JPH10197183A - Finned heat exchanger - Google Patents

Finned heat exchanger

Info

Publication number
JPH10197183A
JPH10197183A JP5497A JP5497A JPH10197183A JP H10197183 A JPH10197183 A JP H10197183A JP 5497 A JP5497 A JP 5497A JP 5497 A JP5497 A JP 5497A JP H10197183 A JPH10197183 A JP H10197183A
Authority
JP
Japan
Prior art keywords
fin
airflow
fins
upstream
air flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP5497A
Other languages
Japanese (ja)
Inventor
Mitsunori Taniguchi
光徳 谷口
Osao Kido
長生 木戸
Satoshi Miyahara
里支 宮原
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 Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 filed Critical Matsushita Refrigeration Co
Priority to JP5497A priority Critical patent/JPH10197183A/en
Publication of JPH10197183A publication Critical patent/JPH10197183A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To prevent the deterioration of heat exchanging amount and restrain frosting at the upstream of air stream to elongate the period of time of heating operation by a method wherein continuous draining groove is provided in the direction of gravity between mutual rows of heat transfer tubes on a fin. SOLUTION: Heat exchange is effected between air flow, which flows between fins 4, and refrigerant, which flows through the inside of a heat transfer tube 2, through the fin 4 and the heat transfer tube 2. In this case, when the evaporating temperature of the refrigerant is lowered, moisture in air is condensed on the surface of the fin 4a at the upstream side of the air flow. The condensate is conducted by the air flow to flow along the fin 4a toward the downstream of the air flow and flows into a draining groove 5, continued in the direction of gravity between mutual rows of the heat transfer tubes 2 on the fin 4, then, is discharged into the direction of gravity. Accordingly, the inflow of the condensate, condensed on the fin 4a at the upstream of the air flow and precluding the heat exchange between the air flow and the fin 4, into a fin 4b at the downstream side of the air flow is prevented whereby the deterioration of heat exchanging amount between the fin 4b at the downstream side of the air flow and the air flow can be prevented.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は空気調和機や冷凍機
器、自動車機器等の冷媒と空気等の流体間で熱の授受を
行うフィン付熱交換器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a finned heat exchanger for transferring heat between a refrigerant and a fluid such as air in an air conditioner, refrigeration equipment, automobile equipment, and the like.

【0002】[0002]

【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、フィン表面にスリ
ットやルーバーなどを設ける等の工夫により高効率化が
図られている。
2. Description of the Related Art In recent years, heat exchangers with fins have been required to be compact in terms of equipment design, and high efficiency has been achieved by providing slits and louvers on the fin surface.

【0003】従来のフィン付熱交換器は、特開昭61−
252494号公報に開示されている。
A conventional finned heat exchanger is disclosed in
No. 252494.

【0004】以下、図面を参照しながら上記従来のフィ
ン付熱交換器を説明する。図7は従来のフィン付熱交換
器の斜視図である。図7において、1は一定間隔で平行
に並べられたフィンで、2はフィン1を貫通し、内部を
流体が流動する伝熱管である。伝熱管2相互を連結する
ことにより、冷媒回路を構成している。図8は従来のフ
ィン付熱交換器の断面図であり、図9は図8におけるA
−A断面図である。図8と図9において、3はフィン1
上に設けられたスリット状の切り起こしである。
Hereinafter, the conventional finned heat exchanger will be described with reference to the drawings. FIG. 7 is a perspective view of a conventional finned heat exchanger. In FIG. 7, reference numeral 1 denotes fins arranged in parallel at regular intervals, and 2 denotes a heat transfer tube which penetrates the fin 1 and through which a fluid flows. A refrigerant circuit is formed by connecting the heat transfer tubes 2 to each other. FIG. 8 is a cross-sectional view of a conventional finned heat exchanger, and FIG.
It is -A sectional drawing. 8 and 9, reference numeral 3 denotes a fin 1
It is a slit-like cut-and-raised provided on the upper side.

【0005】以上のように構成されたフィン付熱交換器
について、以下その動作を説明する。
[0005] The operation of the finned heat exchanger configured as described above will be described below.

