JPH0781760B2 - Multilayer evaporator - Google Patents
Multilayer evaporatorInfo
- Publication number
- JPH0781760B2 JPH0781760B2 JP60259308A JP25930885A JPH0781760B2 JP H0781760 B2 JPH0781760 B2 JP H0781760B2 JP 60259308 A JP60259308 A JP 60259308A JP 25930885 A JP25930885 A JP 25930885A JP H0781760 B2 JPH0781760 B2 JP H0781760B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- pipe
- flat
- flat tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003507 refrigerant Substances 0.000 claims description 257
- 238000009826 distribution Methods 0.000 claims description 45
- 238000005192 partition Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 description 15
- 230000000903 blocking effect Effects 0.000 description 13
- 238000005219 brazing Methods 0.000 description 12
- 238000001816 cooling Methods 0.000 description 10
- 238000010586 diagram Methods 0.000 description 9
- 239000002826 coolant Substances 0.000 description 7
- 229910052782 aluminium Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 238000004891 communication Methods 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Liquid Crystal Substances (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は例えば自動車用空調装置に使用されるエバポレ
ータの如き積層型蒸発器に関する。The present invention relates to a laminated evaporator such as an evaporator used in an air conditioner for automobiles.
[従来の技術] 従来の積層型蒸発器の一例としての、自動車用空調装置
に用いられるエバポレータの構造の概略を第16図と第17
図に、またエバポレータを構成する偏平管の細部構造を
第4図〜第7図に示した。エバポレータBは上端部に冷
媒入口ポート100a及び出口ポート100bを併設し、この両
ポート間を結ぶようにして管内にU字形の冷媒流路を形
成させた金属製偏平管100群をろう付け法によって偏平
方向に積層合体させることによって成り立っている。そ
して隣接偏平管の相互間には冷媒入口ポート100a(100
b)の厚さ分に相当する間隔Gが生じるので、この部分
に伝熱面積増大用のコルゲートフィン102を嵌合ろう付
けして熱交換用空隙として機能させている。偏平管100
の具体的な構造は本発明による熱交換器を構成する偏平
管1と本質的に異なる所はないので、偏平管1の構造説
明図としての第4図〜第7図を借りて概略を説明する
と、アルミ板をプレス加工して第4図の如き平面形状を
備えた全体として極く浅い盆状をなす2枚の管プレー1A
(1B)を用意し、丁度菓子の最中の皮を貼り合わせるよ
うにろう付け接合して形作られている。偏平な管内は下
端部が欠如している縦方向仕切壁1Cが存在することによ
って、管上端部に並設されている冷媒の入口ポート1aと
出口ポート1bを結ぶU字形の冷媒流路12Aと12Bが形成さ
れれいる。両ポート1aと1bにはそれぞれの管の偏平方向
の左右両端面に冷媒の流入または冷媒流通穴aが穿たれ
ている。[Prior Art] An outline of the structure of an evaporator used in an air conditioner for automobiles as an example of a conventional laminated evaporator is shown in Figs. 16 and 17.
The detailed structure of the flat tube constituting the evaporator is shown in FIGS. 4 to 7. The evaporator B is provided with a refrigerant inlet port 100a and an outlet port 100b at the upper end, and a group of metal flat tubes 100 having a U-shaped refrigerant channel formed in the tube by connecting these ports by brazing. It is formed by stacking and laminating in the flat direction. The refrigerant inlet port 100a (100
Since a gap G corresponding to the thickness of b) is generated, a corrugated fin 102 for increasing the heat transfer area is fitted and brazed to this portion to function as a heat exchange space. Flat tube 100
Since the specific structure of the flat tube is essentially the same as that of the flat tube 1 constituting the heat exchanger according to the present invention, the outline will be described with reference to FIGS. 4 to 7 as a structural explanatory view of the flat tube 1. Then, by pressing an aluminum plate, two tube play 1A having a plane shape as shown in FIG. 4 and forming an extremely shallow tray as a whole.
(1B) is prepared and formed by brazing and joining just like the skins in the middle of the confectionery. Due to the presence of the vertical partition wall 1C in which the lower end is absent in the flat pipe, a U-shaped refrigerant flow passage 12A connecting the inlet port 1a and the outlet port 1b of the refrigerant arranged in parallel at the upper end of the pipe is formed. 12B is formed. Both ports 1a and 1b are provided with a coolant inflow or coolant circulation hole a at both left and right end faces in the flat direction of the respective pipes.
エバポレータBの左右両側端に位置するそれぞれの偏平
管は管を形作る1組の管プレーの内、外側管プレートの
ポートが欠如しており、その代りに冷媒供給用配管103
または冷媒排出用配管104の継手部分103Aまたは104Aが
ろう付け結合されている。左右両端間の中間位置を占め
て隣接する1組の偏平管には各々の冷媒入口ポートの連
通を遮断するための冷媒流路遮断板120が冷媒流通穴a
を塞ぐようにして取付けられている。(もっとも実際は
穴aの欠如した偏平管100を用意するが、ここでは冷媒
流路の説明をわかりやすくするために遮断板として示し
た。) 前記の構造を備えた従来のエバポレータB内を冷媒が流
れる有様を模式的に示したのが第18図である。冷媒流路
は矢印によって流れ方向を示した流れ線として描かれて
いる。図中の110は偏平管100群の冷媒入口ポート100aの
冷媒流通穴aが相互に連通されることによって形成され
た冷媒分配路であり、111は同じく冷媒出口ポート100b
の冷媒流通穴aが相互に連通されることによって形成さ
れた冷媒集合路である。112Aと112Bは偏平管100内のU
字形冷媒流路を表しており、偏平管100の積層個数だけ
存在することになる。Each of the flat tubes located at the left and right ends of the evaporator B lacks the port of the outer tube plate in a set of tube forming tubes, and instead, the refrigerant supply piping 103
Alternatively, the joint portion 103A or 104A of the refrigerant discharge pipe 104 is brazed and connected. A pair of adjacent flat tubes occupying an intermediate position between the left and right ends is provided with a refrigerant passage blocking plate 120 for blocking communication of the respective refrigerant inlet ports.
Is installed so as to close the. (Although the flat tube 100 lacking the hole a is actually prepared, it is shown as a blocking plate here for the sake of easy understanding of the refrigerant flow path.) The inside of the conventional evaporator B having the above structure is filled with the refrigerant. FIG. 18 schematically shows the flow. The refrigerant flow path is drawn as a flow line whose flow direction is indicated by an arrow. In the figure, 110 is a refrigerant distribution path formed by mutually communicating the refrigerant circulation holes a of the refrigerant inlet port 100a of the flat tubes 100 group, and 111 is also the refrigerant outlet port 100b.
Is a refrigerant collecting path formed by communicating the refrigerant circulation holes a of each other. 112A and 112B are U in the flat tube 100
It represents a V-shaped refrigerant flow path, and there are as many flat tubes 100 as there are stacked layers.
エバポレータBの作動の概略を説明すると、車載冷凍機
のコンプレッサから吐出された高温高圧の気相冷媒は、
コンデンサに送り込まれて冷却液化し、一旦レシーバに
蓄えられる。レシーバから送出された液相冷媒は減圧装
置を通過させられることによって低圧の霧状体とはって
冷媒供給用配管103からエバポレータB内に流入し冷媒
分配路110(a)内に拡散した後、この分配路を構成し
ている各偏平管100の冷媒入口ポート100aからそれぞれ
の管のU字形冷媒流路112Aおよび112Bをたどって冷媒出
口ポート100bに到達し、ポート100bの集合からなる冷媒
集合路111(a)内で再び合流する。Explaining the outline of the operation of the evaporator B, the high-temperature and high-pressure gas-phase refrigerant discharged from the compressor of the vehicle-mounted refrigerator is
It is sent to the condenser, made into a cooling liquid, and temporarily stored in the receiver. The liquid-phase refrigerant sent from the receiver is passed through the decompression device, becomes a low-pressure atomized body, flows from the refrigerant supply pipe 103 into the evaporator B, and diffuses into the refrigerant distribution path 110 (a). , The refrigerant inlet port 100a of each flat tube 100 constituting this distribution path, reaches the refrigerant outlet port 100b from the refrigerant inlet ports 100a of the respective tubes, reaches the refrigerant outlet port 100b, and is a collection of the ports 100b. It merges again in the path 111 (a).
