JPH04117363U - Evaporator - Google Patents

Evaporator

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Publication number
JPH04117363U
JPH04117363U JP3043291U JP3043291U JPH04117363U JP H04117363 U JPH04117363 U JP H04117363U JP 3043291 U JP3043291 U JP 3043291U JP 3043291 U JP3043291 U JP 3043291U JP H04117363 U JPH04117363 U JP H04117363U
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Prior art keywords
evaporator
tank
edge
refrigerant
joint
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JP3043291U
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JP2572083Y2 (en
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智子 松沢
美章 古賀
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カルソニツク株式会社
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Abstract

(57)【要約】 【目的】冷媒の偏流を防止して、蒸発器を通過する空気
の温度分布を均一化し、性能向上を図る。 【構成】折り返し流路18を有する素子20の端部に形
成した接合部19aを、タンク21内に挿入している。
接合部19aの端縁部には、円弧状の切り欠き35を設
け、上記タンク21内への突出量を少なく抑えている。
(57) [Summary] [Purpose] To prevent uneven flow of refrigerant, equalize the temperature distribution of air passing through the evaporator, and improve performance. [Structure] A joint 19a formed at the end of an element 20 having a folded channel 18 is inserted into a tank 21.
An arcuate notch 35 is provided at the edge of the joint 19a to keep the amount of protrusion into the tank 21 small.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

この考案に係る蒸発器は、自動車用空気調和装置に組み込んで空気を冷却する もので、本考案は、この様な蒸発器に於ける冷媒の流れの均一化により、蒸発器 を通過した空気の温度分布の均一化を図り、この蒸発器の性能向上を図るもので ある。 The evaporator according to this invention is incorporated into an automotive air conditioner to cool the air. Therefore, the present invention improves the evaporator by equalizing the flow of refrigerant in the evaporator. This aims to improve the performance of this evaporator by equalizing the temperature distribution of the air passing through the evaporator. be.

【0002】0002

【従来の技術】[Conventional technology]

空気調和装置には、内部で冷媒を蒸発させ、外部を流通する空気を冷却する蒸 発器が組み込まれている。 Air conditioners have evaporators that evaporate refrigerant inside and cool the air flowing outside. Built-in generator.

【0003】 この様な、空気調和装置に組み込まれる蒸発器として従来から、例えば特開昭 62−798号公報に記載されている様な、複数枚の金属板を互いに積層して成 る、所謂積層型蒸発器が知られている。0003 As an evaporator built into such an air conditioner, for example, the It is made by laminating multiple metal plates together, as described in Publication No. 62-798. A so-called stacked evaporator is known.

【0004】 この積層型蒸発器は、図4に示す様に、それぞれが2枚の金属板1、1を最中 状に組み合わせて成るユニット2、2を複数個、互いに積層する事で構成されて いる。各金属板1、1には、図5〜6に示す様に、各金属板1、1の全周を囲む 平坦部3と、この平坦部3の内側にU字形に形成された浅い第一凹部4と、この 第一凹部4の両端に形成された深い第二、第三凹部5、6と、第二、第三凹部5 、6の中央部に形成された通孔7、8とを設けている。又、第一凹部4の内側に は複数の凸部9、9を設けて、この第一凹部4の内側に於ける冷媒の流れを乱す 様にしている。0004 As shown in Fig. 4, this stacked evaporator has two metal plates 1 and 1 in the middle. It is composed of a plurality of units 2, 2 which are combined in a shape and are stacked on top of each other. There is. Each metal plate 1, 1 is provided with A flat part 3, a shallow first recess 4 formed in a U-shape inside this flat part 3, and this Deep second and third recesses 5 and 6 formed at both ends of the first recess 4, and second and third recesses 5. , 6 are provided with through holes 7 and 8 formed in the center thereof. Also, inside the first recess 4 is provided with a plurality of convex portions 9, 9 to disturb the flow of refrigerant inside this first recessed portion 4. I'm doing it like that.

【0005】 積層型蒸発器を構成する複数のユニット2、2は、それぞれ上述の様な形状を 有する金属板1を2枚、各金属板の平坦部3同士を突き合わせ、最中状に組み合 わせる事で構成されており、第一凹部4により囲まれるU字形の部分を、冷媒を 流す扁平管部12とし、第二、第三凹部5、6により囲まれる部分を、入口側タ ンク、或は出口側タンクの一部として機能させる様にしている。[0005] The plurality of units 2, 2 constituting the stacked evaporator each have the above-mentioned shape. Two metal plates 1 with the metal plates are butted against each other, and assembled in a middle shape. The U-shaped part surrounded by the first recess 4 is filled with refrigerant. The flat pipe part 12 for flowing water is defined as the part surrounded by the second and third recesses 5 and 6 as the inlet side tap. It is designed to function as a tank or part of the outlet tank.

