Nothing Special   »   [go: up one dir, main page]

JP2016023815A - Evaporator - Google Patents

Evaporator Download PDF

Info

Publication number
JP2016023815A
JP2016023815A JP2014145945A JP2014145945A JP2016023815A JP 2016023815 A JP2016023815 A JP 2016023815A JP 2014145945 A JP2014145945 A JP 2014145945A JP 2014145945 A JP2014145945 A JP 2014145945A JP 2016023815 A JP2016023815 A JP 2016023815A
Authority
JP
Japan
Prior art keywords
tube
heat exchange
row
group
downflow
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
Application number
JP2014145945A
Other languages
Japanese (ja)
Inventor
基之 ▲高▼木
基之 ▲高▼木
Motoyuki Takagi
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.)
Mahle Behr Thermal Systems Japan Ltd
Original Assignee
Keihin Thermal Technology Corp
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 Keihin Thermal Technology Corp filed Critical Keihin Thermal Technology Corp
Priority to JP2014145945A priority Critical patent/JP2016023815A/en
Publication of JP2016023815A publication Critical patent/JP2016023815A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Air-Conditioning For Vehicles (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an evaporator capable of unifying the amount of refrigerant flowing in a plurality of refrigerant passages arranged side by side in a width direction of heat exchanging tubes.SOLUTION: An evaporator 1 comprises rows 13 of downstream tubes and rows 14 of upstream tubes composed of a plurality of flat heat exchanging tubes 12. The rows 13 of downstream tubes have a group 13A of descending flow tubes and the rows 14 of upstream tubes have a group 14A of ascending flow tubes. An upper header part 5 of downstream side is provided with an inlet side segment 5a in which refrigerant flows into the heat exchanging tubes 12 of the group 13A of descending flow tubes of the rows 13 of downstream tubes. A lower header part 11 of upstream side is provided with an inlet side segment 11b in which refrigerant flows into the heat exchanging tubes 12 of the group 14A of ascending flow tubes. End portions of the segments inserted into the inlet side segments 5a and 11b at the heat exchanging tubes 12 in the group 13A of descending flow tubes and the group 14A of ascending flow tubes are inclined downward to the upstream side.SELECTED DRAWING: Figure 2

Description

この発明は、たとえば自動車に搭載される冷凍サイクルであるカーエアコンに好適に用いられるエバポレータに関する。   The present invention relates to an evaporator suitably used for a car air conditioner that is a refrigeration cycle mounted on an automobile, for example.

この明細書および特許請求の範囲において、各図面の上下を上下というものとする。   In the present specification and claims, the upper and lower sides of each drawing are referred to as the upper and lower sides.

小型軽量化および高性能化を図りうるエバポレータとして、本出願人は、先に、長手方向を上下方向に向けるとともに幅方向を通風方向に向けた状態で互いに間隔をおいて配置された複数の扁平状熱交換チューブからなり、かつ通風方向に並んで配置された2つのチューブ列と、風下側チューブ列の熱交換チューブの長手方向両端側に長手方向をチューブの並び方向に向けて配置され、かつ風下側チューブ列のチューブの長手方向両端部が接続された第1ヘッダ部および第2ヘッダ部と、風上側チューブ列の熱交換チューブの長手方向両端側に長手方向をチューブの並び方向に向けて配置され、かつ風下側チューブ列のチューブの長手方向両端部が接続された第3ヘッダ部および第4ヘッダ部とを備えており、熱交換チューブが通風方向に並んだ複数の冷媒通路を有し、熱交換チューブの両端寄りの一定長さ部分がヘッダ部内に挿入されているエバポレータであって、第1ヘッダ部および第4ヘッダ部の全体に、熱交換チューブに冷媒が流入する入り側区画が設けられるとともに、第2ヘッダ部および第3ヘッダ部の全体に、熱交換チューブから冷媒が流出する出側区画が設けられており、熱交換チューブにおける入り側区画内に挿入された部分の端部が熱交換チューブの長手方向と直角をなす平面上に位置し、第1〜第4ヘッダ部内が仕切板によって上下2つの空間に分割され、第2ヘッダ部の下側空間と第4ヘッダ部の下側空間とが連通させられ、各ヘッダ部の仕切板に、上下2つの空間を通じさせる貫通穴が形成されているエバポレータを提案した(特許文献1参照)。   As an evaporator that can be reduced in size, weight, and performance, the present applicant has previously made a plurality of flats arranged at intervals from each other in a state where the longitudinal direction is directed in the vertical direction and the width direction is directed in the wind direction. Two tube rows that are formed of a cylindrical heat exchange tube and are arranged side by side in the ventilation direction, and are arranged with the longitudinal direction facing the tube arrangement direction on both ends in the longitudinal direction of the heat exchange tubes of the leeward side tube row, and The first header part and the second header part to which both ends in the longitudinal direction of the tubes of the leeward side tube row are connected, and the longitudinal direction toward the both ends in the longitudinal direction of the heat exchange tubes of the windward side tube row, are directed in the tube arrangement direction. And a third header part and a fourth header part connected to both longitudinal ends of the tubes of the leeward side tube row, and the heat exchange tubes are arranged in the ventilation direction. The evaporator has a plurality of refrigerant passages, and a fixed length portion near both ends of the heat exchange tube is inserted into the header portion, and the heat exchange tube is disposed on the entire first header portion and the fourth header portion. An inlet side section into which the refrigerant flows is provided, and an outlet side section from which the refrigerant flows out of the heat exchange tube is provided in the entire second header part and third header part, and the inside of the inlet side section in the heat exchange tube The end of the inserted portion is positioned on a plane perpendicular to the longitudinal direction of the heat exchange tube, and the first to fourth header portions are divided into two upper and lower spaces by a partition plate, and below the second header portion. An evaporator has been proposed in which the side space communicates with the lower space of the fourth header portion, and through holes are formed in the partition plate of each header portion so as to pass through the upper and lower spaces (see Patent Document 1).

特許文献1記載のエバポレータにおいては、各ヘッダ部内を上下に分割する仕切板および仕切板に形成された貫通穴の働きによって、第1チューブ列および第2チューブ列の全熱交換チューブへの分流が制御され、これにより熱交換性能の向上が図られている。   In the evaporator described in Patent Document 1, the flow of the first tube row and the second tube row to the total heat exchange tubes is divided by the action of the partition plate that divides the inside of each header portion up and down and the through holes formed in the partition plate. The heat exchange performance is thereby improved.

ところで、特許文献1記載のエバポレータにおいて、各熱交換チューブの風上側の冷媒通路においては、風下側の冷媒通路に比べて冷媒の蒸発が促進されるので通路抵抗が増大し、風上側の冷媒通路内に冷媒が流入しにくくなって、各熱交換チューブの風上側と風下側の温度にばらつきが発生する。したがって、エバポレータの風上側の温度分布と風下側の温度分布とに比較的大きな差が生じることになって、冷却性能にばらつきが発生し、さらなる熱交換性能の向上を図ることができない。   By the way, in the evaporator described in Patent Document 1, in the refrigerant passage on the windward side of each heat exchange tube, the evaporation of the refrigerant is promoted compared to the refrigerant passage on the leeward side, so that the passage resistance increases, and the refrigerant passage on the windward side It becomes difficult for the refrigerant to flow into the inside, and variations occur in the temperatures on the windward side and the leeward side of each heat exchange tube. Therefore, a relatively large difference occurs between the temperature distribution on the windward side and the temperature distribution on the leeward side of the evaporator, resulting in variations in cooling performance, and further improvement in heat exchange performance cannot be achieved.

特開2008−232456号公報JP 2008-232456 A

この発明の目的は、上記問題を解決し、各熱交換チューブの幅方向に並んだ複数の冷媒通路に流れる冷媒量を均一化しうるしうるエバポレータを提供することにある。   An object of the present invention is to provide an evaporator that can solve the above problems and can equalize the amount of refrigerant flowing in a plurality of refrigerant passages arranged in the width direction of each heat exchange tube.

本発明は、上記目的を達成するために以下の態様からなる。   In order to achieve the above object, the present invention comprises the following aspects.

1)長手方向を上下方向に向けるとともに幅方向を通風方向に向けた状態で互いに間隔をおいて配置された複数の扁平状熱交換チューブからなる少なくとも1つのチューブ列と、各チューブ列の熱交換チューブの長手方向両端側に長手方向をチューブの並び方向に向けて配置され、かつ当該チューブ列のチューブの長手方向両端部が接続された少なくとも2つのヘッダ部とを備えており、熱交換チューブが通風方向に並んだ複数の冷媒通路を有し、熱交換チューブの両端寄りの一定長さ部分がヘッダ部内に挿入され、少なくとも1つのヘッダ部に、熱交換チューブに冷媒が流入する入り側区画が設けられている熱交換器であって、
熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜しているエバポレータ。
1) Heat exchange between at least one tube row composed of a plurality of flat heat exchange tubes arranged at intervals from each other in a state where the longitudinal direction is directed vertically and the width direction is directed to the ventilation direction And at least two header portions arranged at both ends in the longitudinal direction of the tubes with the longitudinal direction facing the arrangement direction of the tubes and connected to both longitudinal ends of the tubes of the tube row, and the heat exchange tube It has a plurality of refrigerant passages arranged in the ventilation direction, a fixed length portion near both ends of the heat exchange tube is inserted into the header portion, and at least one header portion has an entry side section into which the refrigerant flows into the heat exchange tube A heat exchanger provided,
The evaporator in which the edge part of the part inserted in the entrance side division in a heat exchange tube inclines below toward the windward side.

