JPH05264126A - Refrigerant separator - Google Patents
Refrigerant separatorInfo
- Publication number
- JPH05264126A JPH05264126A JP4064598A JP6459892A JPH05264126A JP H05264126 A JPH05264126 A JP H05264126A JP 4064598 A JP4064598 A JP 4064598A JP 6459892 A JP6459892 A JP 6459892A JP H05264126 A JPH05264126 A JP H05264126A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- refrigerant
- pipe
- cylindrical
- heat transfer
- 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.)
- Granted
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
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/028—Evaporators having distributing means
Landscapes
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、冷凍機器や空調機器に
用いられている熱交換器の冷媒分流器に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigerant flow divider for a heat exchanger used in refrigeration equipment and air conditioning equipment.
【0002】[0002]
【従来の技術】冷凍サイクルを構成している蒸発器は、
蒸発器が小型の場合には冷媒の管内抵抗は小さく冷媒通
路も一流路で良いが、蒸発器が大型の場合には冷媒の総
流量が多く管内抵抗が大きくなるため、冷媒分流器を用
い冷媒通路を複数の流路に分け、管内抵抗を低減する方
法が多く用いられている。その冷媒分流器では蒸発器の
性能を十分に発揮させるため、各流路への分配を均等に
行えることが要求されている。2. Description of the Related Art An evaporator that constitutes a refrigeration cycle is
If the evaporator is small, the internal resistance of the refrigerant is small and the refrigerant passage may be one flow path, but if the evaporator is large, the total flow rate of the refrigerant is large and the internal resistance is large, so a refrigerant shunt is used. A method of dividing the passage into a plurality of passages to reduce the resistance in the tube is often used. In order for the refrigerant flow divider to fully exhibit the performance of the evaporator, it is required that the refrigerant is evenly distributed to each flow path.
【0003】以下、図面を参照しながら従来の冷媒分流
器の一例として特開平3−31665号公報に示す冷媒
分流器について説明する。A refrigerant distributor shown in Japanese Patent Laid-Open No. 3-31665 will be described below as an example of a conventional refrigerant distributor with reference to the drawings.
【0004】図5は従来の冷媒分流器の斜視図、図6は
断面図である。図5と図6において、21は長手方向に
伝熱管接続口22が複数設けられた円筒管で管端封止用
の仕切板23a、23bで両端は封止されている。24
は伝熱管で円筒管21の伝熱管接続口22に接続されて
いる。25は仕切板23bに設けられた穴に接続された
冷媒流入管である。26は円筒管21内部に挿入された
半円柱状の挿入部材であり、挿入部材27の斜視図を示
す図7に示すように伝熱管接続口22から挿入された伝
熱管24の先端が入るように複数の穴が設けられてい
る。FIG. 5 is a perspective view of a conventional refrigerant flow divider, and FIG. 6 is a sectional view. 5 and 6, reference numeral 21 denotes a cylindrical tube having a plurality of heat transfer tube connection ports 22 provided in the longitudinal direction, and both ends thereof are sealed by partition plates 23a and 23b for sealing the tube ends. 24
Is a heat transfer tube connected to the heat transfer tube connection port 22 of the cylindrical tube 21. Reference numeral 25 is a refrigerant inflow pipe connected to a hole provided in the partition plate 23b. Reference numeral 26 is a semi-cylindrical insertion member inserted into the inside of the cylindrical tube 21, and as shown in FIG. 7 showing a perspective view of the insertion member 27, the tip of the heat transfer tube 24 inserted from the heat transfer tube connection port 22 is inserted. Is provided with a plurality of holes.
【0005】以上のように構成された冷媒分流器につい
て、以下図面を用いてその動作を説明する。The operation of the refrigerant flow divider thus configured will be described below with reference to the drawings.