【0006】 上述の様なユニット2、2は、図4に示す様に複数個、各ユニット2、2を構 成する金属板1、1の第二、第三凹部5、6の外面同士を突き合わせる事で積層 し、第二、第三凹部5、6により構成される1対の空間の内の一方の空間に入口 管10を、他方の空間に出口管11を、それぞれ接続している。[0006] The above-mentioned units 2, 2 are configured by a plurality of each unit 2, 2 as shown in FIG. The metal plates 1 and 1 are laminated by butting the outer surfaces of the second and third recesses 5 and 6 together. and an entrance to one of the pair of spaces constituted by the second and third recesses 5 and 6. A pipe 10 is connected to the other space, and an outlet pipe 11 is connected to the other space.

【0007】 この様に複数のユニット2、2を積層した状態で、隣り合うユニット2、2の 扁平管部12、12の間には、コルゲート型のフィン13、13を挟持し、隣り 合う扁平管部12、12の間を流れる空気と、各扁平管部12、12の内側を流 れる冷媒との間の熱交換が良好に行なわれる様にしている。[0007] With multiple units 2, 2 stacked in this way, adjacent units 2, 2 Corrugated fins 13, 13 are sandwiched between the flat tube parts 12, 12, and the adjacent Air flows between the flat tube parts 12, 12 that match, and air flows inside each flat tube part 12, 12. This ensures good heat exchange between the refrigerant and the refrigerant.

【0008】 積層型蒸発器は、上述の様に構成され、造られる為、入口管10から、入口側 タンクとして機能する一方の空間に気液2相状態の冷媒を送り込むと、この冷媒 は、複数のユニット2、2の扁平管部12、12を流れる間に、扁平管部12、 12の外に設けたフィン13、13の間を流通する空気との間で熱交換を行なう 事により蒸発してから、出口側タンクとして機能する他方の空間に送られ、出口 管11を通じて排出される。[0008] Since the stacked evaporator is configured and manufactured as described above, from the inlet pipe 10, the inlet side When a gas-liquid two-phase refrigerant is sent into one space that functions as a tank, this refrigerant While flowing through the flat tube portions 12, 12 of the plurality of units 2, 2, the flat tube portion 12, Heat exchange is performed with the air flowing between the fins 13 and 13 provided outside the fins 12. After evaporating due to the It is discharged through pipe 11.

【0009】 ところで、上述の様に構成され作用する積層型蒸発器の製造を容易にする為、 2枚の金属板を重ね合わせて成るユニットとタンクとを別体とする事が、特開昭 61−27496号公報に開示されている。[0009] By the way, in order to facilitate the manufacture of a stacked evaporator constructed and operated as described above, The idea of separating the tank and the unit made of two overlapping metal plates was discovered in JP-A-Sho. It is disclosed in Japanese Patent No. 61-27496.

【0010】 即ち、図4〜6に示した従来構造の場合、各ユニット2、2の端部にタンクを 一体に形成する為、各ユニット2、2を構成する金属板1、1の端部に深い第二 、第三凹部5、6を形成しているが、これら第二、第三凹部5、6を形成する為 のプレス作業は、浅い第一凹部4を形成するのと同時に行なう必要がある為、プ レス作業の際に大きな力が必要となり、金属板1をプレス成形する為の設備が大 型化して、設備費が嵩む事が避けられない。0010 That is, in the case of the conventional structure shown in Figs. 4 to 6, a tank is installed at the end of each unit 2, 2. Because it is integrally formed, there is a deep second groove at the end of the metal plates 1, 1 that make up each unit 2, 2. , the third recesses 5 and 6 are formed, but in order to form these second and third recesses 5 and 6. The pressing operation of 2 must be performed at the same time as forming the shallow first recess 4. A large amount of force is required during the pressing process, and the equipment required to press-form the metal plate 1 is large. It is unavoidable that the equipment costs will increase due to the standardization.

【0011】 この様な問題を解決する為、タンク別体型の積層型蒸発器の場合、図7〜9に 示す様に、一端縁に互いに間隔をあけて1対の突出部14a、14bを形成した 金属板15の片面にU字形の凹部16を、この凹部16の両端を上記1対の突出 部14a、14bの端縁に迄連続させた状態で形成している。上記凹部16の内 側には多数の突起17、17を形成し、凹部16により構成される折り返し流路 18の内側を流れる冷媒の流れを乱し、この冷媒と金属板15との間の熱交換が 効率良く行なわれる様にしている。[0011] In order to solve such problems, in the case of a stacked evaporator with a separate tank, the steps shown in Figures 7 to 9 are shown. As shown, a pair of protrusions 14a and 14b are formed at one end with a space between them. A U-shaped recess 16 is formed on one side of the metal plate 15, and both ends of the recess 16 are formed with the pair of protrusions described above. It is formed so as to be continuous up to the edges of the portions 14a and 14b. Inside the recess 16 A large number of protrusions 17, 17 are formed on the side, and a folded channel formed by a recess 16 is formed. This disturbs the flow of the refrigerant flowing inside the refrigerant 18 and prevents heat exchange between the refrigerant and the metal plate 15. We make sure that it is done efficiently.

