JPH02197796A - Finned heat exchanger - Google Patents

Finned heat exchanger

Info

Publication number
JPH02197796A
JPH02197796A JP1545289A JP1545289A JPH02197796A JP H02197796 A JPH02197796 A JP H02197796A JP 1545289 A JP1545289 A JP 1545289A JP 1545289 A JP1545289 A JP 1545289A JP H02197796 A JPH02197796 A JP H02197796A
Authority
JP
Japan
Prior art keywords
flat
heat exchanger
fin
flat plate
draining
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
Application number
JP1545289A
Other languages
Japanese (ja)
Other versions
JP2753016B2 (en
Inventor
Osao Kido
長生 木戸
Hiroaki Kase
広明 加瀬
Takashi Nakamura
隆 中邨
Akira Aoki
亮 青木
Osamu Aoyanagi
治 青柳
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.)
Panasonic Ecology Systems Co Ltd
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
Matsushita Seiko Co Ltd
Matsushita Electric Industrial 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 Matsushita Refrigeration Co, Matsushita Seiko Co Ltd, Matsushita Electric Industrial Co Ltd filed Critical Matsushita Refrigeration Co
Priority to JP1015452A priority Critical patent/JP2753016B2/en
Publication of JPH02197796A publication Critical patent/JPH02197796A/en
Application granted granted Critical
Publication of JP2753016B2 publication Critical patent/JP2753016B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F17/00Removing ice or water from heat-exchange apparatus
    • F28F17/005Means for draining condensates from heat exchangers, e.g. from evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/126Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins
    • F28F1/128Fins with openings, e.g. louvered fins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00Fins
    • F28F2215/12Fins with U-shaped slots for laterally inserting conduits

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To permit the falling of water drips from gaps between flat tubes to a lower stage along the draining surface of a flat plate fin even when a heat exchanger is used as an evaporator and the water drips are produced by condensation and are adhered to the outer surface of the heat exchanger by a method wherein draining surfaces, pinched by flat groove provided at the side of a fore rim and the same provided at the side of an aft rim, are provided on the surface of the flat plate fin while the flat tubes are divided by the draining surface utilizing it as a boundary. CONSTITUTION:A heat exchanger is constituted of flat plate fins 7, provided with a plurality of stages of flat grooves 8 constituted by notching both ends of fore and aft rims, and flat tubes 1, inserted from side surfaces into the flat grooves 8 of the flat plate fins 7 arranged in parallel to each other with a given fin pitch Pf, and is provided with draining surfaces 9, pinched by a fore rim side flat groove 8f and aft rim side flat grooves 8r, on the flat plate fins 7 while the flat tubes 11 are divided by the draining surface 9 utilizing it as a boundary. When the finned heat exchanger is used as an evaporator and water drips L adhered to the outer surface of the heat exchanger by condensation, the water drips L may be dropped to a lower stage through the gaps (w) between the divided flat tubes 11 along the draining surface 9 of the flat fins 7. Accordingly, the increase of the ventilating resistance of air stream A as well as the deterioration of heat transfer rate may be restrained.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は空調機器や冷凍機器、自動車機器等に使用され
、冷媒と空気等の流体間で熱の授受を行なうフィン付熱
交換器に関するものである。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a finned heat exchanger that is used in air conditioning equipment, refrigeration equipment, automobile equipment, etc., and exchanges heat between fluids such as refrigerant and air. .

従来の技術 近年、フィン付熱交換器は機器設計の面からコンパクト
化が要求されており、フィン形状及び管内面形状の改善
による高効率化が取り組まれている。
BACKGROUND OF THE INVENTION In recent years, finned heat exchangers have been required to be more compact in terms of equipment design, and efforts have been made to improve efficiency by improving the fin shape and tube inner surface shape.

以下、図面を参照しながら上述した従来のフィン付熱交
換器について説明を行う。
Hereinafter, the conventional finned heat exchanger mentioned above will be explained with reference to the drawings.

