JP7026916B2 - Liquid shunt for heat exchanger and Delon cup type heat exchanger - Google Patents

Liquid shunt for heat exchanger and Delon cup type heat exchanger Download PDF

Info

Publication number
JP7026916B2
JP7026916B2 JP2018076271A JP2018076271A JP7026916B2 JP 7026916 B2 JP7026916 B2 JP 7026916B2 JP 2018076271 A JP2018076271 A JP 2018076271A JP 2018076271 A JP2018076271 A JP 2018076271A JP 7026916 B2 JP7026916 B2 JP 7026916B2
Authority
JP
Japan
Prior art keywords
liquid
heat exchanger
plates
cup type
type heat
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.)
Active
Application number
JP2018076271A
Other languages
Japanese (ja)
Other versions
JP2019184168A (en
Inventor
望 大友
昇 大友
満 石川
秀高 茅沼
徳征 工藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Atago Seisakusho Co Ltd
Ishikawa Energy Research Co Ltd
Original Assignee
Atago Seisakusho Co Ltd
Ishikawa Energy Research Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Atago Seisakusho Co Ltd, Ishikawa Energy Research Co Ltd filed Critical Atago Seisakusho Co Ltd
Priority to JP2018076271A priority Critical patent/JP7026916B2/en
Publication of JP2019184168A publication Critical patent/JP2019184168A/en
Application granted granted Critical
Publication of JP7026916B2 publication Critical patent/JP7026916B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)

Description

本発明は、熱交換器に使用される液体分流器及びそれを備えたドロンカップ型熱交換器に関する。 The present invention relates to a liquid shunt used in a heat exchanger and a drone cup type heat exchanger equipped with the liquid shunt.

近年、省エネルギー意識の高まりから、廃棄熱から熱を回収し、冷凍サイクルを回すことで、空調を行なうシステムが注目されている。それらは、エジェクター冷凍サイクルや吸収式冷凍サイクルなどの熱駆動サイクルで、減圧下で作動するものが多い。 In recent years, due to the growing awareness of energy conservation, a system that recovers heat from waste heat and rotates a refrigeration cycle to perform air conditioning has attracted attention. They are heat-driven cycles such as the ejector refrigeration cycle and the absorption refrigeration cycle, many of which operate under reduced pressure.

エジェクター冷凍サイクルには、多彩な熱交換器が使用される。その1つに、排気ガスなどの高温熱源媒体を利用し、冷媒液を蒸発させる熱交換器(ボイラー)や、低温熱源媒体(ガスや水)から熱を奪って冷媒液を蒸発させる熱交換器(蒸発器)がある。蒸発効率の向上には、気液または液液(熱源媒体と冷媒液)の接触伝熱面積を高密度で集積させることが望ましいため、一対のドロンカッププレートからなるコアユニットを多段に積層してなるドロンカップ型熱交換器が採用される。この場合、供給される冷媒液を分流し、多段に積層されたドロンカッププレート面に、平行かつ均一に分散接触させることが重要である。 A variety of heat exchangers are used in the ejector refrigeration cycle. One of them is a heat exchanger (boiler) that uses a high-temperature heat source medium such as exhaust gas to evaporate the refrigerant liquid, and a heat exchanger that removes heat from the low-temperature heat source medium (gas or water) and evaporates the refrigerant liquid. There is a (evaporator). In order to improve the evaporation efficiency, it is desirable to integrate the contact heat transfer area of gas or liquid (heat source medium and refrigerant liquid) at high density, so core units consisting of a pair of Delon cup plates are stacked in multiple stages. A Delon cup type heat exchanger is adopted. In this case, it is important to separate the supplied refrigerant liquid and bring it into parallel and uniformly dispersed contact with the surface of the Delon cup plates stacked in multiple stages.