【0006】図8は従来の冷媒分流器を使用した蒸発器
の正面図である。図8において、27は熱交換効率を向
上させるため伝熱管間に接続されたフィンである。蒸発
器はフィン27や伝熱管24外面を流れる気流と、伝熱
管24内部を流れる冷媒Rとの間で熱交換を行うもので
あり、冷媒分流器は冷媒流入管25から流れ込んだ冷媒
Rを複数の伝熱管24に分配するものである。FIG. 8 is a front view of an evaporator using a conventional refrigerant flow divider. In FIG. 8, 27 is a fin connected between the heat transfer tubes in order to improve heat exchange efficiency. The evaporator exchanges heat between the airflow flowing through the fins 27 and the outer surface of the heat transfer tube 24 and the refrigerant R flowing inside the heat transfer tube 24, and the refrigerant shunt divides the plurality of refrigerant R flowing from the refrigerant inflow pipe 25. Of the heat transfer tubes 24.
【0007】一般的に蒸発器入口部分の冷媒は気液二相
の状態で流動するため、重力の影響により気相と液相は
上下に分離してしまい、上部の伝熱管では気相分が多
く、下部伝熱管では液相分が多く不均等な分流となりや
すい。しかし本従来例のように、挿入部材26により冷
媒分流器内部の流路断面積を減らし冷媒Rの流速を増す
ことによって、気液を撹はんし各伝熱管24へ均等な分
流を可能にしている。さらに、本来重力の影響により冷
媒分流器の上部では流速が低下するが、本従来例のよう
に挿入部材26の断面積を漸次変え上部ほど流路断面積
を小さくすることによって、冷媒分流器上下での冷媒流
速の差が小さく冷媒Rの均質な状態を実現し、より均等
な分流状態を保つことができる。Generally, since the refrigerant at the inlet of the evaporator flows in a gas-liquid two-phase state, the gas phase and the liquid phase are vertically separated due to the influence of gravity, and the gas phase component is separated in the upper heat transfer tube. In many cases, the lower heat transfer tube has a large amount of liquid phase and is likely to have an uneven flow distribution. However, as in this conventional example, the insertion member 26 reduces the flow passage cross-sectional area inside the refrigerant flow diverter to increase the flow velocity of the refrigerant R, thereby agitating the gas and liquid to enable uniform flow distribution to the heat transfer tubes 24. ing. Further, although the flow velocity is originally reduced in the upper portion of the refrigerant flow divider due to the influence of gravity, the cross-sectional area of the insertion member 26 is gradually changed to reduce the flow passage cross-sectional area in the upper portion as in the conventional example, so that the refrigerant flow divider upper and lower sides are reduced. It is possible to realize a homogeneous state of the refrigerant R with a small difference in the refrigerant flow velocities and to maintain a more uniform split state.
【0008】[0008]
【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、挿入部材26に伝熱管24先端を挿入す
るための精密な穴加工が必要となることから挿入部材2
6そのものが高価となることや、挿入部材26の穴に伝
熱管24を通すため工数が多く必要となるという課題を
有していた。However, in the above-mentioned structure, the insertion member 2 requires precise drilling for inserting the tip of the heat transfer tube 24 into the insertion member 26.
There are problems that 6 itself becomes expensive and that many man-hours are required to pass the heat transfer tube 24 through the hole of the insertion member 26.
【0009】本発明は上記課題に鑑み、簡単な構成によ
り冷媒分流器内の流路断面積を小さくすることによって
冷媒Rの流速を増し、さらに冷媒分流器上部の流路断面
積の方が下部より小さくでき、安価で均等な分流状態が
保てる冷媒分流器を提供するものである。In view of the above problems, the present invention increases the flow velocity of the refrigerant R by reducing the flow passage cross-sectional area in the refrigerant shunt with a simple structure, and the flow passage cross-sectional area above the refrigerant shunt is lower. (EN) Provided is a refrigerant shunt that can be made smaller, is inexpensive, and can maintain a uniform shunt state.
【0010】[0010]
【課題を解決するための手段】上記課題を解決するため
に、本発明の冷媒分流器は、長手方向に複数の流出管接
続口を有した円筒管と、前記円筒管の両端を封止する仕
切り板と、前記下端仕切り板あるいは円筒管下部に接続
された流入管と、その円筒管内部の前記伝熱管接続口の
反対面に挿入され、前記流入管位置より離れるに従い漸
次断面積が大きくなる挿入部材からなるという構成を備
えたものである。In order to solve the above-mentioned problems, a refrigerant distributor of the present invention seals a cylindrical pipe having a plurality of outlet pipe connection ports in the longitudinal direction and both ends of the cylindrical pipe. The partition plate, the lower end partition plate or the inflow pipe connected to the lower part of the cylindrical pipe, and the inner surface of the cylindrical pipe inserted into the surface opposite to the heat transfer pipe connection port, and the cross-sectional area gradually increases as the distance from the inflow pipe position increases. It is provided with a structure of an insertion member.
