The present disclosure relates to a heat exchanger and a refrigeration cycle apparatus.
Japanese Patent Laying-Open No. 2015-113983 discloses a heat exchanger including: a first heat exchange element having a plurality of first flat tubes; a second heat exchange element having a plurality of second flat tubes; and a folded header at which refrigerant having passed through the first heat exchange element is turned and introduced into the second heat exchange element.
PTL 1: Japanese Patent Laying-Open No. 2015-113983
In the above-mentioned heat exchanger, since each of the first flat tubes and each of the second flat tubes are disposed at the same height in the vertical direction, one of each first flat tube and each second flat tube is located downstream of the other in the ventilation direction. In other words, in the ventilation direction, the flat tubes disposed on the downstream side are located in the dead water zone formed behind the flat tubes disposed on the upstream side. As a result, in the above-mentioned heat exchanger, the heat exchange performance of the heat exchange element disposed downstream in the ventilation direction cannot be sufficiently exhibited.
A main object of the present disclosure is to provide a heat exchanger enhanced in heat exchange performance as compared with the above-mentioned conventional heat exchanger, and a refrigeration cycle apparatus including the heat exchanger.
A heat exchanger according to a first aspect of the present disclosure includes: a first heat exchange portion and a second heat exchange portion arranged side by side in a first direction intersecting with a direction of gravity. The first heat exchange portion has: a plurality of first fins extending in the direction of gravity and arranged side by side in a second direction intersecting with the direction of gravity and the first direction; and a plurality of first flat tubes mounted to intersect with each of the first fins and arranged side by side in the direction of gravity. The second heat exchange portion has: a plurality of second fins extending in the direction of gravity and arranged side by side in the second direction; and a plurality of second flat tubes mounted to intersect with each of the second fins and arranged side by side in the direction of gravity. The heat exchanger further includes: a first header connected to a first end of each of the first flat tubes; a second header connected to a first end of each of the second flat tubes; and a third header connected to a second end of each of the first flat tubes and a second end of each of the second flat tubes. When viewed in the first direction, each of the second flat tubes is disposed not to overlap with each of the first flat tubes. The third header has: a first plate provided with a plurality of first insertion holes through which the second ends of the first flat tubes are respectively inserted, and a plurality of second insertion holes through which the second ends of the second flat tubes are respectively inserted; and a second plate provided with a plurality of communication spaces each communicating with a corresponding one of the first insertion holes and a corresponding one of the second insertion holes.
A heat exchanger according to a second aspect of the present disclosure includes a first heat exchange portion and a second heat exchange portion arranged side by side in a first direction intersecting with a direction of gravity. The first heat exchange portion has: a plurality of first fins extending in the direction of gravity and arranged side by side in a second direction intersecting with the direction of gravity and the first direction; and a plurality of first flat tubes mounted to intersect with each of the first fins and arranged side by side in the direction of gravity. The second heat exchange portion has: a plurality of second fins extending in the direction of gravity and arranged side by side in the second direction; and a plurality of second flat tubes mounted to intersect with each of the second fins and arranged side by side in the direction of gravity. The heat exchanger further includes: a first header connected to a first end of each of the first flat tubes; a second header connected to a first end of each of the second flat tubes; and a third header connected to a second end of each of the first flat tubes and a second end of each of the second flat tubes, the third header being provided with a plurality of communication spaces each communicating with a corresponding one of the first flat tubes and a corresponding one of the second flat tubes. When viewed in the first direction, each of the second flat tubes is disposed not to overlap with each of the first flat tubes. At least one of the first flat tubes that is connected to one communication space of the communication spaces is located lower in the direction of gravity than at least one of the second flat tubes that is connected to the one communication space.
The present disclosure can provide a heat exchanger improved in heat exchange performance as compared with the above-mentioned conventional heat exchanger, and a refrigeration cycle apparatus including the heat exchanger.
The following describes embodiments as examples of a heat exchanger according to the present disclosure with reference to the accompanying drawings. In the accompanying drawings, the same or corresponding portions are denoted by the same reference characters, and the description thereof will not be repeated. Further, in each of the figures, for convenience of explanation, an X direction, a Y direction, and a Z direction orthogonal to each other are introduced. The X direction and the Y direction corresponds to the horizontal direction while the Z direction corresponds to the direction of gravity.
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The inner circumferential surface of each through hole provided in second plate 15B has a pair of inclined surfaces facing each other in the Z direction and inclined with respect to the X direction and the Y direction. The pair of inclined surfaces is inclined gradually upward to the leeward side. The distance between the pair of inclined surfaces in the Z direction is larger than the width of each first insertion hole 16 in the Z direction and the width of each second insertion hole 17 in the Z direction.
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In heat exchanger 100, each of second flat tubes 4 is disposed not to overlap with each of first flat tubes 2 when viewed in the Y direction. In other words, in heat exchanger 100, each second flat tube 4 disposed on the leeward side is not located in the dead water zone of each first flat tube 2 disposed on the windward side. Thus, the heat exchange performance of heat exchanger 100 is enhanced as compared with the heat exchange performance of the heat exchanger in which each first flat tube and each second flat tube are disposed at the same height in the vertical direction.