【0012】 この様な凹部16や突起17、17を有する金属板15は、特開平2−169 127号公報に示されている様に、長尺な金属板を1対のロールの間を通過させ る事で、上記凹部16や突起17、17を成形した後、上記長尺な金属板の適当 箇所を切断する事で造れる為、製造装置が比較的簡単なもので済む様になる。0012 A metal plate 15 having such a recess 16 and protrusions 17, 17 is disclosed in Japanese Patent Application Laid-Open No. 2-169. As shown in Publication No. 127, a long metal plate is passed between a pair of rolls. After forming the recesses 16 and protrusions 17, 17, the long metal plate is Since it can be manufactured by cutting the parts, the manufacturing equipment can be relatively simple.

【0013】 そして、この様な金属板15を用いて造る、タンク別体型の積層型蒸発器の場 合、この金属板15、15を2枚1組とし、互いの凹部16、16同士を対向さ せた状態で最中状に重ね合わせて互いに液密に接合する事により、U字形の折り 返し流路18と、この流路18の両端に位置して端縁部から突出した1対の接合 部19a、19bとを有する素子20、20とする。[0013] In the case of a stacked evaporator with a separate tank, which is made using such a metal plate 15, In this case, the metal plates 15, 15 are made into a set of two, and the recessed portions 16, 16 are placed opposite each other. By overlapping each other in the middle and joining them liquid-tightly, a U-shaped fold is created. A return channel 18 and a pair of joints located at both ends of this channel 18 and protruding from the edge. It is assumed that elements 20 and 20 have portions 19a and 19b.

【0014】 そして、複数の素子20、20のそれぞれの接合部19a、19bを、第一、 第二のタンク21、22の側面にそれぞれ形成した、スリット状の接続孔23、 23に挿入すると共に、各接合部19a、19bの外周面と各接続孔23、23 の内周縁とを互いに液密にろう付け接合する。各タンク21、22は、それぞれ 図7に示す様な底板33と天板34とを最中状に組み合わせ、互いに液密にろう 付けする事で構成されており、上記接続孔23、23は、底板33の底面に形成 されている。これと共に、隣り合う素子20、20の間にフィン(図示せず)を 設ける。[0014] Then, the respective joint portions 19a and 19b of the plurality of elements 20 and 20 are connected to the first Slit-shaped connection holes 23 formed on the sides of the second tanks 21 and 22, respectively; 23, and the outer peripheral surface of each joint portion 19a, 19b and each connection hole 23, 23. and the inner circumferential edges thereof are liquid-tightly brazed to each other. Each tank 21, 22 is A bottom plate 33 and a top plate 34 as shown in Fig. 7 are combined in a middle shape and soldered together liquid-tightly. The connection holes 23, 23 are formed on the bottom surface of the bottom plate 33. has been done. Along with this, a fin (not shown) is provided between the adjacent elements 20, 20. establish.

【0015】 上記第一のタンク21の内側は、中間部に固定した隔壁24により仕切る事で 、入口室25と出口室26とに分割し、入口室25の側に冷媒送り込み口27を 、出口室26の側に冷媒取り出し口28を、それぞれ設けている。[0015] The inside of the first tank 21 can be partitioned by a partition wall 24 fixed at the middle part. It is divided into an inlet chamber 25 and an outlet chamber 26, and a refrigerant inlet 27 is provided on the side of the inlet chamber 25. , a refrigerant outlet 28 is provided on the side of the outlet chamber 26, respectively.

【0016】 上述の様に構成されるタンク別体型の積層型蒸発器の場合、第一、第二のタン ク21、22と複数の素子20、20に設けた折り返し流路18とから成る空間 の内側を、図10に示す様に、第一、第二、第三、第四の四室に分割する事が出 来る。[0016] In the case of a stacked evaporator with separate tanks configured as described above, the first and second tanks A space consisting of channels 21 and 22 and a folded passage 18 provided in a plurality of elements 20 and 20. The inside of the chamber can be divided into four chambers, the first, second, third, and fourth, as shown in Figure 10. come.