ところでこのエバポレータBは、先に述べたように積層
偏平管群100のうち両側端間の中間位置を占めて相隣る
1組の偏平管の冷媒入口ポート流通用穴aが遮断板120
によって塞がれているので、上記の冷媒分配路110
(a)の長さはエバポレータBの冷媒入口側端からこの
遮断板120までの長さ、つまりエバポレータBの冷媒の
入口および出口側端の間の距離の半分に相当することに
なる。従って前記の冷媒集合路111(a)の終端個所
は、上記の中間位置を占める偏平管100の冷媒出口ポー
ト100bに他ならない。この出口ポート100bは隣接偏平管
100の冷媒入口ポート100aに連通されることとなって、
この隣接偏平管100を含む下流側偏平管群100の冷媒入口
ポート100aの連続によって第2の冷媒分配路110(b)
が構成される。この分配路に一旦拡散した冷媒は、前記
と同様にして遮断板120の下流側の偏平管100群の冷媒出
口ポート100bによって構成される第2の冷媒集合路111
(b)に向けて各偏平管100内のU字形冷媒流路112Aお
よび112Bをたどらされる。冷媒集合路111(b)に集合
した冷媒はこの集合路の末端に連なる冷媒排出用配管10
4に排出されるが、エバポレータBへの流入時には霧化
液相状態であった冷媒はその時完全に蒸発気化してい
る。というのは積層状態をもって連接されている各偏平
管100内を順次通り抜ける間に、液相冷媒はこれらの偏
平管に接している熱交換用間隙Gに送風機の圧送力によ
って次々に送り込まれてくる温かい被空調空気から気化
の潜熱を吸収し冷房仕事を行うと共に自身は蒸発気化さ
せられるからである。エバポレータBから排出された気
相冷媒はコンプレッサに吸入され、高温高圧に圧縮され
る冷凍サイクルの最初の行程に帰着する。By the way, as described above, in the evaporator B, the refrigerant inlet port distribution holes a of the pair of flat tubes adjacent to each other occupying the intermediate position between the both ends of the laminated flat tube group 100 have the blocking plate 120.
Since it is blocked by the
The length (a) corresponds to the length from the refrigerant inlet side end of the evaporator B to the blocking plate 120, that is, half the distance between the refrigerant inlet side and outlet side ends of the evaporator B. Therefore, the end portion of the refrigerant collecting passage 111 (a) is none other than the refrigerant outlet port 100b of the flat tube 100 occupying the intermediate position. This outlet port 100b is an adjacent flat tube
It will be communicated with the refrigerant inlet port 100a of 100,
The second refrigerant distribution passage 110 (b) is formed by the continuation of the refrigerant inlet port 100a of the downstream flat tube group 100 including the adjacent flat tubes 100.
Is configured. The refrigerant once diffused in this distribution path is the second refrigerant collecting path 111 constituted by the refrigerant outlet port 100b of the group of flat tubes 100 on the downstream side of the blocking plate 120 in the same manner as described above.
The U-shaped refrigerant channels 112A and 112B in each flat tube 100 are traced toward (b). The refrigerant collected in the refrigerant collecting path 111 (b) is connected to the end of this collecting path by the refrigerant discharge pipe 10.
Although it is discharged to 4, the refrigerant that was in the atomized liquid phase state when flowing into the evaporator B is completely evaporated and vaporized at that time. That is, while sequentially passing through the flat tubes 100 that are connected in a laminated state, the liquid-phase refrigerant is successively sent into the heat exchange gap G that is in contact with these flat tubes by the force-feeding force of the blower. This is because the latent heat of vaporization is absorbed from the warm conditioned air to perform the cooling work, and at the same time it is vaporized and vaporized. The vapor-phase refrigerant discharged from the evaporator B is sucked into the compressor and is compressed to high temperature and high pressure, resulting in the first stroke of the refrigeration cycle.
[発明が解決しようとする問題点] 上記の如き構成を備えた従来のエバポレータBに冷媒流
路遮断板120を設けた理由は、もし古いタイプのエバポ
レータのように遮断板120が設けられていない場合に
は、エバポレータB内の冷媒流路Cは第19図に矢印付き
流線で示された状態となり、冷媒分配路110の長さは遮
断板120を設けたタイプのエバポレータBに較べて2倍
となって、この分配路110から冷媒を分配すべき偏平管1
00の数も2倍となり、当然に各偏平管への均等分配がそ
れだけ困難となるという問題を改善するためである。冷
媒供給用配管103から遠い位置にある偏平管100程、近い
位置を占める偏平管100に較べて冷媒供給量が少なくな
り、従って熱交換能力も低下すれば、エバポレータBは
その通風方向の横断面において空気冷却が不均等に行わ
れることとなって甚だ好ましくない。冷媒分配路110の
分配受け持ち偏平管数が減少すれば、それだけ各偏平管
への冷媒分配を均等に行い易くなるのは当然の理であ
る。[Problems to be Solved by the Invention] The reason why the refrigerant flow path blocking plate 120 is provided in the conventional evaporator B having the above-described configuration is that the blocking plate 120 is not provided like the old type evaporator. In this case, the refrigerant flow path C in the evaporator B is in the state shown by the streamline with an arrow in FIG. 19, and the length of the refrigerant distribution path 110 is 2 as compared with the evaporator B of the type having the blocking plate 120. The flat tube 1 in which the refrigerant should be distributed from this distribution path 110
This is to improve the problem that the number of 00s is doubled and naturally it becomes difficult to evenly distribute the flat tubes. If the flat tube 100 located farther from the refrigerant supply pipe 103 has a smaller amount of refrigerant supply than the flat tube 100 occupying the closer position, and therefore the heat exchange capacity also decreases, the evaporator B has a cross section in the ventilation direction. In this case, the air cooling is unevenly performed, which is extremely undesirable. It is a matter of course that, if the number of flat tubes in the refrigerant distribution path 110 is reduced, it becomes easier to equally distribute the refrigerant to the flat tubes.
しかしこのように改良された従来型エバポレータBには
新たに次のような問題が派生してくる。即ち前記に第18
図と第19図を比較してみれば理解されるように、冷媒流
路遮断板120付きの従来のエバポレータBでは、第1の
冷媒分配路110(a)から流通抵抗の大きいU字形冷媒
流路112Aおよび112Bを通り抜けて第1の冷媒集合路111
(a)に一旦たどりついた後、再び第2の冷媒分配路11
0(b)と第2の冷媒集合路111(b)との間に介在する
U字形冷媒流路を通過させられることになって、旧来型
エバポレータの冷媒流路Cに較べて冷媒は2倍の流通抵
抗を受けることとなり、冷媒側の圧力損失が増大し、冷
凍機のコンプレッサへの冷媒補給が円滑に行われず空調
装置の能力低下をきたすという不都合がある。However, the conventional evaporator B thus improved has the following new problems. That is,
As can be understood by comparing FIG. 19 and FIG. 19, in the conventional evaporator B with the refrigerant flow path blocking plate 120, the U-shaped refrigerant flow having a large flow resistance from the first refrigerant distribution path 110 (a). First refrigerant collecting passage 111 passing through passages 112A and 112B
After once reaching (a), the second refrigerant distribution passage 11 is again provided.
The U-shaped refrigerant flow passage interposed between 0 (b) and the second refrigerant collecting passage 111 (b) is passed, and the refrigerant is twice as much as the refrigerant flow passage C of the conventional evaporator. Therefore, there is an inconvenience that the pressure loss on the refrigerant side increases, the refrigerant cannot be smoothly replenished to the compressor of the refrigerator, and the capacity of the air conditioner deteriorates.
