JPH02275266A - Refrigerant shunt - Google Patents
Refrigerant shuntInfo
- Publication number
- JPH02275266A JPH02275266A JP1097146A JP9714689A JPH02275266A JP H02275266 A JPH02275266 A JP H02275266A JP 1097146 A JP1097146 A JP 1097146A JP 9714689 A JP9714689 A JP 9714689A JP H02275266 A JPH02275266 A JP H02275266A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- collision wall
- flows
- small hole
- flow
- 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 50
- 230000002093 peripheral effect Effects 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 abstract description 19
- 238000005057 refrigeration Methods 0.000 abstract description 8
- 239000007791 liquid phase Substances 0.000 abstract description 6
- 239000012071 phase Substances 0.000 abstract description 4
- 239000012808 vapor phase Substances 0.000 abstract 1
- 230000005514 two-phase flow Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000010959 steel Substances 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
- F25B41/45—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)
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υ、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5図から第6図までは従来の分流器の形状を示し、第
7図は分流器の熱交換器への取り付は状態を示し、第8
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5図から第8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
れに続く円錐鋼6および円筒胴8、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。1oは冷媒の分岐部である。Figures 5 to 6 show the shape of a conventional flow divider, Figure 7 shows how the flow divider is attached to a heat exchanger, and Figure 8
The figure shows the state of the refrigerant inside the flow divider when the heat exchanger is operated in a refrigeration cycle. 5 to 8, 1 is a flow divider, which includes an inlet pipe 4 having an inlet 2 and an outlet 3 at the other end, a conical steel 6 and a cylindrical body 8, and a lower inlet and an outlet 3 at the other end. It is composed of a plurality of outflow pipes 9 each having an outlet 8. 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。Reference numeral 11 denotes a heat exchanger that constitutes a refrigerant circuit using 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7図か
ら第8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. 7 to 8.
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−て流入口
2から流入した冷媒Aは、流入管4を経た後円錐胴5、
円筒胴6を通過し分岐部10で複数の流出管9a、9b
へ分流され、それぞれ流出口sa、sbを経て冷媒管1
2a。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 as a two-phase flow of a gas phase A1 and a liquid phase A2.
A plurality of outflow pipes 9a, 9b pass through the cylindrical body 6 and at the branch part 10.
refrigerant pipe 1 through outlet ports sa and sb, respectively.
2a.
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A
2の一部は円筒胴6の上部壁面に衝突、落下し円錐網6
あるいは円筒胴6の下部で滞留、循環し液溜りを形成す
る。同様に気相A1の一部は円筒胴6の上部で滞留、循
環し気溜りを形成する。It will flow out to 12b. At this time, a part of the refrigerant A is not smoothly flowed out from the outflow pipes 9a and 9b, and the liquid phase A
2 collides with the upper wall of the cylindrical body 6 and falls, forming the conical net 6.
Alternatively, the liquid accumulates and circulates in the lower part of the cylindrical body 6 to form a liquid pool. Similarly, a part of the gas phase A1 stays and circulates in the upper part of the cylindrical body 6 to form an air pocket.
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り、この状態は円錐
網62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り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12a 、
12b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。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 inlet 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 mesh 62 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, at the branch part 10, the outflow pipes 9a, 9b and the refrigerant pipe 12a following them,
There was a problem in that it was not possible to divide the refrigerant into the refrigerant 12b evenly in weight.
また、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。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.
課題を解決するだめの手段
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、その周壁に放射状に接合
された複数の流出管と、円筒状分流部の内周にかん合し
、かつ、衝突壁からの距離L f L < 30 rr
rmとする段付き絞り部と流出端に小孔が加工された流
入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 includes a cylindrical flow divider portion with one end serving as a collision wall, a plurality of outflow pipes radially joined to the peripheral wall of the flow divider portion, and a cylindrical Distance L f L < 30 rr that engages with the inner periphery of the flow dividing part and from the collision wall
It consists of a stepped constriction section with a diameter of rm and an inflow pipe with a small hole formed at the outflow end.
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段付き絞り部で加速した後、
流出端の小孔部により噴出、この流れを対向する衝突壁
面に衝突させ絞りによる加速及び小孔部による噴出効果
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
置された流出管へ円滑に流出させることによって各冷媒
管への均等分流を行なうものである。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
りおよび気溜りの形成を無くし、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。また、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 accelerates the flow of gas-liquid separated refrigerant flowing through the inflow pipe at the stepped constriction portion of the inflow pipe, and then
The gas is ejected from the small hole at the outflow end, this flow collides with the opposing collision wall, and the gas-liquid mixture is accelerated by the throttle, the ejection effect from the small hole, the collision at the collision wall, and the disturbance effect.