一方、吸収式冷凍サイクルでは、同様な構成が蒸発器と吸収器に利用される。この場合は、熱源媒体は水などの液体であることが多く、液体と液体の熱交換となる。蒸発器では、水などの低温媒体から熱を奪い冷媒を蒸発させる。一方、吸収器では、冷却水などの熱源媒体を用いて、吸収液が冷媒蒸気を吸収する際に生じる吸収熱を回収する。蒸発器も吸収器も蒸発や吸収の促進のために、適切に供給液(冷媒液や吸収液)を分流することがエジェクター冷凍サイクルと同様に重要である。 On the other hand, in the absorption refrigeration cycle, a similar configuration is used for the evaporator and absorber. In this case, the heat source medium is often a liquid such as water, and heat exchange between the liquid and the liquid occurs. In the evaporator, heat is taken from a low temperature medium such as water to evaporate the refrigerant. On the other hand, in the absorber, a heat source medium such as cooling water is used to recover the absorbed heat generated when the absorbing liquid absorbs the refrigerant vapor. As with the ejector refrigeration cycle, it is as important for both the evaporator and the absorber to properly separate the supply liquid (refrigerant liquid and absorption liquid) in order to promote evaporation and absorption.

図7は従来の液体分流器を備えたドロンカップ型熱交換器を示す図である。ドロンカップ型熱交換器10は、上下を最中状に膨らませて形成し、中間部を細長扁平形状に形成してなる、同形の一対のドロンカッププレートからなるコアユニット11を多段に積層して構成される。 FIG. 7 is a diagram showing a Delon cup type heat exchanger equipped with a conventional liquid shunt. The Delon cup type heat exchanger 10 is formed by inflating the upper and lower parts in the middle, and the core unit 11 made of a pair of Delon cup plates of the same shape, which is formed in an elongated flat shape at the middle portion, is laminated in multiple stages. It is composed.

最端のコアユニット11に熱源媒体の流入口17及び流出口18が設けられている。液体分流器50はドロンカップ型熱交換器10の多段のコアユニット11の上方に配置され、矩形流路の底面に多数の微細孔51を整然均一に加工し、その微細孔51より液体を滴下させる。微細孔51より滴下された液体は、ドロンカッププレートの外面流通路に沿って流通する。蒸発器やボイラーの場合、滴下される液体は冷媒液であり、吸収器の場合、滴下される液体は吸収液(冷媒と吸収剤の混合液)である。 The endmost core unit 11 is provided with an inlet 17 and an outlet 18 for the heat source medium. The liquid shunt 50 is arranged above the multi-stage core unit 11 of the drone cup type heat exchanger 10, and a large number of micropores 51 are neatly and uniformly processed on the bottom surface of the rectangular flow path, and the liquid is dropped from the micropores 51. Let me. The liquid dropped from the micropores 51 flows along the outer flow path of the Delon cup plate. In the case of an evaporator or a boiler, the liquid to be dropped is a refrigerant liquid, and in the case of an absorber, the liquid to be dropped is an absorbing liquid (a mixed liquid of a refrigerant and an absorbent).

特許文献1にはドロンカップ型熱交換器が記載されている。特許文献2には、熱交換器において液滴下チューブの小孔から液体を滴下することが記載されている。 Patent Document 1 describes a Delon cup type heat exchanger. Patent Document 2 describes that a liquid is dropped from a small hole in a tube under the droplet in a heat exchanger.

特開2010-270953号公報Japanese Unexamined Patent Publication No. 2010-27953 特開平6-101984号公報Japanese Unexamined Patent Publication No. 6-101984

しかしながら、多数の微細孔を加工することは、時間を要し、高価である。また、液体の流入方向の違いや孔の寸法差などによって、滴下量が必ずしも均一ではないという問題があった。 However, processing a large number of micropores is time consuming and expensive. Further, there is a problem that the dropping amount is not always uniform due to the difference in the inflow direction of the liquid and the difference in the size of the holes.

さらに、多段に積層されたドロンカッププレートは、個々のプレートの僅かな寸法差の集積で製品全体の積層寸法が変化しやすい。従って、滴下の孔位置と対応するドロンカッププレートの外面流通路にずれが生じやすいという問題があった。 Further, in the multi-stage laminated Delon cup plates, the laminated dimensions of the entire product are likely to change due to the accumulation of slight dimensional differences between the individual plates. Therefore, there is a problem that the outer surface flow passage of the Delon cup plate corresponding to the hole position of the dropping is likely to be displaced.