本発明は冷媒側圧力損失の増大を招くことなく、各偏平
管への冷媒の分配をより均等に行うことのできる積層型
蒸発器を提供することを目的とする。An object of the present invention is to provide a laminated evaporator capable of more evenly distributing the refrigerant to each flat tube without increasing the pressure loss on the refrigerant side.
[問題点を解決するための手段] 本発明は、一端側に冷媒入口ポートと冷媒出口ポートを
設けると共に管内に仕切壁を設け、これら両ポートを結
ぶU字形の冷媒流路を内部に形成させた偏平管群を積層
合体させてなる積層型蒸発器において、冷媒を供給する
冷媒供給管路を2つに分流する分流部と、該分流部の2
つの分流側と前記積層合体された前記偏平管群の両端の
偏平管の冷媒入口ポートとをそれぞれ同等の管路で接続
する2つの冷媒供給用配管とを備え、隣接する前記偏平
管の前記冷媒入口ポートを、前記積層合体された前記偏
平管群の中央部の隣接部を除いて、相互に連通させて2
つの冷媒分配路とするとともに、隣接する前記偏平管の
前記冷媒出口ポートを相互に連通させて冷媒集合路と
し、該冷媒集合路の中央部に冷媒排出用配管を接続した
ことを技術的手段とする。[Means for Solving the Problems] According to the present invention, a coolant inlet port and a coolant outlet port are provided at one end side, a partition wall is provided in a pipe, and a U-shaped coolant flow path connecting these ports is formed inside. In a laminated evaporator in which a group of flat tubes are laminated and combined, a diversion part that diverts a refrigerant supply pipe line that supplies a refrigerant into two parts, and a diversion part
Two refrigerant supply pipes that connect two branching sides and the refrigerant inlet ports of the flat tubes at both ends of the laminated flat tube group with equal pipelines, respectively, and the refrigerant of the adjacent flat tubes is provided. The inlet ports are communicated with each other, except for the adjoining portion of the central portion of the laminated flat tube group.
With one refrigerant distribution path, the refrigerant outlet ports of the adjacent flat tubes are made to communicate with each other to form a refrigerant collecting path, and a refrigerant discharging pipe is connected to a central portion of the refrigerant collecting path as a technical means. To do.
[作用] 上記の技術的手段により、本発明では、冷媒供給管路か
ら供給される冷媒は、分流部で2つの冷媒供給用配管に
分流されて、積層合体された偏平管群の両端の偏平管の
冷媒入口ポートからそれぞれ流入して、冷媒入口ポート
を連通させてなる冷媒分配路を積層方向の中央部に向か
い、また、その一部は、各偏平管において、冷媒分配路
としての冷媒入口ポートから分配されて冷媒流路を経て
冷媒出口ポートへ向かい、各冷媒流路を通過する間に熱
交換を行う。[Operation] According to the present invention, by the above technical means, the refrigerant supplied from the refrigerant supply pipe is divided into two refrigerant supply pipes in the flow dividing portion, and the flat pipes at both ends of the flat pipe group that are laminated and combined are flattened. The refrigerant inlet ports of the pipes respectively flow toward the refrigerant distribution passages communicating with the refrigerant inlet ports toward the central portion in the stacking direction, and some of them are refrigerant inlets as the refrigerant distribution passages in each flat pipe. The heat is exchanged while being distributed from the ports, passing through the refrigerant passages, toward the refrigerant outlet ports, and passing through the respective refrigerant passages.
冷媒出口ポートを連通してなる冷媒集合路の中央部には
冷媒排出配管が接続されているため、各偏平管において
冷媒流路を通過して各冷媒出口ポート側へ達した冷媒
は、冷媒集合路で合流しながら冷媒集合路を中央へ向か
って移動して、冷媒排出管から排出される。Since the refrigerant discharge pipe is connected to the central portion of the refrigerant collecting passage that communicates the refrigerant outlet ports, the refrigerant that has passed through the refrigerant flow path in each flat pipe and reached each refrigerant outlet port side is the refrigerant collecting passage. While merging in the passage, it moves toward the center of the refrigerant collecting passage and is discharged from the refrigerant discharge pipe.
従って、冷媒供給管路から供給されるすべての冷媒は、
分流部で分流されて冷媒供給用配管を通過した後には、
通過する偏平管がどれであっても、積層合体された偏平
管群の厚みの半分に相当する距離と、各偏平管の冷媒流
路の距離との和の分を通過することになる。Therefore, all the refrigerant supplied from the refrigerant supply line is
After being divided in the flow dividing portion and passing through the refrigerant supply pipe,
Whichever flat tube passes through, it will pass through the sum of the distance corresponding to half the thickness of the laminated flat tube group and the distance of the refrigerant flow path of each flat tube.
[実施例] 以下に付図に示す実施例に基づいて発明の具体的な構成
を説明する。[Examples] Specific configurations of the present invention will be described below based on examples shown in the accompanying drawings.
第1図〜第8図はそれぞれ第一実施例の説明図であっ
て、自動車用空気調和装置に使用するための積層型蒸発
器としてのエバポレータA1は、冷媒流路としての偏平管
1群をその偏平方向に積層合体させた構成を備えてい
る。FIG. 1 to FIG. 8 are explanatory views of the first embodiment, and an evaporator A1 as a laminated evaporator for use in an air conditioner for an automobile has a flat tube 1 group as a refrigerant flow path. It is provided with a structure in which they are laminated and united in the flat direction.
偏平管1は、第4図〜第7図にそれぞれ平面図、この平
面図の(イ)−(イ)、(ロ)−(ロ)および(ハ)−
(ハ)断面図として描かれた形状にプレス加工された、
全体として極く浅い盆状をなす2枚の管プレート1Aと1B
を各凹入側を対向させるようにして最中の皮状に貼り合
わせて成り立っている。管プレート1Aと1B(以下単に1A
という)は全く同一の形状寸法を有しており、例えばA3
003のアルミニウム板の表裏両面にA4004などのろう材を
あらかじめクラッドさせた素材を使用する。管プレート
1Aの上端部には冷媒入口ポート1aおよび冷媒出口ポート
1bとして機能する2つの膨出部が、絞り加工によって偏
平管1の外側向きに隣接させて形成されている。この両
ボートの側面にはそれぞれ冷媒の流入または流出用通路
穴aが穿たれている。また縦方向中心線に沿って偏平管
1内の空間を2分割するための仕切壁1Cが打出し成形さ
れているが、その下端部は欠如しているので偏平管1内
には冷媒入口ポート1aと冷媒出口ポート1bとを結ぶU字
形の冷媒竜路12Aと12Bが形成されている。1dおよび1eは
この冷媒竜路に迷路形状を与えて熱交換効率を向上させ
るための斜方向に配向させて設けた小さな打出しリブ群
である。管プレート1Aの周縁は2枚の管プレートの貼り
合わせ面となるフランジ状部1fによって囲繞されてい
る。また下端部は管の外方に向けて水平に屈折突出させ
てあり(図中の1h)、その突出端を更に下向きに屈折さ
せることによって隣接偏平管1とのろう付け接合用のフ
ランジ状貼り合わせ面1gを設けている。The flat tube 1 is a plan view in FIGS. 4 to 7, and (a)-(a), (b)-(b) and (c) -in these plan views.
