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WO2019058514A1 - Échangeur de chaleur, dispositif à cycle frigorifique, et procédé de fabrication d'échangeur de chaleur - Google Patents

Échangeur de chaleur, dispositif à cycle frigorifique, et procédé de fabrication d'échangeur de chaleur Download PDF

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Publication number
WO2019058514A1
WO2019058514A1 PCT/JP2017/034329 JP2017034329W WO2019058514A1 WO 2019058514 A1 WO2019058514 A1 WO 2019058514A1 JP 2017034329 W JP2017034329 W JP 2017034329W WO 2019058514 A1 WO2019058514 A1 WO 2019058514A1
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WO
WIPO (PCT)
Prior art keywords
heat transfer
heat exchanger
transfer tube
fin
header
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.)
Ceased
Application number
PCT/JP2017/034329
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English (en)
Japanese (ja)
Inventor
暁 八柳
石橋　晃
前田　剛志
中村　伸
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to PCT/JP2017/034329 priority Critical patent/WO2019058514A1/fr
Priority to JP2019542917A priority patent/JP6880206B2/ja
Publication of WO2019058514A1 publication Critical patent/WO2019058514A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-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
    • F28D1/02—Heat-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
    • F28D1/04—Heat-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
    • F28D1/053—Heat-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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates

Definitions

  • the present invention relates to a heat exchanger provided with a header, a refrigeration cycle apparatus provided with the heat exchanger, and a method of manufacturing the heat exchanger provided with the header.
  • a plate fin tube type heat composed of a plurality of plate-like fins arranged via a fin pitch and a plurality of circular or flat heat transfer tubes Exchangers are known.
  • a corrugated fin-tube heat exchanger composed of a corrugated fin and a flat heat transfer tube.
  • the flat heat transfer tube is a heat transfer tube in which the width (in the direction of the major axis in the cross section) is larger than the longitudinal width (in the direction of the minor axis in the cross section). It is.
  • the heat transfer tube having a flat cross-sectional shape is referred to as a flat tube.
  • the heat transfer tube having a circular cross section is referred to as a circular tube.
  • the corrugated fin and tube type heat exchanger generally has a configuration in which wavy fins and flat heat transfer tubes are alternately stacked.
  • the plate-fin tube type heat exchanger is configured such that the heat transfer tube is inserted into a through hole or a notch formed in the fin.
  • the heat transfer tubes are attached to the through holes or notches of the fins so as to extend along the direction of arrangement of the fins.
  • the notch is formed to open one side of the fin.
  • the heat transfer tube inserted into the notch is attached to the fin by being inserted into the notch from the open side.
  • a heat transfer tube with a reduced diameter may be used in order to conduct heat exchange efficiently.
  • a flat tube may be used as such a heat transfer tube. Inside the flat tube, a number of finely divided flow paths are formed in parallel.
  • the flow passage formed inside the flat tube is referred to as an internal flow passage.
  • a heat exchanger provided with a heat transfer tube having a plurality of flow paths formed therein and a heat exchanger provided with a heat transfer tube having a groove formed on the inner surface are also known. In such a heat exchanger, the heat exchange performance is improved by increasing the surface area to be exchanged with heat by forming a plurality of flow paths inside the heat transfer pipe or forming a groove on the inner surface of the heat transfer pipe. ing.
  • heat exchangers one having a header (divider) is known.
  • the end of each heat transfer tube is connected to a header that forms a refrigerant flow path together with the heat transfer tube.
  • heat exchange is performed between a heat exchange fluid such as air flowing between the fins and a heat exchange fluid such as water flowing in the heat transfer pipe or a refrigerant.
  • the corrugated fin and tube type heat exchanger can be manufactured by alternately laminating heat transfer tubes and corrugated fins and fixing them by crimping or brazing.
  • a plate-fin tube type heat exchanger can be manufactured by inserting a hairpin-processed tube into a plurality of fins and pressing and expanding the inside of the tube to join the tube and the fins. This manufacturing method is referred to as an expansion method. Moreover, a plate fin tube type heat exchanger can be manufactured by fixing by brazing a tube and a fin.
  • a tube expansion method there is known a method in which a rigid rod is inserted into a heat transfer tube to mechanically spread the heat transfer tube from the inside.
  • This pipe expansion method is referred to as a mechanical pipe expansion method.
  • a pipe expansion method there is known a method in which a fluid is poured into a heat transfer pipe, and pressure is spread from inside the heat transfer pipe by raising the pressure in the heat transfer pipe. This pipe expansion method is referred to as a fluid pressure expansion method.
  • Patent Document 1 discloses a technique for manufacturing a heat exchanger using a fluid pressure expansion method.
  • Patent Document 1 it is necessary to design the inner space of the header and the header wall thickness so that the pressure resistance of the header is equal to or higher than the internal flow passage of the flat tube, and the cost required to ensure reliability It will increase.
  • the heat exchanger can not be realized to obtain the intended performance.
  • the cost increase of the header and the weight increase of the header and the reliability of the heat exchanger are caused due to the pressure resistance design of the header. It is likely to cause a decline. That is, it is necessary to increase the wall thickness of the header to correspond to the high pressure acting on the inside of the header to ensure reliability, and the cost of the header and the weight of the header will be increased accordingly. For this reason, a heat exchanger, a refrigeration cycle apparatus, and a method of manufacturing the heat exchanger, which can ensure the reliability of the heat exchanger while suppressing the increase in the cost of the header, are desired.
  • the present invention has been made to solve the above problems, and is provided with a heat exchanger that can improve the reliability of the heat exchanger while suppressing the increase in the cost of the header, and the heat exchanger.
  • a refrigeration cycle apparatus and a method of manufacturing a heat exchanger are provided.
  • the heat exchanger according to the present invention has a flat cross section, and has a plurality of heat transfer pipes in which a plurality of inner holes are formed, a plurality of fins to which the plurality of heat transfer pipes are joined, and the plurality of heat transfer pipes.
  • a refrigeration cycle apparatus includes a compressor, a first heat exchanger, a throttling device, and a refrigerant circuit in which a second heat exchanger is connected by a refrigerant pipe, and the above-described heat exchanger is the first heat exchanger.
  • the heat exchanger is used as at least one of the heat exchanger and the second heat exchanger.
  • a plurality of through holes are formed in a plate member serving as a fin, a heat transfer pipe is inserted into each of the plurality of through holes, and one end of the heat transfer pipe Sealing, supplying the gas from the other end of the heat transfer tube to expand the heat transfer tube, the heat transfer tube is joined to the fin, and after the heat transfer tube is joined to the fin, The heat transfer tube is brazed to a header having a fluid flow passage.
  • the thickness of the outer wall portion of the header can be made smaller compared to the inner diameter of the header, and the material cost can be reduced accordingly.
