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JP6906141B2 - Heat exchanger shunt - Google Patents
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JP6906141B2 - Heat exchanger shunt - Google Patents

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JP6906141B2
JP6906141B2 JP2017202290A JP2017202290A JP6906141B2 JP 6906141 B2 JP6906141 B2 JP 6906141B2 JP 2017202290 A JP2017202290 A JP 2017202290A JP 2017202290 A JP2017202290 A JP 2017202290A JP 6906141 B2 JP6906141 B2 JP 6906141B2
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refrigerant
pipe
flat
heat exchanger
flow path
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JP2019074287A (en
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立慈 川端
立慈 川端
長谷川 寛
寛 長谷川
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Panasonic Intellectual Property Management Co Ltd
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Description

本発明は、一対のヘッダーパイプと、複数の冷媒流路をもつ複数の扁平管と、で構成され、複数の扁平管の間を流れる空気と、扁平管の冷媒流路の中を流れる冷媒とで熱交換を行う熱交換器の分流器に関するものである。 The present invention is composed of a pair of header pipes and a plurality of flat pipes having a plurality of refrigerant flow paths, and the air flowing between the plurality of flat pipes and the refrigerant flowing in the refrigerant flow paths of the flat pipes. It relates to a refrigerant divider of a heat exchanger that exchanges heat with.

従来から、水平方向の左右に対峙する一対のヘッダーパイプと、複数の冷媒流路をもつ複数の扁平管と、扁平管同士の間に設けられる伝熱フィンと、で構成され、複数の扁平管の間を流れる空気と、扁平管の冷媒流路の中を流れる冷媒とで熱交換を行う熱交換器が知られている。 Conventionally, it has been composed of a pair of header pipes facing each other in the horizontal direction, a plurality of flat pipes having a plurality of refrigerant flow paths, and heat transfer fins provided between the flat pipes, and a plurality of flat pipes. There are known heat exchangers that exchange heat between the air flowing between them and the refrigerant flowing in the refrigerant flow path of the flat pipe.

この種の熱交換器において、各扁平管への冷媒流出量を均一化させるため、複数の扁平管を接続する外管と、重力方向に冷媒孔を設けた内管と、で構成する二重管構造の熱交換器分流器が開示されている。(例えば、特許文献1参照)。
図11、図12、図13は、扁平管内の冷媒流れ方向をx方向、空気流れ方向をy方向、重力上向き方向をz方向とした場合に、図11は、特許文献1に記載された従来の熱交換器分流器のx−z平面の断面図、図12は、図11のA−A断面図(特許文献1に記載された従来の熱交換器分流器のx−y平面の断面図)、図13は、図11のB−B断面図(特許文献1に記載された従来の熱交換器分流器を用いた熱交換器における扁平管のy−z平面の断面図)である。
In this type of heat exchanger, in order to equalize the amount of refrigerant flowing out to each flat pipe, a double structure consisting of an outer pipe connecting a plurality of flat pipes and an inner pipe having refrigerant holes in the direction of gravity. A tube structure heat exchanger diversion device is disclosed. (See, for example, Patent Document 1).
11, 12 and 13 show the conventional method described in Patent Document 1 when the refrigerant flow direction in the flat tube is the x direction, the air flow direction is the y direction, and the gravity upward direction is the z direction. FIG. 12 is a cross-sectional view taken along the line xy of the heat exchanger diversion device, FIG. 12 is a cross-sectional view taken along the line AA of FIG. 11 (cross-sectional view of the xy plane of the conventional heat exchanger diversion device described in Patent Document 1). ), FIG. 13 is a cross-sectional view taken along the line BB of FIG. 11 (cross-sectional view of the yz plane of the flat tube in the heat exchanger using the conventional heat exchanger diversion device described in Patent Document 1).

図11、図12、図13に示すように、熱交換器1は、複数の冷媒流路2で形成された複数の扁平管3と、扁平管3の両端部をそれぞれ接続する一対のヘッダーパイプ4と、で構成され、ヘッダーパイプ4は、複数の扁平管3を接続する外管5と、重力上向き方向(z方向)の下方から上方になるにしたがって順次大きくした気液二相冷媒を吹き出す冷媒孔6を設けた内管7と、で構成された二重管構造としている。 As shown in FIGS. 11, 12, and 13, the heat exchanger 1 includes a plurality of flat pipes 3 formed by a plurality of refrigerant flow paths 2 and a pair of header pipes connecting both ends of the flat pipes 3. The header pipe 4 is composed of 4 and an outer pipe 5 connecting a plurality of flat pipes 3 and blows out a gas-liquid two-phase refrigerant that is sequentially increased from the lower side to the upper side in the upward direction of gravity (z direction). It has a double pipe structure composed of an inner pipe 7 provided with a refrigerant hole 6.

これにより、重力により流れやすい下側の扁平管への冷媒流出量を減少させ、流れにくい上側の扁平管への冷媒流出量を増加させることで、上側の扁平管を流れる冷媒量と下側の扁平管を流れる冷媒量を均一化させることができる。 As a result, the amount of refrigerant flowing out to the lower flat pipe that easily flows due to gravity is reduced, and the amount of refrigerant flowing out to the upper flat pipe that is difficult to flow is increased, so that the amount of refrigerant flowing through the upper flat pipe and the lower side The amount of refrigerant flowing through the flat pipe can be made uniform.

特開平3−195873号公報Japanese Unexamined Patent Publication No. 3-195873

しかしながら従来の構成では、内管に設けた冷媒孔は扁平管の長手方向(y方向)の幅に対して開口面積が小さく、冷媒孔より吹き出した気液二相冷媒の内、密度の大きい液冷媒は慣性力が大きく、直進しやすく、液冷媒より軽いガス冷媒は拡散しやすいため、冷媒孔と、冷媒孔の近傍の冷媒流路との間の空間には湿り度の高い冷媒が存在し、冷媒孔と、冷媒孔から遠方の冷媒流路との間の空間には湿り度の低い冷媒が存在しやすくなり、複数の冷媒流路毎に冷媒の状態が異なって流れることで、各冷媒流路で冷媒が蒸発完了する位置が異なり、扁平管を有効に利用できず、熱交換器性能が低下するという課題を有していた。 However, in the conventional configuration, the refrigerant hole provided in the inner pipe has a small opening area with respect to the width in the longitudinal direction (y direction) of the flat pipe, and among the gas-liquid two-phase refrigerant blown out from the refrigerant hole, a liquid having a high density. Since the refrigerant has a large inertial force, easily travels straight, and the gas refrigerant, which is lighter than the liquid refrigerant, easily diffuses, a highly moist refrigerant exists in the space between the refrigerant hole and the refrigerant flow path near the refrigerant hole. , Refrigerant with low humidity tends to exist in the space between the refrigerant hole and the refrigerant flow path far from the refrigerant hole, and the state of the refrigerant flows differently for each of a plurality of refrigerant flow paths, so that each refrigerant flows. The position where the refrigerant completes evaporation differs in the flow path, the flat tube cannot be used effectively, and there is a problem that the heat exchanger performance deteriorates.