2)長手方向を上下方向に向けて配置された複数の扁平状熱交換チューブからなる第1チューブ列および第2チューブ列が、第1チューブ列が風下側に位置するように通風方向に並んで設けられ、第1チューブ列の熱交換チューブの上下両端側に、第1チューブ列の全熱交換チューブが接続された第1ヘッダ部および第2ヘッダ部が設けられ、第2チューブ列の熱交換チューブの上下両端側に、第2チューブ列の全熱交換チューブが接続された第3ヘッダ部および第4ヘッダ部が設けられており、
第1チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群を有し、第2チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群を有し、第1チューブ列の下降流チューブ群が第2チューブ列の上昇流チューブ群の風下側に位置しており、
第1ヘッダ部に、第1チューブ列の下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第4ヘッダ部に、第2チューブ列の上昇流チューブ群の熱交換チューブの下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第1チューブ列の下降流チューブ群の熱交換チューブおよび第2チューブ列の上昇流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している上記1)記載のエバポレータ。
2) The first tube row and the second tube row made up of a plurality of flat heat exchange tubes arranged with the longitudinal direction facing the vertical direction are arranged in the ventilation direction so that the first tube row is located on the leeward side. A first header portion and a second header portion, to which the total heat exchange tubes of the first tube row are connected, are provided on both upper and lower ends of the heat exchange tubes of the first tube row, and heat exchange of the second tube row is performed. A third header portion and a fourth header portion, to which the total heat exchange tubes of the second tube row are connected, are provided on both upper and lower ends of the tube,
The first tube row is composed of a plurality of heat exchange tubes arranged continuously, and has a downflow tube group in which the refrigerant flows from top to bottom in the heat exchange tube, and the second tube row is arranged continuously. The upflow tube group is composed of a plurality of heat exchange tubes and the refrigerant flows from the bottom to the top in the heat exchange tubes, and the downflow tube group of the first tube row is the leeward side of the upflow tube group of the second tube row Located in the
The upper end portion of the heat exchange tube of the downflow tube group of the first tube row is connected to the first header portion, and an entry side section into which the refrigerant flows into the heat exchange tube of the downflow tube group is provided. The lower end part of the heat exchange tube of the upflow tube group of the second tube row is connected to the 4 header part, and an entrance side section into which the refrigerant flows into the heat exchange tube of the upflow tube group is provided. The ends of the portions inserted in the inlet side sections of the heat exchange tubes of the downflow tube group of the tube row and the heat exchange tubes of the upflow tube group of the second tube row are inclined downward toward the windward side. The evaporator according to 1) above.

3)第1チューブ列に、前記下降流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群とが交互に並んで設けられ、第2チューブ列に、前記上昇流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群とが交互に並んで設けられ、第1チューブ列の下降流チューブ群が第2チューブ列の上昇流チューブ群の風下側に位置するとともに、第1チューブ列の上昇流チューブ群が第2チューブ列の下降流チューブ群の風下側に位置しており、
第2ヘッダ部に、第1チューブ列の上昇流チューブ群の下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第3ヘッダ部に、第2チューブ列の下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第1チューブ列の上昇流チューブ群の熱交換チューブおよび第2チューブ列の下降流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している上記2)記載のエバポレータ。
3) In the first tube row, the downflow tube group and the upflow tube group consisting of a plurality of continuously arranged heat exchange tubes and in which the refrigerant flows from the bottom to the top in the heat exchange tube are alternately arranged. The upward flow tube groups and the downward flow tube groups in which the refrigerant flows from the top to the bottom in the heat exchange tubes are alternately arranged in the second tube row. The downflow tube group of the first tube row is located on the leeward side of the upflow tube group of the second tube row, and the upflow tube group of the first tube row is the downflow tube group of the second tube row. Located on the leeward side of
The second header portion is connected to the lower end portion of the upflow tube group of the first tube row, and is provided with an entry side section through which the refrigerant flows into the heat exchange tube of the upflow tube group. The upper end portion of the heat exchange tube of the downflow tube group of the second tube row is connected, and an entrance side section into which the refrigerant flows into the heat exchange tube of the downflow tube group is provided, and the first tube row rises. The end of the portion inserted into the inlet section of the heat exchange tube of the flow tube group and the heat exchange tube of the downflow tube group of the second tube row is inclined downward toward the windward side 2) The described evaporator.

4)長手方向を上下方向に向けて配置された複数の扁平状熱交換チューブからなる1つのチューブ列が設けられ、チューブ列の熱交換チューブの上下両端側に、チューブ列の全熱交換チューブが接続された第1ヘッダ部および第2ヘッダ部が設けられており、
チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群とを有しており、
第1ヘッダ部に、下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第2ヘッダ部に、上昇流チューブ群の熱交換チューブの下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、下降流チューブ群の熱交換チューブおよび上昇流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している上記1)記載のエバポレータ。
4) One tube row consisting of a plurality of flat heat exchange tubes arranged with the longitudinal direction facing the vertical direction is provided, and the total heat exchange tubes of the tube row are provided on both upper and lower ends of the heat exchange tubes of the tube row. A connected first header portion and a second header portion are provided;
The tube row is composed of a plurality of heat exchange tubes arranged continuously and the downflow tube group in which the refrigerant flows from the top to the bottom in the heat exchange tube, and the plurality of heat exchange tubes arranged in series and the refrigerant is And an upflow tube group that flows from the bottom to the top in the heat exchange tube,
The first header portion is connected to the upper end portion of the heat exchange tube of the downflow tube group, and is provided with an entry side section into which the refrigerant flows into the heat exchange tube of the downflow tube group, and the second header portion, The lower end portion of the heat exchange tube of the upflow tube group is connected, and an inlet side section into which the refrigerant flows into the heat exchange tube of the upflow tube group is provided, and the heat exchange tube and the upflow tube of the downflow tube group The evaporator according to 1) above, wherein an end of a portion inserted into the entrance side section of the heat exchange tube of the group is inclined downward toward the windward side.

上記1)〜4)のエバポレータによれば、熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜しているので、入り側区画から熱交換チューブの幅方向に並んだ複数の冷媒通路に流れる冷媒量を均一化することができる。すなわち、液相冷媒は、上側のヘッダ部の入り側区画の下部に貯まりやすいが、当該入り側区画内に冷媒が上から下に流れる熱交換チューブの上端寄りの一定長さ部分が挿入され、当該熱交換チューブの上端が風上側に向かって下方に傾斜していると、上側ヘッダ部の入り側区画の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路内に流入しやすくなり、下方に位置する風上側の冷媒通路内に流入する冷媒量が、上方に位置する風下側の冷媒通路に流入する冷媒量よりも多くなる。また、液相冷媒は、下側のヘッダ部の入り側区画の下部に貯まりやすいが、当該入り側区画内に冷媒が下から上に流れる熱交換チューブの下端寄りの一定長さ部分が挿入され、当該熱交換チューブの下端が風上側に向かって下方に傾斜していると、下側ヘッダ部の入り側区画の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路内に流入しやすくなり、下方に位置する風上側の冷媒通路内に流入する冷媒量が、上方に位置する風下側の冷媒通路に流入する冷媒量よりも多くなる。したがって、熱交換チューブの風上側の冷媒通路の通路抵抗が、風下側の冷媒通路に比べて増大したとしても、風上側の冷媒通路内に冷媒が流入しやすくなって各熱交換チューブの風上側冷媒通路と風下側冷媒通路を流れる冷媒量が均一化されることになり、各熱交換チューブの風上側と風下側の温度にばらつきが発生することが抑制される。その結果、エバポレータの風上側の温度分布と風下側の温度分布とに比較的大きな差が生じることが抑制されて冷却性能に大きなばらつきが発生することがなくなり、熱交換性能の向上を図ることが可能になる。   According to the evaporators 1) to 4) above, since the end of the portion inserted into the entry side compartment in the heat exchange tube is inclined downward toward the windward side, the heat exchange tube from the entry side compartment The amount of the refrigerant flowing through the plurality of refrigerant passages arranged in the width direction can be made uniform. That is, the liquid phase refrigerant is easily stored in the lower part of the entry side section of the upper header part, but a fixed length portion near the upper end of the heat exchange tube in which the refrigerant flows from the top to the bottom is inserted into the entry side section, If the upper end of the heat exchange tube is inclined downward toward the windward side, the liquid refrigerant stored in the lower part of the entry side section of the upper header portion flows into the refrigerant passage on the windward side located below. The amount of refrigerant flowing into the leeward refrigerant passage located below becomes larger than the amount of refrigerant flowing into the leeward refrigerant passage located above. Further, the liquid-phase refrigerant is easily stored in the lower portion of the entry side section of the lower header portion, but a fixed length portion near the lower end of the heat exchange tube in which the refrigerant flows from the bottom to the top is inserted in the entry side section. When the lower end of the heat exchange tube is inclined downward toward the windward side, the liquid-phase refrigerant stored in the lower part of the entry side section of the lower header portion is placed in the refrigerant path on the windward side located below. It becomes easy to flow in, and the amount of refrigerant flowing into the refrigerant passage on the leeward side located below is larger than the amount of refrigerant flowing into the refrigerant passage on the leeward side located above. Therefore, even if the passage resistance of the refrigerant passage on the windward side of the heat exchange tube is increased as compared with the refrigerant passage on the leeward side, the refrigerant easily flows into the refrigerant passage on the windward side, and the windward side of each heat exchange tube The amount of the refrigerant flowing through the refrigerant passage and the leeward refrigerant passage is made uniform, and the occurrence of variations in the temperatures on the windward side and the leeward side of each heat exchange tube is suppressed. As a result, it is possible to suppress a relatively large difference between the temperature distribution on the windward side and the temperature distribution on the leeward side of the evaporator, thereby preventing a large variation in the cooling performance and improving the heat exchange performance. It becomes possible.