  • the refrigeration cycle apparatus of the present invention since the above-described heat exchanger is used as at least one of the first heat exchanger and the second heat exchanger, the manufacturing cost can be reduced accordingly.
  • the method of manufacturing a heat exchanger according to the present invention it is possible to expand a plurality of heat transfer tubes without using a header, and it is not necessary to provide the header with a pressure resistance equal to or higher than that of the heat transfer tube.
  • coolant It is a schematic sectional drawing which shows the cross section of the heat exchanger tube which comprises the heat exchanger which concerns on Embodiment 1 of this invention. It is a schematic front view of the fin which comprises the heat exchanger which concerns on Embodiment 1 of this invention. It is a schematic side view of the fin which comprises the heat exchanger which concerns on Embodiment 1 of this invention. It is a schematic top view of the fin which comprises the heat exchanger which concerns on Embodiment 1 of this invention.
  • FIG. 1 It is a schematic perspective view which shows the structural example of the header with which the heat exchanger which concerns on Embodiment 1 of this invention is provided. It is a schematic sectional drawing which shows an example of a cross-sectional structure of the header with which the heat exchanger which concerns on Embodiment 1 of this invention is provided. It is a schematic sectional drawing which shows another example of the cross-sectional structure of the header with which the heat exchanger which concerns on Embodiment 1 of this invention is provided. It is a flowchart which shows roughly the process of the manufacturing method of the heat exchanger which concerns on Embodiment 1 of this invention.
  • FIG. 1 is a schematic perspective view showing an example of the configuration of a heat exchanger according to Embodiment 1 of the present invention.
  • the heat exchanger according to the first embodiment is referred to as a heat exchanger 1A.
  • FIG. 2 is a schematic side view showing an example of the heat exchanger 1A as viewed from the air flow direction.
  • FIG. 3 is a schematic side view showing an example of the heat exchanger 1A as viewed from the flow direction of the refrigerant. An example of the heat exchanger 1A will be described based on FIGS. 1 to 3.
  • the heat exchanger 1A includes a plurality of fins 30A, a plurality of heat transfer pipes 20A, a header 40A, and an inter-row connecting member 45A.
  • the heat exchanger 1A is a heat exchanger having a two-row structure, and includes the upwind heat exchanger 41A, the downwind heat exchanger 42A, the upwind header 40A-1, the downwind header 40A-2, and , The inter-row connection member 45A.
  • the windward header 40A-1 and the windward header 40A-2 may be collectively referred to as a header 40A.
  • the upwind side heat exchanger 41A and the downwind side heat exchanger 42A are similarly configured. In the following, when the heat exchanger 1A is described, it is assumed that both the upwind side heat exchanger 41A and the downwind side heat exchanger 42A are described.
  • the windward header 40A-1 and the windward header 40A-2 are attached to the paper right side of the windward heat exchanger 41A and the paper right side of the windward heat exchanger 42A. Furthermore, as shown in FIG. 1, the inter-row connection member 45A is attached to the left side of the windward heat exchanger 41A in the drawing and the left side of the leeward heat exchanger 42A in the drawing. Thus, the heat exchanger 1A is produced.
  • the heat transfer tubes 20A are attached to the windward header 40A-1 at a predetermined interval (pitch P1). Similarly, the heat transfer tubes 20A are attached to the downwind side header 40A-2 at a predetermined interval (pitch P1).
  • the plurality of heat transfer tubes 20A are mounted to penetrate through the plurality of through holes 31A formed in the fins 30A, and intersect the fins 30A. As shown in FIG. 3, the heat transfer tube 20A is configured to have a circular cross section.
  • the plurality of heat transfer tubes 20A are disposed at predetermined intervals in a step direction (vertical direction in the drawing) orthogonal to the flow direction of the refrigerant.
  • the distance in the direction of gravity of the heat transfer tubes 20A vertically adjacent to each other is constant at the pitch P2 of the adjacent through holes 31A of the fins 30A.
  • the heat transfer tube 20A is made of aluminum or an aluminum alloy.
  • FIG. 2 and FIG. 3 show an example in which the number of heat transfer tubes 20A is ten, the number of heat transfer tubes 20A is not particularly limited.
  • the symbols shown in FIGS. 1 to 3 are also used in the following drawings.
  • a region where the through holes 31A of the fins 30A are formed is referred to as a heat transfer tube region 31R.
  • a region which is both ends in the short direction of the fins 30A and in which the fins 30A are continuous in the longitudinal direction without being divided by the through holes 31A is referred to as a fin region 32R.
  • the fin 30A is formed of a rectangular plate-like member having a long side and a short side.
  • the fins 30A have a pitch P1 in the longitudinal direction, and a plurality of through holes 31A are formed through the heat transfer pipe area 31R.
  • the fins 30A are made of aluminum or an aluminum alloy. Further, although the through holes 31A have a circular shape corresponding to the cross sectional shape of the heat transfer tube 20A, the shape is not specified.
  • the long side direction of the fin 30A is referred to as the longitudinal direction
  • the short side direction is referred to as the short direction.
  • FIG. 4 is a schematic perspective view showing an example of the configuration of the heat exchanger 1B.
  • FIG. 5 is a schematic side view showing an example of the heat exchanger 1B as viewed from the flow direction of the refrigerant.
  • FIG. 6 is a schematic cross-sectional view showing a cross section of the heat transfer tube 20B which constitutes the heat exchanger 1B.
  • FIG. 7 is a schematic front view of the fins 30B constituting the heat exchanger 1B.
  • FIG. 8 is a schematic side view of the fins 30B constituting the heat exchanger 1B.
  • FIG. 9 is a schematic top view of the fins 30B constituting the heat exchanger 1B.
  • An example of the heat exchanger 1B will be described based on FIGS. 4 to 9.
  • the heat exchanger 1B is provided with a plurality of plate-like fins 30B, a plurality of heat transfer tubes 20B, a header 40B, and an inter-row connecting member 45B.
  • the heat exchanger 1B is a heat exchanger having a two-row structure, and includes the upwind heat exchanger 41B, the downwind heat exchanger 42B, the upwind header 40B-1, the downwind header 40B-2, and , And inter-row connection member 45B.
  • the windward header 40B-1 and the windward header 40B-2 may be collectively referred to as a header 40B.
  • the upwind side heat exchanger 41B and the downwind side heat exchanger 42B are similarly configured. In the following, when the heat exchanger 1B is described, it is assumed that both the upwind side heat exchanger 41B and the downwind side heat exchanger 42B are described.
  • the windward header 40B-1 and the windward header 40B-2 are attached to the paper right side of the windward heat exchanger 41B and the paper right side of the windward heat exchanger 42B.