【0011】また、本発明の冷媒分流器は、長手方向に
複数の流出管接続口を有し、さらに流出管接続口の反対
面に管の潰し量を流入管位置より離れるに従い漸次大き
くしたプレス部を有した円筒管と、前記円筒管の両端を
封止する仕切板と、前記下端仕切板あるいは円筒管下部
に接続された流入管とからなるという構成を備えたもの
である。Further, the refrigerant flow distributor of the present invention has a plurality of outlet pipe connection ports in the longitudinal direction, and further has a crushed amount on the surface opposite to the outlet pipe connection port that gradually increases as the distance from the inlet pipe position increases. It comprises a cylindrical tube having a portion, a partition plate for sealing both ends of the cylindrical tube, and an inflow pipe connected to the lower end partition plate or the lower portion of the cylindrical tube.
【0012】[0012]
【作用】本発明は上記した構成によって、複雑な加工と
複雑な取り付け作業を要する挿入部材を用いずに、冷媒
分流器内の流路断面積を小さくし、さらに冷媒分流器上
部の流路断面積の方が下部より小さくすることにより冷
媒分流器内部の冷媒状態を均質化し各伝熱管へ均等な分
流ができる。According to the present invention, with the above-described structure, the flow passage cross-sectional area in the refrigerant flow divider is reduced without using an insert member that requires complicated processing and complicated attachment work, and the flow passage cutoff at the upper portion of the refrigerant flow divider is performed. By making the area smaller than that of the lower portion, the refrigerant state inside the refrigerant distributor can be homogenized, and uniform distribution can be made to each heat transfer tube.
【0013】[0013]
【実施例】以下本発明のの一実施例を図面を参照しなが
ら説明する。図1は第1発明の一実施例における冷媒分
流器の断面図である。図1において、1は長手方向に伝
熱管接続口2が複数設けられた円筒管で管端封止仕切り
板3a、3bで両端は封止されている。4は伝熱管で円
筒管1の伝熱管接続口2に接続されている。5は下端の
仕切り板3bに設けられた穴に接続された冷媒流入管で
ある。6は円筒管1内部の伝熱管4非挿入側つまり伝熱
管接続口2の反対面に挿入された挿入部材である。挿入
部材6は図2に示すように円柱を斜めに切断するだけの
もので、長手方向に漸次断面積が大きくなっている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a sectional view of a refrigerant flow divider in one embodiment of the first invention. In FIG. 1, reference numeral 1 denotes a cylindrical tube having a plurality of heat transfer tube connection ports 2 provided in the longitudinal direction, both ends of which are sealed by tube end sealing partition plates 3a and 3b. A heat transfer tube 4 is connected to the heat transfer tube connection port 2 of the cylindrical tube 1. Reference numeral 5 is a refrigerant inflow pipe connected to a hole provided in the partition plate 3b at the lower end. Reference numeral 6 denotes an insertion member inserted inside the cylindrical tube 1 on the non-insertion side of the heat transfer tube 4, that is, on the surface opposite to the heat transfer tube connection port 2. As shown in FIG. 2, the insertion member 6 only cuts a cylinder obliquely, and has a cross-sectional area gradually increasing in the longitudinal direction.