【0017】 即ち、第一のタンク21の片半部(図8の左半部)に存在する入口室25と一 部(同図の左半分)の素子20、20の上流側半部とから成る第一室29と、こ の第一室29の下流側に設けられ、上記一部の素子20、20の下流側半部と第 二のタンク22の片半部(同図の左半部)とから成る第二室30と、この第二室 30の下流側(同図の右側)に設けられ、第二のタンク22の他半部(同図の右 半部)と残部(同図の右半分)の素子20、20の上流側半部とから成る第三室 31と、この第三室31の下流側に設けられ、第一のタンク21の他半部(同図 の右半部)と残部の素子20、20の下流側半部とから成る第四室32とである 。[0017] That is, the inlet chamber 25 existing in one half of the first tank 21 (the left half in FIG. 8) and the a first chamber 29 consisting of an upstream half of the elements 20 and 20 (left half in the figure); is provided on the downstream side of the first chamber 29 of the a second chamber 30 consisting of one half of the second tank 22 (left half in the figure); 30 (on the right side in the figure), and the other half of the second tank 22 (on the right side in the figure). a third chamber consisting of a half part) and a half part on the upstream side of the elements 20 and 20 in the remaining part (right half in the figure); 31, and the other half of the first tank 21 (in the same figure) is provided downstream of this third chamber 31. (the right half of) and the downstream half of the remaining elements 20, 20. .

【0018】 この様な第一〜第四室29〜32に分割される積層型蒸発器に、図10に矢印 aで示す様に、冷媒送り込み口27から冷媒を送り込むと、この冷媒は、同図に 矢印bで示す様に第一室29内を流れ、一部の素子20、20の折り返し流路1 8の折り返し部分を、同図に矢印cで示す様に流れて、第二室30に進入する。[0018] In such a stacked evaporator divided into the first to fourth chambers 29 to 32, the arrows in Figure 10 As shown in a, when refrigerant is sent from the refrigerant inlet 27, this refrigerant is As shown by arrow b, it flows in the first chamber 29, and some of the elements 20, 20 turn around in the flow path 1. 8, it flows as shown by arrow c in the figure and enters the second chamber 30.

【0019】 第二室30内を矢印dで示す様に流れ、この第二室30の下流側端部に迄流れ た冷媒は、次いで、第二のタンク22内を、このタンク22の軸方向に亙って図 10の矢印e方向に流れて、第三室31内に進入した後、この第三室31を構成 する残部の素子20、20の折り返し流路18内を、同図に矢印fで示す様に流 れる。[0019] It flows in the second chamber 30 as shown by the arrow d, and flows to the downstream end of the second chamber 30. The refrigerant then flows inside the second tank 22 in the axial direction of this tank 22. After flowing in the direction of arrow e of 10 and entering the third chamber 31, this third chamber 31 is formed. The flow inside the folded channel 18 of the remaining elements 20, 20 is as shown by the arrow f in the same figure. It will be done.

【0020】 更に冷媒は、同図に矢印gで示す様に、残部の素子20、20の折り返し流路 18の折り返し部分を流れて、第四室32に進入し、この第四室32内を矢印h で示す様に流れる。[0020] Furthermore, the refrigerant flows through the folded passages of the remaining elements 20, 20, as shown by arrow g in the figure. 18, enters the fourth chamber 32, and follows the arrow h inside this fourth chamber 32. It flows as shown in .

【0021】 そして、この第四室32の下流側端部に存在する、第一のタンク21の他半部 (図8の右半部)に迄流れた冷媒は、次いで冷媒取り出し口28から、同図に矢 印iで示す様に流出する。[0021] The other half of the first tank 21 located at the downstream end of the fourth chamber 32 The refrigerant that has flowed to the right half of Fig. 8 is then sent from the refrigerant outlet 28 to the It flows out as shown by mark i.

【0022】[0022]

【考案が解決しようとする課題】[Problem that the idea aims to solve]

ところが、上述の様に構成され作用する、特開平2−169127号公報に開 示された積層型蒸発器の場合も、依然として、次に述べる様な解決すべき問題点 が存在する。 However, the method disclosed in Japanese Patent Application Laid-open No. 2-169127, which is configured and operates as described above, Even in the case of the stacked evaporator shown, there are still problems to be solved as described below. exists.

【0023】 即ち、互いに平行な複数の流路(折り返し流路18に相当する。)を有する蒸 発器に、十分な性能を発揮させる為には、各流路内を流れる冷媒の量が均一であ る事が必要であり、互いに平行な複数の流路の内の一部に多量の冷媒が流れ、残 りの流路に流れる冷媒の量が少なくなった場合、蒸発器全体としての熱交換量が 確保出来ず、蒸発器の性能が悪くなってしまう。[0023] That is, a vaporizer having a plurality of channels (corresponding to the folded channels 18) parallel to each other. In order for the generator to exhibit sufficient performance, the amount of refrigerant flowing through each channel must be uniform. It is necessary for a large amount of refrigerant to flow through some of the multiple flow paths parallel to each other, and the remaining If the amount of refrigerant flowing through the flow path decreases, the amount of heat exchanged by the evaporator as a whole will decrease. If this is not possible, the performance of the evaporator will deteriorate.