特に、前縁効果により熱伝達率が高く、空気流れの上流側に位置する冷媒流路内に、湿
り度の低い冷媒が、空気流れの下流側に位置する冷媒流路内に、湿り度の高い冷媒が流れた場合、空気流れの上流側と下流側の冷媒流路で、冷媒が蒸発完了する位置が大きく異なるため、熱交換器性能が大幅に低下する。
In particular, the heat transfer rate is high due to the front edge effect, and the low-humidity refrigerant is placed in the refrigerant flow path located on the upstream side of the air flow, and the low-humidity refrigerant is placed in the refrigerant flow path located on the downstream side of the air flow. When a high amount of refrigerant flows, the position where the refrigerant completes evaporation differs greatly between the upstream side and the downstream side of the air flow, so that the heat exchanger performance is significantly deteriorated.

本発明は、前記従来の課題を解決するもので、蒸発しやすい流路に湿り度の高い冷媒を、蒸発しにくい流路に湿り度の低い冷媒を流すことにより、各冷媒流路に流れる冷媒が、早めに蒸発することや、蒸発することなく流れることを抑制でき、各冷媒流路で冷媒が蒸発完了する位置を均一化することができる熱交換器分流器を提供することを目的とする。 The present invention solves the above-mentioned conventional problems, and is a refrigerant flowing in each refrigerant flow path by flowing a highly moist refrigerant in a flow path that easily evaporates and a low humidity refrigerant in a flow path that does not easily evaporate. However, it is an object of the present invention to provide a heat exchanger diversion device that can suppress early evaporation or flow without evaporating, and can make the position where the refrigerant completes evaporation uniform in each refrigerant flow path. ..

前記従来の課題を解決するために、本発明の熱交換器は、複数の冷媒流路を有する扁平管と、扁平管の両端部をそれぞれ接続する一対のヘッダーパイプと、を備えた熱交換器において、少なくとも一方のヘッダーパイプを、複数の扁平管を接続する外管と、扁平管へ冷媒を流出する冷媒孔を扁平管の接続方向の側面に設けた内管と、で構成された二重管構造とし、前記内管の中心軸が、前記扁平管の長手方向の幅中央部を通り、重力方向と平行
な中心面より、空気流れの上流側に偏心するものである。
In order to solve the above-mentioned conventional problems, the heat exchanger of the present invention is a heat exchanger provided with a flat pipe having a plurality of refrigerant flow paths and a pair of header pipes connecting both ends of the flat pipe. in, at least one of the header pipe, and the outer tube for connecting a plurality of flat tubes, an inner tube provided with a cold Nakadachiana you outflow refrigerant into the flat tubes in the connection direction of the side surface of the flat tube, in which is constituted With a double pipe structure, the central axis of the inner pipe passes through the central portion of the width in the longitudinal direction of the flat pipe and is parallel to the direction of gravity.
It is eccentric to the upstream side of the air flow from the central surface.

これにより、熱伝達率が高くなる空気流れの上流側の扁平管の冷媒流路の手前へ、湿り度の高い冷媒を内管から吹き出しやすくなるため、空気流れの上流側の扁平管の冷媒流路に、湿り度の高い冷媒が流れやすくなる。 This makes it easier to blow out highly moist refrigerant from the inner pipe to the front of the refrigerant flow path of the flat pipe on the upstream side of the air flow, which has a high heat transfer coefficient. Highly moist refrigerant easily flows through the road.

本発明の熱交換器分流器は、扁平管の各冷媒流路で冷媒が蒸発完了する位置を均一化することができるため、扁平管を有効に利用でき、熱交換器性能を向上することができる。 In the heat exchanger shunt of the present invention, since the position where the refrigerant completes evaporation can be made uniform in each refrigerant flow path of the flat pipe, the flat pipe can be effectively used and the heat exchanger performance can be improved. can.

本発明の実施の形態1におけるヘッダーパイプのx−z平面の断面図Cross-sectional view of the xx plane of the header pipe according to the first embodiment of the present invention. 本発明の実施の形態1におけるヘッダーパイプのx−y平面の断面図Cross-sectional view of the xy plane of the header pipe according to the first embodiment of the present invention. 本発明の実施の形態1のヘッダーパイプを用いた熱交換器における扁平管の y−z平面の断面図Cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe of the first embodiment of the present invention. 本発明の実施の形態1の変形例1におけるヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図Cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe in the first modification of the first embodiment of the present invention. 本発明の実施の形態1の変形例2におけるヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図Cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe in the second modification of the first embodiment of the present invention. 本発明の実施の形態1の変形例3におけるヘッダーパイプを用いた熱交換器 における扁平管のy−z平面の断面図Cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe in the third modification of the first embodiment of the present invention. 熱交換器を適用した室外機の内部構造を示すx−y平面図XY plan view showing the internal structure of the outdoor unit to which the heat exchanger is applied 熱交換器を適用した室外機の内部構造を示すx−z平面図X-z plan view showing the internal structure of the outdoor unit to which the heat exchanger is applied 本発明の実施の形態2におけるヘッダーパイプのx−y平面の断面図Cross-sectional view of the xy plane of the header pipe according to the second embodiment of the present invention. 本発明の実施の形態2におけるヘッダーパイプを用いた熱交換器における 扁平管y−z平面の断面図Cross-sectional view of the flat tube yz plane in the heat exchanger using the header pipe according to the second embodiment of the present invention. 従来の熱交換器のヘッダーパイプのx−z平面の断面図Sectional view of the x-z plane of the header pipe of a conventional heat exchanger 従来の熱交換器のヘッダーパイプのx−y平面の断面図Sectional view of the xy plane of the header pipe of a conventional heat exchanger 従来の熱交換器の扁平管のy−z平面の断面図Cross-sectional view of the yz plane of the flat tube of a conventional heat exchanger

第1の発明は、複数の冷媒流路を有する扁平管と、複数の扁平管を水平方向に設置し、扁平管の両端部をそれぞれ接続する一対のヘッダーパイプと、を備え、複数の扁平管を、ヘッダーパイプの軸方向(重力方向)に沿って、互いに平行に接続された熱交換器において、少なくとも一方のヘッダーパイプを、複数の扁平管を接続する外管と、扁平管へ冷媒
を流出する複数の冷媒孔を扁平管の接続側の側面に設けた内管と、で構成された二重管構造とする。
The first invention includes a flat pipe having a plurality of refrigerant flow paths, a pair of header pipes in which the plurality of flat pipes are installed in the horizontal direction and both ends of the flat pipes are connected to each other, and the plurality of flat pipes. In a heat exchanger connected in parallel with each other along the axial direction (gravity direction) of the header pipe, at least one header pipe flows out to the outer pipe connecting a plurality of flat pipes and the flat pipe. The double pipe structure is composed of an inner pipe having a plurality of refrigerant holes provided on the side surface of the flat pipe on the connecting side.

冷媒孔は、扁平管の長手方向の幅中央部を通り、重力方向と平行な中心面を基準に、空気流れの上流側のほうが、空気流れの下流側よりも広くする。
これにより、内管から、熱伝達率が高くなる空気流れの上流側の扁平管の冷媒流路の手前へ、湿り度の高い冷媒を吹き出し、空気流れの上流側の扁平管の冷媒流路に、湿り度の高い冷媒が流れやすくなる。
The refrigerant hole passes through the central portion of the width in the longitudinal direction of the flat pipe, and is wider on the upstream side of the air flow than on the downstream side of the air flow with reference to the central surface parallel to the direction of gravity.
As a result, a highly moist refrigerant is blown out from the inner pipe to the front of the refrigerant flow path of the flat pipe on the upstream side of the air flow having a high heat transfer coefficient, and into the refrigerant flow path of the flat pipe on the upstream side of the air flow. , The highly moist refrigerant easily flows.

蒸発しやすい流路には、湿り度の高い冷媒が、蒸発しにくい空気流れの下流側の扁平管の流路には、外管に滞留しているガス状態(湿り度の低い)冷媒がそれぞれ流れ、各冷媒流路で冷媒が蒸発完了する位置を均一化することができるため、扁平管を有効に利用でき、熱交換器性能を向上することができる。 Highly moist refrigerant is in the flow path that easily evaporates, and gas-state (low moistness) refrigerant staying in the outer pipe is in the flow path of the flat tube on the downstream side of the air flow that is hard to evaporate. Since the position where the refrigerant is completely evaporated can be made uniform in the flow and each refrigerant flow path, the flat tube can be effectively used and the heat exchanger performance can be improved.

第2の発明は、内管の中心軸が、扁平管の長手方向の幅中央部を通り、重力方向と平行な中心面より、空気流れの上流側に偏心しており、冷媒孔と、内管の中心軸と、を結んだ線が、扁平管の冷媒流路の中の冷媒流れ方向と平行となる位置に、冷媒孔を設ける。
これにより、空気流れの上流側の冷媒流路へ向かって、直進するように気液二相冷媒が内管から吹き出され、冷媒流路と冷媒流路とを隔てる壁に衝突し、外管内で冷媒が攪拌されることが抑制されるため、冷媒の流速が速く、攪拌されやすい、高能力運転時においても、空気流れの上流側の冷媒流路へ、内管より吹き出したままの状態の湿り度の高い冷媒が、空気流れの下流側の冷媒流路へ、外管に滞留している状態の湿り度の低い冷媒が流れやすく、各冷媒流路で冷媒が蒸発完了する位置を均一化することができる。
In the second invention, the central axis of the inner pipe passes through the central portion of the width in the longitudinal direction of the flat pipe and is eccentric to the upstream side of the air flow from the central plane parallel to the direction of gravity. A refrigerant hole is provided at a position where the line connecting the central axis of the above is parallel to the direction of the refrigerant flow in the refrigerant flow path of the flat pipe.
As a result, the gas-liquid two-phase refrigerant is blown out from the inner pipe so as to go straight toward the refrigerant flow path on the upstream side of the air flow, collides with the wall separating the refrigerant flow path and the refrigerant flow path, and inside the outer pipe. Since the refrigerant is suppressed from being agitated, the flow velocity of the refrigerant is fast and it is easy to be agitated. Even during high-capacity operation, the dampness remains blown out from the inner pipe to the refrigerant flow path on the upstream side of the air flow. It is easy for the low-humidity refrigerant that is staying in the outer pipe to flow into the refrigerant flow path on the downstream side of the air flow, and the position where the refrigerant completes evaporation is made uniform in each refrigerant flow path. be able to.

また、冷媒流路と冷媒流路とを隔てる壁に衝突し、流動抵抗となることが抑制されるため、吹き出された冷媒を、冷媒流路内にスムーズに流すことにより、外管の中の下側に液冷媒が残留することを抑制でき、重力方向の気液分布の不均一化を防止し、各扁平管へ流れる冷媒状態を均一化することができる。 Further, since it is suppressed that the refrigerant collides with the wall separating the refrigerant flow path and the refrigerant flow path and becomes a flow resistance, the blown-out refrigerant is smoothly flowed into the refrigerant flow path in the outer pipe. It is possible to suppress the residual liquid refrigerant on the lower side, prevent non-uniformity of the gas-liquid distribution in the direction of gravity, and make the state of the refrigerant flowing to each flat pipe uniform.

また、冷媒が蒸発し、一緒に循環している冷凍機油が残留しやすい、空気流れの上流側の扁平管の冷媒流路に、湿り度の高い冷媒を流すことで、液冷媒とともに残留した冷凍機油を戻すことができるため、冷凍機油の残留による熱交換の阻害を抑制することができ、熱交換器性能を向上することができる。 In addition, refrigeration that remains together with the liquid refrigerant by flowing a highly moist refrigerant through the refrigerant flow path of the flat pipe on the upstream side of the air flow, where the refrigerant evaporates and the refrigerating machine oil that circulates together tends to remain. Since the machine oil can be returned, the inhibition of heat exchange due to the residual refrigerating machine oil can be suppressed, and the heat exchanger performance can be improved.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって、本発明が限定されるものではない。
(実施の形態1)
図1、図2、図3は、扁平管内の冷媒流れ方向をx方向、空気流れ方向をy方向、重力上向き方向をz方向とした場合に、図1は、本発明の実施の形態1の熱交換器分流器のx−z平面の断面図、図2は、図1のA−A断面図(本発明の実施の形態1の熱交換器分流器のx−y平面の断面図)、図3は、図1のB−B断面図(本発明の実施の形態1のヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図)である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings. The present invention is not limited to this embodiment.
(Embodiment 1)
1, FIG. 2 and FIG. 3 show the embodiment of the present invention in the case where the refrigerant flow direction in the flat pipe is the x direction, the air flow direction is the y direction, and the gravity upward direction is the z direction. A cross-sectional view of the xx plane of the heat exchanger diversion device, FIG. 2 is a cross-sectional view of AA of FIG. 1 (cross-sectional view of the xy plane of the heat exchanger diversion device according to the first embodiment of the present invention). FIG. 3 is a cross-sectional view taken along the line BB of FIG. 1 (a cross-sectional view taken along the yz plane of a flat tube in a heat exchanger using the header pipe according to the first embodiment of the present invention).

図1、図2、図3において、熱交換器10は、複数の扁平管11と、一対のヘッダーパイプ12a、12bと、を備えている。 In FIGS. 1, 2, and 3, the heat exchanger 10 includes a plurality of flat tubes 11 and a pair of header pipes 12a and 12b.

複数の扁平管11は、ヘッダーパイプ12a、12bの軸方向(z方向)に沿って、互いが平行になるように、それぞれ水平方向(x方向)に配置されており、扁平管11内の冷媒流路13は、ヘッダーパイプ12a、12bの内部に連通されている。 The plurality of flat pipes 11 are arranged in the horizontal direction (x direction) along the axial direction (z direction) of the header pipes 12a and 12b so as to be parallel to each other, and the refrigerant in the flat pipe 11 is arranged. The flow path 13 communicates with the inside of the header pipes 12a and 12b.

少なくとも一方のヘッダーパイプ12aは、複数の扁平管11を接続する外管14と、扁平管11へ冷媒を流出する冷媒孔15を扁平管11の接続側の側面に設けた内管16と、で構成された二重管構造であり、例えば、アルミニウムなどの金属材料を押出成型することにより、円筒状に形成されている。 At least one header pipe 12a is formed by an outer pipe 14 connecting a plurality of flat pipes 11 and an inner pipe 16 having a refrigerant hole 15 for discharging a refrigerant to the flat pipe 11 on the side surface of the flat pipe 11 on the connecting side. It has a double-tube structure, and is formed into a cylindrical shape by extrusion-molding a metal material such as aluminum.

また、ヘッダーパイプ12a、12bの一端部には、冷媒配管17a、17bがそれぞれ接続されている。これら各冷媒配管17a、17bは、冷媒の流入口または流出口として機能するように構成されている。 Further, refrigerant pipes 17a and 17b are connected to one end of the header pipes 12a and 12b, respectively. Each of these refrigerant pipes 17a and 17b is configured to function as an inlet or outlet of the refrigerant.

冷媒孔15は、扁平管11に対応するように、内管16の軸方向(z方向)に複数個存在しており、内管16の軸方向(z方向)の同一高さ位置においては、扁平管11の長手方向(y方向)の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側のほうが、空気流れの下流側よりも広くなっている。 A plurality of refrigerant holes 15 exist in the axial direction (z direction) of the inner pipe 16 so as to correspond to the flat pipe 11, and at the same height position in the axial direction (z direction) of the inner pipe 16, the refrigerant holes 15 are present. The upstream side of the air flow is wider than the downstream side of the air flow, passing through the central portion of the width of the flat tube 11 in the longitudinal direction (y direction) and parallel to the central surface parallel to the gravity direction (z direction). There is.

なお、図4は、本発明の実施の形態1の変形例1のヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図、図5は、本発明の実施の形態1の変形例2のヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図、図6は、本発明の実施の形態1の変形例3のヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図である。 FIG. 4 is a cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe of the modification 1 of the first embodiment of the present invention, and FIG. 5 is the cross-sectional view of the first embodiment of the present invention. A cross-sectional view of the yz plane of the flat tube in the heat exchanger using the header pipe of the second modification, FIG. 6 shows the flatness in the heat exchanger using the header pipe of the third modification of the first embodiment of the present invention. It is sectional drawing of the yz plane of a pipe.

冷媒孔15は、図4に示すように、扁平管11の長手方向の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側(−y方向)にずらした位置に設けた丸孔でも、図5に示すように、扁平管11の長手方向の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側(−y方向)が大きく、空気流れの下流側(+y方向)が小さい、非対称な孔でも、図6に示すように、扁平管11の長手方向の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側(−y方向)に多く、空気流れの下流側(+y方向)に少なくなるよう、同じ開口面積の丸孔を複数個設けてもよい。 As shown in FIG. 4, the refrigerant hole 15 passes through the central portion of the width in the longitudinal direction of the flat tube 11, and is on the upstream side (−y direction) of the air flow with reference to the central surface parallel to the gravity direction (z direction). As shown in FIG. 5, even if the round hole is provided at a staggered position, it passes through the central portion of the width of the flat tube 11 in the longitudinal direction and is upstream of the air flow with reference to the central surface parallel to the gravity direction (z direction). As shown in FIG. 6, even an asymmetric hole having a large side (−y direction) and a small downstream side (+ y direction) of the air flow passes through the central portion of the width in the longitudinal direction of the flat tube 11 and passes through the center of the width in the longitudinal direction (z). Even if multiple round holes with the same opening area are provided so that the number is large on the upstream side (-y direction) of the air flow and small on the downstream side (+ y direction) of the air flow with reference to the central surface parallel to the direction). good.

以上のように構成された熱交換器について、蒸発器として機能する場合には、冷媒配管17aからヘッダーパイプ12aの内管16の内部に流入した気液二相冷媒が、複数の冷媒孔15から、外管14の内部に吹き出し、各扁平管11内の各冷媒流路13を介して+x方向に流れ、ヘッダーパイプ12bの内部に送られる。扁平管11内の各冷媒流路13を冷媒が流れる際に、各扁平管11の間を+y方向に流れる空気と熱交換を行う。そして、ヘッダーパイプ12bに送られた冷媒は、冷媒配管17bから流出される。 When the heat exchanger configured as described above functions as an evaporator, the gas-liquid two-phase refrigerant flowing from the refrigerant pipe 17a into the inner pipe 16 of the header pipe 12a flows from the plurality of refrigerant holes 15. , It blows out to the inside of the outer pipe 14, flows in the + x direction through each refrigerant flow path 13 in each flat pipe 11, and is sent to the inside of the header pipe 12b. When the refrigerant flows through each of the refrigerant flow paths 13 in the flat pipe 11, heat exchange is performed with the air flowing in the + y direction between the flat pipes 11. Then, the refrigerant sent to the header pipe 12b flows out from the refrigerant pipe 17b.

内管16からは、熱伝達率が高くなる空気流れの上流側の扁平管11の冷媒流路13の手前へ、湿り度の高い冷媒を吹き出しやすくなるため、空気流れの上流側の扁平管11の冷媒流路13に、湿り度の高い冷媒が流れやすくなる。 Since it becomes easy to blow out a highly moist refrigerant from the inner pipe 16 to the front of the refrigerant flow path 13 of the flat pipe 11 on the upstream side of the air flow having a high heat transfer coefficient, the flat pipe 11 on the upstream side of the air flow A highly moist refrigerant easily flows through the refrigerant flow path 13.

なお、冷媒としては、例えば、R410A、R32およびR32を含む混合冷媒などが用いられる。 As the refrigerant, for example, a mixed refrigerant containing R410A, R32 and R32 is used.

次に、本実施形態の利用について、本実施形態の熱交換器10を空気調和装置の室外機20に利用した場合を例に説明する。 Next, the use of the present embodiment will be described by taking as an example the case where the heat exchanger 10 of the present embodiment is used for the outdoor unit 20 of the air conditioner.

図7は、本実施形態の熱交換器10を適用した室外機20の内部構造を示すx−y平面図であり、図8は、本実施形態の熱交換器10を適用した室外機20の内部構造を示すx−z平面図である。 FIG. 7 is a xy plan view showing the internal structure of the outdoor unit 20 to which the heat exchanger 10 of the present embodiment is applied, and FIG. 8 is a plan view of the outdoor unit 20 to which the heat exchanger 10 of the present embodiment is applied. It is an xz plan view which shows the internal structure.

図7、図8に示すように、室外機20は、圧縮機21と、切替弁22と、室外膨張弁23と、送風機24と、熱交換器10を備えている。室外機20と室内機(図示せず)は、液管25と、ガス管26とで接続している。 As shown in FIGS. 7 and 8, the outdoor unit 20 includes a compressor 21, a switching valve 22, an outdoor expansion valve 23, a blower 24, and a heat exchanger 10. The outdoor unit 20 and the indoor unit (not shown) are connected by a liquid pipe 25 and a gas pipe 26.

熱交換器10は、空気流れ方向(y方向)に2つ設置しており、空気流れの上流側に設置している熱交換器10の一方のヘッダーパイプ12aは二重管構造であり、冷媒配管17aを介して、室外膨張弁23と接続しており、空気流れの下流側に設置している熱交換器30の一方のヘッダーパイプ32aは、冷媒配管37aを介して、切替弁22と接続している。 Two heat exchangers 10 are installed in the air flow direction (y direction), and one header pipe 12a of the heat exchanger 10 installed on the upstream side of the air flow has a double pipe structure and has a refrigerant. One header pipe 32a of the heat exchanger 30, which is connected to the outdoor expansion valve 23 via the pipe 17a and is installed on the downstream side of the air flow, is connected to the switching valve 22 via the refrigerant pipe 37a. is doing.

熱交換器10の他方のヘッダーパイプ12bと、熱交換器30の他方のヘッダーパイプ32bと、は冷媒配管17b、37bで接続している。
まず、冷房運転を行う場合は、熱交換器10は凝縮器として機能する。
The other header pipe 12b of the heat exchanger 10 and the other header pipe 32b of the heat exchanger 30 are connected by refrigerant pipes 17b and 37b.
First, when the cooling operation is performed, the heat exchanger 10 functions as a condenser.

室外機20の圧縮機21から送られるガス冷媒は、切替弁22を介して、冷媒配管37aから、ヘッダーパイプ32aの中に流入される。このガス冷媒は、ヘッダーパイプ32aの内部を通り、複数の扁平管31内の冷媒流路33に流入され、水平方向(+x方向)に流れ、ヘッダーパイプ32bに流出する。ヘッダーパイプ32bに流出した冷媒は、冷媒配管17b、37bを介して、ヘッダーパイプ12bの内部を通り、複数の扁平管11の冷媒流路13に流入され、水平方向(−x方向)に流れる。冷媒は、扁平管11、31において、送風機24により送られた空気と熱交換をすることで放熱して凝縮される。 The gas refrigerant sent from the compressor 21 of the outdoor unit 20 flows into the header pipe 32a from the refrigerant pipe 37a via the switching valve 22. This gas refrigerant passes through the inside of the header pipe 32a, flows into the refrigerant flow paths 33 in the plurality of flat pipes 31, flows in the horizontal direction (+ x direction), and flows out to the header pipe 32b. The refrigerant flowing out to the header pipe 32b passes through the inside of the header pipe 12b via the refrigerant pipes 17b and 37b, flows into the refrigerant flow paths 13 of the plurality of flat pipes 11, and flows in the horizontal direction (−x direction). The refrigerant dissipates heat and is condensed in the flat tubes 11 and 31 by exchanging heat with the air sent by the blower 24.

凝縮した冷媒は、二重管構造であるヘッダーパイプ12aの外管14から、冷媒孔15を通り、内管16に流入し、冷媒配管17aから室外膨張弁23、液管25を通り、室内機に流出される。 The condensed refrigerant flows from the outer pipe 14 of the header pipe 12a having a double pipe structure through the refrigerant hole 15 and into the inner pipe 16, passes through the outdoor expansion valve 23 and the liquid pipe 25 from the refrigerant pipe 17a, and is an indoor unit. Is leaked to.

室内機に流れた凝縮した冷媒は、室内熱交換器(図示せず)で空気と熱交換をすることで吸熱し蒸発する。蒸発した冷媒は、ガス管26を通り、切替弁22を介して、圧縮機21に循環する。暖房運転を行う場合は、熱交換器10は蒸発器として機能する。 The condensed refrigerant flowing into the indoor unit absorbs heat and evaporates by exchanging heat with air in an indoor heat exchanger (not shown). The evaporated refrigerant passes through the gas pipe 26 and circulates to the compressor 21 via the switching valve 22. When performing a heating operation, the heat exchanger 10 functions as an evaporator.

室外機20の圧縮機21から送られるガス冷媒は、切替弁22を介して、ガス管26を通り、室内機に流出される。室内機に流れたガス冷媒は、室内機に設けられた室内熱交換器で空気と熱交換をすることで放熱し凝縮する。凝縮した冷媒は、液管25、室外膨張弁23を通り、気液二相冷媒となり、冷媒配管17aから、二重管構造であるヘッダーパイプ12aの内管16に流入される。 The gas refrigerant sent from the compressor 21 of the outdoor unit 20 passes through the gas pipe 26 via the switching valve 22 and flows out to the indoor unit. The gas refrigerant flowing into the indoor unit dissipates heat and condenses by exchanging heat with air in the indoor heat exchanger provided in the indoor unit. The condensed refrigerant passes through the liquid pipe 25 and the outdoor expansion valve 23 to become a gas-liquid two-phase refrigerant, and flows from the refrigerant pipe 17a into the inner pipe 16 of the header pipe 12a having a double pipe structure.

気液二相冷媒は、ヘッダーパイプ12aの内管16の冷媒孔15を通り、複数の扁平管11内の冷媒流路13に流入され、水平方向(+x方向)に流れ、ヘッダーパイプ12bに流出する。ヘッダーパイプ12bに流出した冷媒は、冷媒配管17b、37bを介して、ヘッダーパイプ32bの内部を通り、複数の扁平管31の冷媒流路33に流入され、水平方向(−x方向)に流れる。冷媒は、扁平管11、31において、送風機24により送られた空気と熱交換をすることで吸熱して蒸発される。 The gas-liquid two-phase refrigerant passes through the refrigerant holes 15 of the inner pipe 16 of the header pipe 12a, flows into the refrigerant flow paths 13 in the plurality of flat pipes 11, flows in the horizontal direction (+ x direction), and flows out to the header pipe 12b. do. The refrigerant flowing out to the header pipe 12b passes through the inside of the header pipe 32b via the refrigerant pipes 17b and 37b, flows into the refrigerant flow paths 33 of the plurality of flat pipes 31, and flows in the horizontal direction (−x direction). The refrigerant absorbs heat and evaporates in the flat tubes 11 and 31 by exchanging heat with the air sent by the blower 24.

蒸発した冷媒は、ヘッダーパイプ32aに流入し、内部を通り、冷媒配管37aから切替弁22を介して、圧縮機21に循環する。 The evaporated refrigerant flows into the header pipe 32a, passes through the inside, and circulates from the refrigerant pipe 37a to the compressor 21 via the switching valve 22.

蒸発器として機能する場合、ヘッダーパイプ12aの内管16には気液二相冷媒が流れ、冷媒孔15からは、気液二相冷媒が吹き出すことになる。冷媒孔15より吹き出した気液二相冷媒の内、密度の大きい液冷媒は慣性力が大きく、直進しやすく、液冷媒より軽いガス冷媒は拡散しやすいため、冷媒孔15近傍の空間には、湿り度の高い(液濃度の高い
)冷媒が存在し、冷媒孔15近傍の扁平管11の冷媒流路13を介して湿り度の高い冷媒が流れ、冷媒孔15から離れた空間においては液濃度が低くなり、湿り度の低い(ガス濃度の高い)冷媒が存在し、冷媒孔15遠方の扁平管11の冷媒流路13を介して湿り度の低い冷媒が流れる。
When functioning as an evaporator, a gas-liquid two-phase refrigerant flows through the inner pipe 16 of the header pipe 12a, and a gas-liquid two-phase refrigerant is blown out from the refrigerant hole 15. Of the gas-liquid two-phase refrigerant blown out from the refrigerant hole 15, the liquid refrigerant having a high density has a large inertial force and easily goes straight, and the gas refrigerant lighter than the liquid refrigerant easily diffuses. There is a highly moist (high liquid concentration) refrigerant, and the highly moist refrigerant flows through the refrigerant flow path 13 of the flat tube 11 near the refrigerant hole 15, and the liquid concentration in the space away from the refrigerant hole 15. There is a refrigerant having a low degree of wetness (high gas concentration), and the refrigerant having a low degree of wetness flows through the refrigerant flow path 13 of the flat tube 11 far from the refrigerant hole 15.

冷媒孔15は、扁平管11の長手方向(y方向)の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側のほうが、空気流れの下流側よりも広いため、空気流れの上流側の扁平管11の冷媒流路13の手前へ、湿り度の高い冷媒を吹き出しやすく、空気流れの上流側の扁平管11の冷媒流路13に、湿り度の高い冷媒がより流れやすくなり、空気流れの下流側の扁平管11の冷媒流路13に、湿り度の低い冷媒がより流れやすくなる。 The refrigerant hole 15 passes through the central portion of the width of the flat tube 11 in the longitudinal direction (y direction), and the upstream side of the air flow is the downstream side of the air flow with reference to the central surface parallel to the gravity direction (z direction). Because it is wider than the above, it is easy to blow out a highly moist refrigerant to the front of the refrigerant flow path 13 of the flat tube 11 on the upstream side of the air flow, and the degree of wetness to the refrigerant flow path 13 of the flat tube 11 on the upstream side of the air flow. Higher refrigerant flows more easily, and less wet refrigerant flows more easily into the refrigerant flow path 13 of the flat tube 11 on the downstream side of the air flow.

以上のように、本実施の形態において、熱交換器10は、複数の冷媒流路13を有する扁平管11と、複数の扁平管11を水平方向に設置し、扁平管11の両端部をそれぞれ接続する一対のヘッダーパイプ12と、を備え、複数の扁平管11を、ヘッダーパイプ12の軸方向に沿って、互いに平行に接続される。 As described above, in the present embodiment, in the heat exchanger 10, a flat pipe 11 having a plurality of refrigerant flow paths 13 and a plurality of flat pipes 11 are installed in the horizontal direction, and both ends of the flat pipe 11 are respectively installed. A pair of header pipes 12 to be connected are provided, and a plurality of flat pipes 11 are connected in parallel to each other along the axial direction of the header pipe 12.

少なくとも一方のヘッダーパイプ12aを、複数の扁平管11を接続する外管14と、扁平管へ冷媒を流出する複数の冷媒孔15を、扁平管の接続側の側面に設けた内管16と、で構成された二重管構造し、冷媒孔15は、扁平管11の長手方向(y方向)の幅中央部を通り、重力方向(z方向)と平行な中心面を基準に、空気流れの上流側のほうが、空気流れの下流側よりも広くする。 At least one header pipe 12a is provided with an outer pipe 14 for connecting a plurality of flat pipes 11, and an inner pipe 16 having a plurality of refrigerant holes 15 for discharging refrigerant to the flat pipes on the side surfaces of the flat pipes on the connecting side. The refrigerant hole 15 has a double pipe structure composed of, passes through the central portion of the width of the flat pipe 11 in the longitudinal direction (y direction), and has an air flow with reference to a central surface parallel to the gravity direction (z direction). The upstream side is wider than the downstream side of the air flow.

これにより、熱伝達率が高くなる空気流れの上流側の扁平管11の冷媒流路13の手前へ、内管16から湿り度の高い冷媒を吹き出しやすくなるため、空気流れの上流側の扁平管11の冷媒流路13に、湿り度の高い冷媒が流れやすくなる。蒸発しやすい流路には湿り度の高い冷媒が、蒸発しにくい空気流れの下流側の扁平管の流路には、外管14に滞留している湿り度の低い冷媒が流れることで、各冷媒流路13で冷媒が蒸発完了する位置を均一化することができるため、扁平管11を有効に利用でき、熱交換器性能を向上することができる。 As a result, it becomes easy to blow out a highly moist refrigerant from the inner pipe 16 to the front of the refrigerant flow path 13 of the flat pipe 11 on the upstream side of the air flow having a high heat transfer coefficient, so that the flat pipe on the upstream side of the air flow can be easily blown out. A highly moist refrigerant easily flows through the refrigerant flow path 13 of 11. Highly moist refrigerant flows through the flow path that easily evaporates, and low-humidity refrigerant that stays in the outer pipe 14 flows through the flow path of the flat pipe on the downstream side of the air flow that does not easily evaporate. Since the position where the refrigerant completes evaporation can be made uniform in the refrigerant flow path 13, the flat tube 11 can be effectively used and the heat exchanger performance can be improved.

なお、実施例では、熱交換器10を空気流れ方向(y方向)に2つ設置しているが、例えば、1つでも、3つ以上でもよく、状況に応じて、ヘッダーパイプ12内に仕切板を設け、一方のヘッダーパイプ12aの重力方向(z方向)下側が二重管構造、重力方向(z方向)上側が単管となるような構成で、冷媒配管17a、17bの両方を一方のヘッダーパイプ12aに接続したり、また、重力方向(z方向)に2つの熱交換器10を重ねた構成を用いた場合でも、同様の効果を得られることは言うまでもない。
(実施の形態2)
図9は、本発明の実施の形態2におけるヘッダーパイプのx−y平面の断面図であり、図10は、本発明の実施の形態2のヘッダーパイプを用いた熱交換器における扁平管のy−z平面の断面図である。
In the embodiment, two heat exchangers 10 are installed in the air flow direction (y direction), but for example, one or three or more heat exchangers 10 may be installed, and a partition may be provided in the header pipe 12 depending on the situation. A plate is provided, and one header pipe 12a has a double pipe structure on the lower side in the gravity direction (z direction) and a single pipe on the upper side in the gravity direction (z direction). Needless to say, the same effect can be obtained even when connected to the header pipe 12a or when two heat exchangers 10 are stacked in the gravity direction (z direction).
(Embodiment 2)
FIG. 9 is a cross-sectional view of the xy plane of the header pipe according to the second embodiment of the present invention, and FIG. 10 shows the y of the flat tube in the heat exchanger using the header pipe according to the second embodiment of the present invention. It is sectional drawing of the −z plane.

図9、図10に示すように、内管16の中心軸Cは、扁平管11の長手方向の幅中央部を通り、重力方向(z方向)と平行な中心面より、空気流れの上流側に偏心しており、冷媒孔15と、内管16の中心軸Cと、を結んだ線が、扁平管11の冷媒流路13の流れ方向(x方向)と平行となるように、冷媒孔15を設けたものである。 As shown in FIGS. 9 and 10, the central axis C of the inner pipe 16 passes through the central portion of the width in the longitudinal direction of the flat pipe 11 and is on the upstream side of the air flow from the central plane parallel to the gravity direction (z direction). The refrigerant hole 15 is eccentric so that the line connecting the refrigerant hole 15 and the central axis C of the inner pipe 16 is parallel to the flow direction (x direction) of the refrigerant flow path 13 of the flat pipe 11. Is provided.

これにより、冷媒孔15より、空気流れの上流側の冷媒流路13へ向かって直進するように気液二相冷媒が吹き出され、冷媒が冷媒流路13と冷媒流路13とを隔てる壁に衝突し、冷媒が攪拌されることが抑制されるため、冷媒の流速が速く、攪拌されやすい、高能
力運転時においても、空気流れの上流側の冷媒流路13へ、内管16より吹き出したままの状態の湿り度の高い冷媒が、空気流れの下流側の冷媒流路13へ、外管14に滞留している状態の湿り度の低い冷媒が流れやすく、各冷媒流路13で冷媒が蒸発完了する位置を均一化することができる。
As a result, the gas-liquid two-phase refrigerant is blown out from the refrigerant hole 15 so as to go straight toward the refrigerant flow path 13 on the upstream side of the air flow, and the refrigerant reaches the wall separating the refrigerant flow path 13 and the refrigerant flow path 13. Since collision is suppressed and the refrigerant is agitated, the flow velocity of the refrigerant is high and the refrigerant is easily agitated. Even during high-capacity operation, the refrigerant is blown out from the inner pipe 16 to the refrigerant flow path 13 on the upstream side of the air flow. The highly moist refrigerant in the as-is state easily flows to the refrigerant flow path 13 on the downstream side of the air flow, and the low-humidity refrigerant staying in the outer pipe 14 easily flows, and the refrigerant flows in each refrigerant flow path 13. The position where the evaporation is completed can be made uniform.

また、冷媒が冷媒流路13と冷媒流路13とを隔てる壁に衝突し、流動抵抗となることが抑制されるため、吹き出した気液二相冷媒が冷媒流路13内にスムーズに流れ、外管14の中の下側に液冷媒が残留することで重力方向(z方向)の気液分布が不均一となることを防止でき、各扁平管11へ流れる冷媒の状態を均一化することができる。 Further, since it is suppressed that the refrigerant collides with the wall separating the refrigerant flow path 13 and the refrigerant flow path 13 and becomes a flow resistance, the blown-out gas-liquid two-phase refrigerant smoothly flows into the refrigerant flow path 13. It is possible to prevent the gas-liquid distribution in the gravity direction (z direction) from becoming uneven due to the liquid refrigerant remaining on the lower side inside the outer pipe 14, and to make the state of the refrigerant flowing to each flat pipe 11 uniform. Can be done.

また、冷媒が蒸発し、一緒に循環している冷凍機油が残留しやすい、空気流れの上流側の扁平管11の冷媒流路13に、湿り度の高い冷媒を流すことで、液冷媒とともに残留した冷凍機油を戻すことができるため、冷凍機油の残留による熱交換の阻害を抑制することができ、熱交換器性能を向上することができる。 Further, by flowing a highly moist refrigerant through the refrigerant flow path 13 of the flat pipe 11 on the upstream side of the air flow, where the refrigerant evaporates and the refrigerating machine oil circulating together tends to remain, it remains together with the liquid refrigerant. Since the refined refrigerating machine oil can be returned, the inhibition of heat exchange due to the residual refrigerating machine oil can be suppressed, and the heat exchanger performance can be improved.

なお、内管16に設けた冷媒孔15は、内管16の中心軸Cと、扁平管11の長手方向(y方向)の幅の一端と、を結んだ線と交わる内管16の側面上の点Dと、内管16の中心軸Cと、扁平管11の長手方向(y方向)の幅の他端と、を結んだ線と交わる内管16の側面上の点Eと、の扁平管11の接続側の間の側面上に位置するように設けるのがよい。 The refrigerant hole 15 provided in the inner pipe 16 is on the side surface of the inner pipe 16 that intersects the line connecting the central axis C of the inner pipe 16 and one end of the width in the longitudinal direction (y direction) of the flat pipe 11. Flatness of the point D, the central axis C of the inner pipe 16, and the other end of the width of the flat pipe 11 in the longitudinal direction (y direction), and the point E on the side surface of the inner pipe 16 intersecting the line connecting the points D. It is preferable to provide it so as to be located on the side surface between the connecting sides of the pipe 11.

これにより、内管16から、扁平管11に向かって冷媒が吹き出される。冷媒が外管14に衝突し、流動抵抗となり、冷媒流路13に冷媒が流れにくくなり、外管14の中に液冷媒が残留することが抑制されるため、重力方向(z方向)の気液分布が不均一となることを防止でき、各扁平管11へ流れる冷媒の状態をさらに均一化することができる。 As a result, the refrigerant is blown from the inner pipe 16 toward the flat pipe 11. The refrigerant collides with the outer pipe 14, becomes a flow resistance, makes it difficult for the refrigerant to flow into the refrigerant flow path 13, and suppresses the liquid refrigerant from remaining in the outer pipe 14, so that the air in the gravity direction (z direction) It is possible to prevent the liquid distribution from becoming non-uniform, and it is possible to further make the state of the refrigerant flowing through each flat tube 11 more uniform.

本発明は、扁平管利用の熱交換器において、複数の冷媒流路毎に冷媒の状態が異なって流れることを抑制し、各冷媒流路で冷媒が蒸発完了する位置を均一化することができる熱交換器分流器であり、冷凍機、空気調和装置、給湯空調複合装置などの用途に適用できる。 According to the present invention, in a heat exchanger using a flat tube, it is possible to suppress the flow of different refrigerant states in each of a plurality of refrigerant flow paths, and to make the position where the refrigerant completes evaporation in each refrigerant flow path uniform. It is a heat exchanger / refrigerant, and can be applied to applications such as refrigerators, air conditioners, and hot water supply / air conditioning combined devices.

1 熱交換器
2 冷媒流路
3 扁平管
4 ヘッダーパイプ
5 外管
6 冷媒孔
7 内管
10、30 熱交換器
11、31 扁平管
12、32 ヘッダーパイプ
13、33 冷媒流路
14 外管
15 冷媒孔
16 内管
17、37 冷媒配管
20 室外機
21 圧縮機
22 切替弁
23 室外膨張弁
24 送風機
25 液管
26 ガス管
1 Heat exchanger 2 Coolant flow path 3 Flat pipe 4 Header pipe 5 Outer pipe 6 Refrigerator hole 7 Inner pipe 10, 30 Heat exchanger 11, 31 Flat pipe 12, 32 Header pipe 13, 33 Coolant flow path 14 Outer pipe 15 Refrigerator Hole 16 Inner pipe 17, 37 Coolant pipe 20 Outdoor unit 21 Compressor 22 Switching valve 23 Outdoor expansion valve 24 Blower 25 Liquid pipe 26 Gas pipe

Claims (3)

複数の冷媒流路を有する扁平管と、
前記扁平管の両端部をそれぞれ接続する一対のヘッダーパイプと、
を備えた熱交換器において、少なくとも一方の前記ヘッダーパイプを、複数の前記扁平管を接続する外管と、
前記扁平管へ冷媒を流出する冷媒孔を、前記扁平管の接続方向の側面に設けた内管と、で構成された二重管構造とし、
前記内管の中心軸が、前記扁平管の長手方向の幅中央部を通り、重力方向と平行な中心面より、空気流れの上流側に偏心することを特徴とする熱交換器分流器。
A flat tube with multiple refrigerant channels and
A pair of header pipes connecting both ends of the flat pipe,
In a heat exchanger provided with, at least one of the header pipes is attached to an outer pipe connecting a plurality of the flat pipes.
The cold Nakadachiana you outflow refrigerant into the flat tube, and the inner tube is provided on the side of the connection direction of the flat tube, in a configured double-pipe structure,
A heat exchanger shunt characterized in that the central axis of the inner pipe passes through the central portion of the width in the longitudinal direction of the flat pipe and is eccentric to the upstream side of the air flow from the central surface parallel to the direction of gravity.
前記冷媒孔と、前記内管の中心軸と、を結んだ線が、前記扁平管の前記冷媒流路の流れ方向と平行となるように、冷媒孔を設けることを特徴とする請求項1に記載の熱交換器分流器。 The first aspect of claim 1 is characterized in that the refrigerant hole is provided so that the line connecting the refrigerant hole and the central axis of the inner pipe is parallel to the flow direction of the refrigerant flow path of the flat pipe. The heat exchanger shunt described. 前記内管の中心軸と、前記扁平管の長手方向の幅の一端と、を結んだ線と交わる内管の側面上の点と、前記内管の中心軸と、前記扁平管の長手方向の幅の他端と、を結んだ線と交わる内管の側面上の点と、の扁平管の接続側の間の側面上に位置するように、前記冷媒孔を設けることを特徴とする請求項1に記載の熱交換器分流器。A point on the side surface of the inner tube that intersects the line connecting the central axis of the inner tube and one end of the width in the longitudinal direction of the flat tube, the central axis of the inner tube, and the longitudinal direction of the flat tube. The claim is characterized in that the refrigerant hole is provided so as to be located on the side surface between the other end of the width and the point on the side surface of the inner pipe that intersects the line connecting the flat pipes. The heat exchanger diversion device according to 1.
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