JPH02306070A - Refrigerant flow divider - Google Patents
Refrigerant flow dividerInfo
- Publication number
- JPH02306070A JPH02306070A JP1127043A JP12704389A JPH02306070A JP H02306070 A JPH02306070 A JP H02306070A JP 1127043 A JP1127043 A JP 1127043A JP 12704389 A JP12704389 A JP 12704389A JP H02306070 A JPH02306070 A JP H02306070A
- Authority
- JP
- Japan
- Prior art keywords
- flow
- refrigerant
- flow divider
- liquid
- outflow
- 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.)
- Pending
Links
- 239000003507 refrigerant Substances 0.000 title claims abstract description 39
- 239000007788 liquid Substances 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 10
- 230000002093 peripheral effect Effects 0.000 abstract description 9
- 239000007791 liquid phase Substances 0.000 abstract description 6
- 239000012071 phase Substances 0.000 abstract description 5
- 239000012808 vapor phase Substances 0.000 abstract 1
- 230000005514 two-phase flow Effects 0.000 description 12
- 238000005057 refrigeration Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000002517 constrictor effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 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
- F25B41/48—Arrangements for diverging or converging flows, e.g. branch lines or junctions for flow path resistance control on the downstream side of the diverging point, e.g. by an orifice
-
- 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
-
- 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
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)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は空調機器や冷凍機器等の冷凍サイクルにおいて
、冷媒を均等に分流するための冷媒分流器に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a refrigerant flow divider for uniformly dividing refrigerant in a refrigeration cycle of an air conditioner, a refrigeration equipment, or the like.
従来の技術
近年、冷凍システムのマルチ化、及び熱交換器の伝熱管
細径化に伴う複数回路化等に対応するために冷媒分流器
が用いられてきておシ、その重要度が増している。Conventional technology In recent years, refrigerant flow dividers have been used to cope with the multiplication of refrigeration systems and the creation of multiple circuits as heat exchanger tubes become smaller in diameter, and their importance is increasing. .
前記冷媒分流器の中でも、コンパクトで低コストでしか
も制作、取シ付けが容易であるということから銅製成形
品が多用されている。Among the refrigerant flow dividers, copper molded products are often used because they are compact, low cost, and easy to manufacture and install.
以下、図面を参照しながら上述した従来の分流器につい
て説明を行う。Hereinafter, the conventional flow divider mentioned above will be explained with reference to the drawings.
第4図と第6図は従来の分流器の形状を示し、第6図は
分流器の熱交換器への取シ付は状態を示し、第7図は熱
交換器を冷凍サイクル運転した際の分流器内部の冷媒状
態を示す。第4図から第7図において、1は分流器で、
流入口2と他端に流出口3を備えた流入管4とそれに続
く円錐側6および円筒胴6、さらに流入ロアと他端に流
出口8を備えた複数の流出管9とから構成されている。Figures 4 and 6 show the shape of a conventional flow divider, Figure 6 shows how the flow divider is attached to the heat exchanger, and Figure 7 shows the state when the heat exchanger is operated in a refrigeration cycle. This shows the refrigerant condition inside the flow divider. In Figures 4 to 7, 1 is a flow divider;
It is composed of an inflow pipe 4 having an inflow port 2 and an outflow port 3 at the other end, a conical side 6 and a cylindrical body 6 following the inflow port 2, and a plurality of outflow pipes 9 each having an inflow lower end and an outflow port 8 at the other end. There is.
1oは冷媒の分岐部である。1o is a refrigerant branch.
又、11は冷媒管12によって冷媒回路を構成している
熱交換′器で、分流器1が複数の冷媒回路を形成するた
めに熱交換器11のサイドに取り付けられている。Further, 11 is a heat exchanger which constitutes a refrigerant circuit with refrigerant pipes 12, and a flow divider 1 is attached to the side of the heat exchanger 11 to form a plurality of refrigerant circuits.
以上のように構成された分流器について、以下第6図か
ら第7図を用いてその動作を説明する。The operation of the flow divider configured as described above will be described below with reference to FIGS. 6 and 7.
