EP3425321A1 - Heat exchanger and air conditioner - Google Patents
Heat exchanger and air conditioner Download PDFInfo
- Publication number
- EP3425321A1 EP3425321A1 EP17759597.2A EP17759597A EP3425321A1 EP 3425321 A1 EP3425321 A1 EP 3425321A1 EP 17759597 A EP17759597 A EP 17759597A EP 3425321 A1 EP3425321 A1 EP 3425321A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- header
- connection pipe
- header part
- flow passage
- heat exchanger
- 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.)
- Granted
Links
- 238000005192 partition Methods 0.000 claims abstract description 180
- 239000003507 refrigerant Substances 0.000 claims description 132
- 238000000638 solvent extraction Methods 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 39
- 238000012986 modification Methods 0.000 description 35
- 230000004048 modification Effects 0.000 description 35
- 239000007791 liquid phase Substances 0.000 description 17
- 239000012071 phase Substances 0.000 description 17
- 230000007423 decrease Effects 0.000 description 14
- 238000000265 homogenisation Methods 0.000 description 11
- 238000001816 cooling Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000005219 brazing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
-
- 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
- F28F9/0202—Header boxes having their inner space divided by partitions
- F28F9/0204—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
-
- 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
- F28D1/0535—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 the conduits having a non-circular cross-section
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
-
- 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
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/022—Tubular elements of cross-section which is non-circular with multiple channels
-
- 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
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/025—Tubular elements of cross-section which is non-circular with variable shape, e.g. with modified tube ends, with different geometrical features
-
- 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
- F28F9/0202—Header boxes having their inner space divided by partitions
- F28F9/0204—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
- F28F9/0209—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only transversal partitions
-
- 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
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0265—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
-
- 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
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/06—Derivation channels, e.g. bypass
Definitions
- the present invention relates to a heat exchanger and an air conditioner.
- a heat exchanger in which a plurality of heat transfer tubes extending in a horizontal direction are disposed with a gap left therebetween in a vertical direction and a fin is provided on an outer surface of each heat transfer tube, is known as a heat exchanger of an air conditioner. Both ends of the plurality of heat transfer tubes are connected to a pair of headers extending in the vertical direction, respectively.
- Such a heat exchanger is configured such that a refrigerant, which is introduced into one header out of the pair of headers and is circulated in the other header via the heat transfer tubes, turns back at the other header to return to the one header again via the heat transfer tubes, in order to secure a flow passage length for the refrigerant.
- the inside of the header at a turnback side is partitioned into a plurality of regions with a partition plate partitioning the inside of the header in the vertical direction. Accordingly, a refrigerant introduced in one region of the header via the heat transfer tubes returns to one header on an entrance side via the plurality of heat transfer tubes connected to the other region after being introduced into the other region of the header via a connection pipe.
- a heat exchanger including a connection pipe which has one main pipe portion and branch pipe portions that extend so as to branch off into two portions from the main pipe portion is disclosed in PTL 1.
- the main pipe portion is connected to one region in the header, and the branch pipe portions each are connected to any one of the two regions in the header.
- a refrigerant introduced in one region of the header via the heat transfer tubes is diverted and introduced into the other region of the two regions of the header via the main pipe portion and the branch pipe portions of the connection pipe.
- the heat exchanger is used as an evaporator, not the entire refrigerant introduced into one region of the header via heat transfer tubes evaporates, and the refrigerant is in a state of a gas-liquid two phase refrigerant, in which a liquid phase refrigerant and a gas phase refrigerant are mixed.
- a larger amount of a liquid phase refrigerant circulates only in some of the branch pipes depending on a disposed location of each branch pipe, and thus a deviation in the flow rate or the gas-liquid ratio of the refrigerant occurs between the branch pipes.
- a liquid phase refrigerant tends to concentrate only in the branch pipe located outside the bend.
- connection pipe of PTL 1 handling for avoiding interference between a plurality of connection pipes is complicated, and thus processing or brazing is difficult.
- processing or brazing is difficult.
- An object of the invention is to provide a heat exchanger which can suppress a performance decrease (efficiency decrease) and an air conditioner in which the heat exchanger is used.
- a heat exchanger including a plurality of first heat transfer tubes that allow a refrigerant to circulate therein and are arranged with a gap left therebetween, a first header part that has a cylindrical shape and has an internal space connected to each of the first heat transfer tubes in a communicating state, a plurality of second heat transfer tubes that allow the refrigerant to circulate therein and are arranged with a gap left therebetween, a second header part that has a cylindrical shape extending along an axis and has an internal space connected to each of the second heat transfer tubes in a communicating state, an in-second header partition plate that partitions the internal space of the second header part into two regions, and a connection pipe that has a connection pipe body having a first end connected to an outer circumferential surface of the first header part in a communicating state with the internal space of the first header part and a second end on an opposite side to the first end connected to an outer circumferential surface of the second header part in a communicating state with the internal
- connection pipe body since the opening of the second end of the connection pipe body straddles the two regions of the second header part, the refrigerant introduced in the connection pipe body from the first header part is introduced into each of the two regions. Accordingly, since there is only one connection portion of the connection pipe to each of the first header part and the second header part, the handling of the connection pipe is easy. In addition, an area occupied by the connection pipe can be made small compared to a case where the connection pipe branches off. Accordingly, a wide effective area of the heat exchanger, in which heat is exchanged with air, can be secured.
- the refrigerant which is introduced from the first end of the connection pipe body to be introduced into the two regions of the second header part from the second end, circulates on the same route in the connection pipe body. For this reason, a deviation in the gas-liquid ratio of the refrigerant introduced into the two regions can be reduced. Thus, a performance decrease (efficiency decrease) of the heat exchanger can be suppressed.
- the in-second header partition plate may have a plate shape extending along a plane orthogonal to the axis of the second header part, one of the two regions may be a first space that is partitioned on one side of an axis direction, the axis direction being a direction in which the axis extends, with the in-second header partition plate, and the other one of the two regions may be a second space which is partitioned on the other side in the axis direction with the in-second header partition plate.
- the in-second header partition plate may have a vertical partition portion which has a plate shape extending along a plane including the axis in the second header part and is in contact with the opening of the second end of the connection pipe, a first horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on one side of an axis direction, the axis direction being a direction in which the axis extends, toward only one side of a direction orthogonal to a plate surface of the vertical partition portion, and a second horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on the other side of the axis direction toward only the other side of the direction orthogonal to the plate surface of the vertical partition portion.
- One of the two regions may be a first space which is partitioned on one side of the axis direction with the first horizontal partition portion and the second horizontal partition portion.
- the other one of the two regions may be a second space which is partitioned on the other side of the axis direction with the first horizontal partition portion and the second horizontal partition portion.
- a vertical partition plate that partitions a space in the second header part into an outflow-side region connected to each of the second heat transfer tubes and an inflow-side region connected to the second end of the connection pipe, in sectional view orthogonal to the axis, and a horizontal partition plate that partitions the outflow-side region into a first outflow-side space and a second outflow-side space, which are arranged in an axis direction, the axis direction being a direction in which the axis extends, may be further included.
- the in-second header partition plate may have a plate shape extending along a plane including the axis so as to partition the inflow-side region into a first chamber and a second chamber, which are adjacent to each other in a circumferential direction of the second header part in horizontal sectional view.
- a first through-hole that allows the first chamber to communicate with the first outflow-side space may be formed in a portion of the vertical partition plate facing the first chamber.
- a second through-hole that allows the second chamber to communicate with an upper region of the second outflow-side space may be formed in a portion of the vertical partition plate facing the second chamber.
- One of the two regions may be the first chamber, and the other one of the two regions may be the second chamber.
- connection pipe may have a dividing portion which extends to be continuous in the connection pipe body from the in-second header partition plate and divides a portion including at least the second end of the connection pipe body into a first flow passage communicating only with one region, out of the two regions, and a second flow passage communicating only with the other region.
- the refrigerant introduced in the connection pipe body is separated into a gas phase content and a liquid phase content in some cases in the process of circulating in the connection pipe body.
- a deviation in the gas-liquid ratios of refrigerants introduced into the two regions from the second end can be reduced.
- connection pipe body may have a first pipe portion extending from the first header part to a radially outside of the first header part, a second pipe portion extending from the second header part to a radially outside of the second header part, and a connection pipe portion which extends so as to bend with respect to the first pipe portion and the second pipe portion such that the first pipe portion and the second pipe portion are connected to each other.
- the dividing portion may extend to be continuous from the second end to at least to a middle of the first pipe portion via the second pipe portion and the connection pipe portion.
- a refrigerant with a large proportion of a liquid phase is unevenly distributed in an outside of each of the bends due to centrifugal force at each bend in some cases.
- a larger amount of the unevenly distributed refrigerant is introduced into one of the two regions of the second header part, thereby causing a performance decrease of the heat exchanger.
- the amounts of refrigerants to be introduced into the two regions of the second header part are determined immediately before the bent portion where a liquid phase and a gas phase are easily separated. Accordingly, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions can be achieved.
- the dividing portion may extend from the second end to the first end.
- the amounts of refrigerants circulating in the first flow passage and the second flow passage of the connection pipe are determined. Since the first flow passage and the second flow passage are connected to each other at the same location as the first header, refrigerants with the same gas-liquid ratio are introduced into the first flow passage and the second flow passage. Accordingly, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions of the second header part can be achieved further.
- the first header may have a cylindrical shape extending along the axis on one side of the second header part in the axis direction, and the first pipe portion, the second pipe portion, and the connection pipe portion of the connection pipe may extend on an imaginary plane including the axis.
- connection pipe having such a structure, a difference in the gas-liquid ratio at the first flow passage and the second flow passage can be reduced by the connection pipe being provided with the dividing portion.
- the first flow passage and the second flow passage may be adjacent to each other in a vertical direction on a first end side of the connection pipe body.
- the first flow passage and the second flow passage may be adjacent to each other in a horizontal direction on a first end side of the connection pipe body.
- a refrigerant in a liquid phase state is likely to gather downwards due to gravity, and a refrigerant in a gas phase state is likely to gather upwards.
- the gas-liquid ratio of a refrigerant varies according to the vertical direction in some cases.
- refrigerants with the same gas-liquid ratio are introduced into the first flow passage and the second flow passage by the first flow passage and the second flow passage being adjacent to each other in the horizontal direction. Consequently, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions of the second header can be achieved.
- each of the first flow passage and the second flow passage may have a plurality of small flow passages arranged in a direction where the first flow passage and the second flow passage are adjacent to each other.
- the connection pipe may have a flat tubular shape of which a longitudinal direction is an arranging direction of the small flow passages.
- the curvature radiuses of the bent portions of the connection pipe can be made small, for example, compared to a case where a section of the connection pipe is circular. For this reason, by making the occupying volume of the connection pipe small, a wide effective area of the heat exchanger, in which heat is exchanged with air, can be secured.
- flow passage sectional areas of the first flow passage and the second flow passage may be different from each other.
- the heat exchange efficiency of the heat exchanger can be improved by making the flow passage sectional areas of the first flow passage and the second flow passage different from each other according to a difference in the heat exchange efficiency.
- a notch dented from a radially outside to a radially inside of the second header part may be formed in the in-second header partition plate, and the second end of the connection pipe body may be fitted into the notch.
- connection pipe By configuring in such a manner, the connection pipe can be easily positioned, and thus workability can be improved.
- a slit extending from the second end along the dividing portion may be formed in the connection pipe, and the slit and the in-second header partition plate may be fitted to each other.
- connection pipe By configuring in such a manner, the connection pipe can be easily positioned, and thus workability can be improved.
- the first header part may be a portion of a header, which has a header body having a cylindrical shape of which a center is the axis and a main partition plate partitioning an inside of the header body in an axis direction, the axis direction being a direction in which the axis extends, on one side of the main partition plate in the axis direction.
- the second header part may be a portion of the header on the other side of the main partition plate in the axis direction, the axis direction may be a vertical direction.
- the heat exchanger having the first header part and the second header part can be easily configured by forming the first header part and the second header part with the main partition plate provided in one header.
- an air conditioner including the heat exchanger according to any one of the aspects.
- the heat exchanger according to any one of the aspects are included, a decrease in a heat exchange performance can be suppressed, and thus the air conditioner with a high efficiency can be realized.
- a performance decrease (efficiency decrease) of the heat exchanger or the air conditioner can be suppressed.
- the air conditioner 1 includes a compressor 2, an indoor heat exchanger 3 (heat exchanger 10), an expansion valve 4, an outdoor heat exchanger 5 (heat exchanger 10), a four-way valve 6, and a pipe 7 that connects the configuration elements together, and a refrigerant circuit formed of the configuration elements is configured.
- the compressor 2 compresses a refrigerant and supplies the compressed refrigerant to the refrigerant circuit.
- the indoor heat exchanger 3 performs heat exchange between the refrigerant and indoor air.
- the indoor heat exchanger 3 is used as an evaporator to absorb heat from the inside during cooling operation, and is used as a condenser to radiate heat to the inside during heating operation.
- the expansion valve 4 reduces a pressure by expanding the high-pressure refrigerant liquefied by the condenser exchanging heat.
- the outdoor heat exchanger 5 performs heat exchange between the refrigerant and outdoor air.
- the outdoor heat exchanger 5 is used as a condenser to radiate heat to the outside during cooling operation.
- the outdoor heat exchanger 5 is used as an evaporator to absorb heat from the outside during heating operation.
- the four-way valve 6 switches between directions where a refrigerant circulates during heating operation and during cooling operation. Consequently, a refrigerant circulates in the compressor 2, the outdoor heat exchanger 5, the expansion valve 4, and the indoor heat exchanger 3 in this order during cooling operation. On the other hand, a refrigerant circulates in the compressor 2, the indoor heat exchanger 3, the expansion valve 4, and the outdoor heat exchanger 5 in this order during heating operation.
- the heat exchangers 10 each include a plurality of heat transfer tubes 20, a plurality of fins 28, a pair of headers 30, and a connection pipe 61.
- the heat transfer tubes 20 are tubular members linearly extending in a horizontal direction, and flow passages through which a refrigerant circulates are formed therein.
- the plurality of heat transfer tubes 20 are arranged with a gap left therebetween in a vertical direction, and are disposed so as to be parallel to each other.
- the heat transfer tubes 20 each have a flat tubular shape, and the plurality of flow passages arranged in the horizontal direction orthogonal to an extending direction of the heat transfer tubes 20 are formed inside the heat transfer tubes 20.
- the plurality of flow passages are arranged so as to be parallel to each other.
- a sectional shape orthogonal to the extending direction of the heat transfer tubes 20 is a flat shape of which a longitudinal direction is the horizontal direction orthogonal to the extending direction of the heat transfer tubes 20.
- the fins 28 each are disposed between the heat transfer tubes 20 arranged as described above.
- the fins 28 extend so as to be alternately in contact with the vertically nearby heat transfer tubes 20 (extend in a corrugated shape) as facing the extending direction of each of the heat transfer tubes 20.
- the shapes of the fins 28 may be any shape insofar as the fins are provided so as to protrude from outer peripheral surfaces of the heat transfer tubes 20.
- the pair of headers 30 is provided such that the heat transfer tubes 20 are sandwiched therebetween.
