JPH01155162A - Refrigerant converging instrument for evaporator - Google Patents
Refrigerant converging instrument for evaporatorInfo
- Publication number
- JPH01155162A JPH01155162A JP62314581A JP31458187A JPH01155162A JP H01155162 A JPH01155162 A JP H01155162A JP 62314581 A JP62314581 A JP 62314581A JP 31458187 A JP31458187 A JP 31458187A JP H01155162 A JPH01155162 A JP H01155162A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- orifice
- flow rate
- 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
Landscapes
- Containers, Films, And Cooling For Superconductive Devices (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蒸発器において、冷媒
を均等に流すたのの蒸発器の冷媒合流器に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigerant merger for an evaporator of an air conditioner, a refrigeration equipment, etc., which allows refrigerant to flow uniformly.
従来の技術
近年、熱交換器の伝熱管管径の縮小に伴う複数回路化に
対応するために、冷媒合流器が多用化されてきており、
その重用度が増している。Conventional technology In recent years, refrigerant combiners have been used more and more in order to cope with the need for multiple circuits due to the reduction in the diameter of heat exchanger tubes in heat exchangers.
Its importance is increasing.
以下、図面を参照しながら上述した従来の冷媒合流器に
ついて説明を行う。Hereinafter, the conventional refrigerant merger mentioned above will be explained with reference to the drawings.
第5図は従来の冷媒合流器の断面形状を示し、第6図は
第5図の冷媒合流器を蒸発器に接続した冷媒回路を示す
。第5図と第6図において、1は冷媒合流器で、2は冷
媒合流器1の外郭をなす中空体で、複数の流入口3と単
一の流出口4とを備えている。5は蒸発器、6は冷媒分
流器で、冷媒分流器6で冷媒回路を2回路に分けて2回
路5a。FIG. 5 shows a cross-sectional shape of a conventional refrigerant merger, and FIG. 6 shows a refrigerant circuit in which the refrigerant merger of FIG. 5 is connected to an evaporator. In FIGS. 5 and 6, 1 is a refrigerant merger, and 2 is a hollow body forming the outer shell of the refrigerant merger 1, and is provided with a plurality of inlets 3 and a single outlet 4. 5 is an evaporator, 6 is a refrigerant divider, and the refrigerant divider 6 divides the refrigerant circuit into two circuits, forming two circuits 5a.
5bを持った蒸発器5に接続し、更に蒸発器5を出た後
の2回路を冷媒合流器1で1回路に合流している。5b, and the two circuits after leaving the evaporator 5 are merged into one circuit at the refrigerant merger 1.
以上のように構成された冷媒合流器について、以下第6
図を用いてその動作を説明する。Regarding the refrigerant merger configured as above, the sixth section will be described below.
The operation will be explained using figures.
冷媒Aは冷媒分流器6で冷媒A1と冷媒A2とに分けら
れる。次に冷媒A1と冷媒A2は蒸発器5に流入し、そ
れぞれ蒸発器5内の回i?85a及び5bで蒸完熱交換
する。更に蒸発器5を出た冷媒A1と冷媒A2は、冷媒
合流器1で合流し、1回路となって流出する。Refrigerant A is divided into refrigerant A1 and refrigerant A2 by a refrigerant flow divider 6. Next, the refrigerant A1 and the refrigerant A2 flow into the evaporator 5, and the refrigerant A1 and the refrigerant A2 respectively flow through the i? 85a and 5b exchange heat for complete steaming. Further, the refrigerant A1 and the refrigerant A2 that have exited the evaporator 5 are combined in the refrigerant merger 1, and flow out as one circuit.
発明が解決しようとする問題点
しかしながら上記のような構成では、冷媒分流器6に分
流比率の悪いものを用いたり、蒸発器5内の回!85a
と5bの回路長さや負荷バランスが悪い場合には、冷媒
A1とA2の流量が等しくならず、蒸発器5での蒸発能
力が低下するという問題点を有していた。Problems to be Solved by the Invention However, in the above configuration, a refrigerant flow divider 6 with a poor flow ratio is used, and the flow inside the evaporator 5 is reduced. 85a
If the circuit lengths and load balance between the refrigerants A1 and A2 are not equal, the flow rates of the refrigerants A1 and A2 will not be equal, resulting in a problem that the evaporation capacity of the evaporator 5 will be reduced.