(C) Pressed into the shape drawn as a sectional view,
Two tube plates 1A and 1B that form a very shallow tray as a whole
Is formed by sticking each of the recessed sides so as to face each other in the shape of a skin in the middle. Tube plates 1A and 1B (hereinafter simply 1A
Have exactly the same geometry, for example A3
Use a material in which a brazing material such as A4004 is previously clad on both sides of the aluminum plate of 003. Tube plate
At the upper end of 1A, the refrigerant inlet port 1a and the refrigerant outlet port
Two bulging portions functioning as 1b are formed adjacent to each other in the outward direction of the flat tube 1 by drawing. A passage hole a for inflow or outflow of the refrigerant is formed on the side surface of each of the boats. A partition wall 1C for dividing the space in the flat tube 1 into two along the longitudinal center line is stamped and formed, but the lower end is missing, so the flat tube 1 has a refrigerant inlet port inside. U-shaped coolant channels 12A and 12B connecting 1a and the coolant outlet port 1b are formed. 1d and 1e are small punching ribs arranged in a slanting direction in order to give a maze shape to the refrigerant dragon and improve heat exchange efficiency. The peripheral edge of the tube plate 1A is surrounded by a flange-shaped portion 1f which is a bonding surface of the two tube plates. In addition, the lower end is bent and protruded horizontally toward the outside of the pipe (1h in the figure), and by bending the protruding end further downward, a flange-like attachment for brazing with the adjacent flat pipe 1 is made. There is a mating surface of 1g.
このような構造を備えている多数枚の管プレート1Aを重
ね合せて第1図に側面図、第2図に上面図として描かれ
たようなエバポレータA1を組み立てるには、適宜の組立
用治具の一方の固定端面にまずエバポレータA1の両側端
の保護板となる両表面にろう材をクラッドさせてあるア
ルミ板製のサイドプレート9aを当てがったうえ、熱交換
面積増大用の薄いアルミニウム板製のコルゲートフィン
2を添わせ、ついで最外側に位置する偏平管の一方の管
プレートとなる変則的に平坦な形状のアルミニウム板製
エンドプレート9を当てがい、更に他方皮の管プレート
1Aを重ね合せた後、2つ目のコルゲートフィン2をこれ
に添わせたうえ2つ目の偏平管1を構成する管プレート
1Aを当てがうという具合にして図示の如き構造を備えた
エバポレータA1を仮組立し、治具によってこの状態を固
定させながらろう材の溶融温度にまで加熱されているろ
う付け炉に納めることによって、各構成部材は一挙に接
合されてエバポレータA1の本体部分が完了する。In order to assemble the evaporator A1 as shown in the side view in FIG. 1 and the top view in FIG. 2 by stacking a large number of tube plates 1A having such a structure, an appropriate assembly jig is used. First, apply one side plate 9a made of aluminum plate with brazing material clad on both surfaces to be protective plates at both ends of the evaporator A1 to one fixed end face, and thin aluminum plate for increasing heat exchange area. A corrugated fin 2 made of aluminum is added, and then an end plate 9 made of an aluminum plate having an irregularly flat shape, which is one of the outermost flat tubes, is applied.
After stacking 1A, the second corrugated fin 2 is attached to it, and the second flat plate 1 is constructed.
Temporarily assemble the evaporator A1 with the structure shown in the figure by applying 1A, and fix it in this state with a jig and place it in the brazing furnace heated to the melting temperature of the brazing material. , The constituent members are joined at once to complete the main body of the evaporator A1.
このろう付け接合行程において、各偏平管1を構成する
2枚の管プレート1Aは、変更するリブ分1dおよび1eの対
向する者同志の頂面がX字状に交叉する状態をもってろ
う付け接合されるでの、高い冷媒蒸気圧にも耐えられる
強い管構造が得られる。In this brazing process, the two tube plates 1A forming each flat tube 1 are brazed with the ribs 1d and 1e to be changed in such a manner that the top surfaces of the opposing members cross in an X shape. Therefore, a strong pipe structure that can withstand high refrigerant vapor pressure can be obtained.
また隣接偏平管1のそれぞれの冷媒入口ポート1aまたは
出口ポート1bの側面は相互に貼り合わせろう付けされる
ので、第2図に破線で示されているように、冷媒入口ポ
ート1a群がそれぞれの通路穴aを介して連通されること
によって冷媒分配路10が、また冷媒出口ポート1b群がそ
れぞれの通路穴aを介して連通されることによって冷媒
集合路11が形成される。ただしこの冷媒分配路10と集合
路11は第19図に示されている旧来型エバポレータの冷媒
流路Cとは異なって、共に中央部で分断される構成がと
られている。この実施例では、実は前記のエバポレータ
A1の組立方法の説明個所では記述を省いたが、中央部に
隣接して位置する1組の偏平管1は、それぞれ相対向す
る側の管プレートA1の冷媒の出入用ポート1aおよび1bが
取り除かれており、このポートの代わりとして冷媒排出
用配管5の取付用の各筒状をなす配管継手5Aが介在させ
てあり(第8図参照)、この配管継手5aが冷媒分配路10
の分断の役割を担う分断手段としての機能を果してい
る。冷媒分流の有様については後記する作動説明の個所
で述べる。Further, since the side faces of the respective refrigerant inlet ports 1a or the outlet ports 1b of the adjacent flat tubes 1 are brazed to each other by bonding, the groups of the refrigerant inlet ports 1a are connected to each other as shown by the broken line in FIG. A refrigerant distribution path 10 is formed by communicating through the passage holes a, and a refrigerant collecting path 11 is formed by communicating the refrigerant outlet ports 1b group through the passage holes a. However, unlike the refrigerant flow passage C of the conventional evaporator shown in FIG. 19, the refrigerant distribution passage 10 and the collecting passage 11 are both divided at the central portion. In this embodiment, in fact, the evaporator described above is used.
Although the description of the assembly method of A1 is omitted, one set of flat tubes 1 located adjacent to the central part has the refrigerant inlet / outlet ports 1a and 1b of the tube plates A1 on opposite sides removed. As a substitute for this port, a pipe joint 5A having a cylindrical shape for attaching the refrigerant discharge pipe 5 is interposed (see FIG. 8), and this pipe joint 5a is connected to the refrigerant distribution path 10.
It functions as a dividing means that plays the role of dividing. The state of the refrigerant split flow will be described later in the description of the operation.
エバポレータA1の本体の両側端面には、上記の冷媒分配
路10の両端にそれぞれ連通されるようにして、2本の冷
媒供給用配管3と4の各配管継手3Aと4Aが両端のエバポ
レータ9に各々ろう付け接合されている。6は2本の冷
媒供給用配管3と4の分流用継手、7はこの継手6に接
続された冷媒配管継手であり、8は冷媒排出用配管5の
入口側継手である。On both end surfaces of the main body of the evaporator A1, the pipe joints 3A and 4A of the two refrigerant supply pipes 3 and 4 are connected to the evaporator 9 at both ends so as to communicate with both ends of the refrigerant distribution passage 10 respectively. Each is brazed and joined. Reference numeral 6 is a flow dividing joint between the two refrigerant supply pipes 3 and 4, 7 is a refrigerant pipe joint connected to the joint 6, and 8 is an inlet side joint of the refrigerant discharge pipe 5.
第8図〜第12図に、冷媒供給用配管3と4および冷媒排
出用配管5をエバポレータA1の本体に取付ける方法を例
示した。8 to 12 exemplify a method of attaching the refrigerant supply pipes 3 and 4 and the refrigerant discharge pipe 5 to the main body of the evaporator A1.
第9図と第10図は冷媒供給用配管3または4の第1の取
付方法を描いており、パイプ状の配管4(または3)の
出口端を角筒状に変形加工することによって配管継手4A
を形作らせている。配管継手4Aの末端はキャップ体4Bに
よってろう付け封止されており、継手4Aがエバポレータ
の最外側の偏平管1の冷媒流通穴aに向けて当接される
面には、この穴aの口周縁に形成させた折り返し部を嵌
入させるためのくり抜き孔dが穿たれている。偏平管1
と配管継手4Aとの間にはサイドプレート9aの上辺部が挟
み込まれる。これら各部材を第2図に見られるように接
合させるのにはろう付けを行うが、このろう付け工程は
前述のエバポレータの組立行程に組み込んでもよいし、
別個の後行程としてもよい。FIG. 9 and FIG. 10 depict the first mounting method of the refrigerant supply pipes 3 or 4, and the pipe joint is formed by deforming the outlet end of the pipe pipe 4 (or 3) into a rectangular tube shape. 4A
Is shaped. The end of the pipe joint 4A is brazed and sealed by a cap body 4B, and the surface of the joint 4A abutting toward the refrigerant flow hole a of the outermost flat tube 1 of the evaporator is the opening of this hole a. A cutout hole d is formed for fitting the folded-back portion formed on the peripheral edge. Flat tube 1
The upper side portion of the side plate 9a is sandwiched between and the pipe joint 4A. Although brazing is performed to join each of these members as seen in FIG. 2, this brazing process may be incorporated in the above-described evaporator assembling step,
It may be a separate post process.