Further, bridging header 15 of heat exchanger 100 includes: first plate 15A provided with first insertion holes 16 through which the second ends of first flat tubes 2 are respectively inserted and second insertion holes 17 through which the second ends of second flat tubes 4 are respectively inserted; and second plate 15B provided with communication spaces 18 each communicating with a corresponding one of first insertion holes 16 and a corresponding one of second insertion holes 17.
In bridging header 15 as described above, each of first plate 15A and second plate 15B formed of separate plate members is provided with: first insertion holes 16 and second insertion holes 17 through which first flat tubes 2 and second flat tubes 4 are respectively inserted; and communication spaces 18 each providing communication between each first flat tube 2 and each second flat tube 4 for refrigerant to flow therebetween. Thus, the degree of freedom for the shapes of each first insertion hole 16, each second insertion hole 17, and each communication space 18 in bridging header 15 is enhanced as compared with the degree of freedom for the shape of the bridging header in which each first insertion hole, each second insertion hole, and each communication space are formed in one member. As a result, in bridging header 15, even when each second flat tube 4 is disposed not to overlap with each first flat tube 2 when viewed in the Y direction, the insertion margins for each first insertion hole 16 and each second insertion hole 17 can be readily ensured and the volume of each communication space 18 can be readily increased, as compared with the bridging header in which each first insertion hole, each second insertion hole, and each communication space are provided in one member.
As a result, in heat exchanger 100 including bridging header 15 described above, the heat exchange performance can be readily enhanced as compared with the heat exchanger including the bridging header in which each first insertion hole, each second insertion hole, and each communication space are provided in one member.
In heat exchanger 100, first plate 15A is smaller in thickness than second plate 15B. This makes it possible to simultaneously increase the volume of each communication space 18 and the insertion margins for each first insertion hole 16 and each second insertion hole 17, as compared with the case in which the thickness of first plate 15A is equal to or larger than the thickness of second plate 15B.
In heat exchanger 100, one first flat tube 2 connected to one communication space 18 is located lower in the Z direction than one second flat tube 4 connected to this one communication space 18.
In this way, when refrigerant flows from second flat tube 4 to first flat tube 2 through communication space 18, gravity acts on this refrigerant in the flow direction of the refrigerant. In such heat exchanger 100, as compared with the heat exchanger in which each first flat tube and each second flat tube are disposed at the same height in the vertical direction, the pressure loss of the gas-liquid two-phase refrigerant having flowed out of second flat tube 4 is reduced, so that the heat exchange performance is enhanced.
Each communication space 18 only needs to provide communication between at least one first flat tube 2 and at least one second flat tube 4 for refrigerant to flow therebetween. Each communication space 18 may be formed, for example, to provide communication between the plurality of first flat tubes 2 and the plurality of second flat tubes 4 for refrigerant to flow therebetween.
Second plate 15B may be provided with a plurality of recesses in place of the plurality of through holes. In this case, each communication space 18 is formed of an inner space of a recess provided in second plate 15B. Bridging header 15 may not include third plate 15C and may be formed as a multilayer body of first plate 15A and second plate 15B.
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In bridging header 15, second plate 15B may be configured as a multilayer body formed of a plurality of plates. As long as the entire thickness of second plate 15B is larger than the thickness of first plate 15A, the thickness of each plate forming second plate 15B may be equal to or smaller than the thickness of first plate 15A.
In this way, the pressure resistance of second plate 15B can be enhanced without impairing the formability of second plate 15B as compared with the case in which second plate 15B is formed as one plate.
Further, in bridging header 15, the plurality of first insertion holes 16, the plurality of second insertion holes 17, and the plurality of communication spaces 18 may be provided in one member. Bridging header 15 as described above may be formed by laser processing, for example.
A heat exchanger according to the second embodiment has basically the same configuration and exhibits basically the same effect as those of heat exchanger 100 according to the first embodiment, but is different from heat exchanger 100 in that each first flat tube 2 and each second flat tube 4 have upper surfaces 2A and 4A, respectively, inclined with respect to the horizontal direction and that each communication space 18 extends along upper surfaces 2A and 4A, as shown in
The angle formed by upper surface 2A with respect to the horizontal direction is 5 degrees or more and 45 degrees or less, for example. The angle formed by upper surface 4A with respect to the horizontal direction is 5 degrees or more and 45 degrees or less, for example. The angle formed by upper surface 2A of first flat tube 2 with respect to the horizontal direction is, for example, equal to the angle formed by upper surface 4A of second flat tube 4 with respect to the horizontal direction. Upper surface 2A of one first flat tube 2 connected to one communication space 18 is, for example, disposed to be flush with upper surface 4A of one second flat tube 4 connected to this one communication space 18.
