the distance [m] from the refrigerant inflow port 18 in the first direction in which the heat transfer tubes 70 are arranged.
 図7において、点線Aは、副流路25を有さない場合の主流路15aを流れる冷媒の流量を示し、実線Bは、副流路25を有する場合の主流路15aを流れる冷媒の流量を示している。また、一点鎖線Cは、主流路15aを流れる冷媒の流量が、上下方向で一定の場合を示している。なお、主流路15aを流れる冷媒の流量が上下方向で一定の場合には、第1方向に配列した各伝熱管70に流入する冷媒の流入量が一定になる。そのため、主流路15aの冷媒の流量は、一点鎖線Cで示す冷媒の流量に近い方が望ましい。 In FIG. 7, the dotted line A shows the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided, and the solid line B shows the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided. Shown. Further, the alternate long and short dash line C shows a case where the flow rate of the refrigerant flowing through the main flow path 15a is constant in the vertical direction. When the flow rate of the refrigerant flowing through the main flow path 15a is constant in the vertical direction, the inflow amount of the refrigerant flowing into the heat transfer tubes 70 arranged in the first direction is constant. Therefore, it is desirable that the flow rate of the refrigerant in the main flow path 15a is close to the flow rate of the refrigerant indicated by the alternate long and short dash line C.
 点線Aで示すように、本体151に第2流路である副流路25を設けていない場合には、第1流路である主流路15aの上部に液冷媒が滞留した状態になり、第1流路である主流路15aの上部に液冷媒が多く分布される。 As shown by the dotted line A, when the main body 151 is not provided with the sub-flow path 25 which is the second flow path, the liquid refrigerant stays in the upper part of the main flow path 15a which is the first flow path. A large amount of liquid refrigerant is distributed above the main flow path 15a, which is one flow path.
 これに対し、本体151に第2流路である副流路25を設けている場合には、主流路15aの上部に滞留した液冷媒は、副流路25を介して主流路15aの下部に戻る。そのため、点線Aと実線Bとの間の矢印MUで示すように、主流路15aの上部は、主流路15aの下部に冷媒が戻るため冷媒の流量が低下する。また、点線Aと実線Bとの間の矢印MDで示すように、主流路15aの下部は、主流路15aの上部から冷媒が戻るため冷媒の流量が増加する。そのため、実線Bで示すように、副流路25を有する場合の主流路15aを流れる冷媒の流量は、副流路25を有さない場合の主流路15aを流れる冷媒の流量と比較して、一点鎖線Cで示す冷媒の流量に近づいている。そのため、副流路25を有する冷媒分配器150は、副流路25を有さない冷媒分配器と比較して、各伝熱管70に冷媒を均等に分配することができる。 On the other hand, when the main body 151 is provided with the sub-flow path 25 which is the second flow path, the liquid refrigerant staying in the upper part of the main flow path 15a is transferred to the lower part of the main flow path 15a via the sub-flow path 25. return. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases. Further, as shown by the arrow MD between the dotted line A and the solid line B, the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a. Therefore, as shown by the solid line B, the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
[熱交換器100の効果]
 熱交換器100は、冷媒が流れる主流路15a及び副流路25が内部に形成された冷媒分配器150を有する。第2流路である副流路25は、第1方向(Z軸方向)に延伸し、両端部が第1流路である主流路15aと接続するように形成されている。この第2流路である副流路25は、第1方向(Z軸方向)及び第2方向(X軸方向)に平行な面Pに交差する方向を第3方向と定義した場合に、第1流路である主流路15aに対して第3方向に位置するように形成されている。そのため、熱交換器100は、冷媒を流通させる第2方向への冷媒分配器150の大型化を抑制することができ、構造成約の範囲内で熱交換器100を伝熱管70の管路の延びる第2方向へ大きくすることができる。そのため、熱交換器100は、伝熱管70の伝熱面積を広く確保しつつ、冷媒分配器150を伝熱管70の管路の延伸方向に大型化せずにコンパクトにすることができる。
[Effect of heat exchanger 100]
The heat exchanger 100 has a refrigerant distributor 150 in which a main flow path 15a through which the refrigerant flows and a sub-flow path 25 are formed therein. The sub-flow path 25, which is the second flow path, extends in the first direction (Z-axis direction) and is formed so that both ends are connected to the main flow path 15a, which is the first flow path. The sub-flow path 25, which is the second flow path, is the third direction when the direction intersecting the plane P parallel to the first direction (Z-axis direction) and the second direction (X-axis direction) is defined as the third direction. It is formed so as to be located in the third direction with respect to the main flow path 15a which is one flow path. Therefore, the heat exchanger 100 can suppress the increase in size of the refrigerant distributor 150 in the second direction in which the refrigerant flows, and extends the heat exchanger 100 through the conduit of the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
 また、熱交換器100は、伝熱管70の管路の延伸方向に第1流路と第2流路とを有する熱交換器と比較して、伝熱管70の伝熱面積を広く確保することができる。そのため、熱交換器100は、伝熱管70の管路の延伸方向に第1流路と第2流路とを有する熱交換器と比較して、熱交換の性能を向上させることができる。そのため、熱交換器100は、空調機の運転状態に依存する冷媒流量あるいは乾き度変化に対し、冷媒分配の偏流抑制を向上させることができ、冷媒流量等に対応する幅が広くなる分配ロバスト性を向上させることができる。 Further, the heat exchanger 100 secures a wider heat transfer area of the heat transfer tube 70 as compared with a heat exchanger having a first flow path and a second flow path in the extending direction of the line of the heat transfer tube 70. Can be done. Therefore, the heat exchanger 100 can improve the heat exchange performance as compared with the heat exchanger having the first flow path and the second flow path in the extending direction of the conduit of the heat transfer tube 70. Therefore, the heat exchanger 100 can improve the suppression of the uneven flow of the refrigerant distribution with respect to the change in the refrigerant flow rate or the dryness depending on the operating state of the air conditioner, and has a distribution robustness that widens the range corresponding to the refrigerant flow rate and the like. Can be improved.
 また、熱交換器100は、空調機の運転状態によって主流路15aの上部に液冷媒が滞留する状態において、副流路25を有することによって主流路15aの上部から主流路15aの下部へ冷媒を循環させることで、冷媒の偏流を抑制することができる。そのため、副流路25を有する冷媒分配器150を備えた熱交換器100は、副流路25を有さない冷媒分配器を備えた熱交換器と比較して、各伝熱管70に冷媒を均等に分配することができる。その結果、熱交換器100は、副流路25を有さない冷媒分配器を備えた熱交換器と比較して、熱交換の性能を向上させることができる。 Further, the heat exchanger 100 has a sub-flow path 25 so that the refrigerant can be transferred from the upper part of the main flow path 15a to the lower part of the main flow path 15a in a state where the liquid refrigerant stays in the upper part of the main flow path 15a depending on the operating state of the air conditioner. By circulating the refrigerant, the drift of the refrigerant can be suppressed. Therefore, the heat exchanger 100 provided with the refrigerant distributor 150 having the auxiliary flow path 25 transfers the refrigerant to each heat transfer tube 70 as compared with the heat exchanger provided with the refrigerant distributor having no auxiliary flow path 25. It can be evenly distributed. As a result, the heat exchanger 100 can improve the heat exchange performance as compared with the heat exchanger provided with the refrigerant distributor which does not have the auxiliary flow path 25.
 また、冷媒分配器150は、第1板状部材10と、第2板状部材20と、第3板状部材30との積層方向において、主流路15aと副流路25の両端部とが重なり、主流路15aと分配孔部26と挿入孔31とが重なるように形成されている。そのため、熱交換器100は、伝熱管70の管路の延びる第2方向への冷媒分配器150の大型化を抑制することができ、構造成約の範囲内で熱交換器100を伝熱管70の管路の延びる第2方向へ大きくすることができる。そのため、熱交換器100は、伝熱管70の伝熱面積を広く確保しつつ、冷媒分配器150を伝熱管70の管路の延伸方向に大型化せずにコンパクトにすることができる。 Further, in the refrigerant distributor 150, both ends of the main flow path 15a and the sub-flow path 25 overlap in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. , The main flow path 15a, the distribution hole portion 26, and the insertion hole 31 are formed so as to overlap each other. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
 また、第2流路である副流路25の両端部は、第1流路である主流路15aから冷媒が流入する入口部25bと、第1流路である主流路15aに冷媒を流出する出口部25cと、から構成されている。この入口部25b及び出口部25cは第3方向に延びるように形成されている。そのため、熱交換器100は、伝熱管70の管路の延びる第2方向への冷媒分配器150の大型化を抑制することができ、構造成約の範囲内で熱交換器100を伝熱管70の管路の延びる第2方向へ大きくすることができる。そのため、熱交換器100は、伝熱管70の伝熱面積を広く確保しつつ、冷媒分配器150を伝熱管70の管路の延伸方向に大型化せずにコンパクトにすることができる。 Further, both ends of the sub-flow path 25 which is the second flow path flow out the refrigerant to the inlet portion 25b where the refrigerant flows in from the main flow path 15a which is the first flow path and the main flow path 15a which is the first flow path. It is composed of an outlet portion 25c and an outlet portion 25c. The inlet portion 25b and the outlet portion 25c are formed so as to extend in the third direction. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
 また、第2流路である副流路25は、第3方向において、分配孔部26の両側にそれぞれ形成されている。そのため、熱交換器100は、伝熱管70の管路の延びる第2方向への冷媒分配器150の大型化を抑制することができ、構造成約の範囲内で熱交換器100を伝熱管70の管路の延びる第2方向へ大きくすることができる。そのため、熱交換器100は、伝熱管70の伝熱面積を広く確保しつつ、冷媒分配器150を伝熱管70の管路の延伸方向に大型化せずにコンパクトにすることができる。 Further, the sub-flow path 25, which is the second flow path, is formed on both sides of the distribution hole portion 26 in the third direction. Therefore, the heat exchanger 100 can suppress the enlargement of the refrigerant distributor 150 in the second direction in which the conduit of the heat transfer tube 70 extends, and the heat exchanger 100 can be transferred to the heat transfer tube 70 within the range of the structural contract. It can be increased in the second direction in which the pipeline extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
 また、分配孔部26は、第1方向(Z軸方向)に沿って複数形成されている。複数の分配孔部26のそれぞれは、第1流路である主流路15aと複数の伝熱管70のそれぞれとの間の冷媒流路において、流動抵抗の高い絞り孔として機能する。熱交換器が蒸発器として機能する際には、各分配孔部26が絞り孔として機能することにより、主流路15aの圧力が上昇し、主流路15aの圧力と、複数の挿入孔31のそれぞれの圧力と、の圧力差が増大する。このため、主流路15aの圧力と上段の挿入孔31の圧力との圧力差と、主流路15aの圧力と下段の挿入孔31の圧力との圧力差と、がより均一化する。これにより、主流路15a内の冷媒は、各挿入孔31に均等に分配され、結果として各伝熱管70に均等に分配される。 Further, a plurality of distribution hole portions 26 are formed along the first direction (Z-axis direction). Each of the plurality of distribution hole portions 26 functions as a throttle hole having a high flow resistance in the refrigerant flow path between the main flow path 15a which is the first flow path and each of the plurality of heat transfer tubes 70. When the heat exchanger functions as an evaporator, each distribution hole 26 functions as a throttle hole, so that the pressure in the main flow path 15a rises, and the pressure in the main flow path 15a and the pressure in the plurality of insertion holes 31 are respectively. The pressure difference between the pressure and the pressure increases. Therefore, the pressure difference between the pressure of the main flow path 15a and the pressure of the upper insertion hole 31 and the pressure difference between the pressure of the main flow path 15a and the pressure of the lower insertion hole 31 become more uniform. As a result, the refrigerant in the main flow path 15a is evenly distributed to each insertion hole 31, and as a result, is evenly distributed to each heat transfer tube 70.
