JPH0345303B2 - - Google Patents
Info
- Publication number
- JPH0345303B2 JPH0345303B2 JP58113737A JP11373783A JPH0345303B2 JP H0345303 B2 JPH0345303 B2 JP H0345303B2 JP 58113737 A JP58113737 A JP 58113737A JP 11373783 A JP11373783 A JP 11373783A JP H0345303 B2 JPH0345303 B2 JP H0345303B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- outlet pipe
- flow divider
- cylindrical body
- pipe
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
- F25B41/42—Arrangements for diverging or converging flows, e.g. branch lines or junctions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/028—Evaporators having distributing means
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Branch Pipes, Bends, And The Like (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は冷蔵庫、自動販売機、空気調和機等の
冷凍サイクルの蒸発器への冷媒を分流する冷媒分
流器に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigerant diverter that diverts refrigerant to an evaporator of a refrigeration cycle of a refrigerator, vending machine, air conditioner, or the like.
従来例の構成とその問題点
第1図は従来の冷媒分流器を示している。この
第1図を参考に従来の冷媒分流器について説明す
る。Configuration of conventional example and its problems FIG. 1 shows a conventional refrigerant flow divider. A conventional refrigerant flow divider will be explained with reference to FIG.
図において、1は冷媒分流器の本体で、上部に
凝縮器(図示せず)の出口と接続された配管2が
挿入される吸入口3が形成されている。また、本
体は下面を開口して前記吸入口3と連通した中空
部4が形成されている。5は前記本体1の下面を
覆う蓋でで2個の吐出口6,7を形成している。
この吐出口6,7には各蒸発器(図示せず)に接
続されたキヤピラリチユーブ8,9が取付られる
ものである。このとき、キヤピラリチユーブ8,
9の先端は中空部4に突出させるものであつた。 In the figure, reference numeral 1 denotes a main body of a refrigerant flow divider, and an inlet 3 is formed in the upper part thereof into which a pipe 2 connected to an outlet of a condenser (not shown) is inserted. Further, the main body has a hollow portion 4 that is open at the bottom and communicates with the suction port 3 . Reference numeral 5 denotes a lid that covers the lower surface of the main body 1 and forms two discharge ports 6 and 7.
Capillary tubes 8, 9 connected to respective evaporators (not shown) are attached to the discharge ports 6, 7. At this time, capillary tube 8,
The tip of 9 was made to protrude into the hollow part 4.
このようなもにおいて、吐出口6,7にキヤピ
ラリチユーブ8,9が設けられるため、絞り作用
が働き、吸入口3から流入する気液2相流は、分
流器の本体1内にて分離され、液冷媒が溜まるこ
ととなる。従つて、分流は液相のみで行なわれる
こととなる。しかし、均等な分流を行なうために
は、キヤピラリチユーブ8,9の先端を同一にそ
ろえる必要があり、ところが、蓋5の吐出口6,
7よりキヤピラリチユーブ8,9の挿入代をそろ
えることが難しいものであつた。そのため、キヤ
ピラリチユーブ8,9の先端の高さがことなり、
各蒸発器に流れる冷媒量が不均一となる欠点があ
つた。この冷媒量が不均一となると、もともと蒸
発器の能力をキヤピラリチユーブの抵抗により決
めているのに、冷媒量まで変つて能力が変つてし
まうものである。 In such a device, since the capillary tubes 8 and 9 are provided at the discharge ports 6 and 7, a throttling action is activated, and the gas-liquid two-phase flow flowing from the suction port 3 is separated within the main body 1 of the flow divider. This causes liquid refrigerant to accumulate. Therefore, the flow separation is performed only in the liquid phase. However, in order to divide the flow evenly, it is necessary to align the tips of the capillary tubes 8 and 9 to the same level.
7, it was more difficult to align the insertion distances of the capillary tubes 8 and 9. Therefore, the heights of the tips of the capillary tubes 8 and 9 are different,
There was a drawback that the amount of refrigerant flowing to each evaporator was uneven. If the amount of refrigerant becomes uneven, even though the capacity of the evaporator is originally determined by the resistance of the capillary tube, the capacity changes due to the amount of refrigerant.
また、本体1が傾けて設置された場合、夫々キ
ヤピラリチユーブの入口が異なるので分流にアン
バランスを生じることもあつた。 Further, when the main body 1 is installed at an angle, the inlets of the capillary tubes are different, which may cause imbalance in the divided flow.
発明の目的
本発明はこれらの欠点をとりのぞき、冷媒を均
等に分流することを目的とするものである。OBJECTS OF THE INVENTION The object of the present invention is to eliminate these drawbacks and to distribute the refrigerant evenly.
