WO2014171095A1 - 熱交換器 - Google Patents
熱交換器 Download PDFInfo
- Publication number
- WO2014171095A1 WO2014171095A1 PCT/JP2014/001948 JP2014001948W WO2014171095A1 WO 2014171095 A1 WO2014171095 A1 WO 2014171095A1 JP 2014001948 W JP2014001948 W JP 2014001948W WO 2014171095 A1 WO2014171095 A1 WO 2014171095A1
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- WO
- WIPO (PCT)
- Prior art keywords
- heat exchange
- exchange tube
- flow path
- segment
- heat exchanger
- Prior art date
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Classifications
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- 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
- F28D1/03—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 plate-like or laminated conduits
- F28D1/0308—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 plate-like or laminated conduits the conduits being formed by paired plates touching each other
- F28D1/0325—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 plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another
- F28D1/0333—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 plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another the plates having integrated connecting members
- F28D1/0341—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 plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another the plates having integrated connecting members with U-flow or serpentine-flow inside the conduits
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- 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
- F28D1/05375—Assemblies of conduits connected to common headers, e.g. core type radiators with particular pattern of flow, e.g. change of flow direction
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2270/00—Thermal insulation; Thermal decoupling
Definitions
- the present invention relates to a heat exchanger.
- Patent Document 1 discloses a heat exchanger 301 having a heat exchange tube 302.
- the heat exchanging tube 302 is formed by bending a single plate material so that the central portion 302A has a flat tubular shape, and widened portions 302B and 302C having both ends opened at a thickness about 2 to 4 times that of the central portion 302A. It is formed to become.
- Patent Document 1 describes that the heat exchange tube 302 may have a zigzag-shaped refrigerant flow path, and that the zigzag-shaped refrigerant flow path may be separated by a space.
- Patent Document 2 discloses that a laminated evaporator is formed by bending and bonding a metal plate 401 having a first recess 402A, a second recess 402B, and a partition 403 at the position of the center line X. A method of manufacturing a device for use is described.
- Patent Document 3 includes a pair of upper and lower plate-like members 503 ⁇ / b> A and 503 ⁇ / b> B in which a plurality of rows of semicircular or elliptical concave portions 501 and flat portions 502 are alternately provided.
- a heat exchange tube 510 having a shape in which a plurality of tubes 511 are connected by ribs 512 is disclosed.
- Patent Document 3 describes that adjacent heat exchange tubes 510 may be alternately moved in the vertical direction, and the heat exchange tubes 510 may be arranged in a staggered manner.
- JP 2008-39322 A JP-A-6-106335 Japanese Patent No. 4451981
- Patent Document 1 enables the heat exchanger to be reduced in size and weight.
- the technique disclosed in Patent Document 2 makes it possible to inexpensively manufacture a laminated evaporator (heat exchanger) with good performance.
- the technique disclosed in Patent Document 3 makes it possible to reduce the pressure loss of the airflow flowing through the external flow path formed between adjacent heat exchange tubes at a low cost.
- new proposals that exceed the techniques disclosed in Patent Documents 1 to 3 are required.
- An object of the present invention is to reduce the pressure loss of a fluid flowing in an external flow path formed between adjacent heat exchange tubes while reducing the size of a heat exchange tube.
- this disclosure An internal flow path through which the first fluid flows, an inlet of the internal flow path, and an outlet of the internal flow path are formed, and an external flow path for the second fluid that is to exchange heat with the first fluid is formed.
- the internal flow path has a plurality of segments extending in a specific row direction of the heat exchange tubes,
- the heat exchange tube is composed of a set of plate members bonded together so that the internal flow path is formed, and (i) protrudes on both sides in the thickness direction of the heat exchange tube, and the internal flow path A plurality of flow path forming portions respectively forming the segments, and (ii) located between the flow path forming portions and the flow path forming portions adjacent to each other in the width direction orthogonal to the row direction, A thin-walled portion separating the segments of the internal flow path from each other along the row direction; and (iii) the thickness of the heat exchange tube formed around the inlet of the internal flow path A first protrusion protruding in the direction; and (
- first heat exchange tube When a set of the heat exchange tubes adjacent to each other is defined as a first heat exchange tube and a second heat exchange tube, respectively,
- the first protrusion of the first heat exchange tube is joined to a portion around the inlet of the second heat exchange tube, and the second protrusion of the first heat exchange tube is connected to the second heat exchange tube.
- the flow path forming portion of the first heat exchange tube faces the thin portion of the second heat exchange tube via the external flow channel, and the second heat exchange tube
- the flow path forming part faces the thin part of the first heat exchange tube via the external flow path;
- a heat exchanger in which the plurality of flow path forming portions of the first heat exchange tube and the plurality of flow path forming portions of the second heat exchange tube are arranged in a staggered manner in the width direction.
- the heat exchanger can be reduced in size, and the pressure loss of the fluid flowing in the external flow path formed between the adjacent heat exchange tubes can be reduced.
- the perspective view of the heat exchanger which concerns on 1st Embodiment of this invention.
- the disassembled perspective view of the 1st heat exchange tube of the heat exchanger of FIG. The disassembled perspective view of the 2nd heat exchange tube of the heat exchanger of FIG.
- FIG. 2B The top view of the 2nd board
- ruptured a part of heat exchange tube of FIG. The disassembled perspective view of the 1st heat exchange tube of the heat exchanger which concerns on 2nd Embodiment of this invention.
- the disassembled perspective view of the 2nd heat exchange tube of the heat exchanger which concerns on 2nd Embodiment of this invention The perspective view of the 1st board
- FIG. 7A Sectional drawing along the IX-IX line of the 1st heat exchange tube of FIG. 7A, and the 2nd heat exchange tube of FIG. 7B.
- the thickness of the heat exchange tube 302 is at least the thickness of four plates. It is also difficult to insert a jig or braze inside the heat exchange tube 302. For these reasons, it is not easy to reduce the size and performance of the heat exchanger 301 described in Patent Document 1.
- the first aspect of the present disclosure is: An internal flow path through which the first fluid flows, an inlet of the internal flow path, and an outlet of the internal flow path are formed, and an external flow path for the second fluid that is to exchange heat with the first fluid is formed.
- the internal flow path has a plurality of segments extending in a specific row direction of the heat exchange tubes,
- the heat exchange tube is composed of a set of plate members bonded together so that the internal flow path is formed, and (i) protrudes on both sides in the thickness direction of the heat exchange tube, and the internal flow path
- first heat exchange tube When a set of the heat exchange tubes adjacent to each other is defined as a first heat exchange tube and a second heat exchange tube, respectively,
- the first protrusion of the first heat exchange tube is joined to a portion around the inlet of the second heat exchange tube, and the second protrusion of the first heat exchange tube is connected to the second heat exchange tube.
- the flow path forming portion of the first heat exchange tube faces the thin portion of the second heat exchange tube via the external flow channel, and the second heat exchange tube
- the flow path forming part faces the thin part of the first heat exchange tube via the external flow path;
- a heat exchanger in which the plurality of flow path forming portions of the first heat exchange tube and the plurality of flow path forming portions of the second heat exchange tube are arranged in a staggered manner in the width direction.
- the heat exchange tube is composed of a set of plate members that are bonded together so that an internal flow path is formed.
- the thickness of such a heat exchange tube is at least the thickness of two sheets of plate material. That is, according to the first aspect, the heat exchange tube can be thinned. This directly leads to a reduction in the size of the heat exchanger.
- the heat exchange tube is manufactured by bonding a set of plate materials, the jig can be used and brazed relatively easily.