第8図と第9図は従来のフィン付熱交換器の形状を示し
、第10図は従来のフィン付熱交換器を構成するフィン
形状、第11図は偏平管形状を示す。第8図から第11
図において、1は波形状に屈曲され一定のフィンピッチ
Pfで平行に並べられた波形フィンで、両端の屈曲部2
と気流A方向に分割されたルーバ8が設けられている。
8 and 9 show the shape of a conventional finned heat exchanger, FIG. 10 shows the fin shape constituting the conventional finned heat exchanger, and FIG. 11 shows the flat tube shape. Figures 8 to 11
In the figure, reference numeral 1 denotes wave-shaped fins that are bent in a wave shape and arranged in parallel with a constant fin pitch Pf, with bent portions 2 at both ends.
A louver 8 divided in the direction of the airflow A is provided.

4は前記波形フィン1の上下両端の屈曲部2に密着され
た偏平管で、長辺4aと短辺4b及び管内を分割する分
割板4cとから構成され、長辺4aが気流A方向と平行
となるように水平方向に段ピツチPdで複数段設けられ
ている。5は偏平管4の両端に接続したヘッダで、偏平
管4と共に冷媒Rの管内流路を構成している。
Reference numeral 4 denotes a flat tube that is closely attached to the bent portions 2 at both the upper and lower ends of the corrugated fin 1, and is composed of a long side 4a, a short side 4b, and a dividing plate 4c that divides the inside of the tube, and the long side 4a is parallel to the direction of airflow A. A plurality of stages are provided in the horizontal direction with a stage pitch Pd. 5 is a header connected to both ends of the flat tube 4, and together with the flat tube 4 constitutes an internal flow path for the refrigerant R.

以上のように構成されたについて、以下第12図と第1
3図を用いてその動作を説明する。
The structure configured as above is shown below in Figure 12 and Figure 1.
The operation will be explained using FIG.

波形フィン1間を流れる気流Aと偏平管4内を流れる冷
媒Rとの間で波形フィン1及び偏平管4を介して熱交換
が行なわれる。その際、波形フィン1の表面にはルーバ
3が分割して設けられているため、波形フィン1の表面
に生じる気流Aの温度境界層の発達が抑えられ、気流A
と波形フィン1との熱伝達率の向上が図られている。ま
た、偏平管4の管内は分割板4、Cによって微小流路化
され、偏平管4と冷媒Rとの熱伝達率の向上も図られて
いる。
Heat exchange is performed between the airflow A flowing between the corrugated fins 1 and the refrigerant R flowing within the flat tube 4 via the corrugated fins 1 and the flat tube 4. At this time, since the louver 3 is provided in sections on the surface of the corrugated fin 1, the development of a temperature boundary layer of the airflow A generated on the surface of the corrugated fin 1 is suppressed, and the airflow A
The heat transfer coefficient between the corrugated fins 1 and the corrugated fins 1 is improved. Moreover, the inside of the flat tube 4 is made into a microchannel by the dividing plates 4 and C, and the heat transfer coefficient between the flat tube 4 and the refrigerant R is also improved.

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、このフィン付熱交
換器を蒸発器として使用し外表面に水滴りが凝縮する場
合に、第14図に示すように、波形フィン1の屈曲部2
の内側に水滴りが滞溜するばかりでなく、各段の波形フ
ィン1相互が偏平管4によって分割されているため、波
形フィン1の表面を伝わり落下する水滴りは下段へは落
下し難く偏平管4の上面に滞溜することとなり、気流へ
の通風抵抗の増大を引き起こし、また波形フィン1と気
流へとの熱伝達も阻害する。
Problems to be Solved by the Invention However, with the above configuration, when this finned heat exchanger is used as an evaporator and water droplets condense on the outer surface, as shown in FIG. Bent part 2
Not only do water droplets accumulate inside the fins, but also because the corrugated fins 1 of each stage are separated by the flat tubes 4, the water droplets that travel down the surface of the corrugated fins 1 are difficult to fall to the lower stage, and the flat pipes This accumulates on the upper surface of the tube 4, causing an increase in ventilation resistance to the airflow, and also impeding heat transfer between the corrugated fins 1 and the airflow.