【0014】以上のように構成された冷媒分流器につい
て、その動作を説明する。本実施例では、挿入部材6を
挿入し冷媒分流器内部の流路断面積を減らすことによ
り、冷媒の流速が増加し、冷媒二相流の気液を撹はんし
各伝熱管へ均等な分流を可能にしている。さらに、本来
重力の影響により冷媒分流器の上部では流速が低下する
が、挿入部材6の断面積を漸次変えることにより上部ほ
ど流路断面積が小さくなり、冷媒分流器上下の冷媒流速
の差が小さく均質な状態を実現し、より均等な分流状態
を保つことができる。これらは従来例と同様の効果が得
られるものである。The operation of the refrigerant flow divider configured as described above will be described. In the present embodiment, the flow velocity of the refrigerant is increased by inserting the insertion member 6 and reducing the flow passage cross-sectional area inside the refrigerant shunt, so that the gas and liquid of the refrigerant two-phase flow are agitated to each heat transfer tube. It allows shunting. Further, although the flow velocity is originally reduced at the upper portion of the refrigerant flow divider due to the influence of gravity, the flow passage cross-sectional area becomes smaller toward the upper portion by gradually changing the cross-sectional area of the insertion member 6, and the difference in the refrigerant flow velocity between the upper and lower sides of the refrigerant flow divider is reduced. A small and homogeneous state can be realized, and a more even shunt state can be maintained. These have the same effects as the conventional example.
【0015】以上のように本実施例によれば、長手方向
に複数の流出管接続口2を有した円筒管1と、円筒管1
の両端を封止する仕切板3a、3bと、下端仕切板3b
に接続された流入管5と、円筒管1内部の伝熱管接続口
2の反対面に挿入され、流入管5位置より離れるに従い
漸次断面積が大きくなる挿入部材6から冷媒分流器を構
成することによって、均等な分流状態を安価で簡単な仕
様で実現できるものである。As described above, according to this embodiment, the cylindrical tube 1 having a plurality of outlet pipe connection ports 2 in the longitudinal direction, and the cylindrical tube 1
Partition plates 3a and 3b for sealing both ends of the lower end partition plate 3b
A refrigerant shunt is composed of an inflow pipe 5 connected to the inlet pipe 5 and an insertion member 6 inserted into the opposite surface of the heat transfer pipe connection port 2 inside the cylindrical pipe 1 and having a cross-sectional area that gradually increases with distance from the position of the inflow pipe 5. By this, it is possible to realize a uniform shunt state with inexpensive and simple specifications.
【0016】次に、以下本発明の他の実施例を図面を参
照しながら説明する。図3は他の実施例における冷媒分
流器の斜視図であり、図4は図3の断面図である。図に
おいて、11は長手方向に伝熱管接続口12が複数設け
られた円筒管で、上部には管の潰した面積を流入管位置
より離れるに従い漸次大きくしたプレス部18を有す
る。プレス部18は耐圧強度を確保するためプレス圧着
部をろう材で接合している。また、円筒管11の両端に
は管端封止仕切り板13a、13bを取り付けている。
14は伝熱管で円筒管11の伝熱管接続口12に接続さ
れている。15は下端の仕切り板3bに設けられた穴に
接続された冷媒流入管である。Next, another embodiment of the present invention will be described with reference to the drawings. FIG. 3 is a perspective view of a refrigerant flow divider in another embodiment, and FIG. 4 is a sectional view of FIG. In the figure, 11 is a cylindrical tube provided with a plurality of heat transfer tube connection ports 12 in the longitudinal direction, and has a press portion 18 in the upper part in which the crushed area of the tube is gradually increased as it moves away from the position of the inflow tube. In the press portion 18, the press crimp portion is joined with a brazing material in order to secure pressure resistance. Further, pipe end sealing partition plates 13a and 13b are attached to both ends of the cylindrical pipe 11.
A heat transfer tube 14 is connected to the heat transfer tube connection port 12 of the cylindrical tube 11. Reference numeral 15 is a refrigerant inflow pipe connected to a hole provided in the partition plate 3b at the lower end.
【0017】以上のように構成された冷媒分流器の動作
は、従来例や上述の実施例と同じく、冷媒分流器内の流
路断面積を小さくすることによって、全体的に冷媒二相
流の流速が増加し気液の撹拌が行われ、さらに冷媒分流
器内の上部ほど流路断面積を小さくすることによって重
力の影響による上下部での流速の差を抑え、冷媒分流器
内部の冷媒を均質な状態に保つことができ、均等な分流
状態を得ることができる。The operation of the refrigerant shunt configured as described above is the same as in the conventional example and the above-described embodiment. The flow velocity increases and gas-liquid is agitated.Furthermore, the flow passage cross-sectional area is made smaller in the upper part of the refrigerant flow divider to suppress the difference in flow velocity between the upper and lower parts due to the effect of gravity, and to reduce the refrigerant inside the refrigerant flow divider. It is possible to maintain a homogeneous state and obtain a uniform shunt state.