本発明の熱交換器用液体分流器は上述した課題に鑑みてなされたものであり、2枚の三角形状プレートの2辺同士を接合して両プレートで囲まれた扁平形状を成す液体流通路を形成し、両プレートの残りの底辺を開放端として前記液体流通路に連通するスリット状の液体流出口を形成し、一方のプレートの底辺に対向する三角形頂点付近に前記液体流通路に連通する液体流入口を形成したことを特徴とする。 The liquid diverting device for a heat exchanger of the present invention was made in view of the above-mentioned problems, and a liquid flow path forming a flat shape surrounded by both plates by joining two sides of two triangular plates. A liquid that forms a slit-shaped liquid outlet that communicates with the liquid flow path with the remaining bottoms of both plates as open ends, and communicates with the liquid flow path near the triangular apex facing the bottom of one plate. It is characterized by forming an inflow port.

本発明の熱交換器用液体分流器によれば、安価で製作しやすく、液体を均一に滴下することができる。また、本発明の熱交換器用液体分流器をドロンカップ型熱交換器に使用した場合、ドロンカッププレートの寸法差にかかわらず、ドロンカッププレートの外面流通路に液体を適切に滴下することができる。 According to the liquid shunt for heat exchanger of the present invention, it is inexpensive and easy to manufacture, and the liquid can be dropped uniformly. Further, when the liquid shunt for heat exchanger of the present invention is used for the Delon cup type heat exchanger, the liquid can be appropriately dropped into the outer flow passage of the Delon cup plate regardless of the dimensional difference of the Delon cup plate. ..

本発明の実施形態による熱交換器用液体分流器を備えたドロンカップ型熱交換器を示す概略斜視図である。It is a schematic perspective view which shows the Delon cup type heat exchanger provided with the liquid shunt for a heat exchanger according to the embodiment of this invention. ドロンカップ型熱交換器の断面図である。It is sectional drawing of the Delon cup type heat exchanger. 本発明の実施形態による熱交換器用液体分流器の正面図である。It is a front view of the liquid shunt for a heat exchanger according to the embodiment of this invention. 図3のX-X線における断面図である。FIG. 3 is a cross-sectional view taken along the line XX of FIG. 本発明の実施形態による熱交換器用液体分流器の液体流出口側から見た平面図である。It is a top view seen from the liquid outlet side of the liquid shunt for a heat exchanger according to the embodiment of this invention. 波板の斜視図である。It is a perspective view of a corrugated sheet. 従来の熱交換器用液体分流器を備えたドロンカップ型熱交換器を示す概略斜視図である。It is a schematic perspective view which shows the Delon cup type heat exchanger provided with the liquid shunt for a conventional heat exchanger.

本発明の実施形態による熱交換器用液体分流器及びそれを備えたドロンカップ型熱交換器を図1乃至図6に基づいて説明する。 A liquid shunt for a heat exchanger according to an embodiment of the present invention and a drone cup type heat exchanger provided with the same will be described with reference to FIGS. 1 to 6.

図1及び図2に示すように、ドロンカップ型熱交換器10は、上下を最中状に膨らませて形成し、中間部を細長扁平形状に形成してなる同形の、一対のドロンカッププレートからなるコアユニット11を多段に積層して構成される。 As shown in FIGS. 1 and 2, the drone cup type heat exchanger 10 is formed from a pair of drone cup plates having the same shape, which are formed by inflating the upper and lower parts in the middle and forming an elongated flat shape at the middle portion. The core unit 11 is configured by stacking the core units 11 in multiple stages.

1つのコアユニット11の上下の最中部12,13は隣接するコアユニット11の最中部12,13と接合される。上下の最中部12,13は、それぞれ連通孔14,15を介して連通されている。最端に位置するコアユニット11にはエンドプレート16が接合され、連通孔14,15に対応する位置に熱源媒体の流入口17及び流出口18が設けられている。 The upper and lower middle portions 12, 13 of one core unit 11 are joined to the middle portions 12, 13 of adjacent core units 11. The upper and lower middle portions 12 and 13 are communicated with each other through the communication holes 14 and 15, respectively. An end plate 16 is joined to the core unit 11 located at the outermost end, and an inlet 17 and an outlet 18 of the heat source medium are provided at positions corresponding to the communication holes 14 and 15.