本発明は上記課題に鑑み、このフィン付熱交換器を蒸発
器として使用し外表面に水滴が凝縮する場合にも、水滴
の落下を良好にして、気流の通風抵抗の増大と熱伝達率
の低下を抑えるものである。
In view of the above problems, the present invention has been developed to improve the falling of water droplets even when water droplets condense on the outer surface by using this finned heat exchanger as an evaporator, thereby increasing the ventilation resistance of airflow and reducing the heat transfer coefficient. This is to suppress the decline.

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フィン付熱交換器は
、前後縁両端部を切り欠いて構成される偏平溝を複数段
設けた平板フィンと、前記平板フィンの偏平溝に側面か
ら挿入された偏平管とから成り、前記平板フィンの表面
に前縁側の偏平溝と後縁側の偏平溝に挟まれた排水面を
設け、かつこの排水面を境に偏平管を分割するという構
成を(filえたものである。
Means for Solving the Problems In order to solve the above problems, the finned heat exchanger of the present invention includes a flat plate fin having a plurality of flat grooves formed by cutting out both ends of the front and rear edges, and It consists of a flat tube inserted from the side into a flat groove, and a drainage surface is provided on the surface of the flat plate fin sandwiched between the flat groove on the front edge side and the flat groove on the rear edge side, and the flat tube is inserted with this drainage surface as a boundary. This is a modification of the structure of dividing.

作用 本発明は上記した構成によって、このフィン付熱交換器
を蒸発器として使用し外表面に水滴が凝縮する場合にも
、分割された偏平管の隙間から平板フィンの排水面を伝
わって水滴が下段へ落下することができるため、水滴の
落下を良好にして、気流の通風抵抗の増大と熱伝達率の
低下を抑えることができる。
Effect The present invention has the above-described configuration, so that even when this finned heat exchanger is used as an evaporator and water droplets condense on the outer surface, the water droplets are transmitted through the drainage surface of the flat fin from the gap between the divided flat tubes. Since the water droplets can fall to the lower level, it is possible to improve the falling of water droplets and suppress an increase in the ventilation resistance of the airflow and a decrease in the heat transfer coefficient.

実施例 以下本発明の実施例のフィン付熱交換器について図面を
参照しながら説明する。
EXAMPLE Hereinafter, a finned heat exchanger according to an example of the present invention will be described with reference to the drawings.

第1図と第2図は本発明の実施例におけるフィン付熱交
換器の形状を示すもので、第3図は平板フィンの形状、
第4図は偏平管の形状を示す。第1図から第4図におい
て、7は一定のフィンピッチPfで平行に並べられた複
数の平板フィンで、気流六方向の前後縁両端を切り欠い
て形成され一定の段方向ピッチPdで配列された偏平溝
8と、前縁側の偏平溝8fと後縁側の偏平溝8rの間に
幅Wの排水面9が設けられている。また平板フィン7の
表面には、気流六方向に平板フィン7を分割したルーバ
10も設けられている。11は前記平板フィンの偏平溝
8に前後縁両端から挿入密着された偏平管で、長辺11
aと短辺11b及び管内を分割する分割板11cとから
構成され、長辺11aが気流A方向と平行となるように
段ピツチPd向に対して幅Wの隙間で前縁側の偏平管1
1. fと後縁1Itqの偏平管11rとに分割されて
いる。12は偏平管11の両端に接続したヘッダで、偏
平管11と共に冷媒凡の管内流路を構成している。
1 and 2 show the shape of a finned heat exchanger in an embodiment of the present invention, and FIG. 3 shows the shape of a flat fin,
FIG. 4 shows the shape of the flat tube. In FIGS. 1 to 4, reference numeral 7 denotes a plurality of flat plate fins arranged in parallel at a constant fin pitch Pf, which are formed by cutting out both ends of the front and rear edges in six directions of airflow, and are arranged at a constant pitch Pd in the step direction. A drainage surface 9 having a width W is provided between the flat grooves 8 on the leading edge side and the flat grooves 8f on the leading edge side and the flat grooves 8r on the rear edge side. Further, on the surface of the flat fin 7, louvers 10 are also provided, which are obtained by dividing the flat fin 7 into six directions of air flow. Reference numeral 11 denotes a flat tube inserted into the flat groove 8 of the flat plate fin from both ends of the front and rear edges, and the long side 11
a, a short side 11b, and a dividing plate 11c that divides the inside of the tube, and the flat tube 1 on the leading edge side is formed with a gap of width W in the direction of the step pitch Pd so that the long side 11a is parallel to the direction of the airflow A.
1. f and a flat tube 11r having a trailing edge 1Itq. Headers 12 are connected to both ends of the flat tube 11, and together with the flat tube 11 constitute an internal flow path for the refrigerant.