この発明による実施形態1のエバポレータの全体構成を概略的に示す一部切り欠き斜視図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a partially cutaway perspective view schematically showing an overall configuration of an evaporator according to Embodiment 1 of the present invention. 図1のA−A線断面図である。It is the sectional view on the AA line of FIG. 図1のB−B線断面図である。It is the BB sectional view taken on the line of FIG. この発明による実施形態2のエバポレータの全体構成を概略的に示す一部切り欠き斜視図である。It is a partially notched perspective view which shows roughly the whole structure of the evaporator of Embodiment 2 by this invention. 図4のC−C線断面図である。It is CC sectional view taken on the line of FIG. 図4のD−D線断面図である。It is the DD sectional view taken on the line of FIG.

以下、この発明の実施形態を、図面を参照して説明する。   Embodiments of the present invention will be described below with reference to the drawings.

以下の説明において、隣接する熱交換管どうしの間の通風間隙を流れる空気の下流側(各図に矢印Xで示す方向)を前、これと反対側を後といい、後方から前方を見た際の左右(図1の左右)を左右というものとする。   In the following description, the downstream side of the air flowing in the ventilation gap between adjacent heat exchange tubes (the direction indicated by the arrow X in each figure) is referred to as the front, the opposite side is referred to as the rear, and the front is viewed from the rear. The left and right sides (left and right in FIG. 1) are called left and right.

さらに、以下の説明において、「アルミニウム」という用語には、純アルミニウムの他にアルミニウム合金を含むものとする。   Furthermore, in the following description, the term “aluminum” includes aluminum alloys in addition to pure aluminum.

なお、全図面を通じて同一物および同一部分には同一符号を付す。
実施形態1
この実施形態は図1〜図3に示すものである。
In addition, the same code | symbol is attached | subjected to the same thing and the same part through all drawings.
Embodiment 1
This embodiment is shown in FIGS.

図1はこの発明による実施形態1のエバポレータの全体構成を概略的に示し、図2および図3はその要部の構成を示す。   FIG. 1 schematically shows the overall configuration of an evaporator according to Embodiment 1 of the present invention, and FIGS. 2 and 3 show the configuration of the main part thereof.

図1において、エバポレータ(1)は、上下方向に間隔をおいて配置された左右方向にのびるアルミニウム製上ヘッダタンク(2)およびアルミニウム製下ヘッダタンク(3)と、両ヘッダタンク(2)(3)間に設けられた熱交換コア部(4)とを備えている。   In FIG. 1, the evaporator (1) includes an aluminum upper header tank (2) and an aluminum lower header tank (3) which are arranged in the vertical direction and spaced apart from each other, and both header tanks (2) ( And 3) a heat exchange core portion (4) provided between them.

上ヘッダタンク(2)は、前側(通風方向下流側)に位置する風下側上ヘッダ部(5)(第1ヘッダ部)と、後側(通風方向上流側)に位置しかつ風下側上ヘッダ部(5)に一体化された風上側上ヘッダ部(6)(第3ヘッダ部)とを備えている。風下側上ヘッダ部(5)の右端部に冷媒入口(7)が設けられ、風上側上ヘッダ部(6)の右端部に冷媒出口(8)が設けられている。下ヘッダタンク(3)は、前側に位置する風下側下ヘッダ部(9)(第2ヘッダ部)と、後側に位置しかつ風下側下ヘッダ部(9)に一体化された風上側下ヘッダ部(11)(第4ヘッダ部)とを備えている。   The upper header tank (2) has a leeward upper header part (5) (first header part) located on the front side (downstream side in the ventilation direction) and a leeward side upper header located on the rear side (upstream side in the ventilation direction). A windward upper header portion (6) (third header portion) integrated with the portion (5). A refrigerant inlet (7) is provided at the right end of the leeward upper header (5), and a refrigerant outlet (8) is provided at the right end of the leeward upper header (6). The lower header tank (3) has a leeward lower header section (9) (second header section) located on the front side, and an upwind lower section located on the rear side and integrated with the leeward lower header section (9). A header portion (11) (fourth header portion).

図1〜図3に示すように、上ヘッダタンク(2)の風下側上ヘッダ部(5)内は、アルミニウム製風下側仕切板(17)によって、冷媒入口(7)に通じる右側区画(5a)と、左側区画(5b)とに分割されている。風上側上ヘッダ部(6)内は、風下側仕切板(17)と同一位置に設けられた風上側仕切板(18)によって、左側区画(6a)と、冷媒出口(8)に通じる右側区画(6b)とに分割されている。風下側上ヘッダ部(5)の左側区画(5b)と、風上側上ヘッダ部(6)の左側区画(6a)とは、上ヘッダタンク(2)における両上ヘッダ部(5)(6)間に設けられた左右方向に長い仕切部(2a)に形成された連通穴(19)を介して通じている。なお、風下側下ヘッダ部(9)内および風上側下ヘッダ部(11)内は仕切板によっては分割されていないが、風下側下ヘッダ部(9)内の右側部分を右側区画(9a)とするとともに、同左側部分を左側区画(9b)とし、風上側下ヘッダ部(11)内の左側部分を左側区画(11a)とするとともに、同右側部分を右側区画(11b)とする。   As shown in FIGS. 1 to 3, the leeward upper header portion (5) of the upper header tank (2) has a right compartment (5a) connected to the refrigerant inlet (7) by an aluminum leeward partition plate (17). ) And the left section (5b). Inside the windward upper header section (6), the windward partition plate (18) provided at the same position as the windward partition plate (17), the left partition (6a) and the right partition that leads to the refrigerant outlet (8) It is divided into (6b). The left section (5b) of the leeward upper header section (5) and the left section (6a) of the leeward upper header section (6) are both upper header sections (5) (6) in the upper header tank (2). It communicates via a communication hole (19) formed in a partition (2a) that is provided in the left and right direction and that is long in the left-right direction. The leeward lower header part (9) and the leeward lower header part (11) are not divided by the partition plate, but the right part in the leeward lower header part (9) is the right compartment (9a). And the left part in the upwind lower header (11) is the left part (11a), and the right part is the right part (11b).

熱交換コア部(4)は、長手方向を上下方向に向けるとともに幅方向を通風方向に向けた状態で左右方向に間隔をおいて配置された複数のアルミニウム押出形材製扁平状熱交換チューブ(12)からなるチューブ列(13)(14)が、前後方向に並んで2列設けられ、各チューブ列(13)(14)の隣接する熱交換チューブ(12)どうしの間の通風間隙および左右両端の熱交換チューブ(12)の外側に、それぞれ前後両チューブ列(13)(14)の熱交換チューブ(12)に跨るようにアルミニウム製コルゲートフィン(15)が配置されて熱交換チューブ(12)にろう付され、左右両端のコルゲートフィン(15)の外側にそれぞれアルミニウム製サイドプレート(16)が配置されてコルゲートフィン(15)にろう付されることにより構成されている。熱交換チューブ(12)が通風方向に並んだ複数の冷媒通路(12a)を有している。   The heat exchange core part (4) is a flat heat exchange tube made of a plurality of aluminum extruded sections arranged at intervals in the left-right direction with the longitudinal direction oriented in the vertical direction and the width direction directed in the ventilation direction ( Two tube rows (13) and (14) consisting of 12) are arranged in the front-rear direction, and the ventilation gap between the adjacent heat exchange tubes (12) of each tube row (13) and (14) and the left and right Aluminum corrugated fins (15) are arranged outside the heat exchange tubes (12) at both ends so as to straddle the heat exchange tubes (12) of both the front and rear tube rows (13) and (14). ), And aluminum side plates (16) are disposed on the outer sides of the corrugated fins (15) at both the left and right ends, respectively, and brazed to the corrugated fins (15). The heat exchange tube (12) has a plurality of refrigerant passages (12a) arranged in the ventilation direction.