- the 1st protrusion part and 2nd protrusion part of a 1st heat exchange tube are joined to the part around the inlet_port
- a heat exchanger can be reduced in size compared with the case where the separate hollow tube which couple
- the variation in the width of the external flow path (the interval between adjacent heat exchange tubes) in the thickness direction of the heat exchange tube is small in the width direction of the heat exchange tube (the flow direction of the second fluid).
- the pressure loss of the second fluid flowing through the external flow path can be reduced.
- the heat exchange tube has a rectangular shape in a plan view, and the heat exchange tube includes one end portion and the other end portion in the longitudinal direction of the heat exchange tube.
- a pair of openings as the inlet and the outlet is provided in each of the first and second outlets so as to penetrate the heat exchange tube in the thickness direction.
- the plurality of heat exchange tubes have the same structure, and the inlet of the second heat exchange tube is the first heat exchange tube. In the plane perpendicular to the thickness direction of the heat exchange tube so that the outlet of the second heat exchange tube communicates with the inlet of the first heat exchange tube.
- the positions of the plurality of flow path forming portions and the thin wall portions of the first heat exchange tubes are the width direction, and the positions of the second heat exchange tubes Provided is a heat exchanger that matches the positions of a plurality of flow path forming portions and the thin wall portion. According to such a structure, since the metal mold
- the heat exchange tube is parallel to the width direction in at least one selected from one end side and the other end side in the width direction.
- a heat exchanger is further provided that further includes a plate-like portion protruding in the direction. According to such a structure, since a plate-shaped part functions as a heat-transfer fin, the heat exchange capability of a heat exchanger improves. In particular, when the plate-like portion is protruded in the direction in which the second fluid flows, peeling of the second fluid at the end of the heat exchange tube can be suppressed by the plate-like portion, so that the heat exchange efficiency of the heat exchanger is improved. To do.
- the adjacent heat exchange tubes are wide at the inlet and outlet of the external flow path (second fluid flow path), so that frost formation occurs. Hard to happen. For this reason, in a heat exchanger that only performs heat dissipation from the first fluid to the second fluid, it is desirable to provide a plate-like portion on the heat exchange tube. In a heat exchanger where the first fluid is supposed to absorb heat from the second fluid, it is desirable not to provide a plate-like portion on the heat exchange tube.
- the surface of the flow path forming portion in the cross section perpendicular to the column direction, has the thickness direction of the heat exchange tube and the thickness of the heat exchange tube.
- a heat exchanger extending from the thin portion in a direction inclined with respect to both directions in the width direction. According to such a configuration, when the second fluid flows through the external flow path, it is possible to suppress the separation of the second fluid on the surface of the flow path forming portion. Therefore, the heat exchange efficiency of the heat exchanger is further improved.
- the surface of the flow path forming portion and the surface of the thin portion are connected by a curve.
- a heat exchanger According to such a configuration, when the second fluid flows through the external flow path, it is possible to suppress separation of the second fluid in the vicinity of the boundary between the flow path forming portion and the thin portion. Therefore, the heat exchange efficiency of the heat exchanger is further improved.
- an outline of the flow path forming portion is configured by a curve
- a heat exchanger in which the outline of the flow path forming portion is configured by a combination of a straight line and a curve smoothly connected to the straight line.
- the flow path forming unit in addition to any one of the first to seventh aspects, is configured to join the pair of plate members in the heat exchange tube.
- a heat exchanger is provided that includes one part and the other part separated by a surface, wherein the one part and the other part are symmetrical with respect to the joining surface. According to such a configuration, the expansion and reduction of the width of the external channel can be further suppressed. Therefore, the pressure loss of the second fluid flowing outside the heat exchange tube can be further reduced.
- the internal flow path is a meandering flow in which the flow direction of the first fluid is reversed halfway from the inlet to the outlet.
- the plurality of segments include a first segment and a second segment through which the first fluid flows in a direction opposite to a flow direction of the first fluid in the first segment, and the internal flow path is
- the heat exchanger further includes a bent segment connecting the first segment and the second segment.
- the heat exchange tube is provided in the thin portion, and includes the first fluid flowing through the first segment and the first fluid flowing through the second segment.
- a heat exchanger further having an inhibition structure that inhibits heat transfer therebetween. According to such a configuration, the temperature difference between the first segment and the second segment is maintained. Therefore, the temperature efficiency of the heat exchanger is further improved, and the heat exchange efficiency of the heat exchanger is improved.
- the internal flow path is joined to the first protrusion of the heat exchange tube forming the end face of the heat exchanger.
- An inlet header for supplying the first fluid to the inlet, and the second protrusion of the heat exchange tube forming the end face of the heat exchanger, and the outlet of the internal flow path And an outlet header for discharging the first fluid from the heat exchanger.
- the internal flow path further includes a most upstream segment through which the first fluid flows, which is formed upstream of the first segment and around the inlet
- the heat exchange tube includes: (i) an uppermost thin portion that partitions the bent segment and the uppermost stream segment; and (ii) the first fluid that is provided in the uppermost thin portion and flows through the bent segment.
- an upstream inhibition structure that inhibits heat transfer between the first fluid flowing in the uppermost stream segment.
- the thirteenth aspect provides the heat exchanger according to the twelfth aspect, in which the upstream-side inhibition structure is formed in a portion closest to the inlet in the most upstream thin wall portion. There is a large temperature difference between the first fluid immediately after flowing into the internal flow path and the first fluid flowing through the bending segment. Therefore, when the upstream side inhibition structure is provided in the portion closest to the inlet, the heat transfer between the first fluid flowing through the bent segment and the first fluid flowing through the most upstream segment can be effectively inhibited.
- the upstream-side inhibition structure is a through-hole penetrating the most upstream thin portion in the thickness direction of the one set of plate members. Provide a bowl.
- the upstream side inhibition structure is a through hole, the uppermost stream segment and the bent segment of the internal flow path are separated by a space. Therefore, the heat transfer between the first fluid flowing through the most upstream segment and the first fluid flowing through the bending segment is reliably inhibited.
- the internal flow path further includes a most downstream segment formed downstream of the second segment and around the outlet, through which the first fluid flows
- the heat exchange tube includes: (i) a most downstream thin portion that partitions the bent segment and the most downstream segment; and (ii) the first fluid that is provided in the most downstream thin portion and flows through the bent segment.
- a downstream-side inhibition structure that inhibits heat transfer between the first fluid flowing in the most downstream segment.
- the sixteenth aspect provides the heat exchanger according to the fifteenth aspect, in which the downstream-side inhibition structure is formed in a portion closest to the outlet in the most downstream thin-walled portion. There is a large temperature difference between the first fluid flowing in the bent segment and the first fluid flowing in the most downstream segment. Therefore, when the downstream side inhibition structure is provided in the portion closest to the outlet, the heat transfer between the first fluid flowing through the bent segment and the first fluid flowing through the most downstream segment can be effectively inhibited.
- the downstream-side inhibition structure is a through-hole penetrating the most downstream thin portion in the thickness direction of the one set of plate members. Provide a bowl.
- the downstream side inhibition structure is a through hole, the most downstream segment and the bent segment of the internal flow path are separated by a space. Therefore, the heat transfer between the first fluid flowing through the most downstream segment and the first fluid flowing through the bent segment is reliably inhibited.
- the heat exchanger 1 As shown in FIG. 1, the heat exchanger 1 according to the first embodiment of the present invention includes a plurality of heat exchange tubes 2, an inlet header 10A, and an outlet header 10B.