流入口17からはドロンカップ型熱交換器10の用途に応じて、排気ガスや水等の熱源媒体が流入される。なお、図1において、供給液(冷媒液や吸収液)の流れを破線矢印で、熱源媒体(排気ガスや水等)の流れを実線矢印にて示してある。 A heat source medium such as exhaust gas or water flows in from the inflow port 17 depending on the application of the drone cup type heat exchanger 10. In FIG. 1, the flow of the supply liquid (refrigerant liquid, absorption liquid) is shown by a broken line arrow, and the flow of the heat source medium (exhaust gas, water, etc.) is shown by a solid line arrow.

液体分流器20はドロンカップ型熱交換器10の多段のコアユニット11の上方に配置され、多段に積層されたコアユニット11の外面流通路に向けて液体を滴下する。 The liquid shunt 20 is arranged above the multi-stage core unit 11 of the drone cup type heat exchanger 10, and drops liquid toward the outer surface flow passage of the multi-stage stacked core unit 11.

この液体分流器20の構成を図3乃至図6に基づいて説明する。プレス機で絞り加工された、同形の2枚の三角形状プレート21,22の2辺同士を溶接等により接合して両プレート21,22で囲まれた扁平形状を成す液体流通路23を設ける。 The configuration of the liquid shunt 20 will be described with reference to FIGS. 3 to 6. Two sides of two triangular plates 21 and 22 of the same shape, which have been drawn by a press, are joined to each other by welding or the like to provide a flat liquid flow passage 23 surrounded by both plates 21 and 22.

両プレート21,22の残りの底辺は開放端として液体流通路23に連通するスリット状の液体流出口24を設ける。一方のプレート21の底辺に対向する三角形頂点P付近に液体流通路23に連通する液体流入口25を設ける。液体流入口25からは供給液である液体(例えば、水)が流入される。液体流入口25には、両プレート21,22に対して略垂直となるように液体供給用の配管が接続される。 The remaining bottoms of both plates 21 and 22 are provided with a slit-shaped liquid outlet 24 communicating with the liquid flow passage 23 as an open end. A liquid inlet 25 communicating with the liquid flow passage 23 is provided near the triangular apex P facing the bottom of one plate 21. A liquid (for example, water), which is a supply liquid, flows in from the liquid inlet 25. A pipe for supplying liquid is connected to the liquid inlet 25 so as to be substantially perpendicular to both plates 21 and 22.

この液体分流器20によれば、液体流入口25から流入した液体は、プレート21に対向するプレート22の内壁面26に衝突し、放射状に分散する。液体が略垂直方向から衝突して放射状に均一に分散することで、スリット状の液体流出口24から流出する際にはおよそ均一な分布で、コアユニット11の外面に向けて滴下させることができる。また、液体分流器20はプレス板金加工部品で構成できるため、安価で製作しやすいものである。 According to the liquid shunt 20, the liquid flowing in from the liquid inlet 25 collides with the inner wall surface 26 of the plate 22 facing the plate 21 and is dispersed radially. When the liquid collides from a substantially vertical direction and is uniformly dispersed radially, the liquid can be dropped toward the outer surface of the core unit 11 with a substantially uniform distribution when flowing out from the slit-shaped liquid outlet 24. .. Further, since the liquid shunt 20 can be composed of pressed sheet metal processed parts, it is inexpensive and easy to manufacture.

なお、三角形状プレート21,22は厳密な意味で三角形である必要はなく、図1乃至図3に示すように、左右の頂点付近を切り欠いたものを含む。また、液体の流れを左右対称にするために、プレート21,22は二等辺三角形状を成すことが好ましい。 The triangular plates 21 and 22 do not have to be triangular in a strict sense, and include those cut out near the left and right vertices as shown in FIGS. 1 to 3. Further, in order to make the flow of the liquid symmetrical, it is preferable that the plates 21 and 22 have an isosceles triangle shape.