発明の構成
本発明は上記目的を達成するため、出口パイプ
を1本の直管より形成し、前記直管に切込みを設
けて、この切込みより折曲げ、端面高さをそろえ
ることにより、製造時の組立誤差をなくし、均等
な冷媒分流を得るものである。Structure of the Invention In order to achieve the above object, the present invention forms an outlet pipe from a single straight pipe, provides a notch in the straight pipe, and bends the straight pipe from the notch to make the end face heights uniform. This eliminates assembly errors and achieves even refrigerant distribution.
実施例の説明
以下に本発明の一実施例を図面を参考に説明す
る。DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
10は冷媒分流器の筒体で、上部に凝縮器(図
示せず)の出口と接続された配管2が挿入される
冷媒入口11が形成されている。また、筒体10
は下面を開口して、前記冷媒入口11と連通した
中空部12が形成されている。13,14は吐出
管であり、各蒸発器(図示せず)に接続されてい
る。この吐出管13,14は、1本のキヤピラリ
チユーブからなる出口パイプ15より成形され
る。 Reference numeral 10 denotes a cylindrical body of a refrigerant flow divider, and a refrigerant inlet 11 is formed in the upper part thereof into which a pipe 2 connected to an outlet of a condenser (not shown) is inserted. In addition, the cylindrical body 10
The lower surface thereof is open, and a hollow portion 12 communicating with the refrigerant inlet 11 is formed. 13 and 14 are discharge pipes connected to each evaporator (not shown). The discharge pipes 13, 14 are formed from an outlet pipe 15 consisting of a single capillary tube.
前記出口パイプ15は中央部にV字状の切り込
み16を形成している。この切り込み16により
2つの吸入口17,18を形成している。また、
この切込み16により余つた出口パイプ15の連
結部19を中心に第4図矢印方向に180゜折り曲げ
て平行にすることにより吸入口17,18の高さ
がそろつた吐出管13,14が形成され筒体10
への開口を平行する吐出管13,14と沿う形成
にして、吐出口13,14を挿入してロー付け等
で固定される。このことにより出口パイプ15の
出口端20,211を夫々筒体10の外方へ位置
させる。 The outlet pipe 15 has a V-shaped notch 16 formed in its center. This cut 16 forms two suction ports 17 and 18. Also,
By bending the connecting portion 19 of the remaining outlet pipe 15 by 180 degrees in the direction of the arrow in FIG. body 10
The openings are formed along the parallel discharge pipes 13 and 14, and the discharge ports 13 and 14 are inserted and fixed by brazing or the like. This positions the outlet ends 20, 211 of the outlet pipe 15 to the outside of the cylindrical body 10, respectively.
以上の構成より、動作を説明する。 The operation will be explained based on the above configuration.
このようなものにおいて、吐出管13,14を
なす出口パイプ15はキヤピラリチユーブである
ので絞り作用が働き、冷媒入口11より流入した
気液2相流は分流器の筒体10内にて分離され、
液冷媒が溜まることとなる。従つて、分流は液相
のみで行なわれることとなる。このとき、吐出管
13,14の吸入口17,18側は、全周のうち
一部において連結部19でつながつているため同
一高さとなつており、またずれたとしてもこの間
隔も微小である。このため吐出される冷媒量は均
一となり、安定した蒸発器の能力が得られる。
又、筒体10が傾けて取付られた場合において
も、先端高さの変化量が微少であるため分流バラ
ンスの変化は微少である。 In such a device, since the outlet pipe 15 forming the discharge pipes 13 and 14 is a capillary tube, a throttling action works, and the gas-liquid two-phase flow flowing in from the refrigerant inlet 11 is separated in the cylinder body 10 of the flow divider. is,
Liquid refrigerant will accumulate. Therefore, the flow separation is performed only in the liquid phase. At this time, the suction ports 17 and 18 sides of the discharge pipes 13 and 14 are connected at a connecting part 19 at a part of the entire circumference, so they are at the same height, and even if there is a deviation, this interval is minute. . Therefore, the amount of refrigerant discharged becomes uniform, and stable evaporator performance is obtained.
Further, even when the cylindrical body 10 is installed at an angle, since the amount of change in the tip height is small, the change in the shunt balance is small.
尚、出口パイプ15はキヤピラリチユーブとし
たが、他種の管としても同様な効果が得られる。 Although the outlet pipe 15 is a capillary tube, similar effects can be obtained by using other types of tubes.