風下側チューブ列(13)(第1チューブ列)の熱交換チューブ(12)の上下両端部は、風下側上下両ヘッダ部(5)(9)内に突出するように挿入された状態で両ヘッダ部(5)(9)に連通状に接続され、風上側チューブ列(14)(第2チューブ列)の熱交換チューブ(12)の上下両端部は、風上側上下両ヘッダ部(6)(11)内に突出するように挿入された状態で両ヘッダ部(6)(11)に連通状に接続されている。なお、風下側チューブ列(13)の熱交換チューブ(12)の数と風上側チューブ列(14)の熱交換チューブ(12)の数とは等しくなっている。コルゲートフィン(15)は、風下側チューブ列(13)および風上側チューブ列(14)を構成する前後の熱交換チューブ(12)に共有されている。   The upper and lower ends of the heat exchange tubes (12) of the leeward tube row (13) (first tube row) are both inserted so as to protrude into the leeward upper and lower header portions (5) and (9). The upper and lower ends of the heat exchange tubes (12) of the upwind tube row (14) (second tube row) are connected to the header sections (5) and (9) in a continuous manner. (11) It is connected to both header parts (6) and (11) in a state of being inserted so as to protrude into (11). The number of heat exchange tubes (12) in the leeward tube row (13) is equal to the number of heat exchange tubes (12) in the windward tube row (14). The corrugated fin (15) is shared by the heat exchange tubes (12) before and after the leeward tube row (13) and the windward tube row (14).

風下側チューブ列(13)に、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を上から下に流れる1つの下降流チューブ群(13A)と、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を下から上に流れる上昇流チューブ群(13B)とが左右方向に並んで設けられている。風上側チューブ列(14)に、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を下から上に流れる上昇流チューブ群(14A)と、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を上から下に流れる下降流チューブ群(14B)とが交互に並んで設けられている。風下側チューブ列(13)の下降流チューブ群(13A)が風上側チューブ列(14)の上昇流チューブ群(14A)の風下側に位置するとともに、風下側チューブ列(13)の上昇流チューブ群(13B)が風上側チューブ列(14)の下降流チューブ群(14B)の風下側に位置している。   One downflow tube group (13A) consisting of a plurality of heat exchange tubes (12) arranged in a row on the leeward side tube row (13) and in which the refrigerant flows from top to bottom in the heat exchange tubes (12). And a plurality of heat exchange tubes (12) arranged side by side, and an upflow tube group (13B) in which the refrigerant flows from the bottom to the top in the heat exchange tubes (12) are provided side by side in the left-right direction. . Consecutive with an upflow tube group (14A) consisting of a plurality of heat exchange tubes (12) arranged continuously in the windward tube row (14) and in which the refrigerant flows from the bottom to the top in the heat exchange tubes (12). A plurality of downflow tube groups (14B), which are composed of a plurality of heat exchange tubes (12) arranged in parallel and from which the refrigerant flows from top to bottom in the heat exchange tubes (12), are provided alternately. The downflow tube group (13A) of the leeward tube row (13) is located on the leeward side of the upflow tube group (14A) of the upwind tube row (14), and the upflow tube of the leeward tube row (13). The group (13B) is located on the leeward side of the downflow tube group (14B) in the windward tube row (14).

風下側チューブ列(13)の下降流チューブ群(13A)の熱交換チューブ(12)の上端部は風下側上ヘッダ部(5)の右側区画(5a)内に通じ、下端部は風下側下ヘッダ部(9)の右側区画(9a)に通じている。また、風下側チューブ列(13)の上昇流チューブ群(13B)の熱交換チューブ(12)の上端部は風下側上ヘッダ部(5)の左側区画(5b)内に通じ、下端部は風下側下ヘッダ部(9)の左側区画(9b)に通じている。風上側チューブ列(14)の上昇流チューブ群(14A)の熱交換チューブ(12)の上端部は風上側上ヘッダ部(6)の右側区画(6b)内に通じ、下端部は風上側下ヘッダ部(11)の右側区画(11b)に通じている。また、風上側チューブ列(14)の下降流チューブ群(14B)の熱交換チューブ(12)の上端部は風上側上ヘッダ部(6)の左側区画(6a)内に通じ、下端部は風上側下ヘッダ部(11)の左側区画(11a)に通じている。   The upper end of the heat exchange tube (12) of the downflow tube group (13A) in the leeward tube row (13) leads to the right compartment (5a) of the leeward upper header (5), and the lower end is on the leeward lower side. It leads to the right section (9a) of the header section (9). The upper end of the heat exchange tube (12) of the upflow tube group (13B) in the leeward tube row (13) communicates with the left compartment (5b) of the leeward upper header (5), and the lower end is leeward. It leads to the left section (9b) of the lower header section (9). The upper end of the heat exchange tube (12) of the upflow tube group (14A) in the upwind tube row (14) communicates with the right compartment (6b) of the upwind header (6), and the lower end of the upwind tube group (14A) It leads to the right section (11b) of the header section (11). In addition, the upper end of the heat exchange tube (12) of the downflow tube group (14B) of the upwind tube row (14) communicates with the left compartment (6a) of the upwind upper header (6), and the lower end of the heat exchange tube (12). It leads to the left section (11a) of the upper lower header section (11).

ここで、風下側上ヘッダ部(5)の右側区画(5a)、風下側下ヘッダ部(9)の左側区画(9b)、風上側上ヘッダ部(6)の左側区画(6a)および風上側下ヘッダ部(11)の右側区画(11b)が、熱交換チューブ(12)に冷媒が流入する入り側区画となっており、熱交換チューブ(12)における入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している。すなわち、風下側チューブ列(13)の下降流チューブ群(13A)の熱交換チューブ(12)の上端部、および上昇流チューブ群(13B)の熱交換チューブ(12)の下端部、ならびに風上側チューブ列(14)の上昇流チューブ群(14A)の熱交換チューブ(12)の下端部、および風上側チューブ列(14)の下降流チューブ群(14B)の上端部が、それぞれ風上側に向かって下方に傾斜している。なお、この実施形態においては、風下側チューブ列(13)の下降流チューブ群(13A)の熱交換チューブ(12)の下端部、および上昇流チューブ群(13B)の熱交換チューブ(12)の上端部、ならびに風上側チューブ列(14)の上昇流チューブ群(14A)の熱交換チューブ(12)の上端部、および風上側チューブ列(14)の下降流チューブ群(14B)の下端部も、それぞれ風上側に向かって下方に傾斜しているが、これはすべての熱交換チューブ(12)の形状を同一にし、部品の種類を減らすためである。   Here, the right section (5a) of the leeward upper header section (5), the left section (9b) of the leeward lower header section (9), the left section (6a) of the leeward upper header section (6), and the windward side The right section (11b) of the lower header section (11) is an entry section into which the refrigerant flows into the heat exchange tube (12), and the portion inserted into the entry section of the heat exchange tube (12). The end portion is inclined downward toward the windward side. That is, the upper end of the heat exchange tube (12) of the downflow tube group (13A) of the leeward side tube row (13), the lower end of the heat exchange tube (12) of the upflow tube group (13B), and the upwind side The lower end of the heat exchange tube (12) of the upflow tube group (14A) of the tube row (14) and the upper end of the downflow tube group (14B) of the upwind tube row (14) face the upwind side, respectively. And tilted downward. In this embodiment, the lower end of the heat exchange tube (12) of the downflow tube group (13A) of the leeward side tube row (13) and the heat exchange tube (12) of the upflow tube group (13B). The upper end and the upper end of the heat exchange tube (12) of the upflow tube group (14A) of the upwind tube row (14) and the lower end of the downflow tube group (14B) of the upwind tube row (14) are also provided. These are inclined downward toward the windward side in order to make all the heat exchange tubes (12) have the same shape and reduce the types of parts.

上述したエバポレータ(1)において、圧縮機、コンデンサおよび膨張弁を通過した冷媒が、冷媒入口(7)から風下側上ヘッダ部(5)の右側区画(5a)内に入り、右側区画(5a)から風下側チューブ列(13)の下降流チューブ群(13A)の熱交換チューブ(12)内に流入する。下降流チューブ群(13A)の熱交換チューブ(12)内に流入した冷媒は、当該熱交換チューブ(12)内を下方に流れて風下側下ヘッダ部(9)の右側区画(9a)内に入った後左側区画(9a)内に入り、左側区画(9a)から風下側チューブ列(13)の上昇流チューブ群(13B)の熱交換チューブ(12)内に流入する。上昇流チューブ群(13B)の熱交換チューブ(12)内に流入した冷媒は、当該熱交換チューブ(12)内を上方に流れて風下側上ヘッダ部(5)の左側区画(5b)内に入り、連通穴(19)を通って風上側上ヘッダ部(9)の左側区画(6a)内に入り、左側区画(6a)から風上側チューブ列(14)の下降流チューブ群(14B)の熱交換チューブ(12)内に流入する。下降流チューブ群(14B)の熱交換チューブ(12)内に流入した冷媒は、当該熱交換チューブ(12)内を下方に流れて風上側下ヘッダ部(11)の左側区画(11a)内に入った後右側区画(11b)内に入る。風上側下ヘッダ部(11)の右側区画(11b)内に入った冷媒は、風上側チューブ列(14)の上昇流チューブ群(14A)の熱交換チューブ(12)内に流入し、当該熱交換チューブ(12)内を上方に流れて風上側上ヘッダ部(6)の右側区画(6b)内に入り、冷媒出口(8)から流出する。   In the evaporator (1) described above, the refrigerant that has passed through the compressor, the condenser, and the expansion valve enters the right compartment (5a) of the leeward upper header portion (5) from the refrigerant inlet (7), and the right compartment (5a). The air flows into the heat exchange tubes (12) of the downflow tube group (13A) in the leeward tube row (13). The refrigerant that has flowed into the heat exchange tube (12) of the downflow tube group (13A) flows downward in the heat exchange tube (12) and into the right compartment (9a) of the leeward lower header section (9). After entering, it enters the left compartment (9a) and flows from the left compartment (9a) into the heat exchange tube (12) of the upflow tube group (13B) of the leeward tube row (13). The refrigerant flowing into the heat exchange tube (12) of the upflow tube group (13B) flows upward in the heat exchange tube (12) and enters the left compartment (5b) of the leeward upper header section (5). Into the left compartment (6a) of the windward upstream header section (9) through the communication hole (19), and from the left compartment (6a) to the downflow tube group (14B) of the windward tube row (14). It flows into the heat exchange tube (12). The refrigerant flowing into the heat exchange tube (12) of the downflow tube group (14B) flows downward in the heat exchange tube (12) and enters the left compartment (11a) of the windward lower header portion (11). After entering, enter the right compartment (11b). The refrigerant that has entered the right side section (11b) of the upwind header section (11) flows into the heat exchange tube (12) of the upflow tube group (14A) of the upwind tube row (14), and the heat It flows upward in the exchange tube (12), enters the right compartment (6b) of the upwind header section (6), and flows out from the refrigerant outlet (8).

液相冷媒は、上側に位置するヘッダ部の入り側区画である風下側上ヘッダ部(5)の右側区画(5a)および風上側上ヘッダ部(6)の左側区画(6a)の下部に貯まりやすいが、冷媒が上から下に流れる下降流チューブ群(13A)(14B)の熱交換チューブ(12)の上端寄りの一定長さ部分が右側区画(5a)内および左側区画(6a)挿入され、当該熱交換チューブ(12)の上端が風上側に向かって下方に傾斜しているので、風下側上ヘッダ部(5)の右側区画(5a)および風上側上ヘッダ部(6)の左側区画(6a)の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路(12a)内に流入しやすくなり、下方に位置する風上側の冷媒通路(12a)内に流入する冷媒量が、上方に位置する風下側の冷媒通路(12a)に流入する冷媒量よりも多くなる。   Liquid refrigerant is stored in the lower section of the right section (5a) of the leeward upper header section (5) and the left section (6a) of the leeward upper header section (6), which are the inlet section of the header section located on the upper side. Although it is easy, the fixed length part near the upper end of the heat exchange tube (12) of the downflow tube group (13A) (14B) in which the refrigerant flows from top to bottom is inserted into the right compartment (5a) and the left compartment (6a). Since the upper end of the heat exchange tube (12) is inclined downward toward the windward side, the right partition (5a) of the leeward upper header part (5) and the left partition of the windward upper header part (6) (6a) The liquid refrigerant stored in the lower part of the refrigerant becomes easy to flow into the windward refrigerant passage (12a) located below, and the amount of refrigerant flowing into the windward refrigerant passage (12a) located below However, it becomes larger than the amount of refrigerant flowing into the leeward refrigerant passage (12a) located above.

また、液相冷媒は、下側に位置するヘッダ部の入り側区画である風下側下ヘッダ部(9)の左側区画(9b)および風上側下ヘッダ部(11)の右側区画(11b)の下部に貯まりやすいが、冷媒が下から上に流れる上昇流チューブ群(13B)(14A)の熱交換チューブ(12)の下端寄りの一定長さ部分が左側区画(9b)内および右側区画(11b)内に挿入され、当該熱交換チューブ(12)の下端が風上側に向かって下方に傾斜しているので、風下側下ヘッダ部(9)の左側区画(9b)および風上側下ヘッダ部(11)の右側区画(11b)の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路(12a)内に流入しやすくなり、下方に位置する風上側の冷媒通路(12a)内に流入する冷媒量が、上方に位置する風下側の冷媒通路(12a)に流入する冷媒量よりも多くなる。   Further, the liquid-phase refrigerant is supplied to the left side section (9b) of the leeward side lower header part (9) and the right side section (11b) of the leeward side lower header part (11), which is an entrance side section of the header part located on the lower side. Although it is easy to accumulate in the lower part, the fixed length part near the lower end of the heat exchange tube (12) of the upflow tube group (13B) (14A) where the refrigerant flows from the bottom to the top is in the left compartment (9b) and the right compartment (11b) ) And the lower end of the heat exchange tube (12) is inclined downward toward the windward side, so the left side section (9b) of the leeward lower header part (9) and the windward lower header part ( 11) The liquid-phase refrigerant stored in the lower portion of the right compartment (11b) easily flows into the windward refrigerant passage (12a) located below, and enters the refrigerant passage (12a) located on the windward side below. The amount of refrigerant flowing into the refrigerant becomes larger than the amount of refrigerant flowing into the leeward refrigerant passage (12a) located above.

したがって、各熱交換チューブ(12)の風上側冷媒通路(12a)において、風下側冷媒通路(12a)に比べて冷媒の蒸発が促進されて通路抵抗が増大した場合であっても、風上側の冷媒通路(12a)内に冷媒が流入しやすくなって各熱交換チューブ(12)の風上側冷媒通路(12a)と風下側冷媒通路(12a)を流れる冷媒量が均一化される。その結果、各熱交換チューブ(12)の風上側と風下側の温度にばらつきが発生することが抑制され、エバポレータ(1)の風上側の温度分布と風下側の温度分布とに比較的大きな差が生じることが抑制されて冷却性能に大きなばらつきが発生することがなくなり、熱交換性能の向上を図ることが可能になる。   Therefore, in the windward side refrigerant passage (12a) of each heat exchange tube (12), even when the evaporation of the refrigerant is promoted and the passage resistance is increased as compared with the leeward side refrigerant passage (12a), The refrigerant easily flows into the refrigerant passage (12a), and the amount of refrigerant flowing through the windward refrigerant passage (12a) and the leeward refrigerant passage (12a) of each heat exchange tube (12) is made uniform. As a result, the occurrence of variations in the temperature on the leeward and leeward sides of each heat exchange tube (12) is suppressed, and a relatively large difference between the temperature distribution on the leeward side and the temperature distribution on the leeward side of the evaporator (1). It is possible to improve the heat exchange performance without the occurrence of a large variation in the cooling performance.

上述した実施形態1のエバポレータ(1)において、風下側チューブ列(13)の下降流チューブ群(13A)の熱交換チューブ(12)の下端部、および上昇流チューブ群(13B)の熱交換チューブ(12)の上端部、ならびに風上側チューブ列(14)の上昇流チューブ群(14A)の熱交換チューブ(12)の上端部、および風上側チューブ列(14)の下降流チューブ群(14B)の下端部は、それぞれ風上側に向かって下方に傾斜している必要はなく、水平状であってもよい。
実施形態2
この実施形態は図4〜図6に示すものである。
In the evaporator (1) of Embodiment 1 described above, the lower end of the heat exchange tube (12) of the downflow tube group (13A) of the leeward side tube row (13) and the heat exchange tube of the upflow tube group (13B) The upper end of (12), the upper end of the heat exchange tube (12) of the upflow tube group (14A) of the windward tube row (14), and the downflow tube group (14B) of the windward tube row (14) Each of the lower end portions of each of them may not be inclined downward toward the windward side, and may be horizontal.
Embodiment 2
This embodiment is shown in FIGS.

図4はこの発明による実施形態2のエバポレータの全体構成を概略的に示し、図5および図6はその要部の構成を示す。   FIG. 4 schematically shows the entire configuration of the evaporator according to the second embodiment of the present invention, and FIGS. 5 and 6 show the configuration of the main part thereof.