The purpose is to promote uniformity of the gas-liquid two-phase flow, and to equally distribute the flow to each refrigerant pipe by causing the refrigerant to flow smoothly to the outflow pipes arranged in the radial direction. At this time, by reducing the volume surrounded by the collision wall and the peripheral wall, the formation of liquid pools and air pools can be eliminated, and the flow can be divided evenly without reducing the effect of the jet flow. In addition, since the outflow pipe is radially joined to the peripheral wall of the cylindrical flow divider, it is possible to reduce the size and cost compared to 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
16を備え、段付き絞り部16を有する流入管17およ
びその小孔からの噴流を受ける衝突壁18、それを取り
囲む周壁19、さらに流入口2oと他端に流出口21を
備えた複数の流出管22が分流器13の中心軸に対し放
射状に取り付けられている。23は冷媒管で、従来例と
同じものであり、流出口21に接続されている。Lは小
孔から衝突壁までの距離である。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 has an inlet 14 and a small hole 16 at the other end, an inlet pipe 17 having a stepped constriction 16, a collision wall 18 that receives the jet from the small hole, and a peripheral wall 19 surrounding it. Furthermore, a plurality of outlet pipes 22 each having an inlet 2o and an outlet 21 at the other end are attached radially to the central axis of the flow divider 13. Reference numeral 23 denotes a refrigerant pipe, which is the same as in the conventional example, and is connected to the outlet 21. L is the distance from the small hole to the impact wall.
第4図は分流器のL寸法を変えたときの各流出管への分
流比率を示したものである(本例では3分流)。図中斜
線範囲は熱交換器の性能低下をきたさない実使用上の許
容範囲を示している。FIG. 4 shows the ratio of divided flow to each outflow pipe when the L dimension of the flow divider is changed (in this example, there are three divided flows). The shaded range in the figure indicates the allowable range in actual use without deteriorating the performance of the heat exchanger.
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17を通り、段付き絞り部16で加速さ
れた後、小孔16より噴出する。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 17 and being accelerated by the stepped constriction section 16, it is ejected from the small hole 16.
この時、前記二相流は小孔作用により縮流・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
18に衝突し撹拌混合される。この衝突・撹拌・混合作
用により冷媒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18に沿って放射状
に広がり周壁19に取り付けられた流出管22の流入口
20に流出し分流される。このとき、衝突壁18および
周壁19に囲まれた容積内に液溜りおよび気溜りが形成
されることがないため、冷媒Bの気液混合状態は前記小
孔の効果で均一化されたままであり、それ故、均等に分
流されることとなる。流出管22へ均等に分流された冷
媒Bはそれぞれの流出管22の流出口21から冷媒管2
3へ流出していくこととなる。At this time, the two-phase flow is contracted and accelerated by the action of the small holes, and flows out as a jet flow. Thereafter, the jet of refrigerant B collides with the top collision wall 18 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 18, flows out into the inlet 20 of the outflow pipe 22 attached to the peripheral wall 19, and is divided. At this time, since no liquid pool or air pool is formed in the volume surrounded by the collision wall 18 and the peripheral wall 19, the gas-liquid mixing state of the refrigerant B remains uniform due to the effect of the small holes. , therefore, the flow will be divided equally. The refrigerant B evenly distributed to the outflow pipes 22 flows from the outlet 21 of each outflow pipe 22 to the refrigerant pipe 2.
It will flow to 3.
また、流出管22を放射状に円筒状分流部局壁に接続し
た構成のため、従来の分流器に比べ、小型、低コスト化
が可能である。Further, since the outflow pipe 22 is radially connected to the cylindrical flow dividing portion local wall, it is possible to reduce the size and cost compared to the conventional flow divider.
以上のように本実施例によれば、流入管17に段付き絞
り部16と小孔16を備え、その流出噴流を受ける衝突
壁18および周壁19によって取り囲まれた容積を液溜
りおよび気溜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でき、各流出管22
およびそれの続く冷媒管23への冷媒の分流を均等に近
づけることができる。このとき第4図に示す様にL寸法
を特許請求の範囲に示す範囲に制限すればその効果を保
持でき、段付き絞り部16によって加速のみならずその
寸法制限が容易に、かつ確実に行なえる。As described above, according to this embodiment, the inflow pipe 17 is provided with the stepped constriction part 16 and the small hole 16, and the volume surrounded by the collision wall 18 and the peripheral wall 19 that receive the outflow jet is filled with a liquid pool and a gas pool. By making the gas-liquid two-phase flow of the refrigerant B flowing into the flow divider 13 small, the mixing state of the gas-liquid two-phase flow of the refrigerant B flowing into the flow divider 13 can be made uniform and maintained.