- One of the pair of headers 30 is set as an entrance side header 40, which is an entrance of a refrigerant from the outside into the heat exchanger 10, and the other one is set as a turnback side header 50 for a refrigerant to turn back in the heat exchanger 10.
- the entrance side header 40 is a cylindrical member extending in the vertical direction. An upper end and a lower end of the entrance side header 40 are closed and the inside of the entrance side header is partitioned into two upper and lower regions with a partition plate 41.
- the lower region partitioned with the partition plate 41 is set as a lower entry region 42.
- the upper region is set as an upper entry region 43.
- the lower entry region 42 and the upper entry region 43 are in a state of not communicating with each other in the entrance side header 40.
- the lower entry region 42 and the upper entry region 43 each are connected to the pipe 7 configuring the refrigerant circuit.
- the heat transfer tubes 20 connected to the lower entry region 42 in a communicating state are set as first heat transfer tubes 21.
- the heat transfer tubes 20 connected to the upper entry region 43 in a communicating state are set as second heat transfer tubes 23.
- the turnback side header 50 includes a header body 51, a main partition plate 58, and an in-second header partition plate 60.
- the header body 51 is a cylindrical member which has a center, the center being an axis O of the header body 51, and which extends along the axis O. An upper end and a lower end of the header body 51 are closed.
- the header body 51 of the first embodiment extends in a state where the axis O matches the vertical direction. That is, the vertical direction is set as an axis O direction.
- the main partition plate 58 is provided in the header body 51, and partitions a space in the header body 51 into two upper and lower regions.
- a portion that includes the lower region (on one side of the axis O direction) partitioned with the main partition plate 58 is set as a first header part 52. That is, the lower region partitioned with the main partition plate 58 is set as an internal space of the first header part 52.
- a portion that includes the upper region (on the other side of the axis O direction) partitioned with the main partition plate 58 is set as a second header part 53. That is, the upper region partitioned with the main partition plate 58 is set as an internal space of the second header part 53.
- the first header part 52 and the second header part 53 each of which has a space therein are formed in the turnback side header 50 by the inside of the header body 51 being partitioned with the main partition plate 58.
- the turnback side header 50 is configured with first header part 52 and second header part 53.
- the in-second header partition plate 60 partitions the internal space of the second header part 53 into two regions.
- the in-second header partition plate 60 of the first embodiment has a plate shape extending along a horizontal plane (plane orthogonal to the axis O).
- the in-second header partition plate 60 partitions the internal space of the second header part 53 into a lower region and an upper region.
- the lower region below the in-second header partition plate 60 is set as a lower space 54 (first space)
- the upper region above the in-second header partition plate 60 is set as an upper space 55 (second space).
- the plurality of first heat transfer tubes 21 each are connected to the first header part 52 so as to be in a communicating state with the inside of the first header part 52.
- a first tube group 22 is configured with the plurality of first heat transfer tubes 21.
- the heat transfer tubes 20 connected to the first header part 52 are set as the first heat transfer tubes 21.
- the second heat transfer tubes 23 each are connected to the second header part 53 so as to be in a communicating state with the inside of the lower space 54 and the inside of the upper space 55 of the second header part 53. That is, the heat transfer tubes 20 connected to the second header part 53 are set as the second heat transfer tubes 23.
- a lower second tube group 25 is configured with the plurality of second heat transfer tubes 23, each of which is connected to the lower space 54 in a communicating state, out of the second heat transfer tubes 23.
- an upper second tube group 26 is configured with the plurality of second heat transfer tubes 23 each of which is connected to the upper space 55 in a communicating state.
- connection pipe 61 allows the internal space of the first header part 52 to communicate with the lower space 54 and the upper space 55 in the second header part 53.
- the connection pipe 61 has a connection pipe body 62 and a dividing portion 70.
- connection pipe body 62 is a tubular member, and is configured with a first pipe portion 65, a second pipe portion 66, and a connection pipe portion 67.
- the first pipe portion 65 is connected to an outer circumferential side of the first header part 52. That is, the first pipe portion 65 is a tubular member extending in the horizontal direction (direction orthogonal to the axis O), and has one end connected to a region of the header body 51 where the first header part 52 is formed such that the inside of the first pipe portion is in a communicating state with the inside of the first header part 52.
- the first pipe portion 65 is connected to an opposite portion to a portion, to which the heat transfer tubes 20 are connected, at a circumferential position in the first header part 52 (header body 51) with the axis O interposed therebetween.
- the second pipe portion 66 is connected to a circumferential side of the second header part 53. That is, the second pipe portion 66 is a tubular member extending in the horizontal direction, and has one end connected to a region of the header body 51 where the second header part 53 is formed such that the inside of the second pipe portion is in a communicating state with the inside of the second header part 53.
- the second pipe portion 66 is connected to a portion which is the same as the connection portion of the first pipe portion 65 at a circumferential position in the second header part 53 (header body 51).
- connection pipe portion 67 connects the first pipe portion 65 and the second pipe portion 66 together in the vertical direction. That is, the connection pipe portion 67 is a tubular member extending in the vertical direction, and has a lower end connected to the first pipe portion 65 such that the inside of the connection pipe portion and the inside of the first pipe portion are in a communicating state with each other. In addition, an upper end of the connection pipe portion is connected to the second pipe portion 66 such that the inside of the connection pipe portion and the inside of the second pipe portion are in a communicating state with each other.
- a first bent portion 68 in which a flow passage in the connection pipe 61 bends from the horizontal direction to the vertical direction is configured in a connection portion between the connection pipe portion 67 and the first pipe portion 65.
- a second bent portion 69 in which a flow passage in the connection pipe 61 bends from the horizontal direction to the vertical direction is configured in a connection portion between the connection pipe portion 67 and the second pipe portion 66.
- the first pipe portion 65, the second pipe portion 66, and the connection pipe portion 67 of the connection pipe body 62 configured as described above extend on an imaginary plane including the axis O.
- connection pipe body 62 An end portion of the first pipe portion 65 of the connection pipe body 62, which is connected to the first header part 52, is set as a first end 63 of the connection pipe body 62.
- a vertical position of the second end 64 of the connection pipe body 62 is the same position as the in-second header partition plate 60 partitioning the inside of the second header part 53 into two upper and lower regions. Accordingly, an opening of the second end 64 of the connection pipe body 62 is in contact with the in-second header partition plate 60.
- the thickness (vertical dimension) of the in-second header partition plate 60 is set to be smaller than the vertical dimension of an opening of the second pipe portion 66 of the connection pipe body 62.
- the in-second header partition plate 60 is provided within a range of the vertical dimension of the opening of the second pipe portion 66. Accordingly, the opening of the second end 64 is disposed so as to straddle both spaces including the lower space 54 and the upper space 55, and the inside of the second pipe portion 66 of the connection pipe body 62 is in a communicating state with both of the lower space 54 and the upper space 55 in the second header part 53.
- the dividing portion 70 divides the inside of the connection pipe body 62 into a first flow passage 71 and a second flow passage 72.
- the dividing portion 70 is formed inside the connection pipe body 62 so as to extend from a connection portion of the first pipe portion 65 to the first header part 52 to a connection portion of the second pipe portion 66 to the second header part 53 via the connection pipe portion 67. Accordingly, the first flow passage 71 and the second flow passage 72 are formed over the entire area extending from the first end 63 to the second end 64 in the connection pipe body 62.
- the dividing portion 70 extends in a plate shape along the horizontal plane inside each of the first pipe portion 65 and the second pipe portion 66. Consequently, the dividing portion 70 divides the inside of the first pipe portion 65 and the inside of the second pipe portion 66 into two upper and lower flow passages.
- the dividing portion 70 extends along a vertical plane orthogonal to the plane including the axis O of the header body 51 inside the connection pipe portion 67. Consequently, the dividing portion 70 divides the inside of the connection pipe portion 67 into a flow passage close to the header body 51 and a flow passage separated apart from the header body 51.
- the first flow passage 71 is configured by a lower flow passage in the first pipe portion 65, the flow passage separated apart from the header body 51 in the connection pipe portion 67, and an upper flow passage in the second pipe portion 66.
- the second flow passage 72 is configured by an upper flow passage in the first pipe portion 65, the flow passage close to the header body 51 in the connection pipe portion 67, and a lower flow passage in the second pipe portion 66. Consequently, the first flow passage 71 and the second flow passage 72 are adjacent to each other in the vertical direction even in the openings of both of the first end 63 and the second end 64 of the connection pipe 61.
- connection pipe 61 An end portion of the dividing portion 70 on a second end 64 side is in contact with the in-second header partition plate 60 in the second header part 53. Consequently, the dividing portion 70 extends from the in-second header partition plate 60 so as to be continuous in the connection pipe body 62. For this reason, the first flow passage 71 of the connection pipe 61 communicates only with the upper space 55 out of the spaces inside the second header part 53. The second flow passage 72 of the connection pipe 61 communicates only with the lower space 54 out of the spaces in the second header part 53.
- the heat exchanger 10 is used as an evaporator.
- the heat exchanger 10 is used as an evaporator during cooling operation of the air conditioner 1.
- the heat exchanger is used as an evaporator during heating operation of the air conditioner 1.
- a gas-liquid two phase refrigerant having a high liquid phase content is supplied from the pipe 7 to the lower entry region 42 of the entrance side header 40 illustrated in Fig. 2 .
- the refrigerant is divided and supplied to the plurality of first heat transfer tubes 21 in the lower entry region 42, and exchanges heat with the external atmosphere of the first heat transfer tubes 21 in the process of circulating in the first heat transfer tubes 21, thereby causing evaporation.
- the refrigerant in the first header part 52 is introduced into the second header part 53 via the connection pipe 61. More specifically, the refrigerant is introduced into each of the first flow passage 71 and the second flow passage 72 in the connection pipe 61 from the opening of the first end 63 of the connection pipe 61, and the refrigerant circulating in the first flow passage 71 is introduced into the upper space 55 of the second header part 53 that communicates with the first flow passage 71. The refrigerant circulating in the second flow passage 72 is introduced into the upper space 55 of the second header part 53 that communicates with the second flow passage 72.
- a refrigerant with a high liquid phase content and a high density gathers at the lower portion of the first header part 52 due to gravity, and a refrigerant with a high gas phase content and a low density gathers at the upper portion of the first header part 52. That is, in the first header part 52, the gas-liquid ratio of a refrigerant differs according to a vertical position.
- the first flow passage 71 and the second flow passage 72 which communicate with the lower space 54 and the upper space 55 of the second header part 53 respectively, are formed over the entire area of the connection pipe 61, and only the first end 63 of the connection pipe body 62, in which the first flow passage 71 and the second flow passage 72 are arranged side by side, is connected to the first header part 52.
- the refrigerants in the lower space 54 and the upper space 55 of the second header part 53 are diverted to the plurality of second heat transfer tubes 23 and circulate in the second heat transfer tubes 23. Then, the refrigerants again cause evaporation by exchanging heat with the external atmosphere of the second heat transfer tubes 23 in the process of circulating in the second heat transfer tubes 23. Consequently, in the second heat transfer tubes 23, the remaining liquid phase in the refrigerants changes to the gas phase and the refrigerants in a gas phase state are supplied to the upper entry region 43 of the entrance side header 40. Then, the refrigerants are introduced from the upper entry region 43 to the pipe 7, thereby circulating in the refrigerant circuit.
- the first flow passage 71 and the second flow passage 72 are formed over the entire area of the connection pipe 61 in the extending direction, and the first flow passage 71 and the second flow passage 72 are connected to the first end 63 at the vertical position of the first header part 52.
- refrigerants with almost the same gas-liquid ratio are introduced into the first flow passage 71 and the second flow passage 72.
- the refrigerants introduced in the first flow passage 71 and the second flow passage 72 are introduced into the lower space 54 and the upper space 55 of the second header part 53 as it is without branching off. That is, at a time point when the refrigerants are introduced in the connection pipe 61 from the first header part 52, the gas-liquid ratios of the refrigerants to be introduced into the lower space 54 and the upper space 55 are determined.
- the gas-liquid ratio of the refrigerant flowing into the two spaces also changes significantly in some cases.
- the gas-liquid ratio of the refrigerant introduced into the lower space 54 and the upper space 55 do not change significantly even in a case where the flow rate of the refrigerant has changed.
- connection pipe 61 there is only one connection portion of the connection pipe 61 to each of the first header part 52 and the second header part 53.
- handling of the connection pipe 61 becomes easy, for example, compared to a case where a plurality of flow passages are used or a case where a flow passage branches off.
- connection pipe 61 An area occupied by the connection pipe 61 can be made small by forming the plurality of flow passages (the first flow passage 71 and the second flow passage 72) in the single connection pipe 61.
- the overall size of the heat exchanger 10 is determined in advance when designing, an effective area exchanging heat with air can be increased by the amount of a decrease in the size of the connection pipe 61. Therefore, the heat exchanger 10 with a higher efficiency can be realized.
- connection pipe 61 does not have the dividing portion 70 may be adopted as the first modification example of the first embodiment.
- the connection pipe 61 is configured by only the connection pipe body 62.
- a refrigerant which is introduced from the first end 63 of the connection pipe body 62 to be introduced into the two regions of the second header part 53 from the second end 64, circulates on the same route in the connection pipe body 62, and is introduced into the lower space 54 and the upper space 55 of the second header part 53. For this reason, a deviation in the gas-liquid ratio of the refrigerant introduced into the two regions can be reduced.
- an area where the dividing portion 70 is formed may be different from that of the first embodiment.
- the dividing portion 70 of the connection pipe 61 is formed to extend from the second end 64 of the connection pipe body 62 to a middle of the middle of the first pipe portion 65, that is, immediately before the first end 63 via the second pipe portion 66 and the connection pipe portion 67.
- connection pipe 61 having the configuration where the dividing portion 70 is not included as in the first modification example, a gas phase and a liquid phase of a refrigerant are separated at the first bent portion 68 or the second bent portion 69 in some cases depending on the speed or the flow rate of the refrigerant.
- the dividing portion 70 extends further toward the first end 63 of the connection pipe 61 than the first bent portion 68 does, a refrigerant introduced from the first end 63 of the connection pipe body 62 diverts and circulates in the first flow passage 71 and the second flow passage 72 in the previous stage when a liquid phase and a gas phase are separated at the first bent portion 68.
- the gas-liquid ratio of a refrigerant circulating between the first flow passage 71 and the second flow passage 72 does not change significantly. Therefore, a performance decrease of the heat exchanger 10 can be suppressed as in the first embodiment.
- a notch 75 dented from an outer circumferential side of the in-second header partition plate 60 is configured to be provided in a region where the connection pipe 61 is connected to the in-second header partition plate 60, and the second end 64 of the connection pipe 61, which has entered the inside of the second header part 53, is configured to be fitted into the notch 75.
- the notch 75 is formed in the in-second header partition plate 60 before being attached into the header 30.
- a slit for inserting the in-second header partition plate 60 into the header 30 is provided, and the in-second header partition plate 60 is inserted into the header 30 from the outer circumferential side of the header 30.
- connection pipe 61 is inserted into the header 30 from a hole for connection of the connection pipe 61, which is formed in the header 30, and the second end 64 is fitted into the slit of the in-second header partition plate 60.