- the plurality of heat exchange tubes 2 each have a rectangular shape in plan view, and are arranged at a predetermined interval.
- a first fluid for example, a refrigerant
- the plurality of heat exchange tubes 2 are assembled so that a flow path of a second fluid (for example, outside air) that should exchange heat with the first fluid is formed outside. Specifically, the flow path of the second fluid is formed between the adjacent heat exchange tubes 2.
- a second fluid for example, outside air
- the inlet header 10 ⁇ / b> A and the outlet header 10 ⁇ / b> B are attached to a heat exchange tube 2 that forms one end face (left end face in FIG. 1) of the heat exchanger 1 in the direction in which the heat exchange tubes 2 are arranged. According to such a structure, the heat exchanger 1 can be reduced in size compared with the case where a separate hollow tube including the inlet header 10A and the outlet header 10B is provided.
- the heat exchange tube 2 has an internal flow path 3 through which the first fluid flows.
- the inlet header 10 ⁇ / b> A is a pipe for supplying the first fluid to the inlet 3 ⁇ / b> A of the internal flow path 3.
- the outlet header 10 ⁇ / b> B is a pipe for discharging the first fluid from the outlet 3 ⁇ / b> B of the internal flow path 3.
- the inlet header 10A is connected to an external device (not shown) that supplies the first fluid.
- the outlet header 10B is connected to an external device (not shown) that collects the first fluid.
- the first fluid discharged from the external device is supplied to the internal flow path 3 of the heat exchange tube 2 from the inlet header 10A.
- the first fluid that has exchanged heat with the second fluid by passing through the internal flow path 3 is discharged from the outlet header 10B to an external device that collects the first fluid.
- the second fluid flows in a direction parallel to the width direction of the heat exchange tube 2 through a gap (external flow path 4) between adjacent heat exchange tubes 2.
- the width direction of the heat exchange tube 2 is a direction perpendicular to both the longitudinal direction of the heat exchange tube 2 and the arrangement direction of the plurality of heat exchange tubes 2.
- the upstream portion of the internal flow path 3 is located relatively downstream in the flow direction of the second fluid, and the downstream portion of the internal flow path 3 is relatively upstream in the flow direction of the second fluid. Is located. That is, the flow direction of the second fluid is pseudo-opposed to the flow direction of the first fluid.
- the heat exchange tube 2 is composed of a first plate member 11 and a second plate member 12 which are bonded together so that an internal flow path 3 is formed.
- the internal flow path 3 is a meandering flow path in which the flow direction of the first fluid is reversed in the middle from the inlet 3A to the outlet 3B. In the present embodiment, the flow direction of the first fluid is reversed a plurality of times (twice).
- the heat exchange tube 2 has a rectangular shape in plan view. The opening as the inlet 3A is formed on one end side in the longitudinal direction of the heat exchange tube 2 (lower side in FIG. 2A) so as to penetrate the heat exchange tube 2 in the thickness direction.
- the opening as the outlet 3B is formed on the other end side in the longitudinal direction of the heat exchange tube 2 (upper side in FIG. 2A) so as to penetrate the heat exchange tube 2 in the thickness direction.
- the internal flow path 3 has an odd number of portions extending in the column direction parallel to the longitudinal direction (three portions in the present embodiment, which are a first segment 31, a second segment 32, and a third segment 33 described later). )have.
- the internal flow path 3 includes three portions (a first segment 31, a second segment 32, and a third segment 33) that are parallel to each other. According to such a configuration, since the inner diameters of the inlet header 10A and the outlet header 10B can be increased, pressure loss inside the inlet header 10A and the outlet header 10B can be reduced. Furthermore, since the length of the width direction of the heat exchange tube 2 can be shortened, the heat exchanger 1 can be reduced in size.
- the internal flow path 3 includes the first segment 31, the second segment 32, the third segment 33, the first bent segment 34, the second bent segment 35, and the most upstream flow. It has a segment 36 and a most downstream segment 37.
- 3A shows the first plate member 11 when the first plate member 11 and the second plate member 12 are bonded together
- FIG. 3B shows the second plate member when the first plate member 11 and the second plate member 12 are bonded together. 12 is shown.
- the internal flow path 3 is a space formed when the first plate material 11 and the second plate material 12 are bonded together.
- the first segment 31 extends from the inlet 3 ⁇ / b> A along the longitudinal direction of the heat exchange tube 2.
- the second segment 32 extends so that the first fluid flows in a direction (downward in FIGS. 3A and 3B) opposite to the flow direction of the first fluid in the first segment 31 (upward in FIGS. 3A and 3B).
- the third segment 33 extends so that the first fluid flows in a direction opposite to the flow direction of the first fluid in the second segment 32 (downward in FIGS. 3A and 3B) (upward in FIGS. 3A and 3B).
- the first bent segment 34 connects the first segment 31 and the second segment 32.
- the second bent segment 35 connects the second segment 32 and the third segment 33.
- the most upstream segment 36 is a portion formed on the upstream side of the first segment 31 and around the inlet 3 ⁇ / b> A through which the first fluid flows.
- the most downstream segment 37 is a portion formed on the downstream side of the third segment 33 and around the outlet 3 ⁇ / b> B through which the first fluid flows.
- the first fluid supplied from the inlet header 10A is the inlet 3A, the most upstream segment 36, the first segment 31, the first bent segment 34, the second segment 32, the second bent segment 35, the third segment 33, and the most downstream segment. 37, flowing in the order of the outlet 3B and discharged from the outlet header 10B.
- the heat exchange tube 2 partitions the first thin portion 21 ⁇ / b> A that partitions the first segment 31 and the second segment 32, and the second segment 32 and the third segment 33. And a second thin portion 21B.
- a plurality of first through holes 22A are formed in the first thin portion 21A.
- a plurality of second through holes 22B are formed in the second thin portion 21B.
- the first thin part 21 ⁇ / b> A and the second thin part 21 ⁇ / b> B are joints between the first plate member 11 and the second plate member 12.
- the first through hole 22 ⁇ / b> A functions as an inhibition structure that inhibits heat transfer between the first fluid flowing through the first segment 31 and the first fluid flowing through the second segment 32.
- the second through hole 22 ⁇ / b> B functions as an inhibition structure that inhibits heat transfer between the first fluid flowing through the second segment 32 and the first fluid flowing through the third segment 33.
- the heat exchanger 1 can be miniaturized and the heat exchange efficiency of the heat exchanger 1 can be improved as compared with the conventional heat exchanger.
- the inhibition structure is the through holes 22A and 22B, adjacent segments of the internal flow path 3 are separated by a space. Therefore, the above heat transfer is reliably inhibited.
- the first through hole 22A is a through hole (specifically, a slit) penetrating the first thin portion 21A in the thickness direction of the first plate member 11 and the second plate member 12.
- 22 A of 1st through-holes are formed in the center part of the width direction of 21 A of 1st thin parts, and have a rectangular shape by planar view.
- the second through hole 22 ⁇ / b> B is a through hole (specifically, a slit) penetrating the second thin portion 21 ⁇ / b> B in the thickness direction of the first plate member 11 and the second plate member 12.
- the second through hole 22B is formed at the center in the width direction of the second thin portion 21B, and has a rectangular shape in plan view.
- the plurality of first through holes 22A are arranged at predetermined intervals along the longitudinal direction of the first thin portion 21A.
- the plurality of second through holes 22B are arranged at predetermined intervals along the longitudinal direction of the second thin portion 21B.