以上のように構成されたフィン付熱交換器ついて、以下
第5図と第6図を用いてその動作について説明する。
The operation of the finned heat exchanger constructed as above will be described below with reference to FIGS. 5 and 6.

平板フィン7間を流れる気流Aとへラダ12を経て偏平
管11内を流れる冷媒Rとの間で平板フィン7及び偏平
管11を介して熱交換が行なわれる。
Heat exchange occurs between the airflow A flowing between the flat fins 7 and the refrigerant R flowing through the flat tube 11 via the ladder 12 via the flat fins 7 and the flat tube 11.

その際、平板フィン7の表面にはルーバ10が設けられ
ているため、平板フィン7の表面に生じる気流Aの温度
境界層の発達が抑えられ、気流Aと平板フィン7との熱
伝達率の向上が図られている。
At this time, since the louver 10 is provided on the surface of the flat fin 7, the development of a temperature boundary layer of the airflow A generated on the surface of the flat fin 7 is suppressed, and the heat transfer coefficient between the airflow A and the flat fin 7 is reduced. Improvements are being made.

また、偏平管11の管内は分割板10cによって微小流
路化され、偏平管11と冷媒Rとの熱伝達率の向上が図
られている。
Moreover, the inside of the flat tube 11 is made into microchannels by the dividing plate 10c, and the heat transfer coefficient between the flat tube 11 and the refrigerant R is improved.

またこのフィン付熱交換器を蒸発器として使用し、外表
面に水滴りが凝縮する場合にも、第7図に示すように、
分割された偏平管11の幅Wの隙問から平板フィン7の
排水面9を伝わって水滴りが下段へ落手することができ
るため、水滴I−の落下を良好にして、気流への通風抵
抗の増大と熱伝達率の低下を抑えることができる。
Also, when this finned heat exchanger is used as an evaporator and water droplets condense on the outer surface, as shown in Figure 7,
Water droplets can flow down the drain surface 9 of the flat plate fin 7 from the gap of the width W of the divided flat tube 11 to the lower stage, making it easier for the water droplets I- to fall and providing ventilation to the airflow. It is possible to suppress an increase in resistance and a decrease in heat transfer coefficient.

以上のように本実施例によれば、前後縁両端部を切り欠
いて構成される偏平溝8を複数段設けた平板フィン7と
、一定のフィンピッチPfで平行に並べられた前記平板
フィン7の偏平溝8に側面から挿入された偏平管11と
から成り、前記平板フィン7の表面に前縁側の偏平溝8
fと後縁側の偏平溝8rに挟まれた排水面9を設け、か
つこの排水面9を境に偏平管11を分割することにより
、このフィン付熱交換器を蒸発器として使用し、外表面
に水滴りが凝縮する場合に、分割された偏平管11の幅
Wの隙間から平板フィン7の排水面9を伝わって水滴I
−が下段へ落下することができるため、水滴りの落下を
良好にして、気流Aの通風抵抗の増大と熱伝達率の低下
を抑えることができる。
As described above, according to this embodiment, the flat plate fins 7 are provided with a plurality of flat grooves 8 formed by cutting out both ends of the front and rear edges, and the flat plate fins 7 are arranged in parallel at a constant fin pitch Pf. A flat tube 11 is inserted into the flat groove 8 from the side, and a flat groove 8 on the front edge side is formed on the surface of the flat plate fin 7.
By providing a drainage surface 9 sandwiched between f and the flat groove 8r on the trailing edge side, and dividing the flat tube 11 along this drainage surface 9, this finned heat exchanger can be used as an evaporator, and the outer surface When the water droplets condense in the flat pipe 11, the water droplets I pass through the drainage surface 9 of the flat plate fin 7 from the gap of the width W of the divided flat tube 11.
- can fall to the lower stage, so water droplets can fall smoothly, and an increase in ventilation resistance of the airflow A and a decrease in heat transfer coefficient can be suppressed.