実施の形態2.
 図8は、実施の形態2に係る熱交換器100の要部構成を概念的に示す分解斜視図である。図9は、実施の形態2に係る熱交換器100を構成する冷媒分配器150の第1流路と第2流路との連通位置を概念的に示した断面図である。なお、実施の形態1と同一の機能及び作用を有する構成要素については、同一の符号を付してその説明を省略する。実施の形態2に係る熱交換器100は、冷媒分配器150が更に第4板状部材40及び第5板状部材50を有する点で実施の形態1に係る熱交換器100と異なる。
Embodiment 2.
FIG. 8 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the second embodiment. FIG. 9 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment. The components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted. The heat exchanger 100 according to the second embodiment is different from the heat exchanger 100 according to the first embodiment in that the refrigerant distributor 150 further includes the fourth plate-shaped member 40 and the fifth plate-shaped member 50.
 冷媒分配器150の本体151は、第1板状部材10、第2板状部材20、第3板状部材30、第4板状部材40及び第5板状部材50を有している。第4板状部材40及び第5板状部材50はいずれも、金属平板を用いて形成され、一方向に長い帯状の形状を有している。第1板状部材10、第2板状部材20、第3板状部材30、第4板状部材40及び第5板状部材50のそれぞれの外縁の輪郭は、互いに同一の形状を有している。第1板状部材10、第2板状部材20、第3板状部材30、第4板状部材40及び第5板状部材50は、それぞれの板厚方向が伝熱管70の管路の延伸方向と平行になるように配置されている。すなわち、第1板状部材10、第2板状部材20、第3板状部材30、第4板状部材40及び第5板状部材50は、それぞれの板面が伝熱管70の管路の延伸方向と垂直になるように配置されている。 The main body 151 of the refrigerant distributor 150 has a first plate-shaped member 10, a second plate-shaped member 20, a third plate-shaped member 30, a fourth plate-shaped member 40, and a fifth plate-shaped member 50. Both the fourth plate-shaped member 40 and the fifth plate-shaped member 50 are formed by using a metal flat plate and have a strip-like shape long in one direction. The contours of the outer edges of the first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 have the same shape as each other. There is. The first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 have their respective plate thickness directions extending in the conduit of the heat transfer tube 70. It is arranged so as to be parallel to the direction. That is, the plate surfaces of the first plate-shaped member 10, the second plate-shaped member 20, the third plate-shaped member 30, the fourth plate-shaped member 40, and the fifth plate-shaped member 50 are the conduits of the heat transfer tube 70. It is arranged so as to be perpendicular to the stretching direction.
 冷媒分配器150の本体151は、第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30が、伝熱管70からの距離が遠い方からこの順に積層された構成を有している。第1板状部材10は、本体151において伝熱管70からの距離が最も遠い位置に配置されており、第3板状部材30は、本体151において伝熱管70からの距離が最も近い位置に配置されている。 In the main body 151 of the refrigerant distributor 150, the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 are from the heat transfer tube 70. It has a structure in which the layers are stacked in this order from the farthest distance. The first plate-shaped member 10 is arranged at the position farthest from the heat transfer tube 70 in the main body 151, and the third plate-shaped member 30 is arranged at the position closest to the heat transfer tube 70 in the main body 151. Has been done.
 第4板状部材40は、第1板状部材10と第2板状部材20との間に配置されており、第4板状部材40の板面は、第1板状部材10及び第2板状部材20の板面と隣接する。第5板状部材50は、第2板状部材20と第3板状部材30との間に配置されており、第5板状部材50の板面は、第2板状部材20及び第3板状部材30の板面と隣接する。 The fourth plate-shaped member 40 is arranged between the first plate-shaped member 10 and the second plate-shaped member 20, and the plate surface of the fourth plate-shaped member 40 is the first plate-shaped member 10 and the second plate-shaped member 20. Adjacent to the plate surface of the plate-shaped member 20. The fifth plate-shaped member 50 is arranged between the second plate-shaped member 20 and the third plate-shaped member 30, and the plate surface of the fifth plate-shaped member 50 is the second plate-shaped member 20 and the third plate-shaped member 20. Adjacent to the plate surface of the plate-shaped member 30.
 第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30のうち隣接する部材同士は、ろう付けによって接合されている。第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30は、それぞれの長手方向が第1方向(Z軸方向)に沿うように配置されている。 The adjacent members of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 are joined by brazing. The longitudinal direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30 is in the first direction (Z-axis direction). It is arranged along the line.
 第4板状部材40には、第1流路である主流路15aと副流路25の両端部との間に位置する連通孔45と、第1流路である主流路15aと第2分配孔部46との間に位置する第2分配孔部46とが形成されている。連通孔45及び第2分配孔部46は、貫通孔である。 The fourth plate-shaped member 40 has a communication hole 45 located between the main flow path 15a, which is the first flow path, and both ends of the sub-flow path 25, and the main flow path 15a, which is the first flow path, and the second distribution. A second distribution hole 46 located between the hole 46 is formed. The communication hole 45 and the second distribution hole 46 are through holes.
 連通孔45は、第4板状部材40において、一方の端部151a側に2つ形成されており、他方の端部151b側に2つ形成されている。一方の端部151a側に形成された連通孔45は、副流路25から主流路15aに冷媒が流出する際の出口となる。他方の端部151b側に形成された連通孔45は、主流路15aから副流路25に冷媒が流入する際の入口となる。連通孔45は、図8では矩形状の開口を形成する貫通孔として示されているが、連通孔45の開口形状は矩形状に限定されるものではない。 Two communication holes 45 are formed in the fourth plate-shaped member 40 on one end 151a side and two on the other end 151b side. The communication hole 45 formed on the one end 151a side serves as an outlet when the refrigerant flows out from the sub flow path 25 to the main flow path 15a. The communication hole 45 formed on the other end 151b side serves as an inlet when the refrigerant flows from the main flow path 15a into the sub-flow path 25. The communication hole 45 is shown as a through hole forming a rectangular opening in FIG. 8, but the opening shape of the communication hole 45 is not limited to a rectangular shape.
 連通孔45は、第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30の積層方向において、主流路15aと入口部25bとの間に位置するように形成されている。また、連通孔45は、第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30の積層方向において、主流路15aと出口部25cとの間に位置するように形成されている。したがって、連通孔45は、第1流路である主流路15a及び第2流路である副流路25と連通しており、第1流路である主流路15aと第2流路である副流路25との間を接続する流路としての役割を果たす。 The communication hole 45 is formed with the main flow path 15a and the inlet portion in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30. It is formed so as to be located between 25b. Further, the communication hole 45 is formed with the main flow path 15a in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30. It is formed so as to be located between the outlet portion 25c and the outlet portion 25c. Therefore, the communication hole 45 communicates with the main flow path 15a which is the first flow path and the sub flow path 25 which is the second flow path, and the main flow path 15a which is the first flow path and the sub flow path which is the second flow path. It serves as a flow path connecting the flow path 25.
 第4板状部材40には、それぞれ円形の開口形状を有する複数の第2分配孔部46が形成されている。第2分配孔部46は、第3方向(Y軸方向)において第4板状部材40の中央付近に形成されている。複数の第2分配孔部46は、第2板状部材20に形成された分配孔部26及び後述する第5板状部材50に形成された第3分配孔部51と共に主流路15aと伝熱管70との間の流路を形成し、各伝熱管70に冷媒を分配する。 The fourth plate-shaped member 40 is formed with a plurality of second distribution hole portions 46 each having a circular opening shape. The second distribution hole portion 46 is formed near the center of the fourth plate-shaped member 40 in the third direction (Y-axis direction). The plurality of second distribution hole portions 46 include the main flow path 15a and the heat transfer tube together with the distribution hole portion 26 formed in the second plate-shaped member 20 and the third distribution hole portion 51 formed in the fifth plate-shaped member 50 described later. A flow path is formed between the heat transfer tubes 70 and the refrigerant is distributed to each heat transfer tube 70.
 複数の第2分配孔部46のそれぞれは、第4板状部材40を第4板状部材40の板厚方向に貫通している貫通孔である。複数の第2分配孔部46は、第4板状部材40の長手方向となる第1方向(Z軸方向)に沿って配列している。複数の第2分配孔部46のそれぞれは、第4板状部材40を貫通する貫通孔を形成し、複数の伝熱管70のそれぞれに対応して設けられている。また、複数の第2分配孔部46のそれぞれは、第2板状部材20に形成された分配孔部26のそれぞれに対応して設けられている。更に複数の第2分配孔部46のそれぞれは、後述する第5板状部材50に形成された第3分配孔部51のそれぞれに対応して設けられている。 Each of the plurality of second distribution hole portions 46 is a through hole that penetrates the fourth plate-shaped member 40 in the plate thickness direction of the fourth plate-shaped member 40. The plurality of second distribution hole portions 46 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the fourth plate-shaped member 40. Each of the plurality of second distribution hole portions 46 forms a through hole penetrating the fourth plate-shaped member 40, and is provided corresponding to each of the plurality of heat transfer tubes 70. Further, each of the plurality of second distribution hole portions 46 is provided corresponding to each of the distribution hole portions 26 formed in the second plate-shaped member 20. Further, each of the plurality of second distribution hole portions 46 is provided corresponding to each of the third distribution hole portions 51 formed in the fifth plate-shaped member 50, which will be described later.