発明の効果
以上の説明から明らかなように本発明は、分流
器の出口パイプに切り込みを設けることにより、
この切り込みが冷媒の吸入口となるので、高さを
ほぼ同一にできるため均一な液冷媒の分流が行な
えるとともに、筒体が傾いても連結部でつながつ
ているため吸入口は接近しているので分流のアン
バランスも生じにくいものである。また、組立時
の誤作もなくなるとともに出口パイプを折曲する
ことにより吸入口の端面がそろえられるので、筒
体への接続個所が少なくなり、接続用の銀ロー等
の節約や作業性の向上が図れる。Effects of the Invention As is clear from the above explanation, the present invention provides the following advantages:
This notch becomes the refrigerant suction port, so the heights can be made almost the same, allowing for even distribution of liquid refrigerant, and even if the cylinder is tilted, the suction ports are close together because they are connected at the connecting part. Therefore, unbalanced flow is less likely to occur. In addition, mistakes during assembly are eliminated, and the end faces of the inlet port can be aligned by bending the outlet pipe, reducing the number of connections to the cylinder, saving on silver solder, etc. for connections, and improving work efficiency. can be achieved.
第1図は従来の冷媒分流器の断面図、第2図は
本発明の一実施例の冷媒分流器の断面図、第3図
は、同第2図の出口パイプの加工前の斜視図、第
4図は、同第2図出口パイプの加工後の斜視図を
示す。
10……筒体、13,14……吐出管、15…
…出口パイプ、17,18……吸入口。
FIG. 1 is a cross-sectional view of a conventional refrigerant flow divider, FIG. 2 is a cross-section view of a refrigerant flow divider according to an embodiment of the present invention, and FIG. 3 is a perspective view of the outlet pipe shown in FIG. 2 before processing. FIG. 4 shows a perspective view of the outlet pipe in FIG. 2 after processing. 10... Cylindrical body, 13, 14... Discharge pipe, 15...
...Outlet pipe, 17, 18...Intake port.
Claims (1)
内に切り込みにより余つた連結部を位置させ、こ
の連結部を境に折曲した略平行に位置させた出口
パイプと、前記出口パイプの連結部と冷媒入口と
の間に位置させた中空部とからなる冷媒分流器。1. A cylindrical body of a flow divider having a refrigerant inlet, a surplus connecting portion made by a cut inside the cylindrical body, an outlet pipe bent approximately parallel to the connecting portion, and an outlet pipe of the outlet pipe. A refrigerant flow divider comprising a hollow part located between a connecting part and a refrigerant inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58113737A JPS604770A (en) | 1983-06-23 | 1983-06-23 | Refrigerant distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58113737A JPS604770A (en) | 1983-06-23 | 1983-06-23 | Refrigerant distributor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS604770A JPS604770A (en) | 1985-01-11 |
| JPH0345303B2 true JPH0345303B2 (en) | 1991-07-10 |
Family
ID=14619854
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58113737A Granted JPS604770A (en) | 1983-06-23 | 1983-06-23 | Refrigerant distributor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS604770A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0522765Y2 (en) * | 1985-06-22 | 1993-06-11 | ||
| JP2537131B2 (en) * | 1993-06-28 | 1996-09-25 | 株式会社メイホー | High precision pipe and manufacturing method of this pipe |
-
1983
- 1983-06-23 JP JP58113737A patent/JPS604770A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS604770A (en) | 1985-01-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6443223B2 (en) | Connecting device for heat exchanger | |
| JPH06137695A (en) | Refrigerating cycle | |
| JPS63267868A (en) | Refrigerant evaporator | |
| JPH07103610A (en) | Refrigerant evaporator | |
| US4962811A (en) | Heat exchanger | |
| JP2001050613A (en) | Refrigerant distributor | |
| JPH0331665A (en) | flow divider | |
| US11629896B2 (en) | Heat exchanger and refrigeration cycle apparatus | |
| JPH0345303B2 (en) | ||
| EP0797067B1 (en) | A method of manufacturing a distribution device capable of uniformly distributing a medium to a plurality of tubes of a heat exchanger | |
| US4306421A (en) | Heat exchanger capillary tube routing | |
| JPH0134060Y2 (en) | ||
| KR100309282B1 (en) | A refrigerant distributor for air conditioner | |
| CN109141077A (en) | condenser | |
| JP3133897B2 (en) | Heat exchanger | |
| JPH05203285A (en) | Heat exchanger | |
| JPH06254623A (en) | Manufacture of refrigerant shunt device and refrigerant shunt device | |
| JP3326930B2 (en) | Refrigerant shunt | |
| CN221944554U (en) | Gas-liquid separation structure for gas-liquid separator | |
| JPH02197768A (en) | Distributer | |
| JPH0682125A (en) | Refrigrant distributor | |
| JP2003050063A (en) | Heat exchanger flow divider | |
| JP2880560B2 (en) | Refrigerant flow divider | |
| JPH04148167A (en) | Refrigerant flow divider and refrigerant flow dividing device | |
| JPH0726774B2 (en) | Refrigeration equipment |