  • the inter-row connecting member 45B is attached to the left side of the windward side heat exchanger 41B as viewed in the drawing and the left side of the windward side heat exchanger 42B as viewed.
  • the heat exchanger 1B is produced.
  • a plurality of tube attachment portions 40Ba to which the heat transfer tubes 20B are attached are formed in the windward header 40B-1 at a predetermined interval (pitch P1).
  • a plurality of tube attachment portions 40Bb to which the heat transfer tubes 20B are attached are formed at a predetermined interval (pitch P1).
  • the plurality of heat transfer tubes 20B are attached to penetrate through the plurality of through holes 31B formed in the fins 30B, and intersect with the fins 30B. As shown in FIG. 6, the heat transfer tube 20B is configured to have a flat cross-sectional shape.
  • the plurality of heat transfer tubes 20B are arranged at predetermined intervals in a step direction (vertical direction in the drawing) orthogonal to the flow direction of the refrigerant.
  • the distance in the direction of gravity of the heat transfer tubes 20B vertically adjacent to each other is constant at the pitch P2 of the adjacent through holes 31B of the fins 30B.
  • the heat transfer tube 20B is made of aluminum or an aluminum alloy.
  • FIG. 5 shows an example in which the number of heat transfer tubes 20B is eight, the number of heat transfer tubes 20B is not particularly limited.
  • the symbols shown in FIG. 4 to FIG. 9 are similarly used in the following drawings.
  • a region where the through holes 31B of the fins 30B are formed is referred to as a heat transfer tube region 31R.
  • regions at both ends in the short direction of the fins 30B and not divided by the through holes 31B and in which the fins 30B extend in the longitudinal direction are referred to as fin regions 32R.
  • the fins 30 ⁇ / b> B are formed of rectangular plate members having long sides and short sides.
  • the fins 30B have a pitch P1 in the longitudinal direction, and a plurality of through holes 31B are formed through the heat transfer tube area 31R.
  • the peripheral portion of the through hole 31B functions as a fin collar.
  • the fin collar in the longitudinal direction of the through hole 31B is referred to as a first fin collar 311, and the fin collar in the lateral direction of the through hole 31B is referred to as a second fin collar 312.
  • the fin pitch P3 which is an interval of the plurality of fins 30B is defined by the second fin collar 312.
  • FIG. 7 shows a state in which the through holes 31B have a rectangular shape in which the short direction of the fins 30B is a long side and the longitudinal direction of the fins 30B is a short side.
  • the specific shape of the through hole 31B is not specified, and the through hole 31B may have any shape as long as the heat transfer tube 20B can be inserted.
  • the fins 30B are made of aluminum or an aluminum alloy.
  • the through hole 31B has a rectangular shape, the shape is not specified.
  • the long side direction of the fin 30B is referred to as the longitudinal direction
  • the short side direction is referred to as the short direction.
  • the heat transfer tube 20B will be described in detail. As shown in FIG. 6, the heat transfer tube 20B is formed in a shape in which the lateral width (the length in the cross sectional major axis direction) is larger than the longitudinal width (the length in the cross sectional minor axis direction).
  • the plurality of heat transfer tubes 20B have the direction of the major axis of the cross section as the flow direction of the fluid flowing between the fins 30B, and are arranged at predetermined intervals in the step direction (vertical direction in the drawing) orthogonal to the flow direction.
  • the cross-sectional long axis of the heat transfer tube 20B that is, a portion extending in the width direction (short direction) of the fins 30B may be referred to as the width direction of the heat transfer tube 20B.
  • the heat transfer tube 20B shown in FIG. 6 will be described by way of example in the case of a flat tube having a flat width (length in the cross sectional major axis direction) larger than the vertical width (length in the cross axis minor axis direction). It is not necessary for the heat transfer tube 20B to be strictly formed in a flat shape, as long as the heat transfer tube 20B has a shape having a larger horizontal width than the vertical width.
  • the heat transfer tube 20B includes an upper surface 21a including an upper portion, a lower surface 21c including a lower portion, and one side portion 21b including one end in the width direction (the end on the right side in FIG. 6); It has the other side 21 d including the other end in the width direction (the end on the left side in the drawing of FIG. 6).
  • the upper surface 21a, the lower surface 21c, the one side portion 21b, and the other side portion 21d are collectively referred to as an outer wall 21.
  • FIG. 6 shows an example in which the upper surface 21a and the lower surface 21c are parallel to each other, at least one of the upper surface 21a and the lower surface 21c may be inclined so as not to be parallel to each other.
  • the cross-sectional shape of the heat transfer tube 20B may be elliptical or the like.
  • the heat transfer tube 20B also has a plurality of inner walls 22.
  • the plurality of inner walls 22 are formed to partition the internal space of the heat transfer tube 20B.
  • a plurality of inner holes 23 partitioned in the inner wall 22 will be formed.
  • the inner hole 23 functions as an internal flow path through which the refrigerant flows.
  • a groove or a slit may be formed on the inner surface of the heat transfer tube 20B including the inner wall 22.
  • FIG. 10 is a schematic perspective view showing a configuration example of the header 40 provided in the heat exchanger according to the first embodiment.
  • FIG. 11 is a schematic cross-sectional view showing an example of the cross-sectional configuration of the header 40 provided in the heat exchanger according to the first embodiment.
  • FIG. 12 is a schematic cross-sectional view showing another example of the cross-sectional configuration of the header 40 provided in the heat exchanger according to the first embodiment.
  • the heat transfer pipe 20A and the heat transfer pipe 20B may be collectively referred to as the heat transfer pipe 20.
  • the fins 30A and the fins 30B may be collectively referred to as fins 30.
  • the through holes 31A and the through holes 31B may be collectively referred to as the through holes 31 in some cases.
  • a cylindrical header 40-1 communicating with the inside can be adopted.
  • the cylindrical header 40-1 has a cylindrical portion 46 in which an internal space 44 serving as a flow passage of the heat exchange fluid is formed. That is, the cylindrical header 40-1 is a hollow header.
  • the outer shell of the cylindrical portion 46 is formed by the outer wall portion 41. Further, in the outer wall portion 41, a plurality of heat transfer pipe connection portions 43 to which the heat transfer pipe 20B is connected are formed.
  • the shape of the heat transfer tube connection portion 43 is such that the heat transfer tube 20B can be directly connected.
  • the heat transfer pipe connection portion 43 may have a circular shape. That is, the shape of the heat transfer tube connection part 43 should just be a shape according to the shape of the heat transfer tube to connect.
  • the circular pipe joint will be described with reference to FIG.
  • the cross-sectional long axis of the heat transfer tube 20B is da
  • the number of the inner holes 23 is n
  • the thickness of the outer wall 21 is tp
  • the required withstand pressure is P.