- the header 30, the in-second header partition plate 60, and the connection pipe 61 are integrally brazed together.
- connection pipe 61 of an aluminum alloy
- in-second header partition plate 60 of a clad material, which is formed by bonding a brazing filler metal.
- connection pipe 61 can be easily positioned when manufacturing the heat exchanger 10.
- first flow passage 71 and the second flow passage 72 of the connection pipe 61 are configured to be arranged in the second pipe portion 66 in the vertical direction
- first flow passage and the second flow passage are configured to be arranged in the first pipe portion 65 in the horizontal direction.
- the dividing portion 70 in the first pipe portion 65 has a plate shape extending in the vertical direction, thereby dividing the first pipe portion into the first flow passage 71 and the second flow passage 72 which are arranged in the first pipe portion 65 in the horizontal direction.
- connection pipe 61 According to such a connection pipe 61, the vertical positions of the first flow passage 71 and the second flow passage 72 are the same in the first end 63 since the first flow passage 71 and the second flow passage 72 are arranged in the opening of the first end 63 in the horizontal direction. Consequently, refrigerants with the same gas-liquid ratio are introduced into the first flow passage 71 and the second flow passage 72 respectively.
- the homogenization of gas-liquid ratios of the refrigerants introduced into the lower space 54 and the upper space 55 of the second header part 53 can be achieved further compared to a case where the first flow passage 71 and the second flow passage 72 are arranged in the first end 63 in the vertical direction.
- first flow passage 71 and the second flow passage 72 are arranged in the horizontal direction at least in the first end 63.
- first flow passage 71 and the second flow passage 72 are arranged in the horizontal direction at least in the second end 64, and the first flow passage 71 and the second flow passage 72 may be arranged in any state between the first end 63 and the second end 64. That is, the dividing portion 70 may be formed so as to be twisted in at least one portion of the first pipe portion 65, the second pipe portion 66, and the connection pipe portion 67.
- the dividing portion 70 of the fourth modification example may be applied to the second modification example such that the first flow passage 71 and the second flow passage 72 are arranged in the horizontal direction in the end portion of the dividing portion 70 located in a middle of the first pipe portion 65 in an extending direction thereof.
- a heat exchanger 80 according to a second embodiment of the invention will be described with reference to Figs. 9 and 10 .
- the same configuration elements as the first embodiment will be assigned with the same reference signs as the first embodiment, and the detailed description thereof will be omitted.
- the heat exchanger 80 of the second embodiment is different from that of the first embodiment in terms of structures of an in-second header partition plate 81 and a connection pipe 90.
- the in-second header partition plate 81 of the second embodiment has a vertical partition portion 82, a first horizontal partition portion 83, and a second horizontal partition portion 84.
- the vertical partition portion 82 is a member having a plate shape which extends along a plane including the axis O, and extends in a diameter direction of the second header part 53 (extending direction of the heat transfer tubes 20, a first pipe 94, and a second pipe portion 95) in a part of a vertical area of the second header part 53.
- the vertical partition portion 82 extends in the second header part 53 in the diameter direction from a side connected to the second heat transfer tubes 23 to a side connected to the connection pipe 90.
- the vertical partition portion 82 has a rectangular plate shape. Edges in a longitudinal direction are a lower edge and an upper edge of the vertical partition portion 82, which extend in the diameter direction, and edges in a lateral direction are in contact with an inner circumferential surface of the second header part 53 and extend in the vertical direction.
- the first horizontal partition portion 83 extends from the lower edge of the vertical partition portion 82 toward one side (the left in Fig. 10 ) of a direction orthogonal to a pair of plate surfaces of the vertical partition portion 82.
- the vertical partition portion 82 is a semicircular plate member in plan view. A linear edge of the semicircle forms an intersection ridge with the lower edge of the vertical partition portion 82, and an arc-shaped edge is in contact with a half region of the inner circumferential surface of the second header part 53 in the circumferential direction.
- the second horizontal partition portion 84 extends from the upper edge of the vertical partition portion 82 toward the other side (the right in Fig. 10 ) of the direction orthogonal to the pair of plate surfaces of the vertical partition portion 82.
- the vertical partition portion 82 is a semicircular plate member in plan view. A linear edge of a semicircle forms an intersection ridge with the upper edge of the vertical partition portion 82, and the arc-shaped edge is in contact with the half region of the inner circumferential surface of the second header part 53 in the circumferential direction.
- Such an in-second header partition plate 81 partitions the inside of the second header part 53 into two spaces. Out of the two spaces, a space below the first horizontal partition portion 83 and the second horizontal partition portion 84, that is, a space in contact with a lower surface of the first horizontal partition portion 83, a lower surface of the second horizontal partition portion 84, and a surface of the vertical partition portion 82 on the other side (the right in Fig. 10 ) is set as a lower space 86.
- a space above the first horizontal partition portion 83 and the second horizontal partition portion 84 that is, a space in contact with an upper surface of the first horizontal partition portion 83, an upper of the second horizontal partition portion 84, and a surface of the vertical partition portion 82 on the one side (the left in Fig. 10 ) is set as an upper space 87.
- connection pipe 90 has a connection pipe body 91 and a dividing portion 100.
- the connection pipe body 91 is a tubular member which allows the inside of the first header part 52 to communicate with the inside of the second header part 53, has a first end 92 connected to the outer circumferential surface of the first header part 52, and has a second end 93 connected to the outer circumferential surface of the second header part 53.
- connection pipe body 91 in a section orthogonal to an extending direction thereof has a flat shape of which a longitudinal direction is one direction.
- the outer diameter of the connection pipe body has a flat shape with the horizontal direction as a longitudinal direction thereof.
- the connection pipe body 91 is configured with three tubular members including a first pipe portion 94, a second pipe portion 95, and a connection pipe portion 96 as in the first embodiment, a first bent portion 97 is formed between the first pipe portion 94 and the connection pipe portion 96, and a second bent portion 98 is formed between the second pipe portion 95 and the connection pipe portion 96.
- the first end 92 of the connection pipe body 91 is connected to the first header part 52 with the horizontal direction as a longitudinal direction thereof and the vertical direction as a lateral direction thereof.
- the second end 93 of the connection pipe body 91 is connected to the second header part 53 with the horizontal direction as a longitudinal direction thereof and the vertical direction as a lateral direction thereof.
- connection pipe body 91 The vertical position and the circumferential position of such a second end 93 of the connection pipe body 91 are the same as those of the vertical partition portion 82 of the in-second header partition plate 81. For this reason, an opening of the second end 93 portion of the connection pipe body 91 is in contact with the vertical partition portion 82. Accordingly, the opening of the second end 93 extends over both sides of a direction, in which the pair of plate surfaces of the vertical partition portion 82 faces, and the inside of the second pipe portion 95 of the connection pipe body 91 is in a communicating state with the lower space 86 and the upper space 87 in the second header part 53.
- the second end 93 of the connection pipe body 91 is in a communicating state with the lower space 86 and the upper space 87 so as to straddle horizontally adjacent portions of both of the spaces in the horizontal direction.
- the dividing portion 100 is provided in the connection pipe body 91 so as to divide the inside of the connection pipe body 91 into two flow passages arranged from first end 92 to the second end 93 in the horizontal direction. That is, the dividing portion 100 is provided to bisect the inside of the connection pipe body 91 in a middle portion of the connection pipe body 91 in the longitudinal direction.
- One of the flow passages formed by the dividing portion 100 is set as a first flow passage 101 that allows the inside of the first header part 52 to communicate with the lower space 86 of the second header part 53.
- the other one of the flow passages formed by the dividing portion 100 is set as a second flow passage 103 that allows the inside of the first header part 52 to communicate with the upper space 87 of the second header part 53.
- the first flow passage 101 and the second flow passage 103 each have a flow passage sectional shape of which a longitudinal direction is a direction of being arranged side by side, and extend from the first end 92 to the second end 93 in a state where the flow passage sectional shape is maintained.
- a refrigerant which is introduced in the first flow passage 101 and the second flow passage 103 from the first end 92 of the connection pipe body 91, circulates in the first flow passage 101 and the second flow passage 103 and is introduced into the lower space 86 and the upper space 87 of the second header part 53, as in the first embodiment.
- connection portions of the first flow passage 101 and the second flow passage 103 to the first header part 52 are at the same vertical position. Therefore, while refrigerants with the same gas-liquid ratio are introduced into each of the first flow passage and the second flow passage, the refrigerants are introduced into the lower space 86 and the upper space 87 of the second header part 53 as it is without branching off on the way thereto. For this reason, the homogenization of the gas-liquid ratios of the refrigerants in the two spaces can be achieved, and thus a performance decrease of the heat exchanger 80 can be suppressed, as in the first embodiment.
- connection pipe body 91 is a flat tubular shape
- the curvature radiuses of the first bent portion 97 and the second bent portion 98 can be made small, for example, compared to a circular connection pipe body having the same flow passage sectional area. For this reason, by making the occupying volume of the connection pipe 90 small, a wide effective area of the heat exchanger 80, in which heat is exchanged with air, can be secured.
- first modification example of the second embodiment will be described with reference to Fig. 11 .
- a structure where the first flow passage 101 and the second flow passage 103, each of which is obtained by linearly cutting out a part of a circular section of the flow passage, are provided so as to be arranged side by side via the dividing portion 100 configuring a linear portion is adopted.
- Such a structure may be adopted.
- connection pipe 90 may have a flat tubular structure in which the first flow passage 101 and the second flow passage 103 have a plurality of small flow passages 102 and 104 respectively arranged in a direction where the first flow passage 101 and the second flow passage 103 are adjacent to each other.
- a refrigerant can be introduced from the first header part 52 to each space of the second header part 53 via each of the small flow passages 102 and 104.
- connection pipe body 91 and the dividing portion 100 of the connection pipe 90 have a structure in which a slit 105 extending along the dividing portion 100 toward the first end 92 from the second end 93 is formed and the slit 105 and the in-second header partition plate 81 are fitted to each other.
- connection pipe 90 can be easily positioned while maintaining a state where the first flow passage 101 and the second flow passage 103 do not communicate with each other and a state where the first flow passage 101 communicates with the upper space 87 and the second flow passage 103 communicates with the lower space 86. Therefore, workability can be improved.
- the flow passage sectional areas of the first flow passage 101 and the second flow passage 103 are made different from each other.
- the flow passage sectional area of the second flow passage 103 is smaller than the flow passage sectional area of the first flow passage 101.
- the sectional area of the first flow passage 101 is set to be large as described above to increase the flow rate of a refrigerant introduced into the lower space 86. Therefore, the heat exchange efficiency of the heat exchanger 80 can be improved as a whole.
- the sectional area of the first flow passage 101 is set to be large to increase the flow rate of a refrigerant introduced into the lower space 86, as described above. Therefore, the heat exchange efficiency of the heat exchanger 80 can be improved as a whole.
- the vertical partition portion 82 of the second embodiment extends only in the vertical direction. Without being limited thereto, however, the vertical partition portion may be inclined with respect to the vertical direction and the horizontal direction.
- first horizontal partition portion 83 and the second horizontal partition portion 84 extends only in the horizontal plane, the first horizontal partition portion and the second horizontal partition portion may be somewhat inclined, and may not necessarily have a flat plate shape.
- a heat exchanger 110 according to a third embodiment of the invention will be described with reference to Figs. 15 and 16 .
- the same configuration elements as the first embodiment will be assigned with the same reference signs as the first embodiment, and the detailed description thereof will be omitted.
- the heat exchanger 110 of the third embodiment is different from that of the first embodiment in terms of a structure of the second header part 53. Although illustration thereof is omitted in Figs. 15 and 16 , the first header part 52 which is the same as in the first embodiment is disposed below the second header part 53, and the heat transfer tubes 20 which are the same as in the first embodiment are connected to the first header part 52 and the second header part 53.
- a vertical partition plate 111, a horizontal partition plate 116, and an in-second header partition plate 119 are provided in the second header part 53 of the third embodiment.
- the vertical partition plate 111 partitions a space in the second header part 53 into two regions including a region connected to each of the second heat transfer tubes 23 and a region connected to the connection pipe 61, in horizontal sectional view.
- the region which is partitioned with the vertical partition plate 111 and is connected to the second heat transfer tubes 23 is set as an outflow-side region 112.
- the region which is partitioned with the vertical partition plate 111 and is connected to the connection pipe 61 is set as an inflow-side region 113.
- the second header part 53 has a cylindrical shape extending in the vertical direction, and accordingly an internal space thereof also has a cylindrical shape.
- the vertical partition plate 111 is disposed in a diameter direction of the internal space of the second header part 53 having a cylindrical shape, in horizontal sectional view. Accordingly, each of the inflow-side region 113 and the outflow-side region 112 has a semicircular shape, in horizontal sectional view.
- the horizontal partition plate 116 partitions the outflow-side region 112 into two spaces in the vertical direction.
- the second heat transfer tubes 23 are connected to each of the first outflow-side space 117 and the second outflow-side space 118.
- the horizontal partition plate 116 has a semicircular plate shape in plan view.
- the in-second header partition plate 119 is a plate-shaped member extending in the vertical direction, and is provided in the inflow-side region 113 of the second header part 53.
- the in-second header partition plate 119 partitions the inflow-side region 113 into two adjacent regions in the circumferential direction of the second header part 53, in horizontal sectional view.
- a left region is set as a first chamber 120 and a right region is set as a second chamber 121, out of the two regions.
- the in-second header partition plate 119 is disposed in a radial direction of the internal space of the second header part 53 having a cylindrical shape, in horizontal sectional view.
- the in-second header partition plate 119 is disposed such that the in-second header partition plate extends to be orthogonal to the vertical partition plate 111, and accordingly the volume of the first chamber 120 and the volume of the second chamber 121 are the same.
- a first through-hole 114 that allows the first chamber 120 to communicate with the first outflow-side space 117 of the outflow-side region 112 is formed in a portion of the vertical partition plate 111 facing the first chamber 120.
- a second through-hole 115 that allows the second chamber 121 to communicate with the second outflow-side space 118 of the outflow-side region 112 is formed in a portion of the vertical partition plate 111 facing the second chamber 121.
- the first through-hole 114 and the second through-hole 115 are disposed at locations having vertical positions different from each other.
- the first through-hole 114 is formed at a location close to a lowermost portion of the second header part 53, which is a lower portion of the vertical partition plate 111.
- the second through-hole 115 is formed at a location close to an uppermost portion of the second header part 53, which is an upper portion of the vertical partition plate 111.
- the vertical positions of the first through-hole 114 and the second through-hole 115 are positions different from the vertical position of a connection portion of the connection pipe 61 to the second header part 53.
- Only one of the first through-hole 114 and the second through-hole 115 may have a vertical position different from the connection portion of the connection pipe 61 to the second header part 53.
- connection portion of the connection pipe body 62 of the connection pipe 61 to the second header part 53 is the same portion as the circumferential position of the vertical partition plate 111 in the second header part 53. Consequently, the connection portion of the connection pipe body 62 to the second header part 53 is disposed so as to straddle the first chamber 120 and the second chamber 121. Thus, a refrigerant introduced from the connection pipe body 62 into the second header part 53 is introduced into both of the first chamber 120 and the second chamber 121.