- the cross sectional area (total cross sectional area) of the first through hole 22A is 1 of the cross sectional area of the first thin portion 21A. Narrower than / 2.
- the cross-sectional area of the first through hole 22A is 20% to 50% of the cross-sectional area of the first thin portion 21A.
- the length L1 in the longitudinal direction of the first through hole 22A is longer than the length of the interval L2 between the adjacent first through holes 22A.
- the length L1 in the longitudinal direction of the first through hole 22A is twice to 10 times the length of the interval L2 between the adjacent first through holes 22A.
- the cross-sectional area of the second through hole 22B is narrower than 1 ⁇ 2 of the cross-sectional area of the second thin portion 21B.
- the cross-sectional area of the second through hole 22B is 20% to 50% of the cross-sectional area of the second thin portion 21B.
- the length L3 in the longitudinal direction of the second through hole 22B is longer than the length of the interval L4 between the adjacent second through holes 22B.
- the length L3 in the longitudinal direction of the second through hole 22B is twice to 10 times the length of the interval L4 between the adjacent second through holes 22B.
- the length L3 in the longitudinal direction of the second through hole 22B is the same as the length L1 in the longitudinal direction of the first through hole 22A.
- the length of the interval L4 between the adjacent second through holes 22B is the same as the length of the interval L2 between the adjacent first through holes 22A.
- the shape, arrangement, number, cross-sectional area, etc. of the first through hole 22A and the second through hole 22B are not particularly limited.
- the shape of the first through hole 22A may be other shapes such as a circle, a polygon, and an ellipse in plan view. Only one first through hole 22A may be formed in the first thin portion 21A.
- the first segment is suppressed while suppressing a decrease in strength of the first thin portion 21A.
- the heat transfer between the first fluid flowing through 31 and the first fluid flowing through the second segment 32 can be effectively inhibited. Further, the warpage of the plate members 11 and 12 can be suppressed when the plate members 11 and 12 are processed. These also apply to the second through hole 22B.
- the heat exchange tube 2 is provided in the most upstream thin wall portion 23 that partitions the second bent segment 35 and the most upstream segment 36, and the most upstream thin wall portion 23.
- a third through hole 24 is provided.
- the most upstream thin portion 23 is a thin portion formed when the first plate member 11 and the second plate member 12 are bonded together.
- the third through-hole 24 functions as an upstream-side inhibition structure that inhibits heat transfer between the first fluid that flows through the second bent segment 35 and the first fluid that flows through the most upstream segment 36.
- the third through hole 24 is formed in a portion closest to the inlet 3 ⁇ / b> A in the most upstream thin portion 23.
- the third through hole 24 is a through hole (specifically, a slit) that penetrates the most upstream thin portion 23 in the thickness direction of the first plate member 11 and the second plate member 12.
- the third through hole 24 is formed at the center of the uppermost stream thin portion 23 and has a rectangular shape in plan view. According to such a configuration, heat transfer between the first fluid flowing through the second bent segment 35 and the first fluid flowing through the most upstream segment 36 can be effectively and reliably inhibited.
- the heat exchange tube 2 is provided in the most downstream thin portion 25 that partitions the first bent segment 34 and the most downstream segment 37, and in the most downstream thin portion 25.
- a fourth through hole 26 is provided.
- the most downstream thin portion 25 is a thin portion formed when the first plate member 11 and the second plate member 12 are bonded together.
- the fourth through hole 26 functions as a downstream-side inhibition structure that inhibits heat transfer between the first fluid flowing through the first bent segment 34 and the first fluid flowing through the most downstream segment 37.
- the fourth through hole 26 is formed in a portion closest to the outlet 3 ⁇ / b> B in the most downstream thin portion 25.
- the fourth through hole 26 is a through hole (specifically, a slit) that penetrates the most downstream thin portion 25 in the thickness direction of the first plate member 11 and the second plate member 12.
- the fourth through-hole 26 is formed at the center of the most downstream thin portion 25 and has a rectangular shape in plan view. According to such a configuration, heat transfer between the first fluid flowing through the first bent segment 34 and the first fluid flowing through the most downstream segment 37 can be effectively and reliably inhibited.
- the shape, arrangement, number, cross-sectional area, and the like of the third through hole 24 and the fourth through hole 26 are not particularly limited.
- the heat exchange tube 2 includes a first protrusion 41, a second protrusion 42, a third protrusion 51, a fourth protrusion 52, And an outer edge portion 43.
- the first protrusion 41 is formed around the inlet 3A of the first plate member 11 and protrudes to one side in the thickness direction (left side in FIG. 2A).
- the second protrusion 42 is formed around the outlet 3 ⁇ / b> B of the first plate 11 and protrudes to one side (left side in FIG. 2A) in the thickness direction of the first plate 11.
- the third protrusion 51 is formed around the inlet 3A of the second plate 12 and protrudes to one side (the right side in FIG.
- the fourth protrusion 52 is formed around the outlet 3 ⁇ / b> B of the second plate 12 and protrudes to one side (the right side in FIG. 2A) of the second plate 12 in the thickness direction.
- the outer edge portion 43 is formed by the outer edge portion of the first plate member 11 and the outer edge portion of the second plate member 12. The outer edge portion of the first plate member 11 protrudes to the other side (the right side in FIG. 2A) of the first plate member 11 in the thickness direction. The outer edge portion of the second plate member 12 protrudes to the other side in the thickness direction of the second plate member 12 (left side in FIG. 2A).
- the first protrusion 41, the second protrusion 42, the third protrusion 51, and the fourth protrusion 52 each have an annular shape in plan view.
- the outer edge portion 43 has a frame shape in plan view.
- the outer edge portion 43 functions as a brazing portion when the first plate member 11 and the second plate member 12 are brazed together.
- the outer edge 43 is connected to the most downstream thin portion 23 and the most downstream thin portion 25.
- the most upstream thin portion 23 and the most downstream thin portion 25 also function as brazing portions.
- the most upstream thin portion 23 and the most downstream thin portion 25 are connected to the first thin portion 21A and the second thin portion 21B, respectively.
- the first thin part 21A and the second thin part 21B also function as brazing parts.
- the first through hole 22A is formed in the first thin portion 21A.
- a first thin portion 21A as a brazing portion around the first through hole 22A.
- Other thin portions and through holes have the same structure.
- the minimum width of the brazing part in the cross section parallel to the direction orthogonal to the thickness direction of the first plate member 11 and the second plate member 12 is larger than the thickness of the first plate member 11 and the second plate member 12. That is, when the heat exchange tube 2 is viewed in plan, the minimum widths of the first thin portion 21A, the second thin portion 21B, the most upstream thin portion 23, the most downstream thin portion 25, and the outer edge portion 43 are the first plate material 11 and It is larger than each thickness of the second plate 12.
- the areas of the first thin part 21A, the second thin part 21B, the most upstream thin part 23, the most downstream thin part 25, and the outer edge part 43 as brazing parts can be sufficiently secured.
- the 1 board material 11 and the 2nd board material 12 can be joined firmly.
- a clad material in which a brazing material such as silver brazing is coated on both surfaces of an aluminum alloy plate or a stainless alloy plate is prepared as the first plate material 11 and the second plate material 12.
- portions corresponding to the outer edge portion 43, the first thin portion 21A, the second thin portion 21B, the most upstream thin portion 23, and the most downstream thin portion 25 are formed by roll processing or press processing into the first plate member 11 and the second plate member.
- Each of 12 is formed.