  • the inner diameter of the cylindrical header 40-1 is dh
  • the thickness of the outer wall portion 41 is th
  • the tensile strength is ⁇ .
  • the cylindrical header 40-1 is configured such that dh / th is 2 ⁇ / ⁇ P * (da / n / tp-1) ⁇ or more. By doing this, the thickness of the outer wall portion 41 of the cylindrical header 40-1 can be made smaller compared to the inner diameter of the cylindrical header 40-1, and the material cost can be reduced accordingly.
  • the inner diameter of the cylindrical header 40-1 means the inner diameter of the cylindrical portion 46.
  • a laminated header 40-2 having a plurality of plate-like bodies 90 can be adopted.
  • the plate-like body 90 is formed by alternately laminating a first plate-like member 91a to a first plate-like member 91d to be a bear member and a second plate-like member 92a to a second plate-like member 92d to be a clad material. It is formed. On the outermost side in the stacking direction of the plate-like body 90, the first plate-like member 91a and the first plate-like member 91e are stacked.
  • first plate-like member 91a to the first plate-like member 91e may be collectively referred to as a plurality of first plate-like members 91.
  • second plate-like member 92a to the second plate-like member 92d may be collectively referred to as a plurality of second plate-like members 92.
  • the plurality of first plate members 91 are made of aluminum.
  • the brazing material is not applied to the plurality of first plate members 91.
  • a through hole serving as the distribution / merging flow path 65 is formed in each of the plurality of first plate-like members 91.
  • the through holes penetrate the front and back of the plurality of first plate members 91.
  • the through holes formed in the plurality of first plate members 91 form a flow passage for the heat exchange fluid. Function as a part of the distribution / merging channel 65.
  • the plurality of second plate-like members 92 are made of aluminum, and are formed thinner than the plurality of first plate-like members 91.
  • a brazing material is applied to at least the front and back surfaces of the plurality of second plate members 92.
  • Each of the plurality of second plate-like members 92 is formed with a through hole serving as the distribution and merging channel 65.
  • the through holes penetrate the front and back of the plurality of second plate members 92.
  • the through holes formed in the second plate-like members 92 with the number of hooks formed by stacking the plurality of first plate-like members 91 and the plurality of second plate-like members 92 are flow channels for the heat exchange fluid It functions as a part of the distribution / merging channel 65 which
  • connection pipe 61a is connected to the through hole formed in the first plate-like member 91a.
  • a nozzle or the like may be provided on the surface of the first plate member 91 a on the inflow side of the refrigerant, and the connection pipe 61 a may be connected via the nozzle or the like.
  • the inner peripheral surface of the through hole formed in the first plate-like member 91a is shaped to fit with the outer peripheral surface of the connection pipe 61a, and the connection pipe 61a is directly connected without using a die or the like. Good.
  • connection pipe 62a is connected to the through hole formed in the first plate member 91e.
  • a nozzle or the like may be provided on the surface of the first plate-like member 91 e on which the refrigerant flows, and the connection pipe 62 a may be connected via the nozzle or the like.
  • the inner peripheral surface of the through hole formed in the first plate-like member 91e is shaped to fit with the outer peripheral surface of the connection pipe 62a, and the connection pipe 62a may be directly connected without using a base or the like. Good.
  • the connection piping 62a may be connected by inserting the connection piping 62a so as to reach the through hole of the first plate-like member 91d.
  • the through holes formed in the first plate-like member 91 b and the first plate-like member 91 c are formed to pass through in a Z-shaped flow passage cross section.
  • a flow-path cross section is a cross section which cut the flow path in the direction orthogonal to the flow of the fluid.
  • FIG. 12 illustrates the case where the distribution / merging flow channel 65 has four fluid outlet portions for one fluid inlet portion, the number of branches is limited to four. is not.
  • the refrigerant in the upper stage branch portion 60a when the refrigerant flows in from the connection pipe 61a will be described.
  • the refrigerant having flowed through the connection pipe 61a flows into the inside of the upper stage branch portion 60a as a fluid inlet portion through the through hole of the first plate-like member 91a.
  • the refrigerant flows into the through hole of the second plate-like member 92a.
  • the refrigerant that has flowed into the through hole of the second plate member 92a flows into the center of the through hole of the first plate member 91b.
  • the refrigerant that has flowed into the center of the through hole of the first plate member 91b hits the surface of the second plate member 92d stacked adjacent to it and branches, and flows to the end of the through hole of the first plate member 91b.
  • the refrigerant reaching the end of the through hole of the first plate member 91b passes through the through hole of the second plate member 92b and flows into the center of the through hole of the first plate member 91c.
  • the refrigerant that has flowed into the center of the through hole of the first plate member 91c strikes the surface of the adjacent second laminated plate member 92c and branches, and flows to the end of the through hole of the first plate member 91c.
  • the refrigerant reaching the end of the through hole of the first plate member 91c passes through the through hole of the second plate member 92c and flows into the through hole of the first plate member 91d.
  • the refrigerant that has flowed into the through hole of the first plate member 91d passes through the through hole of the second plate member 92d, and is transferred to the heat transfer pipe 20B through the connection pipe 62a located in the through hole of the first plate member 91e. To flow.
  • the header 40 As described above, by forming the header 40 as the stacked header 40-2, uniformity of distribution of the refrigerant in the header 40 can be improved.
  • FIG. 13 is a flow chart schematically showing the steps of the method of manufacturing the heat exchanger 1B.
  • FIG. 14 is an explanatory view for explaining an example of how to attach the heat transfer tube to the sealing device 70 in the method of manufacturing the heat exchanger 1B.
  • the manufacturing method of the heat exchanger 1B is demonstrated based on FIG.13 and FIG.14. In addition, although the manufacturing method of the heat exchanger 1B is demonstrated here, it is applicable to the heat exchanger 1A similarly.
  • the method of manufacturing the heat exchanger 1B is roughly divided into two steps (a first step 51 and a second step 52).
  • the preparation process 50 is illustrated as a pre-process of the first process 51.
  • the preparation step 50 is a step of inserting the heat transfer tube 20B into the through hole 31B of the fin 30B and performing temporary assembly of the heat exchanger 1B.
  • the plurality of heat transfer pipes 20B are attached in parallel to the plurality of fins 30B arranged in parallel at the fin pitch P3. In this state, the first step 51 is performed.
  • the first step 51 is a step of expanding the heat transfer tube 20B by applying pressure to the inside of the heat transfer tube 20B so as to push and spread the heat transfer tube 20B from the inside.
  • the high pressure gas container 60 and the sealing device 70 are attached to both ends of the heat transfer tube 20B in the direction in which the fins 30B are arranged.
  • the high pressure gas is caused to flow into the heat transfer tube 20B.
