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WO2025062640A1 - Heat exchanger and refrigeration cycle device - Google Patents

Heat exchanger and refrigeration cycle device Download PDF

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Publication number
WO2025062640A1
WO2025062640A1 PCT/JP2023/034538 JP2023034538W WO2025062640A1 WO 2025062640 A1 WO2025062640 A1 WO 2025062640A1 JP 2023034538 W JP2023034538 W JP 2023034538W WO 2025062640 A1 WO2025062640 A1 WO 2025062640A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat transfer
transfer tube
refrigerant
auxiliary
refrigerant flow
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
PCT/JP2023/034538
Other languages
French (fr)
Japanese (ja)
Inventor
克明 與座
諭 太田
崇史 畠田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carrier Japan Corp
Original Assignee
Carrier Japan Corp
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 Carrier Japan Corp filed Critical Carrier Japan Corp
Priority to PCT/JP2023/034538 priority Critical patent/WO2025062640A1/en
Publication of WO2025062640A1 publication Critical patent/WO2025062640A1/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • 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
    • F28D1/047Heat-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 bent, e.g. in a serpentine or zig-zag
    • 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
    • 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
    • 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
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide 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
    • F28F9/26Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators

Definitions

  • An embodiment of the present invention relates to a heat exchanger and a refrigeration cycle device.
  • Heat exchangers are used in air conditioning equipment, refrigeration equipment, and the like.
  • a heat exchanger may have a main heat exchange section and an auxiliary heat exchange section.
  • the refrigerant may flow through the auxiliary heat exchange section and then the main heat exchange section.
  • the auxiliary heat exchange section has multiple refrigerant flow paths, there is a possibility that the heat exchange performance in the main heat exchange section may be reduced due to the effects of factors such as the flow rate difference and pressure loss of the refrigerant in the multiple flow paths.
  • the problem that this invention aims to solve is to provide a heat exchanger and a refrigeration cycle device that can suppress the deterioration of heat exchange performance in the main heat exchange section.
  • the heat exchanger of the embodiment has a main heat exchange section having multiple main refrigerant flow paths through which a refrigerant flows, and an auxiliary heat exchange section through which the refrigerant flows between the main heat exchange section.
  • the auxiliary heat exchange section has multiple heat transfer tubes having auxiliary refrigerant flow paths through which the refrigerant flows, and a header connected to the heat transfer tubes.
  • the header has a first plate material to which a refrigerant flow path that guides the refrigerant is connected, one or more intermediate plate materials in which a spatial flow path into which the refrigerant is introduced is formed, and a second plate material to which the heat transfer tubes are connected.
  • the spatial flow path has a junction section that joins the multiple auxiliary refrigerant flow paths.
  • FIG. 1 is a schematic configuration diagram of a refrigeration cycle device according to an embodiment
  • FIG. 2 is a configuration diagram of a heat exchanger according to an embodiment.
  • FIG. 2 is an exploded perspective view showing the internal structure of the auxiliary heat exchange unit in the first embodiment.
  • FIG. 11 is an exploded perspective view showing the structure of an auxiliary heat exchange section in a second embodiment.
  • FIG. 13 is a configuration diagram showing a structure of an auxiliary heat exchanger in a third embodiment.
  • FIG. 13 is an exploded perspective view showing the structure of an auxiliary heat exchange section in a third embodiment.
  • FIG. 1 is a schematic diagram of a refrigeration cycle device according to an embodiment.
  • the refrigeration cycle apparatus 1 includes a compressor 2, a four-way valve 3, an outdoor heat exchanger (heat exchanger) 4, an expansion device 5, and an indoor heat exchanger (heat exchanger) 6.
  • the components of the refrigeration cycle apparatus 1 are connected by piping 7.
  • the flow direction of the refrigerant (heat medium) during cooling operation is indicated by solid arrows, and the flow direction of the refrigerant during heating operation is indicated by dashed arrows.
  • the compressor 2 comprises a compressor body 2A and an accumulator 2B.
  • the compressor body 2A compresses the low-pressure gas refrigerant taken in to produce high-temperature, high-pressure gas refrigerant.
  • the accumulator 2B separates the gas-liquid two-phase refrigerant and supplies the gas refrigerant to the compressor body 2A.
  • the four-way valve 3 reverses the flow direction of the refrigerant to switch between cooling and heating operation.
  • the refrigerant flows through the compressor 2, four-way valve 3, outdoor heat exchanger 4, expansion device 5, and indoor heat exchanger 6 in that order.
  • the outdoor heat exchanger 4 functions as a condenser.
  • the indoor heat exchanger 6 functions as an evaporator.
  • the refrigerant flows through the compressor 2, four-way valve 3, indoor heat exchanger 6, expansion device 5, and outdoor heat exchanger 4 in that order.
  • the indoor heat exchanger 6 functions as a condenser.
  • the outdoor heat exchanger 4 functions as an evaporator.
  • the condenser converts the high-temperature, high-pressure gas refrigerant discharged from the compressor 2 into high-pressure liquid refrigerant by condensing it through heat transfer to the outside air.
  • the expansion device 5 reduces the pressure of the high-pressure liquid refrigerant sent from the condenser, converting it into a low-temperature, low-pressure two-phase gas-liquid refrigerant.
  • the evaporator converts the low-temperature, low-pressure two-phase gas-liquid refrigerant sent from the expansion device 5 into a low-pressure gas refrigerant by absorbing heat from the outside air and vaporizing it.
  • the refrigerant which is the working fluid, circulates while changing phase between gaseous refrigerant and liquid refrigerant.
  • the refrigerant releases heat during the phase change from gaseous refrigerant to liquid refrigerant.
  • the refrigerant absorbs heat during the phase change from liquid refrigerant to gaseous refrigerant.
  • the refrigeration cycle device 1 uses the heat release or absorption of the refrigerant to perform heating, cooling, defrosting, etc.
  • FIG. 2 is a diagram showing the configuration of a heat exchanger according to an embodiment.
  • the heat exchanger according to the embodiment is used as one or both of the outdoor heat exchanger 4 and the indoor heat exchanger 6 (see FIG. 1) of the refrigeration cycle device 1.
  • the heat exchanger according to the embodiment is used as the outdoor heat exchanger 4 (see FIG. 1) of the refrigeration cycle device 1.
  • the outdoor heat exchanger 4 will be simply referred to as "heat exchanger 4.”
  • the heat exchanger 4 includes a main heat exchange section 100, an auxiliary heat exchange section 200, and a piping unit 70 connecting the main heat exchange section 100 and the auxiliary heat exchange section 200.
  • the main heat exchange section 100 has a plurality of first refrigerant flow paths 101 (main refrigerant flow paths) through which the refrigerant flows, and a plurality of second refrigerant flow paths 102 (main refrigerant flow paths).
  • the piping unit 70 has distributors 71 and 72.
  • the first refrigerant flow path 101 is connected to the first distributor 71.
  • the second refrigerant flow path 102 is connected to the second distributor 72.
  • the two distributors 71 and 72 are connected to the auxiliary heat exchange section 200.
  • FIG. 3 is an exploded perspective view showing the internal structure of the auxiliary heat exchange section 200.
  • the X direction, Y direction, and Z direction are defined as follows:
  • the Z direction is the longitudinal direction of the first header.
  • the Z direction is the height direction.
  • the Z direction is the vertical direction.
  • +Z is upward.
  • -Z is downward.
  • the X direction is the central axis direction (extension direction) of the heat transfer tube.
  • the X direction is perpendicular to the Z direction.
  • the X direction is the horizontal direction.
  • +X is the direction from the heat transfer tube toward the first header.
  • -X is the opposite direction to +X.
  • the Y direction is perpendicular to the X and Z directions.
  • the Y direction is the left-right direction.
  • +Y is one direction of the Y direction.
  • -Y is the other direction of the Y direction.
  • the Y direction is the horizontal direction.
  • the Y direction is the width direction of the first header.
  • the Y direction is the first direction.
  • the X direction is the second direction.
  • the Z direction is the third direction.
  • the YZ plane is the plane formed by the Y and Z directions.
  • the auxiliary heat exchange section 200 has a first header 10, a plurality of heat transfer tubes 30 (heat transfer section), and a second header (not shown).
  • a refrigerant can flow between the auxiliary heat exchange section 200 and the main heat exchange section 100 (see FIG. 2).
  • the first header 10 is connected to the +X side end (one end) of the heat transfer tubes 30.
  • the second header is connected to the -X side end (one end) of the heat transfer tubes 30.
  • the first header 10 is formed in a flat plate shape parallel to the YZ plane. For example, when viewed from the X direction, the first header 10 is rectangular. The shape of the first header 10 is a rectangle whose longitudinal direction is along the Z direction.
  • the first header 10 is formed from a material with high thermal conductivity and low specific gravity. For example, the first header 10 is formed from a metal such as aluminum or an aluminum alloy.
  • the first header 10 (header) comprises a first plate material 11, a first intermediate plate material 12, a second intermediate plate material 13, a third intermediate plate material 14, and a second plate material 15.
  • the first plate material 11, the first intermediate plate material 12, the second intermediate plate material 13, the third intermediate plate material 14, and the second plate material 15 are stacked in this order.
  • the first intermediate plate 12 is placed on the -X side surface of the first plate 11.
  • the second intermediate plate 13 is placed on the -X side surface of the first intermediate plate 12.
  • the third intermediate plate 14 is placed on the -X side surface of the second intermediate plate 13.
  • the second plate 15 is placed on the -X side surface of the third intermediate plate 14.
  • the first plate 11, the first intermediate plate 12, the second intermediate plate 13, the third intermediate plate 14 and the second plate 15 are generally rectangular when viewed from the thickness direction (X direction).
  • the first intermediate plate 12, the second intermediate plate 13 and the third intermediate plate 14 can be collectively referred to as "intermediate plate materials 12 to 14".
  • the intermediate plate materials 12 to 14 are examples of "intermediate plate materials”.
  • the -Y side of the first header 10 is the first side 10a.
  • the +Y side of the first header 10 is the second side 10b.
  • the first plate material 11 is formed in a flat plate shape.
  • a first connection port 50 and a second connection port 51 are formed in the first plate material 11.
  • a first refrigerant port 52 (refrigerant flow pipe) is connected to the first connection port 50.
  • a second refrigerant port 53 (refrigerant flow pipe) is connected to the second connection port 51.
  • the first refrigerant port 52 and the second refrigerant port 53 are attached to the first plate material 11.
  • the first refrigerant port 52 and the second refrigerant port 53 have flow paths through which the refrigerant flows. For example, the first refrigerant port 52 and the second refrigerant port 53 are perpendicular to the first plate material 11.
  • a spatial flow path 16 is formed in the intermediate plate members 12 to 14.
  • the spatial flow path 16 has communicating spaces 17, 18 formed in the first intermediate plate member 12, connecting spaces 21 to 24 formed in the second intermediate plate member 13, and separate chambers 26 to 29 formed in the third intermediate plate member 14.
  • the communicating spaces 17, 18 formed in the first intermediate plate material 12 penetrate the first intermediate plate material 12 in the thickness direction.
  • the communicating spaces 17, 18 are the first communicating space 17 (first junction, junction) and the second communicating space 18 (second junction, junction).
  • the communicating spaces 17, 18 are elliptical when viewed from the X direction.
  • the major axis direction of the communicating spaces 17, 18 is parallel to the Z direction.
  • the major axes of the communicating spaces 17, 18 are the same as each other.
  • the minor axes of the communicating spaces 17, 18 are the same as each other.
  • the first communication space 17 is located on the -Y side of the center of the first intermediate plate 12 in the Y direction.
  • the first communication space 17 is formed at a position closer to the first side portion 10a (one side portion) than the center of the first header 10 in the Y direction (width direction).
  • the center of the first communication space 17 is located lower than the center of the first intermediate plate 12 in the Z direction.
  • the center of the first communication space 17 is located in a position that overlaps with the opening of the first refrigerant port 52.
  • the second communication space 18 is located on the +Y side of the center in the Y direction of the first intermediate plate 12.
  • the second communication space 18 is formed at a position closer to the second side 10b (the other side) than the center in the Y direction (width direction) of the first header 10.
  • the second communication space 18 is located on the +Y side compared to the first communication space 17.
  • the center of the second communication space 18 is located higher than the center of the first communication space 17.
  • the center of the second communication space 18 is located higher than the center in the Z direction of the first intermediate plate 12.
  • the center of the second communication space 18 is located in a position that overlaps with the opening of the second refrigerant port 53.
  • the contact spaces 21 to 24 formed in the second intermediate plate 13 penetrate the second intermediate plate 13 in the thickness direction.
  • the contact spaces 21 to 24 are the first contact space 21, the second contact space 22, the third contact space 23, and the fourth contact space 24.
  • the contact spaces 21 to 24 are formed in a circular shape when viewed from the X direction. The diameters of the contact spaces 21 to 24 are the same.
  • the first communication space 21 and the third communication space 23 are located on the -Y side of the center in the Y direction of the second intermediate plate material 13.
  • the first communication space 21 and the third communication space 23 are separated in the Z direction.
  • the third communication space 23 is located on the +Z side of the first communication space 21.
  • the first communication space 21 is located in communication with the first communication space 17.
  • the first communication space 21 is located so as to overlap the lower end of the first communication space 17.
  • the third communication space 23 is located in communication with the first communication space 17.
  • the third communication space 23 is located so as to overlap the upper end of the first communication space 17.
  • the second communication space 22 and the fourth communication space 24 are located on the +Y side of the center in the Y direction of the second intermediate plate material 13.
  • the second communication space 22 and the fourth communication space 24 are separated in the Z direction.
  • the fourth communication space 24 is located on the +Z side of the second communication space 22.
  • the second communication space 22 is located in communication with the second communication space 18.
  • the second communication space 22 is located in a position overlapping the lower end of the second communication space 18.
  • the fourth communication space 24 is located in communication with the second communication space 18.
  • the fourth communication space 24 is located in a position overlapping the upper end of the second communication space 18.
  • the sub-chambers 26 to 29 formed in the third intermediate plate 14 penetrate the third intermediate plate 14 in the thickness direction.
  • the sub-chambers 26 to 29 are a first sub-chamber 26, a second sub-chamber 27, a third sub-chamber 28, and a fourth sub-chamber 29.
  • the sub-chambers 26 to 29 are elliptical when viewed from the X direction.
  • the major axis direction of the sub-chambers 26 to 29 is parallel to the Y direction.
  • the major axes of the sub-chambers 26 to 29 are the same as each other.
  • the minor axes of the sub-chambers 26 to 29 are the same as each other.
  • the compartments 26 to 29 are spaced apart in the Z direction.
  • the second compartment 27 is on the +Z side of the first compartment 26.
  • the third compartment 28 is on the +Z side of the second compartment 27.
  • the fourth compartment 29 is on the +Z side of the third compartment 28.
  • the first compartment 26 is positioned so as to overlap the first communication space 21.
  • the -Y side end of the first compartment 26 is positioned so as to overlap the first communication space 21.
  • the second compartment 27 is positioned so as to overlap the second communication space 22.
  • the +Y side end of the second compartment 27 is positioned so as to overlap the second communication space 22.
  • the third compartment 28 is positioned so as to overlap the third communication space 23.
  • the -Y side end of the third compartment 28 is positioned so as to overlap the third communication space 23.
  • the fourth compartment 29 is positioned so as to overlap the fourth communication space 24.
  • the +Y side end of the fourth compartment 29 is positioned so as to overlap the fourth communication space 24.
  • the second plate material 15 has a plurality of outlets 41 to 44 formed therein.
  • the outlets 41 to 44 penetrate the second plate material 15 in the thickness direction.
  • the outlets 41 to 44 are a first outlet 41, a second outlet 42, a third outlet 43, and a fourth outlet 44.
  • the outlets 41 to 44 are slit-shaped and extend along the Y direction.
  • the outlets 41 to 44 are spaced apart in the Z direction.
  • the second outlet 42 is on the +Z side of the first outlet 41.
  • the third outlet 43 is on the +Z side of the second outlet 42.
  • the fourth outlet 44 is on the +Z side of the third outlet 43.
  • the first outlet 41 is positioned so as to overlap the first compartment 26.
  • the second outlet 42 is positioned so as to overlap the second compartment 27.
  • the third outlet 43 is positioned so as to overlap the third compartment 28.
  • the fourth outlet 44 is positioned so as to overlap the fourth compartment 29.
  • the heat transfer tube 30 is a flat tube formed in a flat shape.
  • the heat transfer tube 30 has a larger outer dimension (outer diameter) in the Y direction than the outer dimension (outer diameter) in the Z direction.
  • the outer diameter of the heat transfer tube 30 in the Y direction is at least twice the outer diameter in the Z direction.
  • the shape of the cross section (YZ cross section) of the heat transfer tube 30 perpendicular to the length direction is approximately oval or approximately elliptical.
  • refrigerant flow paths 31 are formed inside the heat transfer tube 30. Refrigerant flows through the refrigerant flow paths 31.