また、図5及び図6に示すように、液体流出口付近の両プレート21,22間に波板27を設置することで、より均一な滴下を実現すると同時に、超低流量域でも安定的に滴下させることが可能になる。波板27は平板を折り返して、山部と谷部が交互に繰り返すように形成される。波板27は山部→谷部→山部へと向かう方向が両プレート21,22の底辺と平行となるような向きに挿入される。 Further, as shown in FIGS. 5 and 6, by installing the corrugated plate 27 between the plates 21 and 22 near the liquid outlet, more uniform dropping is realized and at the same time, stable even in the ultra-low flow rate range. It becomes possible to drip. The corrugated sheet 27 is formed by folding back a flat plate so that peaks and valleys are alternately repeated. The corrugated sheet 27 is inserted so that the direction from the mountain portion to the valley portion to the mountain portion is parallel to the bottoms of both plates 21 and 22.

さらに、図4に示すように、両プレート21,22間の対向面の間隔は、液体流入口25の付近では広く、液体流出口24に向かって狭くすることにより、液体流入口25に流入した液体はその付近で一時的に滞留してから液体流出口24に向けて流通するようなり、液体をさらに均一に分散することができる。液体流出口24より滴下された液体は、ドロンカップ型熱交換器10のドロンカッププレートの外面流通路に沿って流通する。 Further, as shown in FIG. 4, the distance between the facing surfaces between the plates 21 and 22 is wide in the vicinity of the liquid inlet 25, and flows into the liquid inlet 25 by narrowing toward the liquid outlet 24. The liquid temporarily stays in the vicinity of the liquid and then flows toward the liquid outlet 24, so that the liquid can be more evenly dispersed. The liquid dropped from the liquid outlet 24 flows along the outer flow path of the Delon cup plate of the Delon cup type heat exchanger 10.

エジェクター冷凍サイクルの場合は、ドロンカップ型熱交換器10はボイラーや蒸発器として用いられ、流入口17からは熱源媒体(排気ガスや水)を流入する。流入口17からドロンカップ内に流入した熱源媒体は、ドロンカップ型熱交換器10の下側の流通路を連通孔14を介して流通し、細長扁平形状の中間部の流通路19を上昇しながら、液体分流器20から滴下された液体(冷媒)と熱交換を行うことにより滴下された液体(冷媒)を蒸発させ、上側の流通路を連通孔15を介して流通して流出口18から回路に戻っていく。図2において、液体(冷媒)の流れを破線矢印で、熱源媒体の流れを実線矢印にて示してある。 In the case of the ejector refrigeration cycle, the drone cup type heat exchanger 10 is used as a boiler or an evaporator, and a heat source medium (exhaust gas or water) flows in from the inflow port 17. The heat source medium that has flowed into the Delon cup from the inflow port 17 flows through the flow passage under the Delon cup type heat exchanger 10 through the communication hole 14, and rises in the flow passage 19 in the middle portion of the elongated flat shape. While exchanging heat with the liquid (refrigerator) dropped from the liquid diversion device 20, the dropped liquid (refrigerator) is evaporated and circulates through the upper flow passage through the communication hole 15 from the outlet 18. Go back to the circuit. In FIG. 2, the flow of the liquid (refrigerant) is indicated by a broken line arrow, and the flow of the heat source medium is indicated by a solid line arrow.

吸収式冷凍サイクルでは、同様な構成が蒸発器と吸収器に利用される。この場合は、液体と液体の熱交換となる。ドロンカップ型熱交換器10を蒸発器として使用する場合は、流入口17から水などの熱源媒体を流入し、液体分流器20から滴下された液体(冷媒)との熱交換により、液体(冷媒)を蒸発させ、冷媒蒸気を作る。一方、ドロンカップ型熱交換器10を吸収器として使用する場合は、流入口17から冷却水などの熱源媒体を流入し、液体分流器20から滴下された液体(吸収液)との熱交換を行うことにより、吸収液が周囲の冷媒蒸気を吸収する際に生じる吸収熱を回収する。 In the absorption refrigeration cycle, a similar configuration is utilized for the evaporator and absorber. In this case, the heat is exchanged between the liquid and the liquid. When the Delon cup type heat exchanger 10 is used as an evaporator, a heat source medium such as water flows in from the inflow port 17, and the liquid (refrigerant) is exchanged with the liquid (refrigerant) dropped from the liquid diversion device 20. ) Is evaporated to make refrigerant steam. On the other hand, when the Delon cup type heat exchanger 10 is used as an absorber, a heat source medium such as cooling water flows in from the inflow port 17 to exchange heat with the liquid (absorbent liquid) dropped from the liquid diversion device 20. By doing so, the absorption heat generated when the absorption liquid absorbs the surrounding refrigerant vapor is recovered.