  • the high pressure gas acts to push and spread the heat transfer pipe 20B from the inside of the heat transfer pipe 20B, and the heat transfer pipe 20B is expanded. That is, in the first step 51, the plurality of heat transfer tubes 20B are expanded without the header 40.
  • the sealing device 70 has an insertion portion 71 into which the heat transfer tube 20B is inserted.
  • the insertion portion 71 is formed with a recess 72 which is recessed toward the outer periphery.
  • a convex mounting portion 24 protruding outward is provided on the outer periphery of the end of the heat transfer tube 20B on the sealing device 70 side. Then, when the heat transfer tube 20B is attached to the sealing device 70, the mounting portion 24 of the heat transfer tube 20B is fitted into the recess 72 of the sealing device 70. By this, it is possible to fix the heat transfer tube 20B to the sealing device 70.
  • the specific configuration of the sealing device 70 is not specified, as long as the heat transfer tube 20B can be fixed.
  • the modification of the instrument 70 for sealing it demonstrates in FIG.15 and FIG.16.
  • the second step 52 is a step of joining the header 40 to the expanded plurality of heat transfer tubes 20B by brazing or the like.
  • the heat transfer tube 20B When the heat transfer tube 20B is expanded in the first step 51, the heat transfer tube 20B may be brought into close contact with the fins 30B, but in the second step 52, the heat transfer tube 20B and the header 40 are brazed simultaneously Both the heat pipe 20B and the fins 30B may be brazed.
  • a brazing material may be applied or laminated on the surface of at least one of the heat transfer tube 20B and the fins 30B, and the heat transfer tube 20B and the fins 30B may be brazed in the second step 52.
  • the adhesion between the heat transfer tube 20B and the fins 30B can be enhanced, and the performance of the heat exchanger 1B can be improved.
  • the heat transfer tube 20B may be in close contact with the fins 30B by any one of the means, or the heat transfer tube 20B may be in close contact with the fins 30B by both means.
  • FIG. 15 is an explanatory diagram for explaining another example of how to attach the heat transfer tube to the sealing device 70 in the method of manufacturing the heat exchanger 1B.
  • FIG. 16 is an explanatory view for explaining still another example of how the heat transfer tube is attached to the sealing device 70 in the method of manufacturing the heat exchanger 1B. Based on FIG.15 and FIG.16, the modification of the instrument 70 for sealing used by the manufacturing method of the heat exchanger 1B is demonstrated.
  • the heat transfer tube 20B is attached to the sealing device 70 by directly inserting the heat transfer tube 20B into the sealing device 70 as an example.
  • the heat transfer tube 20B is attached to the sealing device 70 via the circular pipe joint 80, instead of directly inserting the heat transfer tube 20B into the sealing device 70.
  • the circular pipe joint 80 is for connecting the heat transfer pipe 20B and the sealing device 70. Specifically, the circular pipe joint 80 converts the cross-sectional shape of the heat transfer tube 20B into a shape that can be connected to the sealing device 70.
  • the case where the circular pipe joint 80 connects the heat transfer pipe 20B having a flat cross-sectional shape to a sealing device 70 to which a pipe having a circular cross-sectional shape can be connected is shown as an example.
  • the sealing device 70 is configured to press the circular pipe portion from the inner wall side and the outer wall side by the insertion portion 71 with respect to the circular pipe joint 80 connected to the heat transfer pipe 20B.
  • the circular pipe portion of the circular pipe joint 80 is a portion having a circular cross section which is inserted into the sealing device 70 of the circular pipe joint 80.
  • the heat transfer tube 20B can be attached to the sealing device 70 by pressing this portion with the sealing device 70.
  • the sealing device 70 having such a configuration, in the second step 52, the circular tube portion of the circular pipe joint 80 is fixed more firmly from the inside and the outside by the sealing device 70 and the circular pipe joint 80. As it can be done, the degree of sealing is increased, and the leakage of high pressure gas can be further suppressed. Therefore, it is possible to improve manufacturing safety while improving the pressurizing efficiency in the second step 52. Moreover, highly reliable heat exchanger 1B can be manufactured efficiently. Thus, the reliability of the created heat exchanger 1B is improved.
  • the circular pipe joint 80 corresponds to the “joint” of the present invention. However, even when the heat transfer tube 20A is used, the heat transfer tube 20A may be attached to the sealing device 70 through a joint. In this case, the configuration of the joint corresponds to the heat transfer tube 20A and the sealing device 70.
  • the heat transfer tube 20B is attached to the sealing device 70 by directly inserting the heat transfer tube 20B into the sealing device 70.
  • the case where the attachment portion 24 is provided to the heat transfer tube 20B has been described as an example, but in FIG. 16, a part of the inner wall 22 of the end of the heat transfer tube 20B on the sealing device 70 side is removed There is.
  • the heat transfer tube 20 B is inserted into the insertion portion 71 of the sealing device 70.
  • the sealing device 70 is configured to press the heat transfer tube 20B from the inner wall side and the outer wall side by the insertion portion 71 in a region where the inner wall 22 of the heat transfer tube 20B does not exist. By this, it is possible to fix the heat transfer tube 20B to the sealing device 70.
  • the sealing device 70 By using the sealing device 70 having such a configuration, in the second step 52, the sealing device 70 enables the region where the inner wall 22 of the heat transfer tube 20B is not present to be fixed more firmly from the inside and the outside. Therefore, the degree of sealing is increased, and the leakage of high pressure gas can be further suppressed. Therefore, it is possible to improve manufacturing safety while improving the pressurizing efficiency in the second step 52. Moreover, highly reliable heat exchanger 1B can be manufactured efficiently. Thus, the reliability of the created heat exchanger 1B is improved.
  • FIG. 17 is a view showing a state in which the plate-like member to be the fins 30B provided in the heat exchanger 1B is cut.
  • FIG. 18 is a view showing a state in which the heat transfer pipe 20B is inserted into the through hole 31B of the fin 30B provided in the heat exchanger 1B.
  • FIG. 19 is a view showing a state in which the heat transfer pipe 20B inserted into the through hole 31B of the fin 30B provided in the heat exchanger 1B is expanded.
  • the peripheral portion of the through hole 31B functions as a fin collar.
  • a cut is provided in a portion to be the heat transfer tube region 31R of the plate-like member 30a.
  • a notch 311a is provided at the boundary of the portion where the first fin collar 311 of the plate member 30a is cut and raised.
  • the notch 312a is provided in the boundary of the part which cuts and raises the 2nd fin collar 312 of the plate-shaped member 30a.
  • the plate-like member 30a is bent in one direction via the cuts 311a and the cuts 312a.
  • the figure shows a state in which the plate-like member 30a is bent to the front side of the drawing sheet.