 第2分配孔部46の開口形状は、円形状であるが、円形状に限定されるものではなく、例えば、半円状、半楕円状、半長円状又は矩形状であってもよい。なお、複数の第2分配孔部46の流路断面積は、それぞれ同じ大きさである。ただし、複数の第2分配孔部46の流路断面積は、それぞれ同じ大きさのものに限定されるものではなく、異なる大きさに形成されてもよい。 The opening shape of the second distribution hole portion 46 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape. The flow path cross-sectional areas of the plurality of second distribution hole portions 46 are the same size. However, the flow path cross-sectional areas of the plurality of second distribution holes 46 are not limited to those having the same size, and may be formed to have different sizes.
 また、実施の形態2に係る冷媒分配器150の本体151において、第4板状部材40には第2分配孔部46が複数形成されているが、第2分配孔部46は第4板状部材40に1つだけ形成されていてもよい。この場合、第2分配孔部46は、複数の伝熱管70に対応させるために、第1方向(Z軸方向)に延びるように形成されている。 Further, in the main body 151 of the refrigerant distributor 150 according to the second embodiment, a plurality of second distribution hole portions 46 are formed in the fourth plate-shaped member 40, but the second distribution hole portion 46 has a fourth plate shape. Only one may be formed on the member 40. In this case, the second distribution hole portion 46 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
 複数の第2分配孔部46はいずれも、第4板状部材40の板厚方向に見たとき、第1板状部材10の主流路15aと重なるように形成されている。また、複数の第2分配孔部46のそれぞれは、第4板状部材40の板厚方向に見たとき、第2板状部材20の分配孔部26のそれぞれと重なるように形成されている。また、複数の第2分配孔部46のそれぞれは、第4板状部材40の板厚方向に見たとき、第5板状部材50の第3分配孔部51のそれぞれと重なるように形成されている。また、複数の第2分配孔部46のそれぞれは、第4板状部材40の板厚方向に見たとき、第3板状部材30の複数の挿入孔31のそれぞれと重なるように形成されている。また、複数の第2分配孔部46のそれぞれは、第4板状部材40の板厚方向に見たとき、複数の伝熱管70のそれぞれと重なるように形成されている。 Each of the plurality of second distribution hole portions 46 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fourth plate-shaped member 40. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the distribution hole portions 26 of the second plate-shaped member 20 when viewed in the plate thickness direction of the fourth plate-shaped member 40. .. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the third distribution hole portions 51 of the fifth plate-shaped member 50 when viewed in the plate thickness direction of the fourth plate-shaped member 40. ing. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30 when viewed in the plate thickness direction of the fourth plate-shaped member 40. There is. Further, each of the plurality of second distribution hole portions 46 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the fourth plate-shaped member 40.
 したがって、第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30の積層方向において、第2分配孔部46は、伝熱管70と第1流路である主流路15aとの間に位置している。そして、第1板状部材10の主流路15aと、複数の伝熱管70のそれぞれとは、複数の第2分配孔部46を介して連通する。 Therefore, in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30, the second distribution hole portion 46 is transmitted. It is located between the heat pipe 70 and the main flow path 15a, which is the first flow path. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of second distribution hole portions 46.
 また、第4板状部材40は、平板状の閉塞部44を有している。閉塞部44の一部は、第4板状部材40の板厚方向に見たときに第1板状部材10の主流路15aと重なる。閉塞部44は、主流路15aと複数の伝熱管70のそれぞれとが、第2分配孔部46を介さずに直接連通するのを防ぐ機能を有している。 Further, the fourth plate-shaped member 40 has a flat plate-shaped closing portion 44. A part of the closing portion 44 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fourth plate-shaped member 40. The closing portion 44 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the second distribution hole portion 46.
 また、閉塞部44は、第1板状部材10の配置側から副流路25の一部を覆う。閉塞部44は、第1板状部材10の配置側から少なくとも副流路25の中央部25aを覆う。閉塞部44は、副流路25を構成する管路の一部を形成する。 Further, the closing portion 44 covers a part of the sub-flow path 25 from the arrangement side of the first plate-shaped member 10. The closing portion 44 covers at least the central portion 25a of the sub-flow path 25 from the arrangement side of the first plate-shaped member 10. The closing portion 44 forms a part of the pipeline forming the sub-flow path 25.
 第5板状部材50には、分配孔部26と挿入孔31との間に位置する第3分配孔部51が形成されている。第3分配孔部51は、貫通孔である。 The fifth plate-shaped member 50 is formed with a third distribution hole 51 located between the distribution hole 26 and the insertion hole 31. The third distribution hole portion 51 is a through hole.
 第5板状部材50には、それぞれ円形の開口形状を有する複数の第3分配孔部51が形成されている。第3分配孔部51は、第3方向(Y軸方向)において第5板状部材50の中央付近に形成されている。複数の第3分配孔部51は、第2板状部材20に形成された分配孔部26及び第4板状部材40に形成された第2分配孔部46と共に主流路15aと伝熱管70との間の流路を形成し、各伝熱管70に冷媒を分配する。 The fifth plate-shaped member 50 is formed with a plurality of third distribution holes 51 each having a circular opening shape. The third distribution hole portion 51 is formed near the center of the fifth plate-shaped member 50 in the third direction (Y-axis direction). The plurality of third distribution hole portions 51 include the main flow path 15a and the heat transfer tube 70 together with the distribution hole portion 26 formed in the second plate-shaped member 20 and the second distribution hole portion 46 formed in the fourth plate-shaped member 40. A flow path is formed between the heat transfer tubes 70 to distribute the refrigerant to each heat transfer tube 70.
 複数の第3分配孔部51のそれぞれは、第5板状部材50を第5板状部材50の板厚方向に貫通している貫通孔である。複数の第3分配孔部51は、第5板状部材50の長手方向となる第1方向(Z軸方向)に沿って配列している。複数の第3分配孔部51のそれぞれは、第5板状部材50を貫通する貫通孔を形成し、複数の伝熱管70のそれぞれに対応して設けられている。また、複数の第3分配孔部51のそれぞれは、第2板状部材20に形成された分配孔部26のそれぞれに対応して設けられている。更に複数の第3分配孔部51のそれぞれは、第4板状部材40に形成された第2分配孔部46のそれぞれに対応して設けられている。 Each of the plurality of third distribution hole portions 51 is a through hole that penetrates the fifth plate-shaped member 50 in the plate thickness direction of the fifth plate-shaped member 50. The plurality of third distribution hole portions 51 are arranged along the first direction (Z-axis direction) which is the longitudinal direction of the fifth plate-shaped member 50. Each of the plurality of third distribution hole portions 51 forms a through hole penetrating the fifth plate-shaped member 50, and is provided corresponding to each of the plurality of heat transfer tubes 70. Further, each of the plurality of third distribution hole portions 51 is provided corresponding to each of the distribution hole portions 26 formed in the second plate-shaped member 20. Further, each of the plurality of third distribution hole portions 51 is provided corresponding to each of the second distribution hole portions 46 formed in the fourth plate-shaped member 40.
 第3分配孔部51の開口形状は、円形状であるが、円形状に限定されるものではなく、例えば、半円状、半楕円状、半長円状又は矩形状であってもよい。なお、複数の第3分配孔部51の流路断面積は、それぞれ同じ大きさである。ただし、複数の第3分配孔部51の流路断面積は、それぞれ同じ大きさのものに限定されるものではなく、異なる大きさに形成されてもよい。 The opening shape of the third distribution hole 51 is circular, but is not limited to a circular shape, and may be, for example, a semicircular shape, a semi-elliptical shape, a semi-elliptical shape, or a rectangular shape. The flow path cross-sectional areas of the plurality of third distribution holes 51 are the same size. However, the flow path cross-sectional areas of the plurality of third distribution holes 51 are not limited to those having the same size, and may be formed to have different sizes.
 また、実施の形態1に係る冷媒分配器150の本体151において、第5板状部材50には第3分配孔部51が複数形成されているが、第3分配孔部51は第5板状部材50に1つだけ形成されていてもよい。この場合、第3分配孔部51は、複数の伝熱管70に対応させるために、第1方向(Z軸方向)に延びるように形成されている。 Further, in the main body 151 of the refrigerant distributor 150 according to the first embodiment, a plurality of third distribution hole portions 51 are formed in the fifth plate-shaped member 50, but the third distribution hole portion 51 has a fifth plate shape. Only one may be formed on the member 50. In this case, the third distribution hole 51 is formed so as to extend in the first direction (Z-axis direction) in order to correspond to the plurality of heat transfer tubes 70.
 複数の第3分配孔部51はいずれも、第5板状部材50の板厚方向に見たとき、第1板状部材10の主流路15aと重なるように形成されている。また、複数の第3分配孔部51のそれぞれは、第5板状部材50の板厚方向に見たとき、第2板状部材20の分配孔部26のそれぞれと重なるように形成されている。また、複数の第3分配孔部51のそれぞれは、第5板状部材50の板厚方向に見たとき、第4板状部材40の第2分配孔部46のそれぞれと重なるように形成されている。また、複数の第3分配孔部51のそれぞれは、第5板状部材50の板厚方向に見たとき、第3板状部材30の複数の挿入孔31のそれぞれと重なるように形成されている。また、複数の第3分配孔部51のそれぞれは、第5板状部材50の板厚方向に見たとき、複数の伝熱管70のそれぞれと重なるように形成されている。 Each of the plurality of third distribution hole portions 51 is formed so as to overlap the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fifth plate-shaped member 50. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the distribution hole portions 26 of the second plate-shaped member 20 when viewed in the plate thickness direction of the fifth plate-shaped member 50. .. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the second distribution hole portions 46 of the fourth plate-shaped member 40 when viewed in the plate thickness direction of the fifth plate-shaped member 50. ing. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the plurality of insertion holes 31 of the third plate-shaped member 30 when viewed in the plate thickness direction of the fifth plate-shaped member 50. There is. Further, each of the plurality of third distribution hole portions 51 is formed so as to overlap each of the plurality of heat transfer tubes 70 when viewed in the plate thickness direction of the fifth plate-shaped member 50.
 したがって、第1板状部材10、第4板状部材40、第2板状部材20、第5板状部材50及び第3板状部材30の積層方向において、第3分配孔部51は、伝熱管70と第1流路である主流路15aとの間に位置している。そして、第1板状部材10の主流路15aと、複数の伝熱管70のそれぞれとは、複数の第3分配孔部51を介して連通する。 Therefore, in the stacking direction of the first plate-shaped member 10, the fourth plate-shaped member 40, the second plate-shaped member 20, the fifth plate-shaped member 50, and the third plate-shaped member 30, the third distribution hole portion 51 is transmitted. It is located between the heat pipe 70 and the main flow path 15a, which is the first flow path. Then, the main flow path 15a of the first plate-shaped member 10 and each of the plurality of heat transfer tubes 70 communicate with each other via the plurality of third distribution hole portions 51.