10 ドロンカップ型熱交換器
11 コアユニット
12,13 最中部
14,15 連通孔
16 エンドプレート
17 流入口
18 流出口
20 液体分流器
21,22 三角形状プレート
23 液体流通路
24 液体流出口
25 液体流入口
26 内壁面
27 波板
10 Delon cup type heat exchanger 11 Core unit 12, 13 Central part 14, 15 Communication hole 16 End plate 17 Inlet 18 Outlet 20 Liquid shunt 21,22 Triangular plate 23 Liquid outlet 24 Liquid outlet 25 Liquid flow Entrance 26 Inner wall surface 27 Corrugated sheet

Claims (6)

2枚の三角形状プレートの2辺同士を接合して両プレートで囲まれた扁平形状を成す液体流通路を設け、両プレートの残りの底辺を開放端として前記液体流通路に連通するスリット状の液体流出口を設け、一方のプレートの底辺に対向する三角形頂点付近に前記液体流通路に連通する液体流入口を設けてなることを特徴とする熱交換器用液体分流器。 A slit-shaped liquid flow passage is provided in which two sides of two triangular plates are joined to form a flat shape surrounded by both plates, and the remaining bottoms of both plates are used as open ends to communicate with the liquid flow passage. A liquid diversion device for a heat exchanger, characterized in that a liquid outlet is provided and a liquid inlet communicating with the liquid flow path is provided in the vicinity of a triangular apex facing the bottom of one plate. 前記液体流出口付近の両プレート間に波板が挿入されたことを特徴とする請求項1に記載の熱交換器用液体分流器。 The liquid shunt for a heat exchanger according to claim 1, wherein a corrugated plate is inserted between both plates near the liquid outlet. 両プレート間の対向面の間隔は前記液体流入口付近では広く、前記液体流出口に向かって狭くなっていることを特徴とする請求項1または2に記載の熱交換器用液体分流器。 The liquid shunt for a heat exchanger according to claim 1 or 2, wherein the distance between the facing surfaces between the two plates is wide in the vicinity of the liquid inlet and narrows toward the liquid outlet. 上下を最中状に膨らませて形成し、中間部を細長扁平形状に形成してなる一対のドロンカッププレートを多段に積層して構成されるドロンカップ型熱交換器において、
多段に積層された一対のドロンカッププレートの外面に向けて液体を滴下する液体分流器を備え、
前記液体分流器は、2枚の三角形状プレートの2辺同士を接合して両プレートで囲まれた扁平形状を成す液体流通路を設け、両プレートの残りの底辺を開放端として前記液体流通路に連通するスリット状の液体流出口を設け、一方のプレートの底辺に対向する三角形頂点付近に前記液体流通路に連通する液体流入口を設けてなることを特徴とするドロンカップ型熱交換器。
In a drone cup type heat exchanger formed by stacking a pair of drone cup plates formed by inflating the upper and lower parts in the middle and forming an elongated flat shape in the middle part in multiple stages.
Equipped with a liquid shunt that drops liquid toward the outer surface of a pair of multi-tiered Delon cup plates.
The liquid flow exchanger is provided with a flat-shaped liquid flow passage in which two sides of two triangular plates are joined to each other to form a flat shape surrounded by both plates, and the liquid flow passage is provided with the remaining bottoms of both plates as open ends. A drone cup type heat exchanger characterized in that a slit-shaped liquid outlet communicating with the liquid outlet is provided, and a liquid inlet communicating with the liquid flow passage is provided near a triangular apex facing the bottom of one plate.
前記液体流出口付近の両プレート間に波板が挿入されたことを特徴とする請求項4に記載のドロンカップ型熱交換器。 The drone cup type heat exchanger according to claim 4, wherein a corrugated plate is inserted between both plates near the liquid outlet. 両プレート間の対向面の間隔は前記液体流入口付近では広く、前記液体流出口に向かって狭くなっていることを特徴とする請求項4または5に記載のドロンカップ型熱交換器。 The drone cup type heat exchanger according to claim 4 or 5, wherein the distance between the facing surfaces between the two plates is wide in the vicinity of the liquid inlet and narrows toward the liquid outlet.
JP2018076271A 2018-04-11 2018-04-11 Liquid shunt for heat exchanger and Delon cup type heat exchanger Active JP7026916B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2018076271A JP7026916B2 (en) 2018-04-11 2018-04-11 Liquid shunt for heat exchanger and Delon cup type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2018076271A JP7026916B2 (en) 2018-04-11 2018-04-11 Liquid shunt for heat exchanger and Delon cup type heat exchanger