本発明は」二記問題点に鑑み、冷媒分流器に分流比率の
悪いものを用いたり、蒸発器内の回路長さや負荷バラン
スが悪い場合でも、蒸発器出口の各回路の冷媒試態をほ
ぼ同等に保ち、安定した蒸発能力が得られる冷媒合流器
を提供するものである。In view of the problems described in item 2, the present invention has been developed so that even if a refrigerant divider with a poor distribution ratio is used, or the circuit length or load balance in the evaporator is poor, the refrigerant state in each circuit at the evaporator outlet can be almost maintained. The present invention provides a refrigerant combiner that maintains the same evaporation capacity and provides stable evaporation capacity.
問題点を解決するための手段
」二記問題点を解決するために本発明の冷媒合流器は、
複数の流入口と単一の流出口とからなる中空体と、磁性
体から成るオリフィスとを備え、前記オリフィスが中空
体内で冷媒の流れと垂直方向に稼動し、かつ前記オリフ
ィスが稼動時に接する中空体の内壁面に超電導体を設け
るという構成を備えたものである。Means for Solving the Problems In order to solve the second problem, the refrigerant combiner of the present invention has the following features:
A hollow body comprising a hollow body having a plurality of inlets and a single outlet, and an orifice made of a magnetic material, wherein the orifice operates in a direction perpendicular to the flow of refrigerant within the hollow body, and the orifice is in contact with the flow of the refrigerant during operation. It has a structure in which a superconductor is provided on the inner wall surface of the body.
作用
本発明は−1−記した構成によって、蒸発器内の各回路
の冷媒流量バランスが悪く冷媒合流器に流入するいずれ
かの回路の冷媒温度が一定以下に下がった時に、中空体
の内壁面に取り付けた超電導体が反磁性となって、オリ
フィスを構成する磁性体との間で反発力を生じるために
オリフィスが移動し、冷媒温度が下がった側の回路を狭
めることにより冷媒流量バランスを修正し、合流器に流
入する各回路の冷媒温度をほぼ同等に保って、安定した
蒸発能力が得られることとなる。Effect of the present invention -1- With the configuration described above, when the refrigerant flow rate in each circuit in the evaporator is unbalanced and the refrigerant temperature in any of the circuits flowing into the refrigerant combiner falls below a certain level, the inner wall surface of the hollow body The superconductor attached to the refrigerant becomes diamagnetic and generates a repulsive force with the magnetic material that makes up the orifice, causing the orifice to move and correct the refrigerant flow balance by narrowing the circuit on the side where the refrigerant temperature has decreased. However, the temperature of the refrigerant in each circuit flowing into the confluencer is kept approximately the same, and stable evaporation capacity can be obtained.
実施例
以下本発明の一実施例の冷媒合流器について図面を参照
しながら説明する。EXAMPLE Hereinafter, a refrigerant merger according to an example of the present invention will be described with reference to the drawings.
第1図は本発明の一実施例における冷媒合流器の断面形
状を示すもので、第2図は第1図の冷媒合流器を蒸発器
に接続した冷媒回路を示す。第1図と第2図において、
7は冷媒合流器で、8は冷媒合流器7の外郭をなす中空
体で、複数の流入口9と単一の流出口10とを備えてい
る。11は中空体8内に設けられた稼動式のオリフィス
で、磁性体12から成っている。又、前記オリフィス1
1と接する中空体8の内壁面には超電導体13が設けで
ある。更に、14は蒸発器、15は冷媒分流器で、冷媒
分流器15で冷媒回路を2回路に分けて2回路14a、
14bを持った蒸発器14に接続し、更に蒸発器14を
出た後の2回路を冷媒合流器7で1回路に合流している
。FIG. 1 shows a cross-sectional shape of a refrigerant combiner in one embodiment of the present invention, and FIG. 2 shows a refrigerant circuit in which the refrigerant combiner of FIG. 1 is connected to an evaporator. In Figures 1 and 2,
7 is a refrigerant merger, and 8 is a hollow body forming the outer shell of the refrigerant merger 7, and is provided with a plurality of inlets 9 and a single outlet 10. A movable orifice 11 is provided in the hollow body 8 and is made of a magnetic material 12. Moreover, the orifice 1
A superconductor 13 is provided on the inner wall surface of the hollow body 8 in contact with the superconductor 1 . Furthermore, 14 is an evaporator, 15 is a refrigerant divider, and the refrigerant circuit is divided into two circuits by the refrigerant divider 15, and two circuits 14a,
14b, and the two circuits after leaving the evaporator 14 are merged into one circuit at the refrigerant combiner 7.
以上のように構成された冷媒合流器について、以下第2
図から第4図を用いてその動作について説明する。Regarding the refrigerant merger configured as above, the second
The operation will be explained with reference to FIGS.