第11図は第2の取付方法を示している。冷媒供給用配管
4は末端部を90°折り曲げたうえ、この折り曲げ部にバ
ルジ加工によるツバ状膨出部4Dを形成させることによっ
て配管継手部が形作られている。このような冷媒供給用
配管4の末端をエバポレータA1のエンドプレート9に設
けてある配管取付孔eに挿し来んでろう付けすれば取付
が完了する。FIG. 11 shows the second mounting method. The end portion of the refrigerant supply pipe 4 is bent by 90 °, and the pipe joint portion is formed by forming a brim-shaped bulging portion 4D by bulging at this bent portion. The end of such a refrigerant supply pipe 4 is inserted into a pipe mounting hole e provided in the end plate 9 of the evaporator A1 and brazed to complete the mounting.
第8図と第12図は冷媒排出用配管5をエバポレータA1の
中央部に取付ける方法を示している。冷媒排出用配管5
の末端部は冷媒供給用配管4(または3)と同様に角筒
状をなすように変形加工されて配管継手5Aが形作られて
いる。5Bは継手5Aの末端部開口に嵌着ろう付けされてい
るキャップ体である。配管継手5Aの両側壁面には、それ
ぞれ冷媒集合路11を構成させるために各偏平管1のポー
トに穿たれている冷媒流通穴aと対向する位置に配管取
付孔eが穿たれており、配管継手5Aは冷媒集合路11に連
通される。この配管継手5AはエバポレータA1のろう付け
組立工程において、エバポレータの中央部に隣接して配
置された1組の偏平管1の間に介在させることによって
同時的に両隣りの偏平管1にろう付けされる。8 and 12 show a method of mounting the refrigerant discharge pipe 5 at the center of the evaporator A1. Refrigerant discharge pipe 5
The end portion of is deformed to form a rectangular tube like the refrigerant supply pipe 4 (or 3) to form a pipe joint 5A. Reference numeral 5B is a cap body which is brazed to the end opening of the joint 5A. Piping attachment holes e are formed on both side wall surfaces of the pipe joint 5A at positions facing the refrigerant circulation holes a formed in the ports of the flat tubes 1 to form the refrigerant collecting passages 11, respectively. The joint 5A communicates with the refrigerant collecting passage 11. In the brazing and assembling process of the evaporator A1, the pipe joint 5A is brazed to the flat tubes 1 on both sides at the same time by interposing it between a pair of flat tubes 1 arranged adjacent to the center of the evaporator. To be done.
つぎに上記第一実施例エバポレータA1の作動を、その冷
媒流路図としての第3図および第1図、第2図を参照し
ながら説明する。既述の如くして冷媒の減圧装置から配
管を経て分流用継手6の個所に到達した減圧霧化冷媒
は、2本の冷媒供給用配管3と4に分流されてエバポレ
ータA1の両側端に位置する各々の配管継手3Aおよび4Aか
ら冷媒分配路10の両端に同時に供給される。分配路10内
に流入した2つの冷媒の流れは共にその全長の中間位置
に到って前述の如く角筒状継手5Aの介在によって行く手
をはばまれる。従って2つに分断された各々の冷媒分配
路は、第19図にその冷媒流路を示した旧来型エバポレー
タに較べると、偏平管の個数が同じとした場合には、1/
2の個数の偏平管1への冷媒分配を受け持てば足りるこ
とになる。従って当然の結果として各偏平管1への冷媒
分配ははるかに均等に行われて、エバポレータA1はその
通風方向の横断面において空気冷却能力の片寄り分布傾
向を少なくすることができる。2群に分かれて偏平管1
内のそれぞれのU字形流路を通過する間に被冷却空気か
ら気化の潜熱を奪って冷房仕事を果し気相に戻った冷媒
は、同じく2群にまとまって冷媒集合路11に流入する
が、各群の集合路の末端はそれぞれ冷媒排出用配管5の
配管継手5Aに連通されているので、この継手5A内で合流
した気相冷媒は配管5をたどって冷凍機のコンプレッサ
に再吸入され、エバポレータA1への循環供給が行われ
た。Next, the operation of the evaporator A1 of the first embodiment will be described with reference to FIG. 3, FIG. 1, and FIG. As described above, the reduced pressure atomized refrigerant that has reached the location of the diversion joint 6 from the refrigerant pressure reducing device through the pipe is divided into the two refrigerant supply pipes 3 and 4 and is positioned at both ends of the evaporator A1. Are simultaneously supplied to both ends of the refrigerant distribution passage 10 from the respective pipe joints 3A and 4A. The flows of the two refrigerants that have flowed into the distribution passage 10 reach the intermediate position of their entire lengths and are blocked by the interposition of the rectangular tubular joint 5A as described above. Therefore, each of the refrigerant distribution passages divided into two is 1 / third when the number of flat tubes is the same as compared with the conventional evaporator whose refrigerant passage is shown in FIG.
It suffices to take charge of distributing the refrigerant to the two flat tubes 1. Therefore, as a matter of course, the distribution of the refrigerant to the flat tubes 1 is far more evenly performed, and the evaporator A1 can reduce the uneven distribution tendency of the air cooling capacity in the cross section in the ventilation direction. Flat tube divided into 2 groups 1
While passing through each of the U-shaped flow paths in the inside, the refrigerants that have lost the latent heat of vaporization from the air to be cooled, have performed cooling work, and returned to the gas phase, are likewise grouped into two groups and flow into the refrigerant collecting path 11. Since the end of the collecting passage of each group is communicated with the pipe joint 5A of the refrigerant discharge pipe 5, the gas-phase refrigerant that has merged in this joint 5A is traced through the pipe 5 and re-sucked into the compressor of the refrigerator. , And circulation supply to the evaporator A1 was performed.
ここで第18図に示された従来のエバポレータBの冷媒流
路と上記実施例のエバポレータA1の冷媒流路を描いた第
3図とを比較してみると、冷媒分配路110および10と冷
媒集合路111と11はそれぞれ2分割されているので、各
偏平管への冷媒の分配をより均等化させるという目的は
ほぼ同等に果されるが、エバポレータ内を通過する間に
冷媒が受ける流通抵抗の度合は全く相異している。第3
図中の20は冷媒分配路の分断手段を模式的に示した遮断
板で、実際には配管継手5Aがここに配置される。Now, comparing the refrigerant flow path of the conventional evaporator B shown in FIG. 18 with the refrigerant flow path of the evaporator A1 of the above embodiment shown in FIG. 3, the refrigerant distribution paths 110 and 10 and the refrigerant flow paths are compared. Since the collecting passages 111 and 11 are each divided into two, the purpose of making the distribution of the refrigerant to the flat tubes more equal is fulfilled almost the same, but the flow resistance received by the refrigerant while passing through the evaporator is fulfilled. The degree of is completely different. Third
Reference numeral 20 in the figure is a blocking plate that schematically shows the dividing means of the refrigerant distribution path, and the pipe joint 5A is actually disposed here.