冷凍サイクルを流れる冷媒Aは熱交換器11に流入する
とき、その上流にある分流器1へ流入し分流され冷媒管
12で形成される複数の冷媒回路に流される。分流器1
において気相A1と液相A2との二相流となって流入口
2から流入した冷媒Aは、流入管4を経た後円雄側69
円筒胴6を通過し分岐部1oで複数の流出管9a 、9
bへ分流され、それぞれ流出口sa、sbを経て冷媒管
12a、12bへ流出していくこととなる。このとき冷
媒Aの一部は、流出管9a、9bから円滑に流出されず
、液相A2の一部は円筒胴6の上部壁面に衝突、落下し
円錐用5あるbは円筒胴6の下部で滞留、循環し液溜シ
を形成する。同様に気相A1の一部は円筒胴6の上部で
滞留、循環し気溝りを形成する。When the refrigerant A flowing through the refrigeration cycle flows into the heat exchanger 11 , it flows into the flow divider 1 located upstream of the refrigerant A, and is divided into a plurality of refrigerant circuits formed by refrigerant pipes 12 . Flow divider 1
The refrigerant A flows into the inlet 2 from the inlet 2 as a two-phase flow of gas phase A1 and liquid phase A2.
A plurality of outflow pipes 9a, 9 pass through the cylindrical body 6 and at the branch part 1o.
b, and flow out into the refrigerant pipes 12a, 12b via the outlet sa, sb, respectively. At this time, a part of the refrigerant A is not smoothly flowed out from the outflow pipes 9a and 9b, and a part of the liquid phase A2 collides with the upper wall surface of the cylindrical body 6 and falls. It stays and circulates, forming a liquid reservoir. Similarly, a part of the gas phase A1 stays and circulates in the upper part of the cylindrical body 6, forming an air groove.
発明が解決しようとする課題
しかしながら上記のような構成では、冷媒Aは分流器1
の流入管4内を流れるときにはその断面において気液割
合が不均一な状態で気液分離しておシ、この状態は円錐
側69円筒胴6を通過する間も続く。また液溜りの液面
は流入する二相流によシ撹乱され液面から同伴される液
相量も不均一になる。また分流器1を鉛直に対し傾けて
設置した場合、分流器内に滞留した液相A2が鉛直下部
の流出管9に多く流れる。そのため分岐部10において
流出管9a、9bさらにそれに続く冷媒管12への冷媒
へ重量の均等な分流ができないという課題を有していた
。又、流出管9による後方での抵抗によシ、分流を少し
でも改善しようとしているため、流出管9及びそれに続
く冷媒管12の内径をあまシ小さくできず、したがって
、圧力損失を低減できないという課題を有していた。さ
らに、分流器1は、一端に複数の流出管9を接続するた
め、必然的に大型でコストが高いという課題も有してい
た。Problems to be Solved by the Invention However, in the above configuration, the refrigerant A flows through the flow divider 1.
When flowing through the inflow pipe 4, the gas-liquid ratio is non-uniform in its cross section and the gas-liquid is separated, and this state continues even while passing through the conical side 69 and the cylindrical body 6. Furthermore, the liquid surface of the liquid pool is disturbed by the inflowing two-phase flow, and the amount of liquid phase entrained from the liquid surface also becomes non-uniform. Furthermore, when the flow divider 1 is installed tilted with respect to the vertical direction, a large amount of the liquid phase A2 retained in the flow divider flows into the outflow pipe 9 in the vertical lower part. Therefore, in the branching portion 10, there was a problem in that the refrigerant could not be equally distributed in weight to the outflow pipes 9a, 9b and the subsequent refrigerant pipe 12. In addition, since the attempt is made to improve the flow division even slightly due to the resistance caused by the outflow pipe 9 at the rear, the inner diameter of the outflow pipe 9 and the refrigerant pipe 12 following it cannot be made much smaller, and therefore, the pressure loss cannot be reduced. I had an issue. Furthermore, since the flow divider 1 has a plurality of outflow pipes 9 connected to one end thereof, it is inevitably large and expensive.
本発明は上記課題に鑑み、冷媒の均等な分流が行なえる
小型、低コストの分流器を提供するものである。In view of the above problems, the present invention provides a small, low-cost flow divider that can evenly divide a refrigerant.
課題を解決するための手段
上記課題を解決するために本発明の分流器は、一端が衝
突壁となる円筒状の分流部と、円筒状分流部流入口にか
ん合し、流出端に小孔が加工された流入管と、円筒状分
流部周壁に接合部内径が狭められ接合された複数の流出
管とから構成されたものである。Means for Solving the Problems In order to solve the above problems, the flow divider of the present invention has a cylindrical flow divider part with one end serving as a collision wall, a cylindrical flow divider part that engages with an inlet, and a small hole in the outlet end. It is composed of an inlet pipe which has been machined, and a plurality of outflow pipes which are joined to the circumferential wall of a cylindrical branch part with a narrowed inner diameter at the joint part.