図4〜図6において、エバポレータ(20)は、上下方向に間隔をおいて配置された左右方向にのびるアルミニウム製上ヘッダ部(21)(第1ヘッダ部)およびアルミニウム製下ヘッダ部(22)(第2ヘッダ部)と、両ヘッダ部(21)(22)間に設けられた熱交換コア部(23)とを備えている。   4 to 6, the evaporator (20) includes an aluminum upper header portion (21) (first header portion) and an aluminum lower header portion (22) extending in the left-right direction and spaced apart in the vertical direction. (Second header portion) and a heat exchange core portion (23) provided between the header portions (21) and (22).

上ヘッダ部(21)の右端部に冷媒入口(24)が設けられ、同左端部に冷媒出口(25)が設けられている。上ヘッダ部(21)内は、アルミニウム製仕切板(26)によって、冷媒入口(24)に通じる右側区画(21a)と、冷媒出口(25)に通じる左側区画(21b)とに分割されている。なお、下ヘッダ部(9)内は仕切板によっては分割されていないが、下ヘッダ部(22)内の右側部分を右側区画(22a)とするとともに、同左側部分を左側区画(22b)とする。   A refrigerant inlet (24) is provided at the right end of the upper header (21), and a refrigerant outlet (25) is provided at the left end. The upper header portion (21) is divided into a right compartment (21a) leading to the refrigerant inlet (24) and a left compartment (21b) leading to the refrigerant outlet (25) by an aluminum partition plate (26). . Although the lower header portion (9) is not divided by a partition plate, the right side portion in the lower header portion (22) is a right side partition (22a) and the left side portion is a left side partition (22b). To do.

熱交換コア部(23)は、長手方向を上下方向に向けるとともに幅方向を通風方向に向けた状態で左右方向に間隔をおいて配置された複数のアルミニウム押出形材製扁平状熱交換チューブ(12)からなる1つのチューブ列(27)が設けられ、チューブ列(27)の隣接する熱交換チューブ(12)どうしの間の通風間隙および左右両端の熱交換チューブ(12)の外側に、それぞれアルミニウム製コルゲートフィン(15)が配置されて熱交換チューブ(12)にろう付され、左右両端のコルゲートフィン(15)の外側にそれぞれアルミニウム製サイドプレート(16)が配置されてコルゲートフィン(15)にろう付されることにより構成されている。熱交換チューブ(12)が通風方向に並んだ複数の冷媒通路(12a)を有している。   The heat exchange core part (23) is a flat heat exchange tube made of a plurality of extruded aluminum shapes (a plurality of aluminum extruded shape members arranged at intervals in the left-right direction with the longitudinal direction oriented in the vertical direction and the width direction directed in the ventilation direction ( 12) is provided with one tube row (27), and a ventilation gap between adjacent heat exchange tubes (12) in the tube row (27) and outside the heat exchange tubes (12) at both left and right ends, respectively. Aluminum corrugated fins (15) are arranged and brazed to the heat exchange tubes (12), and aluminum side plates (16) are arranged outside the corrugated fins (15) at the left and right ends, respectively. It is comprised by brazing to. The heat exchange tube (12) has a plurality of refrigerant passages (12a) arranged in the ventilation direction.

チューブ列(27)の熱交換チューブ(12)の上下両端部は、上下両ヘッダ部(21)(22)内に突出するように挿入された状態で両ヘッダ部(21)(22)に連通状に接続されている。   The upper and lower ends of the heat exchange tube (12) in the tube row (27) communicate with both header sections (21) and (22) in a state of being inserted so as to protrude into the upper and lower header sections (21) and (22). Connected.

チューブ列(27)に、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を上から下に流れる1つの下降流チューブ群(27A)と、連続して並んだ複数の熱交換チューブ(12)からなりかつ冷媒が熱交換チューブ(12)内を下から上に流れる上昇流チューブ群(27B)とが左右方向に並んで設けられている。   The tube row (27) is composed of a plurality of heat exchange tubes (12) arranged in succession, and one downflow tube group (27A) in which the refrigerant flows from the top to the bottom in the heat exchange tube (12). And an upflow tube group (27B) which is composed of a plurality of heat exchange tubes (12) arranged side by side and in which the refrigerant flows from the bottom to the top in the heat exchange tube (12).

チューブ列(27)の下降流チューブ群(27A)の上端部は上ヘッダ部(21)の右側区画(21a)内に通じ、下端部は下ヘッダ部(22)の右側区画(22a)に通じている。また、チューブ列(27)の上昇流チューブ群(27B)の上端部は上ヘッダ部(21)の左側区画(21b)内に通じ、下端部は下ヘッダ部(22)の左側区画(22b)に通じている。   The upper end of the downflow tube group (27A) of the tube row (27) communicates with the right compartment (21a) of the upper header section (21), and the lower end communicates with the right section (22a) of the lower header section (22). ing. Further, the upper end portion of the upward flow tube group (27B) of the tube row (27) communicates with the left compartment (21b) of the upper header portion (21), and the lower end portion is the left compartment (22b) of the lower header portion (22). Leads to.

ここで、上ヘッダ部(21)の右側区画(21a)および下ヘッダ部(22)の左側区画(22b)が、熱交換チューブ(12)に冷媒が流入する入り側区画となっており、熱交換チューブ(12)における入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している。すなわち、チューブ列(27)の下降流チューブ群(27A)の熱交換チューブ(12)の上端部、および上昇流チューブ群(27B)の熱交換チューブ(12)の下端部が、それぞれ風上側に向かって下方に傾斜している。なお、この実施形態においては、チューブ列(27)の下降流チューブ群(27A)の熱交換チューブ(12)の下端部および上昇流チューブ群(27B)の熱交換チューブ(12)の上端部も、それぞれ風上側に向かって下方に傾斜しているが、これはすべての熱交換チューブ(12)の形状を同一にし、部品の種類を減らすためである。   Here, the right section (21a) of the upper header section (21) and the left section (22b) of the lower header section (22) are entry sections into which the refrigerant flows into the heat exchange tube (12). The end of the portion of the exchange tube (12) inserted into the entry compartment is inclined downward toward the windward side. That is, the upper end of the heat exchange tube (12) of the downflow tube group (27A) of the tube row (27) and the lower end of the heat exchange tube (12) of the upflow tube group (27B) are respectively on the windward side. It is inclined downward. In this embodiment, the lower end of the heat exchange tube (12) of the downflow tube group (27A) of the tube row (27) and the upper end of the heat exchange tube (12) of the upflow tube group (27B) are also provided. These are inclined downward toward the windward side in order to make all the heat exchange tubes (12) have the same shape and reduce the types of parts.

上述したエバポレータ(20)において、圧縮機、コンデンサおよび膨張弁を通過した冷媒が、冷媒入口(24)から上ヘッダ部(21)の右側区画(21a)内に入り、右側区画(21a)からチューブ列(27)の下降流チューブ群(27A)の熱交換チューブ(12)内に流入する。下降流チューブ群(27A)の熱交換チューブ(12)内に流入した冷媒は、当該熱交換チューブ(12)内を下方に流れて下ヘッダ部(22)の右側区画(22a)内に入った後左側区画(22b)内に入り、左側区画(22b)からチューブ列(27)の上昇流チューブ群(27B)の熱交換チューブ(12)内に流入する。上昇流チューブ群(27B)の熱交換チューブ(12)内に流入した冷媒は、当該熱交換チューブ(12)内を上方に流れて上ヘッダ部(21)の左側区画(21b)内に入り、冷媒出口(25)から流出する。   In the evaporator (20) described above, the refrigerant that has passed through the compressor, the condenser, and the expansion valve enters the right compartment (21a) of the upper header portion (21) from the refrigerant inlet (24), and the tube from the right compartment (21a). It flows into the heat exchange tubes (12) of the downflow tube group (27A) in the row (27). The refrigerant that has flowed into the heat exchange tube (12) of the downflow tube group (27A) flows downward through the heat exchange tube (12) and enters the right compartment (22a) of the lower header portion (22). It enters the rear left compartment (22b) and flows from the left compartment (22b) into the heat exchange tube (12) of the upward flow tube group (27B) in the tube row (27). The refrigerant that has flowed into the heat exchange tube (12) of the upflow tube group (27B) flows upward in the heat exchange tube (12) and enters the left compartment (21b) of the upper header portion (21). It flows out from the refrigerant outlet (25).

液相冷媒は、上側に位置するヘッダ部の入り側区画である上ヘッダ部(21)の右側区画(21a)の下部に貯まりやすいが、冷媒が上から下に流れる下降流チューブ群(27A)の熱交換チューブ(12)の上端寄りの一定長さ部分が右側区画(21a)内に挿入され、当該熱交換チューブ(12)の上端が風上側に向かって下方に傾斜しているので、上ヘッダ部(21)の右側区画(21a)の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路(12a)内に流入しやすくなり、下方に位置する風上側の冷媒通路(12a)内に流入する冷媒量が、上方に位置する風下側の冷媒通路(12a)に流入する冷媒量よりも多くなる。   The liquid refrigerant is easily stored in the lower part of the right side section (21a) of the upper header part (21) that is the entrance side section of the header part located on the upper side, but the downflow tube group (27A) in which the refrigerant flows from top to bottom The fixed length portion near the upper end of the heat exchange tube (12) is inserted into the right section (21a), and the upper end of the heat exchange tube (12) is inclined downward toward the windward side, so The liquid-phase refrigerant stored in the lower portion of the right section (21a) of the header section (21) is likely to flow into the windward refrigerant passage (12a) located below, and the windward refrigerant passage (lower) ( The amount of refrigerant flowing into 12a) is larger than the amount of refrigerant flowing into the leeward refrigerant passage (12a) located above.