偏平管の内部及び出入口部分は既に説明したように、冷
媒通路断面積とその形状が極めて複雑に変化するので、
当然のこととして大きな流通抵抗を及ぼすわけである
が、従来のエバポレータBでは冷媒分配路から冷媒集合
管に抜け出すのに2回偏平管を通過しなければならない
ので、冒頭に述べたように冷媒側の圧力損失は相当に大
きくならざるを得ず、冷凍機の目立った性能低下を招く
ことになるが、本発明によるエバポレータA1は旧来のエ
バポレータの冷媒流路と同様に偏平管1を唯一回通過さ
せられるだけなので、冷媒側圧力損失が増大する不利を
伴わずに上記の利点だけを獲得することができる。理論
的には本発明によるエバポレータA1は従来型エバポレー
タBに較べて冷媒の圧力損失を1/6〜1/8と著しく低減さ
せられると推論できる。As described above, the cross-sectional area of the refrigerant passage and its shape change extremely complicatedly inside the flat tube and the inlet / outlet portion.
As a matter of course, a great flow resistance is exerted, but in the conventional evaporator B, in order to escape from the refrigerant distribution passage to the refrigerant collecting pipe, it has to pass through the flat pipe twice, so that as described at the beginning, the refrigerant side However, the evaporator A1 according to the present invention passes through the flat tube 1 only once like the refrigerant flow path of the conventional evaporator. Only the above advantages can be obtained without the disadvantage that the pressure loss on the refrigerant side increases. Theoretically, it can be inferred that the evaporator A1 according to the present invention can significantly reduce the pressure loss of the refrigerant by 1/6 to 1/8 as compared with the conventional evaporator B.
第15図に本発明によるエバポレータA1と従来のエバポレ
ータBをそれぞれ組込んだ冷凍機の冷凍サイクルをモリ
エル線図として模式的に示した。グラフ(イ)はエバポ
レータA1について、またグラフ(ロ)はエバポレータB
について描かれたものであり、グラフ(ハ)は飽和液お
よび飽和蒸気線である。図中のA→B域は圧縮工程を、
B→Cは凝縮工程を、C→Dは膨張工程を、D→Eは蒸
発工程をそれぞれ示しており、A点はコンプレッサ吸入
口に、またE点はエバポレータ出口に相当する。この図
の意味する所は、エバポレータ通過による冷媒の圧力低
下ΔPは本発明エバポレータA1の圧力低下ΔP1の方が従
来のエバポレータBのΔP2よりはるかに少なく、従って
コンプレッサ吸入口A点における吸入圧もエバポレータ
A1の方が高められて冷凍サイクルを流れる冷媒の循環量
が増大し、冷凍効率が向上されるということである。図
中のΔiは冷媒の単位重量当りの冷房効果を表してお
り、冷房能力QはΔi×G(冷媒循環量)で表される。FIG. 15 schematically shows, as a Mollier diagram, a refrigeration cycle of a refrigerator in which the evaporator A1 according to the present invention and the conventional evaporator B are incorporated. Graph (a) is for evaporator A1, and graph (b) is for evaporator B.
The graph (C) is a saturated liquid and a saturated vapor line. Area A → B in the figure is the compression process,
B → C is a condensation process, C → D is an expansion process, and D → E is an evaporation process. Point A corresponds to the compressor inlet, and point E corresponds to the evaporator outlet. The meaning of this figure is that the pressure drop ΔP of the refrigerant due to passage through the evaporator is much smaller in the pressure drop ΔP1 of the evaporator A1 of the present invention than in the conventional evaporator B, and therefore the suction pressure at the compressor suction port A is also equal to that of the evaporator.
This means that A1 is increased to increase the circulation amount of the refrigerant flowing through the refrigeration cycle and improve refrigeration efficiency. Δi in the figure represents the cooling effect per unit weight of the refrigerant, and the cooling capacity Q is represented by Δi × G (refrigerant circulation amount).
第13図は本発明による第2実施例のエバポレータA2の斜
視図、第14図はその冷媒流路図であって、エバポレータ
の基本的な構造は第1実施例のエバポレータA1と全く同
一である。ただし両者の異なる点は第14図をエバポレー
タA1の冷媒流路図の第3図と比較してみれば理解される
ように、エバポレータA1では冷媒集合路11がその中央部
を境にして2路に分割されていたのが、エバポレータA2
では2分割された冷媒集合路11の各々を更に冷媒流路遮
断板21および22によって2分割する構成をとっている点
である。先にもことわっているように実際には遮断板21
および22の代りに、この板の置かれる個所に位置する偏
平管1の管プレート1Aに冷媒流通穴aを設けないように
している。FIG. 13 is a perspective view of the evaporator A2 of the second embodiment according to the present invention, and FIG. 14 is a refrigerant flow path diagram thereof, and the basic structure of the evaporator is exactly the same as that of the evaporator A1 of the first embodiment. . However, the difference between the two is understood by comparing FIG. 14 with FIG. 3 of the refrigerant flow path diagram of the evaporator A1, and in the evaporator A1, the refrigerant collecting path 11 is divided into two paths with the central part as a boundary. Evaporator A2 was divided into
Is that each of the refrigerant collecting passages 11 divided into two is further divided into two by refrigerant passage blocking plates 21 and 22. As I said earlier, it is actually a blocking plate 21
Instead of 22 and 22, the refrigerant flow hole a is not provided in the tube plate 1A of the flat tube 1 located at the place where this plate is placed.
この第2実施例エバポレータA2の作動上の特長は、冷媒
流路図としての第14図に示されているように、冷媒分配
路10が4つの流路に分断されたことによって、これら4
つの冷媒分配路が冷媒供給の役目を担うべき偏平管1の
数が、第1実施例のそれに較べて更に半減されることに
なり、エバポレータを構成する各偏平管1への冷媒の分
配が更により均等に行える点である。もっともこのエバ
ポレータA2では冷媒分配路から集合路に到達するまでに
2回U字形冷媒流路を通過しなければならず、冷媒圧力
の低下をいう不利を伴うことになるが、従来型エバポレ
ータBに較べれば流路が分割された効果によってこの圧
力低下の度合ははるかに小さく抑えることができる。The operational feature of the evaporator A2 of the second embodiment is that the refrigerant distribution passage 10 is divided into four passages as shown in FIG. 14 as a refrigerant passage diagram.
The number of the flat tubes 1 for which one refrigerant distribution path should play the role of supplying the refrigerant is further halved as compared with that in the first embodiment, and the distribution of the refrigerant to each flat tube 1 constituting the evaporator is further improved. This can be done evenly. However, in this evaporator A2, it has to pass through the U-shaped refrigerant flow path twice before it reaches the collecting path from the refrigerant distribution path, which is accompanied by a disadvantage that the pressure of the refrigerant decreases. In comparison, the degree of pressure drop can be suppressed to a much smaller degree by the effect of dividing the flow path.
上記の第1および第2実施例では冷媒供給用配管を冷媒
分配路の両側端に接続しているが、逆に冷媒排出用配管
を分流継手によって2路に分かち、各々の分流管の末端
を冷媒集合路の両側端に接続する一方、冷媒供給用配管
を冷媒分配路の中程に取付けるようにしてもよい。この
場合には冷媒供給用配管はエバポレータへの送風方向に
対して風下側に、また冷媒排出用配管は風上側に取付け
ることによって冷房効率が向上される。In the above-mentioned first and second embodiments, the refrigerant supply pipes are connected to both ends of the refrigerant distribution passage. On the contrary, the refrigerant discharge pipes are divided into two passages by the diversion joint, and the end of each diversion pipe is connected. While connecting to both ends of the refrigerant collecting passage, the refrigerant supply pipe may be attached in the middle of the refrigerant distributing passage. In this case, the cooling efficiency is improved by installing the refrigerant supply pipe on the leeward side and the refrigerant discharge pipe on the upwind side with respect to the direction of air blown to the evaporator.