 また、第5板状部材50は、平板状の閉塞部53を有している。閉塞部53の一部は、第5板状部材50の板厚方向に見たときに第1板状部材10の主流路15aと重なる。閉塞部53は、主流路15aと複数の伝熱管70のそれぞれとが、第3分配孔部51を介さずに直接連通するのを防ぐ機能を有している。 Further, the fifth plate-shaped member 50 has a flat plate-shaped closing portion 53. A part of the closing portion 53 overlaps with the main flow path 15a of the first plate-shaped member 10 when viewed in the plate thickness direction of the fifth plate-shaped member 50. The closing portion 53 has a function of preventing the main flow path 15a and each of the plurality of heat transfer tubes 70 from directly communicating with each other without passing through the third distribution hole portion 51.
 また、閉塞部53は、第3板状部材30の配置側から副流路25の一部を覆う。閉塞部53は、第3板状部材30の配置側から少なくとも副流路25の中央部25aを覆う。閉塞部53は、副流路25を構成する管路の一部を形成する。 Further, the closing portion 53 covers a part of the sub-flow path 25 from the arrangement side of the third plate-shaped member 30. The closing portion 53 covers at least the central portion 25a of the sub-flow path 25 from the arrangement side of the third plate-shaped member 30. The closing portion 53 forms a part of the pipeline forming the sub-flow path 25.
 図10は、実施の形態2に係る熱交換器100を構成する冷媒分配器150内の冷媒の流れを示した概念図である。冷凍サイクル装置200が暖房運転の場合、冷媒分配器150に流入する冷媒は、気液二相流である。気液二相冷媒は、冷媒流入管60から本体151内に流入し、図10の矢印UFで示すように、第1板状部材10に形成された主流路15aを一方の端部151aから他方の端部151bに向かって鉛直上向きに流れる。鉛直に上昇して流れる冷媒の一部は、第4板状部材40の第2分配孔部46、第2板状部材20の分配孔部26及び第5板状部材50の第3分配孔部51をこの順番に通り、第3板状部材30に形成された挿入孔31を通って各伝熱管70に分配される。 FIG. 10 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment. When the refrigeration cycle device 200 is in a heating operation, the refrigerant flowing into the refrigerant distributor 150 is a gas-liquid two-phase flow. The gas-liquid two-phase refrigerant flows into the main body 151 from the refrigerant inflow pipe 60, and as shown by the arrow UF in FIG. 10, the main flow path 15a formed in the first plate-shaped member 10 is formed from one end 151a to the other. Flows vertically upward toward the end 151b of. A part of the refrigerant that rises vertically and flows is the second distribution hole portion 46 of the fourth plate-shaped member 40, the distribution hole portion 26 of the second plate-shaped member 20, and the third distribution hole portion of the fifth plate-shaped member 50. It passes through 51 in this order and is distributed to each heat transfer tube 70 through an insertion hole 31 formed in the third plate-shaped member 30.
 また、主流路15aの上部に滞留した冷媒は、主流路15aの上端部15a1と連通した連通孔45を介して第2板状部材20に設けられた入口部25bへ流入する。この際、冷媒は、矢印OFで示すように、第1流路である主流路15aから第2流路である副流路25に向かって、第3方向となる外側に向かって流れる。そして、副流路25の入口部25bから流入した冷媒は、矢印DFで示すように、第2板状部材20に形成された副流路25の中央部25aを重力方向に沿って下向きに流れる。 Further, the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 25b provided in the second plate-shaped member 20 through the communication hole 45 communicating with the upper end portion 15a1 of the main flow path 15a. At this time, as shown by the arrow OF, the refrigerant flows from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path, toward the outside, which is the third direction. Then, as shown by the arrow DF, the refrigerant flowing in from the inlet portion 25b of the sub-channel 25 flows downward along the central portion 25a of the sub-channel 25 formed in the second plate-shaped member 20. ..
 副流路25の中央部25aの下端に到達した冷媒は、主流路15aの下端部15a2と連通した連通孔45を介して出口部25cから主流路15aへ流出する。この際、冷媒は、矢印IFで示すように、第2流路である副流路25から第1流路である主流路15aに向かって、第3方向となる内側に向かって流れる。そして、出口部25cから主流路15aへ流出した冷媒は、冷媒流入管60から本体151内に流入した冷媒と共に、主流路15aを鉛直に上昇し、各伝熱管70に分配される。 The refrigerant that has reached the lower end of the central portion 25a of the sub-flow path 25 flows out from the outlet portion 25c to the main flow path 15a through the communication hole 45 that communicates with the lower end portion 15a2 of the main flow path 15a. At this time, as shown by the arrow IF, the refrigerant flows inward in the third direction from the sub-flow path 25 which is the second flow path toward the main flow path 15a which is the first flow path. Then, the refrigerant flowing out from the outlet portion 25c to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
 図11は、実施の形態2に係る熱交換器100を構成する冷媒分配器150内の冷媒の流量分布を表した図である。図11において、横軸は、冷媒流量[kg/h]を表し、縦軸は、伝熱管70が配列する第1方向において、冷媒流入口18からの距離[m]を表している。 FIG. 11 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the second embodiment. In FIG. 11, the horizontal axis represents the refrigerant flow rate [kg / h], and the vertical axis represents the distance [m] from the refrigerant inlet 18 in the first direction in which the heat transfer tubes 70 are arranged.
 実施の形態1と同様に、本体151に第2流路である副流路25を設けている場合には、主流路15aの上部に滞留した液冷媒は、副流路25を介して主流路15aの下部に戻る。そのため、点線Aと実線Bとの間の矢印MUで示すように、主流路15aの上部は、主流路15aの下部に冷媒が戻るため冷媒の流量が低下する。また、点線Aと実線Bとの間の矢印MDで示すように、主流路15aの下部は、主流路15aの上部から冷媒が戻るため冷媒の流量が増加する。そのため、実線Bで示すように、副流路25を有する場合の主流路15aを流れる冷媒の流量は、副流路25を有さない場合の主流路15aを流れる冷媒の流量と比較して、一点鎖線Cで示す冷媒の流量に近づいている。そのため、副流路25を有する冷媒分配器150は、副流路25を有さない冷媒分配器と比較して、各伝熱管70に冷媒を均等に分配することができる。 Similar to the first embodiment, when the main body 151 is provided with the sub-flow path 25 which is the second flow path, the liquid refrigerant staying in the upper part of the main flow path 15a passes through the main flow path 25. Return to the bottom of 15a. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases. Further, as shown by the arrow MD between the dotted line A and the solid line B, the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a. Therefore, as shown by the solid line B, the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
[熱交換器100の効果]
 冷媒分配器150は、第4板状部材40及び第5板状部材50を有している。そして、第4板状部材40には、第1流路である主流路15aと副流路25の両端部との間に位置する連通孔45と、第1流路である主流路15aと分配孔部26との間に位置する第2分配孔部46とが形成されている。また、第5板状部材50には、分配孔部26と挿入孔31との間に位置する第3分配孔部51が形成されている。
[Effect of heat exchanger 100]
The refrigerant distributor 150 has a fourth plate-shaped member 40 and a fifth plate-shaped member 50. The fourth plate-shaped member 40 is divided into a communication hole 45 located between the main flow path 15a, which is the first flow path, and both ends of the sub-flow path 25, and the main flow path 15a, which is the first flow path. A second distribution hole 46 located between the hole 26 is formed. Further, the fifth plate-shaped member 50 is formed with a third distribution hole portion 51 located between the distribution hole portion 26 and the insertion hole 31.
 冷媒分配器150の本体151は、第4板状部材40及び第5板状部材50の上記の貫通を有することで、主流路15aと副流路25との間の冷媒の流通、及び、主流路15aから伝熱管70への冷媒の流通を妨げることがない。更に、冷媒分配器150の本体151は、第4板状部材40の閉塞部44及び第5板状部材50の閉塞部53によって、副流路25の管路を形成することができる。すなわち、冷媒分配器150の本体151は、副流路25の管路を形成するために、第1板状部材10の平板部11及び第3板状部材30の平板部34を必要としない。 The main body 151 of the refrigerant distributor 150 has the above-mentioned penetration of the fourth plate-shaped member 40 and the fifth plate-shaped member 50, so that the refrigerant flows between the main flow path 15a and the sub-flow path 25 and the mainstream. It does not interfere with the flow of the refrigerant from the passage 15a to the heat transfer tube 70. Further, the main body 151 of the refrigerant distributor 150 can form a conduit for the sub-flow path 25 by the closing portion 44 of the fourth plate-shaped member 40 and the closing portion 53 of the fifth plate-shaped member 50. That is, the main body 151 of the refrigerant distributor 150 does not require the flat plate portion 11 of the first plate-shaped member 10 and the flat plate portion 34 of the third plate-shaped member 30 in order to form the conduit of the sub-flow path 25.
 そのため、第2板状部材20は、各板状部材の積層方向に見た場合に、第1板状部材10の主流路15a及び第3板状部材30の挿入孔31と重なるように副流路25を形成することができる。換言すれば、冷媒分配器150の本体151は、第3方向(Y軸方向)において、第2板状部材20に形成される副流路25の幅を大きくすることができ、副流路25の容積を大きくすることができる。そのため、熱交換器100の冷媒分配器150は、副流路25側の圧力損失が小さくなり循環流量が高い時、上部に滞留した多くの冷媒を循環させることができ、冷媒偏流を抑制し、熱交換器100の性能を向上させることができる。 Therefore, the second plate-shaped member 20 has a side flow so as to overlap the main flow path 15a of the first plate-shaped member 10 and the insertion hole 31 of the third plate-shaped member 30 when viewed in the stacking direction of each plate-shaped member. The road 25 can be formed. In other words, the main body 151 of the refrigerant distributor 150 can increase the width of the sub-flow path 25 formed in the second plate-shaped member 20 in the third direction (Y-axis direction), and the sub-flow path 25 can be increased. The volume of the can be increased. Therefore, the refrigerant distributor 150 of the heat exchanger 100 can circulate a large amount of refrigerant staying in the upper part when the pressure loss on the sub-flow path 25 side is small and the circulation flow rate is high, and suppresses the refrigerant drift. The performance of the heat exchanger 100 can be improved.
実施の形態3.
 図12は、実施の形態3に係る熱交換器100の要部構成を概念的に示す分解斜視図である。図13は、実施の形態3に係る熱交換器100を構成する冷媒分配器150の第1流路と第2流路との連通位置を概念的に示した断面図である。図14は、実施の形態3に係る熱交換器100を構成する冷媒分配器150内の冷媒の流れを示した概念図である。なお、実施の形態1と同一の機能及び作用を有する構成要素については、同一の符号を付してその説明を省略する。実施の形態3に係る熱交換器100は、出口部25c1の管軸の角度を特定している点で実施の形態1に係る熱交換器100の出口部25cと異なる。
Embodiment 3.