【0024】 これに対し、前述の様に構成され作用する積層型蒸発器の場合、必ずしも各流 路内を流れる冷媒の量を均一化する事が出来ない。[0024] On the other hand, in the case of a stacked evaporator constructed and operated as described above, each stream is not necessarily It is not possible to equalize the amount of refrigerant flowing through the passage.

【0025】 例えば、冷媒送り込み口27は、前記第一のタンク21の片半部の中央部分に 設けられているが、この冷媒送り込み口27から上記片半部内に送り込まれた冷 媒は、冷媒送り込み口27に近い、片半部中央部分に開口した流路に多く流入し 、冷媒送り込み口27から遠い、片半部両端寄りに開口した流路への流入量は少 なくなってしまう。[0025] For example, the refrigerant inlet 27 is located in the center of one half of the first tank 21. Although the refrigerant feed port 27 is provided in the above-mentioned half, A large amount of the medium flows into the channel opened in the center of one half, which is close to the refrigerant inlet 27. , the amount of inflow into the flow path that is far from the refrigerant inlet 27 and opened toward both ends of one half is small. It's gone.

【0026】 又、第二室30の下流端に達した冷媒が、図10に矢印eで示す様に流れて、 第三室31の上流端に達する際、矢印e方向に流れる冷媒の圧力は下流側程高く なる為、第三室31を構成する複数の折り返し流路18、18に送り込まれる冷 媒の量は、図11に示す様に、下流側(図10、11の右側)に存在する折り返 し流路18程多くなってしまう。[0026] Furthermore, the refrigerant that has reached the downstream end of the second chamber 30 flows as shown by arrow e in FIG. When reaching the upstream end of the third chamber 31, the pressure of the refrigerant flowing in the direction of arrow e is higher downstream. Therefore, the cooling that is sent into the plurality of folded channels 18, 18 that constitute the third chamber 31 is As shown in Figure 11, the amount of medium is However, the number of channels increases by about 18.

【0027】 特に、前述の様に構成される積層型蒸発器の場合、図12に示す様に、各素子 20に形成した接合部19a(19b)の先端部が、第一(第二)のタンク21 (22)内に突出し、この突出部分が堰として機能する事で、冷媒の流れに対す る抵抗となる為、積層型蒸発器内を冷媒が流れる抵抗が大きく、この積層型蒸発 器内を流れる冷媒の量を多く出来ないだけでなく、冷媒の流れが偏る傾向が強い 。[0027] In particular, in the case of a stacked evaporator configured as described above, each element is The tip of the joint 19a (19b) formed in the first (second) tank 21 (22), and this protruding part functions as a weir to prevent the flow of refrigerant. This creates a large resistance to the flow of refrigerant in the stacked evaporator. Not only is it not possible to increase the amount of refrigerant flowing inside the vessel, but the flow of refrigerant tends to be uneven. .

【0028】 冷媒の偏りを解消する為には、第一のタンク21の入口室25に通じる冷媒送 り込み口27の取付位置や流路面積、出口室26に通じる冷媒取り出し口28の 取付位置や流路面積を工夫したり、或は第一のタンク21内に固定する隔壁24 の位置を工夫する事で、或る程度対応する事は出来るが、素子20、20の積層 数を多くした、比較的大型の蒸発器の場合、これらの処置では十分に流量の偏り を少なくする事が出来ない。[0028] In order to eliminate the imbalance of refrigerant, it is necessary to The installation position and flow path area of the inlet port 27, and the refrigerant outlet port 28 leading to the outlet chamber 26. The mounting position and flow path area may be modified, or the partition wall 24 may be fixed within the first tank 21. Although it is possible to deal with this to some extent by devising the position of For relatively large evaporators with a large number of evaporators, these measures are sufficient to reduce flow bias. cannot be reduced.

【0029】 本考案の蒸発器は、上述の様な不都合を解消するものである。[0029] The evaporator of the present invention eliminates the above-mentioned disadvantages.

【0030】[0030]

【課題を解決する為の手段】[Means to solve the problem]

本考案の蒸発器は、それぞれ断面が扁平な流通部の端部を、タンクの側面に形 成したスリット状の接続孔に挿入し、各接続孔の内周縁と各流通部の外周面との 間をろう付けした蒸発器に於いて、上記流通部の端縁部で、上記タンクの内側に 挿入された部分を、円弧状に切り欠いた事を特徴としている。 In the evaporator of this invention, the ends of the flow sections, each with a flat cross section, are shaped into the side of the tank. Insert it into the slit-shaped connection hole that has been formed, and align the inner peripheral edge of each connection hole with the outer peripheral surface of each flow section. In an evaporator with a brazed space between the two, at the edge of the above-mentioned flow section, inside the above-mentioned tank. The inserted part is characterized by an arc-shaped cutout.