And the subsequent branch flow of the refrigerant to the refrigerant pipes 23 can be made nearly uniform. At this time, if the L dimension is limited to the range shown in the claims as shown in FIG. 4, the effect can be maintained, and the stepped throttle section 16 not only accelerates but also limits the dimension easily and reliably. Ru.
発明の効果
以上のように本発明は、段付き絞り部を有し、かつ、小
孔を備えた流入管と、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、しかも液溜りおよび気溜りを形
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
より、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、低コスト化が可能である。Effects of the Invention As described above, the present invention includes an inflow pipe having a stepped constriction portion and a small hole, and an impingement wall that changes the flow of the outflow jet in the vertical direction. By reducing the volume surrounded by the peripheral wall to prevent the formation of air pockets, the refrigerant can be divided evenly, and at the same time, the structure allows for size and cost reduction.
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図は小孔から衝突壁の距離と分流比率の関係を示すグ
ラフ、第6図は従来の分流器の概略形状を示す斜視図、
第6図は第6図の断面図、第7図は第6図の分流器の熱
交換器への取り付は状態を示す斜視図、第8図は第6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、17
・・・・・・流入管、18・・・・・・衝突壁、19・
・・・・・周壁、22・・・・・・流出管、16・・・
・・・段付き絞り部、L・・・・・・衝突壁からの距離
。
代理人の氏名 弁理士 粟 野 重 孝 ほか1名第2
図
13−−一 分 i 偽
+5−一・小 几
16− 段付で絞り部
13− 分流路
15− ノズル5清出口
16− 股付き絞り郁
17− 流入管
+8−−− M 9 W
tq −−−M 壁
22−−一流出管
(mm)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. A cross-sectional view, FIG. 4 is a graph showing the relationship between the distance from the small hole to the collision wall and the flow division ratio, and FIG. 6 is a perspective view showing the schematic shape of a conventional flow divider.
Figure 6 is a sectional view of Figure 6, Figure 7 is a perspective view showing how the flow divider in Figure 6 is attached to the heat exchanger, and Figure 8 is the flow divider in Figure 6 when it is in use. FIG. 3 is a cross-sectional view showing the flow of refrigerant. 13... Flow divider, 16... Small hole, 17
......Inflow pipe, 18...Collision wall, 19.
... Peripheral wall, 22 ... Outflow pipe, 16 ...
...Stepped constriction section, L...Distance from the collision wall. Name of agent: Patent attorney Shigetaka Awano and 1 other person 2nd
Figure 13--1 minute i False +5-1・small 几16- Stepped constriction section 13- Branch channel 15- Nozzle 5 outlet 16- Throttle with crotch 17- Inflow pipe +8-- M 9 W tq- --M wall 22--first outlet pipe (mm)
Claims (1)
射状に接合された複数の流出管と、円管状分流部の内周
にかん合し、かつ、衝突壁からの距離LをL<30mm
とする段付き絞り部と流出端に小孔が加工された流入管
とからなる冷媒分流器。A cylindrical flow divider with one end serving as a collision wall, a plurality of outflow pipes radially joined to the peripheral wall thereof, and a plurality of outflow pipes that are engaged with the inner periphery of the cylindrical flow divider, and the distance L from the collision wall is L< 30mm
A refrigerant flow divider consisting of a stepped constriction section and an inlet pipe with small holes at the outlet end.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1097146A JPH02275266A (en) | 1989-04-17 | 1989-04-17 | Refrigerant shunt |
| KR1019910700369A KR920701766A (en) | 1989-02-21 | 1990-08-06 | Refrigerant Sorter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1097146A JPH02275266A (en) | 1989-04-17 | 1989-04-17 | Refrigerant shunt |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02275266A true JPH02275266A (en) | 1990-11-09 |
Family
ID=14184434
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1097146A Pending JPH02275266A (en) | 1989-02-21 | 1989-04-17 | Refrigerant shunt |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02275266A (en) |
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
- 1989-04-17 JP JP1097146A patent/JPH02275266A/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 |
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