FIG. 12 is an exploded perspective view conceptually showing the main configuration of the heat exchanger 100 according to the third embodiment. FIG. 13 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment. FIG. 14 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment. The components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted. The heat exchanger 100 according to the third embodiment is different from the outlet portion 25c of the heat exchanger 100 according to the first embodiment in that the angle of the pipe axis of the outlet portion 25c1 is specified.
 副流路25は、図12に示すように、中央部25aと、入口部25bと、出口部25c1とを有している。中央部25aは、第1方向(Z軸方向)に延びる流路を形成している。出口部25c1は、第1方向(Z軸方向)において、中央部25aの他方の端部25a2に形成されている。 As shown in FIG. 12, the subchannel 25 has a central portion 25a, an inlet portion 25b, and an outlet portion 25c1. The central portion 25a forms a flow path extending in the first direction (Z-axis direction). The outlet portion 25c1 is formed at the other end portion 25a2 of the central portion 25a in the first direction (Z-axis direction).
 出口部25c1の管軸TAは、第2板状部材20の対角線DLに近づくように第1方向(Z軸方向)及び第3方向(Y軸方向)に対して傾斜している。したがって、出口部25c1は、図14の矢印IF及び矢印UFで示すように、出口部25c1から流出される冷媒の流れる方向が冷媒流入管60から流出される冷媒の流れる方向のベクトル成分を有するように第1方向及び第3方向に対して傾いて形成されている。すなわち、出口部25c1から流出される冷媒は、主流路15aを流れる冷媒の流れに沿う方向に向いている。 The pipe axis TA of the outlet portion 25c1 is inclined with respect to the first direction (Z-axis direction) and the third direction (Y-axis direction) so as to approach the diagonal DL of the second plate-shaped member 20. Therefore, as shown by the arrows IF and UF in FIG. 14, the outlet portion 25c1 has a vector component in which the direction in which the refrigerant flowing out from the outlet portion 25c1 flows has a vector component in the direction in which the refrigerant flowing out from the refrigerant inflow pipe 60 flows. It is formed so as to be inclined with respect to the first direction and the third direction. That is, the refrigerant flowing out from the outlet portion 25c1 is directed in the direction along the flow of the refrigerant flowing through the main flow path 15a.
 第2板状部材20の板面において、出口部25c1の管軸TA方向と、重力方向GDとの間の角度である出口角度θは、90度以上の角度となるように形成されている。 On the plate surface of the second plate-shaped member 20, the outlet angle θ, which is the angle between the pipe axis TA direction of the outlet portion 25c1 and the gravity direction GD, is formed to be an angle of 90 degrees or more.
 図15は、実施の形態3に係る熱交換器100を構成する冷媒分配器150内の冷媒の流量分布を表した図である。図12において、横軸は、冷媒流量[kg/h]を表し、縦軸は、伝熱管70が配列する第1方向において、冷媒流入口18からの距離[m]を表している。 FIG. 15 is a diagram showing the flow rate distribution of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the third embodiment. In FIG. 12, the horizontal axis represents the refrigerant flow rate [kg / h], and the vertical axis represents the distance [m] from the refrigerant inflow port 18 in the first direction in which the heat transfer tubes 70 are arranged.
 実施の形態1と同様に、本体151に第2流路である副流路25を設けている場合には、主流路15aの上部に滞留した液冷媒は、副流路25を介して主流路15aの下部に戻る。そのため、点線Aと実線Bとの間の矢印MUで示すように、主流路15aの上部は、主流路15aの下部に冷媒が戻るため冷媒の流量が低下する。また、点線Aと実線Bとの間の矢印MDで示すように、主流路15aの下部は、主流路15aの上部から冷媒が戻るため冷媒の流量が増加する。そのため、実線Bで示すように、副流路25を有する場合の主流路15aを流れる冷媒の流量は、副流路25を有さない場合の主流路15aを流れる冷媒の流量と比較して、一点鎖線Cで示す冷媒の流量に近づいている。そのため、副流路25を有する冷媒分配器150は、副流路25を有さない冷媒分配器と比較して、各伝熱管70に冷媒を均等に分配することができる。 Similar to the first embodiment, when the main body 151 is provided with the sub-flow path 25 which is the second flow path, the liquid refrigerant staying in the upper part of the main flow path 15a passes through the main flow path 25. Return to the bottom of 15a. Therefore, as shown by the arrow MU between the dotted line A and the solid line B, the refrigerant returns to the lower part of the main flow path 15a in the upper part of the main flow path 15a, so that the flow rate of the refrigerant decreases. Further, as shown by the arrow MD between the dotted line A and the solid line B, the flow rate of the refrigerant increases in the lower part of the main flow path 15a because the refrigerant returns from the upper part of the main flow path 15a. Therefore, as shown by the solid line B, the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is provided is compared with the flow rate of the refrigerant flowing through the main flow path 15a when the sub-flow path 25 is not provided. It is approaching the flow rate of the refrigerant indicated by the alternate long and short dash line C. Therefore, the refrigerant distributor 150 having the auxiliary flow path 25 can evenly distribute the refrigerant to each heat transfer tube 70 as compared with the refrigerant distributor having no auxiliary flow path 25.
[熱交換器100の効果]
 出口部25c1は、図14の矢印IF及び矢印UFで示すように、出口部25c1から流出される冷媒の流れる方向が、冷媒流入管60から流出される冷媒の流れる方向のベクトル成分を有するように第1方向及び第3方向に対して傾いて形成されている。第2板状部材20に形成された副流路25の出口部25c1の向きが鉛直上昇方向であり、副流路25から主流路15aに合流する際の冷媒の流れベクトルが上向きになることで、冷媒の上方向の慣性力が増加する。そのため、熱交換器100の冷媒分配器150は、主流路15aと副流路25とにおける冷媒の循環が促進される。そして、熱交換器100の冷媒分配器150は、主流路15aの上部に滞留した多くの冷媒を循環させることができ、冷媒の偏流を抑制することができる。
[Effect of heat exchanger 100]
As shown by the arrows IF and UF in FIG. 14, the outlet portion 25c1 has a vector component in the direction in which the refrigerant flowing out from the outlet portion 25c1 flows in the direction in which the refrigerant flows out from the refrigerant inflow pipe 60. It is formed so as to be inclined with respect to the first direction and the third direction. The direction of the outlet portion 25c1 of the sub-flow path 25 formed in the second plate-shaped member 20 is the vertical ascending direction, and the flow vector of the refrigerant when merging from the sub-flow path 25 to the main flow path 15a is upward. , The upward inertial force of the refrigerant increases. Therefore, the refrigerant distributor 150 of the heat exchanger 100 promotes the circulation of the refrigerant in the main flow path 15a and the sub-flow path 25. Then, the refrigerant distributor 150 of the heat exchanger 100 can circulate a large amount of refrigerant staying in the upper part of the main flow path 15a, and can suppress the drift of the refrigerant.
実施の形態4.
 図16は、実施の形態4に係る熱交換器100の要部構成を概念的に示す分解斜視図である。図17は、実施の形態4に係る熱交換器100を構成する冷媒分配器150の第1流路と第2流路との連通位置を概念的に示した断面図である。図18は、実施の形態4に係る熱交換器100を構成する冷媒分配器150内の冷媒の流れを示した概念図である。なお、実施の形態1と同一の機能及び作用を有する構成要素については、同一の符号を付してその説明を省略する。実施の形態4に係る熱交換器100は、第1流路である主流路15aの構成を更に特定している点で実施の形態1に係る熱交換器100と異なる。
Embodiment 4.
FIG. 16 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the fourth embodiment. FIG. 17 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the fourth embodiment. FIG. 18 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the fourth embodiment. The components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted. The heat exchanger 100 according to the fourth embodiment is different from the heat exchanger 100 according to the first embodiment in that the configuration of the main flow path 15a, which is the first flow path, is further specified.
 第1流路部15は、上述したように内部に第1流路である主流路15aを形成している。実施の形態4に係る熱交換器100において、第1流路である主流路15aは、冷媒流入管60と連通した側の一方の下端部15a2から、他方の上端部15a1に向かって流路断面積が小さくなるように形成されている。第1方向(Z軸方向)を上下方向と特定する場合には、主流路15aは、上方に向かうにつれて流路断面積が縮小するように形成されている。第1流路部15は、図17に示すように、矩形の断面形状を有している。ただし、第1流路部15の断面形状は、矩形に限定されるものではなく、例えば、半円状、半楕円状又は半長円状であってもよい。 As described above, the first flow path portion 15 forms the main flow path 15a, which is the first flow path, inside. In the heat exchanger 100 according to the fourth embodiment, the main flow path 15a, which is the first flow path, is cut off from one lower end portion 15a2 on the side communicating with the refrigerant inflow pipe 60 toward the other upper end portion 15a1. It is formed so that the area is small. When the first direction (Z-axis direction) is specified as the vertical direction, the main flow path 15a is formed so that the cross-sectional area of the flow path decreases as it goes upward. As shown in FIG. 17, the first flow path portion 15 has a rectangular cross-sectional shape. However, the cross-sectional shape of the first flow path portion 15 is not limited to a rectangle, and may be, for example, a semicircular shape, a semi-elliptical shape, or a semi-elliptical shape.
 第1流路部15は、第1板状部材10の長手方向に沿って、本体部の一方の端部151aから他方の端部151bまで延伸している。第1流路部15の延伸方向の両端は閉塞されている。図16では、第1流路部15は、第1板状部材10、第2板状部材20及び第3板状部材30の積層方向に見た場合に、台形状に形成された側壁15bを有している。第1流路部15は、側壁15bを有した四角柱状に形成されている。第1流路部15は、第1板状部材10の長手方向において、冷媒流入口18側の下端部15a2から他方の上端部15a1に向かって先細りになるように形成されている。なお、第1流路部15は、側壁15bを有した四角柱状に形成されたものに限定されるものではなく、例えば、円錐台形状、あるいは、多角錐台形状等、他の形状であってもよい。 The first flow path portion 15 extends from one end portion 151a of the main body portion to the other end portion 151b along the longitudinal direction of the first plate-shaped member 10. Both ends of the first flow path portion 15 in the stretching direction are closed. In FIG. 16, the first flow path portion 15 has a side wall 15b formed in a trapezoidal shape when viewed in the stacking direction of the first plate-shaped member 10, the second plate-shaped member 20, and the third plate-shaped member 30. Have. The first flow path portion 15 is formed in a square columnar shape having a side wall 15b. The first flow path portion 15 is formed so as to taper from the lower end portion 15a2 on the refrigerant inflow port 18 side toward the other upper end portion 15a1 in the longitudinal direction of the first plate-shaped member 10. The first flow path portion 15 is not limited to the one formed in a square columnar shape having the side wall 15b, and may have another shape such as a truncated cone shape or a truncated cone shape. May be good.
[熱交換器100の効果]
 第1流路である主流路15aは、冷媒流入管60と連通した側の一方の下端部15a2から、他方の上端部15a1に向かって流路断面積が小さくなるように形成されている。第1方向(Z軸方向)とした場合に、主流路15aの流路断面積が鉛直上部に行くほど小さく形成されていることで、熱交換器100の冷媒分配器150は、主流路15aでの冷媒の流速を上げることができる。そのため、空調機の運転状態によって、冷媒循環量が小さくなった場合でも、熱交換器100の冷媒分配器150は、主流路15aの最上部まで冷媒を到達させることができ、冷媒の偏流を抑制することができる。
[Effect of heat exchanger 100]
The main flow path 15a, which is the first flow path, is formed so that the cross-sectional area of the flow path decreases from one lower end portion 15a2 on the side communicating with the refrigerant inflow pipe 60 toward the other upper end portion 15a1. When the first direction (Z-axis direction) is set, the flow path cross-sectional area of the main flow path 15a is formed to be smaller toward the upper vertical direction, so that the refrigerant distributor 150 of the heat exchanger 100 is formed in the main flow path 15a. The flow velocity of the refrigerant can be increased. Therefore, even if the amount of refrigerant circulation becomes small depending on the operating state of the air conditioner, the refrigerant distributor 150 of the heat exchanger 100 can reach the uppermost part of the main flow path 15a and suppress the drift of the refrigerant. can do.
実施の形態5.
 図19は、実施の形態5に係る熱交換器100の要部構成を概念的に示す分解斜視図である。図20は、図19に示す冷媒分配器150の内部を概念的に示す側面図である。図21は、実施の形態5に係る熱交換器100を構成する冷媒分配器150の第1流路と第2流路との連通位置を概念的に示した断面図である。なお、実施の形態1と同一の機能及び作用を有する構成要素については、同一の符号を付してその説明を省略する。実施の形態1~4の冷媒分配器150は、第1板状部材10~第5板状部材50等を積層させて構成されたものである。これに対して、実施の形態5の冷媒分配器150の本体151は、筒状部材を用いて構成されたものである。
Embodiment 5.
FIG. 19 is an exploded perspective view conceptually showing the configuration of a main part of the heat exchanger 100 according to the fifth embodiment. FIG. 20 is a side view conceptually showing the inside of the refrigerant distributor 150 shown in FIG. FIG. 21 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor 150 constituting the heat exchanger 100 according to the fifth embodiment. The components having the same functions and functions as those in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted. The refrigerant distributors 150 of the first to fourth embodiments are configured by laminating the first plate-shaped members 10 to the fifth plate-shaped members 50 and the like. On the other hand, the main body 151 of the refrigerant distributor 150 of the fifth embodiment is configured by using a tubular member.
 冷媒分配器150本体151は、第1方向(Z軸方向)に延伸し、複数の伝熱管70のそれぞれの一端に接続されて複数の伝熱管70に冷媒を分配する。 The refrigerant distributor 150 main body 151 extends in the first direction (Z-axis direction) and is connected to one end of each of the plurality of heat transfer tubes 70 to distribute the refrigerant to the plurality of heat transfer tubes 70.
 冷媒分配器150の本体151は、複数の伝熱管70の配列方向となる第1方向(Z軸方向)に延びる筒状部90を有する。また、冷媒分配器150の本体151は、筒状部90内の中空部95において、主流路15aと副流路25とを第3方向に隔て、第1方向の両端部に貫通孔である入口部92aと出口部92bとが形成された壁部91を有する。更に、冷媒分配器150の本体151は、筒状部90の両端をそれぞれ閉塞する蓋部94を有する。 The main body 151 of the refrigerant distributor 150 has a tubular portion 90 extending in the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. Further, in the hollow portion 95 in the tubular portion 90, the main body 151 of the refrigerant distributor 150 separates the main flow path 15a and the sub flow path 25 in the third direction, and inlets that are through holes at both ends in the first direction. It has a wall portion 91 in which a portion 92a and an outlet portion 92b are formed. Further, the main body 151 of the refrigerant distributor 150 has a lid portion 94 that closes both ends of the tubular portion 90, respectively.
 筒状部90は、伝熱管70の配列方向に延びる中空の円筒形状に形成されている。ただし、筒状部90は、円筒形状に限定されるものではなく、筒状であればよく、例えば、直方体の箱形状に形成されてもよい。また、図19では、筒状部90は、冷媒流入管60と接続する第1筒状部90aと、伝熱管70と接続される第2筒状部90bとを有する。第1筒状部90a及び第2筒状部90bは、第1方向(Z軸方向)に対して垂直な断面において、半円弧状に形成されている。なお、筒状部90は、第1筒状部90aと第2筒状部90bとが分割された構造ではなく、第1筒状部90aと第2筒状部90bとが一体に軽形成された構造であってもよい。 The tubular portion 90 is formed in a hollow cylindrical shape extending in the arrangement direction of the heat transfer tubes 70. However, the tubular portion 90 is not limited to a cylindrical shape, and may be tubular, and may be formed in a rectangular parallelepiped box shape, for example. Further, in FIG. 19, the tubular portion 90 has a first tubular portion 90a connected to the refrigerant inflow pipe 60 and a second tubular portion 90b connected to the heat transfer pipe 70. The first tubular portion 90a and the second tubular portion 90b are formed in a semicircular shape in a cross section perpendicular to the first direction (Z-axis direction). The tubular portion 90 does not have a structure in which the first tubular portion 90a and the second tubular portion 90b are divided, but the first tubular portion 90a and the second tubular portion 90b are integrally lightly formed. It may have a structure.
 壁部91は、一方向に長い帯状の形状を有している。壁部91は、複数の伝熱管70の配列方向に延びる板状の部分であり、壁部91の長手方向は、複数の伝熱管70の配列方向となる第1方向(Z軸方向)である。また、壁部91の短手方向は、第2方向(X軸方向)であり、伝熱管70の管路の延伸方向である。また、壁部91の板厚方向は、伝熱管70の長軸方向である。壁部91は、第1方向(Z軸方向)及び第2方向(X軸方向)に延びる板面を形成する。 The wall portion 91 has a strip-like shape that is long in one direction. The wall portion 91 is a plate-shaped portion extending in the arrangement direction of the plurality of heat transfer tubes 70, and the longitudinal direction of the wall portion 91 is the first direction (Z-axis direction) which is the arrangement direction of the plurality of heat transfer tubes 70. .. Further, the lateral direction of the wall portion 91 is the second direction (X-axis direction), which is the extending direction of the pipe line of the heat transfer tube 70. Further, the plate thickness direction of the wall portion 91 is the major axis direction of the heat transfer tube 70. The wall portion 91 forms a plate surface extending in the first direction (Z-axis direction) and the second direction (X-axis direction).
 壁部91は、冷媒流入管60が接続される側の一方の端部91bに出口部92bを形成している。また、壁部91は、他方の端部91aに入口部92aを形成している。入口部92a及び出口部92bは、壁部91を壁部91の板厚方向に貫通する貫通孔である。本体151において、入口部92a及び出口部92bによって形成される流路の方向は、第3方向である。 The wall portion 91 forms an outlet portion 92b at one end 91b on the side to which the refrigerant inflow pipe 60 is connected. Further, the wall portion 91 forms an inlet portion 92a at the other end portion 91a. The inlet portion 92a and the outlet portion 92b are through holes that penetrate the wall portion 91 in the plate thickness direction of the wall portion 91. In the main body 151, the direction of the flow path formed by the inlet portion 92a and the outlet portion 92b is the third direction.
 壁部91には、更に複数の伝熱管70の一端がそれぞれ挿入される複数の挿入孔93が形成されている。複数の挿入孔93のそれぞれは、壁部91を壁部91の板厚方向に貫通している貫通孔である。また、複数の挿入孔93のそれぞれは、第1方向(Z軸方向)に延びる縁部91eから反対側の縁部91dに向かって切り欠かれた切欠き部でもある。 The wall portion 91 is further formed with a plurality of insertion holes 93 into which one ends of the plurality of heat transfer tubes 70 are inserted. Each of the plurality of insertion holes 93 is a through hole that penetrates the wall portion 91 in the plate thickness direction of the wall portion 91. Further, each of the plurality of insertion holes 93 is also a notch portion cut out from the edge portion 91e extending in the first direction (Z-axis direction) toward the opposite edge portion 91d.
 複数の挿入孔93は、壁部91の長手方向に沿って上下方向に並列している。複数の挿入孔93は、複数の伝熱管70のそれぞれと対応して互いに独立して設けられている。挿入孔93は、伝熱管70の外周形状と同様に扁平な開口形状を有している。挿入孔93の開口端は、ろう付けにより伝熱管70の外周面と全周にわたって接合されている。複数の伝熱管70が壁部91に接合されることによって、複数の伝熱管70は、第1流路である主流路15aと第2流路である副流路25とに連通するように壁部91に接続されている。 The plurality of insertion holes 93 are arranged in parallel in the vertical direction along the longitudinal direction of the wall portion 91. The plurality of insertion holes 93 are provided independently of each other corresponding to each of the plurality of heat transfer tubes 70. The insertion hole 93 has a flat opening shape similar to the outer peripheral shape of the heat transfer tube 70. The open end of the insertion hole 93 is joined to the outer peripheral surface of the heat transfer tube 70 over the entire circumference by brazing. By joining the plurality of heat transfer tubes 70 to the wall portion 91, the plurality of heat transfer tubes 70 communicate with the main flow path 15a, which is the first flow path, and the sub flow path 25, which is the second flow path. It is connected to the unit 91.
 蓋部94は、筒状部90の延伸方向の両端部を閉塞する。蓋部94は、筒状部90の延伸方向の両端部を閉塞するものであればよく、板状の部材でもよく、筒状部90の端部を覆い被さるような部材であってもよい。 The lid portion 94 closes both ends of the tubular portion 90 in the extending direction. The lid portion 94 may be a plate-shaped member as long as it closes both ends of the tubular portion 90 in the extending direction, or may be a member that covers the end portions of the tubular portion 90.
 筒状部90内の中空部95は、筒状部90と、筒状部90の両端を閉塞する蓋部94によって形成される。また、筒状部90内の中空部95は、図21に示すように、壁部91によって第1空間S1及び第2空間S2の2つの空間に隔てられている。第1空間S1と第2空間S2とは、入口部92a及び出口部92bを介して連通する。 The hollow portion 95 in the tubular portion 90 is formed by the tubular portion 90 and the lid portion 94 that closes both ends of the tubular portion 90. Further, as shown in FIG. 21, the hollow portion 95 in the tubular portion 90 is separated into two spaces, a first space S1 and a second space S2, by a wall portion 91. The first space S1 and the second space S2 communicate with each other via the inlet portion 92a and the outlet portion 92b.
