JPS597902B2 - flow divider - Google Patents
flow dividerInfo
- Publication number
- JPS597902B2 JPS597902B2 JP51095032A JP9503276A JPS597902B2 JP S597902 B2 JPS597902 B2 JP S597902B2 JP 51095032 A JP51095032 A JP 51095032A JP 9503276 A JP9503276 A JP 9503276A JP S597902 B2 JPS597902 B2 JP S597902B2
- Authority
- JP
- Japan
- Prior art keywords
- main pipe
- flow divider
- refrigerant
- flow
- tubes
- 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
Links
- 239000003507 refrigerant Substances 0.000 claims description 19
- 239000007788 liquid Substances 0.000 claims description 10
- 238000005057 refrigeration Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 1
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
- F25B41/45—Arrangements for diverging or converging flows, e.g. branch lines or junctions for flow control on the upstream side of the diverging point, e.g. with spiral structure for generating turbulence
-
- 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)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
本発明は冷凍サイクルを構成する蒸発器に液冷媒を均等
に分配する分流器に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flow divider that evenly distributes liquid refrigerant to evaporators that constitute a refrigeration cycle.
冷凍サイクルの蒸発器は該蒸発器が小容量の場合には冷
媒通路も1及至2流路程度で支障はないが、大容量の蒸
発器に対しては、20乃至30流路を並行する細管によ
って構成し該細管内での冷媒気化を均等に行なう必要が
ある。If the evaporator of a refrigeration cycle has a small capacity, there is no problem with one or two refrigerant passages, but for a large capacity evaporator, 20 to 30 parallel channels are required. It is necessary to uniformly vaporize the refrigerant within the thin tube.
しかし、従来の分流器は液冷媒を蒸発器に導く主管の開
口端に対向して円錐状の分流体を設置する丈の構造を基
本としていたため、偏流を避け難く、又、蒸発器形状に
合わせた調整もしにくいために、蒸発器の全面を均一に
冷却し効率良く熱交換させろことが難しく、畢寛、蒸発
器として理論値よりもかなり大型の熱交換器を使用しな
ければならない欠点を有していた。However, conventional flow dividers are based on a long structure in which a conical flow divider is installed opposite the open end of the main pipe that leads liquid refrigerant to the evaporator, making it difficult to avoid drifting. Because it is difficult to make adjustments, it is difficult to uniformly cool the entire surface of the evaporator and exchange heat efficiently. had.
斯る点に鑑みなされた本発明を以下に図面に従い説明す
ると、1は図示を省略した凝縮器から流入する液冷媒を
膨張弁2を介して蒸発器3に導く主管、4は該主管に並
行して配設され蒸発器3からコンプレツサ(図示省略)
へ気化冷媒を導く吸入管5に至る間に独立した多数の冷
媒流路を形成する細管であり、該細管には主管1の先端
に取り付けられた分流器6を介して液冷媒が均等に分配
されるようにしている。The present invention, which was made in view of this point, will be described below with reference to the drawings. Reference numeral 1 indicates a main pipe that guides liquid refrigerant flowing from a condenser (not shown) to an evaporator 3 via an expansion valve 2, and 4 is a main pipe parallel to the main pipe. from the evaporator 3 to the compressor (not shown)
It is a thin tube that forms a number of independent refrigerant flow paths between the suction tube 5 that leads the vaporized refrigerant to the main tube 1, and the liquid refrigerant is evenly distributed to the thin tube through a flow divider 6 attached to the tip of the main tube 1. I'm trying to make it happen.
而して、分流器6は第2図及び第3図にその構造を示す
ように、噴流管7を内蔵する施回室8を有し、該施回室
の軸線方向の下側に主管1、同じく上側に主管1を囲繞
するような配置で細管4を取り付け、かつ、噴流管7は
先端9を一方向に折曲げて施回室8での液冷媒の旋回流
を促すようにした長さの異なる管群7’,7//eもっ
て構成され、個々の噴流管は主管1に連通ずるようにし
てその先端に取り付けられている。As shown in FIGS. 2 and 3, the flow divider 6 has a circulation chamber 8 containing a jet pipe 7, and a main pipe 1, a main pipe 1, Similarly, a thin tube 4 is attached to the upper side in such a manner as to surround the main tube 1, and the jet tube 7 has a length such that the tip 9 is bent in one direction to promote a swirling flow of liquid refrigerant in the circulation chamber 8. It is composed of different groups of tubes 7', 7//e, and each jet tube is attached to the tip of the main tube 1 so as to communicate with it.