発明の効果 以」二のように本発明は、前後縁両端部を切り欠いて構
成される偏平溝を複数段設けた平板フィンと、前記平板
フィンの偏平溝に側面から挿入された偏平管とから成り
、前記平板フィンの表面に前縁側の偏平溝と後縁側の偏
平溝に挟まれた排水面を設け、かつこの排水面を境に偏
平管を分割することにより、このフィン付熱交換器を蒸
発器として使用し外表面に水滴が凝縮する場合にも、分
割された偏平管の隙間から平板フィンの排水面を伝わっ
て水滴が下段へ落下することができるため、水滴の落下
を良好にして、気流の通風抵抗の増大と熱伝達率の低下
を抑えることができる。
Effects of the Invention As described in 2., the present invention provides a flat plate fin having a plurality of flat grooves formed by cutting out both ends of the front and rear edges, and a flat tube inserted from the side into the flat groove of the flat plate fin. This finned heat exchanger is made of Even when used as an evaporator and water droplets condense on the outer surface, the water droplets can fall to the lower stage through the gap between the divided flat tubes and the drainage surface of the flat fin, making it easier for water droplets to fall. This makes it possible to suppress increases in airflow resistance and decreases in heat transfer coefficient.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例におけるフィン付熱交換器の形
状を示す斜視図、第2図は第1図の要部斜視図、第3図
は第1図の平板フィンの形状を示す平面図、第4図は第
1図の偏平管の形状を示す断面図、第5図は第1図の使
用状態における気流の流動状態を示す断面図、第6図は
第1図の冷媒回路を示す斜視図、第7図は第1図の水滴
付着状況を示す断面図、第8図は従来のフィン付熱交換
器の形状を示す斜視図、第9図は第8図の要部斜視図、
第10図は第8図の波形フィンの形状を示す平面図、第
11図は第8図の偏平管の形状を示す断面図、第12図
は第8図の使用状態における気流の流動状態を示す断面
図、第13図は第8図の冷媒回路を示す斜視図、第14
図は第8図の水滴付着状況を示す断面図である。 7・・・平板フィン、8・・・偏平溝、9・・・排水面
、11・・・偏平管。 代理人の氏名 弁理士 粟野 重孝 他1名第 3 図 ワ 子板フィン rO−一ノ12−バ 第4図 7ノーーール鵬背4′庁 第 図 第 図 1O−ル−バ Jl−偏平管 霞°ぐ ■し 第10 第11図 C
Fig. 1 is a perspective view showing the shape of a finned heat exchanger in an embodiment of the present invention, Fig. 2 is a perspective view of the main part of Fig. 1, and Fig. 3 is a plan view showing the shape of the flat plate fin in Fig. 1. Figure 4 is a cross-sectional view showing the shape of the flat tube in Figure 1, Figure 5 is a cross-sectional view showing the flow state of airflow in the operating condition of Figure 1, and Figure 6 is a cross-sectional view showing the refrigerant circuit in Figure 1. 7 is a sectional view showing the water droplet adhesion situation in FIG. 1, FIG. 8 is a perspective view showing the shape of a conventional finned heat exchanger, and FIG. 9 is a perspective view of the main part of FIG. 8. ,
Fig. 10 is a plan view showing the shape of the corrugated fin shown in Fig. 8, Fig. 11 is a sectional view showing the shape of the flat tube shown in Fig. 8, and Fig. 12 shows the flow state of the airflow in the operating state shown in Fig. 8. 13 is a perspective view showing the refrigerant circuit in FIG. 8, and FIG.
The figure is a sectional view showing the state of water droplet adhesion in FIG. 8. 7... Flat plate fin, 8... Flat groove, 9... Drainage surface, 11... Flat pipe. Name of agent: Patent attorney Shigetaka Awano and 1 other person No. 3 Fig. Wako board fin rO-1-12-B Fig. 4 7 Noor Peng back 4' Office Fig. Fig. 1 O-Rouba Jl-Flat pipe Kasumi° Gusushi No. 10 Fig. 11 C

Claims (1)