  • the peripheral portion of the through hole 31B is cut and raised like a tongue.
  • the tongue-like portion cut and raised in the longitudinal direction of the fin 30B through the notch 311a functions as the first fin collar 311.
  • the tongue-like portion cut and raised in the short direction of the fin 30 B through the notch 312 a functions as the second fin collar 312.
  • released functions as a through-hole 31B.
  • the first fin collar 311 and the first fin collar 311 have a length L1 in the short direction of the fins 30B of the first fin collar 311 greater than the length L2 in the longitudinal direction of the fins 30B of the second fin collar 312.
  • Two fin collars 312 are formed. That is, the cut 311a and the cut 312a are formed so as to satisfy the relationship of length L1> length L2. Further, the gap length L3 between the second fin collar 312 and the heat transfer pipe 20B inserted into the through hole 31B is the gap length L4 between the first fin collar 311 and the heat transfer pipe 20B inserted into the through hole 31B. It is set larger than.
  • the heat transfer pipe 20B is inserted into the through hole 31B.
  • the heat transfer pipe 20B is expanded. In this way, when the heat transfer tube 20B is expanded in the first step 51, the first fin collar 311 is in close contact with the surface of the outer wall 21 in the longitudinal direction of the cross section of the heat transfer tube 20B.
  • the first fin collar 311 can ensure the adhesion to the fins 30B on the longitudinal surface of the heat transfer tube 20B, and improve the heat exchange efficiency.
  • the heat transfer pipe 20B can be expanded by the second fin collar 312 while maintaining the distance between the adjacent fins 30B, and the reliability of the heat exchanger 1B can be secured.
  • the longitudinal surface of the heat transfer tube 20B means the surface of the outer wall 21 of the heat transfer tube 20B in the flow direction of the refrigerant.
  • FIG. 20 is a schematic view schematically showing an example of the shape of the end portion of the heat transfer tube 20B provided in the heat exchanger 1B.
  • FIG. 21 is a schematic view showing a state in which the cross section of the X region shown in FIG. 20 is enlarged. Based on FIG. 20 and FIG. 21, another example of the joining method of the heat exchanger tube 20B and the fin 30B is demonstrated. In addition, in FIG. 20, the state at the time of inserting the heat exchanger tube 20B in the fin 30B is illustrated.
  • the plurality of heat transfer pipes 20B are attached in parallel to the through holes 31B of the plurality of fins 30B arranged in parallel at the fin pitch P3.
  • one fin 30B is illustrated as an example.
  • a chamfered portion 21A is formed on the outer wall 21 at the insertion-side end of the heat transfer tube 20B to improve the insertability of the heat transfer tube 20B into the fin 30B.
  • the chamfered portion 21A is formed such that an angle ⁇ between a straight line L4 extending from the tube inner point A to the tube outer end B of the heat transfer tube 20B and the longitudinal direction (L5) of the fin 30B is an acute angle.
  • the insertability of the heat transfer tube 20B into the fins 30B can be improved. That is, when the heat transfer tubes 20B are inserted into the fins 30B, it is possible to prevent the heat transfer tubes 20B and the fins 30B from contacting each other and damaging each other. In addition, since the end on the insertion side of the heat transfer tube 20B is reduced, the insertion to the fin 30B is facilitated. Therefore, it is possible to improve manufacturing safety. Moreover, highly reliable heat exchanger 1B can be manufactured efficiently. Thus, the reliability of the created heat exchanger 1B is improved.
  • the header 40 is configured such that dh / th is 2 ⁇ / ⁇ P * (da / n / tp-1) ⁇ or more. Therefore, in the heat exchanger according to the first embodiment, the thickness of the outer wall portion 41 of the header 40 can be smaller than the inner diameter of the header 40. Therefore, according to the heat exchanger according to the first embodiment, it is possible to reduce the material cost by which the thickness of the outer wall portion 41 of the header 40 can be reduced.
  • the heat transfer tube 20 is brazed to the header 40 having a fluid flow passage inside. That is, in the method of manufacturing the heat exchanger according to the first embodiment, the pressurizing path can be sealed at the time of high-pressure gas supply without connecting the heat transfer pipe 20 to the header 40. Therefore, according to the method of manufacturing a heat exchanger according to the first embodiment, it is possible to expand the plurality of heat transfer tubes 20 without the header 40, and the header 40 has a pressure resistance equal to or higher than that of the heat transfer tubes 20. There is no need to have That is, the thickness of the outer wall portion 41 can be made thinner than the inner space 44 of the header 40. Thereby, the reliability of the heat exchanger according to the first embodiment can be secured while suppressing the weight increase of the heat exchanger according to the first embodiment.
  • the heat transfer tube 20 and the fin 30 are also brazed, so the adhesion between the heat transfer tube 20 and the fin 30 Can enhance the performance of the heat exchanger.
  • the length L1 of the first fin collar 311 is larger than the length L2 of the second fin collar 312, and the gap length L3 is the gap length L4. It is set larger than. Therefore, according to the method of manufacturing the heat exchanger according to the first embodiment, the adhesion between the heat transfer tube 20 and the fins 30 can be enhanced while maintaining the distance between the adjacent fins 30, and the performance of the heat exchanger can be improved. Can be improved.
  • the heat transfer tube 20 is fixed to the sealing device 70 by fitting the attachment portion 24 of the heat transfer tube 20 into the recess 72, the heat transfer tube 20 is sealed. It can be firmly fixed by the device 70, the degree of sealing is increased, and leakage of high pressure gas can be further suppressed. Therefore, according to the method of manufacturing a heat exchanger according to the first embodiment, it is possible to improve manufacturing safety while improving the pressurizing efficiency in the second step 52. In addition, a highly reliable heat exchanger can be manufactured efficiently.
  • the circular pipe portion of the circular pipe joint 80 is pressed down by the insertion portion 71 from the inner wall side and the outer wall side, so that the circular pipe joint 80 is reinforced by the sealing device 70.
  • the degree of sealing is increased, and the leakage of high pressure gas can be further suppressed. Therefore, according to the method of manufacturing a heat exchanger according to the first embodiment, it is possible to improve manufacturing safety while improving the pressurizing efficiency in the second step 52. In addition, a highly reliable heat exchanger can be manufactured efficiently.
  • the heat transfer tube 20 is inserted into the sealing device 70 by the region where the inner wall 22 of the heat transfer tube 20 is not provided being pressed from the inner wall side and the outer wall side by the insertion portion 71. It is fixed. Therefore, since the heat transfer tube 20 can be firmly fixed by the sealing device 70, the degree of sealing can be increased and leakage of high pressure gas can be further suppressed. Therefore, according to the method of manufacturing a heat exchanger according to the first embodiment, it is possible to improve manufacturing safety while improving the pressurizing efficiency in the second step 52. In addition, a highly reliable heat exchanger can be manufactured efficiently.