作 用
本発明は上記した構成によって、流入管を流れる気液分
離した冷媒の流れを流入管流出端の小孔部より噴出、こ
の流れを対向する衝突壁面に衝突させノズルによる噴出
効果と衝突壁面での衝突、撹乱効果により気液混合を進
め、気液二相流の均一化を促進させると共に、放射方向
に配置された流出管入口部で内径が狭められているため
、その絞シ効果で二相流が噴出するため、各流出管への
分流が均等化される。このとき前記衝突壁と周壁によっ
て囲まれた容積を小さくすることで液溜りおよび気溝シ
の形成を無くし、噴流の効果を減することなく均等に分
流を行なうことができる上に、流出管を円筒状分流部の
周壁に放射状に接合するため、従来の分流器に比べ、小
型、低コスト化が可能になる。Effect of the Invention With the above-described configuration, the present invention jets out a flow of gas-liquid separated refrigerant flowing through an inflow pipe from a small hole at the outflow end of the inflow pipe, and collides this flow with an opposing collision wall surface, thereby reducing the jetting effect by the nozzle and the collision wall surface. Collision and disturbance effects promote gas-liquid mixing and promote homogenization of the gas-liquid two-phase flow.In addition, since the inner diameter is narrowed at the inlet of the outlet pipe arranged in the radial direction, the constriction effect Since a two-phase flow is ejected, the flow distribution to each outflow pipe is equalized. At this time, by reducing the volume surrounded by the collision wall and the peripheral wall, the formation of liquid pools and air grooves can be eliminated, and the flow can be divided evenly without reducing the jet effect. Since it is radially joined to the peripheral wall of the cylindrical flow divider, it can be made smaller and lower in cost than conventional flow dividers.
実施例
以下本発明の実施例の分流器について図面を参照しなが
ら説明する。EMBODIMENTS Below, flow dividers according to embodiments of the present invention will be described with reference to the drawings.
第1図から第2図は本発明の実施例における分流器の形
状を示すもので、第3図は熱交換器を冷凍サイクル運転
した際の分流器内部の冷媒状態を示す。第1図から第3
図において、13は分流器で、流入口14と他端に小孔
15を備えた流入管16およびその小孔16からの噴流
を受ける衝突壁17、それを取シ囲む周壁18、さらに
内径が狭められた流入口19と他端に流出口2Qを備え
た複数の流出管21が分流器13の中心軸に対し放射状
に取シ付けられている。1 to 2 show the shape of a flow divider in an embodiment of the present invention, and FIG. 3 shows the state of refrigerant inside the flow divider when the heat exchanger is operated in a refrigeration cycle. Figures 1 to 3
In the figure, 13 is a flow divider, which includes an inlet pipe 16 having an inlet 14 and a small hole 15 at the other end, a collision wall 17 that receives the jet from the small hole 16, a peripheral wall 18 surrounding it, and an inner diameter A plurality of outlet pipes 21 each having a narrowed inlet 19 and an outlet 2Q at the other end are attached radially to the central axis of the flow divider 13.
以上のように構成された分流器について、以下第3図を
用いてその動作について説明する。The operation of the flow divider configured as described above will be explained below using FIG. 3.
冷凍サイクルの閉回路を流れる冷媒Bが気相B1と液相
B2との二相流となって流入口14から分流器13に流
入する。流入管16を通過後、小孔16よシ噴出する。Refrigerant B flowing through the closed circuit of the refrigeration cycle becomes a two-phase flow of gas phase B1 and liquid phase B2 and flows into the flow divider 13 from the inlet 14. After passing through the inflow pipe 16, it is ejected through the small hole 16.