斯る構造ケ有する分流器は主管1から流入する液冷媒を
噴流管7によって旋回室8に噴出させ、冷媒気泡の混入
した気液混合状態での旋回流とすることができ、夫々の
細管4に均等に冷媒を分配して送出することかできる。The flow divider having such a structure can jet the liquid refrigerant flowing from the main pipe 1 into the swirling chamber 8 through the jet pipe 7 to create a swirling flow in a gas-liquid mixed state with refrigerant bubbles mixed in, and each thin pipe 4 The refrigerant can be evenly distributed and delivered.
すなわち、従来の分流器においては主管からの液冷媒を
液状態のまま直ちに細管に分流する機構となっているた
めに、重力、個々の細管取付状態や抵抗の違い、更には
蒸発器中を流下する際の乾き度の影響が個々の分流量の
違いとして現われる欠点を有していたが、本発明の分流
器では細管に分流される直前の冷媒に気泡が混入するこ
とによって比重量は小さくなり、重力や管抵抗の影響を
受けることは少なく、又、乾き度との関係も殆どなくな
る。In other words, in conventional flow dividers, the liquid refrigerant from the main pipe is immediately diverted to the capillary tubes in its liquid state. However, in the flow divider of the present invention, air bubbles are mixed into the refrigerant immediately before it is divided into the thin tubes, so that the specific weight becomes smaller. , it is less affected by gravity and pipe resistance, and there is almost no relationship with dryness.
更に又、本発明の分流器においては細管と主管とを旋回
室を介して接続していろために、蒸発器の構造からみて
一部の細管に対する冷媒流量を増減する必要がある場合
、旋回室内に適当な補助金具を取り付けて斯る要望に応
じることもでき、単に冷媒分流の偏流を無くして分流効
率を上げるのみならず、蒸発器と共に功率の良い冷凍サ
イクルの構成を成し得る等、応用範囲の広い分流器でも
ある。Furthermore, in the flow divider of the present invention, since the thin tubes and the main tube are connected through the swirl chamber, if it is necessary to increase or decrease the refrigerant flow rate to some of the thin tubes due to the structure of the evaporator, the swirl chamber It is possible to meet such requests by attaching appropriate auxiliary fittings to the refrigerant, and it is possible to not only increase the efficiency of the divided refrigerant flow by eliminating uneven flow of the refrigerant flow, but also to form a highly efficient refrigeration cycle structure with the evaporator. It is also a wide range flow divider.
第1図は本発明による分流器の使用状態の一例を示す斜
視図、第2図は同じく分流器の縦断側面図、第3図は第
2図の■一■断面図である。
1・・・・・・主管、4・・・・・・細管、7・・・・
・・噴流管、8・・・・・・旋回室。FIG. 1 is a perspective view showing an example of a usage state of a flow divider according to the present invention, FIG. 2 is a vertical side view of the flow divider, and FIG. 3 is a sectional view taken along line 1 of FIG. 1... Main tube, 4... Thin tube, 7...
... Jet pipe, 8... Turning chamber.
Claims (1)
端に取り付けた旋回室を介して接続し、旋回室には先端
を一方向に折曲げた長さの異なる管群から成る複数本の
噴流管を主管と連通させて取り付けることにより主管か
ら流入する液冷媒を細管に均等に分流するようにしたこ
とケ特徴とする分流器。1 A main pipe and a number of thin tubes parallel to the main pipe are connected via a swirling chamber attached to the tip of the main pipe, and the swirling chamber has a plurality of tubes each consisting of a group of tubes of different lengths with their tips bent in one direction. A flow divider characterized in that a jet flow pipe is installed in communication with a main pipe so that liquid refrigerant flowing from the main pipe is evenly divided into thin pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51095032A JPS597902B2 (en) | 1976-08-06 | 1976-08-06 | flow divider |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51095032A JPS597902B2 (en) | 1976-08-06 | 1976-08-06 | flow divider |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5320151A JPS5320151A (en) | 1978-02-24 |
| JPS597902B2 true JPS597902B2 (en) | 1984-02-21 |
Family
ID=14126736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51095032A Expired JPS597902B2 (en) | 1976-08-06 | 1976-08-06 | flow divider |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS597902B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60192107A (en) * | 1984-03-14 | 1985-09-30 | Aisin Seiki Co Ltd | Fluid pressure-operated actuator |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110131931A (en) * | 2019-06-25 | 2019-08-16 | 北京鑫红苑制冷设备工程有限公司 | Spiral centrifugal separator |
-
1976
- 1976-08-06 JP JP51095032A patent/JPS597902B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60192107A (en) * | 1984-03-14 | 1985-09-30 | Aisin Seiki Co Ltd | Fluid pressure-operated actuator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5320151A (en) | 1978-02-24 |
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