また、液相冷媒は、下側に位置するヘッダ部の入り側区画である下ヘッダ部(22)の左側区画(22b)の下部に貯まりやすいが、冷媒が下から上に流れる上昇流チューブ群(27B)の熱交換チューブ(12)の下端寄りの一定長さ部分が左側区画(22b)内に挿入され、当該熱交換チューブ(12)の下端が風上側に向かって下方に傾斜しているので、下ヘッダ部(22)の左側区画(22b)の下部に貯まった液相冷媒が、下方に位置する風上側の冷媒通路(12a)内に流入しやすくなり、下方に位置する風上側の冷媒通路(12a)内に流入する冷媒量が、上方に位置する風下側の冷媒通路(12a)に流入する冷媒量よりも多くなる。   Further, the liquid phase refrigerant is easily stored in the lower part of the left side section (22b) of the lower header part (22) which is the entry side section of the header part located on the lower side, but the upward flow tube group in which the refrigerant flows from the bottom to the top A fixed length portion near the lower end of the heat exchange tube (12) of (27B) is inserted into the left compartment (22b), and the lower end of the heat exchange tube (12) is inclined downward toward the windward side. Therefore, the liquid refrigerant stored in the lower part of the left section (22b) of the lower header part (22) is likely to flow into the windward refrigerant passage (12a) located below, and the windward refrigerant located below is located on the windward side. The amount of refrigerant flowing into the refrigerant passage (12a) is larger than the amount of refrigerant flowing into the leeward refrigerant passage (12a) located above.

したがって、各熱交換チューブ(12)の風上側冷媒通路(12a)において、風下側冷媒通路(12a)に比べて冷媒の蒸発が促進されて通路抵抗が増大した場合であっても、風上側の冷媒通路(12a)内に冷媒が流入しやすくなって各熱交換チューブ(12)の風上側冷媒通路(12a)と風下側冷媒通路(12a)を流れる冷媒量が均一化される。その結果、各熱交換チューブ(12)の風上側と風下側の温度にばらつきが発生することが抑制され、エバポレータ(20)の風上側の温度分布と風下側の温度分布とに比較的大きな差が生じることが抑制されて冷却性能に大きなばらつきが発生することがなくなり、熱交換性能の向上を図ることが可能になる。   Therefore, in the windward side refrigerant passage (12a) of each heat exchange tube (12), even when the evaporation of the refrigerant is promoted and the passage resistance is increased as compared with the leeward side refrigerant passage (12a), The refrigerant easily flows into the refrigerant passage (12a), and the amount of refrigerant flowing through the windward refrigerant passage (12a) and the leeward refrigerant passage (12a) of each heat exchange tube (12) is made uniform. As a result, the occurrence of variations in the temperature on the leeward and leeward sides of each heat exchange tube (12) is suppressed, and there is a relatively large difference between the temperature distribution on the leeward side and the temperature distribution on the leeward side of the evaporator (20). It is possible to improve the heat exchange performance without the occurrence of a large variation in the cooling performance.

上述した実施形態2のエバポレータ(20)において、チューブ列(27)の下降流チューブ群(27A)の熱交換チューブ(12)の下端部、および上昇流チューブ群(27B)の熱交換チューブ(12)の上端部は、それぞれ風上側に向かって下方に傾斜している必要はなく、水平状であってもよい。   In the evaporator (20) of the second embodiment described above, the lower end of the heat exchange tube (12) of the downflow tube group (27A) of the tube row (27) and the heat exchange tube (12 of the upflow tube group (27B)) ) Are not necessarily inclined downward toward the windward side, and may be horizontal.

この発明によるエバポレータは、自動車に搭載される冷凍サイクルであるカーエアコンに好適に用いられる。   The evaporator according to the present invention is suitably used for a car air conditioner that is a refrigeration cycle mounted on an automobile.

(1):エバポレータ
(5):風下側上ヘッダ部(第1ヘッダ部)
(5a):右側区画(入り側区画)
(6):風上側上ヘッダ部(第3ヘッダ部)
(6a):左側区画(入り側区画)
(9);風下側下ヘッダ部(第2ヘッダ部)
(9b):左側区画(入り側区画)
(11):風上側下ヘッダ部(第4ヘッダ部)
(11b):右側区画(入り側区画)
(12):熱交換チューブ
(12a):冷媒通路
(13):風下側チューブ列(第1チューブ列)
(13A):下降流チューブ群
(13B):上昇流チューブ群
(14):風上側チューブ列
(14A):上昇流チューブ群
(14B):下降流チューブ群
(20):エバポレータ
(21):上ヘッダ部(第1ヘッダ部)
(21a):右側区画(入り側区画)
(22):下ヘッダ部(第2ヘッダ部)
(22b):左側区画(入り側区画)
(27):チューブ列
(27A):下降流チューブ群
(27B):上昇流チューブ群
(1): Evaporator
(5): Downward upper header (first header)
(5a): Right section (entrance section)
(6): Upwind header section (third header section)
(6a): Left compartment (entrance compartment)
(9); Downward lower header (second header)
(9b): Left section (entrance section)
(11): Upwind lower header (fourth header)
(11b): Right section (entrance section)
(12): Heat exchange tube
(12a): Refrigerant passage
(13): Downward tube row (first tube row)
(13A): Downflow tube group
(13B): Upflow tube group
(14): Windward tube row
(14A): Upflow tube group
(14B): Downflow tube group
(20): Evaporator
(21): Upper header (first header)
(21a): Right section (entrance section)
(22): Lower header (second header)
(22b): Left compartment (entrance compartment)
(27): Tube row
(27A): Downflow tube group
(27B): Upflow tube group

Claims (4)