冷媒Bは冷媒分流器15で2回路の冷媒B1と冷媒B2
とに分けられる。次に冷媒B1と冷媒B2は蒸発器14
に流入し、それぞれ蒸発器14内の回路14a及び14
bで蒸発熱交換する。更に蒸発器14を出た冷媒B1と
冷媒B2は冷媒合流器7で合流し、1回路となって流出
する。The refrigerant B is divided into two circuits, refrigerant B1 and refrigerant B2, by the refrigerant flow divider 15.
It can be divided into Next, the refrigerant B1 and refrigerant B2 are transferred to the evaporator 14.
into circuits 14a and 14 in evaporator 14, respectively.
The heat of evaporation is exchanged in b. Further, the refrigerant B1 and the refrigerant B2 that have exited the evaporator 14 are combined in the refrigerant merger 7, and flow out as one circuit.
この際、蒸発器14の各回路14a及び14 bにおけ
る冷媒B1と冷媒B2の流量バランスが良いときには、
蒸発器14出口の冷媒B1と冷媒B2の温度がほぼ等し
くかつ一定の冷媒過熱域温度を保つので、中空体8の内
壁面に設けられた超電導体13は反磁性を生じることな
く、オリフィス11との間には力が働かず、オリフィス
11は中空体8のほぼ中央に位置し、冷媒B1と冷媒B
2を均等に流す。At this time, when the flow rate balance of refrigerant B1 and refrigerant B2 in each circuit 14a and 14b of the evaporator 14 is good,
Since the temperatures of refrigerant B1 and refrigerant B2 at the outlet of the evaporator 14 are approximately equal and maintain a constant refrigerant superheating region temperature, the superconductor 13 provided on the inner wall surface of the hollow body 8 does not generate diamagnetic properties and is able to interact with the orifice 11. No force acts between them, and the orifice 11 is located approximately in the center of the hollow body 8, and the refrigerant B1 and the refrigerant B
Pour 2 evenly.
又、蒸発器14の各回路14a及び14bにおける冷媒
B1と冷媒B2の流量バランスが悪いときには、蒸発器
14出口の冷媒B1と冷媒B2の温度に大きく差を生じ
、第3図に示すように冷媒B1の流量が大きい場合には
、蒸発器14の14a側回路出口の冷媒B1の過熱度が
取れなくなり、冷媒合流器8の流入口9a側に流入する
冷媒B1の温度が下がるために超電導体13aが反磁性
となり、磁性体12aとの間で反発力Fを生じてオリフ
ィス11は流入口9b側へ移動し、その結果、冷媒B1
側の流路が挟まり、冷媒B2側の流路が広がることとな
り、冷媒B1と冷媒B2との流量差を小さくするように
働く。逆に、第4図に示すように冷媒132の流量が大
きい場合には、蒸発器14の14 b i!l’1回路
出口の冷媒B2の過熱度が取れなくなり、冷媒合流器8
の流入[LIQb側に流入する冷媒B2の温度が下がる
ために超電導体13bが反磁性となり、磁性体12bと
の間で反発力Fを生じてオリフィス11は流入D Q
a側へ移動し、その結果、冷媒B2側の流路が挟まり、
冷媒B1側の流路が広がることとなり、冷媒B1と冷媒
B2との流量差を小さくするように働く。Further, when the flow rate balance of refrigerant B1 and refrigerant B2 in each circuit 14a and 14b of the evaporator 14 is poor, a large difference occurs in the temperature of refrigerant B1 and refrigerant B2 at the outlet of the evaporator 14, and as shown in FIG. When the flow rate of B1 is large, the degree of superheating of the refrigerant B1 at the 14a side circuit outlet of the evaporator 14 cannot be maintained, and the temperature of the refrigerant B1 flowing into the inlet 9a side of the refrigerant combiner 8 decreases, so that the superconductor 13a becomes diamagnetic, generates a repulsive force F with the magnetic body 12a, and the orifice 11 moves toward the inlet port 9b. As a result, the refrigerant B1
The flow path on the side is pinched, and the flow path on the refrigerant B2 side is widened, working to reduce the difference in flow rate between the refrigerant B1 and the refrigerant B2. Conversely, when the flow rate of the refrigerant 132 is large as shown in FIG. 4, 14 b i! The degree of superheating of the refrigerant B2 at the l'1 circuit outlet cannot be removed, and the refrigerant combiner 8
Inflow [Due to the temperature of refrigerant B2 flowing into the LIQb side decreasing, superconductor 13b becomes diamagnetic, and a repulsive force F is generated between the superconductor 13b and the magnetic material 12b, causing orifice 11 to
As a result, the flow path on the refrigerant B2 side is pinched,
The flow path on the side of the refrigerant B1 is widened, which works to reduce the difference in flow rate between the refrigerant B1 and the refrigerant B2.