【0031】[0031]

【作用】 上述の様に構成される本考案の蒸発器により、蒸発器の内部を流れる冷媒と蒸 発器の外部を流れる空気との間で熱交換を行なう際の作用自体は、前述した従来 の蒸発器の場合と同様である。[Effect] By using the evaporator of the present invention configured as described above, the refrigerant flowing inside the evaporator and the evaporator are separated. The action itself when exchanging heat with the air flowing outside the generator is similar to the conventional method described above. The same is true for the evaporator.

【0032】 但し、本考案の蒸発器の場合、流通部の端縁部を円弧状に切り欠いている為、 上記流通部の端縁部による通液抵抗の増大が最小限に抑えられ、蒸発器内を流れ る冷媒の量を多く出来ると共に、冷媒の流れが偏る傾向を小さくして、蒸発器の 性能向上を図れる。[0032] However, in the case of the evaporator of the present invention, the edge of the flow section is cut out in an arc shape, so The increase in flow resistance due to the edges of the above-mentioned flow section is minimized, and the flow inside the evaporator is reduced to a minimum. In addition to increasing the amount of refrigerant in the evaporator, it also reduces the tendency for the refrigerant flow to become biased. Performance can be improved.

【0033】[0033]

【実施例】【Example】

図1〜3は本考案を積層型蒸発器に適用した例を示しているが、その構造は、 複数の素子20のそれぞれの接合部19a(19b)の端縁を円弧状に切り欠く 以外、前述した特開平2−169127号公報に開示された積層型蒸発器と同様 である為、重複する説明を省略し、以下本考案の特徴部分に就いて説明する。 1 to 3 show an example in which the present invention is applied to a stacked evaporator, whose structure is as follows: The edges of the joint portions 19a (19b) of each of the plurality of elements 20 are cut out in an arc shape. Other than that, it is the same as the stacked evaporator disclosed in the above-mentioned Japanese Patent Application Laid-Open No. 2-169127. Therefore, repeated explanations will be omitted and the characteristic parts of the present invention will be explained below.

【0034】 積層型蒸発器のコア部を構成する複数の素子20に設けられ、流通部である、 各素子20の折り返し流路18の両端に位置する接合部19a(19b)は、ス リット状の接続孔23を通じて、第一(第二)のタンク21(22)内に挿入さ れている。そして、上記接合部19a(19b)の端縁部には円弧状の切り欠き 35を設けて、第一(第二)のタンク21(22)内への、上記接合部19a( 19b)の突出量を少なくしている。[0034] Provided in a plurality of elements 20 constituting the core part of the stacked evaporator, and serving as a flow part. The joint portions 19a (19b) located at both ends of the folded channel 18 of each element 20 are Inserted into the first (second) tank 21 (22) through the lit-shaped connection hole 23. It is. An arc-shaped notch is provided at the edge of the joint portion 19a (19b). 35 is provided to connect the joint 19a (to the first (second) tank 21 (22)). The amount of protrusion of 19b) is reduced.

【0035】 この様に、折り返し流路18の端部に存在する接合部19a(19b)の端縁 部に円弧状の切り欠き35を設けた事により、上記接合部19a(19b)の端 縁部による通液抵抗の増大が最小限に抑えられる。この結果、積層型蒸発器内を 流れる冷媒の量を多く出来ると共に、冷媒の流れが偏る傾向を小さくして、積層 型蒸発器を通過した空気の温度分布を均一化して、この積層型蒸発器の性能向上 を図れる。[0035] In this way, the edge of the joint 19a (19b) existing at the end of the folded channel 18 By providing an arc-shaped notch 35 in the part, the end of the joint part 19a (19b) Increase in fluid flow resistance due to edges is minimized. As a result, inside the stacked evaporator In addition to increasing the amount of refrigerant that flows, it also reduces the tendency for the refrigerant flow to become uneven. The performance of this stacked evaporator is improved by uniformizing the temperature distribution of the air that passes through the stacked evaporator. can be achieved.

【0036】 尚、各接合部19a(19b)に形成する切り欠き35の大きさは、総て同じ でも或る程度積層型蒸発器の性能向上を図れるが、場所により切り欠き35の大 きさを異ならせれば、より性能向上を図る事が出来る。[0036] In addition, the size of the notch 35 formed in each joint part 19a (19b) is all the same. Although it is possible to improve the performance of the stacked evaporator to some extent, the size of the notch 35 may vary depending on the location. By varying the size, performance can be further improved.