- connection portion of the connection pipe body 62 to the second header part 53 is at a lower portion of the second header part 53.
- the dividing portion 70 may be formed inside the connection pipe 61 as in the first embodiment. In this case, out of the first flow passage 71 and the second flow passage 72, which are partitioned with the dividing portion 70, the first flow passage 71 is in a communicating state with the first chamber 120, and the second flow passage 72 is in a communicating state with the second chamber 121.
- connection pipe body 62 communicates with both of the first chamber 120 and the second chamber 121, refrigerants introduced from the connection pipe 61 into the second header part 53, in particular, refrigerants with almost the same gas-liquid ratio are introduced into the first chamber 120 and the second chamber 121.
- the refrigerant introduced in the first chamber 120 is introduced into the first outflow-side space 117 of the outflow-side region 112 via the first through-hole 114 formed in the lower portion of the second header part 53.
- the refrigerant is introduced into a lower portion of the outflow-side region 112 via the first through-hole 114 without being stored in the first chamber 120.
- the refrigerant is introduced into the first outflow-side space 117 via the first through-hole 114 in turn in a state where the refrigerant is stored in the first chamber 120 to some extent.
- the refrigerant introduced in the second chamber 121 moves upwards in the second chamber 121 in turn as the refrigerant continues to be supplied, and is introduced into the second outflow-side space 118 of the outflow-side region 112 via the second through-hole 115 formed in the upper portion of the second header part 53. That is, while the connection portion of the connection pipe 61 to the second header part 53 is disposed in the lower portion of the second header part 53, the second through-hole 115 that allows the second chamber 121 to communicate with the outflow-side region 112 is disposed in the upper portion of the second header part 53. Therefore, the refrigerant introduced in the second chamber 121 is introduced into an upper portion of the outflow-side region 112 after being moved from the lower side to the upper side in the second chamber 121.
- a liquid phase content and a gas phase content in the refrigerant are mixed.
- Each of refrigerants in a gas-liquid two phase state introduced from the first chamber 120 and the second chamber 121 to the first outflow-side space 117 and the second outflow-side space 118 of the outflow-side region 112 is introduced into each of the heat transfer tubes 20 connected to the second header part 53.
- connection pipe body 62 is connected to the first chamber 120 and the second chamber 121 of the second header part 53 so as to straddle the chambers as in the first embodiment and the second embodiment, refrigerants with almost the same gas-liquid ratio can be introduced into the two chambers.
- Each of the refrigerants is introduced into the second heat transfer tubes 23 via the flow passages of the second header part 53.
- the homogenization of gas-liquid ratios of refrigerants introduced into the second heat transfer tubes 23 can be achieved, and a decrease in a heat exchange performance can be avoided.
- the first through-hole 114 and the second through-hole 115 are not limited to the disposition described above.
- both of the through-holes may be disposed in the lower portion of the vertical partition plate 111. That is, the first through-hole 114 and the second through-hole 115 may be disposed at any locations in the vertical partition plate 111.
- a plurality of first through-holes 114 and a plurality of second through-holes 115 may be formed without being limited to forming only one first through-hole and one second through-hole.
- the axis O direction may be the horizontal direction, or may be an inclination direction of inclining with respect to the horizontal direction and the vertical direction.
- first header part 52 and the second header part 53 may be separately configured.
- the posture of the first header part 52 and the posture of the second header part 53 may be different from each other, that is, the first header part 52 may have a cylindrical shape extending along an axis O different from the axis O of the second header part 53.
- the invention can be applied to a heat exchanger and an air conditioner including the heat exchanger.
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Abstract
Description
- The present invention relates to a heat exchanger and an air conditioner.
- This application claims priority based on Japanese Patent Application No.
2016-038327 filed on February 29, 2016 - A heat exchanger, in which a plurality of heat transfer tubes extending in a horizontal direction are disposed with a gap left therebetween in a vertical direction and a fin is provided on an outer surface of each heat transfer tube, is known as a heat exchanger of an air conditioner. Both ends of the plurality of heat transfer tubes are connected to a pair of headers extending in the vertical direction, respectively.
- Such a heat exchanger is configured such that a refrigerant, which is introduced into one header out of the pair of headers and is circulated in the other header via the heat transfer tubes, turns back at the other header to return to the one header again via the heat transfer tubes, in order to secure a flow passage length for the refrigerant.
- The inside of the header at a turnback side is partitioned into a plurality of regions with a partition plate partitioning the inside of the header in the vertical direction. Accordingly, a refrigerant introduced in one region of the header via the heat transfer tubes returns to one header on an entrance side via the plurality of heat transfer tubes connected to the other region after being introduced into the other region of the header via a connection pipe.
- For example, a heat exchanger including a connection pipe which has one main pipe portion and branch pipe portions that extend so as to branch off into two portions from the main pipe portion is disclosed in
PTL 1. In the heat exchanger, the main pipe portion is connected to one region in the header, and the branch pipe portions each are connected to any one of the two regions in the header. - In a case where the heat exchanger is used as an evaporator, a refrigerant introduced in one region of the header via the heat transfer tubes is diverted and introduced into the other region of the two regions of the header via the main pipe portion and the branch pipe portions of the connection pipe.
- [PTL 1] Japanese Unexamined Patent Application Publication No.
2015-55404 - However, in a case where the heat exchanger is used as an evaporator, not the entire refrigerant introduced into one region of the header via heat transfer tubes evaporates, and the refrigerant is in a state of a gas-liquid two phase refrigerant, in which a liquid phase refrigerant and a gas phase refrigerant are mixed.
- For this reason, a larger amount of a liquid phase refrigerant circulates only in some of the branch pipes depending on a disposed location of each branch pipe, and thus a deviation in the flow rate or the gas-liquid ratio of the refrigerant occurs between the branch pipes. In particular, in a case where the main pipe portion has a bent portion on an upstream side of the branch pipe and the main pipe portion and the branch pipes extend in the same plane as the bent portion, a liquid phase refrigerant tends to concentrate only in the branch pipe located outside the bend.
- As described above, if a deviation of a liquid phase refrigerant occurs in each branch pipe, a significant change in a refrigerant distribution ratio occurs at the time of diversion also due to a change in the flow rate of the entire refrigerant. In addition, if a refrigerant is diverted in a state where there is a deviation in the flow rate or the gas-liquid ratio of the refrigerant, some heat transfer tubes end up having a refrigerant with an extremely low flow rate, and thus a heat transfer region of the heat exchanger cannot be sufficiently used.
- In the connection pipe of
PTL 1, handling for avoiding interference between a plurality of connection pipes is complicated, and thus processing or brazing is difficult. In addition, as a result of making an area occupied by the connection pipes larger, it is necessary to make an effective area exchanging heat with air smaller, and thus a heat exchange performance decreases. - An object of the invention is to provide a heat exchanger which can suppress a performance decrease (efficiency decrease) and an air conditioner in which the heat exchanger is used.
- According to a first aspect of the invention, there is provided a heat exchanger including a plurality of first heat transfer tubes that allow a refrigerant to circulate therein and are arranged with a gap left therebetween, a first header part that has a cylindrical shape and has an internal space connected to each of the first heat transfer tubes in a communicating state, a plurality of second heat transfer tubes that allow the refrigerant to circulate therein and are arranged with a gap left therebetween, a second header part that has a cylindrical shape extending along an axis and has an internal space connected to each of the second heat transfer tubes in a communicating state, an in-second header partition plate that partitions the internal space of the second header part into two regions, and a connection pipe that has a connection pipe body having a first end connected to an outer circumferential surface of the first header part in a communicating state with the internal space of the first header part and a second end on an opposite side to the first end connected to an outer circumferential surface of the second header part in a communicating state with the internal space of the second header part and being disposed so as to straddle the two regions such that an opening of the second end is in contact with the in-second header partition plate to partition the opening of the second end with the in-second header partition plate.
- In such a heat exchanger, since the opening of the second end of the connection pipe body straddles the two regions of the second header part, the refrigerant introduced in the connection pipe body from the first header part is introduced into each of the two regions. Accordingly, since there is only one connection portion of the connection pipe to each of the first header part and the second header part, the handling of the connection pipe is easy. In addition, an area occupied by the connection pipe can be made small compared to a case where the connection pipe branches off. Accordingly, a wide effective area of the heat exchanger, in which heat is exchanged with air, can be secured.
- The refrigerant, which is introduced from the first end of the connection pipe body to be introduced into the two regions of the second header part from the second end, circulates on the same route in the connection pipe body. For this reason, a deviation in the gas-liquid ratio of the refrigerant introduced into the two regions can be reduced. Thus, a performance decrease (efficiency decrease) of the heat exchanger can be suppressed.
- In the heat exchanger according to a second aspect of the invention, the in-second header partition plate may have a plate shape extending along a plane orthogonal to the axis of the second header part, one of the two regions may be a first space that is partitioned on one side of an axis direction, the axis direction being a direction in which the axis extends, with the in-second header partition plate, and the other one of the two regions may be a second space which is partitioned on the other side in the axis direction with the in-second header partition plate.
- By configuring in such a manner, the homogenization of gas-liquid ratios of refrigerants introduced into the respective first space and second space, which are divided in the axis direction of the second header part, can be achieved.
- In the heat exchanger according to a third aspect of the invention, the in-second header partition plate may have a vertical partition portion which has a plate shape extending along a plane including the axis in the second header part and is in contact with the opening of the second end of the connection pipe, a first horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on one side of an axis direction, the axis direction being a direction in which the axis extends, toward only one side of a direction orthogonal to a plate surface of the vertical partition portion, and a second horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on the other side of the axis direction toward only the other side of the direction orthogonal to the plate surface of the vertical partition portion. One of the two regions may be a first space which is partitioned on one side of the axis direction with the first horizontal partition portion and the second horizontal partition portion. The other one of the two regions may be a second space which is partitioned on the other side of the axis direction with the first horizontal partition portion and the second horizontal partition portion.
- By configuring in such a manner, the homogenization of gas-liquid ratios of refrigerants introduced into the respective first space and second space partitioned with the in-second header partition plate can be achieved.
- In the heat exchanger according to a fourth aspect of the invention, a vertical partition plate that partitions a space in the second header part into an outflow-side region connected to each of the second heat transfer tubes and an inflow-side region connected to the second end of the connection pipe, in sectional view orthogonal to the axis, and a horizontal partition plate that partitions the outflow-side region into a first outflow-side space and a second outflow-side space, which are arranged in an axis direction, the axis direction being a direction in which the axis extends, may be further included. The in-second header partition plate may have a plate shape extending along a plane including the axis so as to partition the inflow-side region into a first chamber and a second chamber, which are adjacent to each other in a circumferential direction of the second header part in horizontal sectional view. A first through-hole that allows the first chamber to communicate with the first outflow-side space may be formed in a portion of the vertical partition plate facing the first chamber. A second through-hole that allows the second chamber to communicate with an upper region of the second outflow-side space may be formed in a portion of the vertical partition plate facing the second chamber. One of the two regions may be the first chamber, and the other one of the two regions may be the second chamber.
- By configuring in such a manner, the homogenization of gas-liquid ratios of refrigerants introduced into the respective first chamber and second chamber, which are divided in the circumferential direction by the in-second header partition plate, can be achieved.
- In heat exchanger according to a fifth aspect of the invention, the connection pipe may have a dividing portion which extends to be continuous in the connection pipe body from the in-second header partition plate and divides a portion including at least the second end of the connection pipe body into a first flow passage communicating only with one region, out of the two regions, and a second flow passage communicating only with the other region.
- The refrigerant introduced in the connection pipe body is separated into a gas phase content and a liquid phase content in some cases in the process of circulating in the connection pipe body. On the contrary, by the dividing portion dividing the inside of the connection pipe body into the first flow passage and the second flow passage, a deviation in the gas-liquid ratios of refrigerants introduced into the two regions from the second end can be reduced.
- In the heat exchanger according to a sixth aspect of the invention, the connection pipe body may have a first pipe portion extending from the first header part to a radially outside of the first header part, a second pipe portion extending from the second header part to a radially outside of the second header part, and a connection pipe portion which extends so as to bend with respect to the first pipe portion and the second pipe portion such that the first pipe portion and the second pipe portion are connected to each other. The dividing portion may extend to be continuous from the second end to at least to a middle of the first pipe portion via the second pipe portion and the connection pipe portion.
- In general, in a bent portion between the first pipe portion and the connection pipe portion and a bent portion between the connection pipe portion and the second pipe portion, a refrigerant with a large proportion of a liquid phase is unevenly distributed in an outside of each of the bends due to centrifugal force at each bend in some cases. In this case, a larger amount of the unevenly distributed refrigerant is introduced into one of the two regions of the second header part, thereby causing a performance decrease of the heat exchanger.
- On the contrary, by configuring such that the dividing portion of the connection pipe extends to a first header side of the bent portion between the first pipe portion and the connection pipe portion, the amounts of refrigerants to be introduced into the two regions of the second header part are determined immediately before the bent portion where a liquid phase and a gas phase are easily separated. Accordingly, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions can be achieved.
- In the heat exchanger of a seventh aspect of the invention, the dividing portion may extend from the second end to the first end.
- By configuring in such a manner, at a time point when the refrigerant is introduced from the first header part into the connection pipe, the amounts of refrigerants circulating in the first flow passage and the second flow passage of the connection pipe are determined. Since the first flow passage and the second flow passage are connected to each other at the same location as the first header, refrigerants with the same gas-liquid ratio are introduced into the first flow passage and the second flow passage. Accordingly, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions of the second header part can be achieved further.
- In the heat exchanger according to an eighth aspect of the invention, the first header may have a cylindrical shape extending along the axis on one side of the second header part in the axis direction, and the first pipe portion, the second pipe portion, and the connection pipe portion of the connection pipe may extend on an imaginary plane including the axis.
- Even in the connection pipe having such a structure, a difference in the gas-liquid ratio at the first flow passage and the second flow passage can be reduced by the connection pipe being provided with the dividing portion.
- In the heat exchanger of a ninth aspect of the invention, the first flow passage and the second flow passage may be adjacent to each other in a vertical direction on a first end side of the connection pipe body.
- Even in a case of having such a configuration, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions of the second header can be achieved since refrigerants with gas-liquid ratios close to each other are introduced into the first flow passage and the second flow passage.
- In the heat exchanger of a tenth aspect of the invention, the first flow passage and the second flow passage may be adjacent to each other in a horizontal direction on a first end side of the connection pipe body.
- In general, a refrigerant in a liquid phase state is likely to gather downwards due to gravity, and a refrigerant in a gas phase state is likely to gather upwards. For this reason, even in the first header part, the gas-liquid ratio of a refrigerant varies according to the vertical direction in some cases. Even in this case, refrigerants with the same gas-liquid ratio are introduced into the first flow passage and the second flow passage by the first flow passage and the second flow passage being adjacent to each other in the horizontal direction. Consequently, the homogenization of gas-liquid ratios of refrigerants introduced into the two regions of the second header can be achieved.
- In the heat exchanger of an eleventh aspect of the invention, each of the first flow passage and the second flow passage may have a plurality of small flow passages arranged in a direction where the first flow passage and the second flow passage are adjacent to each other. The connection pipe may have a flat tubular shape of which a longitudinal direction is an arranging direction of the small flow passages.