  • FIG. 22 is a schematic configuration diagram showing an example of the refrigerant circuit configuration of the refrigeration cycle apparatus 100. As shown in FIG. The case where the refrigeration cycle apparatus 100 is an air conditioner will be described as an example. In FIG. 22, the flow of the refrigerant during the cooling operation is indicated by a broken arrow, and the flow of the refrigerant during the heating operation is indicated by the solid arrow.
  • the refrigeration cycle apparatus 100 includes the compressor 101, the first heat exchanger 102, the first fan 105, the expansion device 103, the second heat exchanger 104, the second fan 106, and the flow path switching.
  • a device 107 is provided.
  • the compressor 101, the first heat exchanger 102, the expansion device 103, the second heat exchanger 104, and the flow path switching device 107 are connected by the refrigerant pipe 110 to form a refrigerant circuit.
  • the first heat exchanger 102 and the second heat exchanger 104 is the heat exchanger according to the first embodiment.
  • the compressor 101 compresses a refrigerant.
  • the refrigerant compressed by the compressor 101 is discharged and sent to the flow path switching device 107.
  • the compressor 101 can be configured by a rotary compressor, a scroll compressor, a screw compressor, a reciprocating compressor, or the like.
  • the first heat exchanger 102 functions as a condenser during heating operation and functions as an evaporator during cooling operation.
  • the first heat exchanger 102 is a finned tube type heat exchanger, a microchannel heat exchanger, a shell and tube type heat exchanger, a heat pipe type heat exchanger, a double pipe type heat exchanger, or a plate heat exchanger. And so on.
  • the first heat exchanger 102 is a finned tube heat exchanger.
  • the expansion device 103 expands and reduces the pressure of the refrigerant having passed through the first heat exchanger 102 or the second heat exchanger 104.
  • the expansion device 103 may be configured by an electric expansion valve or the like capable of adjusting the flow rate of the refrigerant.
  • As the expansion device 103 not only a motorized expansion valve but also a mechanical expansion valve employing a diaphragm in a pressure receiving portion, a capillary tube or the like can be applied.
  • the second heat exchanger 104 functions as an evaporator during heating operation and functions as a condenser during cooling operation.
  • the first heat exchanger 102 is a finned tube type heat exchanger, a microchannel heat exchanger, a shell and tube type heat exchanger, a heat pipe type heat exchanger, a double pipe type heat exchanger, or a plate heat exchanger. And so on.
  • the second heat exchanger 104 is a finned tube heat exchanger.
  • the flow path switching device 107 switches the flow of the refrigerant in the heating operation and the cooling operation. That is, the flow path switching device 107 is switched to connect the compressor 101 and the first heat exchanger 102 during heating operation, and connects the compressor 101 and the second heat exchanger 104 during cooling operation. It is switched.
  • the flow path switching device 107 may be configured by a four-way valve. However, a combination of a two-way valve or a three-way valve may be employed as the flow path switching device 107.
  • the first fan 105 is attached to the first heat exchanger 102 and supplies air, which is a heat exchange fluid, to the first heat exchanger 102.
  • the second fan 106 is attached to the second heat exchanger 104 and supplies air, which is a heat exchange fluid, to the second heat exchanger 104.
  • the cooling operation performed by the refrigeration cycle apparatus 100 will be described.
  • the compressor 101 when the compressor 101 is driven, the refrigerant in a high temperature / high pressure gas state is discharged from the compressor 101.
  • the refrigerant flows according to the broken arrow.
  • the high temperature / high pressure gas refrigerant (single phase) discharged from the compressor 101 flows into the second heat exchanger 104 functioning as a condenser via the flow path switching device 107.
  • the second heat exchanger 104 heat exchange is performed between the inflowing high-temperature and high-pressure gas refrigerant and the air supplied by the second fan 106, and the high-temperature and high-pressure gas refrigerant is condensed to a high pressure liquid. It becomes a refrigerant (single phase).
  • the high-pressure liquid refrigerant delivered from the second heat exchanger 104 is converted by the expansion device 103 into a two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant.
  • the two-phase refrigerant flows into the first heat exchanger 102 that functions as an evaporator.
  • heat exchange is performed between the inflowing two-phase refrigerant and the air supplied by the first fan 105, and the liquid refrigerant in the two-phase refrigerant is evaporated to evaporate. It is a low pressure gas refrigerant (single phase). By this heat exchange, the air conditioning target space is cooled.
  • the low-pressure gas refrigerant sent from the first heat exchanger 102 flows into the compressor 101 via the flow path switching device 107, is compressed and becomes a high-temperature and high-pressure gas refrigerant, and is discharged again from the compressor 101. Hereinafter, this cycle is repeated.
  • the heating operation performed by the refrigeration cycle apparatus 100 will be described.
  • the compressor 101 when the compressor 101 is driven, the refrigerant in a high temperature / high pressure gas state is discharged from the compressor 101.
  • the refrigerant flows according to the solid arrow.
  • the high temperature / high pressure gas refrigerant (single phase) discharged from the compressor 101 flows into the first heat exchanger 102 functioning as a condenser via the flow path switching device 107.
  • the first heat exchanger 102 heat exchange is performed between the inflowing high temperature / high pressure gas refrigerant and the air supplied by the first fan 105, and the high temperature / high pressure gas refrigerant is condensed to a high pressure It becomes a refrigerant (single phase). By this heat exchange, the air conditioning target space is heated.
  • the high-pressure liquid refrigerant delivered from the first heat exchanger 102 is converted by the expansion device 103 into a two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant.
  • the two-phase refrigerant flows into the second heat exchanger 104 which functions as an evaporator.
  • heat exchange is performed between the inflowing two-phase refrigerant and the air supplied by the second fan 106, and the liquid refrigerant in the two-phase refrigerant is evaporated to evaporate. It is a low pressure gas refrigerant (single phase).
  • the low-pressure gas refrigerant sent from the second heat exchanger 104 flows into the compressor 101 via the flow path switching device 107, is compressed and becomes a high-temperature and high-pressure gas refrigerant, and is discharged again from the compressor 101. Hereinafter, this cycle is repeated.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

La présente invention concerne un échangeur de chaleur comprenant : une pluralité de tuyaux de transfert de chaleur présentant une forme plate en section transversale et comportant une pluralité de trous internes formés à leur intérieur ; une pluralité d'ailettes reliées à la pluralité de tuyaux de transfert de chaleur ; et un collecteur relié à la pluralité de tuyaux de transfert de chaleur et comportant à son intérieur un circuit d'écoulement pour la circulation d'un fluide. Lorsque da est la longueur de l'axe longitudinal dans la section transversale des tuyaux de transfert de chaleur, n est le nombre de trous internes dans les tuyaux de transfert de chaleur, tp est l'épaisseur de la paroi externe des tuyaux de transfert de chaleur, P est la pression de résistance requise des tuyaux de transfert de chaleur, dh est le diamètre interne du collecteur, th est l'épaisseur de la partie paroi externe du collecteur, et σ est la résistance à la traction du collecteur, le rapport dh/th du collecteur n'est pas inférieur à 2σ/{P*(da/n/tp-1)}.