以上のように本実施例によれば、複数の流入口9と単一
の流出口10とからなる中空体7と、磁性体12から成
るオリフィス11とを備え、前記オリフィス11が中空
体8内で冷媒の流れと垂直方向に稼動し、かつ前記オリ
フィス11が稼動時に接する中空体8の内壁面に超電導
体13を設けた冷媒合流器7を蒸発器14の冷媒出口側
に接続することにより、蒸発器14の2回路14a及び
14bを流れる冷媒B1と冷媒B2との流量バランスを
ほぼ同等に保ち、安定した蒸発能力を得ることができる
。As described above, according to this embodiment, the hollow body 7 includes a plurality of inlets 9 and a single outlet 10, and the orifice 11 includes a magnetic material 12, and the orifice 11 is located inside the hollow body 8. By connecting the refrigerant merger 7 to the refrigerant outlet side of the evaporator 14, which operates in a direction perpendicular to the flow of the refrigerant and has a superconductor 13 on the inner wall surface of the hollow body 8 that the orifice 11 contacts during operation. The flow balance of the refrigerant B1 and the refrigerant B2 flowing through the two circuits 14a and 14b of the evaporator 14 can be kept almost equal, and stable evaporation capacity can be obtained.
なお常温付近で超電導を示す材料としては、5rBaY
Cu307−δが知られている。製造に際しては、まず
原料粉末の粉砕、混合を行なう。それを、920°C空
気中で5時間焼製した後粉砕し、それを3回繰り返す、
その粉末を整形し、1000゜C空気中で焼結1)、炉
中で冷却する。このようにして作製された焼結体は、3
38K(65°C)で超電導を示す(イハラ他、ジャパ
ニーズ ジャーナル オブ アプライド フィジックス
(JAPANESE JOUrtNAL OF
APPLIED PHYS LC3) Vo I、
26.No8゜August、1,987.PP167
171 )。Note that 5rBaY is a material that exhibits superconductivity near room temperature.
Cu307-δ is known. During production, first the raw material powder is crushed and mixed. It is baked at 920°C in air for 5 hours, then crushed, and the process is repeated three times.
The powder is shaped, sintered at 1000°C in air (1), and cooled in a furnace. The sintered body produced in this way has 3
Shows superconductivity at 38K (65°C) (Ihara et al., Japanese Journal of Applied Physics)
APPLIED PHYS LC3) Vo I,
26. No. 8° August, 1,987. PP167
171).
発明の効果
以上のように本発明は、複数の流入口と単一の流出口と
からなる中空体と、磁性体から成るオリフィスとを備え
、前記オリフィスが中空体内で冷媒の流れと垂直方向に
稼動し、かつ前記オリフィスが稼動時に接する中空体の
内壁面に超電導体を設けることにより、蒸発器内の各回
路の冷媒流量バランスが悪く冷媒合流器に流入するいず
れかの回路の冷媒温度が一定以下に下がった時に、中空
体の内壁面に取り付けた超電導体が反磁性となってオリ
フィスを構成する磁性体との間で反発力を生じるために
オリフィスが移動し、冷媒温度が下がった側の回路を狭
めることにより冷媒流量バランスを修正し、合流器に流
入する各回路の冷媒温度をほぼ同等に保って安定した蒸
発能力を得ることができる。Effects of the Invention As described above, the present invention includes a hollow body consisting of a plurality of inlets and a single outlet, and an orifice made of a magnetic material, and the orifice is arranged in the hollow body in a direction perpendicular to the flow of refrigerant. By providing a superconductor on the inner wall surface of the hollow body that is in operation and in contact with the orifice during operation, the refrigerant temperature in any circuit that flows into the refrigerant merger due to unbalanced refrigerant flow rate in each circuit in the evaporator is kept constant. When the temperature of the refrigerant drops to below, the superconductor attached to the inner wall of the hollow body becomes diamagnetic and generates a repulsive force between the orifice and the magnetic material that makes up the orifice, causing the orifice to move. By narrowing the circuits, the refrigerant flow balance can be corrected, and the refrigerant temperature in each circuit flowing into the confluencer can be kept approximately the same, thereby achieving stable evaporation capacity.