- By configuring in such a manner, the curvature radiuses of the bent portions of the connection pipe can be made small, for example, compared to a case where a section of the connection pipe is circular. For this reason, by making the occupying volume of the connection pipe small, a wide effective area of the heat exchanger, in which heat is exchanged with air, can be secured.
- In the heat exchanger of a twelfth aspect of the invention, flow passage sectional areas of the first flow passage and the second flow passage may be different from each other.
- In a case where the heat exchange efficiency of the second heat transfer tubes connected to each of the two regions of the second header part differs, the heat exchange efficiency of the heat exchanger can be improved by making the flow passage sectional areas of the first flow passage and the second flow passage different from each other according to a difference in the heat exchange efficiency.
- In the heat exchanger according to a thirteenth aspect of the invention, a notch dented from a radially outside to a radially inside of the second header part may be formed in the in-second header partition plate, and the second end of the connection pipe body may be fitted into the notch.
- By configuring in such a manner, the connection pipe can be easily positioned, and thus workability can be improved.
- In the heat exchanger according to the fourteenth aspect of the invention, a slit extending from the second end along the dividing portion may be formed in the connection pipe, and the slit and the in-second header partition plate may be fitted to each other.
- By configuring in such a manner, the connection pipe can be easily positioned, and thus workability can be improved.
- In the heat exchanger according to a fifteenth aspect of the invention, the first header part may be a portion of a header, which has a header body having a cylindrical shape of which a center is the axis and a main partition plate partitioning an inside of the header body in an axis direction, the axis direction being a direction in which the axis extends, on one side of the main partition plate in the axis direction. The second header part may be a portion of the header on the other side of the main partition plate in the axis direction, the axis direction may be a vertical direction.
- As described above, the heat exchanger having the first header part and the second header part can be easily configured by forming the first header part and the second header part with the main partition plate provided in one header.
- According to a sixteenth aspect of the invention, there is provided an air conditioner including the heat exchanger according to any one of the aspects.
- As described above, since the heat exchanger according to any one of the aspects are included, a decrease in a heat exchange performance can be suppressed, and thus the air conditioner with a high efficiency can be realized.
- According to the invention, a performance decrease (efficiency decrease) of the heat exchanger or the air conditioner can be suppressed.
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Fig. 1 is an overall configuration view of an air conditioner according to a first embodiment of the invention. -
Fig. 2 is a longitudinal sectional view of a heat exchanger according to the first embodiment of the invention. -
Fig. 3 is a perspective view of the heat exchanger according to the first embodiment of the invention. -
Fig. 4A is a sectional view of a first pipe portion of a connection pipe of the heat exchanger according to the first embodiment of the invention. -
Fig. 4B is a sectional view of a second pipe portion of the connection pipe of the heat exchanger according to the first embodiment of the invention. -
Fig. 5 is a longitudinal sectional view of a heat exchanger according to a first modification example of the first embodiment of the invention. -
Fig. 6 is a longitudinal sectional view of a heat exchanger according to a second modification example of the first embodiment of the invention. -
Fig. 7 is a horizontal sectional view of a second header part of a heat exchanger according to a third modification example of the first embodiment of the invention. -
Fig. 8A is a sectional view of a first pipe portion of a connection pipe of a heat exchanger according to a fourth modification example of the first embodiment of the invention. -
Fig. 8B is a sectional view of a second pipe portion of the connection pipe of the heat exchanger according to the fourth modification example of the first embodiment of the invention. -
Fig. 9 is a perspective view of a heat exchanger according to a second embodiment of the invention. -
Fig. 10 is a view of a second header part of the heat exchanger according to the second embodiment of the invention seen from a connecting direction of a connection pipe. -
Fig. 11 is a sectional view of a connection pipe of a heat exchanger according to a first modification example of the second embodiment of the invention. -
Fig. 12 is a sectional view of a connection pipe of a heat exchanger according to a second modification example of the second embodiment of the invention. -
Fig. 13 is a perspective view of a connection pipe of a heat exchanger according to a third modification example of the second embodiment of the invention. -
Fig. 14 is a sectional view of a connection pipe of a heat exchanger according to a fourth modification example of the second embodiment of the invention. -
Fig. 15 is a perspective view of a second header part of a heat exchanger according to a third embodiment of the invention. -
Fig. 16 is a horizontal sectional view of the second header part of the heat exchanger according to the third embodiment of the invention. - Hereinafter, an
air conditioner 1 includingheat exchangers 10 according to a first embodiment of the invention will be described with reference toFigs. 1 to 3 andFigs. 4A and 4B . - As illustrated in
Fig. 1 , theair conditioner 1 includes acompressor 2, an indoor heat exchanger 3 (heat exchanger 10), anexpansion valve 4, an outdoor heat exchanger 5 (heat exchanger 10), a four-way valve 6, and apipe 7 that connects the configuration elements together, and a refrigerant circuit formed of the configuration elements is configured. - The
compressor 2 compresses a refrigerant and supplies the compressed refrigerant to the refrigerant circuit. - The
indoor heat exchanger 3 performs heat exchange between the refrigerant and indoor air. Theindoor heat exchanger 3 is used as an evaporator to absorb heat from the inside during cooling operation, and is used as a condenser to radiate heat to the inside during heating operation. - The
expansion valve 4 reduces a pressure by expanding the high-pressure refrigerant liquefied by the condenser exchanging heat. - The
outdoor heat exchanger 5 performs heat exchange between the refrigerant and outdoor air. Theoutdoor heat exchanger 5 is used as a condenser to radiate heat to the outside during cooling operation. Theoutdoor heat exchanger 5 is used as an evaporator to absorb heat from the outside during heating operation. - The four-
way valve 6 switches between directions where a refrigerant circulates during heating operation and during cooling operation. Consequently, a refrigerant circulates in thecompressor 2, theoutdoor heat exchanger 5, theexpansion valve 4, and theindoor heat exchanger 3 in this order during cooling operation. On the other hand, a refrigerant circulates in thecompressor 2, theindoor heat exchanger 3, theexpansion valve 4, and theoutdoor heat exchanger 5 in this order during heating operation. - Next, the
heat exchangers 10 which are used as theindoor heat exchanger 3 and theoutdoor heat exchanger 5 will be described with reference toFigs. 2 to 5 . - The
heat exchangers 10 each include a plurality ofheat transfer tubes 20, a plurality offins 28, a pair ofheaders 30, and aconnection pipe 61. - The
heat transfer tubes 20 are tubular members linearly extending in a horizontal direction, and flow passages through which a refrigerant circulates are formed therein. The plurality ofheat transfer tubes 20 are arranged with a gap left therebetween in a vertical direction, and are disposed so as to be parallel to each other. - In the first embodiment, the
heat transfer tubes 20 each have a flat tubular shape, and the plurality of flow passages arranged in the horizontal direction orthogonal to an extending direction of theheat transfer tubes 20 are formed inside theheat transfer tubes 20. The plurality of flow passages are arranged so as to be parallel to each other. For this reason, a sectional shape orthogonal to the extending direction of theheat transfer tubes 20 is a flat shape of which a longitudinal direction is the horizontal direction orthogonal to the extending direction of theheat transfer tubes 20. - The
fins 28 each are disposed between theheat transfer tubes 20 arranged as described above. In the first embodiment, thefins 28 extend so as to be alternately in contact with the vertically nearby heat transfer tubes 20 (extend in a corrugated shape) as facing the extending direction of each of theheat transfer tubes 20. Without being limited thereto, the shapes of thefins 28 may be any shape insofar as the fins are provided so as to protrude from outer peripheral surfaces of theheat transfer tubes 20. - At both ends of the plurality of
heat transfer tubes 20, the pair ofheaders 30 is provided such that theheat transfer tubes 20 are sandwiched therebetween. One of the pair ofheaders 30 is set as anentrance side header 40, which is an entrance of a refrigerant from the outside into theheat exchanger 10, and the other one is set as aturnback side header 50 for a refrigerant to turn back in theheat exchanger 10. - The
entrance side header 40 is a cylindrical member extending in the vertical direction. An upper end and a lower end of theentrance side header 40 are closed and the inside of the entrance side header is partitioned into two upper and lower regions with apartition plate 41. The lower region partitioned with thepartition plate 41 is set as alower entry region 42. The upper region is set as anupper entry region 43. Thelower entry region 42 and theupper entry region 43 are in a state of not communicating with each other in theentrance side header 40. Thelower entry region 42 and theupper entry region 43 each are connected to thepipe 7 configuring the refrigerant circuit. - Out of the plurality of
heat transfer tubes 20, theheat transfer tubes 20 connected to thelower entry region 42 in a communicating state are set as firstheat transfer tubes 21. Theheat transfer tubes 20 connected to theupper entry region 43 in a communicating state are set as secondheat transfer tubes 23. - The
turnback side header 50 includes aheader body 51, amain partition plate 58, and an in-secondheader partition plate 60. - The
header body 51 is a cylindrical member which has a center, the center being an axis O of theheader body 51, and which extends along the axis O. An upper end and a lower end of theheader body 51 are closed. Theheader body 51 of the first embodiment extends in a state where the axis O matches the vertical direction. That is, the vertical direction is set as an axis O direction. - The
main partition plate 58 is provided in theheader body 51, and partitions a space in theheader body 51 into two upper and lower regions. - A portion that includes the lower region (on one side of the axis O direction) partitioned with the
main partition plate 58 is set as afirst header part 52. That is, the lower region partitioned with themain partition plate 58 is set as an internal space of thefirst header part 52. - A portion that includes the upper region (on the other side of the axis O direction) partitioned with the
main partition plate 58 is set as asecond header part 53. That is, the upper region partitioned with themain partition plate 58 is set as an internal space of thesecond header part 53. - In the first embodiment, the
first header part 52 and thesecond header part 53 each of which has a space therein are formed in theturnback side header 50 by the inside of theheader body 51 being partitioned with themain partition plate 58. In other words, theturnback side header 50 is configured withfirst header part 52 andsecond header part 53. - The in-second
header partition plate 60 partitions the internal space of thesecond header part 53 into two regions. The in-secondheader partition plate 60 of the first embodiment has a plate shape extending along a horizontal plane (plane orthogonal to the axis O). - Accordingly, the in-second
header partition plate 60 partitions the internal space of thesecond header part 53 into a lower region and an upper region. In thesecond header part 53, the lower region below the in-secondheader partition plate 60 is set as a lower space 54 (first space), and the upper region above the in-secondheader partition plate 60 is set as an upper space 55 (second space). - The plurality of first
heat transfer tubes 21 each are connected to thefirst header part 52 so as to be in a communicating state with the inside of thefirst header part 52. Afirst tube group 22 is configured with the plurality of firstheat transfer tubes 21. In other words, theheat transfer tubes 20 connected to thefirst header part 52 are set as the firstheat transfer tubes 21. - The second
heat transfer tubes 23 each are connected to thesecond header part 53 so as to be in a communicating state with the inside of thelower space 54 and the inside of theupper space 55 of thesecond header part 53. That is, theheat transfer tubes 20 connected to thesecond header part 53 are set as the secondheat transfer tubes 23. A lowersecond tube group 25 is configured with the plurality of secondheat transfer tubes 23, each of which is connected to thelower space 54 in a communicating state, out of the secondheat transfer tubes 23. In addition, an uppersecond tube group 26 is configured with the plurality of secondheat transfer tubes 23 each of which is connected to theupper space 55 in a communicating state. - The
connection pipe 61 allows the internal space of thefirst header part 52 to communicate with thelower space 54 and theupper space 55 in thesecond header part 53. Theconnection pipe 61 has aconnection pipe body 62 and a dividingportion 70. - The
connection pipe body 62 is a tubular member, and is configured with afirst pipe portion 65, asecond pipe portion 66, and aconnection pipe portion 67. - The
first pipe portion 65 is connected to an outer circumferential side of thefirst header part 52. That is, thefirst pipe portion 65 is a tubular member extending in the horizontal direction (direction orthogonal to the axis O), and has one end connected to a region of theheader body 51 where thefirst header part 52 is formed such that the inside of the first pipe portion is in a communicating state with the inside of thefirst header part 52. Thefirst pipe portion 65 is connected to an opposite portion to a portion, to which theheat transfer tubes 20 are connected, at a circumferential position in the first header part 52 (header body 51) with the axis O interposed therebetween. - The
second pipe portion 66 is connected to a circumferential side of thesecond header part 53. That is, thesecond pipe portion 66 is a tubular member extending in the horizontal direction, and has one end connected to a region of theheader body 51 where thesecond header part 53 is formed such that the inside of the second pipe portion is in a communicating state with the inside of thesecond header part 53. Thesecond pipe portion 66 is connected to a portion which is the same as the connection portion of thefirst pipe portion 65 at a circumferential position in the second header part 53 (header body 51). - The
connection pipe portion 67 connects thefirst pipe portion 65 and thesecond pipe portion 66 together in the vertical direction. That is, theconnection pipe portion 67 is a tubular member extending in the vertical direction, and has a lower end connected to thefirst pipe portion 65 such that the inside of the connection pipe portion and the inside of the first pipe portion are in a communicating state with each other. In addition, an upper end of the connection pipe portion is connected to thesecond pipe portion 66 such that the inside of the connection pipe portion and the inside of the second pipe portion are in a communicating state with each other. - Accordingly, a first
bent portion 68 in which a flow passage in theconnection pipe 61 bends from the horizontal direction to the vertical direction is configured in a connection portion between theconnection pipe portion 67 and thefirst pipe portion 65. In addition, a secondbent portion 69 in which a flow passage in theconnection pipe 61 bends from the horizontal direction to the vertical direction is configured in a connection portion between theconnection pipe portion 67 and thesecond pipe portion 66. - The
first pipe portion 65, thesecond pipe portion 66, and theconnection pipe portion 67 of theconnection pipe body 62 configured as described above extend on an imaginary plane including the axis O. - An end portion of the
first pipe portion 65 of theconnection pipe body 62, which is connected to thefirst header part 52, is set as afirst end 63 of theconnection pipe body 62. In addition, an end portion of thesecond pipe portion 66 of theconnection pipe body 62, which is connected to thesecond header part 53, is set as asecond end 64 of theconnection pipe body 62. - A vertical position of the
second end 64 of theconnection pipe body 62 is the same position as the in-secondheader partition plate 60 partitioning the inside of thesecond header part 53 into two upper and lower regions. Accordingly, an opening of thesecond end 64 of theconnection pipe body 62 is in contact with the in-secondheader partition plate 60. - In addition, the thickness (vertical dimension) of the in-second
header partition plate 60 is set to be smaller than the vertical dimension of an opening of thesecond pipe portion 66 of theconnection pipe body 62. The in-secondheader partition plate 60 is provided within a range of the vertical dimension of the opening of thesecond pipe portion 66. Accordingly, the opening of thesecond end 64 is disposed so as to straddle both spaces including thelower space 54 and theupper space 55, and the inside of thesecond pipe portion 66 of theconnection pipe body 62 is in a communicating state with both of thelower space 54 and theupper space 55 in thesecond header part 53. - The dividing
portion 70 divides the inside of theconnection pipe body 62 into afirst flow passage 71 and asecond flow passage 72. In the first embodiment, the dividingportion 70 is formed inside theconnection pipe body 62 so as to extend from a connection portion of thefirst pipe portion 65 to thefirst header part 52 to a connection portion of thesecond pipe portion 66 to thesecond header part 53 via theconnection pipe portion 67. Accordingly, thefirst flow passage 71 and thesecond flow passage 72 are formed over the entire area extending from thefirst end 63 to thesecond end 64 in theconnection pipe body 62. - As illustrated in
Fig. 6 , the dividingportion 70 extends in a plate shape along the horizontal plane inside each of thefirst pipe portion 65 and thesecond pipe portion 66. Consequently, the dividingportion 70 divides the inside of thefirst pipe portion 65 and the inside of thesecond pipe portion 66 into two upper and lower flow passages. - The dividing