  • multiple refrigerant flow paths 31 arranged in the Y direction (width direction) may be formed by one or more partition walls.
  • the heat transfer tube 30 is formed of a material with high thermal conductivity and low specific gravity.
  • the heat transfer tube 30 is formed of a metal such as aluminum or an aluminum alloy.
  • the multiple heat transfer tubes 30 include a first heat transfer tube 32, a second heat transfer tube 33, a third heat transfer tube 34, and a fourth heat transfer tube 35.
  • the first heat transfer tube 32 is connected to a first outlet 41.
  • the second heat transfer tube 33 is connected to a second outlet 42.
  • the third heat transfer tube 34 is connected to a third outlet 43.
  • the fourth heat transfer tube 35 is connected to a fourth outlet 44.
  • the first heat transfer tube 32, the second heat transfer tube 33, the third heat transfer tube 34, and the fourth heat transfer tube 35 are located at different heights.
  • the first heat transfer tube 32, the second heat transfer tube 33, the third heat transfer tube 34, and the fourth heat transfer tube 35 are arranged at intervals in the Z direction.
  • the second heat transfer tube 33 is located adjacent to the first heat transfer tube 32 on the +Z side.
  • the third heat transfer tube 34 is located adjacent to the second heat transfer tube 33 on the +Z side.
  • the fourth heat transfer tube 35 is located adjacent to the third heat transfer tube 34 on the +Z side.
  • the first heat transfer tube 32 can circulate the refrigerant between the first compartment 26.
  • the second heat transfer tube 33 can circulate the refrigerant between the second compartment 27.
  • the third heat transfer tube 34 can circulate the refrigerant between the third compartment 28.
  • the fourth heat transfer tube 35 can circulate the refrigerant between the fourth compartment 29.
  • an outside air flow path is formed along the Y direction.
  • the heat exchanger 4 circulates outside air (external gas) through the outside air flow path by a blower fan (not shown) or the like.
  • F indicates the flow direction of the outside air.
  • the heat exchanger 4 can exchange heat between the outside air flowing through the outside air flow path and the refrigerant flowing through the refrigerant flow path 31. The heat exchange is performed indirectly via the heat transfer tubes 30.
  • Fig. 3 shows the flow of the refrigerant when the heat exchanger 4 functions as an evaporator.
  • the refrigerant that flows into the first header 10 of the auxiliary heat exchange section 200 through the second refrigerant port 53 is introduced into the second communication space 18.
  • the refrigerant that flows into the second communication space 18 is divided into the -Z side and the +Z side.
  • the refrigerant divided into the -Z side flows into the second compartment 27 through the second communication space 22.
  • the refrigerant flows from the second compartment 27 to the second heat transfer tube 33.
  • the refrigerant divided into the +Z side flows into the fourth compartment 29 through the fourth communication space 24.
  • the refrigerant flows from the fourth compartment 29 to the fourth heat transfer tube 35.
  • the refrigerant that flows through the second heat transfer tube 33 and the fourth heat transfer tube 35 circulates within the auxiliary heat exchange section 200, then turns around, for example, through the second header (not shown), and flows into the first heat transfer tube 32 and the third heat transfer tube 34.
  • the refrigerant flows through the first heat transfer tube 32 and the third heat transfer tube 34 and into the spatial flow path 16 of the first header 10.
  • the refrigerant from the first heat transfer tube 32 (refrigerant flow path 31) is introduced into the first communication space 17 through the first compartment 26 and the first communication space 21.
  • the refrigerant from the third heat transfer tube 34 (refrigerant flow path 31) is introduced into the first communication space 17 through the third compartment 28 and the third communication space 23.
  • the refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see Figure 2).
  • the refrigerant flow path 31, the first sub-chamber 26, and the first communication space 21 of the first heat transfer tube 32 form a first auxiliary refrigerant flow path.
  • the refrigerant flow path 31, the third sub-chamber 28, and the third communication space 23 of the third heat transfer tube 34 form a third auxiliary refrigerant flow path.
  • the first communication space 17 joins the two auxiliary refrigerant flow paths (the first auxiliary refrigerant flow path and the third auxiliary refrigerant flow path).
  • the first communication space 17 is a junction that joins the refrigerant flow path 31 of the first heat transfer tube 32 and the refrigerant flow path 31 of the third heat transfer tube 34.
  • the refrigerant flows in the opposite direction to when the heat exchanger 4 functions as an evaporator (see FIG. 3).
  • the first side 10a of the first header 10 is located upstream of the flow direction F of the outside air.
  • the refrigerant flow path 31, the second sub-chamber 27, and the second communication space 22 of the second heat transfer tube 33 form a second auxiliary refrigerant flow path.
  • the refrigerant flow path 31, the fourth sub-chamber 29, and the fourth communication space 24 of the fourth heat transfer tube 35 form a fourth auxiliary refrigerant flow path.
  • the second communication space 18 merges the two auxiliary refrigerant flow paths (the second auxiliary refrigerant flow path and the fourth auxiliary refrigerant flow path).
  • a first communication space 17 (confluence portion) is formed in the first header 10, which merges the refrigerant flow path of the first heat transfer tube 32 and the refrigerant flow path of the third heat transfer tube 34 when used as an evaporator.
  • a second communication space 18 (confluence portion) is formed in the first header 10, which merges the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the fourth heat transfer tube 35 when used as a condenser. This allows the refrigerant flow path structure to be simplified.
  • the heat exchanger 4 requires less piping than when the junction is located outside the header. This reduces the number of parts. This allows the heat exchanger 4 to be made more compact (smaller).
  • the first communication space 17 (confluence portion) is formed in a position close to the first side portion 10a on the upstream side of the outside air flow direction F in the first header 10. Therefore, when the heat exchanger 4 is used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, a large amount of refrigerant can be flowed to a position close to the upstream side of the heat transfer tube 30 in the flow direction F. Since the temperature difference between the outside air and the refrigerant is large on the upstream side of the outside air flow direction F, the amount of heat exchange can be increased. Therefore, the heat exchange performance in the auxiliary heat exchange section 200 can be improved.
  • Second Embodiment 4 is an exploded perspective view showing the structure of the auxiliary heat exchange section 300 in the heat exchanger according to the second embodiment.
  • the same reference numerals are used for the common components with the heat exchanger according to the first embodiment (see FIG. 3), and the description thereof will be omitted.
  • the auxiliary heat exchange section 300 has a first header 310 and a plurality of heat transfer tubes 30 .
  • the first header 310 includes a first plate material 11, a first intermediate plate material 112, a second intermediate plate material 113, a third intermediate plate material 114, and a second plate material 15.
  • the first plate material 11, the first intermediate plate material 112, the second intermediate plate material 113, the third intermediate plate material 114, and the second plate material 15 are stacked in this order.
  • a spatial flow path 116 is formed in the intermediate plate members 112 to 114.
  • the spatial flow path 116 has a communication space 117 and a connecting space 118 formed in the first intermediate plate member 112, separate chambers 121, 122 and a connecting space 123 formed in the second intermediate plate member 113, and separate chambers 126, 127 and a connecting space 128 formed in the third intermediate plate member 114.
  • the contact space 117 formed in the first intermediate plate material 112 is formed in a circular shape.
  • the contact space 117 is located on the +Y side of the center of the first intermediate plate material 112 in the Y direction.
  • the communication space 118 is located on the -Y side of the center in the Y direction of the first intermediate plate material 112.
  • the communication space 118 is located on the -Y side compared to the contact space 117.
  • the communication space 118 has an elliptical shape.
  • the long diameter direction of the communication space 118 is parallel to the Z direction.
  • the compartments 121, 122 formed in the second intermediate plate 113 are the first compartment 121 and the second compartment 122.
  • the compartments 121, 122 are elliptical in shape.
  • the major axis direction of the compartments 121, 122 is parallel to the Y direction.
  • the compartments 121, 122 are formed at an interval in the Z direction.
  • the second compartment 122 is on the +Z side of the first compartment 121.
  • the compartments 121, 122 are located in a position that communicates with the communication space 118.
  • the communication space 123 is circular.
  • the communication space 123 is on the +Z side of the first compartment 121 and on the -Z side of the second compartment 122.
  • the communication space 123 is located in a position that communicates with the communication space 117.
  • the compartments 126, 127 formed in the third intermediate plate 114 are a first compartment 126 and a second compartment 127.
  • the compartments 126, 127 are elliptical in shape.
  • the major axis direction of the compartments 126, 127 is parallel to the Y direction.
  • the compartments 126, 127 are formed at an interval in the Z direction.
  • the second compartment 127 is on the +Z side of the first compartment 126.
  • the first compartment 126 is located in communication with the first compartment 121.
  • the second compartment 127 is located in communication with the second compartment 122.
  • the first outlet 41 of the second plate member 15 is positioned so as to overlap the first compartment 126.
  • the fourth outlet 44 of the second plate member 15 is positioned so as to overlap the second compartment 127.
  • the flow of the refrigerant is shown when the heat exchanger 4 functions as an evaporator. As shown in FIG. 4 , the refrigerant that flows into the first header 310 of the auxiliary heat exchange section 300 through the second refrigerant port 53 flows through the contact space 117, the contact space 123, and the communication space 128 to the second heat transfer tube 33 and the third heat transfer tube 34.
  • the refrigerant that flows through the second heat transfer tube 33 and the third heat transfer tube 34 circulates within the auxiliary heat exchange section 300, then turns around, for example, through the second header (not shown), and flows from the first heat transfer tube 32 and the fourth heat transfer tube 35 into the spatial flow path 116 of the first header 310.
  • the refrigerant from the first heat transfer tube 32 (refrigerant flow path 31) is introduced into the communication space 118 via the first compartment 126 and the first compartment 121.
  • the refrigerant from the fourth heat transfer tube 35 (refrigerant flow path 31) is introduced into the communication space 118 via the second compartment 127 and the second compartment 122.
  • the refrigerant from the first heat transfer tube 32 and the refrigerant from the fourth heat transfer tube 35 join in the communication space 118.
  • the refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see FIG. 2).
  • the refrigerant flow path 31, the first sub-chamber 126, and the first sub-chamber 121 of the first heat transfer tube 32 form a first auxiliary refrigerant flow path.
  • the refrigerant flow path 31, the second sub-chamber 127, and the second sub-chamber 122 of the fourth heat transfer tube 35 form a fourth auxiliary refrigerant flow path.
  • the communication space 118 merges the two auxiliary refrigerant flow paths (the first auxiliary refrigerant flow path and the fourth auxiliary refrigerant flow path).
  • the refrigerant flows in the opposite direction to when the heat exchanger 4 functions as an evaporator (see FIG. 4).
  • the first side 10a of the first header 10 is located upstream of the flow direction F of the outside air.
  • the refrigerant flow path 31 of the second heat transfer tube 33 is the second auxiliary refrigerant flow path.
  • the refrigerant flow path 31 of the third heat transfer tube 34 is the third auxiliary refrigerant flow path.
  • the communication space 128 merges the two auxiliary refrigerant flow paths (the second auxiliary refrigerant flow path and the third auxiliary refrigerant flow path).
  • a communication space 118 (junction) is formed in the first header 310 to join the refrigerant flow path of the first heat transfer tube 32 and the refrigerant flow path of the fourth heat transfer tube 35 when used as an evaporator.
  • a communication space 128 (junction) is formed in the first header 310 to join the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the third heat transfer tube 34 when used as a condenser.
  • the heat exchanger 4 requires less piping than when the junction is located outside the header. This reduces the number of parts. This allows the heat exchanger 4 to be made more compact (smaller).
  • the communication space 118 is formed in a position close to the first side portion 10a on the upstream side of the outside air flow direction F in the first header 310. Therefore, when the heat exchanger 4 is used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, a large amount of refrigerant can be flowed to a position close to the upstream side of the heat transfer tube 30 in the flow direction F. Since the temperature difference between the outside air and the refrigerant is large on the upstream side of the outside air flow direction F, the amount of heat exchange can be increased. Therefore, the heat exchange performance in the auxiliary heat exchange section 300 can be improved.
  • the compartments 121, 122 formed in the second intermediate plate 113 are elliptical, but the shape of the compartments 121, 122 is not limited to this and may be circular.
  • the heat exchanger 4 when used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, more refrigerant can be flowed to a position closer to the upstream side of the flow direction F.
  • Fig. 5 is a configuration diagram showing the structure of the auxiliary heat exchange section 400 in the heat exchanger according to the third embodiment.
  • Fig. 6 is an exploded perspective view showing the structure of the auxiliary heat exchange section 400.
  • the same reference numerals are used for the common components with the heat exchangers according to the other embodiments, and the description thereof will be omitted.
  • the auxiliary heat exchange section 400 has a first header 410, a plurality of heat transfer tubes 30, and a third header 420.
  • the heat transfer tubes 30 may be serpentine tubes.
  • the first header 410 includes a first plate material 411, an intermediate plate material 414, and a second plate material 415. The first plate material 411, the intermediate plate material 414, and the second plate material 415 are stacked in this order.
  • the first header 410 has a spatial flow path 216.
  • the spatial flow path 216 has a communication space 128 formed in the intermediate plate material 414.
  • the second plate material 415 has a second outlet 42 and a third outlet 43.
  • FIG. 6 shows the flow of refrigerant when the heat exchanger functions as an evaporator.
  • the refrigerant that flows into the third header 420 of the auxiliary heat exchange section 400 through the second refrigerant port (not shown) branches and flows into the first heat transfer tube 32 and the fourth heat transfer tube 35 (see FIG. 4).
  • the refrigerant that flows into the first heat transfer tube 32 and the fourth heat transfer tube 35 circulates within the auxiliary heat exchange section 400, and then turns back, for example, through the second header (not shown), and flows into the spatial flow path 216 of the first header 410 through the second heat transfer tube 33 and the third heat transfer tube 34.
  • the refrigerant from the second heat transfer tube 33 (refrigerant flow path 31) and the refrigerant from the third heat transfer tube 34 (refrigerant flow path 31) are introduced into the communication space 128 (junction) and merge.
  • the refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see Figure 2).
  • a communication space 128 (junction) is formed in the first header 410, which joins the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the third heat transfer tube 34.
  • This allows the refrigerant flow path structure to be simplified. This reduces the effects of refrigerant flow rate differences and pressure losses in multiple flow paths compared to when the junction is provided outside the header. This makes it possible to suppress deterioration of heat exchange performance in the main heat exchange section 100 (see FIG. 1).
  • the configurations of the embodiments are not limited to the above examples.
  • the first header 10 has three intermediate plates 12 to 14, but the number of intermediate plates may be one or more (any number equal to or greater than two). That is, the number of intermediate plates may be one or more.
  • flat tubes are used as the heat transfer tubes 30, but serpentine tubes may also be used as the heat transfer tubes 30.
  • the diameters of the communication spaces are the same, but the diameters of the communication spaces do not have to be the same.
  • the piping unit 70 has two distributors 71, 72, which distribute the refrigerant to the two refrigerant flow paths 101, 102 (see FIG. 2), but the flow path structure is not limited to this.
  • the flow path may be structured such that one distributor distributes the refrigerant to the two refrigerant flow paths 101, 102.
  • the junction unit joins two auxiliary refrigerant flow paths, but the number of auxiliary refrigerant flow paths joined by the junction unit may be multiple (any number greater than or equal to two). For example, the junction unit may join three or more auxiliary refrigerant flow paths.
  • a junction section that joins multiple auxiliary refrigerant flow paths is formed in the header. This allows the refrigerant flow path structure to be simplified. Therefore, compared to when the junction section is provided outside the header, the effects of refrigerant flow rate differences and pressure losses in multiple flow paths can be reduced. This makes it possible to suppress a decrease in heat exchange performance in the main heat exchange section.
  • Refrigeration cycle device 4 Heat exchanger 10, 310, 410 First header (header) 10a First side portion (one side portion) 11,411 First plate material 12,112 First intermediate plate material (intermediate plate material) 13,113 Second intermediate plate material (intermediate plate material) 14,114 Third intermediate plate material (intermediate plate material) 15, 415 Second plate material 16, 116, 216 Spatial flow passage 17 First communication space (junction) 18,118 Second communication space (merging part) 26 1st branch room (branch room) 28 3rd branch office (branch room) 30 Heat transfer tube 31 Refrigerant flow path (auxiliary refrigerant flow path) 32 First heat transfer tube (heat transfer tube) 33 Second heat transfer tube (heat transfer tube) 34 Third heat transfer tube (heat transfer tube) 35 Fourth heat transfer tube (heat transfer tube) 52 First refrigerant port (refrigerant flow pipe) 53 Second refrigerant port (refrigerant flow pipe) 100 Main heat exchange section 101 First refrigerant flow path (main refrigerant flow path) 102