【0018】以上のように本実施例によれば、長手方向
に複数の流出管接続口12を有し、さらに流出管接続口
12の反対面に管の潰し量を流入管15より離れるに従
い漸次大きくしたプレス部18を有した円筒管11と、
円筒管11の両端を封止する仕切板13a、13bと、
下端仕切板13a接続された流入管15とからなる構成
によって、均等な分流状態を安価で簡単な仕様で実現で
きるものである。As described above, according to this embodiment, a plurality of outlet pipe connecting ports 12 are provided in the longitudinal direction, and the crushed amount of the pipe is gradually increased on the opposite surface of the outlet pipe connecting port 12 from the inlet pipe 15. A cylindrical tube 11 having an enlarged press portion 18,
Partition plates 13a and 13b for sealing both ends of the cylindrical tube 11,
With the configuration including the inflow pipe 15 connected to the lower end partition plate 13a, it is possible to realize a uniform distribution state at low cost and with simple specifications.
【0019】なお、前述の2つの実施例とも、熱交換器
の仕様として多穴伝熱管を用いたが丸管を用いたフィン
&チューブ型熱交換器でも同等の効果が得られることは
いうまでもない。In both of the above-described two embodiments, the multi-hole heat transfer tube was used as the heat exchanger specification, but it is needless to say that the same effect can be obtained with a fin & tube type heat exchanger using a round tube. Nor.
【0020】[0020]
【発明の効果】以上のように本発明は、長手方向に複数
の流出管接続口を有した円筒管と、前記円筒管の両端を
封止する仕切板と、前記下端仕切板あるいは円筒管下部
に接続された流入管と、前記円筒管内部の前記伝熱管接
続口の反対面に挿入され、前記流入管位置より離れるに
従い漸次断面積が大きくなる挿入部材から冷媒分流器を
構成することによって、均等な分流状態を安価で簡単な
仕様で実現できるものである。As described above, according to the present invention, a cylindrical pipe having a plurality of outlet pipe connection ports in the longitudinal direction, a partition plate for sealing both ends of the cylindrical pipe, the lower end partition plate or the lower part of the cylindrical pipe. By configuring the refrigerant flow divider from an inflow pipe connected to, and inserted into the surface opposite to the heat transfer pipe connection port inside the cylindrical pipe, the cross-sectional area of which gradually increases with increasing distance from the inflow pipe position. It is possible to realize a uniform shunt state with inexpensive and simple specifications.
【0021】又、本発明は、長手方向に複数の流出管接
続口を有し、さらに前記流出管接続口の反対面に管の潰
し量を前記流入管位置より離れるに従い漸次大きくした
プレス部を有した円筒管と、前記円筒管の両端を封止す
る仕切板と、前記下端仕切板あるいは円筒管下部に接続
された流入管とからなる構成によって、均等な分流状態
を安価で簡単な仕様で実現できるものである。Further, according to the present invention, there is provided a press portion having a plurality of outlet pipe connecting ports in the longitudinal direction and further having a crushed amount of the pipe gradually increased with distance from the inlet pipe position on the surface opposite to the outlet pipe connecting port. With a cylindrical tube having a partition plate that seals both ends of the cylindrical tube, and an inflow tube connected to the lower end partition plate or the lower portion of the cylindrical tube, a uniform diversion state can be obtained at low cost and with simple specifications. It can be realized.
【図1】本発明の一実施例における冷媒分流器の断面図FIG. 1 is a sectional view of a refrigerant flow divider according to an embodiment of the present invention.
【図2】本発明の一実施例における挿入部材の斜視図FIG. 2 is a perspective view of an insertion member according to an embodiment of the present invention.
【図3】本発明の他の実施例における冷媒分流器の斜視
図FIG. 3 is a perspective view of a refrigerant flow divider according to another embodiment of the present invention.
【図4】図3における冷媒分流器の断面図FIG. 4 is a sectional view of the refrigerant flow divider in FIG.