portion 70 extends along a vertical plane orthogonal to the plane including the axis O of theheader body 51 inside theconnection pipe portion 67. Consequently, the dividingportion 70 divides the inside of theconnection pipe portion 67 into a flow passage close to theheader body 51 and a flow passage separated apart from theheader body 51. - In the first embodiment, the
first flow passage 71 is configured by a lower flow passage in thefirst pipe portion 65, the flow passage separated apart from theheader body 51 in theconnection pipe portion 67, and an upper flow passage in thesecond pipe portion 66. Thesecond flow passage 72 is configured by an upper flow passage in thefirst pipe portion 65, the flow passage close to theheader body 51 in theconnection pipe portion 67, and a lower flow passage in thesecond pipe portion 66. Consequently, thefirst flow passage 71 and thesecond flow passage 72 are adjacent to each other in the vertical direction even in the openings of both of thefirst end 63 and thesecond end 64 of theconnection pipe 61. - An end portion of the dividing
portion 70 on asecond end 64 side is in contact with the in-secondheader partition plate 60 in thesecond header part 53. Consequently, the dividingportion 70 extends from the in-secondheader partition plate 60 so as to be continuous in theconnection pipe body 62. For this reason, thefirst flow passage 71 of theconnection pipe 61 communicates only with theupper space 55 out of the spaces inside thesecond header part 53. Thesecond flow passage 72 of theconnection pipe 61 communicates only with thelower space 54 out of the spaces in thesecond header part 53. - Next, operation and effects in a case where the
heat exchanger 10 is used as an evaporator will be described. In a case where theheat exchanger 10 is theindoor heat exchanger 3, theheat exchanger 10 is used as an evaporator during cooling operation of theair conditioner 1. In a case where the heat exchanger is theoutdoor heat exchanger 5, the heat exchanger is used as an evaporator during heating operation of theair conditioner 1. - In a case where the
heat exchanger 10 is used as an evaporator, a gas-liquid two phase refrigerant having a high liquid phase content is supplied from thepipe 7 to thelower entry region 42 of theentrance side header 40 illustrated inFig. 2 . The refrigerant is divided and supplied to the plurality of firstheat transfer tubes 21 in thelower entry region 42, and exchanges heat with the external atmosphere of the firstheat transfer tubes 21 in the process of circulating in the firstheat transfer tubes 21, thereby causing evaporation. - Consequently, some of the refrigerant supplied from the first
heat transfer tubes 21 into thefirst header part 52 of theturnback side header 50 changes from the liquid phase to a gas phase, and thus the refrigerant becomes a gas-liquid two phase refrigerant which has a higher proportion of a gas phase than that of the refrigerant in thelower entry region 42. - The refrigerant in the
first header part 52 is introduced into thesecond header part 53 via theconnection pipe 61. More specifically, the refrigerant is introduced into each of thefirst flow passage 71 and thesecond flow passage 72 in theconnection pipe 61 from the opening of thefirst end 63 of theconnection pipe 61, and the refrigerant circulating in thefirst flow passage 71 is introduced into theupper space 55 of thesecond header part 53 that communicates with thefirst flow passage 71. The refrigerant circulating in thesecond flow passage 72 is introduced into theupper space 55 of thesecond header part 53 that communicates with thesecond flow passage 72. - Out of gas-liquid two phase refrigerants supplied into the
first header part 52, a refrigerant with a high liquid phase content and a high density gathers at the lower portion of thefirst header part 52 due to gravity, and a refrigerant with a high gas phase content and a low density gathers at the upper portion of thefirst header part 52. That is, in thefirst header part 52, the gas-liquid ratio of a refrigerant differs according to a vertical position. - In the first embodiment, the
first flow passage 71 and thesecond flow passage 72, which communicate with thelower space 54 and theupper space 55 of thesecond header part 53 respectively, are formed over the entire area of theconnection pipe 61, and only thefirst end 63 of theconnection pipe body 62, in which thefirst flow passage 71 and thesecond flow passage 72 are arranged side by side, is connected to thefirst header part 52. - For this reason, refrigerants, which are at almost the same vertical position, are supplied to the
first flow passage 71 and thesecond flow passage 72 respectively. Therefore, gas-liquid ratios of refrigerants in thelower space 54 and theupper space 55 are close to each other since the refrigerants with almost the same gas-liquid ratio are introduced into thelower space 54 and theupper space 55 of thesecond header part 53 via thefirst flow passage 71 and thesecond flow passage 72. - After then, the refrigerants in the
lower space 54 and theupper space 55 of thesecond header part 53 are diverted to the plurality of secondheat transfer tubes 23 and circulate in the secondheat transfer tubes 23. Then, the refrigerants again cause evaporation by exchanging heat with the external atmosphere of the secondheat transfer tubes 23 in the process of circulating in the secondheat transfer tubes 23. Consequently, in the secondheat transfer tubes 23, the remaining liquid phase in the refrigerants changes to the gas phase and the refrigerants in a gas phase state are supplied to theupper entry region 43 of theentrance side header 40. Then, the refrigerants are introduced from theupper entry region 43 to thepipe 7, thereby circulating in the refrigerant circuit. - As described above, in the first embodiment, the
first flow passage 71 and thesecond flow passage 72 are formed over the entire area of theconnection pipe 61 in the extending direction, and thefirst flow passage 71 and thesecond flow passage 72 are connected to thefirst end 63 at the vertical position of thefirst header part 52. - For this reason, refrigerants with almost the same gas-liquid ratio are introduced into the
first flow passage 71 and thesecond flow passage 72. In addition, the refrigerants introduced in thefirst flow passage 71 and thesecond flow passage 72 are introduced into thelower space 54 and theupper space 55 of thesecond header part 53 as it is without branching off. That is, at a time point when the refrigerants are introduced in theconnection pipe 61 from thefirst header part 52, the gas-liquid ratios of the refrigerants to be introduced into thelower space 54 and theupper space 55 are determined. - Thus, the homogenization of gas-liquid ratios of refrigerants introduced into the
lower space 54 and theupper space 55 can be achieved. After then, it is possible to perform an efficient heat exchange at the secondheat transfer tubes 23 into which the refrigerants are introduced, and a performance decrease of theheat exchanger 10 can be suppressed. - In a case where the
first header part 52 and thelower space 54 and theupper space 55 of thesecond header part 53 are connected to a flow passage branching off on the way thereto, in particular, in a case where the flow rate of a refrigerant has changed, the gas-liquid ratio of the refrigerant flowing into the two spaces also changes significantly in some cases. - In the first embodiment, since the refrigerant introduced in the
first flow passage 71 and thesecond flow passage 72 from thefirst header part 52 is introduced into thelower space 54 and theupper space 55 of thesecond header part 53 as it is, the gas-liquid ratio of the refrigerant introduced into thelower space 54 and theupper space 55 do not change significantly even in a case where the flow rate of the refrigerant has changed. - In the first embodiment, there is only one connection portion of the
connection pipe 61 to each of thefirst header part 52 and thesecond header part 53. As a consequence, handling of theconnection pipe 61 becomes easy, for example, compared to a case where a plurality of flow passages are used or a case where a flow passage branches off. - An area occupied by the
connection pipe 61 can be made small by forming the plurality of flow passages (thefirst flow passage 71 and the second flow passage 72) in thesingle connection pipe 61. For example, in a case where the overall size of theheat exchanger 10 is determined in advance when designing, an effective area exchanging heat with air can be increased by the amount of a decrease in the size of theconnection pipe 61. Therefore, theheat exchanger 10 with a higher efficiency can be realized. - Next, a first modification example of the first embodiment will be described with reference to
Fig. 5 . A configuration where theconnection pipe 61 does not have the dividingportion 70 may be adopted as the first modification example of the first embodiment. In this case, theconnection pipe 61 is configured by only theconnection pipe body 62. - According to the first modification example of the first embodiment configured in such a manner, even in a configuration where the
connection pipe 61 does not have the dividingportion 70, a refrigerant, which is introduced from thefirst end 63 of theconnection pipe body 62 to be introduced into the two regions of thesecond header part 53 from thesecond end 64, circulates on the same route in theconnection pipe body 62, and is introduced into thelower space 54 and theupper space 55 of thesecond header part 53. For this reason, a deviation in the gas-liquid ratio of the refrigerant introduced into the two regions can be reduced. - Next, a second modification example of the first embodiment will be described with reference to
Fig. 6 . In the second modification example of the first embodiment, an area where the dividingportion 70 is formed may be different from that of the first embodiment. - In the second modification example of the first embodiment, the dividing
portion 70 of theconnection pipe 61 is formed to extend from thesecond end 64 of theconnection pipe body 62 to a middle of the middle of thefirst pipe portion 65, that is, immediately before thefirst end 63 via thesecond pipe portion 66 and theconnection pipe portion 67. - For example, in a case of the
connection pipe 61 having the configuration where the dividingportion 70 is not included as in the first modification example, a gas phase and a liquid phase of a refrigerant are separated at the firstbent portion 68 or the secondbent portion 69 in some cases depending on the speed or the flow rate of the refrigerant. - That is, due to centrifugal force received when the refrigerant passes through the first
bent portion 68 of theconnection pipe body 62, a liquid phase content of the refrigerant with a higher density is unevenly distributed in an outside of the bend. In this case, a liquid phase refrigerant is distributed in theconnection pipe body 62 in the circumferential direction. As a result, the refrigerant, of which a gas-liquid ratio has changed significantly, is introduced into thelower space 54 and theupper space 55 of thesecond header part 53. - On the contrary, in the second modification example, since the dividing
portion 70 extends further toward thefirst end 63 of theconnection pipe 61 than the firstbent portion 68 does, a refrigerant introduced from thefirst end 63 of theconnection pipe body 62 diverts and circulates in thefirst flow passage 71 and thesecond flow passage 72 in the previous stage when a liquid phase and a gas phase are separated at the firstbent portion 68. For this reason, the gas-liquid ratio of a refrigerant circulating between thefirst flow passage 71 and thesecond flow passage 72 does not change significantly. Therefore, a performance decrease of theheat exchanger 10 can be suppressed as in the first embodiment. - Next, a third modification example of the first embodiment will be described with reference to
Fig. 7 . In the third modification example of the first embodiment, anotch 75 dented from an outer circumferential side of the in-secondheader partition plate 60 is configured to be provided in a region where theconnection pipe 61 is connected to the in-secondheader partition plate 60, and thesecond end 64 of theconnection pipe 61, which has entered the inside of thesecond header part 53, is configured to be fitted into thenotch 75. - The
notch 75 is formed in the in-secondheader partition plate 60 before being attached into theheader 30. A slit for inserting the in-secondheader partition plate 60 into theheader 30 is provided, and the in-secondheader partition plate 60 is inserted into theheader 30 from the outer circumferential side of theheader 30. - After then, the
second end 64 of theconnection pipe 61 is inserted into theheader 30 from a hole for connection of theconnection pipe 61, which is formed in theheader 30, and thesecond end 64 is fitted into the slit of the in-secondheader partition plate 60. After assembling in such a manner, theheader 30, the in-secondheader partition plate 60, and theconnection pipe 61 are integrally brazed together. - It is preferable to form the
connection pipe 61 of an aluminum alloy, and it is preferable to form the in-secondheader partition plate 60 of a clad material, which is formed by bonding a brazing filler metal. - According to the third modification example of the first embodiment, it is possible to improve workability since the
connection pipe 61 can be easily positioned when manufacturing theheat exchanger 10. - Next, a fourth modification example of the first embodiment will be described with reference to
Figs. 8A and 8B . In the fourth modification example of the first embodiment, while thefirst flow passage 71 and thesecond flow passage 72 of theconnection pipe 61 are configured to be arranged in thesecond pipe portion 66 in the vertical direction, the first flow passage and the second flow passage are configured to be arranged in thefirst pipe portion 65 in the horizontal direction. - That is, in the fourth modification example, the dividing
portion 70 in thefirst pipe portion 65 has a plate shape extending in the vertical direction, thereby dividing the first pipe portion into thefirst flow passage 71 and thesecond flow passage 72 which are arranged in thefirst pipe portion 65 in the horizontal direction. - According to such a
connection pipe 61, the vertical positions of thefirst flow passage 71 and thesecond flow passage 72 are the same in thefirst end 63 since thefirst flow passage 71 and thesecond flow passage 72 are arranged in the opening of thefirst end 63 in the horizontal direction. Consequently, refrigerants with the same gas-liquid ratio are introduced into thefirst flow passage 71 and thesecond flow passage 72 respectively. Thus, the homogenization of gas-liquid ratios of the refrigerants introduced into thelower space 54 and theupper space 55 of thesecond header part 53 can be achieved further compared to a case where thefirst flow passage 71 and thesecond flow passage 72 are arranged in thefirst end 63 in the vertical direction. - In the fourth modification example, it is sufficient that the
first flow passage 71 and thesecond flow passage 72 are arranged in the horizontal direction at least in thefirst end 63. In addition, it is sufficient that thefirst flow passage 71 and thesecond flow passage 72 are arranged in the horizontal direction at least in thesecond end 64, and thefirst flow passage 71 and thesecond flow passage 72 may be arranged in any state between thefirst end 63 and thesecond end 64. That is, the dividingportion 70 may be formed so as to be twisted in at least one portion of thefirst pipe portion 65, thesecond pipe portion 66, and theconnection pipe portion 67. - The dividing
portion 70 of the fourth modification example may be applied to the second modification example such that thefirst flow passage 71 and thesecond flow passage 72 are arranged in the horizontal direction in the end portion of the dividingportion 70 located in a middle of thefirst pipe portion 65 in an extending direction thereof. - A
heat exchanger 80 according to a second embodiment of the invention will be described with reference toFigs. 9 and10 . InFigs. 9 and10 , the same configuration elements as the first embodiment will be assigned with the same reference signs as the first embodiment, and the detailed description thereof will be omitted. - The
heat exchanger 80 of the second embodiment is different from that of the first embodiment in terms of structures of an in-secondheader partition plate 81 and aconnection pipe 90. - The in-second
header partition plate 81 of the second embodiment has avertical partition portion 82, a firsthorizontal partition portion 83, and a secondhorizontal partition portion 84. Thevertical partition portion 82 is a member having a plate shape which extends along a plane including the axis O, and extends in a diameter direction of the second header part 53 (extending direction of theheat transfer tubes 20, afirst pipe 94, and a second pipe portion 95) in a part of a vertical area of thesecond header part 53. - In the second embodiment, the
vertical partition portion 82 extends in thesecond header part 53 in the diameter direction from a side connected to the secondheat transfer tubes 23 to a side connected to theconnection pipe 90. Thevertical partition portion 82 has a rectangular plate shape. Edges in a longitudinal direction are a lower edge and an upper edge of thevertical partition portion 82, which extend in the diameter direction, and edges in a lateral direction are in contact with an inner circumferential surface of thesecond header part 53 and extend in the vertical direction. - The first
horizontal partition portion 83 extends from the lower edge of thevertical partition portion 82 toward one side (the left inFig. 10 ) of a direction orthogonal to a pair of plate surfaces of thevertical partition portion 82. Thevertical partition portion 82 is a semicircular plate member in plan view. A linear edge of the semicircle forms an intersection ridge with the lower edge of thevertical partition portion 82, and an arc-shaped edge is in contact with a half region of the inner circumferential surface of thesecond header part 53 in the circumferential direction. - The second
horizontal partition portion 84 extends from the upper edge of thevertical partition portion 82 toward the other side (the right inFig. 10 ) of the direction orthogonal to the pair of plate surfaces of thevertical partition portion 82. Thevertical partition portion 82 is a semicircular plate member in plan view. A linear edge of a semicircle forms an intersection ridge with the upper edge of thevertical partition portion 82, and the arc-shaped edge is in contact with the half region of the inner circumferential surface of thesecond header part 53 in the circumferential direction. - Such an in-second
header partition plate 81 partitions the inside of thesecond header part 53 into two spaces. Out of the two spaces, a space below the firsthorizontal partition portion 83 and the secondhorizontal partition portion 84, that is, a space in contact with a lower surface of the firsthorizontal partition portion 83, a lower surface of the secondhorizontal partition portion 84, and a surface of thevertical partition portion 82 on the other side (the right inFig. 10 ) is set as alower space 86. In addition, out of the two spaces, a space above the firsthorizontal partition portion 83 and the secondhorizontal partition portion 84, that is, a space in contact with an upper surface of the firsthorizontal partition portion 83, an upper of the secondhorizontal partition portion 84, and a surface of thevertical partition portion 82 on the one side (the left inFig. 10 ) is set as anupper space 87. - As in the first embodiment, the