PCT/JP2017/034329 2017-09-22 2017-09-22 Échangeur de chaleur, dispositif à cycle frigorifique, et procédé de fabrication d'échangeur de chaleur Ceased WO2019058514A1 (fr)

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JP2019542917A JP6880206B2 (ja) 2017-09-22 2017-09-22 熱交換器の製造方法

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020262378A1 (fr) * 2019-06-28 2020-12-30 ダイキン工業株式会社 Échangeur de chaleur et dispositif de pompe à chaleur
CN116507871A (zh) * 2020-10-20 2023-07-28 三菱电机株式会社 热交换器和制冷循环装置
WO2026022698A1 (fr) 2024-07-25 2026-01-29 Lu-Ve S.P.A. Échangeur de chaleur à air du type amélioré, procédé et appareil de fabrication de celui-ci

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5450467A (en) * 1977-09-09 1979-04-20 Ferodo Sa Assemblly consisting of fins and tubes for use as heat exchanger and method of making same
JPS6046866A (ja) * 1983-08-25 1985-03-13 Mitsubishi Heavy Ind Ltd フインと管の接続方法
JPH05187786A (ja) * 1992-02-20 1993-07-27 Nippondenso Co Ltd 空調装置用コンデンサ
JPH07127985A (ja) * 1993-11-04 1995-05-19 Toshiba Corp 熱交換器およびその製造方法
JPH09192765A (ja) * 1996-01-18 1997-07-29 Nippon Light Metal Co Ltd プレートフィン型熱交換器における偏平状熱交換管の作製方法
JP2004333028A (ja) * 2003-05-08 2004-11-25 Denso Corp 熱交換器
JP2004353954A (ja) * 2003-05-29 2004-12-16 Denso Corp 熱交換器
JP2005221117A (ja) * 2004-02-04 2005-08-18 Hidaka Seiki Kk 熱交換器の製造方法
JP2007093036A (ja) * 2005-09-27 2007-04-12 Matsushita Electric Ind Co Ltd 熱交換器及びその製造方法並びにその製造装置
JP2008232600A (ja) * 2007-03-23 2008-10-02 Mitsubishi Electric Corp 熱交換器及びこの熱交換器を備えた空気調和機
JP2009293849A (ja) * 2008-06-04 2009-12-17 Mitsubishi Electric Corp 熱交換器、及びこの熱交換器を用いた空気調和機
JP2015055398A (ja) * 2013-09-11 2015-03-23 ダイキン工業株式会社 熱交換器のロウ付け方法
JP2017026281A (ja) * 2015-07-28 2017-02-02 サンデンホールディングス株式会社 熱交換器
JP2017122549A (ja) * 2016-01-08 2017-07-13 株式会社デンソー 熱交換器及びその製造方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57195545A (en) * 1981-05-26 1982-12-01 Sanyo Electric Co Ltd Tube expanding jig for finned heat exchanger
JP2773459B2 (ja) * 1991-04-12 1998-07-09 日立電線株式会社 フィンアンドチューブ式熱交換器の製造方法
JPH06114543A (ja) * 1992-10-02 1994-04-26 Hitachi Cable Ltd 熱交換器の製造方法
JP3329222B2 (ja) * 1997-03-06 2002-09-30 日立電線株式会社 熱交換器の製造方法
JP2002361346A (ja) * 2001-06-05 2002-12-17 Fujitsu General Ltd 熱交換器の製造方法
JP4109444B2 (ja) * 2001-11-09 2008-07-02 Ｇａｃ株式会社 熱交換器およびその製造方法

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5450467A (en) * 1977-09-09 1979-04-20 Ferodo Sa Assemblly consisting of fins and tubes for use as heat exchanger and method of making same
JPS6046866A (ja) * 1983-08-25 1985-03-13 Mitsubishi Heavy Ind Ltd フインと管の接続方法
JPH05187786A (ja) * 1992-02-20 1993-07-27 Nippondenso Co Ltd 空調装置用コンデンサ
JPH07127985A (ja) * 1993-11-04 1995-05-19 Toshiba Corp 熱交換器およびその製造方法
JPH09192765A (ja) * 1996-01-18 1997-07-29 Nippon Light Metal Co Ltd プレートフィン型熱交換器における偏平状熱交換管の作製方法
JP2004333028A (ja) * 2003-05-08 2004-11-25 Denso Corp 熱交換器
JP2004353954A (ja) * 2003-05-29 2004-12-16 Denso Corp 熱交換器
JP2005221117A (ja) * 2004-02-04 2005-08-18 Hidaka Seiki Kk 熱交換器の製造方法
JP2007093036A (ja) * 2005-09-27 2007-04-12 Matsushita Electric Ind Co Ltd 熱交換器及びその製造方法並びにその製造装置
JP2008232600A (ja) * 2007-03-23 2008-10-02 Mitsubishi Electric Corp 熱交換器及びこの熱交換器を備えた空気調和機
JP2009293849A (ja) * 2008-06-04 2009-12-17 Mitsubishi Electric Corp 熱交換器、及びこの熱交換器を用いた空気調和機
JP2015055398A (ja) * 2013-09-11 2015-03-23 ダイキン工業株式会社 熱交換器のロウ付け方法
JP2017026281A (ja) * 2015-07-28 2017-02-02 サンデンホールディングス株式会社 熱交換器
JP2017122549A (ja) * 2016-01-08 2017-07-13 株式会社デンソー 熱交換器及びその製造方法

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020262378A1 (fr) * 2019-06-28 2020-12-30 ダイキン工業株式会社 Échangeur de chaleur et dispositif de pompe à chaleur
JP2021008973A (ja) * 2019-06-28 2021-01-28 ダイキン工業株式会社 熱交換器およびヒートポンプ装置
US11740026B2 (en) 2019-06-28 2023-08-29 Daikin Industries, Ltd. Heat exchanger and heat pump apparatus
CN116507871A (zh) * 2020-10-20 2023-07-28 三菱电机株式会社 热交换器和制冷循环装置
WO2026022698A1 (fr) 2024-07-25 2026-01-29 Lu-Ve S.P.A. Échangeur de chaleur à air du type amélioré, procédé et appareil de fabrication de celui-ci

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