【図5】従来の冷媒分流器の斜視図FIG. 5 is a perspective view of a conventional refrigerant flow divider.
【図6】従来の冷媒分流器の断面図FIG. 6 is a sectional view of a conventional refrigerant flow divider.
【図7】従来の挿入部材の斜視図FIG. 7 is a perspective view of a conventional insertion member.
【図8】従来の冷媒分流器を用いた熱交換器の正面図FIG. 8 is a front view of a heat exchanger using a conventional refrigerant flow divider.
1、11 円筒管 2、12 伝熱管接続口 3a、3b、13a、13b 仕切板 4、14 伝熱管 5、15 流入管 6 挿入部材 18 プレス部 1, 11 Cylindrical tube 2, 12 Heat transfer tube connection port 3a, 3b, 13a, 13b Partition plate 4, 14 Heat transfer tube 5, 15 Inflow tube 6 Insert member 18 Press section
Claims (2)
筒管と、前記円筒管の両端を封止する仕切板と、前記下
端仕切板あるいは円筒管下部に接続された流入管と、前
記円筒管内部の前記伝熱管接続口の反対面に挿入され、
前記流入管位置より離れるに従い漸次断面積が大きくな
る挿入部材からなる冷媒分流器。1. A cylindrical pipe having a plurality of outlet pipe connection ports in a longitudinal direction, partition plates for sealing both ends of the cylindrical pipe, and an inflow pipe connected to the lower end partition plate or the lower part of the cylindrical pipe. Inserted on the opposite surface of the heat transfer tube connection port inside the cylindrical tube,
A refrigerant flow divider comprising an insertion member whose cross-sectional area gradually increases with distance from the inflow pipe position.
らに前記流出管接続口の反対面に管の潰し量を流入管位
置より離れるに従い漸次大きくしたプレス部を有した円
筒管と、前記円筒管の両端を封止する仕切板と、前記下
端仕切板あるいは円筒管下部に接続された流入管とから
なる冷媒分流器2. A cylindrical pipe having a plurality of outlet pipe connecting ports in the longitudinal direction, and further having a press portion on the surface opposite to the outlet pipe connecting port, in which the crushed amount of the pipe is gradually increased as the distance from the inlet pipe position increases. A refrigerant distributor comprising a partition plate for sealing both ends of the cylindrical pipe and an inflow pipe connected to the lower end partition plate or the lower part of the cylindrical pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06459892A JP3210062B2 (en) | 1992-03-23 | 1992-03-23 | Refrigerant flow divider |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06459892A JP3210062B2 (en) | 1992-03-23 | 1992-03-23 | Refrigerant flow divider |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05264126A true JPH05264126A (en) | 1993-10-12 |
JP3210062B2 JP3210062B2 (en) | 2001-09-17 |
Family
ID=13262856
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP06459892A Expired - Fee Related JP3210062B2 (en) | 1992-03-23 | 1992-03-23 | Refrigerant flow divider |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3210062B2 (en) |
Cited By (13)
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EP1798506A2 (en) * | 2005-12-13 | 2007-06-20 | Behr GmbH & Co. KG | Heat exchanger, more particularly evaporator |
JP2013002688A (en) * | 2011-06-14 | 2013-01-07 | Sharp Corp | Parallel flow type heat exchanger and air conditioner with the same |
EP2236973A3 (en) * | 2009-03-25 | 2014-04-23 | Sanhua Holding Group Co., Ltd. | Refrigerant distributer for heat exchanger and heat exchanger |
CN104764256A (en) * | 2015-03-31 | 2015-07-08 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system with the same |
EP2570754A3 (en) * | 2011-09-19 | 2015-10-21 | Liebherr-Hausgeräte Ochsenhausen GmbH | Multi channel evaporator system |
JP6155412B1 (en) * | 2016-09-12 | 2017-06-28 | 三菱電機株式会社 | Header, heat exchanger and air conditioner |