In the heat exchanger according to the second embodiment, each first flat tube 2 and each second flat tube 4 have upper surfaces 2A and 4A, respectively, inclined with respect to the horizontal direction, and each communication space 18 extends along upper surfaces 2A and 4A, and thereby, imbalance in distribution of the refrigerant from communication space 18 to the flow paths of first flat tubes 2 is suppressed.
Note that modifications similar to those of the heat exchanger according to the first embodiment are allowable also in the heat exchanger according to the second embodiment.
A heat exchanger 101 according to the third embodiment has basically the same configuration and exhibits basically the same effect as those of heat exchanger 100 according to the first embodiment, but is different from heat exchanger 100 in that bridging header 15 is divided into a plurality of sections as shown in
Bridging header 15 is divided into a first bridging header 19 disposed above in the Z direction and a second bridging header 20 disposed below in the Z direction. The plurality of first flat tubes 2 are divided into first flat tubes 2 of a first group disposed above and first flat tubes 2 of a second group disposed below first flat tubes 2 of the first group. The plurality of second flat tubes 4 are divided into second flat tubes 4 of a first group disposed above and second flat tubes 4 of a second group disposed below second flat tubes 4 of the first group.
First bridging header 19 is connected to each of the second ends of first flat tubes 2 of the first group and each of the second ends of second flat tubes 4 of the first group, and allows merging of the refrigerant having flowed out of each of second flat tubes 4 of the first group and also allows splitting of the refrigerant that is to flow into each of first flat tubes 2 of the first group.
Second bridging header 20 is connected to each of the second ends of first flat tubes 2 of the second group and each of the second ends of second flat tubes 4 of the second group, and allows merging of the refrigerant having flowed out of each of second flat tubes 4 of the second group and also allows splitting of the refrigerant that is to flow into each of first flat tubes 2 of the second group.
First bridging header 19 includes a first plate 19A, a second plate 19B, and a third plate 19C. First plate 19A, second plate 19B, and third plate 19C have the same configurations as those of first plate 15A, second plate 15B, and third plate 15C described above.
Second bridging header 20 includes a first plate 20A, a second plate 20B, and a third plate 20C. First plate 20A, second plate 20B, and third plate 20C have the same configurations as those of first plate 15A, second plate 15B, and third plate 15C described above.
First plates 19A and 20A are configured as plate members different from each other, for example. Second plates 19B and 20B are configured as plate members different from each other, for example. Third plates 19C and 20C are configured as plate members different from each other, for example. Note that first plates 19A and 20A may be configured as one plate member. Second plates 19B and 20B may be configured as one plate member. Third plates 19C and 20C may be configured as one plate member, for example.
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The inner circumferential surface of each through hole provided in each of second plates 19B and 20B has a pair of inclined surfaces facing each other in the Z direction and inclined with respect to the X direction and the Y direction. The pair of inclined surfaces is inclined gradually upward to the leeward side. The distance between the pair of inclined surfaces in the Z direction is larger than the width of each first insertion hole 21 in the Z direction and the width of each second insertion hole 22 in the Z direction.
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Note that modifications similar to those of the heat exchanger according to the first embodiment are allowable also in heat exchanger 101 according to the third embodiment.
A refrigeration cycle apparatus 200 according to the fourth embodiment includes any one of the heat exchangers according to the first to third embodiments as an evaporator. Refrigeration cycle apparatus 200 mainly includes a compressor 111, heat exchangers 100, 101, a heat exchanger 113, and an expansion valve 114. In refrigeration cycle apparatus 200, second header 14 serves as an inflow portion of refrigerant, and first header 13 serves as an outflow portion of refrigerant. In each of heat exchangers 100 and 101 serving as evaporators, the refrigerant flows through second header 14, second heat exchange portion 12, bridging header 15, first heat exchange portion 11, and first header 13 in this order. The gas-liquid two-phase refrigerant that has been condensed in heat exchanger 113 and then decompressed by expansion valve 114 flows into second header 14. The gas-liquid two-phase refrigerant exchanges heat with air flowing in the Y direction through second heat exchange portion 12 and first heat exchange portion 11 and thereby evaporates and turns into gas-phase refrigerant. This gas-phase refrigerant flows out of first header 13 and is suctioned into compressor 111. Note that refrigeration cycle apparatus 200 may further include a four-way valve 112 for switching the flow direction of the refrigerant. Four-way valve 112 switches the operation mode between an operation mode in which heat exchanger 100, 101 serves as an evaporator and an operation mode in which heat exchanger 100, 101 serves as a condenser.
Although the embodiments of the present disclosure have been described as above, the above-described embodiments can also be variously modified. Further, the scope of the present disclosure is not limited to the above-described embodiments. The scope of the present disclosure is defined by the terms of the claims and is intended to include any modifications within the meaning and scope equivalent to the terms of the claims.
This application is a U.S. national stage application of International Patent Application No. PCT/JP2020/039355 filed on Oct. 20, 2020, the disclosure of which is incorporated herein by reference.
Filing Document | Filing Date | Country | Kind |
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PCT/JP2020/039355 | 10/20/2020 | WO |