- Holes for forming the first through hole 22A, the second through hole 22B, the third through hole 24, and the fourth through hole 26 are formed in the first plate member 11 and the second plate member 12 at the same time.
- the first plate member 11 and the second plate member 12 are overlapped so that the first thin portion 21A, the second thin portion 21B, the most upstream thin portion 23, the most downstream thin portion 25, and the outer edge portion 43 are formed.
- Pressure and heat are applied between the first plate member 11 and the second plate member 12.
- the heat exchange tube 2 is obtained by brazing the 1st board
- plate material 12 it cuts into the 1st through-hole by the 1st thin part 21A, the 2nd thin part 21B, the most upstream thin part 23, and the most downstream thin part 25. 22A, 2nd through-hole 22B, 3rd through-hole 24, and 4th through-hole 26 may be formed.
- the plurality of heat exchange tubes 2 are directly joined to each other.
- a set of heat exchange tubes 2 adjacent to each other is defined as a first heat exchange tube 2A and a second heat exchange tube 2B, respectively.
- FIG. 2A shows a first plate 11 of the first heat exchange tube 2A and a second plate 12 of the first heat exchange tube 2A.
- FIG. 2B shows the first plate member 11 of the second heat exchange tube 2B and the second plate member 12 of the second heat exchange tube 2B.
- FIG. 2C shows the first plate 11 of the first heat exchange tube 2A and the second plate 12 of the second heat exchange tube 2B.
- the first heat exchange tube 2A and the second heat exchange tube 2B have the same structure. As shown in FIG.
- the second heat exchange tube 2B is obtained by rotating the first heat exchange tube 2A by 180 degrees.
- the 1st heat exchange tube 2A is arrange
- the inlet 3A and the outlet 3B of the internal flow path 3 of the first heat exchange tube 2A are arranged at positions symmetrical with respect to the center line S1 in the longitudinal direction of the heat exchange tube 2.
- the center P1 of the inlet 3A and the center Q1 of the outlet 3B are at positions offset in the width direction with respect to the center line R1 in the width direction of the heat exchange tube 2.
- the inlet 3C and the outlet 3D of the internal flow path 3 of the second heat exchange tube 2B are arranged at positions symmetrical with respect to the center line S2 in the longitudinal direction of the heat exchange tube 2.
- the center P2 of the inlet 3C and the center Q2 of the outlet 3D are at positions offset in the width direction with respect to the center line R2 in the width direction of the heat exchange tube 2.
- the second heat exchange tube 2B is obtained by rotating 180 degrees around the center point O1 of the first heat exchange tube 2A shown in FIG. 3A.
- the center point O1 is an intersection of the center line S1 and the center line R1.
- the center point O2 of the second heat exchange tube 2B shown in FIG. 3C is at the same position as the center point O1 of the first heat exchange tube 2A. That is, when the center point O1 is orthogonally projected in the direction in which the heat exchange tubes 2 are arranged, the center point O1 overlaps the center point O2.
- the center point O2 is an intersection of the center line S2 and the center line R2.
- the structure of the internal flow path 3 of the 2nd heat exchange tube 2B is the same as the structure of the internal flow path 3 of the 1st heat exchange tube 2A, detailed description is abbreviate
- the internal flow path 3 has the first segment 31, the second segment 32, and the third segment 33 extending in the column direction as described above.
- the heat exchange tube 2 has a first flow path forming portion 61, a second flow path forming portion 62, and a third flow path forming portion 63.
- the first flow path forming portion 61 is a portion that protrudes on both sides (the upper side and the lower side in FIG. 4A) in the thickness direction of the heat exchange tube 2 and forms the first segment 31.
- the second flow path forming portion 62 is a portion that protrudes on both sides in the thickness direction of the heat exchange tube 2 and forms the second segment 32.
- the third flow path forming portion 63 is a portion that protrudes on both sides in the thickness direction of the heat exchange tube 2 and forms the third segment 33.
- 21 A of 1st thin parts are located between the 1st flow path formation part 61 and the 2nd flow path formation part 62 which are mutually adjacent in the width direction of the heat exchange tube 2.
- the second thin portion 21 ⁇ / b> B is located between the second flow path forming portion 62 and the third flow path forming portion 63 that are adjacent to each other in the width direction of the heat exchange tube 2.
- the first protrusion 41 of the first heat exchange tube 2A is joined to a portion around the inlet 3C of the second heat exchange tube 2B, and the second protrusion 42 of the first heat exchange tube 2A is joined. It is joined to a portion around the outlet 3D of the second heat exchange tube 2B.
- the first flow path forming portion 61 and the second flow path forming portion of the internal flow path 3 of the first heat exchange tube 2A. 62 faces the first thin portion 21A and the second thin portion 21B of the second heat exchange tube 2B via the external flow path 4, respectively.
- the second flow path forming part 62 and the third flow path forming part 63 of the internal flow path 3 of the second heat exchange tube 2B are connected via the external flow path 4 to the first thin portion 21A of the first heat exchange tube 2A and The second thin portions 21B face each other.
- the first flow path forming part 61, the second flow path forming part 62 and the third flow path forming part 63 of the first heat exchange tube 2A, the first flow path forming part 61 of the second heat exchange tube 2B, the second flow The path forming part 62 and the third flow path forming part 63 are arranged in a staggered manner in the width direction of the heat exchange tube 2.
- the inlet 3C of the second heat exchange tube 2B communicates with the inlet 3A of the first heat exchange tube 2A
- the outlet 3D of the second heat exchange tube 2B is the outlet 3B of the first heat exchange tube 2A
- the first heat exchange tube 2A and the second heat exchange tube 2B are joined so as to communicate with each other.
- the inlet 3C of the second heat exchange tube 2B communicates with the outlet 3B of the first heat exchange tube 2A
- the outlet 3D of the second heat exchange tube 2B communicates with the inlet 3A of the first heat exchange tube 2A.
- the second heat exchange tube 2B is virtually rotated 180 degrees in a plane perpendicular to the thickness direction of the heat exchange tube 2.
- the position of the 1st flow path formation part 61 of the 1st heat exchange tube 2A and the 2nd flow path formation part 62 is the 1st flow path formation part of the 2nd heat exchange tube 2B in the width direction of the heat exchange tube 2.
- the positions of the second flow path forming portion 62 and the third flow path forming portion 63 coincide with each other.
- the positions of the first thin portion 21A and the second thin portion 21B of the first heat exchange tube 2A coincide with the positions of the first thin portion 21A and the second thin portion 21B of the second heat exchange tube 2B.
- the gap between the first heat exchange tube 2 ⁇ / b> A and the second heat exchange tube 2 ⁇ / b> B passes through the external flow path 4 through which the second fluid flows. It is composed.
- the external flow path 4 gently meanders from the inlet (upstream side) to the outlet (downstream side). Since the external flow path 4 meanders, the development of the boundary layer on the surface of the heat exchange tube 2 is suppressed.
- the surfaces of the first flow path forming part 61, the second flow path forming part 62, and the third flow path forming part 63 are directed in a direction inclined with respect to both the thickness direction and the width direction of the heat exchange tube 2. Extending from the first thin part 21A and the second thin part 21B. According to such a configuration, the separation of the second fluid on the surfaces of the flow path forming portions 61, 62, and 63 can be suppressed, so that the heat exchange efficiency of the heat exchanger 1 is further improved. In other words, the thicknesses of the first flow path forming part 61, the second flow path forming part 62, and the third flow path forming part 63 continuously increase and decrease along the flow direction of the second fluid.