【特許請求の範囲】[Claims] 前後縁両端部を切り欠いて構成される偏平溝を複数段設
けた平板フィンと、前記平板フィンの偏平溝に側面から
挿入された偏平管とから成り、前記平板フィンの表面に
前縁側の偏平溝と後縁側の偏平溝に挟まれた排水面を設
け、かつこの排水面を境に偏平管を分割したことを特徴
とするフィン付熱交換器。
It consists of a flat plate fin with a plurality of flat grooves formed by cutting out both ends of the front and rear edges, and a flat tube inserted into the flat groove of the flat plate fin from the side. A finned heat exchanger characterized in that a drainage surface is provided between the groove and the flat groove on the trailing edge side, and the flat tube is divided along the drainage surface.
JP1015452A 1989-01-25 1989-01-25 Finned heat exchanger Expired - Fee Related JP2753016B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1015452A JP2753016B2 (en) 1989-01-25 1989-01-25 Finned heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1015452A JP2753016B2 (en) 1989-01-25 1989-01-25 Finned heat exchanger

Publications (2)

Publication Number Publication Date
JPH02197796A true JPH02197796A (en) 1990-08-06
JP2753016B2 JP2753016B2 (en) 1998-05-18

Family

ID=11889195

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1015452A Expired - Fee Related JP2753016B2 (en) 1989-01-25 1989-01-25 Finned heat exchanger

Country Status (1)

Country Link
JP (1) JP2753016B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08247678A (en) * 1995-03-10 1996-09-27 Nagano Haruo Heat-exchanger made of aluminum
US20160061475A1 (en) * 2013-04-24 2016-03-03 Mitsubishi Electric Corporation Dehumidifier
EP3173725A4 (en) * 2014-07-25 2018-04-04 Mitsubishi Electric Corporation Heat exchanger and air-conditioning and refrigerating apparatus with heat exchanger

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4425113Y1 (en) * 1966-10-20 1969-10-22
JPS558874U (en) * 1978-07-05 1980-01-21
JPS55144948U (en) * 1979-04-05 1980-10-17

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4425113Y1 (en) * 1966-10-20 1969-10-22
JPS558874U (en) * 1978-07-05 1980-01-21
JPS55144948U (en) * 1979-04-05 1980-10-17

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08247678A (en) * 1995-03-10 1996-09-27 Nagano Haruo Heat-exchanger made of aluminum
US20160061475A1 (en) * 2013-04-24 2016-03-03 Mitsubishi Electric Corporation Dehumidifier
US10907911B2 (en) * 2013-04-24 2021-02-02 Mitsubishi Electric Corporation Dehumidifier
EP3173725A4 (en) * 2014-07-25 2018-04-04 Mitsubishi Electric Corporation Heat exchanger and air-conditioning and refrigerating apparatus with heat exchanger

Also Published As

Publication number Publication date
JP2753016B2 (en) 1998-05-18

Similar Documents

Publication Publication Date Title
JP4122578B2 (en) Heat exchanger
EP1106951A2 (en) Continuous combination fin for a heat exchanger
JP5550106B2 (en) Corrugated fin heat exchanger drainage structure
JP2001059690A (en) Heat exchanger
JPS58217195A (en) Heat exchanger
US6435268B1 (en) Evaporator with improved condensate drainage
JPH07109353B2 (en) Heat exchanger with fins
JP2568968Y2 (en) Heat exchanger
JP3359466B2 (en) Evaporator for room air conditioner
JPH02251093A (en) Finned heat exchanger
JPH02197796A (en) Finned heat exchanger
JP2624336B2 (en) Finned heat exchanger
JP2990947B2 (en) Refrigerant condenser
JPH02309193A (en) Heat exchanger with fin
JP2002048491A (en) Heat exchanger for cooling
EP0803695A2 (en) Plate-fin type heat exchanger
JPH0755380A (en) Heat exchanger
JPH02309194A (en) Heat exchanger with fin
JPH0313794A (en) Heat exchanger with fin
JPH02154987A (en) Finned heat exchanger
JPH02166393A (en) Heat exchanger with fin
JPS58214783A (en) Heat exchanger
JPH0331692A (en) Heat exchanger
JPH025331Y2 (en)
JPH0886581A (en) Cross-fin tube type heat exchanger

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees