JP4688538B2

JP4688538B2 - Heat exchanger

Info

Publication number: JP4688538B2
Application number: JP2005094698A
Authority: JP
Inventors: 健栗原; 武司桑原; 圭児古賀; 昌宏大下; 加寿紀北; 功典青野; 達也岩崎; 隆雄森本; 博志山口; 浩濱本
Original assignee: Japan Climate Systems Corp
Current assignee: Japan Climate Systems Corp
Priority date: 2005-03-29
Filing date: 2005-03-29
Publication date: 2011-05-25
Anticipated expiration: 2025-03-29
Also published as: JP2006275402A

Description

本発明は、一対の成形プレートを重ねて接合することにより形成された複数の伝熱部材が伝熱フィンを介して積層された熱交換器に関する。 The present invention relates to a heat exchanger in which a plurality of heat transfer members formed by stacking and joining a pair of molded plates are stacked via heat transfer fins.

従来より、例えば、特許文献１に開示されているように、車両用空調装置に用いられる蒸発器等の熱交換器として、一対の成形プレートを重ねて接合することにより形成された複数の伝熱部材と伝熱フィンとを備えたものが知られている。各成形プレートの風上側には、熱交換媒体としての冷媒が流れる冷媒通路を構成する風上側通路構成部と、該冷媒通路の一端部に連通する一側タンクを構成する風上側タンク構成部とが成形されている。各成形プレートの風下側にも冷媒通路を構成する風下側通路構成部と風下側タンク構成部とが成形されている。上記成形プレートの通路構成部には、冷媒通路内へ膨出する膨出部が互いに間隔をあけて多数設けられている。上記風上側の冷媒通路の他端部と風下側の冷媒通路の他端部とは伝熱部材内で連通している。 Conventionally, for example, as disclosed in Patent Document 1, as a heat exchanger such as an evaporator used in a vehicle air conditioner, a plurality of heat transfer formed by overlapping and joining a pair of molded plates The thing provided with the member and the heat-transfer fin is known. On the windward side of each forming plate, an windward side passage constituting part that constitutes a refrigerant passage through which a refrigerant as a heat exchange medium flows, and an upside tank constituting part that constitutes a one-side tank that communicates with one end of the refrigerant path, Is molded. A leeward side passage constituting portion and a leeward side tank constituting portion constituting a refrigerant passage are also formed on the leeward side of each forming plate. A large number of bulging portions that bulge into the refrigerant passage are provided at intervals in the passage constituting portion of the molding plate. The other end portion of the leeward refrigerant passage communicates with the other end portion of the leeward refrigerant passage in the heat transfer member.

上記伝熱部材は伝熱フィンを介して積層されており、この積層方向に隣接する伝熱部材の一側タンク構成部により風上側と風下側とに一側タンクがそれぞれ形成されるようになっている。そして、例えば高圧の冷媒を膨張弁により減圧してから風下側の一側タンクに導入させると、この冷媒は、該一側タンクから風下側の冷媒通路を通って風上側の冷媒通路に流入し、該冷媒通路を通って風上側の一側タンクに流入し、該一側タンクから熱交換器の外部に導出される。この冷媒通路を流れる冷媒の流れは膨出部によって乱される。これにより、冷媒通路内の冷媒を略均一に外部空気と熱交換させることが可能になって、熱交換効率が高まる。
特開平５−１４９６５１号公報 The heat transfer members are stacked via heat transfer fins, and one side tanks are respectively formed on the leeward side and the leeward side by the one side tank components of the heat transfer members adjacent in the stacking direction. ing. For example, when the high-pressure refrigerant is decompressed by the expansion valve and then introduced into the leeward side one tank, the refrigerant flows from the one side tank through the leeward side refrigerant passage into the leeward side refrigerant passage. Then, the refrigerant flows into the one side tank on the windward side through the refrigerant passage, and is led out of the heat exchanger from the one side tank. The flow of the refrigerant flowing through the refrigerant passage is disturbed by the bulging portion. This makes it possible to exchange heat between the refrigerant in the refrigerant passage and the outside air substantially uniformly, and the heat exchange efficiency is increased.
JP-A-5-149651

ところが、特許文献１の熱交換器のように一側タンク内に導入された冷媒を冷媒通路に流入し又は冷媒通路を流れた冷媒を一側タンクに流入させるようにした場合には、一側タンクの断面形状と冷媒通路の断面形状とが大きく異なることや、一側タンク内の冷媒の流れ方向と冷媒通路内の冷媒の流れ方向とが異なること等により、一側タンクと冷媒通路との境界部分近傍で冷媒に乱流が発生する。その上、特許文献１では、冷媒通路に膨出する膨出部を設けて冷媒の流れを積極的に乱すことにより熱交換効率の向上を図っているため、この膨出部の影響が上記一側タンクと冷媒通路との境界近傍にも及んで、該境界近傍で冷媒の乱流が大きく成長し易い。このように冷媒の乱流が大きく成長すると、冷媒の流動音が大きくなって熱交換器の外部に騒音として漏れるので、車両の乗員に違和感を与えてしまう。 However, when the refrigerant introduced into the one-side tank flows into the refrigerant passage or the refrigerant that has flowed through the refrigerant passage flows into the one-side tank as in the heat exchanger of Patent Document 1, Due to the fact that the cross-sectional shape of the tank and the cross-sectional shape of the refrigerant passage are significantly different, the flow direction of the refrigerant in the one-side tank is different from the flow direction of the refrigerant in the refrigerant passage, etc. Turbulent flow is generated in the refrigerant near the boundary. In addition, in Patent Document 1, since the bulging portion that bulges in the refrigerant passage is provided to improve the heat exchange efficiency by actively disturbing the flow of the refrigerant, the influence of the bulging portion is the same as that described above. The turbulent flow of the refrigerant tends to grow greatly near the boundary between the side tank and the refrigerant passage. When the turbulent flow of the refrigerant grows greatly in this way, the flow noise of the refrigerant increases and leaks as noise to the outside of the heat exchanger, which makes the vehicle occupant feel uncomfortable.

本発明は斯かる点に鑑みてなされたものであり、その目的とするところは、媒体通路を流れる熱交換媒体の流れを積極的に乱して外部空気との熱交換効率を高くしながら、媒体通路とタンクとの境界部分近傍では熱交換媒体の乱流が大きく成長するのを抑制し、熱交換媒体の流動音による騒音を小さくすることにある。 The present invention has been made in view of such points, and the object of the present invention is to positively disturb the flow of the heat exchange medium flowing through the medium passage and increase the heat exchange efficiency with external air, In the vicinity of the boundary between the medium passage and the tank, the turbulent flow of the heat exchange medium is prevented from growing greatly, and noise due to the flow noise of the heat exchange medium is reduced.

上記目的を達成するために、本発明では、媒体通路を流れる熱交換媒体の流れをタンクの近傍で整流させるようにした。 In order to achieve the above object, in the present invention, the flow of the heat exchange medium flowing through the medium passage is rectified in the vicinity of the tank.

具体的には、請求項１の発明では、熱交換媒体が流れる上下方向に延びる媒体通路を構成する通路構成部及び該媒体通路の上下方向一端部に連通する一側タンクを構成する一側タンク構成部が成形された一対の成形プレートを重ねて接合してなる伝熱部材と、伝熱フィンとを備え、上記伝熱部材が伝熱フィンを介して複数積層され、上記一側タンク内に導入された熱交換媒体が上記媒体通路に流入し又は上記媒体通路を流れた熱交換媒体が上記一側タンクに流入するように構成された熱交換器を対象とする。 Specifically, in the first aspect of the present invention, the one-side tank constituting the one-side tank that communicates with the passage-constituting portion that constitutes the vertically extending medium passage through which the heat exchange medium flows and the one- upward end portion of the medium passage. A heat transfer member formed by stacking and joining a pair of molded plates formed with components and heat transfer fins, and a plurality of the heat transfer members are stacked via the heat transfer fins, A heat exchanger configured such that the introduced heat exchange medium flows into the medium passage or the heat exchange medium flowing through the medium passage flows into the one-side tank is an object.

そして、上記成形プレートの通路構成部には、熱交換媒体の流れ方向中間部に、媒体通路内を流れる熱交換媒体の流れを乱す乱流形成部が該媒体通路内へ膨出するように設けられ、上記一側タンク構成部から他側へ延び、上記媒体通路内を流れる熱交換媒体の流れを整流する整流部が設けられ、上記整流部の長手方向他側は、直線状に延びており、上記整流部の長手方向一側の幅方向の寸法は、上記一側タンク構成部に近づくほど長くなるように設定されて上記媒体通路が絞られている構成とする。 Further, a turbulent flow forming portion that disturbs the flow of the heat exchange medium flowing in the medium passage is provided in the intermediate portion in the flow direction of the heat exchange medium in the passage constituting portion of the forming plate so as to bulge into the medium passage. And a rectifying unit that rectifies the flow of the heat exchange medium flowing in the medium passage from the one side tank component to the other side, and the other side in the longitudinal direction of the rectifying unit extends linearly. The size in the width direction on one side in the longitudinal direction of the rectifying unit is set so as to become longer as it approaches the one-side tank component, and the medium passage is narrowed .

この構成によれば、媒体通路における熱交換媒体の流れ方向上流端に一側タンクを連通させた場合には、該一側タンクに導入された熱交換媒体が媒体通路に流入して該媒体通路を流れる。熱交換媒体が媒体通路を流れるときには、該媒体通路の流れ方向中間部に設けられた乱流形成部により熱交換媒体に乱流が形成される。これにより、媒体通路内の熱交換媒体を外部空気と略均一に熱交換させることが可能になる。一方、一側タンクから媒体通路に流入する熱交換媒体は、整流部により整流されるので、上記乱流形成部の影響が媒体通路と一側タンクとの境界近傍に及ぶのを抑制して、該境界近傍で熱交換媒体の乱流が大きく成長するのを抑制することが可能になる。 According to this configuration, when the one-side tank is communicated with the upstream end of the heat exchange medium in the medium passage, the heat exchange medium introduced into the one-side tank flows into the medium passage and the medium passage Flowing. When the heat exchange medium flows through the medium passage, a turbulent flow is formed in the heat exchange medium by the turbulent flow forming portion provided at the intermediate portion in the flow direction of the medium passage. As a result, the heat exchange medium in the medium passage can be substantially uniformly heat exchanged with the external air. On the other hand, since the heat exchange medium flowing into the medium passage from the one side tank is rectified by the rectification unit, the influence of the turbulent flow forming unit is suppressed from reaching near the boundary between the medium passage and the one side tank, It becomes possible to suppress the turbulent flow of the heat exchange medium from growing greatly in the vicinity of the boundary.

また、媒体通路における熱交換媒体の流れ方向下流端に一側タンクを連通させた場合には、媒体通路を流れた熱交換媒体が一側タンクに流入する。熱交換媒体が媒体通路を流れるときには、乱流形成部により媒体通路内の熱交換媒体を外部空気と略均一に熱交換させることが可能になる。一方、媒体通路から一側タンクに流入する前の熱交換媒体の流れは整流部により整流される。これにより、一側タンクと媒体通路との境界部分近傍で熱交換媒体の乱流が大きく成長するのを抑制することが可能になる。 Further, when the one-side tank is communicated with the downstream end of the medium passage in the flow direction of the heat exchange medium, the heat exchange medium that has flowed through the medium passage flows into the one-side tank. When the heat exchange medium flows through the medium passage, the heat exchange medium in the medium passage can be exchanged with the external air substantially uniformly by the turbulent flow forming portion. On the other hand, the flow of the heat exchange medium before flowing into the one-side tank from the medium passage is rectified by the rectification unit. Thereby, it is possible to suppress the turbulent flow of the heat exchange medium from growing greatly in the vicinity of the boundary portion between the one side tank and the medium passage.

請求項２の発明では、請求項１の発明において、整流部は、成形プレートの通路構成部を媒体通路内へ膨出させることにより構成されているものとする。 According to a second aspect of the present invention, in the first aspect of the present invention, the rectifying portion is configured by causing a passage constituting portion of the forming plate to bulge into the medium passage.

この構成によれば、成形プレートを成形する際に、乱流形成部と同時に整流部を形成することが可能になる。 According to this configuration, when the molding plate is molded, the rectification unit can be formed simultaneously with the turbulent flow forming unit.

請求項３の発明では、請求項１または２の発明において、成形プレートには、媒体通路の他端部に連通する他側タンクを構成する他側タンク構成部が成形され、伝熱部材は、一側タンクに導入された熱交換媒体を上記媒体通路に流して上記他側タンクに流入させるように構成され、整流部は、通路構成部の一側タンク構成部側にのみ設けられている構成とする。 In the invention of claim 3, in the invention of claim 1 or 2, in the molding plate, the other side tank constituting portion constituting the other side tank communicating with the other end portion of the medium passage is formed, and the heat transfer member is The heat exchange medium introduced into the one-side tank is configured to flow through the medium passage and flow into the other-side tank, and the rectifying unit is provided only on the one-side tank component side of the passage component unit And

この構成によれば、一側タンクから媒体通路に流入した直後の熱交換媒体の流れが整流される。これにより、媒体通路の入口近傍で熱交換媒体の乱流が大きく成長するのを抑制することが可能になる。 According to this configuration, the flow of the heat exchange medium immediately after flowing into the medium passage from the one side tank is rectified. Thereby, it is possible to suppress the turbulent flow of the heat exchange medium from growing greatly in the vicinity of the inlet of the medium passage.

請求項４の発明では、請求項１または２の発明において、成形プレートには、媒体通路の他端部に連通する他側タンクを構成する他側タンク構成部が成形され、伝熱部材は、上記他側タンクに導入された熱交換媒体を上記媒体通路に流して一側タンクに流入させるように構成され、整流部は、通路構成部の一側タンク構成部側にのみ設けられている構成とする。 In the invention of claim 4, in the invention of claim 1 or 2, the molding plate is molded with the other side tank constituting portion constituting the other side tank communicating with the other end portion of the medium passage, and the heat transfer member is The heat exchange medium introduced into the other side tank is configured to flow through the medium passage and flow into the one side tank, and the rectifying unit is provided only on the one side tank constituent unit side of the passage constituent unit And

この構成によれば、媒体通路から一側タンクへ流入する直前の熱交換媒体の流れが整流される。これにより、媒体通路の出口近傍で熱交換媒体の乱流が大きく成長するのを抑制することが可能になる。 According to this configuration, the flow of the heat exchange medium immediately before flowing into the one-side tank from the medium passage is rectified. Thereby, it is possible to suppress the turbulent flow of the heat exchange medium from growing greatly in the vicinity of the outlet of the medium passage.

請求項５の発明では、請求項１または２の発明において、成形プレートには、媒体通路の他端部に連通する他側タンクを構成する他側タンク構成部が成形され、伝熱部材は、一側タンクに導入された熱交換媒体を上記媒体通路に流して上記他側タンクに流入させるように構成されており、上記成形プレートの通路構成部には、上記他側タンク構成部側に、上記媒体通路内を流れる熱交換媒体の流れを整流する整流部が設けられている構成とする。 In the invention of claim 5, in the invention of claim 1 or 2, in the molding plate, the other side tank constituting part constituting the other side tank communicating with the other end of the medium passage is formed, and the heat transfer member is The heat exchange medium introduced into the one-side tank is configured to flow through the medium passage and flow into the other-side tank, and the passage-constituting part of the molding plate has the side of the other-side tank constituent part, A rectifying unit that rectifies the flow of the heat exchange medium flowing in the medium passage is provided.

この構成によれば、媒体通路の入口近傍及び出口近傍で熱交換媒体の乱流が大きく成長するのを抑制することが可能になる。また、成形プレートの通路構成部の両端側の形状が同じになるので、熱交換器の製造時に一対の成形プレートを重ねて伝熱部材を形成する際、これら一対の成形プレートの向きが通路構成部の両端側について関係なくなる。これにより、蒸発器の製造工程及び製造設備を簡素化することが可能になる。 According to this configuration, it is possible to suppress a large growth of the turbulent flow of the heat exchange medium in the vicinity of the inlet and the outlet of the medium passage. In addition, since the shape of the both end sides of the passage configuration portion of the molding plate is the same, when the heat transfer member is formed by stacking a pair of molding plates at the time of manufacturing the heat exchanger, the direction of the pair of molding plates is the passage configuration. It becomes irrelevant for both ends of the part. Thereby, it becomes possible to simplify the manufacturing process and manufacturing equipment of an evaporator.

請求項６の発明では、請求項１から５のいずれか１つの発明において、一対の成形プレートのうち、一方の成形プレートの整流部が、他方の成形プレートの整流部に接合されている構成とする。 In the invention of claim 6, in any one of the inventions of claims 1 to 5, in one of the pair of forming plates, the rectifying part of one forming plate is joined to the rectifying part of the other forming plate; To do.

この構成によれば、一方の成形プレートの整流部と他方の成形プレートの整流部とが接合されて伝熱部材の耐圧強度が向上する。 According to this structure, the rectification | straightening part of one shaping | molding plate and the rectification | straightening part of the other shaping | molding plate are joined, and the pressure | voltage resistant strength of a heat-transfer member improves.

請求項７の発明では、熱交換媒体が流れる媒体通路を構成する上下方向に延びる通路構成部及び該媒体通路の上下方向一端部に連通する一側タンクを構成する一側タンク構成部が成形された一対の成形プレートを重ねて接合してなる伝熱部材と、伝熱フィンとを備え、上記伝熱部材が伝熱フィンを介して複数積層され、上記一側タンク内に導入された熱交換媒体が上記媒体通路に流入し又は上記媒体通路を流れた熱交換媒体が上記一側タンクに流入するように構成された熱交換器であって、上記成形プレートの通路構成部には、熱交換媒体の流れ方向中間部に、媒体通路内を流れる熱交換媒体の流れを乱す乱流形成部が該媒体通路内へ膨出するように設けられ、上記一側タンク構成部に、上記媒体通路内を流れる熱交換媒体の流れを整流する整流部が設けられ、上記媒体通路の断面形状が、扁平形状とされ、上記整流部は、媒体通路の平面視で略Ｘ形状とされ、上記整流部の熱交換媒体の流れ方向の寸法は、上記乱流形成部の熱交換媒体の流れ方向の寸法よりも長く設定され、上記整流部の平面視における幅方向の寸法は、上記乱流形成部の平面視における幅方向の寸法よりも長く設定されている構成とする。 In the seventh aspect of the invention, a vertically extending passage constituting portion that constitutes a medium passage through which a heat exchange medium flows and a one side tank constituting portion that constitutes a one side tank communicating with one end of the medium passage in the up and down direction are formed. A heat exchange member formed by stacking and joining a pair of molded plates, and a heat transfer fin, and a plurality of the heat transfer members are stacked via the heat transfer fins and introduced into the one-side tank. A heat exchanger configured such that a medium flows into the medium passage or a heat exchange medium that has flowed through the medium passage flows into the one-side tank, and a heat exchange is performed in a passage configuration portion of the molding plate. A turbulent flow forming portion for disturbing the flow of the heat exchange medium flowing in the medium passage is provided in the middle of the medium flow direction so as to swell into the medium passage, and the one-side tank constituting portion is provided in the medium passage. The flow of heat exchange medium flowing through Flow portion is provided, the cross-sectional shape of the medium passages, is a flat shape, the rectifying portion is a substantially X shape in a plan view of the media path, the dimensions of the flow direction of the heat exchange medium of the rectifier, The dimension of the turbulent flow forming part is set to be longer than the dimension in the flow direction of the heat exchange medium, and the dimension of the rectifying part in the width direction in plan view is set to be longer than the dimension in the width direction of the turbulent flow forming part in plan view. The configuration is as follows.

この構成によれば、一方の成形プレートの整流部と他方の成形プレートの整流部とが、媒体通路の幅方向及び流れ方向に広がる形状となるので、両成形プレートの接合面積が増大する。 According to this configuration, since the rectifying part of one molding plate and the rectifying part of the other molding plate have a shape that spreads in the width direction and the flow direction of the medium passage, the joining area of both molding plates increases.

請求項８の発明では、請求項１から６のいずれか１つの発明において、整流部は、熱交換媒体の流れ方向に延びる略直線状に形成されている構成とする。 According to an eighth aspect of the present invention, in any one of the first to sixth aspects, the rectifying section is formed in a substantially linear shape extending in the flow direction of the heat exchange medium.

この構成によれば、熱交換媒体の流れが整流部において略直線状になる。 According to this configuration, the flow of the heat exchange medium is substantially linear in the rectification unit.

請求項９の発明では、請求項１から８のいずれか１つの発明において、熱交換媒体の流れ方向に連通する複数のパスが、積層方向に隣接する複数の伝熱部材の媒体通路で構成され、熱交換媒体の流れ方向上流側に位置する上流側パスには、高圧の熱交換媒体が減圧手段により減圧された状態で導入され、上記上流側パスよりも熱交換媒体の流れ方向下流側に位置するパスに対応する通路構成部にのみ整流部が設けられている構成とする。 In a ninth aspect of the present invention, in any one of the first to eighth aspects, the plurality of paths communicating in the flow direction of the heat exchange medium are configured by medium passages of the plurality of heat transfer members adjacent in the stacking direction. The high-pressure heat exchange medium is introduced into the upstream path located upstream in the flow direction of the heat exchange medium in a state where the pressure is reduced by the pressure reducing means, and is further downstream in the flow direction of the heat exchange medium than the upstream path. The rectification unit is provided only in the passage configuration unit corresponding to the located path.

この構成によれば、高圧の熱交換媒体が減圧手段により減圧された状態で上流側パスに流入した後、下流側のパスに流入する。この熱交換媒体は、上流側及び下流側のパスを流れる間に外部空気と熱交換して蒸発していくため、下流側パスを流れる熱交換媒体の気体成分が占める割合は、上流側のパスを流れる熱交換媒体の気体成分が占める割合よりも多い。熱交換媒体中で気体成分が占める割合が多いと熱交換媒体の流速が上昇して流動音が大きくなるが、この気体成分が占める割合の多い下流側パスに対応した通路構成部に整流部が設けられているので、この部分で流動音を効果的に小さくすることが可能になる。また、気体成分が占める割合の少ない熱交換媒体が流れる上流側パスにおいては流動音が比較的小さいので、整流部を設けずに、熱交換媒体の乱流を維持して熱交換効率を高めることが可能になる。 According to this configuration, the high-pressure heat exchange medium flows into the upstream path while being decompressed by the decompression means, and then flows into the downstream path. Since this heat exchange medium evaporates by exchanging heat with external air while flowing through the upstream and downstream paths, the proportion of the gas component of the heat exchange medium flowing through the downstream path is the upstream path. More than the proportion of the gas component of the heat exchange medium flowing through. If the proportion of the gas component in the heat exchange medium is large, the flow rate of the heat exchange medium increases and the flow noise increases, but the rectifying unit is located in the passage component corresponding to the downstream path in which the proportion of the gas component is large. Since it is provided, the flowing sound can be effectively reduced in this portion. In addition, since the flow noise is relatively small in the upstream path through which the heat exchange medium with a small proportion of the gas component flows, the turbulent flow of the heat exchange medium is maintained and the heat exchange efficiency is improved without providing a rectifying unit. Is possible.

請求項１０の発明では、請求項９の発明において、パスが伝熱部材の積層方向に３つ構成されているものとする。 In the invention of claim 10, in the invention of claim 9, it is assumed that there are three paths in the stacking direction of the heat transfer members.

この構成によれば、媒体通路が、伝熱部材の積層方向に並ぶ３つのパスに分けられるので、パスが１つや２つの場合に比べて、パス１つ当たりの熱交換媒体の流路断面積が狭くなって、熱交換媒体の流速が上がる。 According to this configuration, since the medium passage is divided into three paths arranged in the stacking direction of the heat transfer member, the flow path cross-sectional area of the heat exchange medium per path is larger than in the case of one or two paths. Becomes narrower and the flow rate of the heat exchange medium increases.

請求項１の発明によれば、媒体通路の流れ方向中間部に乱流形成部を設けたので、媒体通路内の熱交換媒体と外部空気との熱交換効率を高めることができる。そして、媒体通路の一側タンク側に整流部を設けたので、一側タンクと媒体通路との境界近傍で熱交換媒体の乱流が大きく成長するのを抑制することができて、熱交換媒体の流動音による騒音を小さくすることができる。 According to the first aspect of the present invention, since the turbulent flow forming portion is provided at the intermediate portion in the flow direction of the medium passage, the heat exchange efficiency between the heat exchange medium in the medium passage and the external air can be increased. And since the rectification | straightening part was provided in the one side tank side of the medium passage, it can suppress that the turbulent flow of a heat exchange medium grows large in the vicinity of the boundary of a one side tank and a medium passage, and a heat exchange medium It is possible to reduce the noise caused by the flowing sound.

請求項２の発明によれば、整流部を乱流形成部と同時に形成することができて、製造工数を削減することができる。 According to invention of Claim 2, a rectification | straightening part can be formed simultaneously with a turbulent flow formation part, and a manufacturing man-hour can be reduced.

請求項３の発明によれば、媒体通路の入口近傍で発生する熱交換媒体の流動音による騒音を小さくすることができ、請求項４の発明によれば、媒体通路の出口近傍で発生する熱交換媒体の流動音による騒音を小さくすることができる。 According to the invention of claim 3, it is possible to reduce the noise caused by the flow sound of the heat exchange medium generated near the inlet of the medium passage. According to the invention of claim 4, the heat generated near the outlet of the medium passage. Noise due to the flow sound of the exchange medium can be reduced.

請求項５の発明によれば、媒体通路の入口近傍及び出口近傍の両方で熱交換媒体の流動音による騒音を小さくすることができる。また、成形プレートの通路構成部の両端側を同じ形状にすることができるので、製造時に成形プレートの向きが関係なくなる。これにより、蒸発器の製造工程及び製造設備を簡素化して製造コストを低減することができる。 According to invention of Claim 5, the noise by the flow sound of a heat exchange medium can be made small both in the inlet_port | entrance vicinity of a medium channel | path, and exit vicinity. Moreover, since the both ends of the channel | path structure part of a shaping | molding plate can be made into the same shape, the direction of a shaping | molding plate becomes irrelevant at the time of manufacture. Thereby, the manufacturing process and manufacturing equipment of an evaporator can be simplified and manufacturing cost can be reduced.

請求項６の発明によれば、一対の成形プレートの整流部同士を接合したので、伝熱部材の耐圧強度を落とすことなく成形プレートを薄肉にして軽量化することができる。 According to invention of Claim 6, since the rectification | straightening part of a pair of shaping | molding plate was joined, the shaping | molding plate can be made thin and weight-reduced, without reducing the pressure-resistant intensity | strength of a heat-transfer member.

請求項７の発明によれば、整流部の形状を略Ｘ形状としたので、伝熱部材の耐圧強度をより一層向上させることができる。 According to invention of Claim 7, since the shape of the rectification | straightening part was made into substantially X shape, the proof pressure intensity | strength of a heat-transfer member can be improved further.

請求項８の発明によれば、整流部における熱交換媒体の流れを略直線状にして整流効果を十分に得ることができる。 According to invention of Claim 8, the flow of the heat exchange medium in a rectification | straightening part can be made substantially linear, and a rectification effect can fully be acquired.

請求項９の発明によれば、伝熱部材の媒体通路で複数のパスを構成し、減圧手段により減圧された状態の熱交換媒体を上流側パスに流入させるようにし、下流側パスに対応した通路構成部にのみ整流部を設けたので、高い熱交換効率を維持しながら流動音による騒音を効果的に小さくすることができる。 According to the ninth aspect of the present invention, a plurality of paths are formed by the medium passage of the heat transfer member, and the heat exchange medium that has been decompressed by the decompression means is allowed to flow into the upstream path, corresponding to the downstream path. Since the rectification unit is provided only in the passage component, it is possible to effectively reduce the noise due to the flowing sound while maintaining high heat exchange efficiency.

請求項１０の発明によれば、３つのパスを備えているので、熱交換器内での熱交換媒体の流速が上がり、単位時間当たりの熱交換量を増大させることができる。 According to the tenth aspect of the invention, since three paths are provided, the flow rate of the heat exchange medium in the heat exchanger is increased, and the amount of heat exchange per unit time can be increased.

以下、本発明の実施形態を図面に基づいて詳細に説明する。尚、以下の好ましい実施形態の説明は、本質的に例示に過ぎず、本発明、その適用物或いはその用途を制限することを意図するものではない。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. It should be noted that the following description of the preferred embodiment is merely illustrative in nature, and is not intended to limit the present invention, its application, or its use.

図１及び図２は、本発明の実施形態に係る熱交換器を示すものである。この実施形態の説明では、熱交換器が、車両用空調装置の冷却用熱交換器を構成する蒸発器１である場合について説明する。図示しないが、上記空調装置は、車室の前部に配設されたインストルメントパネル内に収容されており、この空調装置の樹脂製ケーシング内に上記蒸発器１が収容されている。 1 and 2 show a heat exchanger according to an embodiment of the present invention. In the description of this embodiment, the case where the heat exchanger is the evaporator 1 constituting the cooling heat exchanger of the vehicle air conditioner will be described. Although not shown, the air conditioner is accommodated in an instrument panel disposed in the front part of the passenger compartment, and the evaporator 1 is accommodated in a resin casing of the air conditioner.

蒸発器１は、一対の成形プレート２を重ねて接合することにより形成された複数の伝熱部材３が伝熱フィン４を介して左右方向（図１及び図２の左右方向）に積層された本体５と、該本体５の積層方向両端部、即ち左端部及び右端部に設けられたエンドプレート６とで構成されている。そして、図示しない送風機から送風された空気は、各伝熱部材３間のフィン４を該伝熱部材３の積層方向に略直交する方向（図２及び図５に白抜きの矢印で示す方向）に通過するようになっている。 In the evaporator 1, a plurality of heat transfer members 3 formed by overlapping and joining a pair of molding plates 2 are stacked in the left-right direction (the left-right direction in FIGS. 1 and 2) via the heat transfer fins 4. The main body 5 and the end plate 6 provided at both ends of the main body 5 in the stacking direction, that is, the left end and the right end are configured. Then, the air blown from a blower (not shown) is a direction in which the fins 4 between the heat transfer members 3 are substantially orthogonal to the stacking direction of the heat transfer members 3 (directions indicated by white arrows in FIGS. 2 and 5). To pass through.

各伝熱部材３内には、上下方向に平行に延びる風上側冷媒通路７及び風下側冷媒通路８（共に図４にのみ示す）と、風上側冷媒通路７の上端部及び下端部に連通する風上側上部空間及び風上側下部空間（図示せず）と、風下側冷媒通路８の上端部及び下端部に連通する風下側上部空間及び風下側下部空間（図示せず）とが形成されている。風上側冷媒通路７及び風下側冷媒通路８は、空気流れ方向に長い扁平形状とされている。 In each heat transfer member 3, it communicates with the windward side refrigerant passage 7 and the leeward side refrigerant passage 8 (both shown only in FIG. 4) extending in parallel in the vertical direction, and the upper end portion and the lower end portion of the windward refrigerant passage 7. A windward upper space and a windward lower space (not shown) and a leeward upper space and a leeward lower space (not shown) communicating with the upper and lower ends of the leeward refrigerant passage 8 are formed. . The windward side refrigerant passage 7 and the leeward side refrigerant passage 8 have a flat shape that is long in the air flow direction.

図３に示すように、上記一対の成形プレート２は、各々、アルミニウム製の板材をプレス成形して得られたものである。各成形プレート２の上部には、図２にも示すように、風上側上部カップ部１０及び風下側上部カップ部１１が外部空気の流れ方向に並んで形成されている。これら風上側上部カップ部１０及び風下側上部カップ部１１は略同じ形状とされている。また、成形プレート２の下部には、風上側下部カップ部１２及び風下側下部カップ部１３が外部空気の流れ方向に並んで形成されている。これら下部カップ部１２、１３は略同じ形状とされている。上記カップ部１０〜１３の底面には、空気流れ方向に長い略長円形の開口部１０ａ〜１３ａが形成されている。 As shown in FIG. 3, the pair of molding plates 2 are each obtained by press molding an aluminum plate. As shown also in FIG. 2, the windward upper cup part 10 and the leeward upper cup part 11 are formed in the upper part of each shaping | molding plate 2 along with the flow direction of external air. The windward upper cup part 10 and the leeward upper cup part 11 have substantially the same shape. Further, an upwind lower cup portion 12 and a leeward lower cup portion 13 are formed in the lower portion of the forming plate 2 along the flow direction of the external air. These lower cup portions 12 and 13 have substantially the same shape. On the bottom surfaces of the cup portions 10 to 13, substantially oval openings 10 a to 13 a that are long in the air flow direction are formed.

成形プレート２には、風上側上部カップ部１０から風上側下部カップ部１２に亘って延びる風上側通路構成部１５と、風下側上部カップ部１１から風下側下部カップ部１３に亘って延びる風下側通路構成部１６とが形成されている。上記風上側通路構成部１５の幅は、風上側上部カップ部１０の同方向の寸法と略同じに設定されている。風上側通路構成部１５の深さは、風上側上部カップ部１０の深さよりも浅く設定されている。上記風下側通路構成部１６は、上記風上側通路構成部１５と略同じ形状とされている。 The forming plate 2 includes an upwind passage component 15 extending from the upwind upper cup portion 10 to the upwind lower cup portion 12 and an upwind side extending from the downwind upper cup portion 11 to the downwind lower cup portion 13. A passage component 16 is formed. The width of the windward side passage component 15 is set to be substantially the same as the dimension in the same direction of the windward upper cup portion 10. The depth of the windward side passage component 15 is set to be shallower than the depth of the windward upper cup portion 10. The leeward side passage component 16 has substantially the same shape as the leeward side passage component 15.

上記成形プレート２には、接合相手となる成形プレート２に接合される接合部１７が形成されている。この接合部１７は、成形プレート２の周縁部、風上側上部カップ部１０と風下側上部カップ部１１との間、風上側下部カップ部１２と風下側下部カップ部１３との間及び風上側通路構成部１５と風下側通路構成部１６との間に連続して形成されている。尚、成形プレート２の両面にはろう材が層状に設けられており、このろう材により接合相手の成形プレート２に接合されるようになっている。 The molding plate 2 is formed with a joint portion 17 to be joined to the molding plate 2 to be joined. The joint portion 17 includes a peripheral portion of the forming plate 2, between the windward upper cup portion 10 and the leeward upper cup portion 11, between the windward lower cup portion 12 and the leeward lower cup portion 13, and the windward passage. It is formed continuously between the component 15 and the leeward passage component 16. Note that a brazing material is provided in layers on both surfaces of the molding plate 2, and the brazing material is joined to the molding plate 2 to be joined.

風上側通路構成部１５の上端側には、図４にも示すように、風上側冷媒通路７側に向けて膨出する第１膨出部２０が３つ形成されている。各第１膨出部２０の先端面は上記接合部１７と略同一面上に位置付けられており、接合相手となる成形プレート２の第１膨出部２０先端面と接合されるようになっている。第１膨出部２０は、風上側冷媒通路７を幅方向に４分割する位置にそれぞれ配置され、各々、上下方向に直線状に延びている。各第１膨出部２０の上下方向の寸法、即ち冷媒流れ方向の寸法は、通路構成部１５の同方向の寸法の１５％以上２５％以下に設定されている。各第１膨出部２０の幅方向の寸法、即ち風上側冷媒通路７の幅方向の寸法は、下半部よりも上半部の方が長く設定されている。さらに、第１膨出部２０の上半部の幅方向の寸法は、上側へ行くほど長く設定されている。また、風上側通路構成部１５の下端側にも上記上側の第１膨出部２０と同じように第１膨出部２０が形成されている。詳細は後述するが、この第１膨出部２０が本発明の整流部である。尚、第１膨出部２０の数は、２つ以下であってもよいし、４つ以上であってもよい。 As shown in FIG. 4, three first bulging portions 20 that bulge toward the windward refrigerant passage 7 are formed on the upper end side of the windward passage constituting portion 15. The front end surface of each first bulging portion 20 is positioned substantially on the same plane as the joint portion 17, and is joined to the front end surface of the first bulge portion 20 of the molding plate 2 to be joined. Yes. The first bulging portions 20 are respectively arranged at positions where the windward side refrigerant passage 7 is divided into four in the width direction, and each extend linearly in the vertical direction. The vertical dimension of each first bulge 20, that is, the dimension in the refrigerant flow direction is set to 15% or more and 25% or less of the dimension in the same direction of the passage component 15. The dimension in the width direction of each first bulging part 20, that is, the dimension in the width direction of the windward refrigerant passage 7 is set to be longer in the upper half part than in the lower half part. Furthermore, the dimension in the width direction of the upper half portion of the first bulging portion 20 is set longer as it goes upward. The first bulging portion 20 is also formed on the lower end side of the windward side passage constituting portion 15 in the same manner as the upper first bulging portion 20. Although details will be described later, the first bulging portion 20 is the rectifying portion of the present invention. In addition, the number of the 1st bulging parts 20 may be two or less, and may be four or more.

また、風上側通路構成部１５の上側第１膨出部２０と下側第１膨出部２０との間には、風上側冷媒通路７側に膨出する多数の第２膨出部２１が形成されている。各第２膨出部２１の先端面は上記突条部１７の先端面と略同一面上に位置付けられており、接合相手となる成形プレート２の第２膨出部２１先端面と接合されるようになっている。各第２膨出部２１は、上記第１膨出部２０よりも小さく、冷媒の流れ方向に長い略長円形状とされている。詳細は後述するが、この第２膨出部２１が本発明の乱流形成部である。 In addition, between the upper first bulging portion 20 and the lower first bulging portion 20 of the windward side passage constituting portion 15, a large number of second bulging portions 21 bulging toward the windward side refrigerant passage 7 are provided. Is formed. The distal end surface of each second bulging portion 21 is positioned substantially on the same plane as the distal end surface of the ridge portion 17 and is joined to the distal end surface of the second bulging portion 21 of the molding plate 2 to be joined. It is like that. Each second bulge portion 21 is smaller than the first bulge portion 20 and has a substantially oval shape that is long in the refrigerant flow direction. Although details will be described later, the second bulging portion 21 is the turbulent flow forming portion of the present invention.

上記第２膨出部２１は、上下方向及び風上側通路構成部１５の幅方向に間隔をあけて配置されている。つまり、風上側通路構成部１５の上側第１膨出部２０よりも下方には、風上側通路構成部１５を幅方向に３分割する位置に２つの第２膨出部２１ａが形成されている。これら２つの第２膨出部２１ａの下方には、風上側通路構成部１５を幅方向に４分割する位置に３つの第２膨出部２１ｂが形成されている。また、風上側通路構成部１５の下側第１膨出部２０よりも上方には、上記２つの第２膨出部２１ａが形成され、これら第２膨出部２１ａの上方には３つの第２膨出部２１ｂが形成されている。このように、風上側通路構成部１５の幅方向に並ぶ２つの第２膨出部２１ａ及び３つの第２膨出部２１ｂが、上下方向に交互に形成されている。 The second bulging portion 21 is arranged at intervals in the up-down direction and the width direction of the windward passage constituting portion 15. That is, two second bulging portions 21 a are formed below the upper first bulging portion 20 of the windward side passage constituting portion 15 at a position where the windward side passage constituting portion 15 is divided into three in the width direction. . Below these two second bulges 21a, three second bulges 21b are formed at positions where the windward passage component 15 is divided into four in the width direction. In addition, the two second bulging portions 21a are formed above the lower first bulging portion 20 on the windward side passage constituting portion 15, and three second bulging portions 21a are formed above the second bulging portions 21a. Two bulging portions 21b are formed. As described above, the two second bulging portions 21a and the three second bulging portions 21b arranged in the width direction of the windward passage constituting portion 15 are alternately formed in the vertical direction.

上記風下側通路構成部１６にも、上記風上側通路構成部１５と同様に、第１膨出部２０及び第２膨出部２１が形成されている。 The leeward side passage constituting portion 16 is also formed with a first bulging portion 20 and a second bulging portion 21 similarly to the leeward side passage constituting portion 15.

一対の成形プレート２を重ねて突条部１７を接合すると、風上側通路構成部１５及び風下側通路構成部１６により風上側冷媒通路７及び風下側冷媒通路８がそれぞれ構成される。このとき、風上側上部カップ部１０により上記風上側上部空間が構成され、風下側上部カップ部１１により上記風下側上部空間が構成される。さらに、風上側下部カップ部１２により上記風上側下部空間が構成され、風下側下部カップ部１３により上記風下側下部空間が構成される。 When the pair of molding plates 2 are overlapped to join the protrusions 17, the windward side refrigerant passage 7 and the leeward side refrigerant passage 8 are constituted by the windward side passage constituting portion 15 and the leeward side passage constituting portion 16, respectively. At this time, the windward upper space is constituted by the windward upper cup portion 10, and the leeward upper space is constituted by the leeward upper cup portion 11. Further, the windward lower cup portion 12 constitutes the windward lower space, and the leeward lower cup portion 13 constitutes the leeward lower space.

上記伝熱部材３を積層していくと、積層方向に隣接する各カップ部１０〜１３の開口部１０ａ、１１ａ、１２ａ、１３ａ周縁が接触する。この状態で積層方向に隣接する開口部１０ａ、１１ａ、１２ａ、１３ａ周縁を接合すると、図２及び図５に示すように、該開口部１０ａ、１１ａ、１２ａ、１３ａを介し、積層方向に並ぶ風上側上部空間が連通して風上側上部タンク２３が構成され、風下側上部空間が連通して風下側上部タンク２４が構成され、風上側下部空間が連通して風上側下部タンク２５が構成され、風下側下部空間が連通して風下側下部タンク２６が構成される。つまり、カップ部１０〜１３は、本発明のタンク構成部である。 When the heat transfer member 3 is laminated, the peripheral edges of the opening portions 10a, 11a, 12a, and 13a of the cup portions 10 to 13 adjacent in the laminating direction come into contact with each other. In this state, when the peripheral edges of the openings 10a, 11a, 12a, and 13a adjacent to each other in the stacking direction are joined, as shown in FIGS. 2 and 5, winds aligned in the stacking direction through the openings 10a, 11a, 12a, and 13a. The upper side upper space communicates to constitute the windward upper tank 23, the leeward side upper space communicates to constitute the leeward upper tank 24, the windward lower space communicates to constitute the windward lower tank 25, The leeward side lower space 26 communicates with the leeward side lower space to form the leeward side lower tank 26. That is, the cup parts 10-13 are the tank structure part of this invention.

また、図１に示すように、蒸発器１における左端部には、フィン４が配置されており、このフィン４の左側に上記エンドプレート６が接合されている。蒸発器１の右端部にも同様にフィン４が配置され、その右側に上記エンドプレート６が接合されている。 As shown in FIG. 1, a fin 4 is disposed at the left end of the evaporator 1, and the end plate 6 is joined to the left side of the fin 4. Similarly, the fin 4 is disposed at the right end of the evaporator 1, and the end plate 6 is joined to the right side thereof.

風下側上部タンク２４の右端部には、図２に示すように、冷媒の導入管部２７が設けられている。また、風上側上部タンク２３の右端部には、冷媒の導出管部２８が設けられている。これら導入管部２７及び導出管部２８には、減圧手段としての膨張弁を内蔵した膨張弁ブロック（図示せず）が接続されるようになっている。図外の圧縮機や凝縮器を経て生成された高圧の液冷媒は、上記膨張弁ブロックを介して減圧されて導入管部２７から蒸発器１内に導入され、また、蒸発器１内の冷媒は導出管部２８から膨張弁ブロックを介して外部に導出されるようになっている。 As shown in FIG. 2, a refrigerant introduction pipe portion 27 is provided at the right end portion of the leeward side upper tank 24. A refrigerant outlet pipe 28 is provided at the right end of the windward upper tank 23. An expansion valve block (not shown) incorporating an expansion valve as a decompression means is connected to the introduction pipe portion 27 and the outlet pipe portion 28. The high-pressure liquid refrigerant generated through a compressor and a condenser outside the figure is decompressed through the expansion valve block and introduced into the evaporator 1 from the introduction pipe portion 27, and the refrigerant in the evaporator 1 Is led out from the lead-out pipe portion 28 through the expansion valve block.

上記左右方向に積層された伝熱部材３のうち、蒸発器１の右寄りに位置する伝熱部材３ａの成形プレート２ａには、風上側上部カップ部１０及び風下側上部カップ部１１の開口部１０ａ、１１ａが形成されていない。この右寄りに位置する伝熱部材３ａにより、図５に示すように、風上側上部タンク２３及び風下側上部タンク２４が左右方向右寄りの部位で左側空間２３ａ、２４ａと右側空間２３ｂ、２４ｂとにそれぞれ区画されている。また、左右方向に積層された伝熱部材３のうち、蒸発器１の左寄りに位置する伝熱部材３ｂの成形プレート２ｂには、風上側下部カップ部１２及び風下側下部カップ部１３の開口部１２ａ、１３ａが形成されていない。この左寄りに位置する伝熱部材３ｂにより、風上側下部タンク２５及び風下側下部タンク２６が左右方向左寄りの部位で左側空間２５ａ、２６ａと右側空間２５ｂ、２６ｂとにそれぞれ区画されている。 Among the heat transfer members 3 stacked in the left-right direction, the molding plate 2a of the heat transfer member 3a located on the right side of the evaporator 1 has an opening 10a of the windward upper cup portion 10 and the leeward upper cup portion 11. 11a is not formed. With the heat transfer member 3a located on the right side, as shown in FIG. 5, the windward upper tank 23 and the leeward upper tank 24 are respectively located in the left space 23a, 24a and the right space 23b, 24b at the right side in the left-right direction. It is partitioned. Of the heat transfer members 3 stacked in the left-right direction, the forming plate 2b of the heat transfer member 3b located on the left side of the evaporator 1 has openings on the windward lower cup portion 12 and the leeward lower cup portion 13. 12a and 13a are not formed. By the heat transfer member 3b located on the left side, the windward lower tank 25 and the leeward lower tank 26 are partitioned into left space 25a, 26a and right space 25b, 26b at the left side in the left-right direction.

また、上記左寄りに位置する伝熱部材３ｂよりも左側に位置する伝熱部材３ｃを構成する成形プレート２ｃの風上側下部カップ部１２と風下側下部カップ部１３との間は、切り欠かれた形状をなしている。この切り欠かれた部分により、図２（ｂ）に示すように、伝熱部材３ｃの風上側下部空間と風下側下部空間とを連通させる連通路３０が形成されている。そして、この連通路３０を介して風上側下部タンク２５の左側空間２５ａと風下側下部タンク２６の左側空間２６ａとが連通している。 Further, the gap between the windward lower cup portion 12 and the leeward lower cup portion 13 of the molding plate 2c constituting the heat transfer member 3c located on the left side of the heat transfer member 3b located on the left side is cut out. It has a shape. As shown in FIG. 2 (b), a communication passage 30 is formed by the cut-out portion to communicate the windward lower space and the leeward lower space of the heat transfer member 3c. The left space 25 a of the leeward lower tank 25 and the left space 26 a of the leeward lower tank 26 communicate with each other via the communication path 30.

次に、上記のように構成された蒸発器１内部での冷媒の流れについて、図５に基づいて説明する。まず、導入管部２７から風下側上部タンク２４の右側空間２４ｂに導入された冷媒は、該右側空間２４ｂに連通する冷媒通路８に流入して下方へ流れ、風下側下部タンク２６の右側空間２６ｂに流入する。この風下側上部タンク２４の右側空間２４ｂに連通する冷媒通路８で第１パスＰ１が構成されている。 Next, the flow of the refrigerant in the evaporator 1 configured as described above will be described with reference to FIG. First, the refrigerant introduced into the right space 24 b of the leeward upper tank 24 from the introduction pipe portion 27 flows into the refrigerant passage 8 communicating with the right space 24 b and flows downward, and the right space 26 b of the leeward lower tank 26. Flow into. A first path P1 is constituted by the refrigerant passage 8 communicating with the right space 24b of the leeward side upper tank 24.

風下側下部タンク２６の右側空間２６ｂに流入した冷媒は左側へ流れて伝熱部材３ａと伝熱部材３ｂとの間の冷媒通路８に流入して上方へ流れ、風下側上部タンク２４の左側空間２４ａに流入する。この伝熱部材３ａと伝熱部材３ｂとの間の冷媒通路８で第２パスＰ２が構成されている。 The refrigerant flowing into the right space 26b of the leeward lower tank 26 flows to the left, flows into the refrigerant passage 8 between the heat transfer member 3a and the heat transfer member 3b, flows upward, and the left space of the leeward upper tank 24. It flows into 24a. A second path P2 is configured by the refrigerant passage 8 between the heat transfer member 3a and the heat transfer member 3b.

風下側上部タンク２４の左側空間２４ａに流入した冷媒は、左側へ流れて風下側下部タンク２６の左側空間２６ａに連通する冷媒通路８に流入して下方へ流れ、風下側下部タンク２６の左側空間２６ａに流入する。この風下側下部タンク２６の左側空間２６ａに連通する冷媒通路８で第３パスＰ３が構成されている。 The refrigerant that has flowed into the left space 24a of the leeward upper tank 24 flows to the left, flows into the refrigerant passage 8 that communicates with the left space 26a of the leeward lower tank 26, flows downward, and flows into the left space of the leeward lower tank 26. 26a. A third path P3 is constituted by the refrigerant passage 8 communicating with the left space 26a of the leeward lower tank 26.

風下側下部タンク２６の左側空間２６ａに流入した冷媒は連通路３０を通って風上側下部タンク２５の左側空間２５ａに流入し、該左側空間２５ａに連通する冷媒通路７に流入して上方へ流れ、風上側上部タンク２３の左側空間２３ａに流入する。この風上側下部タンク２５の左側空間２５ａに連通する冷媒通路７で第４パスＰ４が構成されている。 The refrigerant flowing into the left space 26a of the leeward lower tank 26 flows into the left space 25a of the windward lower tank 25 through the communication passage 30, flows into the refrigerant passage 7 communicating with the left space 25a, and flows upward. Then, it flows into the left space 23 a of the windward upper tank 23. A fourth path P4 is formed by the refrigerant passage 7 communicating with the left space 25a of the upwind lower tank 25.

風上側上部タンク２３の左側空間２３ａに流入した冷媒は、右側へ流れて伝熱部材３ａと伝熱部材３ｂとの間の冷媒通路７に流入して下方へ流れ、風上側下部タンク２５の右側空間２５ｂに流入する。この伝熱部材３ａと伝熱部材３ｂとの間の冷媒通路７で第５パスＰ５が構成されている。 The refrigerant that has flowed into the left space 23a of the windward upper tank 23 flows to the right, flows into the refrigerant passage 7 between the heat transfer member 3a and the heat transfer member 3b, flows downward, and flows to the right of the windward lower tank 25. It flows into the space 25b. The refrigerant path 7 between the heat transfer member 3a and the heat transfer member 3b constitutes a fifth path P5.

風上側下部タンク２５の右側空間２５ｂに流入した冷媒は、右側へ流れて風上側上部タンク２３の右側空間２３ｂに連通する冷媒通路７に流入して上方へ流れ、風上側上部タンク２３の右側空間２３ｂに流入する。この風上側上部タンク２３の右側空間２３ｂに連通する冷媒通路７で第６パスＰ６が構成されている。風上側上部タンク２３の右側空間２３ｂに流入した冷媒は導出管部２８から外部に導出される。 The refrigerant that has flowed into the right space 25b of the windward lower tank 25 flows to the right, flows into the refrigerant passage 7 that communicates with the right space 23b of the windward upper tank 23, flows upward, and flows into the right space of the windward upper tank 23. 23b. A sixth path P <b> 6 is configured by the refrigerant passage 7 that communicates with the right space 23 b of the upwind upper tank 23. The refrigerant that has flowed into the right space 23 b of the windward upper tank 23 is led out to the outside from the lead-out pipe portion 28.

上記冷媒通路７、８を流れる冷媒には、第２膨出部２１により乱流が形成される。これにより、冷媒通路７、８内の冷媒を外部空気と略均一に熱交換させることが可能になり、単位時間当たりの熱伝達量が高まる。そして、例えば第１パスＰ１を構成する冷媒通路８に流入した冷媒は、第２膨出部２１よりも下流側へ流れると、第１膨出部２０と冷媒通路８内側面との間及び第１膨出部２０間を通る。このとき第１膨出部２０が冷媒通路８の延びる方向に直線状に延びているので、冷媒の流れが整流される。これにより、第２膨出部２１により形成した乱流の影響が冷媒通路８と風下側下部タンク２６との境界近傍に及ぶのを抑制することが可能になる。また、例えば風下側上部タンク２４の冷媒が第１パスＰ１を構成する冷媒通路８に流入するときにも同様に冷媒の流れが第１膨出部２０により整流される。その結果、上側第１膨出部２０の下流側に位置する第２膨出部２１によって形成される乱流の影響が冷媒通路８と風下側上部タンク２４との境界近傍に及ぶのを抑制することが可能になる。これにより、冷媒通路８とタンク２４との境界近傍で冷媒の乱流が大きく成長するのを抑制することが可能になる。尚、他のタンクと冷媒通路との境界部分近傍においても、同様に冷媒の乱流が大きく成長するのを抑制することが可能になる。 A turbulent flow is formed by the second bulging portion 21 in the refrigerant flowing through the refrigerant passages 7 and 8. As a result, the refrigerant in the refrigerant passages 7 and 8 can be heat-exchanged with the external air substantially uniformly, and the amount of heat transfer per unit time is increased. For example, when the refrigerant that has flowed into the refrigerant passage 8 configuring the first path P1 flows downstream from the second bulge portion 21, the refrigerant flows between the first bulge portion 20 and the inner surface of the refrigerant passage 8. 1 It passes between the bulging portions 20. At this time, since the first bulging portion 20 extends linearly in the direction in which the refrigerant passage 8 extends, the flow of the refrigerant is rectified. Thereby, it is possible to suppress the influence of the turbulent flow formed by the second bulging portion 21 from reaching the vicinity of the boundary between the refrigerant passage 8 and the leeward lower tank 26. For example, when the refrigerant in the leeward side upper tank 24 flows into the refrigerant passage 8 constituting the first path P1, the flow of the refrigerant is rectified by the first bulging portion 20 in the same manner. As a result, the influence of the turbulent flow formed by the second bulging portion 21 located on the downstream side of the upper first bulging portion 20 is suppressed from reaching the vicinity of the boundary between the refrigerant passage 8 and the leeward upper tank 24. It becomes possible. Thereby, it becomes possible to suppress the turbulent flow of the refrigerant from growing greatly in the vicinity of the boundary between the refrigerant passage 8 and the tank 24. It is also possible to suppress the turbulent flow of the refrigerant from growing greatly in the vicinity of the boundary portion between the other tank and the refrigerant passage.

したがって、この実施形態に係る蒸発器１によれば、冷媒通路７、８の上下方向中間部に第２膨出部２１を設けたので、冷媒通路７、８内の冷媒と外部空気との熱交換効率を高めることができる。そして、冷媒通路７、８の上流側及び下流側に略直線状に延びる第１膨出部２０をそれぞれ設けたので、冷媒通路７、８と上部タンク２３、２４や下部タンク２５、２６との境界近傍で冷媒の乱流が大きく成長するのを抑制することができて、冷媒の流動音による騒音を小さくすることができる。 Therefore, according to the evaporator 1 which concerns on this embodiment, since the 2nd bulging part 21 was provided in the up-down direction intermediate part of the refrigerant paths 7 and 8, the heat | fever of the refrigerant | coolant in the refrigerant paths 7 and 8 and external air is provided. Exchange efficiency can be improved. And since the 1st bulging part 20 extended substantially linearly was provided in the upstream and downstream of the refrigerant passages 7 and 8, respectively, the refrigerant passages 7 and 8 and the upper tanks 23 and 24 and the lower tanks 25 and 26 are connected. It is possible to suppress the turbulent flow of the refrigerant from growing greatly in the vicinity of the boundary, and to reduce the noise due to the flow noise of the refrigerant.

また、成形プレート２をプレス成形する際に、第１膨出部２０及び第２膨出部２１を同時に形成することができて、製造工数を削減することができる。 Moreover, when press-molding the shaping | molding plate 2, the 1st bulging part 20 and the 2nd bulging part 21 can be formed simultaneously, and a manufacturing man-hour can be reduced.

また、成形プレート２の上下両端側に同じ形状の第１膨出部２０を設けたので、冷媒通路７、８の入口近傍及び出口近傍の両方で冷媒の流動音による騒音を小さくすることができるとともに、成形プレート２の形状を上下方向について対称形状にすることができる。このように成形プレート２を上下方向について対称形状にすることにより、蒸発器１の製造時、成形プレート２の上下方向の向きが関係なくなるので、製造工程及び設備を簡素化して低コスト化を図ることができる。 In addition, since the first bulging portions 20 having the same shape are provided on both the upper and lower ends of the molding plate 2, it is possible to reduce noise due to the flow noise of the refrigerant both near the inlet and the outlet of the refrigerant passages 7 and 8. At the same time, the shape of the forming plate 2 can be made symmetrical with respect to the vertical direction. By making the molding plate 2 symmetrical in the vertical direction in this way, the vertical direction of the molding plate 2 becomes irrelevant when the evaporator 1 is manufactured. Therefore, the manufacturing process and equipment are simplified and the cost is reduced. be able to.

また、一方の成形プレート２の第１膨出部２０及び第２膨出部２１と、他方の成形プレート２の第１膨出部２０及び第２膨出部２１とを接合するので、伝熱部材３の耐圧強度を落とすことなく、成形プレート２を薄肉にして軽量化することができる。 Moreover, since the 1st bulging part 20 and the 2nd bulging part 21 of one shaping | molding plate 2 and the 1st bulging part 20 and the 2nd bulging part 21 of the other shaping | molding plate 2 are joined, heat transfer Without lowering the pressure strength of the member 3, the molding plate 2 can be made thinner and lighter.

また、第１膨出部２０を直線状にしているので、冷媒の流れを整流する効果を十分に得ることができる。 Moreover, since the 1st bulging part 20 is made linear, the effect which rectifies | straightens the flow of a refrigerant | coolant can fully be acquired.

また、蒸発器１内の冷媒通路７、８を風下側で第１〜第３パスＰ１〜Ｐ３の３つに分け、風上側で第４〜第６パスＰ４〜Ｐ６の３つに分けたので、風下側及び風上側の各々でパスが１つや２つ設定されている場合に比べて、パス１つ当たりの冷媒の流路断面積が狭くなって、蒸発器１内で冷媒の流速を上げることができる。これにより、単位時間当たりの熱交換量をより一層増大させることができて、外部空気の冷却能力を高めることができる。 Moreover, since the refrigerant passages 7 and 8 in the evaporator 1 are divided into three of the first to third paths P1 to P3 on the leeward side and divided into three of the fourth to sixth paths P4 to P6 on the leeward side. Compared to the case where one or two paths are set on the leeward side and the windward side, the refrigerant cross-sectional area of the refrigerant per path is narrowed, and the flow rate of the refrigerant is increased in the evaporator 1. be able to. Thereby, the heat exchange amount per unit time can be further increased, and the cooling capacity of the external air can be increased.

尚、この実施形態では、成形プレート２の上端側及び下端側の両方に第１膨出部２０を設けたが、これに限らず、第１膨出部２０は成形プレート２の上端側にのみ設けてもよいし、下端側にのみ設けてもよい。例えば、冷媒通路７、８の入口側にのみ第１膨出部２０が設けられている場合には、入口近傍で発生する騒音を小さくすることができ、冷媒通路７、８の出口側にのみ第１膨出部２０が設けられている場合には、出口近傍で発生する騒音を小さくすることができる。 In this embodiment, the first bulging portion 20 is provided on both the upper end side and the lower end side of the molding plate 2. However, the present invention is not limited to this, and the first bulging portion 20 is only on the upper end side of the molding plate 2. You may provide, and you may provide only in a lower end side. For example, when the first bulging portion 20 is provided only on the inlet side of the refrigerant passages 7 and 8, noise generated in the vicinity of the inlet can be reduced, and only on the outlet side of the refrigerant passages 7 and 8. When the 1st bulging part 20 is provided, the noise which generate | occur | produces in the exit vicinity can be made small.

また、この実施形態では、第１膨出部２０を直線状に形成しているが、これに限らず、例えば図６及び図７に示す変形例の第１膨出部５０のように、冷媒通路７、８の平面視で略Ｘ形状にしてもよい。この第１膨出部５０は、第２膨出部２１よりも冷媒通路７、８の幅方向に長くかつ上下方向に長く形成されている。このように第１膨出部５０を第２膨出部２１よりも大型にして１つだけ設けることにより、第２膨出部２１により乱された冷媒の流れが第２膨出部５０により整流される。尚、図６及び図７の符号２２は、冷媒通路７、８へ向けて膨出する第３膨出部である。 Moreover, in this embodiment, although the 1st bulging part 20 is formed in linear form, it is not restricted to this, For example, like the 1st bulging part 50 of the modification shown in FIG.6 and FIG.7, it is a refrigerant | coolant. The passages 7 and 8 may have a substantially X shape in plan view. The first bulging portion 50 is formed longer than the second bulging portion 21 in the width direction of the refrigerant passages 7 and 8 and longer in the vertical direction. Thus, by providing only one first bulging part 50 larger than the second bulging part 21, the flow of the refrigerant disturbed by the second bulging part 21 is rectified by the second bulging part 50. Is done. In addition, the code | symbol 22 of FIG.6 and FIG.7 is the 3rd bulging part which bulges toward the refrigerant paths 7 and 8. FIG.

この変形例では、第１膨出部５０を冷媒通路７、８の幅方向及び流れ方向に延びる略Ｘ形状としたので、相手側の成形プレート２への接合面積が増大して接合強度が高まるので、伝熱部材３の耐圧強度をより一層向上させることができる。 In this modification, since the first bulging portion 50 has a substantially X shape extending in the width direction and the flow direction of the refrigerant passages 7 and 8, the bonding area to the molding plate 2 on the other side is increased and the bonding strength is increased. Therefore, the pressure strength of the heat transfer member 3 can be further improved.

また、蒸発器１に導入された冷媒は第１パスＰ１から第６パスＰ６へ向けて流れる間に外部空気と熱交換して蒸発していく。このため、例えば第２パスＰ２を流れる冷媒の気体成分が占める割合は、第１パスＰ１を流れる冷媒の気体成分が占める割合よりも多い。冷媒中で気体成分が占める割合が多いと冷媒の流速が上昇して流動音が大きくなるが、この気体成分が占める割合の多い下流側のパスに対応した通路構成部１５、１６にのみ第１膨出部２０、５０を設けてもよい。こうすることで、冷媒の流動音を効果的に小さくすることができる。また、この場合、気体成分が占める割合の少ない冷媒が流れている上流側のパスにおいては、冷媒の流動音が比較的小さいので、第１膨出部２０、５０を設けずに冷媒の乱流を維持して熱伝達率を高めることができる。 In addition, the refrigerant introduced into the evaporator 1 evaporates by exchanging heat with external air while flowing from the first path P1 toward the sixth path P6. For this reason, for example, the ratio which the gas component of the refrigerant | coolant which flows through 2nd path | pass P2 accounts is larger than the ratio which the gas component of the refrigerant | coolant which flows through 1st path | pass P1 occupies. When the proportion of the gas component in the refrigerant is large, the flow velocity of the refrigerant is increased and the flow noise is increased. However, the first is only in the passage components 15 and 16 corresponding to the downstream path in which the proportion of the gas component is large. The bulging portions 20 and 50 may be provided. By doing so, the flow noise of the refrigerant can be effectively reduced. Further, in this case, in the upstream path in which the refrigerant with a small proportion of the gas component flows, the flow noise of the refrigerant is relatively small. Therefore, the turbulent flow of the refrigerant without providing the first bulging portions 20 and 50 Can be maintained to increase the heat transfer rate.

また、この実施形態では、蒸発器１の風上側及び風下側にそれぞれ３つずつパスＰ１〜Ｐ３、Ｐ４〜Ｐ６を設けているが、パスの数はこれに限られるものではなく、伝熱部材３ａ、３ｂの配置や連通路３０の形成位置を変更することでパスの数を任意に変えることが可能である。また、この実施形態では、冷媒通路を外部空気の流れ方向に２列設けているが、冷媒通路は外部空気の流れ方向に１列であってもよいし、３列以上であってもよい。 In this embodiment, three passes P1 to P3 and P4 to P6 are provided on the windward side and the leeward side of the evaporator 1, respectively, but the number of passes is not limited to this, and the heat transfer member It is possible to arbitrarily change the number of passes by changing the arrangement of 3a and 3b and the position where the communication passage 30 is formed. In this embodiment, the refrigerant passages are provided in two rows in the direction of external air flow. However, the refrigerant passages may be in one row in the direction of external air flow, or may be in three or more rows.

以上説明したように、本発明に係る熱交換器は、例えば、車両用空調装置の冷却用熱交換器に適用することができる。 As described above, the heat exchanger according to the present invention can be applied to, for example, a cooling heat exchanger of a vehicle air conditioner.

本発明の実施形態に係る蒸発器を外部空気の流れ方向下流側から見た図である。It is the figure which looked at the evaporator which concerns on embodiment of this invention from the flow direction downstream of external air. （ａ）は蒸発器の平面図であり、（ｂ）は蒸発器の底面図である。(A) is a top view of an evaporator, (b) is a bottom view of an evaporator. 成形プレートの側面図である。It is a side view of a shaping | molding plate. （ａ）は図３のＡ−Ａ線に相当する伝熱部材の断面図であり、（ｂ）は図３のＢ−Ｂ線に相当する伝熱部材の断面図であり、（ｃ）は図３のＣ−Ｃ線に相当する伝熱部材の断面図である。(A) is sectional drawing of the heat-transfer member corresponded to the AA line of FIG. 3, (b) is sectional drawing of the heat-transfer member corresponded to the BB line of FIG. 3, (c) is It is sectional drawing of the heat-transfer member corresponded to CC line of FIG. 蒸発器内部での冷媒の流れを示す概略図である。It is the schematic which shows the flow of the refrigerant | coolant inside an evaporator. 実施形態の変形例に係る図３相当図である。FIG. 4 is a view corresponding to FIG. 3 according to a modification of the embodiment. （ａ）は図６のＡ−Ａ線に相当する伝熱部材の断面図であり、（ｂ）は図６のＢ−Ｂ線に相当する伝熱部材の断面図である。(A) is sectional drawing of the heat-transfer member corresponded to the AA line of FIG. 6, (b) is sectional drawing of the heat-transfer member corresponded to the BB line of FIG.

１蒸発器（熱交換器）
２成形プレート
３伝熱部材
４伝熱フィン
７風上側冷媒通路（媒体通路）
８風下側冷媒通路（媒体通路）
１５風上側通路構成部
１６風下側通路構成部
２０、５０第１膨出部（整流部）
２１第２膨出部（乱流形成部）
Ｐ１〜Ｐ６第１パス〜第６パス 1 Evaporator (heat exchanger)
2 Molding plate 3 Heat transfer member 4 Heat transfer fin 7 Windward side refrigerant path (medium path)
8 Downward refrigerant passage (medium passage)
15 leeward side passage component 16 leeward side channel component 20, 50 first bulge (rectifier)
21 2nd swelling part (turbulent flow formation part)
P1-P6 1st pass-6th pass

Claims

Superimposing a pair of molding plates one side tank constituting portion constituting the one side tank connected in the vertical direction one end portion of the vertically extending passage forming portion and said medium passage is formed which constitutes the media path heat exchange medium flows A plurality of the heat transfer members stacked via the heat transfer fins, and the heat exchange medium introduced into the one-side tank flows into the medium passage. Or a heat exchanger configured such that the heat exchange medium flowing through the medium passage flows into the one-side tank,
In the passage constituting part of the molding plate, a turbulent flow forming part that disturbs the flow of the heat exchange medium flowing in the medium passage is provided in the middle part in the flow direction of the heat exchange medium so as to bulge into the medium passage. A rectifying unit that rectifies the flow of the heat exchange medium that extends from the one side tank component to the other side and flows in the medium passage is provided ,
The other side in the longitudinal direction of the rectifying portion extends linearly,
The heat exchanger according to claim 1, wherein a dimension in the width direction on one side in the longitudinal direction of the rectifying unit is set so as to become longer as it approaches the one-side tank component, and the medium passage is narrowed .

The heat exchanger according to claim 1,
The rectifying unit is configured by expanding a passage constituting part of a forming plate into a medium passage.

The heat exchanger according to claim 1 or 2,
In the molding plate, the other side tank constituting part constituting the other side tank communicating with the other end of the medium passage is formed,
The heat transfer member is configured to flow the heat exchange medium introduced into the one side tank through the medium passage and into the other side tank,
The rectifying unit is provided only on the one-side tank component part side of the passage component part.

The heat exchanger according to claim 1 or 2,
In the molding plate, the other side tank constituting part constituting the other side tank communicating with the other end of the medium passage is formed,
The heat transfer member is configured to flow the heat exchange medium introduced into the other side tank through the medium passage and into the one side tank,
The rectifying unit is provided only on the one-side tank component part side of the passage component part.

The heat exchanger according to claim 1 or 2,
In the molding plate, the other side tank constituting part constituting the other side tank communicating with the other end of the medium passage is formed,
The heat transfer member is configured to flow the heat exchange medium introduced into the one side tank through the medium passage and into the other side tank,
The heat exchanger according to claim 1, wherein a rectification unit that rectifies the flow of the heat exchange medium flowing in the medium passage is provided on the side of the other side tank component on the passage component of the molding plate.

The heat exchanger according to any one of claims 1 to 5,
The heat exchanger characterized by the rectification | straightening part of one shaping | molding plate being joined to the rectification | straightening part of the other shaping | molding plate among a pair of shaping | molding plates.

A pair of molding plates formed by molding a passage constituting portion that constitutes a medium passage through which a heat exchange medium flows and a one-side tank constituting a one-side tank that communicates with one end of the medium passage in the up-down direction are stacked. A plurality of the heat transfer members stacked via the heat transfer fins, and the heat exchange medium introduced into the one-side tank flows into the medium passage. Or a heat exchanger configured such that the heat exchange medium flowing through the medium passage flows into the one-side tank,
In the passage constituting part of the molding plate, a turbulent flow forming part that disturbs the flow of the heat exchange medium flowing in the medium passage is provided in the middle part in the flow direction of the heat exchange medium so as to bulge into the medium passage. The one side tank component is provided with a rectifying unit that rectifies the flow of the heat exchange medium flowing in the medium passage,
The cross-sectional shape of the medium passage is a flat shape,
The rectifying unit is substantially X-shaped in a plan view of the medium passage ,
The dimension in the flow direction of the heat exchange medium of the rectifying unit is set to be longer than the dimension of the flow direction of the heat exchange medium in the turbulent flow forming unit, and the dimension in the width direction in the plan view of the rectifying unit is the turbulent flow. A heat exchanger characterized in that it is set longer than the dimension in the width direction in plan view of the forming part .

The heat exchanger according to any one of claims 1 to 6,
The rectifying unit is formed in a substantially linear shape extending in the flow direction of the heat exchange medium.

The heat exchanger according to any one of claims 1 to 8,
A plurality of paths communicating in the flow direction of the heat exchange medium are configured by medium passages of a plurality of heat transfer members adjacent in the stacking direction,
In the upstream path located on the upstream side in the flow direction of the heat exchange medium, the high-pressure heat exchange medium is introduced in a state where the pressure is reduced by the decompression means,
A heat exchanger, wherein a rectification unit is provided only in a passage configuration unit corresponding to a path located downstream of the upstream path in the flow direction of the heat exchange medium.

The heat exchanger according to claim 9, wherein
A heat exchanger characterized in that three paths are provided in the stacking direction of the heat transfer members.