【0037】 例えば、第一のタンク21の一方の側に形成された接続孔23内に挿入された 接合部19aの端縁を、図2に示した上記第一のタンク21の片半部中央に設け た冷媒送り込み口27からの距離xが小さい程大きく切り欠き、この冷媒送り込 み口27からの距離xが大きくなるに従って小さく切り欠く様にすれば、上記冷 媒送り込み口27から上記第一のタンク21の片半部内に送り込まれ、図2に矢 印で示す方向に流れる冷媒が、この片半部に一端を開口させた複数の折り返し流 路18、18内に、偏りなく流入する。[0037] For example, when inserted into the connection hole 23 formed on one side of the first tank 21 The edge of the joint portion 19a is provided at the center of one half of the first tank 21 shown in FIG. The smaller the distance x from the refrigerant inlet 27, the larger the notch becomes. If the cutout is made smaller as the distance x from the opening 27 increases, the above-mentioned cold The medium is fed into one half of the first tank 21 from the medium feeding port 27, and is shown by the arrow in FIG. The refrigerant flowing in the direction indicated by the mark forms multiple folded streams with one end open in this half. It flows evenly into the channels 18, 18.

【0038】 又、第二のタンク22(図8〜9)の下流側半部(第三室31(図10)の上 流端部)に形成された接続孔内に挿入された接合部19bの端縁を、上流側程大 きく切り欠く様にすれば、図3、10の矢印eで示す様に、上記第二のタンク2 2を上流側から下流側に流れる冷媒が、上記第二のタンク22の下流側半部に一 端を開口させた複数の折り返し流路18、18内に、偏りなく流入する。[0038] Also, the downstream half of the second tank 22 (Figs. 8 to 9) (above the third chamber 31 (Fig. 10) The edge of the joint 19b inserted into the connection hole formed in the flow end (flow end) is If the notch is sharply cut out, the second tank 2 will open as shown by arrow e in FIGS. The refrigerant flowing through the second tank 22 from the upstream side to the downstream side flows into the downstream half of the second tank 22. It flows evenly into the plurality of folded channels 18, 18 whose ends are open.

【0039】[0039]

【考案の効果】[Effect of the idea]

本考案の蒸発器は、以上に述べた通り構成され作用するが、蒸発器を構成する 、互いに並列な複数の流路中に流れる冷媒の量を、ほぼ等しくする事が出来、蒸 発器を通過した空気の温度分布の均一化を図って、蒸発器の性能向上を図る事が 出来る。 The evaporator of the present invention is constructed and operates as described above. It is possible to make the amount of refrigerant flowing in multiple channels parallel to each other almost equal. It is possible to improve the performance of the evaporator by making the temperature distribution of the air that has passed through the generator uniform. I can do it.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】接続部に切り欠きを形成した図8の拡大A−A
断面に相当する図。
[Fig. 1] Enlarged A-A of Fig. 8 with a notch formed in the connection part
A diagram corresponding to a cross section.

【図2】図10のB矢視に相当する図。FIG. 2 is a view corresponding to arrow B in FIG. 10;

【図3】図10のC矢視に相当する図。FIG. 3 is a view corresponding to arrow C in FIG. 10;

【図4】従来の積層型蒸発器の第1例を示す正面図。FIG. 4 is a front view showing a first example of a conventional stacked evaporator.

【図5】この蒸発器を構成する金属板の側面図。FIG. 5 is a side view of a metal plate constituting this evaporator.

【図6】図5のD−D断面図。FIG. 6 is a sectional view taken along line DD in FIG. 5;

【図7】従来の積層型蒸発器の第2例を示す部分分解斜
視図。
FIG. 7 is a partially exploded perspective view showing a second example of a conventional stacked evaporator.

【図8】同じく組み立てた状態を示す平面図。FIG. 8 is a plan view showing the same assembled state.

【図9】同じく側面図。FIG. 9 is a side view as well.

【図10】冷媒の流れを示す略斜視図。FIG. 10 is a schematic perspective view showing the flow of refrigerant.

【図11】冷媒が偏って流れる状態を示す、図10のE
−E断面に相当する図。
[Fig. 11] E in Fig. 10 showing a state in which the refrigerant flows unevenly.
-A diagram corresponding to the E cross section.

【図12】図8のA−A断面図。FIG. 12 is a sectional view taken along line AA in FIG. 8;

【符合の説明】[Explanation of sign]

1 金属板 2 ユニット 3 平坦部 4 第一凹部 5 第二凹部 6 第三凹部 7 通孔 8 通孔 9 凸部 10 入口管 11 出口管 12 扁平管部 13 フィン 14a 突出部 14b 突出部 15 金属板 16 凹部 17 突起 18 折り返し流路 19a 接合部 19b 接合部 20 素子 21 第一のタンク 22 第二のタンク 23 接続孔 24 隔壁 25 入口室 26 出口室 27 冷媒送り込み口 28 冷媒取り出し口 29 第一室 30 第二室 31 第三室 32 第四室 33 底板 34 天板 35 切り欠き 1 metal plate 2 units 3 Flat area 4 First recess 5 Second recess 6 Third recess 7 Through hole 8 Through hole 9 Convex part 10 Inlet pipe 11 Outlet pipe 12 Flat tube part 13 Fin 14a Projection part 14b Projection 15 Metal plate 16 Recess 17 Protrusion 18 Folded channel 19a Joint part 19b Joint 20 elements 21 First tank 22 Second tank 23 Connection hole 24 Bulkhead 25 Entrance room 26 Exit room 27 Refrigerant inlet 28 Refrigerant outlet 29 First room 30 Second room 31 Third room 32 Fourth room 33 Bottom plate 34 Top plate 35 Notch