この時、前記二相流はノズル作用により縮流・加速され
噴流となって流出する。その後冷媒Bの噴流は頂部衝突
壁17に衝突し撹拌混合される。この衝突・撹拌・混合
作用によシ冷媒Bの気液二相流の混合状態は均一化され
る。均一化された冷媒Bは頂部衝突壁17に沿って放射
状に広がシ周壁18に取り付けられた流出管21の流入
口19に流出し分流する。このとき衝突壁17および周
壁18に囲まれた容積内に液溜シおよび気溝りが形成さ
れることがないため、冷媒Bの気液混合状態は前記ノズ
ル効果で均一化されたままであシ、流入口19の内径が
狭められているため、その絞り効果で、均一化された二
相流が噴出するため、各流出管21への分流が均等化さ
れる。又、流出管21による後方での抵抗により分流を
改善する必要がないため、流出管21及びそれに続く冷
媒管(図示せず)の内径を大きくできるため、圧力損失
を低減できることになる。At this time, the two-phase flow is contracted and accelerated by the nozzle action, and flows out as a jet flow. Thereafter, the jet of refrigerant B collides with the top collision wall 17 and is stirred and mixed. Due to this collision, stirring, and mixing action, the mixed state of the gas-liquid two-phase flow of the refrigerant B is made uniform. The homogenized refrigerant B spreads radially along the top collision wall 17, flows out into the inlet 19 of the outflow pipe 21 attached to the peripheral wall 18, and is divided into streams. At this time, since no liquid reservoir or air groove is formed in the volume surrounded by the collision wall 17 and the peripheral wall 18, the gas-liquid mixing state of the refrigerant B remains uniform due to the nozzle effect. Since the inner diameter of the inflow port 19 is narrowed, a homogenized two-phase flow is jetted out due to its throttling effect, so that the branched flow to each outflow pipe 21 is equalized. Further, since there is no need to improve the flow division due to the resistance at the rear of the outflow pipe 21, the inner diameter of the outflow pipe 21 and the refrigerant pipe (not shown) following it can be increased, so that pressure loss can be reduced.
以上のように本実施例によれば、流入管16に小孔15
を備え、その流出噴流を受ける衝突壁17および周壁1
8によって取シ囲まれた容積を液溜りおよび気溝りが形
成しないように小さくすることにより、分流器13に流
入した冷媒Bの気液二相流の混合状態を均一にしそれを
保持することが出来、さらに、各流出管21の流入口1
90絞シ効果で、均一化された二相流が噴出するため、
各流出管21およびそれの続く冷媒管(図示せず)への
冷媒の分流を均等に近づけることができる。As described above, according to this embodiment, the small hole 15 is provided in the inflow pipe 16.
and a collision wall 17 and a peripheral wall 1 that receive the outflow jet.
By reducing the volume surrounded by 8 so as not to form liquid pools and air grooves, the mixed state of the gas-liquid two-phase flow of refrigerant B flowing into the flow divider 13 is made uniform and maintained. is completed, and furthermore, the inlet 1 of each outlet pipe 21 is
Due to the 90 diaphragm effect, a homogenized two-phase flow is ejected,
The refrigerant can be equally divided into each outlet pipe 21 and its subsequent refrigerant pipe (not shown).
発明の効果
以上のように本発明は、ノズル流出口を備えた流入管と
、その流出噴流の流れを垂直方向に変更する衝突壁を備
え、しかも液溜シおよび気溝シを形成しないように周壁
に囲まれた容積を小さくすることによシ、気液二相流の
混合を均一化し、さらに、周壁に放射状に接合された流
出管の流入口内径を狭めることで、二相流が噴出し冷媒
の均等分流を行なうことができ、同時に、その構造上、
小型、低コスト化か可能である。Effects of the Invention As described above, the present invention includes an inflow pipe having a nozzle outlet and a collision wall that changes the flow of the outflow jet in the vertical direction, and also prevents the formation of liquid reservoirs and air grooves. By reducing the volume surrounded by the surrounding wall, the mixing of the gas-liquid two-phase flow is made uniform, and by narrowing the inner diameter of the inlet of the outflow pipe radially joined to the surrounding wall, the two-phase flow is ejected. It is possible to divide the refrigerant evenly, and at the same time, due to its structure,
Small size and low cost are possible.
第1図は本発明の実施例における分流器の概略形状を示
す斜視図、第2図は第1図の断面図、第3図は第1図の
分流器の使用状態における冷媒の流れを示す断面図、第
4図は従来の分流器の概略形状を示す斜視図、第5図は
第4図の断面図、第6図は第4図の分流器の熱交換器へ
の取シ付は状態を示す斜視図、第7図は第4図の分流器
の使用状態における冷媒の流れを示す断面図である。
13・・・・・・分流器、16・・・・・・小孔、16
・・・・・・流入管、17・・・・・・衝突壁、18・
・・・・・周壁、21・・・・・・流出管、19・・・
・・・流入口。
代理人の氏名 弁理士 粟 野 重 孝 ほか1名13
− 分流器
第3図
−−障 口か
姻鴨〈叱極ぐ祖
C’) S −、o lミ(ばトゝ
−N \ \ ・N、++\ ぐQ
−ぎ
(\ %
へ N”−
第6図
第7図
◇Fig. 1 is a perspective view showing the schematic shape of a flow divider in an embodiment of the present invention, Fig. 2 is a sectional view of Fig. 1, and Fig. 3 shows the flow of refrigerant when the flow divider of Fig. 1 is in use. 4 is a perspective view showing the general shape of a conventional flow divider, Figure 5 is a sectional view of Figure 4, and Figure 6 shows how the flow divider shown in Figure 4 is attached to a heat exchanger. FIG. 7 is a perspective view showing the state, and FIG. 7 is a sectional view showing the flow of refrigerant when the flow divider of FIG. 4 is in use. 13... Flow divider, 16... Small hole, 16
......Inflow pipe, 17...Collision wall, 18.