【図面の簡単な説明】
第1図は本発明の冷媒合流器の概略形状を示す断面図、
第2図は第1図の冷媒合流器を蒸発器に接続した冷媒回
路図、第3図及び第4図は第1図の冷媒分流器の動作状
態を示す断面図、第5図は従来の冷媒合流器の概略形状
を示す断面図、第6図は第5図の冷媒合流器を蒸発器に
接続した冷媒回路図である。
7・・・冷媒合流器、8・・・中空体、9・・・流入口
、10・・・流出口、11・・・オリフィス、12・・
・磁性体、13・・・超電導体。
代理人の氏名 弁理士 中尾敏男 他1名7−玲媒合3
乏6
8− 中証体
?−流流入
−2−磁性体
13−・Jiat体
9−0流入口
+3−Jt弧善美
体 4 図
第 5 図
第6図[BRIEF DESCRIPTION OF THE DRAWINGS] FIG. 1 is a sectional view showing the general shape of the refrigerant combiner of the present invention;
Fig. 2 is a refrigerant circuit diagram in which the refrigerant merger shown in Fig. 1 is connected to an evaporator, Figs. 3 and 4 are sectional views showing the operating state of the refrigerant divider shown in Fig. 1, and Fig. 5 is a conventional refrigerant flow divider. FIG. 6 is a sectional view showing the general shape of the refrigerant merger, and is a refrigerant circuit diagram in which the refrigerant merger of FIG. 5 is connected to an evaporator. 7... Refrigerant merger, 8... Hollow body, 9... Inlet, 10... Outlet, 11... Orifice, 12...
・Magnetic material, 13... superconductor. Name of agent: Patent attorney Toshio Nakao and 1 other person 7 - Rei Media 3
Poor 6 8- Medium body? -Inflow/Inflow-2-Magnetic body 13-・Jiat body 9-0 inlet +3-Jt arc good body 4 Figure 5 Figure 6
Claims (1)
性体から成るオリフィスとを備え、前記オリフィスが中
空体内で冷媒の流れと垂直方向に稼動し、かつ前記オリ
フィスが稼動時に接する中空体の内壁面に超電導体を設
けたことを特徴とする蒸発器の冷媒合流器。A hollow body comprising a hollow body having a plurality of inlets and a single outlet, and an orifice made of a magnetic material, wherein the orifice operates in a direction perpendicular to the flow of refrigerant within the hollow body, and the orifice is in contact with the flow of the refrigerant during operation. A refrigerant mixer for an evaporator, characterized in that a superconductor is provided on the inner wall surface of the evaporator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62314581A JPH01155162A (en) | 1987-12-11 | 1987-12-11 | Refrigerant converging instrument for evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62314581A JPH01155162A (en) | 1987-12-11 | 1987-12-11 | Refrigerant converging instrument for evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01155162A true JPH01155162A (en) | 1989-06-19 |
Family
ID=18055018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62314581A Pending JPH01155162A (en) | 1987-12-11 | 1987-12-11 | Refrigerant converging instrument for evaporator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01155162A (en) |
-
1987
- 1987-12-11 JP JP62314581A patent/JPH01155162A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20210102759A1 (en) | Heat exchanger and air-conditioning system | |
| KR102031021B1 (en) | Layered header, heat exchanger, and air-conditioning device | |
| US5076353A (en) | Liquefier for the coolant in a vehicle air-conditioning system | |
| US20020179294A1 (en) | Tube and shell heat exchanger for multiple circuit refrigerant system | |
| EP3760949A1 (en) | Heat exchanger unit and air conditioner using same | |
| US3120743A (en) | Refrigeration system including metering and distributing means | |
| JPH01155162A (en) | Refrigerant converging instrument for evaporator | |
| US11402161B2 (en) | Distributor, heat exchanger, indoor unit, outdoor unit, and air-conditioning device | |
| JPH01219458A (en) | Refrigerant confluence device | |
| JP4449153B2 (en) | Outdoor heat exchanger, indoor heat exchanger, and air conditioner | |
| JPH1183349A (en) | Two-layer pipe having self-temperature control function and heat exchanger using the same | |
| US20250063688A1 (en) | Optimized chip cooling infrastructure | |
| JP3336628B2 (en) | Refrigeration equipment | |
| CN115077135B (en) | Heat exchanger, control method for heat exchanger and heat pump system | |
| JPH06194003A (en) | Air conditioner | |
| JPH1144461A (en) | refrigerator | |
| JPH07294061A (en) | Refrigerant flow divider | |
| JPH02219986A (en) | Heat exchanger | |
| JP2749549B2 (en) | Double inlet pulse tube refrigerator | |
| JPH01169281A (en) | Evaporator | |
| JPS6433479A (en) | Flow diverter for refrigerator | |
| JP3326930B2 (en) | Refrigerant shunt | |
| JPH02115668A (en) | Evaporator | |
| Gessner et al. | Miniature Claude and Reverse Brayton Cycle Turbomachinery Refrigerators | |
| JPS5918277Y2 (en) | Refrigeration equipment |