- the surfaces of the flow path forming portions 61, 62, and 63 and the surfaces of the first thin portion 21A and the second thin portion 21B are connected by a curve.
- the surfaces of the flow path forming portions 61 and 63 and the surface of the outer edge portion 43 are connected by a curve.
- the contours of the flow path forming portions 61, 62, and 63 are configured by a combination of a straight line and a curve smoothly connected to the straight line. When the curve and the straight line are connected so as not to have a non-differentiable point, it can be determined that the straight line and the curve are smoothly connected.
- the flow path forming portions 61, 62, and 63 are respectively divided into one part and the other part of the heat exchange tube 2 divided by the joint surfaces of the first plate member 11 and the second plate member 12. Part. One part is a part close to the first plate 11 (upper part in FIG. 4A). The other part is a part close to the second plate 12 (the lower part in FIG. 4A).
- the portions of the flow path forming portions 61, 62, and 63 that are close to the first plate material 11 and the portions of the flow path forming portions 61, 62, and 63 that are close to the second plate material 12 are symmetric with respect to the joint surface. According to such a configuration, the expansion and reduction of the width of the external flow path 4 can be further suppressed. Therefore, the pressure loss of the second fluid flowing through the external flow path 4 can be further reduced.
- the dimension of the external flow path 4 in the direction in which the heat exchange tubes 2 are arranged is substantially constant from the upstream end to the downstream end of the external flow path 4.
- the shapes of the flow path forming portions 61, 62, and 63 are adjusted so that the distance (shortest distance) between the first heat exchange tube 2A and the second heat exchange tube 2B is constant. According to such a configuration, the pressure loss of the second fluid flowing through the external flow path 4 can be further reduced.
- the heat exchange tube 2 may further include a first plate-like portion 44 and a second plate-like portion 54.
- the first plate-like portion 44 is a portion protruding from the outer edge portion 43 toward the direction parallel to the width direction on one end side in the width direction of the first heat exchange tube 2A.
- the 2nd plate-shaped part 54 is a part which protrudes from the outer edge part 43 toward the direction parallel to the width direction in the other end side of the width direction of the 2nd heat exchange tube 2B. According to such a configuration, the first plate-like portion 44 and the second plate-like portion 54 function as heat transfer fins, so that the heat exchange capability of the heat exchanger 1 is improved.
- the second plate-like portion 54 protrudes in the direction in which the second fluid flows. Since the second plate-like portion 54 can suppress the separation of the second fluid at the other end of the second heat exchange tube 2B, the heat exchange efficiency of the heat exchanger 1 is improved. Further, these plate-like portions 44 and 54 make it possible to effectively utilize the occupied volume of the heat exchanger 1.
- the first plate-like portion 44 and the second plate-like portion 54 may protrude from the outer edge portion 43 on both sides in the width direction.
- the width of the first plate-like portion 44 is twice the width of the outer edge portion 43.
- the width of the second plate-like portion 54 is twice the width of the outer edge portion 43.
- the first plate-like portion 44 of the first heat exchange tube 2A is located in a range not exceeding the outer edge portion 43 of the second heat exchange tube 2B.
- the second plate-like portion 54 of the second heat exchange tube 2B is located in a range not exceeding the outer edge portion 43 of the first heat exchange tube 2A.
- the first protrusion 41 of the first heat exchange tube 2A is joined to a portion around the inlet 3C of the second heat exchange tube 2B by brazing.
- the first protrusion 41 of the first heat exchange tube 2A is joined to the third protrusion 51 of the second heat exchange tube 2B by brazing.
- the second protrusion 42 of the first heat exchange tube 2A is joined to a portion around the outlet 3D of the second heat exchange tube 2B by brazing.
- the second protrusion 42 of the first heat exchange tube 2A is joined to the fourth protrusion 52 of the second heat exchange tube 2B by brazing. That is, the protruding portions of the adjacent heat exchange tubes 2 are joined to each other.
- the first heat exchange tube 2A is combined with the second heat exchange tube 2B via the first protrusion 41 and the second protrusion 42.
- the inlet 3A of the first plate 11 of the first heat exchange tube 2A communicates with the inlet 3C of the second plate 12 of the second heat exchange tube 2B.
- the outlet 3B of the first plate 11 of the first heat exchange tube 2A communicates with the outlet 3D of the second plate 12 of the second heat exchange tube 2B.
- the second plate 12 has an inlet 3C and an outlet 3D. Not formed.
- the heat exchange tube 2 is composed of the first plate member 11 and the second plate member 12 that are bonded together so that the internal flow path 3 is formed.
- the replacement tube 1 can be thinned.
- the heat exchanger 1 can be reduced in size.
- the flow path forming parts 61, 62 and 63 of the first heat exchange tube 2A and the flow path forming parts 61, 62 and 63 of the second heat exchange tube 2B are arranged in a staggered manner in the width direction. According to such a configuration, the width of the external flow path 4 between the first heat exchange tube 2A and the second heat exchange tube 2B is larger than when the flow path forming portions are not arranged in a staggered manner. Expansion and reduction can be suppressed, and the pressure loss of the second fluid flowing through the external flow path 4 can be reduced.
- FIGS. 7A to 10 a heat exchanger according to a second embodiment of the present invention will be described with reference to FIGS. 7A to 10.
- the same components as those in the above embodiment are denoted by the same reference numerals plus 100, and a part of the description is omitted. That is, the description regarding the heat exchanger of the first embodiment can be applied to the following embodiment as long as there is no technical contradiction.
- the heat exchange tube 102 includes a first plate-like portion 144 and a second plate-like portion 154.
- the first plate-like portion 144 is in a direction parallel to the width direction at one end side in the width direction of the first heat exchange tube 102A (left side in FIG. 7A, left side in FIG. 8A, left side in FIG. 8B, and left side in FIG. 9). This is a portion that protrudes to the left from the outer edge portion 143.
- the second plate-like portion 154 is a direction parallel to the width direction on the other end side in the width direction of the second heat exchange tube 102B (the right side in FIG. 7B, the right side in FIG. 8C, the right side in FIG. 8D, and the right side in FIG. 9). It is the part which protrudes from the outer edge part 143 to the right side toward.
- the width of the first plate-like portion 144 is three times the width of the outer edge portion 143.
- the width of the second plate-shaped portion 154 is three times the width of the outer edge portion 143.
- one end of the first plate-like portion 144 of the first heat exchange tube 102A is located at the same position as one end of the outer edge portion 143 of the second heat exchange tube 102B.
- the other end of the second plate-like portion 154 of the second heat exchange tube 102B is located at the same position as the other end of the outer edge portion 143 of the first heat exchange tube 102A.
- the heat exchange capability of the heat exchanger is improved.
- the second plate-like portion 154 protrudes in the direction in which the second fluid flows. Since the second plate portion 154 can suppress the separation of the second fluid at the other end of the second heat exchange tube 102B, the heat exchange efficiency of the heat exchanger is improved. Furthermore, these plate-like parts 144 and 154 make it possible to effectively utilize the occupied volume of the heat exchanger. Note that the first plate-like portion 144 and the second plate-like portion 154 may protrude from the outer edge portion 143 on both sides in the width direction.
- the internal flow path 203 includes a first segment 231, a second segment 232, and a third segment 233 that extend in the column direction of the heat exchange tubes 202.
- Each of the segments 231, 232, and 233 forms a straight channel.
- the first fluid is diverted from the inlet 203A to each of the segments 231, 232, and 233.
- the first fluid that has flowed through the segments 231, 232, and 233 is collected at the outlet 203B.