 冷媒分配器150の本体151は、第1空間S1を主流路15aとして構成している。主流路15aは、本体151の冷媒流入管60が接続された側の一方の端部151aから、他方の端部151bに冷媒が流れる流路である。第1方向(Z軸方向)を上下方向とした場合に、主流路15aは、冷媒が上昇する流路である。第1流路である主流路15aは、第1方向に延伸するように形成されており、複数の伝熱管70と連通すると共に、第1方向の下端部15a2において、冷媒分配器150内に冷媒を流入させる冷媒流入管60と接続している。 The main body 151 of the refrigerant distributor 150 has a first space S1 as a main flow path 15a. The main flow path 15a is a flow path in which the refrigerant flows from one end 151a on the side to which the refrigerant inflow pipe 60 of the main body 151 is connected to the other end 151b. When the first direction (Z-axis direction) is the vertical direction, the main flow path 15a is a flow path through which the refrigerant rises. The main flow path 15a, which is the first flow path, is formed so as to extend in the first direction, communicates with a plurality of heat transfer tubes 70, and has a refrigerant in the refrigerant distributor 150 at the lower end portion 15a2 in the first direction. Is connected to the refrigerant inflow pipe 60.
 冷媒分配器150の本体151は、第2空間S2、入口部92a及び出口部92bを副流路25として構成している。副流路25は、他方の端部151bから本体151の冷媒流入管60が接続された側の一方の端部151aに冷媒が流れる流路である。第1方向(Z軸方向)を上下方向とした場合に、副流路25は、冷媒が降下する流路である。第2流路である副流路25は、第1方向に延伸し、入口部92a及び出口部92bの両端部が第1流路である主流路15aと接続するように形成されている。第2流路である副流路25は、第1流路である主流路15aに対して第3方向に位置するように形成されている。すなわち、主流路15a及び副流路25は、図1に示す室外送風機108あるいは室内送風機109によって形成される風の通風方向において、上流側と下流側とに位置するように形成されている。 The main body 151 of the refrigerant distributor 150 includes a second space S2, an inlet portion 92a, and an outlet portion 92b as a sub-flow path 25. The sub-flow path 25 is a flow path through which the refrigerant flows from the other end 151b to one end 151a on the side to which the refrigerant inflow pipe 60 of the main body 151 is connected. When the first direction (Z-axis direction) is the vertical direction, the sub-flow path 25 is a flow path through which the refrigerant drops. The sub-flow path 25, which is the second flow path, extends in the first direction and is formed so that both ends of the inlet portion 92a and the outlet portion 92b are connected to the main flow path 15a, which is the first flow path. The sub-flow path 25, which is the second flow path, is formed so as to be located in the third direction with respect to the main flow path 15a, which is the first flow path. That is, the main flow path 15a and the sub-flow path 25 are formed so as to be located on the upstream side and the downstream side in the ventilation direction of the wind formed by the outdoor blower 108 or the indoor blower 109 shown in FIG.
 冷媒分配器150の本体151は、冷媒が流れる第1流路である主流路15a及び第2流路である副流路25を内部に形成している。冷媒分配器150の本体151は、主流路15aと副流路25とによって冷媒が循環する流路を形成している。 The main body 151 of the refrigerant distributor 150 has a main flow path 15a, which is a first flow path through which the refrigerant flows, and a sub flow path 25, which is a second flow path, formed therein. The main body 151 of the refrigerant distributor 150 forms a flow path through which the refrigerant circulates by the main flow path 15a and the sub flow path 25.
 図22は、実施の形態5に係る熱交換器を構成する変形例の冷媒分配器の第1流路と第2流路との連通位置を概念的に示した断面図である。筒状部90は、図21に示すような円筒形状に限定されるものではない。筒状部90は、筒状であればよく、例えば、図22示すような半円筒形状に形成されてもよい。 FIG. 22 is a cross-sectional view conceptually showing the communication position between the first flow path and the second flow path of the refrigerant distributor of the modified example constituting the heat exchanger according to the fifth embodiment. The tubular portion 90 is not limited to the cylindrical shape as shown in FIG. 21. The tubular portion 90 may be tubular, and may be formed in a semi-cylindrical shape as shown in FIG. 22, for example.
 図23は、実施の形態5に係る熱交換器100を構成する冷媒分配器150内の冷媒の流れを示した概念図である。実施の形態1と同様に、主流路15aの上部に滞留した冷媒は、主流路15aの上端部15a1と連通した第2板状部材20に設けられた入口部92aへ流入する。この際、冷媒は、矢印OFで示すように、第1流路である主流路15aから第2流路である副流路25に向かって、第3方向に流れる。そして、副流路25の入口部92aから流入した冷媒は、矢印DFで示すように、第2板状部材20に形成された副流路25を重力方向に沿って下向きに流れる。 FIG. 23 is a conceptual diagram showing the flow of the refrigerant in the refrigerant distributor 150 constituting the heat exchanger 100 according to the fifth embodiment. Similar to the first embodiment, the refrigerant staying in the upper part of the main flow path 15a flows into the inlet portion 92a provided in the second plate-shaped member 20 communicating with the upper end portion 15a1 of the main flow path 15a. At this time, as shown by the arrow OF, the refrigerant flows in the third direction from the main flow path 15a, which is the first flow path, toward the sub-flow path 25, which is the second flow path. Then, as shown by the arrow DF, the refrigerant flowing in from the inlet portion 92a of the sub-flow path 25 flows downward along the sub-flow path 25 formed in the second plate-shaped member 20 in the direction of gravity.
 副流路25の下端に到達した冷媒は、主流路15aの下端部15a2と連通した出口部92bから主流路15aへ流出する。この際、冷媒は、矢印IFで示すように、第2流路である副流路25から第1流路である主流路15aに向かって、第3方向に流れる。そして、出口部92bから主流路15aへ流出した冷媒は、冷媒流入管60から本体151内に流入した冷媒と共に、主流路15aを鉛直に上昇し、各伝熱管70に分配される。 The refrigerant that has reached the lower end of the sub-flow path 25 flows out to the main flow path 15a from the outlet portion 92b that communicates with the lower end portion 15a2 of the main flow path 15a. At this time, as shown by the arrow IF, the refrigerant flows in the third direction from the sub-flow path 25, which is the second flow path, toward the main flow path 15a, which is the first flow path. Then, the refrigerant flowing out from the outlet portion 92b to the main flow path 15a vertically rises up the main flow path 15a together with the refrigerant flowing into the main body 151 from the refrigerant inflow pipe 60, and is distributed to each heat transfer pipe 70.
[熱交換器100の効果]
 冷媒分配器150は、筒状部90と、蓋部94と、第1流路である主流路15aと第2流路である副流路25とを第3方向に隔て、第1方向の両端部に貫通孔である入口部92aと出口部92bとが形成された壁部91と、を有する。そして、複数の伝熱管70は、第1流路である主流路15aと第2流路である副流路25とに連通するように壁部91に接続されている。熱交換器100は、本体151が円管のような筒状体であったとしても、冷媒を流通させる第2方向への冷媒分配器150の大型化を抑制することができ、構造成約の範囲内で熱交換器100を伝熱管70の管路の延びる第2方向へ大きくすることができる。そのため、熱交換器100は、伝熱管70の伝熱面積を広く確保しつつ、冷媒分配器150を伝熱管70の管路の延伸方向に大型化せずにコンパクトにすることができる。
[Effect of heat exchanger 100]
The refrigerant distributor 150 separates the tubular portion 90, the lid portion 94, the main flow path 15a which is the first flow path, and the sub flow path 25 which is the second flow path in the third direction, and both ends in the first direction. The portion has a wall portion 91 in which an inlet portion 92a and an outlet portion 92b, which are through holes, are formed. The plurality of heat transfer tubes 70 are connected to the wall portion 91 so as to communicate with the main flow path 15a which is the first flow path and the sub flow path 25 which is the second flow path. Even if the main body 151 of the heat exchanger 100 is a tubular body such as a circular pipe, it is possible to suppress an increase in the size of the refrigerant distributor 150 in the second direction in which the refrigerant flows, and the range of structural contracts can be concluded. Within, the heat exchanger 100 can be enlarged in the second direction in which the conduit of the heat transfer tube 70 extends. Therefore, the heat exchanger 100 can make the refrigerant distributor 150 compact without increasing the size in the extending direction of the pipe line of the heat transfer tube 70, while securing a wide heat transfer area of the heat transfer tube 70.
 なお、冷凍サイクル装置200は、実施の形態1~5のいずれかに係る熱交換器100を備えたものである。したがって、冷凍サイクル装置200は、実施の形態1~5のいずれかと同様の効果が得られる。 The refrigeration cycle device 200 includes the heat exchanger 100 according to any one of the first to fifth embodiments. Therefore, the refrigeration cycle device 200 can obtain the same effect as that of any one of the first to fifth embodiments.
 上記の各実施の形態1~5は、互いに組み合わせて実施することが可能である。また、以上の実施の形態に示した構成は、一例を示すものであり、別の公知の技術と組み合わせることも可能であるし、要旨を逸脱しない範囲で、構成の一部を省略、変更することも可能である。たとえば、実施の形態1~5に係る冷媒分配器150等は、本体151が鉛直方向に延びる縦置型でもよく、本体151が水平方向に延びる横置型であってもよい。また、実施の形態1~5に係る冷媒分配器150等は、本体151が鉛直方向に対して傾くような構成であってもよい。 Each of the above embodiments 1 to 5 can be implemented in combination with each other. Further, the configuration shown in the above embodiment is an example, and can be combined with another known technique, and a part of the configuration is omitted or changed without departing from the gist. It is also possible. For example, the refrigerant distributors 150 and the like according to the first to fifth embodiments may be of a vertical type in which the main body 151 extends in the vertical direction or a horizontal type in which the main body 151 extends in the horizontal direction. Further, the refrigerant distributor 150 and the like according to the first to fifth embodiments may have a configuration in which the main body 151 is tilted with respect to the vertical direction.