... Peripheral wall, 21 ... Outflow pipe, 19 ...
...Inlet. Name of agent: Patent attorney Shigetaka Awano and 1 other person13
- Flow divider Figure 3 - S -, o l mi (Batoゝ-N \ \ ・N, ++\ guQ -gi (\% to N") - Figure 6 Figure 7 ◇
Claims (1)
入口にかん合し、流出端に小孔が加工された流入管と、
円筒状分流部周壁に接合部内径が狭められ接合された複
数の流出管とからなる冷媒分流器。a cylindrical branch part with one end serving as a collision wall; an inflow pipe that engages with the inlet of the cylindrical branch part and has a small hole machined in the outlet end;
A refrigerant flow divider consisting of a plurality of outflow pipes connected to a circumferential wall of a cylindrical flow distribution part with a narrowed inner diameter of the joint.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1127043A JPH02306070A (en) | 1989-05-19 | 1989-05-19 | Refrigerant flow divider |
| KR1019910700369A KR920701766A (en) | 1989-02-21 | 1990-08-06 | Refrigerant Sorter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1127043A JPH02306070A (en) | 1989-05-19 | 1989-05-19 | Refrigerant flow divider |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02306070A true JPH02306070A (en) | 1990-12-19 |
Family
ID=14950209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1127043A Pending JPH02306070A (en) | 1989-02-21 | 1989-05-19 | Refrigerant flow divider |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02306070A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3161393A1 (en) * | 2014-06-26 | 2017-05-03 | Valeo Klimasysteme GmbH | Branching means for a refrigerant flow of a refrigerant circuit |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS508131A (en) * | 1973-05-28 | 1975-01-28 | ||
| JPS504345B1 (en) * | 1970-05-21 | 1975-02-18 |
-
1989
- 1989-05-19 JP JP1127043A patent/JPH02306070A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS504345B1 (en) * | 1970-05-21 | 1975-02-18 | ||
| JPS508131A (en) * | 1973-05-28 | 1975-01-28 |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3161393A1 (en) * | 2014-06-26 | 2017-05-03 | Valeo Klimasysteme GmbH | Branching means for a refrigerant flow of a refrigerant circuit |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4193910B2 (en) | Expansion valve with integrated refrigerant flow divider | |
| JP2002130868A (en) | Refrigerant flow divider and air conditioner using the same | |
| US5243838A (en) | Refrigerant shunt | |
| CN115773599B (en) | Liquid dispenser and its application | |
| CN214307717U (en) | Distributors and Air Conditioning Equipment | |
| CN117128672B (en) | Dispenser | |
| JP2745981B2 (en) | Refrigerant flow divider | |
| JP5193630B2 (en) | Heat exchanger | |
| JPH02306070A (en) | Refrigerant flow divider | |
| JP2746681B2 (en) | Refrigerant flow divider | |
| JP2006349238A (en) | Refrigerant shunt | |
| JP2880562B2 (en) | Refrigerant flow divider | |
| JPH0498055A (en) | Refrigerant flow divider | |
| JPH01121667A (en) | Refrigerant flow diverter | |
| CN114923225A (en) | Flow divider, indoor heat exchanger and air conditioner indoor unit | |
| JP2820443B2 (en) | Shunt | |
| WO1991002931A1 (en) | Flow diverter for refrigerant | |
| JPH02166366A (en) | Refrigerant flow diverter | |
| JPH01123963A (en) | refrigerant flow divider | |
| JPH03113251A (en) | Gas/liquid two phase fluid distributor | |
| JPH02275266A (en) | Refrigerant shunt | |
| JPH02197769A (en) | Flow divider | |
| CN111692783A (en) | Shunt and air conditioner with same | |
| JPH04148167A (en) | Refrigerant flow divider and refrigerant flow dividing device | |
| JPH0297860A (en) | Refrigerant flow divider |