- the internal flow path 203 may be a straight flow path in which the flow direction of the first fluid from the inlet 203A to the outlet 203B is straight. According to this configuration, since the structure of the heat exchange tube 202 is simplified, the manufacturing cost of the heat exchange tube 202 can be reduced.
- the inhibition structure that inhibits heat transfer is not limited to the through hole.
- the first thin wall portion 21A and the second thin wall portion 21B have heat relatively lower than the material (for example, metal) of the heat exchange tube 2 other than the first thin wall portion 21A and the second thin wall portion 21B. It may be made of a material having conductivity (for example, resin).
- the heat exchanger of the present invention is particularly useful for heat exchangers for vehicle air conditioners, computers, home appliances, and the like.
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Abstract
Description
第1流体が流れる内部流路と、前記内部流路の入口と、前記内部流路の出口とをそれぞれ有し、前記第1流体と熱交換するべき第2流体のための外部流路が形成されるように組み立てられた複数の熱交換チューブを備え、
前記内部流路は、前記熱交換チューブの特定の列方向に延びている複数のセグメントを有し、
前記熱交換チューブは、前記内部流路が形成されるように互いに貼り合わされた1組の板材で構成されており、(i)前記熱交換チューブの厚さ方向の両側に突出し、前記内部流路の前記セグメントをそれぞれ形成している複数の流路形成部と、(ii)前記列方向と直交する幅方向において互いに隣り合う前記流路形成部と前記流路形成部との間に位置し、前記列方向に沿って前記内部流路の前記セグメントと前記セグメントとを互いに隔てている薄肉部と、(iii)前記内部流路の前記入口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第1突出部と、(iv)前記内部流路の前記出口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第2突出部と、をさらに有し、
互いに隣り合う1組の前記熱交換チューブをそれぞれ第1熱交換チューブ及び第2熱交換チューブと定義したとき、
前記第1熱交換チューブの前記第1突出部が前記第2熱交換チューブの前記入口の周囲の部分に接合され、前記第1熱交換チューブの前記第2突出部が前記第2熱交換チューブの前記出口の周囲の部分に接合されており、
前記列方向に垂直な断面において、前記第1熱交換チューブの前記流路形成部が前記外部流路を介して前記第2熱交換チューブの前記薄肉部に向かい合い、かつ前記第2熱交換チューブの前記流路形成部が前記外部流路を介して前記第1熱交換チューブの前記薄肉部に向かい合っており、
前記第1熱交換チューブの前記複数の流路形成部と前記第2熱交換チューブの前記複数の流路形成部とが前記幅方向において千鳥状に配列している、熱交換器を提供する。
第1流体が流れる内部流路と、前記内部流路の入口と、前記内部流路の出口とをそれぞれ有し、前記第1流体と熱交換するべき第2流体のための外部流路が形成されるように組み立てられた複数の熱交換チューブを備え、
前記内部流路は、前記熱交換チューブの特定の列方向に延びている複数のセグメントを有し、
前記熱交換チューブは、前記内部流路が形成されるように互いに貼り合わされた1組の板材で構成されており、(i)前記熱交換チューブの厚さ方向の両側に突出し、前記内部流路の前記セグメントをそれぞれ形成している複数の流路形成部と、(ii)前記列方向と直交する幅方向において互いに隣り合う前記流路形成部と前記流路形成部との間に位置し、前記列方向に沿って前記内部流路の前記セグメントと前記セグメントとを互いに隔てている薄肉部と、(iii)前記内部流路の前記入口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第1突出部と、(iv)前記内部流路の前記出口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第2突出部と、をさらに有し、
互いに隣り合う1組の前記熱交換チューブをそれぞれ第1熱交換チューブ及び第2熱交換チューブと定義したとき、
前記第1熱交換チューブの前記第1突出部が前記第2熱交換チューブの前記入口の周囲の部分に接合され、前記第1熱交換チューブの前記第2突出部が前記第2熱交換チューブの前記出口の周囲の部分に接合されており、
前記列方向に垂直な断面において、前記第1熱交換チューブの前記流路形成部が前記外部流路を介して前記第2熱交換チューブの前記薄肉部に向かい合い、かつ前記第2熱交換チューブの前記流路形成部が前記外部流路を介して前記第1熱交換チューブの前記薄肉部に向かい合っており、
前記第1熱交換チューブの前記複数の流路形成部と前記第2熱交換チューブの前記複数の流路形成部とが前記幅方向において千鳥状に配列している、熱交換器を提供する。
図1に示すように、本発明の第1実施形態に係る熱交換器1は、複数の熱交換チューブ2、入口ヘッダ10A及び出口ヘッダ10Bを備えている。複数の熱交換チューブ2は、それぞれ平面視で矩形の形状を有し、所定の間隔をあけて並べられている。複数の熱交換チューブ2の内部に第1流体(例えば、冷媒)が流れる。複数の熱交換チューブ2は、第1流体と熱交換するべき第2流体(例えば、外気)の流路が外部に形成されるように組み立てられている。詳細には、第2流体の流路は、隣り合う熱交換チューブ2の間に形成されている。入口ヘッダ10A及び出口ヘッダ10Bは、それぞれ、熱交換チューブ2の並び方向における熱交換器1の一方側の端面(図1の左側端面)を形成している熱交換チューブ2に装着されている。このような構成によれば、入口ヘッダ10A及び出口ヘッダ10Bを含む別体の中空管を設ける場合に比して、熱交換器1を小型化できる。
次に、図7A~図10を参照して、本発明の第2実施形態に係る熱交換器を説明する。なお、本実施形態では、上記実施形態と同一構成部分には同一符号に100を加えた符号を付し、その説明を一部省略する。すなわち、第1実施形態の熱交換器に関する説明は、技術的に矛盾しない限り、以下の本実施形態にも適用されうる。
図11に示すように、内部流路203は、熱交換チューブ202の列方向に延びている第1セグメント231、第2セグメント232及び第3セグメント233を備えている。セグメント231,232及び233は、それぞれ、直線的な流路を形成している。第1流体は、入口203Aからセグメント231,232及び233のそれぞれに分流される。セグメント231,232及び233を流れた第1流体は、出口203Bに集められる。このように、内部流路203は、入口203Aから出口203Bへの第1流体の流れ方向がまっすぐとなる直線流路であってもよい。この構成によれば、熱交換チューブ202の構造が簡素になるので、熱交換チューブ202の製造コストを削減することができる。
Claims (17)
- 第1流体が流れる内部流路と、前記内部流路の入口と、前記内部流路の出口とをそれぞれ有し、前記第1流体と熱交換するべき第2流体のための外部流路が形成されるように組み立てられた複数の熱交換チューブを備え、
前記内部流路は、前記熱交換チューブの特定の列方向に延びている複数のセグメントを有し、
前記熱交換チューブは、前記内部流路が形成されるように互いに貼り合わされた1組の板材で構成されており、(i)前記熱交換チューブの厚さ方向の両側に突出し、前記内部流路の前記セグメントをそれぞれ形成している複数の流路形成部と、(ii)前記列方向と直交する幅方向において互いに隣り合う前記流路形成部と前記流路形成部との間に位置し、前記列方向に沿って前記内部流路の前記セグメントと前記セグメントとを互いに隔てている薄肉部と、(iii)前記内部流路の前記入口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第1突出部と、(iv)前記内部流路の前記出口の周囲に形成され、前記熱交換チューブの前記厚さ方向に突出している第2突出部と、をさらに有し、
互いに隣り合う1組の前記熱交換チューブをそれぞれ第1熱交換チューブ及び第2熱交換チューブと定義したとき、
前記第1熱交換チューブの前記第1突出部が前記第2熱交換チューブの前記入口の周囲の部分に接合され、前記第1熱交換チューブの前記第2突出部が前記第2熱交換チューブの前記出口の周囲の部分に接合されており、
前記列方向に垂直な断面において、前記第1熱交換チューブの前記流路形成部が前記外部流路を介して前記第2熱交換チューブの前記薄肉部に向かい合い、かつ前記第2熱交換チューブの前記流路形成部が前記外部流路を介して前記第1熱交換チューブの前記薄肉部に向かい合っており、
前記第1熱交換チューブの前記複数の流路形成部と前記第2熱交換チューブの前記複数の流路形成部とが前記幅方向において千鳥状に配列している、熱交換器。 - 前記熱交換チューブは、平面視で矩形の形状を有し、
前記熱交換チューブには、前記熱交換チューブの長手方向の一端部及び他端部のそれぞれに前記入口及び前記出口としての1対の開口部が前記熱交換チューブを前記厚さ方向に貫通する形で設けられている、請求項1に記載の熱交換器。 - 前記複数の熱交換チューブは、互いに同一の構造を有しており、
前記第2熱交換チューブの前記入口が前記第1熱交換チューブの前記出口に連通し、かつ前記第2熱交換チューブの前記出口が前記第1熱交換チューブの前記入口に連通するように、前記熱交換チューブの前記厚さ方向に垂直な平面内で前記第2熱交換チューブを仮想的に180度回転させたとき、前記第1熱交換チューブの前記複数の流路形成部及び前記薄肉部の位置が、前記幅方向において、前記第2熱交換チューブの前記複数の流路形成部及び前記薄肉部の位置に一致する、請求項1に記載の熱交換器。 - 前記熱交換チューブは、前記幅方向の一端側及び他端側から選ばれる少なくとも一方において、前記幅方向に平行な方向に向かって突出している板状部をさらに有する、請求項1に記載の熱交換器。
- 前記列方向に垂直な前記断面において、前記流路形成部の表面が前記熱交換チューブの前記厚さ方向及び前記幅方向の両方向に対して傾斜した方向に向かって前記薄肉部から延びている、請求項1に記載の熱交換器。
- 前記列方向に垂直な前記断面において、前記流路形成部の表面と前記薄肉部の表面とが曲線でつながっている、請求項1に記載の熱交換器。
- 前記列方向に垂直な前記断面において、(i)前記流路形成部の輪郭が曲線で構成されている、又は(ii)前記流路形成部の輪郭が直線と、その直線に滑らかにつながった曲線との組み合わせで構成されている、請求項1に記載の熱交換器。
- 前記列方向に垂直な前記断面において、前記流路形成部は、前記熱交換チューブにおける前記1組の板材の接合面によって分けられた一方の部分と他方の部分とを含み、
前記一方の部分と前記他方の部分とが前記接合面に関して対称である、請求項1に記載の熱交換器。 - 前記内部流路は、前記入口から前記出口への途中で前記第1流体の流れ方向が反転している蛇行流路であり、
前記複数のセグメントは、第1セグメントと、前記第1セグメントにおける前記第1流体の流れ方向と反対の方向に前記第1流体が流れる第2セグメントとを含み、
前記内部流路は、前記第1セグメントと前記第2セグメントとを連絡している曲がりセグメントをさらに含む、請求項1に記載の熱交換器。 - 前記熱交換チューブは、前記薄肉部に設けられ、前記第1セグメントを流れる前記第1流体と、前記第2セグメントを流れる前記第1流体との間の熱移動を阻害する阻害構造をさらに有する、請求項9に記載の熱交換器。
- 前記熱交換器の端面を形成している前記熱交換チューブの前記第1突出部に接合され、前記内部流路の前記入口に前記第1流体を供給するための入口ヘッダと、
前記熱交換器の前記端面を形成している前記熱交換チューブの前記第2突出部に接合され、前記内部流路の前記出口から前記第1流体を排出するための出口ヘッダと、
をさらに備える、請求項1に記載の熱交換器。 - 前記内部流路は、前記第1セグメントよりも上流側かつ前記入口の周囲に形成された、前記第1流体が流れる最上流セグメントをさらに含み、
前記熱交換チューブは、(i)前記曲がりセグメントと前記最上流セグメントとを仕切っている最上流薄肉部と、(ii)前記最上流薄肉部に設けられ、前記曲がりセグメントを流れる前記第1流体と、前記最上流セグメントを流れる前記第1流体との間の熱移動を阻害する上流側阻害構造と、をさらに有する、請求項9に記載の熱交換器。 - 前記上流側阻害構造は、前記最上流薄肉部における前記入口に最も近い部分に形成されている、請求項12に記載の熱交換器。
- 前記上流側阻害構造は、前記1組の板材の厚さ方向に前記最上流薄肉部を貫通している貫通孔である、請求項12に記載の熱交換器。
- 前記内部流路は、前記第2セグメントよりも下流側かつ前記出口の周囲に形成された、前記第1流体が流れる最下流セグメントをさらに含み、
前記熱交換チューブは、(i)前記曲がりセグメントと前記最下流セグメントとを仕切っている最下流薄肉部と、(ii)前記最下流薄肉部に設けられ、前記曲がりセグメントを流れる前記第1流体と、前記最下流セグメントを流れる前記第1流体との間の熱移動を阻害する下流側阻害構造と、をさらに有する、請求項9に記載の熱交換器。 - 前記下流側阻害構造は、前記最下流薄肉部における前記出口に最も近い部分に形成されている、請求項15に記載の熱交換器。
- 前記下流側阻害構造は、前記1組の板材の厚さ方向に前記最下流薄肉部を貫通している貫通孔である、請求項15に記載の熱交換器。
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JP2018155481A (ja) * | 2017-03-16 | 2018-10-04 | ダイキン工業株式会社 | 伝熱管ユニットを有する熱交換器 |
WO2018168772A1 (ja) * | 2017-03-16 | 2018-09-20 | ダイキン工業株式会社 | 伝熱管ユニットを有する熱交換器 |
JP7001917B2 (ja) | 2017-03-16 | 2022-01-20 | ダイキン工業株式会社 | 伝熱管ユニットを有する熱交換器 |
WO2019167840A1 (ja) * | 2018-03-01 | 2019-09-06 | ダイキン工業株式会社 | 熱交換器 |
JP2019152361A (ja) * | 2018-03-01 | 2019-09-12 | ダイキン工業株式会社 | 熱交換器 |
JP7044969B2 (ja) | 2018-03-01 | 2022-03-31 | ダイキン工業株式会社 | 熱交換器 |
US11874034B2 (en) | 2018-03-01 | 2024-01-16 | Daikin Industries, Ltd. | Heat exchanger |
DE102022112511A1 (de) | 2022-05-18 | 2023-11-23 | Man Truck & Bus Se | Temperiervorrichtung mit mechanisch entkoppeltem Kühlbereich |
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JPWO2014171095A1 (ja) | 2017-02-16 |
EP2975352A1 (en) | 2016-01-20 |
EP2975352A4 (en) | 2016-08-17 |
CN105102917A (zh) | 2015-11-25 |
US9766015B2 (en) | 2017-09-19 |
EP2975352B1 (en) | 2019-02-27 |
US20160054068A1 (en) | 2016-02-25 |
JP5892453B2 (ja) | 2016-03-23 |
CN105102917B (zh) | 2019-05-03 |
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