connection pipe 90 has aconnection pipe body 91 and a dividingportion 100. Theconnection pipe body 91 is a tubular member which allows the inside of thefirst header part 52 to communicate with the inside of thesecond header part 53, has afirst end 92 connected to the outer circumferential surface of thefirst header part 52, and has asecond end 93 connected to the outer circumferential surface of thesecond header part 53. - The outer diameter of the
connection pipe body 91 in a section orthogonal to an extending direction thereof has a flat shape of which a longitudinal direction is one direction. In the second embodiment, the outer diameter of the connection pipe body has a flat shape with the horizontal direction as a longitudinal direction thereof. Theconnection pipe body 91 is configured with three tubular members including afirst pipe portion 94, asecond pipe portion 95, and aconnection pipe portion 96 as in the first embodiment, a firstbent portion 97 is formed between thefirst pipe portion 94 and theconnection pipe portion 96, and a secondbent portion 98 is formed between thesecond pipe portion 95 and theconnection pipe portion 96. - The
first end 92 of theconnection pipe body 91 is connected to thefirst header part 52 with the horizontal direction as a longitudinal direction thereof and the vertical direction as a lateral direction thereof. As in thefirst end 92, also thesecond end 93 of theconnection pipe body 91 is connected to thesecond header part 53 with the horizontal direction as a longitudinal direction thereof and the vertical direction as a lateral direction thereof. - The vertical position and the circumferential position of such a
second end 93 of theconnection pipe body 91 are the same as those of thevertical partition portion 82 of the in-secondheader partition plate 81. For this reason, an opening of thesecond end 93 portion of theconnection pipe body 91 is in contact with thevertical partition portion 82. Accordingly, the opening of thesecond end 93 extends over both sides of a direction, in which the pair of plate surfaces of thevertical partition portion 82 faces, and the inside of thesecond pipe portion 95 of theconnection pipe body 91 is in a communicating state with thelower space 86 and theupper space 87 in thesecond header part 53. - As described above, in the second embodiment, the
second end 93 of theconnection pipe body 91 is in a communicating state with thelower space 86 and theupper space 87 so as to straddle horizontally adjacent portions of both of the spaces in the horizontal direction. - The dividing
portion 100 is provided in theconnection pipe body 91 so as to divide the inside of theconnection pipe body 91 into two flow passages arranged fromfirst end 92 to thesecond end 93 in the horizontal direction. That is, the dividingportion 100 is provided to bisect the inside of theconnection pipe body 91 in a middle portion of theconnection pipe body 91 in the longitudinal direction. - One of the flow passages formed by the dividing
portion 100 is set as afirst flow passage 101 that allows the inside of thefirst header part 52 to communicate with thelower space 86 of thesecond header part 53. The other one of the flow passages formed by the dividingportion 100 is set as asecond flow passage 103 that allows the inside of thefirst header part 52 to communicate with theupper space 87 of thesecond header part 53. Thefirst flow passage 101 and thesecond flow passage 103 each have a flow passage sectional shape of which a longitudinal direction is a direction of being arranged side by side, and extend from thefirst end 92 to thesecond end 93 in a state where the flow passage sectional shape is maintained. - In the
heat exchanger 80 of the second embodiment described above, a refrigerant, which is introduced in thefirst flow passage 101 and thesecond flow passage 103 from thefirst end 92 of theconnection pipe body 91, circulates in thefirst flow passage 101 and thesecond flow passage 103 and is introduced into thelower space 86 and theupper space 87 of thesecond header part 53, as in the first embodiment. - The connection portions of the
first flow passage 101 and thesecond flow passage 103 to thefirst header part 52 are at the same vertical position. Therefore, while refrigerants with the same gas-liquid ratio are introduced into each of the first flow passage and the second flow passage, the refrigerants are introduced into thelower space 86 and theupper space 87 of thesecond header part 53 as it is without branching off on the way thereto. For this reason, the homogenization of the gas-liquid ratios of the refrigerants in the two spaces can be achieved, and thus a performance decrease of theheat exchanger 80 can be suppressed, as in the first embodiment. - In the second embodiment, since the shape of the
connection pipe body 91 is a flat tubular shape, the curvature radiuses of the firstbent portion 97 and the secondbent portion 98 can be made small, for example, compared to a circular connection pipe body having the same flow passage sectional area. For this reason, by making the occupying volume of theconnection pipe 90 small, a wide effective area of theheat exchanger 80, in which heat is exchanged with air, can be secured. - Next, a first modification example of the second embodiment will be described with reference to
Fig. 11 . In the first modification example of the second embodiment, a structure where thefirst flow passage 101 and thesecond flow passage 103, each of which is obtained by linearly cutting out a part of a circular section of the flow passage, are provided so as to be arranged side by side via the dividingportion 100 configuring a linear portion is adopted. Such a structure may be adopted. - Next, a second modification example of the second embodiment will be described with reference to
Fig. 12 . In the second modification example of the second embodiment, theconnection pipe 90 may have a flat tubular structure in which thefirst flow passage 101 and thesecond flow passage 103 have a plurality ofsmall flow passages first flow passage 101 and thesecond flow passage 103 are adjacent to each other. - Accordingly, also in the second embodiment, a refrigerant can be introduced from the
first header part 52 to each space of thesecond header part 53 via each of thesmall flow passages - Next, a third modification example of the second embodiment will be described with reference to
Fig. 13 . In the third modification example of the second embodiment, theconnection pipe body 91 and the dividingportion 100 of theconnection pipe 90 have a structure in which aslit 105 extending along the dividingportion 100 toward thefirst end 92 from thesecond end 93 is formed and theslit 105 and the in-secondheader partition plate 81 are fitted to each other. - By configuring in such a manner, the
connection pipe 90 can be easily positioned while maintaining a state where thefirst flow passage 101 and thesecond flow passage 103 do not communicate with each other and a state where thefirst flow passage 101 communicates with theupper space 87 and thesecond flow passage 103 communicates with thelower space 86. Therefore, workability can be improved. - Next, a fourth modification example of the second embodiment will be described with reference to
Fig. 14 . In the fourth modification example of the second embodiment, the flow passage sectional areas of thefirst flow passage 101 and thesecond flow passage 103 are made different from each other. In the fourth modification example of the second embodiment, the flow passage sectional area of thesecond flow passage 103 is smaller than the flow passage sectional area of thefirst flow passage 101. - For example, in a case where the number of the second
heat transfer tubes 23 of the lowersecond tube group 25 connected to thelower space 86 of thesecond header part 53 is larger than the number of the secondheat transfer tubes 23 of the uppersecond tube group 26 connected to theupper space 87, the sectional area of thefirst flow passage 101 is set to be large as described above to increase the flow rate of a refrigerant introduced into thelower space 86. Therefore, the heat exchange efficiency of theheat exchanger 80 can be improved as a whole. - For example, also in a case where the speed of blowing air to the lower
second tube group 25 is higher than the speed of blowing air to the uppersecond tube group 26, the sectional area of thefirst flow passage 101 is set to be large to increase the flow rate of a refrigerant introduced into thelower space 86, as described above. Therefore, the heat exchange efficiency of theheat exchanger 80 can be improved as a whole. - That is, by changing the amount of a refrigerant introduced into each of the
lower space 86 and theupper space 87 according to the heat exchange performance of thesecond tube group 24 into which the refrigerant is introduced from thelower space 86 and theupper space 87, heat exchange efficiency can be improved. - The
vertical partition portion 82 of the second embodiment extends only in the vertical direction. Without being limited thereto, however, the vertical partition portion may be inclined with respect to the vertical direction and the horizontal direction. - In addition, although each of the first
horizontal partition portion 83 and the secondhorizontal partition portion 84 extends only in the horizontal plane, the first horizontal partition portion and the second horizontal partition portion may be somewhat inclined, and may not necessarily have a flat plate shape. - A
heat exchanger 110 according to a third embodiment of the invention will be described with reference toFigs. 15 and16 . In the third embodiment, the same configuration elements as the first embodiment will be assigned with the same reference signs as the first embodiment, and the detailed description thereof will be omitted. - The
heat exchanger 110 of the third embodiment is different from that of the first embodiment in terms of a structure of thesecond header part 53. Although illustration thereof is omitted inFigs. 15 and16 , thefirst header part 52 which is the same as in the first embodiment is disposed below thesecond header part 53, and theheat transfer tubes 20 which are the same as in the first embodiment are connected to thefirst header part 52 and thesecond header part 53. - A
vertical partition plate 111, ahorizontal partition plate 116, and an in-secondheader partition plate 119 are provided in thesecond header part 53 of the third embodiment. - The
vertical partition plate 111 partitions a space in thesecond header part 53 into two regions including a region connected to each of the secondheat transfer tubes 23 and a region connected to theconnection pipe 61, in horizontal sectional view. The region which is partitioned with thevertical partition plate 111 and is connected to the secondheat transfer tubes 23 is set as an outflow-side region 112. The region which is partitioned with thevertical partition plate 111 and is connected to theconnection pipe 61 is set as an inflow-side region 113. - In the third embodiment, the
second header part 53 has a cylindrical shape extending in the vertical direction, and accordingly an internal space thereof also has a cylindrical shape. Thevertical partition plate 111 is disposed in a diameter direction of the internal space of thesecond header part 53 having a cylindrical shape, in horizontal sectional view. Accordingly, each of the inflow-side region 113 and the outflow-side region 112 has a semicircular shape, in horizontal sectional view. - The
horizontal partition plate 116 partitions the outflow-side region 112 into two spaces in the vertical direction. A lower space, out of the two spaces, is set as a first outflow-side space 117. In addition, an upper space, out of the two spaces, is set as a second outflow-side space 118. The secondheat transfer tubes 23 are connected to each of the first outflow-side space 117 and the second outflow-side space 118. Thehorizontal partition plate 116 has a semicircular plate shape in plan view. - The in-second
header partition plate 119 is a plate-shaped member extending in the vertical direction, and is provided in the inflow-side region 113 of thesecond header part 53. The in-secondheader partition plate 119 partitions the inflow-side region 113 into two adjacent regions in the circumferential direction of thesecond header part 53, in horizontal sectional view. When seen from the other side in the horizontal direction, which is a connecting direction of theconnection pipe 61, a left region is set as afirst chamber 120 and a right region is set as asecond chamber 121, out of the two regions. - In the third embodiment, the in-second
header partition plate 119 is disposed in a radial direction of the internal space of thesecond header part 53 having a cylindrical shape, in horizontal sectional view. In addition, the in-secondheader partition plate 119 is disposed such that the in-second header partition plate extends to be orthogonal to thevertical partition plate 111, and accordingly the volume of thefirst chamber 120 and the volume of thesecond chamber 121 are the same. - Herein, a first through-
hole 114 that allows thefirst chamber 120 to communicate with the first outflow-side space 117 of the outflow-side region 112 is formed in a portion of thevertical partition plate 111 facing thefirst chamber 120. In addition, a second through-hole 115 that allows thesecond chamber 121 to communicate with the second outflow-side space 118 of the outflow-side region 112 is formed in a portion of thevertical partition plate 111 facing thesecond chamber 121. - The first through-
hole 114 and the second through-hole 115 are disposed at locations having vertical positions different from each other. In the third embodiment, the first through-hole 114 is formed at a location close to a lowermost portion of thesecond header part 53, which is a lower portion of thevertical partition plate 111. In addition, the second through-hole 115 is formed at a location close to an uppermost portion of thesecond header part 53, which is an upper portion of thevertical partition plate 111. The vertical positions of the first through-hole 114 and the second through-hole 115 are positions different from the vertical position of a connection portion of theconnection pipe 61 to thesecond header part 53. - Only one of the first through-
hole 114 and the second through-hole 115 may have a vertical position different from the connection portion of theconnection pipe 61 to thesecond header part 53. - The connection portion of the
connection pipe body 62 of theconnection pipe 61 to thesecond header part 53 is the same portion as the circumferential position of thevertical partition plate 111 in thesecond header part 53. Consequently, the connection portion of theconnection pipe body 62 to thesecond header part 53 is disposed so as to straddle thefirst chamber 120 and thesecond chamber 121. Thus, a refrigerant introduced from theconnection pipe body 62 into thesecond header part 53 is introduced into both of thefirst chamber 120 and thesecond chamber 121. - In the third embodiment, the connection portion of the
connection pipe body 62 to thesecond header part 53 is at a lower portion of thesecond header part 53. - The dividing
portion 70 may be formed inside theconnection pipe 61 as in the first embodiment. In this case, out of thefirst flow passage 71 and thesecond flow passage 72, which are partitioned with the dividingportion 70, thefirst flow passage 71 is in a communicating state with thefirst chamber 120, and thesecond flow passage 72 is in a communicating state with thesecond chamber 121. - Also in the
heat exchanger 110 of the third embodiment, since theconnection pipe body 62 communicates with both of thefirst chamber 120 and thesecond chamber 121, refrigerants introduced from theconnection pipe 61 into thesecond header part 53, in particular, refrigerants with almost the same gas-liquid ratio are introduced into thefirst chamber 120 and thesecond chamber 121. - The refrigerant introduced in the
first chamber 120 is introduced into the first outflow-side space 117 of the outflow-side region 112 via the first through-hole 114 formed in the lower portion of thesecond header part 53. At this time, in a case where the flow rate of the refrigerant is low, the refrigerant is introduced into a lower portion of the outflow-side region 112 via the first through-hole 114 without being stored in thefirst chamber 120. On the other hand, in a case where the flow rate of the refrigerant is high, the refrigerant is introduced into the first outflow-side space 117 via the first through-hole 114 in turn in a state where the refrigerant is stored in thefirst chamber 120 to some extent. - On the other hand, the refrigerant introduced in the
second chamber 121 moves upwards in thesecond chamber 121 in turn as the refrigerant continues to be supplied, and is introduced into the second outflow-side space 118 of the outflow-side region 112 via the second through-hole 115 formed in the upper portion of thesecond header part 53. That is, while the connection portion of theconnection pipe 61 to thesecond header part 53 is disposed in the lower portion of thesecond header part 53, the second through-hole 115 that allows thesecond chamber 121 to communicate with the outflow-side region 112 is disposed in the upper portion of thesecond header part 53. Therefore, the refrigerant introduced in thesecond chamber 121 is introduced into an upper portion of the outflow-side region 112 after being moved from the lower side to the upper side in thesecond chamber 121. - By making the moving route of a refrigerant longer as described above, a liquid phase content and a gas phase content in the refrigerant are mixed. Each of refrigerants in a gas-liquid two phase state introduced from the
first chamber 120 and thesecond chamber 121 to the first outflow-side space 117 and the second outflow-side space 118 of the outflow-side region 112 is introduced into each of theheat transfer tubes 20 connected to thesecond header part 53. - As described above, also in the third embodiment, since the
connection pipe body 62 is connected to thefirst chamber 120 and thesecond chamber 121 of thesecond header part 53 so as to straddle the chambers as in the first embodiment and the second embodiment, refrigerants with almost the same gas-liquid ratio can be introduced into the two chambers. Each of the refrigerants is introduced into the secondheat transfer tubes 23 via the flow passages of thesecond header part 53. Thus, the homogenization of gas-liquid ratios of refrigerants introduced into the secondheat transfer tubes 23 can be achieved, and a decrease in a heat exchange performance can be avoided. - The first through-
hole 114 and the second through-hole 115 are not limited to the disposition described above. For example, both of the through-holes may be disposed in the lower portion of thevertical partition plate 111. That is, the first through-hole 114 and the second through-hole 115 may be disposed at any locations in thevertical partition plate 111. In addition, a plurality of first through-holes 114 and a plurality of second through-holes 115 may be formed without being limited to forming only one first through-hole and one second through-hole. - Although the embodiments of the invention are described, the invention is not limited to the embodiments, and can be modified as appropriate without departing from the technical scope of the invention.