US9772145B2 (en) | 2011-06-24 | 2017-09-26 | Mitsubishi Electric Corporation | Flat plate heat exchanger having fluid distributor inside manifold |
JP2017207204A (en) * | 2016-05-12 | 2017-11-24 | 三菱ケミカルインフラテック株式会社 | Header member, manufacturing method of header member, water/hot water supply pipe facility, and water/hot water supply system |
WO2018047416A1 (en) * | 2016-09-12 | 2018-03-15 | 三菱電機株式会社 | Air conditioner |
JP2018044759A (en) * | 2017-06-05 | 2018-03-22 | 三菱電機株式会社 | Header and air conditioner |
WO2018173256A1 (en) * | 2017-03-24 | 2018-09-27 | 三菱電機株式会社 | Air conditioning device |
US11421947B2 (en) * | 2015-09-07 | 2022-08-23 | Mitsubishi Electric Corporation | Laminated header, heat exchanger, and air-conditioning apparatus |
WO2024111331A1 (en) * | 2022-11-24 | 2024-05-30 | サンデン株式会社 | Heat exchanger |
-
1992
- 1992-03-23 JP JP06459892A patent/JP3210062B2/en not_active Expired - Fee Related
Cited By (21)
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EP1798506A2 (en) * | 2005-12-13 | 2007-06-20 | Behr GmbH & Co. KG | Heat exchanger, more particularly evaporator |
EP1798506A3 (en) * | 2005-12-13 | 2012-06-06 | Behr GmbH & Co. KG | Heat exchanger, more particularly evaporator |
EP2236973A3 (en) * | 2009-03-25 | 2014-04-23 | Sanhua Holding Group Co., Ltd. | Refrigerant distributer for heat exchanger and heat exchanger |
JP2013002688A (en) * | 2011-06-14 | 2013-01-07 | Sharp Corp | Parallel flow type heat exchanger and air conditioner with the same |
US9772145B2 (en) | 2011-06-24 | 2017-09-26 | Mitsubishi Electric Corporation | Flat plate heat exchanger having fluid distributor inside manifold |
EP2570754A3 (en) * | 2011-09-19 | 2015-10-21 | Liebherr-Hausgeräte Ochsenhausen GmbH | Multi channel evaporator system |
CN104764256A (en) * | 2015-03-31 | 2015-07-08 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system with the same |
WO2016155367A1 (en) * | 2015-03-31 | 2016-10-06 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system having same |
US11421947B2 (en) * | 2015-09-07 | 2022-08-23 | Mitsubishi Electric Corporation | Laminated header, heat exchanger, and air-conditioning apparatus |
JP2017207204A (en) * | 2016-05-12 | 2017-11-24 | 三菱ケミカルインフラテック株式会社 | Header member, manufacturing method of header member, water/hot water supply pipe facility, and water/hot water supply system |
WO2018047332A1 (en) * | 2016-09-12 | 2018-03-15 | 三菱電機株式会社 | Header, heat exchanger, and air conditioner |
WO2018047416A1 (en) * | 2016-09-12 | 2018-03-15 | 三菱電機株式会社 | Air conditioner |
WO2018047330A1 (en) * | 2016-09-12 | 2018-03-15 | 三菱電機株式会社 | Air conditioner |
GB2569898A (en) * | 2016-09-12 | 2019-07-03 | Mitsubishi Electric Corp | Air conditioner |
US10760832B2 (en) | 2016-09-12 | 2020-09-01 | Mitsubishi Electric Corporation | Air-conditioning apparatus |
GB2569898B (en) * | 2016-09-12 | 2021-02-03 | Mitsubishi Electric Corp | Air-conditioning apparatus |
JP6155412B1 (en) * | 2016-09-12 | 2017-06-28 | 三菱電機株式会社 | Header, heat exchanger and air conditioner |
WO2018173256A1 (en) * | 2017-03-24 | 2018-09-27 | 三菱電機株式会社 | Air conditioning device |
JPWO2018173256A1 (en) * | 2017-03-24 | 2019-11-07 | 三菱電機株式会社 | Air conditioner |
JP2018044759A (en) * | 2017-06-05 | 2018-03-22 | 三菱電機株式会社 | Header and air conditioner |
WO2024111331A1 (en) * | 2022-11-24 | 2024-05-30 | サンデン株式会社 | Heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
JP3210062B2 (en) | 2001-09-17 |
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