Claims (4)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 それぞれ断面が扁平な流通部の端部を、
タンクの側面に形成したスリット状の接続孔に挿入し、
各接続孔の内周縁と各流通部の外周面との間をろう付け
した蒸発器に於いて、上記流通部の端縁部で、上記タン
クの内側に挿入された部分を、円弧状に切り欠いた事を
特徴とする蒸発器。
[Claim 1] The ends of the flow portions each having a flat cross section,
Insert into the slit-shaped connection hole formed on the side of the tank,
In an evaporator in which the inner circumferential edge of each connection hole and the outer circumferential surface of each circulation part are brazed, the part inserted inside the tank is cut into an arc shape at the edge of the circulation part. An evaporator characterized by the lack of.
【請求項2】 一端縁に、互いに間隔をあけて1対の突
出部を形成した金属板の片面にU字形の凹部を、この凹
部の両端を上記1対の突出部の端縁に迄連続させた状態
で形成すると共に、この金属板を2枚1組とし、互いの
凹部同士を対向させた状態で最中状に重ね合わせて互い
に液密に接合する事により、U字形の折り返し流路と、
この流路の両端に位置して端縁部から突出した1対の接
合部とを有する素子とし、複数の素子のそれぞれの接合
部を、第一、第二のタンクの側面にそれぞれ形成したス
リット状の接続孔に挿入して、各接合部の外周面と各接
続孔の内周縁とを互いに液密に接合すると共に、隣り合
う素子の間にフィンを設け、中間部を隔壁により仕切っ
た第一のタンクの一方の側に冷媒送り込み口を、他方の
側に冷媒取り出し口を、それぞれ設ける事で構成された
蒸発器に於いて、上記接合部の端縁で第一、第二のタン
クの内側に挿入された部分を、円弧状に切り欠いた事を
特徴とする蒸発器。
2. A U-shaped recess is formed on one side of a metal plate having a pair of protrusions spaced apart from each other on one edge, and both ends of the recess are continuous to the edges of the pair of protrusions. At the same time, these metal plates are made into a set of two, overlapped in the middle with their concave portions facing each other, and bonded liquid-tightly to each other to form a U-shaped folded flow path. and,
The element has a pair of joint parts located at both ends of the flow path and protruding from the edge, and each joint part of the plurality of elements is formed in a slit formed on the side surface of the first and second tanks. The outer circumferential surface of each joint part and the inner circumferential edge of each connection hole are liquid-tightly bonded to each other by being inserted into a shaped connection hole, and a fin is provided between adjacent elements and the middle part is partitioned off by a partition wall. In an evaporator configured by providing a refrigerant inlet on one side of the first tank and a refrigerant outlet on the other side, the first and second tanks are connected at the edge of the joint. An evaporator characterized by an arc-shaped cutout in the inner part.
【請求項3】 第一のタンクの一方の側に形成された接
続孔内に挿入された接合部の端縁を、冷媒送り込み口に
近い程大きく切り欠いた、請求項2に記載の蒸発器。
3. The evaporator according to claim 2, wherein the edge of the joint inserted into the connection hole formed on one side of the first tank is cut out to a larger extent closer to the refrigerant inlet. .
【請求項4】 第二のタンクの下流側半部に形成された
接続孔内に挿入された接合部の端縁を、上流側程大きく
切り欠いた、請求項2〜3の何れかに記載の蒸発器。
4. According to any one of claims 2 to 3, the edge of the joint inserted into the connection hole formed in the downstream half of the second tank is cut out to be larger toward the upstream side. evaporator.
JP1991030432U 1991-04-05 1991-04-05 Evaporator Expired - Fee Related JP2572083Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991030432U JP2572083Y2 (en) 1991-04-05 1991-04-05 Evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991030432U JP2572083Y2 (en) 1991-04-05 1991-04-05 Evaporator

Publications (2)

Publication Number Publication Date
JPH04117363U true JPH04117363U (en) 1992-10-21
JP2572083Y2 JP2572083Y2 (en) 1998-05-20

Family

ID=31914038

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991030432U Expired - Fee Related JP2572083Y2 (en) 1991-04-05 1991-04-05 Evaporator

Country Status (1)

Country Link
JP (1) JP2572083Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122988U (en) * 1989-03-11 1990-10-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122988U (en) * 1989-03-11 1990-10-09

Also Published As

Publication number Publication date
JP2572083Y2 (en) 1998-05-20

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