- For example, although the
first header part 52 and thesecond header part 53 share the axis O and the axis O extends in the vertical direction in the third embodiment, the axis is not limited thereto. For example, the axis O direction may be the horizontal direction, or may be an inclination direction of inclining with respect to the horizontal direction and the vertical direction. - In addition, although a case where the
first header part 52 and thesecond header part 53 are formed in thesame header 30 is described as an example, thefirst header part 52 and thesecond header part 53 may be separately configured. In this case, the posture of thefirst header part 52 and the posture of thesecond header part 53 may be different from each other, that is, thefirst header part 52 may have a cylindrical shape extending along an axis O different from the axis O of thesecond header part 53. - The invention can be applied to a heat exchanger and an air conditioner including the heat exchanger.
-
- 1
- air conditioner
- 2
- compressor
- 3
- indoor heat exchanger
- 4
- expansion valve
- 5
- outdoor heat exchanger
- 6
- four-way valve
- 7
- pipe
- 10, 80, 110
- heat exchanger
- 20
- heat transfer tube
- 21
- first heat transfer tube
- 22
- first tube group
- 23
- second heat transfer tube
- 24
- second tube group
- 25
- lower second tube group
- 26
- upper second tube group
- 28
- fin
- 30
- header
- 40
- entrance side header
- 41
- partition plate
- 42
- lower entry region
- 43
- upper entry region
- 50
- turnback side header
- 51
- header body
- 52
- first header part
- 53
- second header part
- 54, 86
- lower space
- 55, 87
- upper space
- 58
- main partition plate
- 60, 81, 119
- in-second header partition plate
- 61, 90
- connection pipe
- 62, 91
- connection pipe body
- 63, 92
- first end
- 64, 93
- second end
- 65, 94
- first pipe portion
- 66, 95
- second pipe portion
- 67, 96
- connection pipe portion
- 68, 97
- first bent portion
- 69, 98
- second bent portion
- 70, 100
- dividing portion
- 71, 101
- first flow passage
- 72, 103
- second flow passage
- 75
- notch
- 82
- vertical partition portion
- 83
- first horizontal partition portion
- 84
- second horizontal partition portion
- 102, 104
- small flow passage
- 105
- slit
- 111
- vertical partition plate
- 112
- outflow-side region
- 113
- inflow-side region
- 114
- first through-hole
- 115
- second through-hole
- 116
- horizontal partition plate
- 117
- first outflow-side space
- 118
- second outflow-side space
- 120
- first chamber
- 121
- second chamber
- O
- axis
Claims (16)
- A heat exchanger comprising:a plurality of first heat transfer tubes that allow a refrigerant to circulate therein and are arranged with a gap left therebetween;a first header part that has a cylindrical shape and has an internal space connected to each of the first heat transfer tubes in a communicating state;a plurality of second heat transfer tubes that allow the refrigerant to circulate therein and are arranged with a gap left therebetween;a second header part that has a cylindrical shape extending along an axis and has an internal space connected to each of the second heat transfer tubes in a communicating state;an in-second header partition plate that partitions the internal space of the second header part into two regions; anda connection pipe that has a connection pipe body having a first end connected to an outer circumferential surface of the first header part in a communicating state with the internal space of the first header part and a second end on an opposite side to the first end connected to an outer circumferential surface of the second header part in a communicating state with the internal space of the second header part,wherein an opening of the second end is disposed so as to straddle the two regions partitioned with the in-second header partition plate by the opening of the second end being in contact with the in-second header partition plate.
- The heat exchanger according to Claim 1,
wherein the in-second header partition plate has a plate shape extending along a plane orthogonal to the axis of the second header part,
one of the two regions is a first space that is partitioned on one side of an axis direction, the axis direction being a direction in which the axis extends, with the in-second header partition plate, and
the other one of the two regions is a second space which is partitioned on the other side in the axis direction with the in-second header partition plate. - The heat exchanger according to Claim 1,
wherein the in-second header partition plate hasa vertical partition portion which has a plate shape extending along a plane including the axis in the second header part and is in contact with the opening of the second end of the connection pipe,a first horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on one side of an axis direction, the axis direction being a direction in which the axis extends, toward only one side of a direction orthogonal to a plate surface of the vertical partition portion, anda second horizontal partition portion which has a plate shape extending from an edge of the vertical partition portion on the other side of the axis direction toward only the other side of the direction orthogonal to the plate surface of the vertical partition portion,one of the two regions is a first space which is partitioned on one side of the axis direction with the first horizontal partition portion and the second horizontal partition portion, and
the other one of the two regions is a second space which is partitioned on the other side of the axis direction with the first horizontal partition portion and the second horizontal partition portion. - The heat exchanger according to Claim 1, further comprising:a vertical partition plate that partitions a space in the second header part into an outflow-side region connected to each of the second heat transfer tubes and an inflow-side region connected to the second end of the connection pipe, in sectional view orthogonal to the axis; anda horizontal partition plate that partitions the outflow-side region into a first outflow-side space and a second outflow-side space, which are arranged in an axis direction, the axis direction being a direction in which the axis extends,wherein the in-second header partition plate has a plate shape extending along a plane including the axis so as to partition the inflow-side region into a first chamber and a second chamber, which are adjacent to each other in a circumferential direction of the second header part in horizontal sectional view,a first through-hole that allows the first chamber to communicate with the first outflow-side space is formed in a portion of the vertical partition plate facing the first chamber,a second through-hole that allows the second chamber to communicate with an upper region of the second outflow-side space is formed in a portion of the vertical partition plate facing the second chamber,one of the two regions is the first chamber, andthe other one of the two regions is the second chamber.
- The heat exchanger according to any one of Claims 1 to 4,
wherein the connection pipe has
a dividing portion which extends to be continuous in the connection pipe body from the in-second header partition plate and divides a portion including at least the second end of the connection pipe body into a first flow passage communicating only with one region, out of the two regions, and a second flow passage communicating only with the other region. - The heat exchanger according to Claim 5,
wherein the connection pipe body hasa first pipe portion extending from the first header part to a radially outside of the first header part,a second pipe portion extending from the second header part to a radially outside of the second header part, anda connection pipe portion which extends so as to bend with respect to the first pipe portion and the second pipe portion such that the first pipe portion and the second pipe portion are connected to each other, andthe dividing portion extends to be continuous from the second end to at least to a middle of the first pipe portion via the second pipe portion and the connection pipe portion. - The heat exchanger according to Claim 6,
wherein the dividing portion extends from the second end to the first end. - The heat exchanger according to Claim 6 or 7,
wherein the first header part has a cylindrical shape extending along the axis on one side of the second header part in the axis direction, and
the first pipe portion, the second pipe portion, and the connection pipe portion of the connection pipe extend on an imaginary plane including the axis. - The heat exchanger according to any one of Claims 5 to 8,
wherein the first flow passage and the second flow passage are adjacent to each other in a vertical direction on a first end side of the connection pipe body. - The heat exchanger according to any one of Claims 5 to 8,
wherein the first flow passage and the second flow passage are adjacent to each other in a horizontal direction on a first end side of the connection pipe body. - The heat exchanger according to any one of Claims 5 to 10,
each of the first flow passage and the second flow passage has a plurality of small flow passages arranged in a direction where the first flow passage and the second flow passage are adjacent to each other, and
the connection pipe has a flat tubular shape of which a longitudinal direction is an arranging direction of the small flow passages. - The heat exchanger according to any one of Claims 5 to 11,
wherein flow passage sectional areas of the first flow passage and the second flow passage are different from each other. - The heat exchanger according to any one of Claims 5 to 12,
wherein a notch dented from a radially outside to a radially inside of the second header part is formed in the in-second header partition plate, and
the second end of the connection pipe body is fitted into the notch. - The heat exchanger according to any one of Claims 5 to 12,
wherein a slit extending from the second end along the dividing portion is formed in the connection pipe, and the slit and the in-second header partition plate are fitted to each other. - The heat exchanger according to any one of Claims 1 to 14,
wherein the first header part is a portion of a header, which has a header body having a cylindrical shape of which a center is the axis and a main partition plate partitioning an inside of the header body in an axis direction, the axis direction being a direction in which the axis extends, on one side of the main partition plate in the axis direction,
the second header part is a portion of the header on the other side of the main partition plate in the axis direction, and
the axis direction is a vertical direction. - An air conditioner comprising the heat exchanger according to any one of Claims 1 to 15.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016038327A JP6145189B1 (en) | 2016-02-29 | 2016-02-29 | Heat exchanger and air conditioner |
PCT/JP2017/004744 WO2017150126A1 (en) | 2016-02-29 | 2017-02-09 | Heat exchanger and air conditioner |
Publications (3)
Publication Number | Publication Date |
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EP3425321A1 true EP3425321A1 (en) | 2019-01-09 |
EP3425321A4 EP3425321A4 (en) | 2019-02-20 |
EP3425321B1 EP3425321B1 (en) | 2021-01-27 |
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EP17759597.2A Active EP3425321B1 (en) | 2016-02-29 | 2017-02-09 | Heat exchanger and air conditioner |
Country Status (3)
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EP (1) | EP3425321B1 (en) |
JP (1) | JP6145189B1 (en) |
WO (1) | WO2017150126A1 (en) |
Cited By (2)
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EP3922941A4 (en) * | 2019-02-04 | 2022-02-16 | Mitsubishi Electric Corporation | Heat exchanger and air-conditioner provided with same |
WO2022069528A1 (en) * | 2020-09-29 | 2022-04-07 | Miba Emobility Gmbh | Cooling device for a rechargeable battery |
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CN107270591B (en) * | 2017-07-24 | 2022-11-18 | 江苏必领能源科技有限公司 | Two-phase distributor for falling film evaporator |
JP6466047B1 (en) * | 2018-08-22 | 2019-02-06 | 三菱電機株式会社 | Heat exchanger and air conditioner |
WO2020217271A1 (en) * | 2019-04-22 | 2020-10-29 | 三菱電機株式会社 | Refrigerant distributor, heat exchanger, and refrigeration cycle device |
JP7195434B2 (en) * | 2019-07-08 | 2022-12-23 | 三菱電機株式会社 | Refrigerant distributors, heat exchangers, heat exchanger units, and refrigeration cycle devices |
CN114174758B (en) * | 2019-07-31 | 2024-09-20 | 日本开利株式会社 | Heat exchanger and refrigeration cycle device |
JP6927352B1 (en) * | 2020-03-23 | 2021-08-25 | 株式会社富士通ゼネラル | Heat exchanger |
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JPS648086U (en) * | 1987-07-02 | 1989-01-17 | ||
JP3373940B2 (en) * | 1994-07-14 | 2003-02-04 | シャープ株式会社 | Heat exchanger |
JP2007333311A (en) * | 2006-06-15 | 2007-12-27 | Calsonic Kansei Corp | Heat exchanger |
WO2009048451A1 (en) * | 2007-10-12 | 2009-04-16 | Carrier Corporation | Heat exchangers having baffled manifolds |
JP4881276B2 (en) * | 2007-10-19 | 2012-02-22 | 株式会社ティラド | Heat exchanger manufacturing method and heat exchanger |
JP5376010B2 (en) * | 2011-11-22 | 2013-12-25 | ダイキン工業株式会社 | Heat exchanger |
JP2015055414A (en) * | 2013-09-11 | 2015-03-23 | ダイキン工業株式会社 | Heat exchanger |
JP5741657B2 (en) * | 2013-09-11 | 2015-07-01 | ダイキン工業株式会社 | Heat exchanger and air conditioner |
-
2016
- 2016-02-29 JP JP2016038327A patent/JP6145189B1/en active Active
-
2017
- 2017-02-09 EP EP17759597.2A patent/EP3425321B1/en active Active
- 2017-02-09 WO PCT/JP2017/004744 patent/WO2017150126A1/en active Application Filing
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3922941A4 (en) * | 2019-02-04 | 2022-02-16 | Mitsubishi Electric Corporation | Heat exchanger and air-conditioner provided with same |
WO2022069528A1 (en) * | 2020-09-29 | 2022-04-07 | Miba Emobility Gmbh | Cooling device for a rechargeable battery |
Also Published As
Publication number | Publication date |
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EP3425321B1 (en) | 2021-01-27 |
JP6145189B1 (en) | 2017-06-07 |
JP2017155989A (en) | 2017-09-07 |
EP3425321A4 (en) | 2019-02-20 |
WO2017150126A1 (en) | 2017-09-08 |
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