次に第3実施例としてのエバポレータA3について第20図
〜第26図を参照しながら説明する。この実施例のエバポ
レータA3が前記の実施例エバポレータA1及びA2と異なる
点は、冷媒分配路10の分配手段としての冷媒入口ポート
の一方の連通路を封鎖した偏平管の使用を省略した点に
ある。それに伴って冷媒排出用配管5をエバポレータに
取付けるための配管継手5Aは不要化し配管取付け構造も
簡略化される。Next, an evaporator A3 as a third embodiment will be described with reference to FIGS. 20 to 26. The evaporator A3 of this embodiment is different from the evaporators A1 and A2 of the above embodiment in that the use of a flat tube that blocks one of the communication paths of the refrigerant inlet port as the distribution means of the refrigerant distribution path 10 is omitted. . Along with this, the pipe joint 5A for attaching the refrigerant discharge pipe 5 to the evaporator is not required and the pipe mounting structure is simplified.
積層された偏平管1群の中央部に位置する冷媒排出用配
管5の取付け用の偏平管201は基本的な構造において他
の偏平管1と全く同一である。唯異なる所は、この偏平
管201を構成する管プレート201Aの平面図としての第22
図および管プレート201Bの側面図としての第22−a図及
びエバポレータの冷媒排出用配管5の取付け部分の横断
面図としての第25図に示されている様に、冷媒出口ポー
ト201bに連通される様にして配管5の嵌合用フランジ部
202が管プレート201A及び201Bのプレス成形時に一体的
に形成させてある点である。冷媒排出用配管5の冷媒入
口側端はフランジ部202に嵌入された状態のもとにろう
付け固定される。尚201aは冷媒入口ポートであり、図中
の他の符号は前記実施例のそれと共通している。The flat tube 201 for mounting the refrigerant discharge pipe 5 located at the center of the stacked flat tube 1 group is completely the same as the other flat tubes 1 in the basic structure. The only difference is the 22nd plan view of the tube plate 201A that constitutes this flat tube 201.
As shown in FIG. 22-a as a side view of the tube plate 201B and as FIG. 25 as a cross-sectional view of a portion of the evaporator for installing the refrigerant discharge pipe 5, the refrigerant outlet port 201b is communicated with. The fitting flange of the pipe 5
The point 202 is that the tube plates 201A and 201B are integrally formed during press molding. The end of the refrigerant discharge pipe 5 on the refrigerant inlet side is fixed by brazing while being fitted in the flange portion 202. Reference numeral 201a is a refrigerant inlet port, and other reference numerals in the drawing are common to those in the above-described embodiment.
この実施例のエバポレータA3の作動をエバポレータ内の
冷媒の流れを模式的に描いた第26図を参照しながら説明
すると、エバポレータA3の両側端にそれぞれ取付けられ
ている冷媒供給用配管3及び4から流入した霧化冷媒
は、偏平管1群の各冷媒入口ポート1aの連接からなる冷
媒分配路に流入して前進しエバポレータA3の中央部に位
置する偏平管201の入口ポート201aに到って2つの冷媒
の圧力が拮抗している所から冷媒の流れは止まる。各偏
平管1の冷媒入口ポート1aと出口ポート1bとは既述の様
にU字形流路12A及び12Bを介して連通しているのでそれ
ぞれの入口ポート1aに行き亘った冷媒は低圧側の出口ポ
ート1bに向けてU字形冷媒流路内を通過し、この間に暖
かい空気から気化の潜熱を奪って冷却仕事を行う。各偏
平管1の冷媒出口ポート1bの連接からなる冷媒集合路11
に、第26図に見られる様に集合した2組の冷媒の流れは
エバポレータの中央部に位置する偏平管201の冷媒出口
ポート201bに到って合流し冷媒排出用配管5の末端に連
らなるコンプレッサの吸引力によって配管5から排出さ
れる。The operation of the evaporator A3 of this embodiment will be described with reference to FIG. 26 schematically showing the flow of the refrigerant in the evaporator. From the refrigerant supply pipes 3 and 4 attached to both side ends of the evaporator A3, respectively. The atomized refrigerant that has flowed in flows into the refrigerant distribution path formed by connecting the respective refrigerant inlet ports 1a of the group of flat tubes 1 and advances to reach the inlet port 201a of the flat tube 201 located at the center of the evaporator A3. The flow of the refrigerant stops where the pressures of the two refrigerants compete with each other. Since the refrigerant inlet port 1a and the outlet port 1b of each flat tube 1 are communicated with each other through the U-shaped passages 12A and 12B as described above, the refrigerant that has spread to the respective inlet ports 1a is the outlet on the low pressure side. It passes through the U-shaped refrigerant flow path toward the port 1b, and during this time, the latent heat of vaporization is taken from the warm air to perform the cooling work. Refrigerant collecting path 11 formed by connecting the refrigerant outlet ports 1b of the flat tubes 1
As shown in FIG. 26, the two sets of refrigerant flows reach the refrigerant outlet port 201b of the flat tube 201 located in the central portion of the evaporator and merge with each other to reach the end of the refrigerant discharge pipe 5. Is discharged from the pipe 5 by the suction force of the compressor.
従って既述の2つの実施例の様に、冷媒分配路又は集合
路を分断するために、冷媒入口ポートの片側の連通口を
塞いた偏平管を用意しなくても、おのずから冷媒分配路
及び集合路の流路が分断短縮されて本発明の目的とする
効果を得ることができる。Therefore, as in the two embodiments described above, it is not necessary to prepare a flat tube that blocks the communication port on one side of the refrigerant inlet port in order to divide the refrigerant distribution channel or the collecting channel, and the refrigerant distribution channel and the collecting channel are naturally prepared. The flow path of the passage is divided and shortened, and the effect intended by the present invention can be obtained.
上記のエバポレータA3は冷媒排出用配管5を中央部に又
冷媒供給用配管3及び4をエバポレータの両側端部に取
付けているが、これら両配管の取付け位置関係を逆転さ
せて前者を両側端部に接続させてもよい。In the evaporator A3 described above, the refrigerant discharge pipe 5 is attached to the central portion and the refrigerant supply pipes 3 and 4 are attached to both end portions of the evaporator. May be connected to.
[発明の効果] 上記の如き構成を備えた積層型蒸発器は、冷媒供給管か
ら供給される冷媒を2つに分流させて、それぞれ積層合
体された偏平管群の両端部から供給し、中央部から排出
させるようにし、その間で、冷媒分配路で各偏平管に供
給するようにしたので、一つの冷媒分配路当りの分配す
べき偏平管の受け持ち個数を少なくすることができて、
技術的に極めて困難だった各偏平管への冷媒分配をより
均等に行えるようになる。従って蒸発器の通風方向横断
面における冷却能力の不均等分布状態が改善されてより
均等に冷却された吹出空気流を得ることができる。[Effects of the Invention] In the laminated evaporator having the above-described structure, the refrigerant supplied from the refrigerant supply pipe is divided into two, and the refrigerant is supplied from both ends of the flat tube group which is laminated and integrated. Since it is configured to be discharged from each section, and in the meantime, each flat pipe is supplied through the refrigerant distribution path, the number of flat tubes to be distributed per one refrigerant distribution path can be reduced,
It becomes possible to more evenly distribute the refrigerant to each flat tube, which was technically extremely difficult. Therefore, the uneven distribution of the cooling capacity in the cross section in the ventilation direction of the evaporator is improved, and a more evenly cooled blown air flow can be obtained.
また冷媒分配路に流入した冷媒が偏平管内のU字形流路
をたどって冷媒集合路に達するまでに、従来型の冷媒分
配路分断手段を設けた蒸発器では、極めて通過抵抗の大
きいU字形流路を2回くぐり抜けなければならなかった
のに対して、本発明の蒸発器では唯一回通過させるだけ
なので、冷媒の圧力損失による冷凍機の冷房能力低下を
充分に低く抑えることができる。In addition, in the evaporator provided with the conventional refrigerant distribution path dividing means, the U-shaped flow having extremely large passage resistance is required until the refrigerant flowing into the refrigerant distribution path follows the U-shaped flow path in the flat pipe and reaches the refrigerant collecting path. Since the evaporator of the present invention only has to pass through the passage twice, the cooling capacity of the refrigerator due to pressure loss of the refrigerant can be sufficiently reduced.
第1図〜第8図はいずれも本発明の第1実施例図であっ
て、第1図は自動車用空調装置に組込まれるエバポレー
タとしての積層型蒸発器の正面図、第2図は上面図、第
3図は冷媒流路図、第4図はエバポレータを構成する偏
平管の構成部材としての管プレートの平面図、第5図、
第6図および第7図はそれぞれ第4図の(イ)−
(イ)、(ロ)−(ロ)、(ハ)−(ハ)断面図、第8
図はエバポレータの部分縦断面図である。第9図と第10
図は冷媒供給用配管の取付方法の説明図、第11図は同じ
く別の取付方法の説明図、第12図は冷媒排出用配管の取
付方法説明図である。 第13図は第2実施例のエバポレータの斜視図であり、第
14図はその冷媒流路図である。 第15図は従来のエバポレータと本発明によるエバポレー
タの各々のモリエル線図の比較図である。 第16図〜第18図はそれぞれ従来のエバポレータの側面
図、上面図、並びに冷媒流路図であり、第19図は旧来の
エバポレータの冷媒流路図である。 第20図〜第26図はいずれも第3実施例のエバポレータに
かかわる図であって、第20図は正面図、第21図は上面
図、第22図は中央部の偏平管を構成する管プレートの平
面図、第22−a図と第22−b図は第22図の側面図と
(ハ)−(ハ)断面図、第23図と第24図は第22図の
(イ)−(イ)断面図と(ロ)−(ロ)断面図、第25図
は冷媒排出用配管の取付け部分の横断面図、そして第26
図はエバポレータ内の冷媒流路の説明図である。 図中A1、A2……積層型蒸発器(エバポレータ)、1……
偏平管、2……コルゲートフィン、3、4……冷媒供給
用配管、5……冷媒排出用配管、10……冷媒分配路、11
……冷媒集合路、20〜22……冷媒分配路の分断手段、1a
……冷媒入口ポート、1b……冷媒出口ポート、1c……仕
切壁、12A+12B……U字形冷媒流路1 to 8 are all diagrams of the first embodiment of the present invention, in which FIG. 1 is a front view of a laminated evaporator as an evaporator incorporated in an automobile air conditioner, and FIG. 2 is a top view. 3, FIG. 3 is a refrigerant flow path diagram, FIG. 4 is a plan view of a tube plate as a constituent member of a flat tube which constitutes the evaporator, FIG.
FIGS. 6 and 7 are (a) -of FIG. 4, respectively.
(A), (b)-(b), (c)-(c) sectional view, 8th
The figure is a partial vertical cross-sectional view of the evaporator. Figures 9 and 10
FIG. 11 is an explanatory view of a method of mounting the refrigerant supply pipe, FIG. 11 is an explanatory view of another mounting method of the same, and FIG. 12 is an explanatory view of a method of mounting the refrigerant discharge pipe. FIG. 13 is a perspective view of the evaporator of the second embodiment.
FIG. 14 is a refrigerant flow path diagram thereof. FIG. 15 is a comparison diagram of Mollier diagrams of the conventional evaporator and the evaporator according to the present invention. 16 to 18 are a side view, a top view, and a refrigerant flow path view of a conventional evaporator, respectively, and FIG. 19 is a refrigerant flow path view of a conventional evaporator. 20 to 26 are all views relating to the evaporator of the third embodiment, wherein FIG. 20 is a front view, FIG. 21 is a top view, and FIG. 22 is a tube forming a flat tube in the central portion. The plan view of the plate, FIGS. 22-a and 22-b are the side view and (c)-(c) sectional view of FIG. 22, and FIGS. 23 and 24 are the (a) -of FIG. (A) Cross-sectional view and (b)-(b) cross-sectional view, FIG. 25 is a cross-sectional view of the mounting portion of the refrigerant discharge pipe, and FIG.
The figure is an illustration of a refrigerant flow path in the evaporator. In the figure, A1, A2 ... Multilayer evaporator (evaporator), 1 ...
Flat pipe, 2 ... Corrugated fins, 3, 4 ... Refrigerant supply pipe, 5 ... Refrigerant discharge pipe, 10 ... Refrigerant distribution passage, 11
...... Refrigerant collecting path, 20 to 22 ...... Refrigerant distribution path dividing means, 1a
…… Refrigerant inlet port, 1b …… Refrigerant outlet port, 1c …… Partition wall, 12A + 12B …… U-shaped refrigerant flow path
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 実開 昭54−38956(JP,U) 実開 昭51−83966(JP,U) 実開 昭52−150063(JP,U) 実開 昭56−28578(JP,U) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Bibliography Sho 54-38956 (JP, U) Rikai 51-83966 (JP, U) Rikai 52-150063 (JP, U) Rikai 56- 28578 (JP, U)
Claims (1)
を設けると共に管内に仕切壁を設け、これら両ポートを
結ぶU字形の冷媒流路を内部に形成させた偏平管群を積
層合体させてなる積層型蒸発器において、 冷媒を供給する冷媒供給管路を2つに分流する分流部
と、 該分流部の2つの分流側と前記積層合体された前記偏平
管群の両端の偏平管の冷媒入口ポートとそれぞれ同等の
管路で接続する2つの冷媒供給用配管とを備え、 隣接する前記偏平管の前記冷媒入口ポートを、前記積層
合体された前記偏平管群の中央部の隣接部を除いて、相
互に連通させて2つの冷媒分配路とするとともに、隣接
する前記偏平管の前記冷媒出口ポートを相互に連通させ
て冷媒集合路とし、該冷媒集合路の中央部に冷媒排出用
配管を接続したことを特徴とする積層形蒸発器。1. A flat tube group in which a refrigerant inlet port and a refrigerant outlet port are provided on one end side, a partition wall is provided in the pipe, and a U-shaped refrigerant channel connecting these ports is formed inside is laminated and combined. In the laminated evaporator, the diversion part that diverts the refrigerant supply pipe for supplying the refrigerant into two parts, and the refrigerant of the flat tubes at both ends of the flat tube group that is laminated and integrated with the two diversion sides of the diversion part An inlet port and two refrigerant supply pipes connected to each other by equivalent pipelines; and the refrigerant inlet ports of the adjacent flat tubes except for an adjoining portion of the central portion of the laminated flat tube group. And the two refrigerant distribution paths are communicated with each other, and the refrigerant outlet ports of the adjacent flat tubes are communicated with each other to form a refrigerant collecting path, and a refrigerant discharge pipe is provided at the center of the refrigerant collecting path. Characterized by being connected Layer type evaporator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60259308A JPH0781760B2 (en) | 1985-11-19 | 1985-11-19 | Multilayer evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60259308A JPH0781760B2 (en) | 1985-11-19 | 1985-11-19 | Multilayer evaporator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62119373A JPS62119373A (en) | 1987-05-30 |
| JPH0781760B2 true JPH0781760B2 (en) | 1995-09-06 |
Family
ID=17332270
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60259308A Expired - Lifetime JPH0781760B2 (en) | 1985-11-19 | 1985-11-19 | Multilayer evaporator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0781760B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010127510A (en) * | 2008-11-26 | 2010-06-10 | Sharp Corp | Heat exchanger |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0614782U (en) * | 1991-12-16 | 1994-02-25 | 日本軽金属株式会社 | Heat exchanger |
| JP4536243B2 (en) * | 2000-10-31 | 2010-09-01 | 株式会社ティラド | Heat exchanger for air conditioning |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5438956U (en) * | 1977-08-24 | 1979-03-14 |
-
1985
- 1985-11-19 JP JP60259308A patent/JPH0781760B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010127510A (en) * | 2008-11-26 | 2010-06-10 | Sharp Corp | Heat exchanger |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62119373A (en) | 1987-05-30 |
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