長手方向を上下方向に向けるとともに幅方向を通風方向に向けた状態で互いに間隔をおいて配置された複数の扁平状熱交換チューブからなる少なくとも1つのチューブ列と、各チューブ列の熱交換チューブの長手方向両端側に長手方向をチューブの並び方向に向けて配置され、かつ当該チューブ列のチューブの長手方向両端部が接続された少なくとも2つのヘッダ部とを備えており、熱交換チューブが通風方向に並んだ複数の冷媒通路を有し、熱交換チューブの両端寄りの一定長さ部分がヘッダ部内に挿入され、少なくとも1つのヘッダ部に、熱交換チューブに冷媒が流入する入り側区画が設けられている熱交換器であって、
熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜しているエバポレータ。
At least one tube row composed of a plurality of flat heat exchange tubes arranged at intervals in a state where the longitudinal direction is directed in the vertical direction and the width direction is directed in the ventilation direction, and the heat exchange tubes of each tube row The heat exchange tube is provided with at least two header portions arranged at both ends in the longitudinal direction so that the longitudinal direction is directed in the tube arranging direction and connected to both ends in the longitudinal direction of the tubes in the tube row. A fixed length portion near both ends of the heat exchange tube is inserted into the header portion, and at least one header portion is provided with an entry side section into which the refrigerant flows into the heat exchange tube. A heat exchanger,
The evaporator in which the edge part of the part inserted in the entrance side division in a heat exchange tube inclines below toward the windward side.
長手方向を上下方向に向けて配置された複数の扁平状熱交換チューブからなる第1チューブ列および第2チューブ列が、第1チューブ列が風下側に位置するように通風方向に並んで設けられ、第1チューブ列の熱交換チューブの上下両端側に、第1チューブ列の全熱交換チューブが接続された第1ヘッダ部および第2ヘッダ部が設けられ、第2チューブ列の熱交換チューブの上下両端側に、第2チューブ列の全熱交換チューブが接続された第3ヘッダ部および第4ヘッダ部が設けられており、
第1チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群を有し、第2チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群を有し、第1チューブ列の下降流チューブ群が第2チューブ列の上昇流チューブ群の風下側に位置しており、
第1ヘッダ部に、第1チューブ列の下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第4ヘッダ部に、第2チューブ列の上昇流チューブ群の熱交換チューブの下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第1チューブ列の下降流チューブ群の熱交換チューブおよび第2チューブ列の上昇流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している請求項1記載のエバポレータ。
A first tube row and a second tube row composed of a plurality of flat heat exchange tubes arranged with the longitudinal direction directed in the vertical direction are provided side by side in the ventilation direction so that the first tube row is located on the leeward side. The first header portion and the second header portion to which the total heat exchange tubes of the first tube row are connected are provided on the upper and lower ends of the heat exchange tubes of the first tube row, and the heat exchange tubes of the second tube row are provided. A third header part and a fourth header part to which the total heat exchange tubes of the second tube row are connected are provided on both upper and lower ends.
The first tube row is composed of a plurality of heat exchange tubes arranged continuously, and has a downflow tube group in which the refrigerant flows from top to bottom in the heat exchange tube, and the second tube row is arranged continuously. The upflow tube group is composed of a plurality of heat exchange tubes and the refrigerant flows from the bottom to the top in the heat exchange tubes, and the downflow tube group of the first tube row is the leeward side of the upflow tube group of the second tube row Located in the
The upper end portion of the heat exchange tube of the downflow tube group of the first tube row is connected to the first header portion, and an entry side section into which the refrigerant flows into the heat exchange tube of the downflow tube group is provided. The lower end part of the heat exchange tube of the upflow tube group of the second tube row is connected to the 4 header part, and an entrance side section into which the refrigerant flows into the heat exchange tube of the upflow tube group is provided. The ends of the portions inserted in the inlet side sections of the heat exchange tubes of the downflow tube group of the tube row and the heat exchange tubes of the upflow tube group of the second tube row are inclined downward toward the windward side. The evaporator according to claim 1.
第1チューブ列に、前記下降流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群とが交互に並んで設けられ、第2チューブ列に、前記上昇流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群とが交互に並んで設けられ、第1チューブ列の下降流チューブ群が第2チューブ列の上昇流チューブ群の風下側に位置するとともに、第1チューブ列の上昇流チューブ群が第2チューブ列の下降流チューブ群の風下側に位置しており、
第2ヘッダ部に、第1チューブ列の上昇流チューブ群の下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第3ヘッダ部に、第2チューブ列の下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第1チューブ列の上昇流チューブ群の熱交換チューブおよび第2チューブ列の下降流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している請求項2記載のエバポレータ。
In the first tube row, the downflow tube groups and the upflow tube groups that are composed of a plurality of heat exchange tubes arranged in succession and in which the refrigerant flows from the bottom to the top in the heat exchange tubes are alternately arranged. In the second tube row, the upflow tube groups and the downflow tube groups comprising a plurality of continuously arranged heat exchange tubes and the refrigerant flowing from top to bottom in the heat exchange tubes are alternately arranged. And the downflow tube group of the first tube row is located on the leeward side of the upflow tube group of the second tube row, and the upflow tube group of the first tube row is leeward of the downflow tube group of the second tube row. Located on the side,
The second header portion is connected to the lower end portion of the upflow tube group of the first tube row, and is provided with an entry side section through which the refrigerant flows into the heat exchange tube of the upflow tube group. The upper end portion of the heat exchange tube of the downflow tube group of the second tube row is connected, and an entrance side section into which the refrigerant flows into the heat exchange tube of the downflow tube group is provided, and the first tube row rises. The end part of the part inserted in the entrance side section in the heat exchange tube of the flow tube group and the heat exchange tube of the downflow tube group of the second tube row is inclined downward toward the windward side. The described evaporator.
長手方向を上下方向に向けて配置された複数の扁平状熱交換チューブからなる1つのチューブ列が設けられ、チューブ列の熱交換チューブの上下両端側に、チューブ列の全熱交換チューブが接続された第1ヘッダ部および第2ヘッダ部が設けられており、
チューブ列が、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を上から下に流れる下降流チューブ群と、連続して並んだ複数の熱交換チューブからなりかつ冷媒が熱交換チューブ内を下から上に流れる上昇流チューブ群とを有しており、
第1ヘッダ部に、下降流チューブ群の熱交換チューブの上端部が接続されるとともに、当該下降流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、第2ヘッダ部に、上昇流チューブ群の熱交換チューブの下端部が接続されるとともに、当該上昇流チューブ群の熱交換チューブに冷媒が流入する入り側区画が設けられ、下降流チューブ群の熱交換チューブおよび上昇流チューブ群の熱交換チューブにおける入り側区画内に挿入された部分の端部が、風上側に向かって下方に傾斜している請求項1記載のエバポレータ。
One tube row consisting of a plurality of flat heat exchange tubes arranged with the longitudinal direction facing the vertical direction is provided, and the total heat exchange tubes of the tube row are connected to the upper and lower ends of the heat exchange tubes of the tube row. A first header portion and a second header portion are provided,
The tube row is composed of a plurality of heat exchange tubes arranged continuously and the downflow tube group in which the refrigerant flows from the top to the bottom in the heat exchange tube, and the plurality of heat exchange tubes arranged in series and the refrigerant is And an upflow tube group that flows from the bottom to the top in the heat exchange tube,
The first header portion is connected to the upper end portion of the heat exchange tube of the downflow tube group, and is provided with an entry side section into which the refrigerant flows into the heat exchange tube of the downflow tube group, and the second header portion, The lower end portion of the heat exchange tube of the upflow tube group is connected, and an inlet side section into which the refrigerant flows into the heat exchange tube of the upflow tube group is provided, and the heat exchange tube and the upflow tube of the downflow tube group The evaporator according to claim 1, wherein an end of a portion inserted into the entrance side section of the heat exchange tube of the group is inclined downward toward the windward side.
JP2014145945A 2014-07-16 2014-07-16 Evaporator Pending JP2016023815A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2014145945A JP2016023815A (en) 2014-07-16 2014-07-16 Evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2014145945A JP2016023815A (en) 2014-07-16 2014-07-16 Evaporator

Publications (1)

Publication Number Publication Date
JP2016023815A true JP2016023815A (en) 2016-02-08

Family

ID=55270739

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2014145945A Pending JP2016023815A (en) 2014-07-16 2014-07-16 Evaporator

Country Status (1)

Country Link
JP (1) JP2016023815A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018062519A1 (en) * 2016-09-29 2018-04-05 ダイキン工業株式会社 Heat exchanger and air conditioner
JP2022122229A (en) * 2021-02-09 2022-08-22 崇賢 ▲黄▼ Tank and multiple flow-passage liquid-cooled radiator using the same

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58119083U (en) * 1982-01-30 1983-08-13 カルソニックカンセイ株式会社 Heat exchanger
US20060201198A1 (en) * 2005-03-09 2006-09-14 Denso Corporation Heat exchanger
US20110017438A1 (en) * 2009-07-23 2011-01-27 Danfoss Sanhua (Hangzhou) Micro Channel Heat Exchanger Co., Ltd. Multi-channel heat exchanger with improved uniformity of refrigerant fluid distribution
JP2013019581A (en) * 2011-07-11 2013-01-31 Hitachi Appliances Inc Refrigeration cycle apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58119083U (en) * 1982-01-30 1983-08-13 カルソニックカンセイ株式会社 Heat exchanger
US20060201198A1 (en) * 2005-03-09 2006-09-14 Denso Corporation Heat exchanger
JP2006250412A (en) * 2005-03-09 2006-09-21 Denso Corp Heat exchanger
US20110017438A1 (en) * 2009-07-23 2011-01-27 Danfoss Sanhua (Hangzhou) Micro Channel Heat Exchanger Co., Ltd. Multi-channel heat exchanger with improved uniformity of refrigerant fluid distribution
JP2013019581A (en) * 2011-07-11 2013-01-31 Hitachi Appliances Inc Refrigeration cycle apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018062519A1 (en) * 2016-09-29 2018-04-05 ダイキン工業株式会社 Heat exchanger and air conditioner
JP2018059704A (en) * 2016-09-29 2018-04-12 ダイキン工業株式会社 Heat exchanger and air conditioner
US10794636B2 (en) 2016-09-29 2020-10-06 Daikin Industries, Ltd. Heat exchanger and air conditioner
JP2022122229A (en) * 2021-02-09 2022-08-22 崇賢 ▲黄▼ Tank and multiple flow-passage liquid-cooled radiator using the same
JP7173629B2 (en) 2021-02-09 2022-11-16 崇賢 ▲黄▼ Tank and multi-channel liquid cooling radiator using the same

Similar Documents

Publication Publication Date Title
JP5486782B2 (en) Evaporator
JP5740134B2 (en) Evaporator
JP5693346B2 (en) Evaporator
JP5585543B2 (en) Vehicle cooling system
JP5764345B2 (en) Evaporator
JP5759762B2 (en) Evaporator
JP2012197974A5 (en)
JP6842915B6 (en) Evaporator
JP2015034670A (en) Evaporator
JP5636215B2 (en) Evaporator
JP2013174398A (en) Heat exchanger
JP2011257111A5 (en)
JP2016023815A (en) Evaporator
JP6486223B2 (en) Evaporator
JP5194279B2 (en) Evaporator
JP6785137B2 (en) Evaporator
JP2018087646A5 (en)
JP5736164B2 (en) Evaporator
JP5674376B2 (en) Evaporator
JP6617003B2 (en) Heat exchanger
JP2015040641A (en) Evaporator
JP2016057036A (en) Heat exchanger
JP6486212B2 (en) Evaporator and vehicle air conditioner using the same
JP2018119736A (en) Evaporator
JP2018119747A (en) Evaporator

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20170418

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20180219

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20180410

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20181204