 10 第1板状部材、11 平板部、11a 平板部、11b 平板部、15 第1流路部、15a 主流路、15a1 上端部、15a2 下端部、15b 側壁、18 冷媒流入口、20 第2板状部材、24 閉塞部、25 副流路、25a 中央部、25a1 端部、25a2 端部、25b 入口部、25c 出口部、25c1 出口部、26 分配孔部、30 第3板状部材、31 挿入孔、34 平板部、40 第4板状部材、44 閉塞部、45 連通孔、46 第2分配孔部、50 第5板状部材、51 第3分配孔部、53 閉塞部、60 冷媒流入管、70 伝熱管、70a 第1側端部、70b 第2側端部、70c 平坦面、70d 平坦面、71 隙間、72 冷媒通路、75 伝熱フィン、90 筒状部、90a 第1筒状部、90b 第2筒状部、91 壁部、91a 端部、91b 端部、91d 縁部、91e 縁部、92a 入口部、92b 出口部、93 挿入孔、94 蓋部、95 中空部、100 熱交換器、101 圧縮機、102 流路切替装置、103 室内熱交換器、104 減圧装置、105 室外熱交換器、106 室外機、107 室内機、108 室外送風機、109 室内送風機、110 冷媒回路、111 延長配管、112 延長配管、115 流路部、150 冷媒分配器、151 本体、151a 端部、151b 端部、200 冷凍サイクル装置。 10 1st plate-shaped member, 11 flat plate, 11a flat plate, 11b flat plate, 15 1st flow path, 15a main flow path, 15a1 upper end, 15a2 lower end, 15b side wall, 18 refrigerant inlet, 20 2nd plate Shaped member, 24 closed part, 25 auxiliary flow path, 25a central part, 25a1 end part, 25a2 end part, 25b inlet part, 25c outlet part, 25c1 outlet part, 26 distribution hole part, 30 third plate-shaped member, 31 insertion Hole, 34 flat plate part, 40 fourth plate-shaped member, 44 closed part, 45 communication hole, 46 second distribution hole part, 50 fifth plate-shaped member, 51 third distribution hole part, 53 closed part, 60 refrigerant inflow pipe , 70 heat transfer tube, 70a first side end, 70b second side end, 70c flat surface, 70d flat surface, 71 gap, 72 refrigerant passage, 75 heat transfer fin, 90 tubular part, 90a first tubular part , 90b 2nd tubular part, 91 wall part, 91a end part, 91b end part, 91d edge part, 91e edge part, 92a inlet part, 92b outlet part, 93 insertion hole, 94 lid part, 95 hollow part, 100 heat Exchanger, 101 compressor, 102 flow path switching device, 103 indoor heat exchanger, 104 decompression device, 105 outdoor heat exchanger, 106 outdoor unit, 107 indoor unit, 108 outdoor blower, 109 indoor blower, 110 refrigerant circuit, 111 Extension pipe, 112 extension pipe, 115 flow path, 150 refrigerant distributor, 151 main body, 151a end, 151b end, 200 refrigeration cycle device.

Claims (10)

  1.  第1方向に互いに間隔をあけて配置された複数の伝熱管であって、前記第1方向と交差する第2方向に冷媒を流通させる前記複数の伝熱管と、
     前記第1方向に延伸し、前記複数の伝熱管のそれぞれの一端に接続されて前記複数の伝熱管に前記冷媒を分配する冷媒分配器と、
    を備え、
     前記冷媒分配器は、
     前記冷媒が流れる第1流路及び第2流路が内部に形成されており、
     前記第1流路は、
     前記第1方向に延伸するように形成されており、前記複数の伝熱管と連通すると共に、前記冷媒分配器の内部に前記冷媒を流入させる流入管と接続しており、
     前記第2流路は、
     前記第1方向に延伸し、両端部が前記第1流路と接続するように形成されており、
     前記第1方向及び前記第2方向に平行な面に交差する方向を第3方向と定義した場合に、前記第1流路に対して前記第3方向に位置するように形成されている熱交換器。
    A plurality of heat transfer tubes arranged at intervals in the first direction, and the plurality of heat transfer tubes for flowing a refrigerant in a second direction intersecting with the first direction.
    A refrigerant distributor that extends in the first direction and is connected to one end of each of the plurality of heat transfer tubes to distribute the refrigerant to the plurality of heat transfer tubes.
    With
    The refrigerant distributor is
    The first flow path and the second flow path through which the refrigerant flows are formed inside.
    The first flow path is
    It is formed so as to extend in the first direction, communicates with the plurality of heat transfer pipes, and is connected to an inflow pipe for flowing the refrigerant into the inside of the refrigerant distributor.
    The second flow path is
    It is formed so as to extend in the first direction and connect both ends to the first flow path.
    Heat exchange formed so as to be located in the third direction with respect to the first flow path when the direction intersecting the first direction and the plane parallel to the second direction is defined as the third direction. vessel.
  2.  前記冷媒分配器は、
     前記第1流路が形成された第1板状部材と、
     前記複数の伝熱管と前記第1流路との間に位置する貫通孔である分配孔部と、前記第2流路とが形成された第2板状部材と、
     前記複数の伝熱管が挿入される貫通孔である挿入孔が形成された第3板状部材と、
    を有し、
     前記第1板状部材と、前記第2板状部材と、前記第3板状部材とが積層されており、
     前記第1板状部材と、前記第2板状部材と、前記第3板状部材との積層方向において、前記第1流路と前記両端部とが重なり、前記第1流路と前記分配孔部と前記挿入孔とが重なるように形成されている請求項1に記載の熱交換器。
    The refrigerant distributor is
    The first plate-shaped member on which the first flow path is formed and
    A distribution hole portion which is a through hole located between the plurality of heat transfer tubes and the first flow path, and a second plate-shaped member in which the second flow path is formed.
    A third plate-shaped member having an insertion hole, which is a through hole into which the plurality of heat transfer tubes are inserted,
    Have,
    The first plate-shaped member, the second plate-shaped member, and the third plate-shaped member are laminated.
    In the stacking direction of the first plate-shaped member, the second plate-shaped member, and the third plate-shaped member, the first flow path and both ends thereof overlap, and the first flow path and the distribution hole The heat exchanger according to claim 1, wherein the portion and the insertion hole are formed so as to overlap each other.
  3.  前記分配孔部は、
     前記第1方向に沿って複数形成されている請求項2に記載の熱交換器。
    The distribution hole is
    The heat exchanger according to claim 2, wherein a plurality of heat exchangers are formed along the first direction.
  4.  前記第2流路は、
     前記第3方向において、前記分配孔部の両側にそれぞれ形成されている請求項2又は3に記載の熱交換器。
    The second flow path is
    The heat exchanger according to claim 2 or 3, which is formed on both sides of the distribution hole in the third direction, respectively.
  5.  前記冷媒分配器は、
     前記第1板状部材と前記第2板状部材との間に第4板状部材を有し、
     前記第2板状部材と前記第3板状部材との間に第5板状部材を有し、
     前記第4板状部材には、
     前記第1流路と前記両端部との間に位置する貫通孔である連通孔と、前記第1流路と前記分配孔部との間に位置する貫通孔である第2分配孔部とが形成されており、
     前記第5板状部材には、
     前記分配孔部と前記挿入孔との間に位置する貫通孔である第3分配孔部が形成されている請求項2~4のいずれか1項に記載の熱交換器。
    The refrigerant distributor is
    A fourth plate-shaped member is provided between the first plate-shaped member and the second plate-shaped member.
    A fifth plate-shaped member is provided between the second plate-shaped member and the third plate-shaped member.
    The fourth plate-shaped member has
    A communication hole, which is a through hole located between the first flow path and both ends thereof, and a second distribution hole portion, which is a through hole located between the first flow path and the distribution hole portion, are formed. Has been formed and
    The fifth plate-shaped member has
    The heat exchanger according to any one of claims 2 to 4, wherein a third distribution hole portion, which is a through hole located between the distribution hole portion and the insertion hole, is formed.
  6.  前記両端部は、
     前記第1流路から冷媒が流入する入口部と、
     前記第1流路に冷媒を流出する出口部と、
    から構成されており、
     前記入口部及び前記出口部は前記第3方向に延びるように形成されている請求項2~5のいずれか1項に記載の熱交換器。
    Both ends
    The inlet where the refrigerant flows in from the first flow path and
    An outlet portion that allows the refrigerant to flow out to the first flow path, and an outlet portion.
    Consists of
    The heat exchanger according to any one of claims 2 to 5, wherein the inlet portion and the outlet portion are formed so as to extend in the third direction.
  7.  前記両端部は、
     前記第1流路から前記冷媒が流入する入口部と、
     前記第1流路に前記冷媒を流出する出口部と、
    から構成されており、
     前記出口部は、
     前記出口部から流出される前記冷媒の流れる方向が、前記流入管から流出される前記冷媒の流れる方向のベクトル成分を有するように前記第1方向及び前記第3方向に対して傾いて形成されている請求項2~5のいずれか1項に記載の熱交換器。
    Both ends
    An inlet portion into which the refrigerant flows from the first flow path and
    An outlet portion for flowing out the refrigerant to the first flow path and
    Consists of
    The exit part
    The flow direction of the refrigerant flowing out from the outlet portion is formed to be inclined with respect to the first direction and the third direction so as to have a vector component of the flow direction of the refrigerant flowing out from the inflow pipe. The heat exchanger according to any one of claims 2 to 5.
  8.  前記第1流路は、
     前記流入管と接続した側の一方の端部から、他方の端部に向かって流路断面積が小さくなるように形成されている請求項1~7のいずれか1項に記載の熱交換器。
    The first flow path is
    The heat exchanger according to any one of claims 1 to 7, which is formed so that the cross-sectional area of the flow path decreases from one end on the side connected to the inflow pipe toward the other end. ..
  9.  前記冷媒分配器は、
     前記第1方向に延びる筒状部と、
     前記筒状部の両端をそれぞれ閉塞する蓋部と、
     前記筒状部の中空部において、前記第1流路と前記第2流路とを前記第3方向に隔て、前記第1方向の両端部に貫通孔である入口部と出口部とが形成された壁部と、
    を有し、
     前記複数の伝熱管は、
     前記第1流路と前記第2流路とに連通するように前記壁部に接続されている請求項1に記載の熱交換器。
    The refrigerant distributor is
    The tubular portion extending in the first direction and
    A lid that closes both ends of the tubular portion and
    In the hollow portion of the tubular portion, the first flow path and the second flow path are separated in the third direction, and inlet portions and outlet portions, which are through holes, are formed at both ends of the first direction. With the wall
    Have,
    The plurality of heat transfer tubes
    The heat exchanger according to claim 1, which is connected to the wall portion so as to communicate with the first flow path and the second flow path.
  10.  請求項1~9のいずれか1項に記載の熱交換器、を備えた冷凍サイクル装置。 A refrigeration cycle apparatus including the heat exchanger according to any one of claims 1 to 9.
PCT/JP2020/002321 2020-01-23 2020-01-23 Heat exchanger and refrigeration cycle apparatus WO2021149223A1 (en)

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US11506434B2 (en) * 2016-12-07 2022-11-22 Johnson Controls Tyco IP Holdings LLP Adjustable inlet header for heat exchanger of an HVAC system

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JPWO2021149223A1 (en) 2021-07-29
TW202129218A (en) 2021-08-01
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EP4095476A1 (en) 2022-11-30
JP7278430B2 (en) 2023-05-19
EP4095476A4 (en) 2023-01-11

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