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Abstract

A heat exchanger according to an embodiment has: a main heat exchange unit having a plurality of main refrigerant flow paths through which a refrigerant flow; and an auxiliary heat exchange unit through which the refrigerant flows between the main heat exchange unit and the auxiliary heat exchange unit. The auxiliary heat exchange unit has a plurality of heat transfer tubes having auxiliary refrigerant flow paths through which the refrigerant flows, and a header connected to the heat transfer tubes. The header has: a first plate material to which a refrigerant flow pipe for guiding the refrigerant is connected; one or a plurality of intermediate plate materials in which a space flow path into which the refrigerant is introduced is formed; and a second plate material to which the heat transfer tubes are connected. The space flow path has a merging part that merges the plurality of auxiliary refrigerant flow paths.

Description

熱交換器および冷凍サイクル装置Heat exchanger and refrigeration cycle device

 本発明の実施形態は、熱交換器および冷凍サイクル装置に関する。 An embodiment of the present invention relates to a heat exchanger and a refrigeration cycle device.

 熱交換器は、空調機器、冷凍機器などに用いられる。例えば、熱交換器は、主熱交換部と、補助熱交換部とを備える。この熱交換器では、補助熱交換部、主熱交換部の順で冷媒が流れることがある。補助熱交換部が複数の冷媒流路を有する場合、複数の流路における冷媒の流量差、圧力損失などの影響により、主熱交換部における熱交換性能の低下が生じる可能性があった。 Heat exchangers are used in air conditioning equipment, refrigeration equipment, and the like. For example, a heat exchanger may have a main heat exchange section and an auxiliary heat exchange section. In this heat exchanger, the refrigerant may flow through the auxiliary heat exchange section and then the main heat exchange section. When the auxiliary heat exchange section has multiple refrigerant flow paths, there is a possibility that the heat exchange performance in the main heat exchange section may be reduced due to the effects of factors such as the flow rate difference and pressure loss of the refrigerant in the multiple flow paths.

国際公開第2015/133626号International Publication No. 2015/133626

 本発明が解決しようとする課題は、主熱交換部における熱交換性能の低下を抑えることができる熱交換器および冷凍サイクル装置を提供することである。 The problem that this invention aims to solve is to provide a heat exchanger and a refrigeration cycle device that can suppress the deterioration of heat exchange performance in the main heat exchange section.

 実施形態の熱交換器は、冷媒が流通する複数の主冷媒流路を有する主熱交換部と、前記主熱交換部との間で前記冷媒が流通する補助熱交換部と、を持つ。前記補助熱交換部は、前記冷媒が流通する補助冷媒流路を有する複数の伝熱管と、前記伝熱管に接続されたヘッダと、を持つ。前記ヘッダは、前記冷媒を導く冷媒流通管が接続される第1板材と、前記冷媒が導入される空間流路が形成された1または複数の中間板材と、前記伝熱管が接続される第2板材と、を持つ。前記空間流路は、複数の前記補助冷媒流路を合流させる合流部を有する。 The heat exchanger of the embodiment has a main heat exchange section having multiple main refrigerant flow paths through which a refrigerant flows, and an auxiliary heat exchange section through which the refrigerant flows between the main heat exchange section. The auxiliary heat exchange section has multiple heat transfer tubes having auxiliary refrigerant flow paths through which the refrigerant flows, and a header connected to the heat transfer tubes. The header has a first plate material to which a refrigerant flow path that guides the refrigerant is connected, one or more intermediate plate materials in which a spatial flow path into which the refrigerant is introduced is formed, and a second plate material to which the heat transfer tubes are connected. The spatial flow path has a junction section that joins the multiple auxiliary refrigerant flow paths.

実施形態の冷凍サイクル装置の概略構成図。1 is a schematic configuration diagram of a refrigeration cycle device according to an embodiment; 実施形態の熱交換器の構成図。FIG. 2 is a configuration diagram of a heat exchanger according to an embodiment. 第1の実施形態における補助熱交換部の内部構造を示す分解斜視図。FIG. 2 is an exploded perspective view showing the internal structure of the auxiliary heat exchange unit in the first embodiment. 第2の実施形態における補助熱交換部の構造を示す分解斜視図。FIG. 11 is an exploded perspective view showing the structure of an auxiliary heat exchange section in a second embodiment. 第3の実施形態における補助熱交換部の構造を示す構成図。FIG. 13 is a configuration diagram showing a structure of an auxiliary heat exchanger in a third embodiment. 第3の実施形態における補助熱交換部の構造を示す分解斜視図。FIG. 13 is an exploded perspective view showing the structure of an auxiliary heat exchange section in a third embodiment.

 以下、実施形態の熱交換器および冷凍サイクル装置を、図面を参照して説明する。 The heat exchanger and refrigeration cycle device of the embodiment will be described below with reference to the drawings.

 図1は、実施形態の冷凍サイクル装置の概略構成図である。
 図1に示すように、冷凍サイクル装置1は、圧縮機2と、四方弁3と、室外熱交換器(熱交換器)4と、膨張装置5と、室内熱交換器(熱交換器)6と、を備える。冷凍サイクル装置1の構成要素は、配管7によって接続されている。図1では、冷房運転時の冷媒(熱媒体)の流通方向は実線矢印で示す。暖房運転時の冷媒の流通方向は破線矢印で示す。
FIG. 1 is a schematic diagram of a refrigeration cycle device according to an embodiment.
As shown in Fig. 1, the refrigeration cycle apparatus 1 includes a compressor 2, a four-way valve 3, an outdoor heat exchanger (heat exchanger) 4, an expansion device 5, and an indoor heat exchanger (heat exchanger) 6. The components of the refrigeration cycle apparatus 1 are connected by piping 7. In Fig. 1, the flow direction of the refrigerant (heat medium) during cooling operation is indicated by solid arrows, and the flow direction of the refrigerant during heating operation is indicated by dashed arrows.

 圧縮機2は、圧縮機本体2Aと、アキュムレータ2Bと、を備える。圧縮機本体2Aは、内部に取り込まれる低圧の気体冷媒を圧縮して高温・高圧の気体冷媒にする。アキュムレータ2Bは、気液二相冷媒を分離して、気体冷媒を圧縮機本体2Aに供給する。 The compressor 2 comprises a compressor body 2A and an accumulator 2B. The compressor body 2A compresses the low-pressure gas refrigerant taken in to produce high-temperature, high-pressure gas refrigerant. The accumulator 2B separates the gas-liquid two-phase refrigerant and supplies the gas refrigerant to the compressor body 2A.

 四方弁3は、冷媒の流通方向を逆転させ、冷房運転と暖房運転とを切り替える。冷房運転時に、冷媒は、圧縮機2、四方弁3、室外熱交換器4、膨張装置5、室内熱交換器6の順に流れる。このとき、室外熱交換器4は凝縮器として機能する。室内熱交換器6は蒸発器として機能する。 The four-way valve 3 reverses the flow direction of the refrigerant to switch between cooling and heating operation. During cooling operation, the refrigerant flows through the compressor 2, four-way valve 3, outdoor heat exchanger 4, expansion device 5, and indoor heat exchanger 6 in that order. At this time, the outdoor heat exchanger 4 functions as a condenser. The indoor heat exchanger 6 functions as an evaporator.

 暖房運転時に、冷媒は、圧縮機2、四方弁3、室内熱交換器6、膨張装置5、室外熱交換器4の順に流れる。このとき、室内熱交換器6は凝縮器として機能する。室外熱交換器4は蒸発器として機能する。 During heating operation, the refrigerant flows through the compressor 2, four-way valve 3, indoor heat exchanger 6, expansion device 5, and outdoor heat exchanger 4 in that order. At this time, the indoor heat exchanger 6 functions as a condenser. The outdoor heat exchanger 4 functions as an evaporator.

 凝縮器は、圧縮機2から吐出される高温・高圧の気体冷媒を、外気へ放熱させて凝縮させることにより、高圧の液体冷媒にする。膨張装置5は、凝縮器から送り込まれる高圧の液体冷媒の圧力を下げ、低温・低圧の気液二相冷媒にする。蒸発器は、膨張装置5から送り込まれる低温・低圧の気液二相冷媒を、外気から吸熱させて気化させることにより、低圧の気体冷媒にする。 The condenser converts the high-temperature, high-pressure gas refrigerant discharged from the compressor 2 into high-pressure liquid refrigerant by condensing it through heat transfer to the outside air. The expansion device 5 reduces the pressure of the high-pressure liquid refrigerant sent from the condenser, converting it into a low-temperature, low-pressure two-phase gas-liquid refrigerant. The evaporator converts the low-temperature, low-pressure two-phase gas-liquid refrigerant sent from the expansion device 5 into a low-pressure gas refrigerant by absorbing heat from the outside air and vaporizing it.

 冷凍サイクル装置1では、作動流体である冷媒は気体冷媒と液体冷媒との間で相変化しながら循環する。冷媒は、気体冷媒から液体冷媒に相変化する過程で放熱する。冷媒は、液体冷媒から気体冷媒に相変化する過程で吸熱する。冷凍サイクル装置1は、冷媒の放熱または吸熱を利用して、暖房、冷房、除霜などを行う。 In the refrigeration cycle device 1, the refrigerant, which is the working fluid, circulates while changing phase between gaseous refrigerant and liquid refrigerant. The refrigerant releases heat during the phase change from gaseous refrigerant to liquid refrigerant. The refrigerant absorbs heat during the phase change from liquid refrigerant to gaseous refrigerant. The refrigeration cycle device 1 uses the heat release or absorption of the refrigerant to perform heating, cooling, defrosting, etc.

 図2は、実施形態の熱交換器の構成図である。例えば、実施形態の熱交換器は、冷凍サイクル装置1の室外熱交換器4および室内熱交換器6(図1参照)のうち一方または両方として使用される。以下、実施形態の熱交換器が、冷凍サイクル装置1の室外熱交換器4(図1参照)として使用される場合を例にして説明する。室外熱交換器4を単に「熱交換器4」と呼ぶ。 FIG. 2 is a diagram showing the configuration of a heat exchanger according to an embodiment. For example, the heat exchanger according to the embodiment is used as one or both of the outdoor heat exchanger 4 and the indoor heat exchanger 6 (see FIG. 1) of the refrigeration cycle device 1. Below, an example will be described in which the heat exchanger according to the embodiment is used as the outdoor heat exchanger 4 (see FIG. 1) of the refrigeration cycle device 1. The outdoor heat exchanger 4 will be simply referred to as "heat exchanger 4."

(第1の実施形態)
 図2に示すように、第1の実施形態に係る熱交換器4は、主熱交換部100と、補助熱交換部200と、それらをつなぐ配管ユニット70と、を備える。
First Embodiment
As shown in FIG. 2, the heat exchanger 4 according to the first embodiment includes a main heat exchange section 100, an auxiliary heat exchange section 200, and a piping unit 70 connecting the main heat exchange section 100 and the auxiliary heat exchange section 200.

 主熱交換部100は、冷媒が流通する複数の第1の冷媒流路101(主冷媒流路)と、複数の第2の冷媒流路102(主冷媒流路)とを有する。配管ユニット70は、分配器71,72を有する。第1の冷媒流路101は、第1の分配器71と接続される。第2の冷媒流路102は、第2の分配器72と接続される。2つの分配器71,72は、補助熱交換部200と接続される。 The main heat exchange section 100 has a plurality of first refrigerant flow paths 101 (main refrigerant flow paths) through which the refrigerant flows, and a plurality of second refrigerant flow paths 102 (main refrigerant flow paths). The piping unit 70 has distributors 71 and 72. The first refrigerant flow path 101 is connected to the first distributor 71. The second refrigerant flow path 102 is connected to the second distributor 72. The two distributors 71 and 72 are connected to the auxiliary heat exchange section 200.

 図3は、補助熱交換部200の内部構造を示す分解斜視図である。
 X方向、Y方向およびZ方向は、以下のように定義される。Z方向は、第1ヘッダの長手方向である。Z方向は高さ方向である。例えば、Z方向は鉛直方向である。+Zは上方である。-Zは下方である。X方向は、伝熱管の中心軸方向(延在方向)である。X方向は、Z方向と直交する。例えば、X方向は水平方向である。+Xは伝熱管から第1ヘッダに向かう向きである。-Xは+Xと反対の向きである。
FIG. 3 is an exploded perspective view showing the internal structure of the auxiliary heat exchange section 200. As shown in FIG.
The X direction, Y direction, and Z direction are defined as follows: The Z direction is the longitudinal direction of the first header. The Z direction is the height direction. For example, the Z direction is the vertical direction. +Z is upward. -Z is downward. The X direction is the central axis direction (extension direction) of the heat transfer tube. The X direction is perpendicular to the Z direction. For example, the X direction is the horizontal direction. +X is the direction from the heat transfer tube toward the first header. -X is the opposite direction to +X.

 Y方向は、X方向およびZ方向と直交する。Y方向は、左右方向である。+YはY方向の一方の向きである。-YはY方向の他方の向きである。例えば、Y方向は水平方向である。Y方向は、第1ヘッダの幅方向である。Y方向は第1方向である。X方向は第2方向である。Z方向は第3方向である。YZ平面は、Y方向とZ方向とによって形成される平面である。 The Y direction is perpendicular to the X and Z directions. The Y direction is the left-right direction. +Y is one direction of the Y direction. -Y is the other direction of the Y direction. For example, the Y direction is the horizontal direction. The Y direction is the width direction of the first header. The Y direction is the first direction. The X direction is the second direction. The Z direction is the third direction. The YZ plane is the plane formed by the Y and Z directions.

 図3に示すように、補助熱交換部200は、第1ヘッダ10と、複数の伝熱管30(伝熱部)と、第2ヘッダ(不図示)と、を有する。補助熱交換部200は、主熱交換部100(図2参照)との間で冷媒が流通可能である。第1ヘッダ10は、伝熱管30の+X側の端部(一端部)に接続される。第2ヘッダは、伝熱管30の-X側の端部(一端部)に接続される。 As shown in FIG. 3, the auxiliary heat exchange section 200 has a first header 10, a plurality of heat transfer tubes 30 (heat transfer section), and a second header (not shown). A refrigerant can flow between the auxiliary heat exchange section 200 and the main heat exchange section 100 (see FIG. 2). The first header 10 is connected to the +X side end (one end) of the heat transfer tubes 30. The second header is connected to the -X side end (one end) of the heat transfer tubes 30.

 第1ヘッダ10は、YZ平面と平行な平板状に形成される。例えば、X方向から見て、第1ヘッダ10は矩形状である。第1ヘッダ10の形状は、長手方向がZ方向に沿う長方形状である。第1ヘッダ10は、熱伝導率が高く、かつ比重が小さい材料で形成される。例えば、第1ヘッダ10は、アルミニウム、アルミニウム合金等の金属によって形成される。 The first header 10 is formed in a flat plate shape parallel to the YZ plane. For example, when viewed from the X direction, the first header 10 is rectangular. The shape of the first header 10 is a rectangle whose longitudinal direction is along the Z direction. The first header 10 is formed from a material with high thermal conductivity and low specific gravity. For example, the first header 10 is formed from a metal such as aluminum or an aluminum alloy.

 第1ヘッダ10(ヘッダ)は、第1板材11と、第1中間板材12と、第2中間板材13と、第3中間板材14と、第2板材15と、を備える。第1板材11と、第1中間板材12と、第2中間板材13と、第3中間板材14と、第2板材15とは、この順に積層されている。 The first header 10 (header) comprises a first plate material 11, a first intermediate plate material 12, a second intermediate plate material 13, a third intermediate plate material 14, and a second plate material 15. The first plate material 11, the first intermediate plate material 12, the second intermediate plate material 13, the third intermediate plate material 14, and the second plate material 15 are stacked in this order.

 第1中間板材12は、第1板材11の-X側の面に重ねられる。第2中間板材13は、第1中間板材12の-X側の面に重ねられる。第3中間板材14は、第2中間板材13の-X側の面に重ねられる。第2板材15は、第3中間板材14の-X側の面に重ねられる。第1板材11、第1中間板材12、第2中間板材13、第3中間板材14および第2板材15は、厚さ方向(X方向)から見て、略矩形状とされている。第1中間板材12、第2中間板材13および第3中間板材14は、「中間板材12~14」と総称することができる。中間板材12~14は「中間板材」の例である。 The first intermediate plate 12 is placed on the -X side surface of the first plate 11. The second intermediate plate 13 is placed on the -X side surface of the first intermediate plate 12. The third intermediate plate 14 is placed on the -X side surface of the second intermediate plate 13. The second plate 15 is placed on the -X side surface of the third intermediate plate 14. The first plate 11, the first intermediate plate 12, the second intermediate plate 13, the third intermediate plate 14 and the second plate 15 are generally rectangular when viewed from the thickness direction (X direction). The first intermediate plate 12, the second intermediate plate 13 and the third intermediate plate 14 can be collectively referred to as "intermediate plate materials 12 to 14". The intermediate plate materials 12 to 14 are examples of "intermediate plate materials".

 第1ヘッダ10の-Y側の側部は第1側部10aである。第1ヘッダ10の+Y側の側部は第2側部10bである。 The -Y side of the first header 10 is the first side 10a. The +Y side of the first header 10 is the second side 10b.

 第1板材11は、平板状に形成されている。第1板材11には、第1接続口50と第2接続口51とが形成されている。第1接続口50には、第1冷媒ポート52(冷媒流通管)が接続される。第2接続口51には第2冷媒ポート53(冷媒流通管)が接続される。第1冷媒ポート52および第2冷媒ポート53は第1板材11に取り付けられる。第1冷媒ポート52および第2冷媒ポート53は、冷媒が流れる流路を有する。例えば、第1冷媒ポート52および第2冷媒ポート53は、第1板材11に対して垂直である。 The first plate material 11 is formed in a flat plate shape. A first connection port 50 and a second connection port 51 are formed in the first plate material 11. A first refrigerant port 52 (refrigerant flow pipe) is connected to the first connection port 50. A second refrigerant port 53 (refrigerant flow pipe) is connected to the second connection port 51. The first refrigerant port 52 and the second refrigerant port 53 are attached to the first plate material 11. The first refrigerant port 52 and the second refrigerant port 53 have flow paths through which the refrigerant flows. For example, the first refrigerant port 52 and the second refrigerant port 53 are perpendicular to the first plate material 11.

 中間板材12~14には、空間流路16が形成されている。空間流路16は、第1中間板材12に形成された連通空間17,18と、第2中間板材13に形成された連絡空間21~24と、第3中間板材14に形成された分室26~29と、を有する。 A spatial flow path 16 is formed in the intermediate plate members 12 to 14. The spatial flow path 16 has communicating spaces 17, 18 formed in the first intermediate plate member 12, connecting spaces 21 to 24 formed in the second intermediate plate member 13, and separate chambers 26 to 29 formed in the third intermediate plate member 14.

 第1中間板材12に形成された連通空間17,18は、第1中間板材12を厚さ方向に貫通する。連通空間17,18は、第1連通空間17(第1合流部、合流部)および第2連通空間18(第2合流部、合流部)である。連通空間17,18はX方向から見て長円形状とされている。連通空間17,18の長径方向はZ方向と平行である。連通空間17,18の長径は、互いに同じである。連通空間17,18の短径は、互いに同じである。 The communicating spaces 17, 18 formed in the first intermediate plate material 12 penetrate the first intermediate plate material 12 in the thickness direction. The communicating spaces 17, 18 are the first communicating space 17 (first junction, junction) and the second communicating space 18 (second junction, junction). The communicating spaces 17, 18 are elliptical when viewed from the X direction. The major axis direction of the communicating spaces 17, 18 is parallel to the Z direction. The major axes of the communicating spaces 17, 18 are the same as each other. The minor axes of the communicating spaces 17, 18 are the same as each other.

 第1連通空間17は、第1中間板材12のY方向の中央より-Y側に位置する。第1連通空間17は、第1ヘッダ10のY方向(幅方向)の中央に対して第1側部10a(一方の側部)に近い位置に形成されている。第1連通空間17の中心は、第1中間板材12のZ方向における中心より低い位置にある。第1連通空間17の中央部は、第1冷媒ポート52の開口と重なる位置にある。 The first communication space 17 is located on the -Y side of the center of the first intermediate plate 12 in the Y direction. The first communication space 17 is formed at a position closer to the first side portion 10a (one side portion) than the center of the first header 10 in the Y direction (width direction). The center of the first communication space 17 is located lower than the center of the first intermediate plate 12 in the Z direction. The center of the first communication space 17 is located in a position that overlaps with the opening of the first refrigerant port 52.

 第2連通空間18は、第1中間板材12のY方向の中央より+Y側に位置する。第2連通空間18は、第1ヘッダ10のY方向(幅方向)の中央に対して第2側部10b(他方の側部)に近い位置に形成されている。第2連通空間18は、第1連通空間17に比べて+Y側に位置する。第2連通空間18の中心は第1連通空間17の中心より高い位置にある。第2連通空間18の中心は、第1中間板材12のZ方向における中心より高い位置にある。第2連通空間18の中央部は、第2冷媒ポート53の開口と重なる位置にある。 The second communication space 18 is located on the +Y side of the center in the Y direction of the first intermediate plate 12. The second communication space 18 is formed at a position closer to the second side 10b (the other side) than the center in the Y direction (width direction) of the first header 10. The second communication space 18 is located on the +Y side compared to the first communication space 17. The center of the second communication space 18 is located higher than the center of the first communication space 17. The center of the second communication space 18 is located higher than the center in the Z direction of the first intermediate plate 12. The center of the second communication space 18 is located in a position that overlaps with the opening of the second refrigerant port 53.

 第2中間板材13に形成された連絡空間21~24は、第2中間板材13を厚さ方向に貫通する。連絡空間21~24は、第1連絡空間21、第2連絡空間22、第3連絡空間23、および第4連絡空間24である。連絡空間21~24は、X方向から見て円形状に形成されている。連絡空間21~24の径は、互いに同じである。 The contact spaces 21 to 24 formed in the second intermediate plate 13 penetrate the second intermediate plate 13 in the thickness direction. The contact spaces 21 to 24 are the first contact space 21, the second contact space 22, the third contact space 23, and the fourth contact space 24. The contact spaces 21 to 24 are formed in a circular shape when viewed from the X direction. The diameters of the contact spaces 21 to 24 are the same.

 第1連絡空間21および第3連絡空間23は、第2中間板材13のY方向の中央より-Y側に位置する。第1連絡空間21と第3連絡空間23とはZ方向に離れている。第3連絡空間23は、第1連絡空間21に対して+Z側に位置する。第1連絡空間21は、第1連通空間17と連通する位置にある。例えば、第1連絡空間21は、第1連通空間17の下端部に重なる位置にある。第3連絡空間23は、第1連通空間17と連通する位置にある。例えば、第3連絡空間23は、第1連通空間17の上端部に重なる位置にある。 The first communication space 21 and the third communication space 23 are located on the -Y side of the center in the Y direction of the second intermediate plate material 13. The first communication space 21 and the third communication space 23 are separated in the Z direction. The third communication space 23 is located on the +Z side of the first communication space 21. The first communication space 21 is located in communication with the first communication space 17. For example, the first communication space 21 is located so as to overlap the lower end of the first communication space 17. The third communication space 23 is located in communication with the first communication space 17. For example, the third communication space 23 is located so as to overlap the upper end of the first communication space 17.

 第2連絡空間22および第4連絡空間24は、第2中間板材13のY方向の中央より+Y側に位置する。第2連絡空間22と第4連絡空間24とはZ方向に離れている。第4連絡空間24は、第2連絡空間22に対して+Z側に位置する。第2連絡空間22は、第2連通空間18と連通する位置にある。例えば、第2連絡空間22は、第2連通空間18の下端部に重なる位置にある。第4連絡空間24は、第2連通空間18と連通する位置にある。例えば、第4連絡空間24は、第2連通空間18の上端部に重なる位置にある。 The second communication space 22 and the fourth communication space 24 are located on the +Y side of the center in the Y direction of the second intermediate plate material 13. The second communication space 22 and the fourth communication space 24 are separated in the Z direction. The fourth communication space 24 is located on the +Z side of the second communication space 22. The second communication space 22 is located in communication with the second communication space 18. For example, the second communication space 22 is located in a position overlapping the lower end of the second communication space 18. The fourth communication space 24 is located in communication with the second communication space 18. For example, the fourth communication space 24 is located in a position overlapping the upper end of the second communication space 18.

 第3中間板材14に形成された分室26~29は、第3中間板材14を厚さ方向に貫通する。分室26~29は、第1分室26、第2分室27、第3分室28、および第4分室29である。分室26~29は、X方向から見て長円形状とされている。分室26~29の長径方向はY方向と平行である。分室26~29の長径は、互いに同じである。分室26~29の短径は、互いに同じである。 The sub-chambers 26 to 29 formed in the third intermediate plate 14 penetrate the third intermediate plate 14 in the thickness direction. The sub-chambers 26 to 29 are a first sub-chamber 26, a second sub-chamber 27, a third sub-chamber 28, and a fourth sub-chamber 29. The sub-chambers 26 to 29 are elliptical when viewed from the X direction. The major axis direction of the sub-chambers 26 to 29 is parallel to the Y direction. The major axes of the sub-chambers 26 to 29 are the same as each other. The minor axes of the sub-chambers 26 to 29 are the same as each other.

 分室26~29は、Z方向に間隔をおいて形成されている。第2分室27は、第1分室26に対して+Z側にある。第3分室28は、第2分室27に対して+Z側にある。第4分室29は、第3分室28に対して+Z側にある。 The compartments 26 to 29 are spaced apart in the Z direction. The second compartment 27 is on the +Z side of the first compartment 26. The third compartment 28 is on the +Z side of the second compartment 27. The fourth compartment 29 is on the +Z side of the third compartment 28.

 第1分室26は第1連絡空間21に重なる位置にある。例えば、第1分室26の-Y側の端部は第1連絡空間21に重なる位置にある。第2分室27は第2連絡空間22に重なる位置にある。例えば、第2分室27の+Y側の端部は第2連絡空間22に重なる位置にある。第3分室28は第3連絡空間23に重なる位置にある。例えば、第3分室28の-Y側の端部は第3連絡空間23に重なる位置にある。第4分室29は第4連絡空間24に重なる位置にある。例えば、第4分室29の+Y側の端部は第4連絡空間24に重なる位置にある。 The first compartment 26 is positioned so as to overlap the first communication space 21. For example, the -Y side end of the first compartment 26 is positioned so as to overlap the first communication space 21. The second compartment 27 is positioned so as to overlap the second communication space 22. For example, the +Y side end of the second compartment 27 is positioned so as to overlap the second communication space 22. The third compartment 28 is positioned so as to overlap the third communication space 23. For example, the -Y side end of the third compartment 28 is positioned so as to overlap the third communication space 23. The fourth compartment 29 is positioned so as to overlap the fourth communication space 24. For example, the +Y side end of the fourth compartment 29 is positioned so as to overlap the fourth communication space 24.

 第2板材15には、複数の導出口41~44が形成されている。導出口41~44は、第2板材15を厚さ方向に貫通する。導出口41~44は、第1導出口41、第2導出口42、第3導出口43、および第4導出口44である。導出口41~44は、Y方向に沿うスリット状とされている。 The second plate material 15 has a plurality of outlets 41 to 44 formed therein. The outlets 41 to 44 penetrate the second plate material 15 in the thickness direction. The outlets 41 to 44 are a first outlet 41, a second outlet 42, a third outlet 43, and a fourth outlet 44. The outlets 41 to 44 are slit-shaped and extend along the Y direction.

 導出口41~44は、Z方向に間隔をおいて形成されている。第2導出口42は、第1導出口41に対して+Z側にある。第3導出口43は、第2導出口42に対して+Z側にある。第4導出口44は、第3導出口43に対して+Z側にある。 The outlets 41 to 44 are spaced apart in the Z direction. The second outlet 42 is on the +Z side of the first outlet 41. The third outlet 43 is on the +Z side of the second outlet 42. The fourth outlet 44 is on the +Z side of the third outlet 43.

 第1導出口41は、第1分室26に重なる位置にある。第2導出口42は、第2分室27に重なる位置にある。第3導出口43は、第3分室28に重なる位置にある。第4導出口44は、第4分室29に重なる位置にある。 The first outlet 41 is positioned so as to overlap the first compartment 26. The second outlet 42 is positioned so as to overlap the second compartment 27. The third outlet 43 is positioned so as to overlap the third compartment 28. The fourth outlet 44 is positioned so as to overlap the fourth compartment 29.

 伝熱管30は、扁平形状に形成される扁平管である。伝熱管30は、Z方向の外形寸法(外径)に比べてY方向の外形寸法(外径)が大きい。例えば、伝熱管30のY方向の外径は、Z方向の外径に比べて2倍以上である。例えば、伝熱管30の、長さ方向に直交する断面(YZ断面)の形状は、略長円形状、または略楕円形状である。 The heat transfer tube 30 is a flat tube formed in a flat shape. The heat transfer tube 30 has a larger outer dimension (outer diameter) in the Y direction than the outer dimension (outer diameter) in the Z direction. For example, the outer diameter of the heat transfer tube 30 in the Y direction is at least twice the outer diameter in the Z direction. For example, the shape of the cross section (YZ cross section) of the heat transfer tube 30 perpendicular to the length direction is approximately oval or approximately elliptical.

 伝熱管30の内部には、1または複数の冷媒流路31(補助冷媒流路)が形成されている。冷媒流路31には冷媒が流通する。伝熱管30の内部空間には、1または複数の隔壁によって、Y方向(幅方向)に並ぶ複数の冷媒流路31が形成されていてもよい。伝熱管30は、熱伝導率が高く、かつ比重が小さい材料で形成される。例えば、伝熱管30は、アルミニウム、アルミニウム合金等の金属によって形成される。 One or more refrigerant flow paths 31 (auxiliary refrigerant flow paths) are formed inside the heat transfer tube 30. Refrigerant flows through the refrigerant flow paths 31. In the internal space of the heat transfer tube 30, multiple refrigerant flow paths 31 arranged in the Y direction (width direction) may be formed by one or more partition walls. The heat transfer tube 30 is formed of a material with high thermal conductivity and low specific gravity. For example, the heat transfer tube 30 is formed of a metal such as aluminum or an aluminum alloy.

 複数の伝熱管30は、第1伝熱管32と、第2伝熱管33と、第3伝熱管34と、第4伝熱管35と、を含む。第1伝熱管32は第1導出口41に接続される。第2伝熱管33は第2導出口42に接続される。第3伝熱管34は第3導出口43に接続される。第4伝熱管35は第4導出口44に接続される。 The multiple heat transfer tubes 30 include a first heat transfer tube 32, a second heat transfer tube 33, a third heat transfer tube 34, and a fourth heat transfer tube 35. The first heat transfer tube 32 is connected to a first outlet 41. The second heat transfer tube 33 is connected to a second outlet 42. The third heat transfer tube 34 is connected to a third outlet 43. The fourth heat transfer tube 35 is connected to a fourth outlet 44.

 第1伝熱管32と、第2伝熱管33と、第3伝熱管34と、第4伝熱管35とは高さ位置が異なる。第1伝熱管32と、第2伝熱管33と、第3伝熱管34と、第4伝熱管35とはZ方向に間隔をおいて配置されている。第2伝熱管33は第1伝熱管32に対して+Z側に隣り合って位置する。第3伝熱管34は第2伝熱管33に対して+Z側に隣り合って位置する。第4伝熱管35は第3伝熱管34に対して+Z側に隣り合って位置する。 The first heat transfer tube 32, the second heat transfer tube 33, the third heat transfer tube 34, and the fourth heat transfer tube 35 are located at different heights. The first heat transfer tube 32, the second heat transfer tube 33, the third heat transfer tube 34, and the fourth heat transfer tube 35 are arranged at intervals in the Z direction. The second heat transfer tube 33 is located adjacent to the first heat transfer tube 32 on the +Z side. The third heat transfer tube 34 is located adjacent to the second heat transfer tube 33 on the +Z side. The fourth heat transfer tube 35 is located adjacent to the third heat transfer tube 34 on the +Z side.

 第1伝熱管32は、第1分室26との間で冷媒を流通させることができる。第2伝熱管33は、第2分室27との間で冷媒を流通させることができる。第3伝熱管34は、第3分室28との間で冷媒を流通させることができる。第4伝熱管35は、第4分室29との間で冷媒を流通させることができる。 The first heat transfer tube 32 can circulate the refrigerant between the first compartment 26. The second heat transfer tube 33 can circulate the refrigerant between the second compartment 27. The third heat transfer tube 34 can circulate the refrigerant between the third compartment 28. The fourth heat transfer tube 35 can circulate the refrigerant between the fourth compartment 29.

 上下に隣り合う伝熱管30(32~35)の間には、Y方向に沿う外気流路が形成される。例えば、熱交換器4は、送風ファン(不図示)等により外気流路に外気(外部気体)を流通させる。Fは、外気の流れ方向を示す。熱交換器4は、外気流路を流通する外気と、冷媒流路31を流通する冷媒との間で熱交換させることができる。熱交換は、伝熱管30を介して間接的に行われる。 Between adjacent heat transfer tubes 30 (32-35) vertically, an outside air flow path is formed along the Y direction. For example, the heat exchanger 4 circulates outside air (external gas) through the outside air flow path by a blower fan (not shown) or the like. F indicates the flow direction of the outside air. The heat exchanger 4 can exchange heat between the outside air flowing through the outside air flow path and the refrigerant flowing through the refrigerant flow path 31. The heat exchange is performed indirectly via the heat transfer tubes 30.

 以下、冷媒の流れについて詳しく説明する。図3は、熱交換器4が蒸発器として機能する場合の冷媒の流れを示す。
 図3に示すように、第2冷媒ポート53を通じて、補助熱交換部200の第1ヘッダ10に流入した冷媒は、第2連通空間18に導入される。第2連通空間18に流入した冷媒は-Z側と+Z側とに分流される。-Z側に分流された冷媒は、第2連絡空間22を通して第2分室27に流入する。冷媒は第2分室27から第2伝熱管33に流れる。+Z側に分流された冷媒は、第4連絡空間24を通して第4分室29に流入する。冷媒は第4分室29から第4伝熱管35に流れる。
The flow of the refrigerant will be described in detail below. Fig. 3 shows the flow of the refrigerant when the heat exchanger 4 functions as an evaporator.
As shown in Fig. 3, the refrigerant that flows into the first header 10 of the auxiliary heat exchange section 200 through the second refrigerant port 53 is introduced into the second communication space 18. The refrigerant that flows into the second communication space 18 is divided into the -Z side and the +Z side. The refrigerant divided into the -Z side flows into the second compartment 27 through the second communication space 22. The refrigerant flows from the second compartment 27 to the second heat transfer tube 33. The refrigerant divided into the +Z side flows into the fourth compartment 29 through the fourth communication space 24. The refrigerant flows from the fourth compartment 29 to the fourth heat transfer tube 35.

 第2伝熱管33および第4伝熱管35に流れた冷媒は、補助熱交換部200内で流通したのち、例えば第2ヘッダ(不図示)を介して折り返し、第1伝熱管32および第3伝熱管34に流入する。冷媒は、第1伝熱管32および第3伝熱管34を流通して第1ヘッダ10の空間流路16に流入する。 The refrigerant that flows through the second heat transfer tube 33 and the fourth heat transfer tube 35 circulates within the auxiliary heat exchange section 200, then turns around, for example, through the second header (not shown), and flows into the first heat transfer tube 32 and the third heat transfer tube 34. The refrigerant flows through the first heat transfer tube 32 and the third heat transfer tube 34 and into the spatial flow path 16 of the first header 10.

 第1伝熱管32(冷媒流路31)からの冷媒は、第1分室26、第1連絡空間21を通して第1連通空間17に導入される。第3伝熱管34(冷媒流路31)からの冷媒は、第3分室28、第3連絡空間23を通して第1連通空間17に導入される。 The refrigerant from the first heat transfer tube 32 (refrigerant flow path 31) is introduced into the first communication space 17 through the first compartment 26 and the first communication space 21. The refrigerant from the third heat transfer tube 34 (refrigerant flow path 31) is introduced into the first communication space 17 through the third compartment 28 and the third communication space 23.

 第1連絡空間21からの冷媒と、第3連絡空間23からの冷媒とは、第1連通空間17(合流部)で合流する。冷媒は、第1冷媒ポート52から主熱交換部100(図2参照)に向けて導出される。 The refrigerant from the first communication space 21 and the refrigerant from the third communication space 23 merge in the first communication space 17 (merging section). The refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see Figure 2).

 第1伝熱管32の冷媒流路31、第1分室26、および第1連絡空間21は、第1の補助冷媒流路である。第3伝熱管34の冷媒流路31、第3分室28、および第3連絡空間23は、第3の補助冷媒流路である。第1連通空間17は、2つの補助冷媒流路(第1の補助冷媒流路と第3の補助冷媒流路)を合流させる。第1連通空間17は、第1伝熱管32の冷媒流路31と第3伝熱管34の冷媒流路31とを合流させる合流部である。 The refrigerant flow path 31, the first sub-chamber 26, and the first communication space 21 of the first heat transfer tube 32 form a first auxiliary refrigerant flow path. The refrigerant flow path 31, the third sub-chamber 28, and the third communication space 23 of the third heat transfer tube 34 form a third auxiliary refrigerant flow path. The first communication space 17 joins the two auxiliary refrigerant flow paths (the first auxiliary refrigerant flow path and the third auxiliary refrigerant flow path). The first communication space 17 is a junction that joins the refrigerant flow path 31 of the first heat transfer tube 32 and the refrigerant flow path 31 of the third heat transfer tube 34.

 熱交換器4が凝縮器として機能する場合、冷媒は、熱交換器4が蒸発器として機能する場合(図3参照)とは反対の方向に流れる。第1ヘッダ10の第1側部10aは、外気の流れ方向Fの上流側に位置する。 When the heat exchanger 4 functions as a condenser, the refrigerant flows in the opposite direction to when the heat exchanger 4 functions as an evaporator (see FIG. 3). The first side 10a of the first header 10 is located upstream of the flow direction F of the outside air.

 第2伝熱管33の冷媒流路31、第2分室27、および第2連絡空間22は、第2の補助冷媒流路である。第4伝熱管35の冷媒流路31、第4分室29、および第4連絡空間24は、第4の補助冷媒流路である。第2連通空間18は、2つの補助冷媒流路(第2の補助冷媒流路と第4の補助冷媒流路)を合流させる。 The refrigerant flow path 31, the second sub-chamber 27, and the second communication space 22 of the second heat transfer tube 33 form a second auxiliary refrigerant flow path. The refrigerant flow path 31, the fourth sub-chamber 29, and the fourth communication space 24 of the fourth heat transfer tube 35 form a fourth auxiliary refrigerant flow path. The second communication space 18 merges the two auxiliary refrigerant flow paths (the second auxiliary refrigerant flow path and the fourth auxiliary refrigerant flow path).

 本実施形態の熱交換器4は、第1ヘッダ10に、蒸発器として利用される場合に第1伝熱管32の冷媒流路と第3伝熱管34の冷媒流路とを合流させる第1連通空間17(合流部)が形成されている。本実施形態の熱交換器4は、第1ヘッダ10に、凝縮器として利用される場合に第2伝熱管33の冷媒流路と第4伝熱管35の冷媒流路とを合流させる第2連通空間18(合流部)が形成されている。そのため、冷媒の流路構造を簡略にすることができる。したがって、合流部がヘッダの外に設けられている場合に比べ、複数の流路における冷媒の流量差、圧力損失などの影響を小さくできる。よって、主熱交換部100(図1参照)における熱交換性能の低下を抑えることができる。 In the heat exchanger 4 of this embodiment, a first communication space 17 (confluence portion) is formed in the first header 10, which merges the refrigerant flow path of the first heat transfer tube 32 and the refrigerant flow path of the third heat transfer tube 34 when used as an evaporator. In the heat exchanger 4 of this embodiment, a second communication space 18 (confluence portion) is formed in the first header 10, which merges the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the fourth heat transfer tube 35 when used as a condenser. This allows the refrigerant flow path structure to be simplified. Therefore, compared to when the confluence portion is provided outside the header, the effects of the flow rate difference and pressure loss of the refrigerant in the multiple flow paths can be reduced. This allows the deterioration of heat exchange performance in the main heat exchange section 100 (see FIG. 1) to be suppressed.

 熱交換器4では、合流部がヘッダの外に設けられている場合に比べて配管を少なくできる。そのため、部品数を少なくすることができる。よって、熱交換器4をコンパクト化(小型化)することができる。 The heat exchanger 4 requires less piping than when the junction is located outside the header. This reduces the number of parts. This allows the heat exchanger 4 to be made more compact (smaller).

 第1連通空間17(合流部)は、第1ヘッダ10における外気の流れ方向Fの上流側の第1側部10aに近い位置に形成されている。そのため、熱交換器4を凝縮器として用いて、伝熱管30において外気と熱交換が行われる際に、多くの冷媒を伝熱管30における流れ方向Fの上流側に近い位置に流すことができる。外気の流れ方向Fの上流側では、外気と冷媒との温度差が大きいため、熱交換量を大きくできる。したがって、補助熱交換部200における熱交換性能を高めることができる。 The first communication space 17 (confluence portion) is formed in a position close to the first side portion 10a on the upstream side of the outside air flow direction F in the first header 10. Therefore, when the heat exchanger 4 is used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, a large amount of refrigerant can be flowed to a position close to the upstream side of the heat transfer tube 30 in the flow direction F. Since the temperature difference between the outside air and the refrigerant is large on the upstream side of the outside air flow direction F, the amount of heat exchange can be increased. Therefore, the heat exchange performance in the auxiliary heat exchange section 200 can be improved.

(第2の実施形態)
 図4は、第2の実施形態に係る熱交換器における補助熱交換部300の構造を示す分解斜視図である。第1の実施形態に係る熱交換器(図3参照)との共通構成については同じ符号を付して説明を省略する。
Second Embodiment
4 is an exploded perspective view showing the structure of the auxiliary heat exchange section 300 in the heat exchanger according to the second embodiment. The same reference numerals are used for the common components with the heat exchanger according to the first embodiment (see FIG. 3), and the description thereof will be omitted.

 図4に示すように、補助熱交換部300は、第1ヘッダ310と、複数の伝熱管30と、を有する。
 第1ヘッダ310は、第1板材11と、第1中間板材112と、第2中間板材113と、第3中間板材114と、第2板材15とを備える。第1板材11と、第1中間板材112と、第2中間板材113と、第3中間板材114と、第2板材15とは、この順に積層されている。
As shown in FIG. 4 , the auxiliary heat exchange section 300 has a first header 310 and a plurality of heat transfer tubes 30 .
The first header 310 includes a first plate material 11, a first intermediate plate material 112, a second intermediate plate material 113, a third intermediate plate material 114, and a second plate material 15. The first plate material 11, the first intermediate plate material 112, the second intermediate plate material 113, the third intermediate plate material 114, and the second plate material 15 are stacked in this order.

 中間板材112~114には、空間流路116が形成されている。空間流路116は、第1中間板材112に形成された連絡空間117および連通空間118と、第2中間板材113に形成された分室121,122および連絡空間123と、第3中間板材114に形成された分室126,127および連通空間128と、を有する。 A spatial flow path 116 is formed in the intermediate plate members 112 to 114. The spatial flow path 116 has a communication space 117 and a connecting space 118 formed in the first intermediate plate member 112, separate chambers 121, 122 and a connecting space 123 formed in the second intermediate plate member 113, and separate chambers 126, 127 and a connecting space 128 formed in the third intermediate plate member 114.

 第1中間板材112に形成された連絡空間117は、円形状に形成されている。連絡空間117は、第1中間板材112のY方向の中央より+Y側に位置する。 The contact space 117 formed in the first intermediate plate material 112 is formed in a circular shape. The contact space 117 is located on the +Y side of the center of the first intermediate plate material 112 in the Y direction.

 連通空間118は、第1中間板材112のY方向の中央より-Y側に位置する。連通空間118は、連絡空間117に比べて-Y側に位置する。連通空間118は、長円形状とされている。連通空間118の長径方向はZ方向と平行である。 The communication space 118 is located on the -Y side of the center in the Y direction of the first intermediate plate material 112. The communication space 118 is located on the -Y side compared to the contact space 117. The communication space 118 has an elliptical shape. The long diameter direction of the communication space 118 is parallel to the Z direction.

 第2中間板材113に形成された分室121,122は、第1分室121および第2分室122である。分室121,122は、長円形状とされている。分室121,122の長径方向はY方向と平行である。分室121,122は、Z方向に間隔をおいて形成されている。第2分室122は、第1分室121に対して+Z側にある。分室121,122は、連通空間118と連通する位置にある。 The compartments 121, 122 formed in the second intermediate plate 113 are the first compartment 121 and the second compartment 122. The compartments 121, 122 are elliptical in shape. The major axis direction of the compartments 121, 122 is parallel to the Y direction. The compartments 121, 122 are formed at an interval in the Z direction. The second compartment 122 is on the +Z side of the first compartment 121. The compartments 121, 122 are located in a position that communicates with the communication space 118.

 連絡空間123は、円形状とされている。連絡空間123は、第1分室121より+Z側、かつ第2分室122より-Z側にある。連絡空間123は、連絡空間117と連通する位置にある。 The communication space 123 is circular. The communication space 123 is on the +Z side of the first compartment 121 and on the -Z side of the second compartment 122. The communication space 123 is located in a position that communicates with the communication space 117.

 第3中間板材114に形成された分室126,127は、第1分室126および第2分室127である。分室126,127は、長円形状とされている。分室126,127の長径方向はY方向と平行である。分室126,127は、Z方向に間隔をおいて形成されている。第2分室127は、第1分室126に対して+Z側にある。第1分室126は、第1分室121と連通する位置にある。第2分室127は、第2分室122と連通する位置にある。
 また、第2板材15の第1導出口41は、第1分室126に重なる位置にある。第2板材15の第4導出口44は、第2分室127に重なる位置にある。
The compartments 126, 127 formed in the third intermediate plate 114 are a first compartment 126 and a second compartment 127. The compartments 126, 127 are elliptical in shape. The major axis direction of the compartments 126, 127 is parallel to the Y direction. The compartments 126, 127 are formed at an interval in the Z direction. The second compartment 127 is on the +Z side of the first compartment 126. The first compartment 126 is located in communication with the first compartment 121. The second compartment 127 is located in communication with the second compartment 122.
Additionally, the first outlet 41 of the second plate member 15 is positioned so as to overlap the first compartment 126. The fourth outlet 44 of the second plate member 15 is positioned so as to overlap the second compartment 127.

 連通空間128(合流部)は、略矩形状(角丸四角形状)とされている。連通空間128は、第1分室126より+Z側、かつ第2分室127より-Z側にある。連通空間128は、連絡空間123と連通する位置にある。
 また、第2板材15の第2導出口42および第3導出口43は、連通空間128に重なる位置にある。
The communication space 128 (junction) is generally rectangular (rounded square). The communication space 128 is located on the +Z side of the first compartment 126 and on the -Z side of the second compartment 127. The communication space 128 is located in communication with the connection space 123.
Additionally, the second outlet 42 and the third outlet 43 of the second plate member 15 are positioned to overlap the communication space 128 .

 熱交換器4が蒸発器として機能する場合の冷媒の流れを示す。
 図4に示すように、第2冷媒ポート53を通じて、補助熱交換部300の第1ヘッダ310に流入した冷媒は、連絡空間117、連絡空間123、連通空間128を経て第2伝熱管33および第3伝熱管34に流れる。
The flow of the refrigerant is shown when the heat exchanger 4 functions as an evaporator.
As shown in FIG. 4 , the refrigerant that flows into the first header 310 of the auxiliary heat exchange section 300 through the second refrigerant port 53 flows through the contact space 117, the contact space 123, and the communication space 128 to the second heat transfer tube 33 and the third heat transfer tube 34.

 第2伝熱管33および第3伝熱管34に流れた冷媒は、補助熱交換部300内で流通したのち、例えば第2ヘッダ(不図示)を介して折り返し、第1伝熱管32および第4伝熱管35から第1ヘッダ310の空間流路116に流入する。 The refrigerant that flows through the second heat transfer tube 33 and the third heat transfer tube 34 circulates within the auxiliary heat exchange section 300, then turns around, for example, through the second header (not shown), and flows from the first heat transfer tube 32 and the fourth heat transfer tube 35 into the spatial flow path 116 of the first header 310.

 第1伝熱管32(冷媒流路31)からの冷媒は、第1分室126、第1分室121を経て連通空間118に導入される。第4伝熱管35(冷媒流路31)からの冷媒は、第2分室127、第2分室122を経て連通空間118に導入される。第1伝熱管32からの冷媒と第4伝熱管35からの冷媒とは、連通空間118で合流する。冷媒は、第1冷媒ポート52から主熱交換部100(図2参照)に向けて導出される。 The refrigerant from the first heat transfer tube 32 (refrigerant flow path 31) is introduced into the communication space 118 via the first compartment 126 and the first compartment 121. The refrigerant from the fourth heat transfer tube 35 (refrigerant flow path 31) is introduced into the communication space 118 via the second compartment 127 and the second compartment 122. The refrigerant from the first heat transfer tube 32 and the refrigerant from the fourth heat transfer tube 35 join in the communication space 118. The refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see FIG. 2).

 第1伝熱管32の冷媒流路31、第1分室126、および第1分室121は、第1の補助冷媒流路である。第4伝熱管35の冷媒流路31、第2分室127、および第2分室122は、第4の補助冷媒流路である。連通空間118は、2つの補助冷媒流路(第1の補助冷媒流路と第4の補助冷媒流路)を合流させる。 The refrigerant flow path 31, the first sub-chamber 126, and the first sub-chamber 121 of the first heat transfer tube 32 form a first auxiliary refrigerant flow path. The refrigerant flow path 31, the second sub-chamber 127, and the second sub-chamber 122 of the fourth heat transfer tube 35 form a fourth auxiliary refrigerant flow path. The communication space 118 merges the two auxiliary refrigerant flow paths (the first auxiliary refrigerant flow path and the fourth auxiliary refrigerant flow path).

 熱交換器4が凝縮器として機能する場合、冷媒は、熱交換器4が蒸発器として機能する場合(図4参照)とは反対の方向に流れる。第1ヘッダ10の第1側部10aは、外気の流れ方向Fの上流側に位置する。 When the heat exchanger 4 functions as a condenser, the refrigerant flows in the opposite direction to when the heat exchanger 4 functions as an evaporator (see FIG. 4). The first side 10a of the first header 10 is located upstream of the flow direction F of the outside air.

 第2伝熱管33の冷媒流路31は、第2の補助冷媒流路である。第3伝熱管34の冷媒流路31は、第3の補助冷媒流路である。連通空間128は、2つの補助冷媒流路(第2の補助冷媒流路と第3の補助冷媒流路)を合流させる。 The refrigerant flow path 31 of the second heat transfer tube 33 is the second auxiliary refrigerant flow path. The refrigerant flow path 31 of the third heat transfer tube 34 is the third auxiliary refrigerant flow path. The communication space 128 merges the two auxiliary refrigerant flow paths (the second auxiliary refrigerant flow path and the third auxiliary refrigerant flow path).

 本実施形態の熱交換器4は、第1ヘッダ310に、蒸発器として利用される場合に第1伝熱管32の冷媒流路と第4伝熱管35の冷媒流路とを合流させる連通空間118(合流部)が形成されている。本実施形態の熱交換器は、第1ヘッダ310に、凝縮器として利用される場合に第2伝熱管33の冷媒流路と第3伝熱管34の冷媒流路とを合流させる連通空間128(合流部)が形成されている。そのため、冷媒の流路構造を簡略にすることができる。したがって、合流部がヘッダの外に設けられている場合に比べ、複数の流路における冷媒の流量差、圧力損失などの影響を小さくできる。よって、主熱交換部100(図1参照)における熱交換性能の低下を抑えることができる。 In the heat exchanger 4 of this embodiment, a communication space 118 (junction) is formed in the first header 310 to join the refrigerant flow path of the first heat transfer tube 32 and the refrigerant flow path of the fourth heat transfer tube 35 when used as an evaporator. In the heat exchanger 4 of this embodiment, a communication space 128 (junction) is formed in the first header 310 to join the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the third heat transfer tube 34 when used as a condenser. This allows the refrigerant flow path structure to be simplified. Therefore, compared to when the junction is provided outside the header, the effects of the flow rate difference and pressure loss of the refrigerant in the multiple flow paths can be reduced. This allows the deterioration of heat exchange performance in the main heat exchange section 100 (see FIG. 1) to be suppressed.

 熱交換器4では、合流部がヘッダの外に設けられている場合に比べて配管を少なくできる。そのため、部品数を少なくすることができる。よって、熱交換器4をコンパクト化(小型化)することができる。 The heat exchanger 4 requires less piping than when the junction is located outside the header. This reduces the number of parts. This allows the heat exchanger 4 to be made more compact (smaller).

 連通空間118は、第1ヘッダ310における外気の流れ方向Fの上流側の第1側部10aに近い位置に形成されている。そのため、熱交換器4を凝縮器として用いて、伝熱管30において外気と熱交換が行われる際に、多くの冷媒を伝熱管30における流れ方向Fの上流側に近い位置に流すことができる。外気の流れ方向Fの上流側では、外気と冷媒との温度差が大きいため、熱交換量を大きくできる。したがって、補助熱交換部300における熱交換性能を高めることができる。 The communication space 118 is formed in a position close to the first side portion 10a on the upstream side of the outside air flow direction F in the first header 310. Therefore, when the heat exchanger 4 is used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, a large amount of refrigerant can be flowed to a position close to the upstream side of the heat transfer tube 30 in the flow direction F. Since the temperature difference between the outside air and the refrigerant is large on the upstream side of the outside air flow direction F, the amount of heat exchange can be increased. Therefore, the heat exchange performance in the auxiliary heat exchange section 300 can be improved.

 本実施形態において、第2中間板材113に形成された分室121,122は、長円形状とされているが、分室121,122の形状はこの限りではなく、円形状とされていてもよい。この場合、熱交換器4を凝縮器として用いて、伝熱管30において外気と熱交換が行われる際に、より多くの冷媒を流れ方向Fの上流側に近い位置に流すことができる。 In this embodiment, the compartments 121, 122 formed in the second intermediate plate 113 are elliptical, but the shape of the compartments 121, 122 is not limited to this and may be circular. In this case, when the heat exchanger 4 is used as a condenser and heat exchange with the outside air is performed in the heat transfer tube 30, more refrigerant can be flowed to a position closer to the upstream side of the flow direction F.

(第3の実施形態)
 図5は、第3の実施形態に係る熱交換器における補助熱交換部400の構造を示す構成図である。図6は、補助熱交換部400の構造を示す分解斜視図である。他の実施形態に係る熱交換器との共通構成については同じ符号を付して説明を省略する。
Third Embodiment
Fig. 5 is a configuration diagram showing the structure of the auxiliary heat exchange section 400 in the heat exchanger according to the third embodiment. Fig. 6 is an exploded perspective view showing the structure of the auxiliary heat exchange section 400. The same reference numerals are used for the common components with the heat exchangers according to the other embodiments, and the description thereof will be omitted.

 図5に示すように、補助熱交換部400は、第1ヘッダ410と、複数の伝熱管30と、第3ヘッダ420と、を有する。伝熱管30は、サーペンタイン管であってもよい。
 図6に示すように、第1ヘッダ410は、第1板材411と、中間板材414と、第2板材415と、を備える。第1板材411と、中間板材414と、第2板材415とは、この順に積層される。
5, the auxiliary heat exchange section 400 has a first header 410, a plurality of heat transfer tubes 30, and a third header 420. The heat transfer tubes 30 may be serpentine tubes.
6, the first header 410 includes a first plate material 411, an intermediate plate material 414, and a second plate material 415. The first plate material 411, the intermediate plate material 414, and the second plate material 415 are stacked in this order.

 第1ヘッダ410には、空間流路216が形成されている。空間流路216は、中間板材414に形成された連通空間128を有する。第2板材415には、第2導出口42および第3導出口43が形成されている。 The first header 410 has a spatial flow path 216. The spatial flow path 216 has a communication space 128 formed in the intermediate plate material 414. The second plate material 415 has a second outlet 42 and a third outlet 43.

 図6は、熱交換器が蒸発器として機能する場合の冷媒の流れを示す。
 図5および図6に示すように、第2冷媒ポート(図示略)を通じて、補助熱交換部400の第3ヘッダ420に流入した冷媒は、第1伝熱管32および第4伝熱管35(図4参照)に分岐して流れる。第1伝熱管32および第4伝熱管35に流れた冷媒は、補助熱交換部400内で流通したのち、例えば第2ヘッダ(不図示)を介して折り返し、第2伝熱管33および第3伝熱管34を通して第1ヘッダ410の空間流路216に流入する。
FIG. 6 shows the flow of refrigerant when the heat exchanger functions as an evaporator.
5 and 6, the refrigerant that flows into the third header 420 of the auxiliary heat exchange section 400 through the second refrigerant port (not shown) branches and flows into the first heat transfer tube 32 and the fourth heat transfer tube 35 (see FIG. 4). The refrigerant that flows into the first heat transfer tube 32 and the fourth heat transfer tube 35 circulates within the auxiliary heat exchange section 400, and then turns back, for example, through the second header (not shown), and flows into the spatial flow path 216 of the first header 410 through the second heat transfer tube 33 and the third heat transfer tube 34.