Publications (2)

Publication Number Publication Date
JP2019184168A JP2019184168A (en) 2019-10-24
JP7026916B2 true JP7026916B2 (en) 2022-03-01

Family

ID=68340592

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2018076271A Active JP7026916B2 (en) 2018-04-11 2018-04-11 Liquid shunt for heat exchanger and Delon cup type heat exchanger

Country Status (1)

Country Link
JP (1) JP7026916B2 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3214000B2 (en) 1991-10-26 2001-10-02 ミノルタ株式会社 Temperature measuring device
JP2005345072A (en) 2004-06-07 2005-12-15 Denso Corp Heat exchanger
JP4947254B2 (en) 2004-08-05 2012-06-06 ブリヂストンスポーツ株式会社 Golf ball materials

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947254U (en) * 1972-07-26 1974-04-25
JP2738760B2 (en) * 1990-01-19 1998-04-08 松下冷機株式会社 Stacked heat exchanger
JP3376534B2 (en) * 1994-08-18 2003-02-10 株式会社日立製作所 Refrigerant distributor
JP3815921B2 (en) * 1999-06-30 2006-08-30 荏原冷熱システム株式会社 Liquid membrane plate heat exchanger and liquid distributor used therefor
JP2002081892A (en) * 2000-09-08 2002-03-22 Yazaki Corp Liquid distributor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3214000B2 (en) 1991-10-26 2001-10-02 ミノルタ株式会社 Temperature measuring device
JP2005345072A (en) 2004-06-07 2005-12-15 Denso Corp Heat exchanger
JP4947254B2 (en) 2004-08-05 2012-06-06 ブリヂストンスポーツ株式会社 Golf ball materials

Also Published As

Publication number Publication date
JP2019184168A (en) 2019-10-24

Similar Documents

Publication Publication Date Title
JP4047891B2 (en) Heat exchanger
WO2014147804A1 (en) Plate-type heat exchanger and refrigeration cycle device with same
US10113817B2 (en) Heater core
US10655894B2 (en) Refrigeration cycle of refrigerator
EP1808218B1 (en) Dryer for humid compressed gases
KR19990067881A (en) Liquid cooled, two phase heat exchanger
EP3059542B1 (en) Laminated header, heat exchanger, and air-conditioner
US11402162B2 (en) Distributor and heat exchanger
WO2018095153A1 (en) Heat exchanger and air conditioner
KR102151782B1 (en) Filter type print circuit heat exchanger, and radiator, heat recovery steam generator and outdoor unit of air conditioner comprising the same
WO2008071731A1 (en) An evaporator
JPWO2006077785A1 (en) Plate heat exchanger
KR20120044848A (en) Heat exchanger and micro-channel tube for the same
US20140374074A1 (en) Heat exchanger
JP6554182B2 (en) Heat exchanger having a plurality of stacked plates
WO2017135442A1 (en) Heat exchanger
JP7026916B2 (en) Liquid shunt for heat exchanger and Delon cup type heat exchanger
JP2013122368A (en) Vehicle heat exchanger
CN203533875U (en) Heat exchanger for hot water supply
EA037011B1 (en) Heat exchange unit for devices with a heat pump, in particular evaporator for manufacturing and storing ice
JP2008117035A (en) Vending machine
CN104748592A (en) Brazed heat exchanger with fluid flow and performing heat exchange by series connection with different refrigerant loops
KR20130023487A (en) Evaporator for heat pump including microchannel heat exchanger
JPH05215482A (en) Heat exchanger
CN208620665U (en) A kind of novel dividing wall type micro heat exchanger

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20210302

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20210331

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20210331

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20210407

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20210709

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20211223

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20220203

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20220207

R150 Certificate of patent or registration of utility model

Ref document number: 7026916

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150