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WO2001004560A1 - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
WO2001004560A1
WO2001004560A1 PCT/JP2000/001809 JP0001809W WO0104560A1 WO 2001004560 A1 WO2001004560 A1 WO 2001004560A1 JP 0001809 W JP0001809 W JP 0001809W WO 0104560 A1 WO0104560 A1 WO 0104560A1
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WO
WIPO (PCT)
Prior art keywords
heat exchanger
tank
refrigerant
group
pair
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2000/001809
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French (fr)
Japanese (ja)
Inventor
Kunihiko Nishishita
Mutsumi Hukushima
Muneo Sakurada
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Bosch Corp
Original Assignee
Bosch Automotive Systems Corp
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Filing date
Publication date
Application filed by Bosch Automotive Systems Corp filed Critical Bosch Automotive Systems Corp
Publication of WO2001004560A1 publication Critical patent/WO2001004560A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03Heat-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
    • F28D1/0308Heat-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
    • F28D1/0325Heat-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
    • F28D1/0333Heat-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
    • F28D1/0341Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels

Definitions

  • the present invention relates to a heat exchanger used for a vehicle air conditioner.
  • Japanese Utility Model Laid-Open No. 7-127778 discloses a pair of upper and lower headers formed at one end in the longitudinal direction, and a pair of lower front and rear headers formed at the other end in the longitudinal direction. Stacked heat exchanger formed by laminating, via fins, an intermediate plate having the upper front and rear header portions and a flat tube portion communicating each of the lower front and rear header portions. A vessel is disclosed. In this stacked heat exchanger, the pair of upper and lower ink tanks formed by stacking the upper and lower headers is cut off at a substantially central portion and each is divided into two tank blocks. Further, the lower front and rear header portions are laminated to form a pair of lower ink groups.
  • the refrigerant flowing into the first upper front evening block flows down the flat tube section, flows into the lower front evening group, and flows into the lower front tank group.
  • the amount of refrigerant rising in the flat tube part located near the partition is smaller than in other parts.
  • the nearby refrigerant temperature rises.
  • the refrigerant descends from the second upper rear tank block to the lower rear tank group, moves through the lower rear tank group, and rises to the first upper rear tank block.
  • the amount of refrigerant rising in the flat tube portion located near the partition is smaller than in other portions, so that the temperature in the vicinity increases.
  • an object of the present invention is to provide a heat exchanger which does not have a high passage resistance even in a thinned heat exchanger, has a good temperature distribution of the heat exchanger, and has a high heat exchanger capacity. Disclosure of the invention
  • a refrigerant inlet provided at an end plate disposed at one end in the direction, and a refrigerant inflow passage formed in the one end plate;
  • a communication passage communicating with the ink tank located near the end and a tank portion located at one end of the second tank group through a refrigerant outflow passage formed in the one end plate.
  • a refrigerant outlet portion is provided.
  • the communication passage may include a communication pipe having one end connected to the refrigerant inflow passage, and a sunset located at the other end of the communication pipe and the other end of the first sunset group. It is desirable to be constituted by a turn-back path communicating with the section. By this, it passes through the communication pipe As a result, the refrigerant flows into the first tank group after passing through the return passage, so that the momentum of the refrigerant flowing into the first tank group is impeded, so that the refrigerant flows into the refrigerant passage from the first tank group. There is no difference in the amount of refrigerant between the near side and the back side of the first evening group in the refrigerant inflow direction, and a uniform temperature distribution can be obtained.
  • the present invention provides a plurality of tank portions formed at one end in the longitudinal direction, and a plurality of refrigerant passages extending to near the other end in the longitudinal direction and being folded, and having a refrigerant flow path fluidly communicating the pair of tank portions.
  • a heat exchanger including at least a tube element, fins alternately stacked with the plurality of tube elements, and a pair of end plates provided at both ends in the stacking direction, the one of the heat exchangers A first evening group formed by connecting the ink portions in the stacking direction, a second evening group formed by connecting the other evening portions in the stacking direction, and the first tank group.
  • a first path and a second path in which the refrigerant descends through the refrigerant flow path toward the second tank group are formed.
  • the communication pipe or the distribution pipe may penetrate the inside of the first sunset group. As a result, it is possible to cope with a case where a space for mounting cannot be secured even between the pair of sunset portions and a space for mounting outside the heat exchanger cannot be secured due to space saving.
  • the width of the heat exchanger in the ventilation direction is approximately 30 mm or more and 57 mm or less.
  • FIG. 7 is a left side view of the stacked heat exchanger according to the second embodiment
  • (b) of FIG. 7 is a right side view thereof
  • FIG. 8 is a second embodiment of the present invention.
  • FIG. 9 is a schematic diagram illustrating the flow of the refrigerant
  • FIG. 9 is a front view of a laminated heat exchanger according to a third embodiment of the present invention
  • FIG. Fig. 11 is a bottom view of the stacked heat exchanger according to the embodiment of the present invention
  • Fig. 11 (a) is a left side view of the stacked heat exchanger according to the third embodiment of the present invention.
  • (B) of FIG. 11 is a right side view thereof
  • FIG. 17 is a schematic diagram illustrating a laminated heat exchanger according to a fifth embodiment of the present invention.
  • FIG. 18 is a bottom view of a laminated heat exchanger according to a fifth embodiment of the present invention
  • FIG. 19 (a) is a view of the present invention.
  • number 5 FIG. 19 is a left side view of the laminated heat exchanger according to the embodiment of FIG. 19, (b) of FIG. 19 is a right side view thereof
  • FIG. 20 is a fifth embodiment of the present invention.
  • FIG. 21 is a schematic diagram illustrating the flow of the refrigerant in the stacked heat exchanger, and FIG. 21 is a front view of the stacked heat exchanger according to the sixth embodiment of the present invention; FIG. FIG.
  • FIG. 23 is a bottom view of the stacked heat exchanger according to the sixth embodiment of the present invention.
  • FIG. 23 (a) is a sectional view of the stacked heat exchanger according to the sixth embodiment of the present invention.
  • FIG. 23 (b) is a right side view of the left side view
  • FIG. 24 is a view showing the flow of the refrigerant in the laminated heat exchanger according to the sixth embodiment of the present invention.
  • FIG. 25 is a schematic view for explaining, FIG. 25 is a front view of a laminated heat exchanger according to a seventh embodiment of the present invention, and
  • FIG. 26 is a seventh embodiment of the present invention.
  • the pair of tank portions 2 and 3 has a communication hole (not shown) opened in the laminating direction, and one of the tank portions 2 communicated in the laminating direction by the communicating hole.
  • a first tank group A is formed
  • a second tank group B is formed by the other tank portion 3 communicating in the stacking direction.
  • the other end of the refrigerant inflow passage 9 communicates with one end of a communication pipe 15 arranged between the pair of tanks 2 and 3 of the tube element 5, and the other end of the communication pipe 15 It communicates with a return path 16 integrally formed below the other end plate 8.
  • the turn-back passage 16 communicates with the first tank group A through an opening 18 formed in the end plate 8 held on the other side in the stacking direction.
  • the other end side of the refrigerant outflow passage 10 is connected to the second tank group B through an opening 17 formed below an end plate ⁇ disposed at one end in the stacking direction.
  • the refrigerant that has passed through the refrigerant inflow passage 9 from the inlet pipe portion 13 provided on one side in the stacking direction passes through the return pipe provided on the other side in the stacking direction via the communication pipe 15. It reaches 16 and flows into the first evening group A from the other side in the stacking direction. Since the direction of the refrigerant flow is changed by 180 ° by passing through the return passage 16, the momentum of the refrigerant flowing into the first tank group A is obstructed, and the first tank group A is moved from the first tank group to the first tank group.
  • the amount of the refrigerant flowing into each of the refrigerant flow paths 4 communicating with the group A is substantially equal on the near side in the inflow direction and the back side in the inflow direction of the first ink group A.
  • FIGS. 25 to 28 show a laminated heat exchanger 70 according to a seventh embodiment of the present invention.
  • the distribution pipes 15a and 15b are the same as those in the case of the communication pipe 15 of the laminated heat exchanger 30 according to the third embodiment described above.
  • the heat exchanger is provided on the downstream side of the laminated heat exchanger 70 in the ventilation direction.
  • the tank portions located at both ends in the stacking direction are the enlarged tank portions 71, 72 extending in the ventilation direction of the heat exchanger, and the distribution pipes 15a, 15b are:
  • the inlet pipe section 13 and these enlarged tank sections 71 and 72 are connected to it.

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

Abstract

A stacked heat exchanger having a refrigerant inlet and a refrigerant outlet on its one end side in stacking direction in order to obtain a heat exchanger which is excellent in heat exchanger temperature distribution and high in heat exchanger capability even in a thinned heat exchanger, wherein a communication path is provided to connect one end of a refrigerant flow-in path communicating with the refrigerant inlet to a tank part located at the other end of a first tank group in stacking direction and one end of a refrigerant flow-out path communicating with the refrigerant outlet is communicated directly with the tank part located on one end side of a second tank group in stacking direction, the refrigerant inlet is provided generally at the center of the first tank group, a communication path is provided to connect the refrigerant inlet to the tank part located at both ends of the first tank group in stacking direction, and the refrigerant outlet is provided at the tank part positioned generally at the center of the second tank group in stacking direction so that the refrigerant outlet is positioned in parallel with the refrigerant inlet and the refrigerant inlet and outlet can be communicated directly with each other.

Description

明 細 熱交換器 技術分野  Akira Fine heat exchanger technical field

この発明は、 車両用空調装置に用いられる熱交換器に関する。 背景技術  The present invention relates to a heat exchanger used for a vehicle air conditioner. Background art

実開平 7— 1 2 7 7 8号公報は、長手方向の一端に形成された一対 の上前後側へッダ部と、長手方向の他端に形成された一対の下前後側 へッダ部と、前記上前後側へッダ部と前記下前後側へッダ部の各々を 連通する扁平管部とを有する中間プレー トをフィ ンを介して積層し て形成された積層型型熱交換器を開示する。この積層型熱交換器にお いて、前記上前後側へッダ部を積層して構成される一対の上夕ンク群 は、略中央部分で遮断されてそれそれ 2つのタンクプロ ックに分割さ れ、さらに前記下前後側へッダ部を積層して一対の下夕ンク群を構成 する。  Japanese Utility Model Laid-Open No. 7-127778 discloses a pair of upper and lower headers formed at one end in the longitudinal direction, and a pair of lower front and rear headers formed at the other end in the longitudinal direction. Stacked heat exchanger formed by laminating, via fins, an intermediate plate having the upper front and rear header portions and a flat tube portion communicating each of the lower front and rear header portions. A vessel is disclosed. In this stacked heat exchanger, the pair of upper and lower ink tanks formed by stacking the upper and lower headers is cut off at a substantially central portion and each is divided into two tank blocks. Further, the lower front and rear header portions are laminated to form a pair of lower ink groups.

そして、 前記上タンク群の分割されたタンクブロ ックを、 第 1の上 前側タンクブロ ック、 第 2の上前側タンクブロ ック、 第 1の上後側夕 ンクブロック、 第 2の上後側夕ンクブロ ックとして説明すると、 上記 積層型熱交換器において、 冷媒は、 流体導入口から第 1の上前側夕ン クブロックに入り、 扁平管部を降下して下前側タンク群に入り、 この 下前側タンク群から扁平管部を上昇して第 2の上前側タンクブロ ッ クに入る。 そして、 冷媒は、 連通部 2 1 を迂回して第 2の上後側夕ン クブロックに入り、この第 2の上後側タンクブロックから扁平管部を 降下して下後側タンク群に入り、この下後側タンク群を移動し扁平管 の上昇して第 1の上後ろ側タンクブロ ックに流入して流体排出口か ら流出するものである。 Then, the divided tank blocks of the upper tank group are divided into a first upper front tank block, a second upper front tank block, a first upper rear tank block, and a second upper rear tank block. In the stacked heat exchanger described above, the refrigerant enters the first upper front tank block from the fluid inlet, descends the flat tube section, enters the lower front tank group, and enters the lower front tank group. The flat tube section rises from the front tank group and enters the second upper front tank block. Then, the refrigerant bypasses the communication portion 21 and enters the second upper and lower tank block, descends from the second upper and lower tank block through the flat tube portion, and enters the lower and rear tank group. Then, the lower rear tank group moves, the flat tube rises, flows into the first upper rear tank block, Outflows.

しかしながら、 上記引例の構成の熱交換器においては、 第 1の上前 側夕ンクブロ ックに流入した冷媒は、扁平管部を降下して下前側夕ン ク群に流入し、下前側タンク群を移動して扁平管部を上昇して第 2の 上前側夕ンクブロ ックに至るが、前記仕切近傍の位置する扁平管部を 上昇する冷媒量が他の部分に比べて少なくなるので、この付近の冷媒 温度が上昇する。 同様に、 第 2の上後側タンクプロ ックから下後側タ ンク群に降下し、前記下後側夕ンク群を移動して第 1の上後側夕ンク ブロ ックに上昇する冷媒においても、仕切近傍に位置する扁平管部を 上昇する冷媒量が他の部分比べて少なくなるので、 この付近の温度が 上昇する。  However, in the heat exchanger having the configuration of the above-mentioned reference, the refrigerant flowing into the first upper front evening block flows down the flat tube section, flows into the lower front evening group, and flows into the lower front tank group. To move up the flat tube part to reach the second upper front side ink block, but the amount of refrigerant rising in the flat tube part located near the partition is smaller than in other parts. The nearby refrigerant temperature rises. Similarly, the refrigerant descends from the second upper rear tank block to the lower rear tank group, moves through the lower rear tank group, and rises to the first upper rear tank block. Also in this case, the amount of refrigerant rising in the flat tube portion located near the partition is smaller than in other portions, so that the temperature in the vicinity increases.

以上のように、仕切の近傍において冷媒量が減少して温度が上昇す るので、通風量が最も安定する熱交換器の中央部近傍の温度分布が極 端に悪くなるという不具合が生じる。 特に、 車両内部の省スペース化 に伴う空調装置の小型化が要求されることから、熱交換器自体の小型 化が要望される現今において、 熱交換器自体の薄幅化を図った場合、 中央部近傍の温度分布の悪化は極端な熱交換能力の低下を意味する ことから大きな問題となる。 また、 薄幅化した際に、 通路抵抗が高く なる。  As described above, since the amount of the refrigerant decreases near the partition and the temperature rises, there is a problem that the temperature distribution near the center of the heat exchanger, where the ventilation amount is most stable, extremely deteriorates. In particular, since the size of the air conditioner is required to be reduced due to the space saving inside the vehicle, the demand for downsizing of the heat exchanger itself is increasing. Deterioration of the temperature distribution in the vicinity of the part is a serious problem because it means an extreme decrease in heat exchange capacity. In addition, when the width is reduced, the passage resistance increases.

よって、 この発明は、 薄型化した熱交換器においても、 通路抵抗が 高くならず、 しかも熱交換器の温度分布が良好で熱交換器能力の高い 熱交換器を提供することにある。 発明の開示  Therefore, an object of the present invention is to provide a heat exchanger which does not have a high passage resistance even in a thinned heat exchanger, has a good temperature distribution of the heat exchanger, and has a high heat exchanger capacity. Disclosure of the invention

したがって、 この発明は、 長手方向一端に形成された一対のタンク 部及び前記長手方向他端近傍まで延出して折り返すと共に前記一対 の夕ンク部を流体的に連通する冷媒流路を有する複数のチューブェ レメ ン ト と、該複数のチューブエレメ ン ト と交互に積層されるフィ ン と、前記積層方向両端に設けられる一対のェン ドプレー ト とを少なく とも具備する熱交換器において、前記一方の夕ンク部を積層方向に連 通して形成される第 1の夕ンク群と、前記他方の夕ンク部を積層方向 に連通して形成される第 2の夕ンク群と、前記熱交換器の積層方向一 端に配されたエン ドプレー トに設けられる冷媒入口部と、前記一方の ェン ドブレー トに形成された冷媒流入通路を介して、前記冷媒入口部 と前記第 1の夕ンク群の他端近傍に位置する夕ンク部とを連通する 連通路と、前記一方のェン ドプレートに形成された冷媒流出通路を介 して、前記第 2のタンク群の一端に位置するタンク部と連通する冷媒 出口部とを具備することにある。 Accordingly, the present invention provides a plurality of tube portions having a pair of tank portions formed at one longitudinal end and extending near the other end in the longitudinal direction to be folded and having a refrigerant flow path fluidly communicating the pair of ink portions. A heat exchanger comprising at least a plurality of elements, a plurality of fins alternately stacked with the plurality of tube elements, and a pair of end plates provided at both ends in the stacking direction. A first evening group formed by connecting the ink portions in the laminating direction, a second evening group formed by communicating the other evening portions in the laminating direction, and a lamination of the heat exchanger. A refrigerant inlet provided at an end plate disposed at one end in the direction, and a refrigerant inflow passage formed in the one end plate; A communication passage communicating with the ink tank located near the end and a tank portion located at one end of the second tank group through a refrigerant outflow passage formed in the one end plate. And a refrigerant outlet portion.

したがって、 この発明によれば、 積層方向の一端側に冷媒入口部及 び冷媒出口部を有する積層型熱交換器において、冷媒入口部と連通す る冷媒流入通路の一端と第 1のタンク群の積層方向他端のタンク部 とを接続する連通路を設け、また冷媒出口部と連通する冷媒流出通路 の一端と第 2のタンク群の積層方向一端側のタンク部とを直接連通 したので、 冷媒入口部から冷媒流入通路を通過した冷媒を、 連通路を 介して積層方向他端側から第 1のタンク群に流入でき、 これによつて、 冷媒が第 1の夕ンク群から冷媒流路を上昇する第 1のパスと、冷媒が 前記冷媒流路を第 2のタンク群に向かって下降する第 2のパスとが 形成されるので、 従来の 4パスの場合に比べて、 熱交換器の中央部分 に流れる冷媒量を簡易な構造で確保でき、熱交換器の温度分布を良好 にできるものである。  Therefore, according to the present invention, in the laminated heat exchanger having the refrigerant inlet and the refrigerant outlet at one end in the stacking direction, one end of the refrigerant inflow passage communicating with the refrigerant inlet and the first tank group are provided. A communication path connecting the tank at the other end in the stacking direction was provided, and one end of the refrigerant outflow passage communicating with the refrigerant outlet was directly connected to the tank at one end in the stacking direction of the second tank group. The refrigerant that has passed through the refrigerant inflow passage from the inlet portion can flow into the first tank group from the other end in the stacking direction through the communication passage, whereby the refrigerant flows from the first evening group into the refrigerant flow path. A first path that rises and a second path in which the refrigerant descends through the refrigerant flow path toward the second tank group are formed. The amount of refrigerant flowing to the center can be secured with a simple structure, Those capable of the temperature distribution well.

また、 本発明において、 前記連通路は、 前記冷媒流入通路に接続さ れる一端を有する連通パイプと、該連通パイプの他端と前記第 1の夕 ンク群の他方側端部に位置する夕ンク部とを連通する折返通路とに よって構成されることが望ましい。 これによつて、 連通パイプを通過 して冷媒が折返通路を通過して第 1のタンク群に流入することから、 第 1のタンク群に流入する冷媒の勢いが阻害されるので、第 1のタン ク群から冷媒通路に流入する冷媒量が、第 1の夕ンク群の冷媒流入方 向の手前側と奥側とで差がなくなり、均一な温度分布を得ることがで きるものである。 Further, in the present invention, the communication passage may include a communication pipe having one end connected to the refrigerant inflow passage, and a sunset located at the other end of the communication pipe and the other end of the first sunset group. It is desirable to be constituted by a turn-back path communicating with the section. By this, it passes through the communication pipe As a result, the refrigerant flows into the first tank group after passing through the return passage, so that the momentum of the refrigerant flowing into the first tank group is impeded, so that the refrigerant flows into the refrigerant passage from the first tank group. There is no difference in the amount of refrigerant between the near side and the back side of the first evening group in the refrigerant inflow direction, and a uniform temperature distribution can be obtained.

さらに、 本発明は、 長手方向一端に形成された一対の夕ンク部及び 前記長手方向他端近傍まで延出して折り返すと共に前記一対のタン ク部を流体的に連通する冷媒流路を有する複数のチューブェレメ ン ト と、 該複数のチューブエレメ ン ト と交互に積層されるフィ ンと、 前 記積層方向両端に設けられる一対のエン ドプレー ト とを少なく とも 具備する熱交換器において、前記一方の夕ンク部を積層方向に連通し て形成される第 1の夕ンク群と、前記他方の夕ンク部を積層方向に連 通して形成される第 2の夕ンク群と、前記第 1のタンク群の略中央の 夕ンク部外側に設けられる冷媒入口部と、前記冷媒入口部と前記第 1 の夕ンク群の両端端近傍に位置する夕ンク部とを連通する連通路と、 前記第 2の夕ンク群の略中央で前記冷媒入口部に並設されると共に、 前記第 2のタンク群の略中央に位置する夕ンク部と直接連通される 冷媒出口部とを具備することにある。  Further, the present invention provides a plurality of tank portions formed at one end in the longitudinal direction, and a plurality of refrigerant passages extending to near the other end in the longitudinal direction and being folded, and having a refrigerant flow path fluidly communicating the pair of tank portions. In a heat exchanger including at least a tube element, fins alternately stacked with the plurality of tube elements, and a pair of end plates provided at both ends in the stacking direction, the one of the heat exchangers A first evening group formed by connecting the ink portions in the stacking direction, a second evening group formed by connecting the other evening portions in the stacking direction, and the first tank group. A refrigerant inlet portion provided substantially outside the evening portion, a communication passage communicating the coolant inlet portion with the evening portions located near both ends of the first evening group, and the second passage; The refrigerant inlet at approximately the center of the evening group And a refrigerant outlet directly communicated with an ink tank located substantially at the center of the second tank group.

したがって、 この発明によれば、 積層型熱交換器において、 冷媒入 口部を第 1のタンク群の略中央に設けると共に、該冷媒入口部と第 1 のタンク群の積層方向両端に位置する夕ンク部とを接続する連通路 を設け、さらに冷媒出口部を前記冷媒入口部と並設するように第 2の タンク群の積層方向略中央に位置するタンク部に設けてこれらを直 接連通するようにしたので、冷媒入口部から流入した冷媒を連通路を 介して積層方向両端から第 1の夕ンク群に流入するでき、冷媒が第 1 の夕ンク群から前記冷媒流路を上昇する第 1のパスと、冷媒が前記冷 媒流路を第 2のタンク群に向かって下降する第 2のパスが形成され るので、 従来の 4パスの場合に比べて、 熱交換器の中央部分での冷媒 の流れが良好となるので、熱交換器の温度分布を良好にできるもので ある。 Therefore, according to the present invention, in the laminated heat exchanger, the refrigerant inlet is provided substantially at the center of the first tank group, and the refrigerant inlet and the first tank group are located at both ends in the laminating direction of the first tank group. A communication passage for connecting to the ink tank is provided, and a refrigerant outlet is provided in the tank located substantially at the center in the stacking direction of the second tank group so as to be juxtaposed with the refrigerant inlet, and these are directly connected to each other. As a result, the refrigerant flowing from the refrigerant inlet can flow into the first group through both ends in the stacking direction through the communication path, and the refrigerant rises up the refrigerant flow path from the first group. A first path and a second path in which the refrigerant descends through the refrigerant flow path toward the second tank group are formed. As a result, the flow of the refrigerant in the central portion of the heat exchanger is better than in the conventional four-pass case, so that the temperature distribution of the heat exchanger can be improved.

また、 この発明において、 前記連通路は、 前記冷媒流入通路に接続 される一端を有する一対の分配パイプと、前記第 1のタンク群の両端 近傍に位置する夕ンク部の各々のから延出し、前記分配パイプの各々 の他端と連通する拡大夕ンク部とによって構成されることが望ま し い。 これによつて、 分配パイプを通過した冷媒が第 1のタンク群に流 入する際に、 その方向が帰られることから流入速度が制限され、 第 1 のタンク群から冷媒流路に流入する冷媒量を各部分において均一化 することができるので、 温度分布を均一化できるものである。  Further, in the present invention, the communication passage extends from each of a pair of distribution pipes having one end connected to the refrigerant inflow passage, and an ink tank located near both ends of the first tank group, It is preferable that the distributing pipe be constituted by an enlarged ink portion communicating with the other end of each of the distribution pipes. As a result, when the refrigerant that has passed through the distribution pipe flows into the first tank group, its direction is returned, so that the inflow speed is limited, and the refrigerant flowing from the first tank group into the refrigerant flow path Since the amount can be made uniform in each part, the temperature distribution can be made uniform.

さらに、 前記連通パイプ又は前記分配パイプは、 一対のタンク部の 間に配されることが望ましい。前記一対の夕ンク部間に形成された凹 部をそのまま装着溝部として利用することができるからである。  Further, it is preferable that the communication pipe or the distribution pipe is disposed between a pair of tank portions. This is because the concave portion formed between the pair of ink portions can be used as it is as the mounting groove portion.

また、 前記連通パイ プ又は前記分配パイプを、 一対の夕ンク部の外 側に配するようにしても良いものである。 これによつて、 前記一対の 夕ンク部間に連通パイ プ等を装着する空間を確保できない場合にも 対応することが可能となる。  Further, the communication pipe or the distribution pipe may be arranged outside a pair of the ink portions. Accordingly, it is possible to cope with a case where a space for mounting a communication pipe or the like cannot be secured between the pair of evening portions.

さらにまた、 前記連通パイ プ又は前記分配パイプを、 前記第 1の夕 ンク群の内部を貫通するようにしても良いものである。これによつて、 一対の夕ンク部間にも装着する空間が確保できず、さらに省スペース 化によって熱交換器外部にも装着する空間を確保できない場合にも 対応することが可能となる。  Furthermore, the communication pipe or the distribution pipe may penetrate the inside of the first sunset group. As a result, it is possible to cope with a case where a space for mounting cannot be secured even between the pair of sunset portions and a space for mounting outside the heat exchanger cannot be secured due to space saving.

さらに、 前記熱交換器の通風方向の幅は、 略 3 0 m m以上 5 7 m m 以下であることが望ま しい。 上記構成の熱交換器を、 この範囲内で形 成することによって、所定以上の熱交換器能力を維持することができ るものである。 図面の簡単な説明 Further, it is desirable that the width of the heat exchanger in the ventilation direction is approximately 30 mm or more and 57 mm or less. By forming the heat exchanger having the above configuration within this range, it is possible to maintain a heat exchanger capacity of a predetermined level or more. BRIEF DESCRIPTION OF THE FIGURES

第 1図は、本願発明の第 1の実施の形態に係る積層型熱交換器の正 面図であり、 第 2図は、 本願発明の第 1の実施の形態に係る積層型熱 交換器の底面図であり、 第 3図の ( a ) は本願発明の第 1の実施の形 態に係る積層型熱交換器の左側面図であり、 第 3図の ( b ) はその右 側面図であり、 第 4図は、 本願発明の第 1の実施の形態に係る積層型 熱交換器の冷媒の流れを説明した概略図であり、 第 5図は、 本願発明 の第 2の実施の形態に係る積層型熱交換器の正面図であり、第 6図は. 本願発明の第 2の実施の形態に係る積層型熱交換器の底面図であり、 第 7図の ( a ) は本願発明の第 2の実施の形態に係る積層型熱交換器 の左側面図であり、第 7図の( b )はその右側面図であり、第 8図は、 本願発明の第 2の実施の形態に係る積層型熱交換器の冷媒の流れを 説明した概略図であり、 第 9図は、 本願発明の第 3の実施の形態に係 る積層型熱交換器の正面図であり、 第 1 0図は、 本願発明の第 3の実 施の形態に係る積層型熱交換器の底面図であり、 第 1 1図の ( a ) は 本願発明の第 3の実施の形態に係る積層型熱交換器の左側面図であ り、 第 1 1図の ( b ) はその右側面図であり、 第 1 2図は、 本願発明 の第 3の実施の形態に係る積層型熱交換器の冷媒の流れを説明した 概略図であり、 第 1 3図は、 本願発明の第 4の実施の形態に係る積層 型熱交換器の正面図であり、 第 1 4図は、 本願発明の第 4の実施の形 態に係る積層型熱交換器の底面図であり、 第 1 5図の ( a ) は本願発 明の第 4の実施の形態に係る積層型熱交換器の左側面図であり、第 1 5図の ( b ) はその右側面図であり、 第 1 6図は、 本願発明の第 4の 実施の形態に係る積層型熱交換器の冷媒の流れを説明した概略図で あり、 第 1 7図は、 本願発明の第 5の実施の形態に係る積層型熱交換 器の正面図であり、 第 1 8図は、 本願発明の第 5の実施の形態に係る 積層型熱交換器の底面図であり、 第 1 9図の ( a ) は本願発明の第 5 の実施の形態に係る積層型熱交換器の左側面図であり、 第 1 9図の ( b ) はその右側面図であり、 第 2 0図は、 本願発明の第 5の実施の 形態に係る積層型熱交換器の冷媒の流れを説明した概略図であり、第 2 1図は、本願発明の第 6の実施の形態に係る積層型熱交換器の正面 図であり、 第 2 2図は、 本願発明の第 6の実施の形態に係る積層型熱 交換器の底面図であり、 第 2 3図の ( a ) は本願発明の第 6の実施の 形態に係る積層型熱交換器の左側面図であり、 第 2 3図の ( b ) はそ の右側面図であり、 第 2 4図は、 本願発明の第 6の実施の形態に係る 積層型熱交換器の冷媒の流れを説明した概略図であり、 第 2 5図は、 本願発明の第 7の実施の形態に係る積層型熱交換器の正面図であり、 第 2 6図は、本願発明の第 7の実施の形態に係る積層型熱交換器の底 面図であり、 第 2 7図の ( a ) は本願発明の第 7の実施の形態に係る 積層型熱交換器の左側面図であり、 第 2 7図の ( b ) はその右側面図 であり、 第 2 8図は、 本願発明の第 7の実施の形態に係る積層型熱交 換器の冷媒の流れを説明した概略図であり、 第 2 9図は、 本願発明の 第 8の実施の形態に係る積層型熱交換器の正面図であり、第 3 0図は、 本願発明の第 8の実施の形態に係る積層型熱交換器の底面図であり、 第 3 1図の ( a ) は本願発明の第 8の実施の形態に係る積層型熱交換 器の左側面図であり、 第 3 1図の ( b ) はその右側面図であり、 第 3 2図は、本願発明の第 8の実施の形態に係る積層型熱交換器の冷媒の 流れを説明した概略図であり、 第 3 3図は、 熱交換器の通風方向の幅 と熱交換器能力との関係を示した特性線図である。 発明を実施するための最良の形態 FIG. 1 is a front view of the laminated heat exchanger according to the first embodiment of the present invention, and FIG. 2 is a front view of the laminated heat exchanger according to the first embodiment of the present invention. FIG. 3 (a) is a left side view of the laminated heat exchanger according to the first embodiment of the present invention, and FIG. 3 (b) is a right side view thereof. Yes, FIG. 4 is a schematic diagram illustrating the flow of the refrigerant in the laminated heat exchanger according to the first embodiment of the present invention, and FIG. 5 is a schematic view of the second embodiment of the present invention. FIG. 6 is a front view of the stacked heat exchanger, and FIG. 6 is a bottom view of the stacked heat exchanger according to the second embodiment of the present invention. FIG. 7 is a left side view of the stacked heat exchanger according to the second embodiment, (b) of FIG. 7 is a right side view thereof, and FIG. 8 is a second embodiment of the present invention. Such a stacked heat exchanger FIG. 9 is a schematic diagram illustrating the flow of the refrigerant, FIG. 9 is a front view of a laminated heat exchanger according to a third embodiment of the present invention, and FIG. Fig. 11 is a bottom view of the stacked heat exchanger according to the embodiment of the present invention, and Fig. 11 (a) is a left side view of the stacked heat exchanger according to the third embodiment of the present invention. (B) of FIG. 11 is a right side view thereof, and FIG. 12 is a schematic diagram illustrating the flow of the refrigerant in the laminated heat exchanger according to the third embodiment of the present invention. FIG. 13 is a front view of a laminated heat exchanger according to a fourth embodiment of the present invention, and FIG. 14 is a laminated heat exchanger according to the fourth embodiment of the present invention. FIG. 15 (a) is a bottom view of the heat exchanger, and FIG. 15 (a) is a left side view of the laminated heat exchanger according to the fourth embodiment of the present invention, and FIG. 15 (b) is FIG. FIG. 6 is a schematic diagram illustrating the flow of a refrigerant in a laminated heat exchanger according to a fourth embodiment of the present invention. FIG. 17 is a schematic diagram illustrating a laminated heat exchanger according to a fifth embodiment of the present invention. FIG. 18 is a bottom view of a laminated heat exchanger according to a fifth embodiment of the present invention, and FIG. 19 (a) is a view of the present invention. number 5 FIG. 19 is a left side view of the laminated heat exchanger according to the embodiment of FIG. 19, (b) of FIG. 19 is a right side view thereof, and FIG. 20 is a fifth embodiment of the present invention. FIG. 21 is a schematic diagram illustrating the flow of the refrigerant in the stacked heat exchanger, and FIG. 21 is a front view of the stacked heat exchanger according to the sixth embodiment of the present invention; FIG. FIG. 23 is a bottom view of the stacked heat exchanger according to the sixth embodiment of the present invention. FIG. 23 (a) is a sectional view of the stacked heat exchanger according to the sixth embodiment of the present invention. FIG. 23 (b) is a right side view of the left side view, and FIG. 24 is a view showing the flow of the refrigerant in the laminated heat exchanger according to the sixth embodiment of the present invention. FIG. 25 is a schematic view for explaining, FIG. 25 is a front view of a laminated heat exchanger according to a seventh embodiment of the present invention, and FIG. 26 is a seventh embodiment of the present invention. Laminated heat exchange FIG. 27 (a) is a left side view of the laminated heat exchanger according to the seventh embodiment of the present invention, and FIG. 27 (b) is the bottom view. FIG. 28 is a right side view, FIG. 28 is a schematic diagram illustrating the flow of the refrigerant in the laminated heat exchanger according to the seventh embodiment of the present invention, and FIG. FIG. 30 is a front view of the laminated heat exchanger according to the eighth embodiment, and FIG. 30 is a bottom view of the laminated heat exchanger according to the eighth embodiment of the present invention. (A) of the figure is a left side view of the laminated heat exchanger according to the eighth embodiment of the present invention, (b) of FIG. 31 is a right side view thereof, and FIG. And FIG. 33 is a schematic diagram illustrating the flow of the refrigerant in the stacked heat exchanger according to the eighth embodiment of the present invention. FIG. 33 is a graph showing the relationship between the width of the heat exchanger in the ventilation direction and the heat exchanger capacity. In the characteristic diagram showing the relationship is there. BEST MODE FOR CARRYING OUT THE INVENTION

以下、 この発明の実施の形態について図面により説明する。  Hereinafter, embodiments of the present invention will be described with reference to the drawings.

第 1図乃至第 4図において、本願発明の第 1の実施の形態に係る積 層型熱交換器 1が示される。 この積層型熱交換器 1は、 例えば、 車両 用空調装置に搭載される蒸発器であり、長手方向の一端に形成された 一対の夕ンク部 2 , 3 と、 前記長手方向他端近傍まで延出して折り返 すと共に前記一対の夕ンク部 2 , 3を流体的に連通する冷媒流路 4を 有する複数のチューブエレメ ン ト 5を有し、 これら複数のチューブェ レメ ン ト 5 と交互に積層される複数のフィ ン 6 とによって構成され る FIGS. 1 to 4 show a laminated heat exchanger 1 according to a first embodiment of the present invention. This laminated heat exchanger 1 is, for example, a vehicle Evaporator mounted on an air conditioner for use in a vehicle, the elongator being formed at one end in the longitudinal direction, a pair of ink portions 2, 3; It has a plurality of tube elements 5 having a refrigerant flow path 4 that fluidly communicates 2 and 3, and is constituted by a plurality of fins 6 alternately stacked with the plurality of tube elements 5.

さらに、 この積層型熱交換器 1において、 前記一対のタンク部 2 , 3は積層方向に開口する図示しない連通孔を有しており、この連通孔 によって積層方向に連通する一方のタ ンク部 2によって第 1のタン ク群 Aが形成され、また積層方向に連通する他方のタンク部 3によつ て第 2の夕ンク群 Bが形成される。  Further, in the laminated heat exchanger 1, the pair of tank portions 2 and 3 has a communication hole (not shown) opened in the laminating direction, and one of the tank portions 2 communicated in the laminating direction by the communicating hole. Thus, a first tank group A is formed, and a second tank group B is formed by the other tank portion 3 communicating in the stacking direction.

この積層型熱交換器 1 には、積層方向の両端に一対のエン ドプレー ト 7 , 8が配される。 そして、 一方のエン ドプレー ト 7は、 チューブ エレメン ト 5 と合わさつて冷媒流路 4を形成している。 さらに、 ェン ドブレ一 ト 7には、冷媒流入通路 9 と冷媒流出通路 1 0 とを画成する 出入口通路形成用プレー ト 1 1が固着され、さ らに前記冷媒流入通路 9 と冷媒流出通路 1 0の一端には、図示しないブロ ック型膨張弁を装 着固定するための装着ブロ ック 1 2が設けられ、 この装着ブロ ック 1 2には入口パイプ部 1 3及び出口パイプ部 1 4が設けられている。  In the laminated heat exchanger 1, a pair of end plates 7, 8 are arranged at both ends in the laminating direction. The one end plate 7 is combined with the tube element 5 to form the refrigerant flow path 4. Further, an inlet / outlet passage forming plate 11 that defines a refrigerant inflow passage 9 and a refrigerant outflow passage 10 is fixed to the end plate 7, and further, the refrigerant inflow passage 9 and the refrigerant outflow passage At one end of 10, there is provided a mounting block 12 for mounting and fixing a block type expansion valve (not shown). The mounting block 12 has an inlet pipe section 13 and an outlet pipe section. There are 14 provided.

また、 前記冷媒流入通路 9の他端側は、 前記チューブェレメン ト 5 の一対のタンク部 2 , 3間に配される連通パイプ 1 5の一端と連通し、 この連通パイプ 1 5の他端は、前記他方のェン ドブレー ト 8の下方に 一体に形成された折返通路 1 6 と連通する。 この折返通路 1 6は、 前 記第 1のタンク群 Aと積層方向の他方の側に背さえたエン ドプレー ト 8に形成された開口部 1 8を介して連通する。 また、 前記冷媒流出 通路 1 0の他端側は、積層方向の一方の端部に配されたェン ドブレー ト Ίの下方に形成された開口部 1 7 を介して前記第 2のタンク群 B と連通する。 The other end of the refrigerant inflow passage 9 communicates with one end of a communication pipe 15 arranged between the pair of tanks 2 and 3 of the tube element 5, and the other end of the communication pipe 15 It communicates with a return path 16 integrally formed below the other end plate 8. The turn-back passage 16 communicates with the first tank group A through an opening 18 formed in the end plate 8 held on the other side in the stacking direction. Further, the other end side of the refrigerant outflow passage 10 is connected to the second tank group B through an opening 17 formed below an end plate 配 disposed at one end in the stacking direction. Communicate with

これによつて、積層方向の一方の側に設けられた入口パイプ部 1 3 から冷媒流入通路 9を通過した冷媒は、連通パイプ 1 5を介して積層 方向の他方の側に設けられた折返通路 1 6に至り、積層方向の他方の 側から第 1の夕ンク群 Aへ流入する。この折返通路 1 6を通過するこ とによって冷媒流の方向が 1 8 0 ° 変わるので、第 1のタンク群 Aへ 流入する冷媒の勢いが阻害され、第 1のタンク群 Aから第 1のタンク 群 Aと連通するそれそれの冷媒流路 4へ流入する冷媒量は、第 1の夕 ンク群 Aの流入方向の手前側と流入方向奥側で略等しくなる。  As a result, the refrigerant that has passed through the refrigerant inflow passage 9 from the inlet pipe portion 13 provided on one side in the stacking direction passes through the return pipe provided on the other side in the stacking direction via the communication pipe 15. It reaches 16 and flows into the first evening group A from the other side in the stacking direction. Since the direction of the refrigerant flow is changed by 180 ° by passing through the return passage 16, the momentum of the refrigerant flowing into the first tank group A is obstructed, and the first tank group A is moved from the first tank group to the first tank group. The amount of the refrigerant flowing into each of the refrigerant flow paths 4 communicating with the group A is substantially equal on the near side in the inflow direction and the back side in the inflow direction of the first ink group A.

そして、第 1の夕ンク群 Aから冷媒流路 4を上昇する第 1のパスと- 冷媒流路 4を第 2のタンク群 Bに向かって降下する第 2のパスとを 通過する冷媒は、 フィ ン 6を介してフィ ン 6を通過する空気の熱を吸 収して気化するが、各冷媒流路 4を通過する冷媒量が略均一化してい るので各部分での温度変化が一定となり、熱交換器の温度分布を均一 にすることができるものである。 そして、 気化した冷媒は、 第 2の夕 ンク群 Bから冷媒流出通路 1 0及び冷媒出口パイプ部 1 4を介して 次なる行程へ冷媒が流出されるものである。  Then, the refrigerant passing through the first path going up the refrigerant flow path 4 from the first sunset group A and the second path going down the refrigerant flow path 4 toward the second tank group B is: Although the heat of the air passing through the fins 6 is absorbed and vaporized via the fins 6, the amount of the refrigerant passing through each of the refrigerant flow paths 4 is substantially uniform, so that the temperature change in each portion becomes constant. In addition, the temperature distribution of the heat exchanger can be made uniform. Then, the vaporized refrigerant is to be discharged from the second tank group B to the next step through the refrigerant outflow passage 10 and the refrigerant outlet pipe portion 14.

第 5図乃至第 8図において、本願発明の第 2の実施の形態に係る積 層型熱交換器 2 0が開示される。 尚、 以下に説明する実施の形態にお いて、第 1の実施の形態に係る積層型熱交換器 1 と同様の箇所又は同 様の効果を奏する箇所には同一の符号を付してその説明を省略する。  5 to 8, a laminated heat exchanger 20 according to a second embodiment of the present invention is disclosed. Note that, in the embodiment described below, the same reference numerals are given to the same portions or portions having the same effects as those of the stacked heat exchanger 1 according to the first embodiment, and the description thereof will be omitted. Is omitted.

この第 2の実施の形態に係る積層型熱交換器 2 0は、積層方向他端 側に位置するチューブエレメ ン ト 2 1が、第 1のタンク群 A側から第 2のタンク群 B側に延出する拡大タンク部 2 2を有し、前記連通パイ プ 1 5の他端がこの拡大夕ンク部 2 2 と連通する構成となっている ものである。 これによつて、 拡大タンク部 2 2が折返通路 2 3を構成 することから、 拡大タンク部 2 2に流入した冷媒は、 拡大タンク部 2 2内に形成された折返通路 2 3 を介して 1 8 0 ° 方向転換して第 1 のタンク群 Aに流入するため、また拡大タンク部のチューブエレメ ン トでは、 9 0 ° 方向転換に続いて 9 0 ° 方向転換してチューブェレメ ン トへ流れるので、上述した第 1の実施の形態と同様に効果を奏する ものである。 In the laminated heat exchanger 20 according to the second embodiment, the tube element 21 located on the other end side in the laminating direction is such that the tube element 21 is moved from the first tank group A side to the second tank group B side. It has an extended tank portion 22 that extends, and the other end of the communication pipe 15 is configured to communicate with the enlarged ink portion 22. As a result, the expanded tank portion 22 constitutes a turn-back passage 23, and the refrigerant flowing into the expanded tank portion 22 receives the refrigerant from the expanded tank portion 22. After turning 180 ° through the turn-back passage 23 formed in 2 and flowing into the first tank group A, and in the tube element of the expanded tank part, turning 90 ° Since the direction is changed by 90 ° and flows to the tube element, the same effects as in the above-described first embodiment can be obtained.

第 9図乃至第 1 2図において、本願発明の第 3の実施の形態に係る 積層型熱交換器 4 0が閧示される。この積層型熱交換器 3 0において. 連通パイプ 1 5は熱交換器の外部に設けられる。 このため、 ェン ドプ レー ト 7, 8は、 通風方向下流側に延出する延出部 7 a, 8 aが形成 され、 一方のエン ドプレー ト 7では、 この形状に合致するように出入 口通路形成用プレート 1 1が形成され、冷媒流入通路 9が外方へ延出 して前記連通パイプ 1 5の一端と連通する。 また、 他方のエン ドプレ —ト 8では、この形状に合致するようにこのエン ドプレー ト 8で閉塞 される積層方向他方の端部に位置するタンク部 3 1が拡大して形成 され、 前記連通パイプ 1 5の他端が連通する。  9 to 12 show a laminated heat exchanger 40 according to a third embodiment of the present invention. In the laminated heat exchanger 30, the communication pipe 15 is provided outside the heat exchanger. For this reason, the end plates 7 and 8 are formed with extended portions 7a and 8a extending to the downstream side in the ventilation direction, and the end plate 7 enters and exits so as to conform to this shape. An opening passage forming plate 11 is formed, and the refrigerant inflow passage 9 extends outward and communicates with one end of the communication pipe 15. In the other end plate 8, a tank portion 31 located at the other end in the stacking direction, which is closed by the end plate 8, is formed so as to conform to this shape. The other end of 15 communicates.

これによつて、 連通パイ プ 1 5を通過した冷媒は、 前記拡大された タンク部 3 1に流入し、 1 8 0 ° 方向転換して前記第 1のタンク群 A に流入する。 これによつて、 熱交換器自体の通風方向の幅が小さ く形 成され、 タンク部 2 , 3間に連通パイプ 1 5を配する充分な空間を得 ることができない場合にも、上記第 1及び第 2の実施の形態と同様の 効果を奏することができるものである。  Thereby, the refrigerant having passed through the communication pipe 15 flows into the expanded tank portion 31, changes its direction by 180 °, and flows into the first tank group A. As a result, even if the width of the heat exchanger itself in the ventilation direction is small and it is not possible to obtain a sufficient space for arranging the communication pipe 15 between the tank sections 2 and 3, the above-mentioned method can be used. The same effects as in the first and second embodiments can be obtained.

第 1 3図乃至第 1 6図において、本願発明の第 4の実施の形態に係 る積層型熱交換器 4 0が開示される。この積層型熱交換器 4 0におい て、連通パイプ 1 5は第 1の夕ンク群 Aの内部を貫通して前記第 1の 夕ンク群 Aの積層方向他端側に位置するタンク部 4 1 まで延出して 配される。 このため、 前記冷媒流入通路 9は、 前記第 1及び第 2の実 施の形態と異なり、その他端側が第 1の夕ンク群 A側カーブするよう に形成される。 13 to 16 show a laminated heat exchanger 40 according to a fourth embodiment of the present invention. In this stacked heat exchanger 40, the communication pipe 15 penetrates through the inside of the first evening group A and is located at the other end of the first evening group A in the stacking direction. It is extended and distributed. For this reason, the refrigerant inflow passage 9 is different from the first and second embodiments in that the other end side is curved to the first evening group A side. Formed.

これによつて、 第 4の実施の形態においては、 連通パイプ 1 5を通 過した冷媒は、タンク部 4 1で該タンク部 4 1の積層方向外方を閉塞 するェン ドプレー ト 8に衝突して冷媒流方向を 1 8 0 ° 転換するこ ととなり、 さらに、 第 1の夕ンク群 A内を連通パイプ 1 5が貫通して いることから、第 1の夕ンク群 Aを通過する冷媒流の勢いが阻害され るので、第 1の夕ンク群 Aと連通する冷媒流路 4を通過する冷媒量を 均一化でき、上述した実施の形態と同様の効果を奏することができる ものである。  Accordingly, in the fourth embodiment, the refrigerant that has passed through the communication pipe 15 collides with the end plate 8 that closes the tank portion 41 outside the stacking direction of the tank portion 41. As a result, the refrigerant flow direction is changed by 180 °, and since the communication pipe 15 penetrates through the first evening group A, the refrigerant passing through the first evening group A Since the momentum of the flow is obstructed, the amount of the refrigerant passing through the refrigerant passage 4 communicating with the first ink group A can be made uniform, and the same effect as in the above-described embodiment can be obtained. .

第 1 7図乃至第 2 0図において、第 5の実施の形態に係る積層型熱 交換器 5 0が開示される。 この積層型熱交換器 5 0において、 連通パ イブ 1 5は、 冷媒流入通路 9の他端と、 前記積層方向他方の側の一つ 手前に位置し、第 2のタンク群側に延出した拡大タンク部 5 1 と連通 する。 この拡大タンク部 5 1は、 前述した第 2の実施の形態に係る拡 大タンク部 5 2が、積層方向の他方の側の外端部に位置して容積が通 常の夕ンク部の半分であるのに対して、通常の容積を有する夕ンク部 の最外端部に位置するものである。  17 to 20 disclose a stacked heat exchanger 50 according to a fifth embodiment. In the laminated heat exchanger 50, the communication pipe 15 is located at the other end of the refrigerant inflow passage 9 and one side before the other side in the laminating direction, and extends toward the second tank group. Communicates with the enlarged tank 51. The enlarged tank portion 51 is different from the enlarged tank portion 52 of the second embodiment in that the enlarged tank portion 52 is located at the outer end on the other side in the stacking direction and has a normal capacity. On the other hand, it is located at the outermost end of the sunken part having a normal volume.

これによつて、 連通パイプ 1 5を通過した冷媒は、 この拡大タンク 部 5 1から第 1の夕ンク群 A内に流れ込むので、実質的に第 1のタン ク群 A内を流れる冷媒は、連通パイプ 1 5を流れる方向に対して 1 8 0 ° 方向転換したことになるので、上述した実施の形態と同様の効果 を奏することができるものである。 ここで、 連通パイプ 1 5は、 積層 方向他方の側の一つ手前に位置させたが、さ らなる実施の形態として 3つ又は 4つ手前に位置させるようにしても良いものである。  As a result, the refrigerant that has passed through the communication pipe 15 flows from the expanded tank section 51 into the first evening tank group A, so that the refrigerant that substantially flows through the first tank group A is: Since the direction has been changed by 180 ° with respect to the direction in which the communication pipe 15 flows, the same effect as in the above-described embodiment can be obtained. Here, the communication pipe 15 is located immediately before the other side in the stacking direction, but may be located three or four before as a further embodiment.

第 2 1図乃至第 2 4図において、第 6の実施の形態に係る積層型熱 交換器 6 0が開示される。 この積層型熱交換器 6 0は、 積層方向の略 中央に装着ブロ ック 1 2 ' が設けられ、 この装着ブロック 1 2 ' に設 けられた入口パイプ部 1 3, が直接分配パイプ 1 5 a , 1 5 bに接続 され、 前記装着プロ ック 1 2, に設けられた出口パイプ部 1 4, は、 第 2のタンク群 Bの略中央に位置するタンク部 3 a, 3 bと直接接続 される。 また、 前記分配パイ プ 1 5 aは、 前記入口パイ プ部 1 3, と 積層方向他端側に位置する場所に設けられた拡大タンク部 6 1 と連 通し、 前記分配パイブ 1 5 bは、 前記入口パイブ部 1 3, と積層方向 一端側に位置する場所に設けられた拡大タンク部 6 2 と連通する。 21 to 24, a stacked heat exchanger 60 according to a sixth embodiment is disclosed. In the stacked heat exchanger 60, a mounting block 12 'is provided substantially at the center in the laminating direction, and the mounting block 12' is provided in the mounting block 12. The inlet pipe section 13 is directly connected to the distribution pipes 15a and 15b, and the outlet pipe section 14 provided in the mounting block 12 is connected to the second tank group B. It is directly connected to the tanks 3a and 3b located at the approximate center of the. Further, the distribution pipe 15 a communicates with the inlet pipe section 13 and an enlarged tank section 61 provided at a location located on the other end side in the stacking direction, and the distribution pipe 15 b is It communicates with the inlet pipe section 13 and an enlarged tank section 62 provided at a position located on one end side in the stacking direction.

これによつて、 入口パイプ部 1 3 ' から分配パイプ 1 5 a , 1 5 b を介して第 1の夕ンク群 Aの両端側の拡大夕ンク部 6 1 , 6 2から第 1のタンク群 Aに流入し、冷媒流路 4を介して第 2のタンク群 Bに流 入して前記出口パイプ部 1 4 'から次なる行程に流出する。このため、 拡大夕ンク部 6 1 , 6 2において、 分配パイプ 1 5 a , 1 5 bを流れ る方向と 1 8 0 ° 方向転換して第 1の夕ンク群 Aに流れ込むと共に、 中央方向に向かって両方から流れ込むことから熱交換器の中央部分 における冷媒量を確保できるので、熱交換器自体の熱交換器能力を向 上させることができ、さらに各冷媒流路 4への冷媒量を均一化できる ため、 温度分布を良好にすることができるものである。  As a result, from the inlet pipe section 13 'through the distribution pipes 15a and 15b, the expanded tank sections 6 1 and 6 2 at both ends of the first tank group A are expanded to the first tank group. A, flows into the second tank group B via the refrigerant flow path 4, and flows out of the outlet pipe section 14 'in the next stroke. For this reason, in the enlarged sunset sections 61 and 62, the direction of the distribution pipes 15a and 15b is changed by 180 ° to the direction of the distribution pipes and flows into the first sunset group A, and the center Since the refrigerant flows from both sides, the amount of refrigerant in the central part of the heat exchanger can be secured, so that the heat exchanger capacity of the heat exchanger itself can be improved and the amount of refrigerant to each refrigerant flow path 4 can be uniform. Therefore, the temperature distribution can be improved.

第 2 5図乃至第 2 8図において、本願発明の第 7の実施の形態に係 る積層型熱交換器 7 0が閧示される。この積層型熱交換器 7 0におい て、 前記分配パイプ 1 5 a , 1 5 bは、 前述した第 3の実施の形態に 係る積層型熱交換器 3 0の連通パイ プ 1 5の場合と同様に積層型熱 交換器 7 0の通風方向下流側に設けられる。 これに伴って、 積層方向 両端部に位置するタンク部が、熱交換器の通風方向に延出する拡大夕 ンク部 7 1 , 7 2であり、 前記分配パイプ 1 5 a , 1 5 bは、 前記入 口パイプ部 1 3, とこれら拡大タンク部 7 1 , 7 2をそれそれに連通 する。 これによつて、 前述した実施の形態と同様の効果が得られるも のである。 第 2 9図乃至第 3 2図において、本願発明の第 8の実施の形態に係 る積層型熱交換器 8 0が開示される。この積層型熱交換器 7 0におい て、 前記分配パイプ 1 5 a , 1 5 bは、 前記第 1のタンク群 Aの内部 に貫通して設けられ、 前記入口パイブ部 1 3 ' と前記第 1のタンク群 Aの積層方向両端部に位置する夕ンク部 8 1, 8 2 とをそれそれ連通 するものである。 これによつて、 上述した実施の形態と同様の効果を 得ることができるものである。 FIGS. 25 to 28 show a laminated heat exchanger 70 according to a seventh embodiment of the present invention. In the laminated heat exchanger 70, the distribution pipes 15a and 15b are the same as those in the case of the communication pipe 15 of the laminated heat exchanger 30 according to the third embodiment described above. The heat exchanger is provided on the downstream side of the laminated heat exchanger 70 in the ventilation direction. Along with this, the tank portions located at both ends in the stacking direction are the enlarged tank portions 71, 72 extending in the ventilation direction of the heat exchanger, and the distribution pipes 15a, 15b are: The inlet pipe section 13 and these enlarged tank sections 71 and 72 are connected to it. Thereby, the same effect as in the above-described embodiment can be obtained. 29 to 32, a stacked heat exchanger 80 according to an eighth embodiment of the present invention is disclosed. In the stacked heat exchanger 70, the distribution pipes 15a and 15b are provided so as to penetrate inside the first tank group A, and the inlet pipe section 13 'and the first In this case, the ink tanks A and 8 at the both ends in the stacking direction of the tank group A communicate with each other. Thus, the same effect as in the above-described embodiment can be obtained.

また、 第 3 3図に示すように、 上述した熱交換器の構成において、 冷凍能力/通負抵抗で示す熱交換器能力 F aは、上記熱交換器の通風 方向の幅 C wが 4 0 m mの時に最大能力を得ることができたが、所定 の能力以上 (例えば、 8 0 % ) を得ることの出来る範囲は、 前記熱交 換器の通風方向の幅 C wが、 略 3 0 m m以上 5 7 m m以下であった。 このことから、 この範囲内に熱交換器の通風方向の幅を設定すること が望ましい。 産業上の利用可能性  Further, as shown in FIG. 33, in the configuration of the heat exchanger described above, the heat exchanger capacity F a represented by the refrigerating capacity / the negative resistance is such that the width C w in the ventilation direction of the heat exchanger is 40 °. mm, the maximum capacity could be obtained.However, the range in which the specified capacity or more (for example, 80%) can be obtained is that the width Cw in the ventilation direction of the heat exchanger is approximately 30 mm. More than 57 mm. For this reason, it is desirable to set the width of the heat exchanger in the ventilation direction within this range. Industrial applicability

以上説明したように、 この発明によれば、 タンク群に仕切りを設け ない 2パスとすると共に、連通パイプによって第 1のタンク群に流れ 込む冷媒の方向を 1 8 0 ° 方向転換するようにしたので、第 1のタン ク群の流れ込む冷媒の勢いを抑制することができ、タンク群を構成す る夕ンク部から冷媒流路に至る冷媒量を各冷媒流路において均一化 することができ、 また通路抵抗を低減でき、 さらに熱交換器の中央部 分を流れる冷媒量が確保できるため、熱交換器の温度分布を良好にで きるものである。  As described above, according to the present invention, the tank group has two paths without partitions, and the direction of the refrigerant flowing into the first tank group is changed by 180 ° by the communication pipe. Therefore, the momentum of the refrigerant flowing into the first tank group can be suppressed, and the amount of refrigerant from the ink tank forming the tank group to the refrigerant flow path can be made uniform in each refrigerant flow path. In addition, the passage resistance can be reduced, and the amount of refrigerant flowing in the central part of the heat exchanger can be secured, so that the temperature distribution of the heat exchanger can be improved.

Claims

請 求 の 範 囲 The scope of the claims 1 .長手方向一端に形成された一対の夕ンク部及び前記長手方向他端 近傍まで延出して折り返すと共に前記一対のタ ンク部を流体的に連 通する冷媒流路を有する複数のチューブエレメン ト と、該複数のチュ —ブエレメン ト と交互に積層されるフィ ンと、前記積層方向両端に設 けられるエン ドプレー ト とを少なく とも具備する熱交換器において、 前記一方の夕ンク部を積層方向に連通して形成される第 1のタ ン ク群と、 1. A pair of tube elements formed at one end in the longitudinal direction and a plurality of tube elements having a refrigerant flow path extending to the vicinity of the other end in the longitudinal direction and being folded and fluidly communicating the pair of tank parts. And a fin alternately stacked with the plurality of tube elements, and end plates provided at both ends in the stacking direction, wherein the one ink portion is stacked in the stacking direction. A first group of tanks formed in communication with 前記他方のタンク部を積層方向に連通して形成される第 2のタン ク群と、  A second tank group formed by connecting the other tank portion in the stacking direction; 前記熱交換器の積層方向一端に配された一方のェン ドブレ一 卜に 設けられる冷媒入口部と、  A refrigerant inlet provided on one end bracket disposed at one end in the stacking direction of the heat exchanger; 前記一方のエン ドプレー トに形成された冷媒流入通路を介して、前 記冷媒入口部と前記第 1のタ ンク群の他端近傍に位置するタンク部 とを連通する連通路と、 前記一方のェン ドプレー トに形成された冷 媒流出通路を介して、前記第 2のタンク群の一端に位置するタンク部 と連通する冷媒出口部とを具備することを特徴とする熱交換器。  A communication passage communicating between the refrigerant inlet and a tank located near the other end of the first tank group via a refrigerant inflow passage formed in the one end plate; A heat exchanger, comprising: a refrigerant outlet communicating with a tank located at one end of the second tank group via a refrigerant outlet passage formed in an end plate. 2 . 前記連通路は、 前記冷媒流入通路に接続される一端を有する連通 パイプと、該連通パイプの他端と前記第 1の夕ンク群の他方側端部に 位置する夕ンク部とを連通する折返通路とによって構成されること を特徴とする請求の範囲第 1項記載の熱交換器。  2. The communication path connects a communication pipe having one end connected to the refrigerant inflow path, and a second end of the communication pipe and a sunset portion located at the other end of the first sunset group. 2. The heat exchanger according to claim 1, wherein the heat exchanger is formed by a turn-back passage. 3 . 前記連通路は、 前記冷媒流入通路に接続される一端を有する連通 パイプと、前記第 1の夕ンク群の他方側端部に位置する夕ンク部から 延出し、前記連通パイブの他端と連通する拡大タンク部とによって構 成されることを特徴とする請求の範囲第 1項記載の熱交換器。  3. The communication passage extends from a communication pipe having one end connected to the refrigerant inflow passage and an ink portion located at the other end of the first ink group, and has another end of the communication pipe. 2. The heat exchanger according to claim 1, wherein the heat exchanger is constituted by an expansion tank portion communicating with the heat exchanger. 4 . 前記連通パイプは、 一対のタンク部の間に配されることを特徴と する請求の範囲第 2項又は第 3項記載の熱交換器。 4. The communication pipe is disposed between a pair of tank parts. The heat exchanger according to claim 2 or 3, wherein 5 . 前記連通パイプは、 一対の夕ンク部の外側に配されることを特徴 とする請求の範囲第 2項又は第 3項記載の熱交換器。  5. The heat exchanger according to claim 2, wherein the communication pipe is disposed outside a pair of the ink portions. 6 . 前記連通パイ プは、 前記第 1のタンク群の内部を貫通することを 特徴とする請求の範囲第 2項又は第 3項記載の熱交換器。  6. The heat exchanger according to claim 2, wherein the communication pipe penetrates through the inside of the first tank group. 7 .長手方向一端に形成された一対の夕ンク部及び前記長手方向他端 近傍まで延出して折り返すと共に前記一対のタ ンク部を流体的に連 通する冷媒流路を有する複数のチューブエレメ ン ト と、該複数のチュ ーブエレメ ン ト と交互に積層されるフィ ンと、前記積層方向両端に設 けられる一対のエン ドプレー ト とを少なく とも具備する熱交換器に おいて、  7. A pair of tube elements formed at one end in the longitudinal direction and a plurality of tube elements having a refrigerant flow path extending to the vicinity of the other end in the longitudinal direction and being folded and fluidly communicating the pair of tank parts. And a pair of end plates provided at both ends in the laminating direction of the heat exchanger, the fin being alternately stacked with the plurality of tube elements, and a pair of end plates provided at both ends in the stacking direction. 前記一方の夕ンク部を積層方向に連通して形成される第 1のタン ク群と、  A first tank group formed by connecting the one ink portion in the stacking direction; 前記他方のタンク部を積層方向に連通して形成される第 2のタン ク群と、  A second tank group formed by connecting the other tank portion in the stacking direction; 前記第 1のタンク群の略中央のタンク部外側に設けられる冷媒入 口部と、  A refrigerant inlet provided substantially outside the tank at the center of the first tank group; 前記冷媒入口部と前記第 1のタンク群の両端近傍に位置するタン ク部とを連通する連通路と、  A communication passage for communicating the refrigerant inlet with tanks located near both ends of the first tank group; 前記第 2のタンク群の略中央で前記冷媒入口部に並設されると共 に、前記第 2のタンク群の略中央に位置する夕ンク部と直接連通され る冷媒出口部とを具備することを特徴とする熱交換器。  A coolant outlet is provided substantially at the center of the second tank group and in parallel with the coolant inlet, and is directly communicated with an ink tank located substantially at the center of the second tank group. A heat exchanger, characterized in that: 8 . 前記連通路は、 前記冷媒流入通路に接続される一端を有する連通 パイプと、該連通パイプの他端と前記第 1の夕ンク群の他方側端部に 位置するタンク部とを連通する折返通路とによって構成されること を特徴とする請求の範囲第 7項記載の熱交換器。  8. The communication path communicates a communication pipe having one end connected to the refrigerant inflow path, and a second end of the communication pipe and a tank located at the other end of the first group of ink. 8. The heat exchanger according to claim 7, wherein the heat exchanger is constituted by a turnback passage. 9 . 前記連通路は、 前記冷媒流入通路に接続される一端を有する一対 の分配パイブと、前記第 1の夕ンク群の両端近傍に位置する夕ンク部 の各々のから延出し、前記分配パイプの各々の他端と連通する拡大夕 ンク部とによって構成されることを特徴とする請求の範囲第 7項記 載の熱交換器。 9. The communication path is a pair having one end connected to the refrigerant inflow path. A distribution pipe and an enlarged ink section extending from each of the evening water sections located near both ends of the first evening water group and communicating with the other end of each of the distribution pipes. A heat exchanger as set forth in claim 7 characterized by the above-mentioned. 1 0 . 前記分配パイプは、 一対のタンク部の間に配されることを特徴 とする請求の範囲第 7項又は第 9項記載の熱交換器。  10. The heat exchanger according to claim 7, wherein the distribution pipe is disposed between a pair of tank portions. 1 1 . 前記分配パイプは、 一対のタンク部の外側に配されることを特 徴とする請求の範囲第 7項又は第 9項記載の熱交換器。  11. The heat exchanger according to claim 7, wherein the distribution pipe is disposed outside a pair of tank portions. 1 2 . 前記分配パイプは、 前記第 1のタンク群の内部を貫通すること を特徴とする請求の範囲第 7項又は第 9項記載の熱交換器。  12. The heat exchanger according to claim 7 or 9, wherein the distribution pipe penetrates through the inside of the first tank group. 1 3 . 前記熱交換器の通風方向の幅は、 略 3 0 m m以上 5 7 m m以下 であることを特徴とする請求の範囲第 1項から第 1 2項のいずれか に記載の熱交換器。  13. The heat exchanger according to any one of claims 1 to 12, wherein the width of the heat exchanger in the ventilation direction is approximately 30 mm or more and 57 mm or less. .
PCT/JP2000/001809 1999-07-08 2000-03-24 Heat exchanger Ceased WO2001004560A1 (en)

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JP11/193841 1999-07-08

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Cited By (3)

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Publication number Priority date Publication date Assignee Title
US20130312942A1 (en) * 2010-10-25 2013-11-28 Sylvain Moreau Heat Exchanger With Lateral Fluid Supply
WO2018206818A1 (en) * 2017-05-12 2018-11-15 Valeo Systemes Thermiques Multi-pass heat exchanger that forms part of a refrigerant circuit
FR3066149A1 (en) * 2017-05-12 2018-11-16 Valeo Systemes Thermiques MULTI-PASS HEAT EXCHANGER COMPRISING A REFRIGERANT FLUID CIRCUIT

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JPH0645150Y2 (en) * 1987-09-14 1994-11-16 株式会社ゼクセル Vehicle heat exchanger
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JPH0933187A (en) * 1995-07-19 1997-02-07 Showa Alum Corp Stacked heat exchanger
JPH09152293A (en) * 1995-11-30 1997-06-10 Zexel Corp Single tank type heat exchanger
JPH09309321A (en) * 1996-05-23 1997-12-02 Zexel Corp Lamination type heat exchanger

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Publication number Priority date Publication date Assignee Title
JPS6314093A (en) * 1986-06-28 1988-01-21 Nippon Denso Co Ltd Laminated type heat exchanger
JPH0645150Y2 (en) * 1987-09-14 1994-11-16 株式会社ゼクセル Vehicle heat exchanger
JPH0712481A (en) * 1993-06-21 1995-01-17 Toshiba Corp Air-conditioning heat exchanger manufacturing method and manufacturing apparatus thereof
JPH0886591A (en) * 1994-07-22 1996-04-02 Nippondenso Co Ltd Heat exchanger and refrigerant evaporator
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JPH09152293A (en) * 1995-11-30 1997-06-10 Zexel Corp Single tank type heat exchanger
JPH09309321A (en) * 1996-05-23 1997-12-02 Zexel Corp Lamination type heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130312942A1 (en) * 2010-10-25 2013-11-28 Sylvain Moreau Heat Exchanger With Lateral Fluid Supply
US9829255B2 (en) * 2010-10-25 2017-11-28 Valeo Systemes Thermiques Heat exchanger with lateral fluid supply
WO2018206818A1 (en) * 2017-05-12 2018-11-15 Valeo Systemes Thermiques Multi-pass heat exchanger that forms part of a refrigerant circuit
FR3066149A1 (en) * 2017-05-12 2018-11-16 Valeo Systemes Thermiques MULTI-PASS HEAT EXCHANGER COMPRISING A REFRIGERANT FLUID CIRCUIT

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