 第2伝熱管33(冷媒流路31)からの冷媒と、第3伝熱管34(冷媒流路31)からの冷媒とは、連通空間128(合流部)に導入されて合流する。冷媒は、第1冷媒ポート52から主熱交換部100(図2参照)に向けて導出される。 The refrigerant from the second heat transfer tube 33 (refrigerant flow path 31) and the refrigerant from the third heat transfer tube 34 (refrigerant flow path 31) are introduced into the communication space 128 (junction) and merge. The refrigerant is discharged from the first refrigerant port 52 toward the main heat exchange section 100 (see Figure 2).

 本実施形態の熱交換器は、第1ヘッダ410に、第2伝熱管33の冷媒流路と第3伝熱管34の冷媒流路とを合流させる連通空間128(合流部)が形成されている。そのため、冷媒の流路構造を簡略にすることができる。したがって、合流部がヘッダの外に設けられている場合に比べ、複数の流路における冷媒の流量差、圧力損失などの影響を小さくできる。よって、主熱交換部100(図1参照)における熱交換性能の低下を抑えることができる。 In the heat exchanger of this embodiment, a communication space 128 (junction) is formed in the first header 410, which joins the refrigerant flow path of the second heat transfer tube 33 and the refrigerant flow path of the third heat transfer tube 34. This allows the refrigerant flow path structure to be simplified. This reduces the effects of refrigerant flow rate differences and pressure losses in multiple flow paths compared to when the junction is provided outside the header. This makes it possible to suppress deterioration of heat exchange performance in the main heat exchange section 100 (see FIG. 1).

 以上、実施形態の熱交換器および冷凍サイクル装置について説明したが、実施形態の構成は前述の例に限定されない。
 例えば、図3に示す熱交換器4では、第1ヘッダ10は3つの中間板材12~14を有するが、中間板材の数は1でもよいし、複数(2以上の任意の数)でもよい。すなわち、中間板の数は1または複数であってよい。第1の実施形態および第2の実施形態では、伝熱管30として扁平管を用いているが、伝熱管30としてはサーペンタイン管を用いてもよい。第1の実施形態および第2の実施形態では、連絡空間の径は互いに同じであるが、連絡空間の径は互いに同じでなくてもよい。
Although the heat exchanger and the refrigeration cycle apparatus according to the embodiment have been described above, the configurations of the embodiments are not limited to the above examples.
For example, in the heat exchanger 4 shown in Fig. 3, the first header 10 has three intermediate plates 12 to 14, but the number of intermediate plates may be one or more (any number equal to or greater than two). That is, the number of intermediate plates may be one or more. In the first and second embodiments, flat tubes are used as the heat transfer tubes 30, but serpentine tubes may also be used as the heat transfer tubes 30. In the first and second embodiments, the diameters of the communication spaces are the same, but the diameters of the communication spaces do not have to be the same.

 また、本実施形態では、配管ユニット70は2つの分配器71,72を有し、それぞれの分配器71,72によって2つの冷媒流路101,102に分配しているが(図2参照)、流路構造はこの限りではない。例えば、流路は、1つの分配器で2つの冷媒流路101,102に分配する構造でもよい。 In addition, in this embodiment, the piping unit 70 has two distributors 71, 72, which distribute the refrigerant to the two refrigerant flow paths 101, 102 (see FIG. 2), but the flow path structure is not limited to this. For example, the flow path may be structured such that one distributor distributes the refrigerant to the two refrigerant flow paths 101, 102.

 本実施形態では、合流部は2つの補助冷媒流路を合流させるが、合流部が合流させる補助冷媒流路の数は、複数(2以上の任意の数)であってよい。例えば、合流部は、3以上の補助冷媒流路を合流させてもよい。 In this embodiment, the junction unit joins two auxiliary refrigerant flow paths, but the number of auxiliary refrigerant flow paths joined by the junction unit may be multiple (any number greater than or equal to two). For example, the junction unit may join three or more auxiliary refrigerant flow paths.

 以上説明した少なくともひとつの実施形態によれば、ヘッダに、複数の補助冷媒流路を合流させる合流部が形成されている。そのため、冷媒の流路構造を簡略にすることができる。したがって、合流部がヘッダの外に設けられている場合に比べ、複数の流路における冷媒の流量差、圧力損失などの影響を小さくできる。よって、主熱交換部における熱交換性能の低下を抑えることができる。 According to at least one of the embodiments described above, a junction section that joins multiple auxiliary refrigerant flow paths is formed in the header. This allows the refrigerant flow path structure to be simplified. Therefore, compared to when the junction section is provided outside the header, the effects of refrigerant flow rate differences and pressure losses in multiple flow paths can be reduced. This makes it possible to suppress a decrease in heat exchange performance in the main heat exchange section.

 本発明のいくつかの実施形態を説明したが、これらの実施形態は、例として提示したものであり、発明の範囲を限定することは意図していない。これら実施形態は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で、種々の省略、置き換え、変更を行うことができる。これら実施形態やその変形は、発明の範囲や要旨に含まれると同様に、特許請求の範囲に記載された発明とその均等の範囲に含まれるものである。 Although several embodiments of the present invention have been described, these embodiments are presented as examples and are not intended to limit the scope of the invention. These embodiments can be implemented in various other forms, and various omissions, substitutions, and modifications can be made without departing from the gist of the invention. These embodiments and their modifications are within the scope of the invention and its equivalents as set forth in the claims, as well as the scope and gist of the invention.

 1 冷凍サイクル装置
 4 熱交換器
 10,310,410 第1ヘッダ(ヘッダ)
 10a 第1側部(一方の側部)
 11,411 第1板材
 12,112 第1中間板材(中間板材)
 13,113 第2中間板材(中間板材)
 14,114 第3中間板材(中間板材)
 15,415 第2板材
 16,116,216 空間流路
 17 第1連通空間(合流部)
 18,118 第2連通空間(合流部)
 26 第1分室(分室)
 28 第3分室(分室)
 30 伝熱管
 31 冷媒流路(補助冷媒流路)
 32 第1伝熱管(伝熱管)
 33 第2伝熱管(伝熱管)
 34 第3伝熱管(伝熱管)
 35 第4伝熱管(伝熱管)
 52 第1冷媒ポート(冷媒流通管)
 53 第2冷媒ポート(冷媒流通管)
 100 主熱交換部
 101 第1の冷媒流路(主冷媒流路)
 102 第2の冷媒流路(主冷媒流路)
 128 連通空間(合流部)
 200,300,400 補助熱交換部
 414 中間板材
1 Refrigeration cycle device 4 Heat exchanger 10, 310, 410 First header (header)
10a First side portion (one side portion)
11,411 First plate material 12,112 First intermediate plate material (intermediate plate material)
13,113 Second intermediate plate material (intermediate plate material)
14,114 Third intermediate plate material (intermediate plate material)
15, 415 Second plate material 16, 116, 216 Spatial flow passage 17 First communication space (junction)
18,118 Second communication space (merging part)
26 1st branch room (branch room)
28 3rd branch office (branch room)
30 Heat transfer tube 31 Refrigerant flow path (auxiliary refrigerant flow path)
32 First heat transfer tube (heat transfer tube)
33 Second heat transfer tube (heat transfer tube)
34 Third heat transfer tube (heat transfer tube)
35 Fourth heat transfer tube (heat transfer tube)
52 First refrigerant port (refrigerant flow pipe)
53 Second refrigerant port (refrigerant flow pipe)
100 Main heat exchange section 101 First refrigerant flow path (main refrigerant flow path)
102 Second refrigerant flow path (main refrigerant flow path)
128 Communication space (merging part)
200,300,400 Auxiliary heat exchange section 414 Intermediate plate material

Claims (5)

 冷媒が流通する複数の主冷媒流路を有する主熱交換部と、
 前記主熱交換部との間で前記冷媒が流通する補助熱交換部と、を備え、
 前記補助熱交換部は、前記冷媒が流通する補助冷媒流路を有する複数の伝熱管と、
 前記伝熱管に接続されたヘッダと、を備え、
 前記ヘッダは、
  前記冷媒を導く冷媒流通管が接続される第1板材と、
  前記冷媒が導入される空間流路が形成された1または複数の中間板材と、
  前記伝熱管が接続される第2板材と、
  を備え、
 前記空間流路は、複数の前記補助冷媒流路を合流させる合流部を有する、
 熱交換器。
a main heat exchange unit having a plurality of main refrigerant flow paths through which a refrigerant flows;
an auxiliary heat exchange unit through which the refrigerant flows between the main heat exchange unit and the auxiliary heat exchange unit;
The auxiliary heat exchange section includes a plurality of heat transfer tubes having an auxiliary refrigerant flow path through which the refrigerant flows;
a header connected to the heat transfer tube,
The header includes:
A first plate member to which a refrigerant flow pipe for guiding the refrigerant is connected;
One or more intermediate plates having spatial flow paths through which the coolant is introduced;
A second plate member to which the heat transfer tube is connected;
Equipped with
The spatial flow path has a junction portion where the plurality of auxiliary refrigerant flow paths join together.
Heat exchanger.
 前記複数の伝熱管は、第1伝熱管と前記第1伝熱管の鉛直方向に隣り合う第2伝熱管と前記第2伝熱管の鉛直方向に隣り合う第3伝熱管とを有し、
 前記合流部は、前記第1伝熱管の前記補助冷媒流路と、前記第3伝熱管の前記補助冷媒流路とを合流させる、請求項1に記載の熱交換器。
the plurality of heat transfer tubes include a first heat transfer tube, a second heat transfer tube adjacent to the first heat transfer tube in a vertical direction, and a third heat transfer tube adjacent to the second heat transfer tube in a vertical direction,
The heat exchanger according to claim 1 , wherein the junction portion joins the auxiliary refrigerant flow passage of the first heat transfer tube and the auxiliary refrigerant flow passage of the third heat transfer tube.
 前記複数の伝熱管は、第1伝熱管と前記第1伝熱管の鉛直方向に隣り合う第2伝熱管と前記第2伝熱管の鉛直方向に隣り合う第3伝熱管とを有し、
 前記合流部は、前記第2伝熱管の前記補助冷媒流路と、前記第3伝熱管の前記補助冷媒流路とを合流させる、請求項1に記載の熱交換器。
the plurality of heat transfer tubes include a first heat transfer tube, a second heat transfer tube adjacent to the first heat transfer tube in a vertical direction, and a third heat transfer tube adjacent to the second heat transfer tube in a vertical direction,
The heat exchanger according to claim 1 , wherein the junction portion joins the auxiliary refrigerant flow passage of the second heat transfer tube and the auxiliary refrigerant flow passage of the third heat transfer tube.
 前記合流部は、前記ヘッダの幅方向の中央に対して一方の側部に近い位置に形成され、
 前記側部は、前記伝熱管において外部気体と熱交換が行われる際に前記外部気体の流れ方向の上流側に位置する、
 請求項1に記載の熱交換器。
The joining portion is formed at a position close to one side portion with respect to a center in a width direction of the header,
The side portion is located upstream in a flow direction of the external gas when heat exchange between the external gas and the heat transfer tube is performed.
2. The heat exchanger of claim 1.
 請求項1ないし4のいずれか一項に記載の熱交換器を備える、冷凍サイクル装置。 A refrigeration cycle device equipped with a heat exchanger according to any one of claims 1 to 4.
PCT/JP2023/034538 2023-09-22 2023-09-22 Heat exchanger and refrigeration cycle device Pending WO2025062640A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014184916A1 (en) * 2013-05-15 2014-11-20 三菱電機株式会社 Laminated header, heat exchanger, and air conditioner
WO2015097876A1 (en) * 2013-12-27 2015-07-02 三菱電機株式会社 Stacked header, heat exchanger, and air conditioner
WO2017042866A1 (en) * 2015-09-07 2017-03-16 三菱電機株式会社 Distributor, laminated header, heat exchanger, and air conditioner
WO2018179311A1 (en) * 2017-03-31 2018-10-04 三菱電機株式会社 Heat exchanger and refrigeration cycle device provided with same
EP3988887A1 (en) * 2019-06-19 2022-04-27 Zhejiang Yinlun Machinery Co., Ltd. Header assembly and heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014184916A1 (en) * 2013-05-15 2014-11-20 三菱電機株式会社 Laminated header, heat exchanger, and air conditioner
WO2015097876A1 (en) * 2013-12-27 2015-07-02 三菱電機株式会社 Stacked header, heat exchanger, and air conditioner
WO2017042866A1 (en) * 2015-09-07 2017-03-16 三菱電機株式会社 Distributor, laminated header, heat exchanger, and air conditioner
WO2018179311A1 (en) * 2017-03-31 2018-10-04 三菱電機株式会社 Heat exchanger and refrigeration cycle device provided with same
EP3988887A1 (en) * 2019-06-19 2022-04-27 Zhejiang Yinlun Machinery Co., Ltd. Header assembly and heat exchanger

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