【0006】このフィン付熱交換器では、フィン1の間
を流れる気流と伝熱管2の管内を流れる冷媒との間で、
フィン1及び伝熱管2を介して熱交換が行なわれる。こ
の際、フィン1にはスリット状の切り起こし3が設けら
れており、この切り起こし3によって、フィン1間を流
れる気流の境界層を更新することで、気流とフィン1の
熱交換を促進し、その結果、気流と伝熱管内を流れる冷
媒との熱交換を促進している。
In this finned heat exchanger, the airflow flowing between the fins 1 and the refrigerant flowing in the heat transfer tubes 2 are
Heat exchange is performed via the fins 1 and the heat transfer tubes 2. At this time, the fin 1 is provided with a slit-shaped cut-and-raised portion 3, and the cut-and-raised portion 3 updates a boundary layer of an airflow flowing between the fins 1 to promote heat exchange between the airflow and the fin 1. As a result, heat exchange between the airflow and the refrigerant flowing in the heat transfer tube is promoted.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、上記従
来の構成では、暖房運転時の蒸発器として機能した場
合、冷媒の蒸発温度が低下したとき、気流上流のフィン
1aの表面に凝縮した空気中の水分は気流によりフィン
1を伝って、徐々に気流下流に流され、気流下流のフィ
ン1bに流入する。この凝縮水が、気流と気流下流のフ
ィン1bとの熱交換を阻害し、フィン付熱交換器の熱交
換量が低下するという欠点があった。
However, in the above-described conventional configuration, when functioning as an evaporator during a heating operation, when the evaporating temperature of the refrigerant decreases, the air in the air condensed on the surface of the fins 1a upstream of the airflow flows. Moisture travels along the fins 1 by the airflow, gradually flows downstream of the airflow, and flows into the fins 1b downstream of the airflow. This condensed water hinders heat exchange between the airflow and the fins 1b downstream of the airflow, and has the disadvantage that the heat exchange amount of the finned heat exchanger is reduced.

【0008】本発明は従来の課題を解決するもので、暖
房運転時の蒸発器として機能した場合、冷媒の蒸発温度
が低下したとき、気流下流での熱交換量の低下を防ぐこ
とにより、フィン付熱交換器の熱交換量を維持すること
を目的とする。
SUMMARY OF THE INVENTION The present invention solves the conventional problem. When the evaporator functions as an evaporator during a heating operation, when the evaporating temperature of the refrigerant is reduced, the amount of heat exchange downstream of the airflow is prevented from being reduced. The purpose is to maintain the heat exchange amount of the attached heat exchanger.

【0009】また、上記従来の構成では、暖房運転時の
蒸発器として機能した場合、冷媒の蒸発温度が低下した
とき、気流上流のフィン1aの表面に凝縮した水分は、
気流上流においても気流とフィン1の熱交換を阻害し、
フィン付熱交換器の熱交換量が低下するという欠点があ
った。
Further, in the above-described conventional configuration, when functioning as an evaporator during the heating operation, when the evaporation temperature of the refrigerant decreases, the water condensed on the surface of the fin 1a upstream of the air flow is
In the upstream of the airflow, it hinders heat exchange between the airflow and the fins 1,
There is a disadvantage that the heat exchange amount of the finned heat exchanger is reduced.

【0010】本発明の他の目的は、気流下流での熱交換
量の低下を防ぐとともに、気流上流での熱交換量の低下
を防ぐことにより、フィン付熱交換器の熱交換量を維持
することである。
Another object of the present invention is to maintain the heat exchange amount of the finned heat exchanger by preventing a decrease in the amount of heat exchange downstream of the airflow and preventing a decrease in the amount of heat exchange upstream of the airflow. That is.

【0011】さらに、上記従来の構成では、暖房運転時
の蒸発器として機能した場合、冷媒の蒸発温度が低下
し、冷媒の蒸発温度が0℃以下になると、気流上流のフ
ィン1の表面に凝縮した水分は、熱交換量が大きい気流
の境界層を更新する切り起こし3の前縁部で、運転開始
後すぐに多量の着霜を生じ、切り起こし3とベースのフ
ィン1との隙間が目詰まりを起こすため、通風抵抗が増
大し、気流下流での熱交換が可能であるにも関わらず暖
房運転を停止し、除霜運転を開始するため、頻繁に除霜
運転を行わざるを得なくなるという欠点があった。
Furthermore, in the above-described conventional configuration, when the evaporator functions as an evaporator during the heating operation, the evaporation temperature of the refrigerant decreases, and when the evaporation temperature of the refrigerant becomes 0 ° C. or less, the refrigerant condenses on the surface of the fin 1 upstream of the airflow. The generated moisture causes a large amount of frost immediately after the start of operation at the leading edge of the cut-and-raised portion 3 that renews the boundary layer of the airflow having a large heat exchange amount. In order to cause clogging, ventilation resistance increases, and although heat exchange can be performed downstream of the airflow, heating operation is stopped and defrosting operation is started, so frequent defrosting operations have to be performed. There was a disadvantage.

【0012】本発明のさらに他の目的は、フィン付熱交
換器の熱交換量の低下を防ぐとともに、気流上流での着
霜を抑制することにより、フィン付熱交換器の熱交換量
を低下させることなく、暖房運転時間の延長を図ること
である。
Still another object of the present invention is to reduce the amount of heat exchange of the finned heat exchanger by preventing the heat exchange amount of the finned heat exchanger from lowering and suppressing frost formation upstream of the airflow. It is intended to extend the heating operation time without causing the heating operation.

【0013】[0013]

【課題を解決するための手段】この目的を達成するため
に本発明は、フィンの伝熱管の列相互間に重力方向に連
続する排水溝を設けるものである。
In order to achieve this object, the present invention provides a gravitationally continuous drain groove between rows of heat transfer tubes of fins.

【0014】これにより、暖房運転時の蒸発器として機
能した場合、冷媒の蒸発温度が低下したとき、気流上流
のフィンの表面に凝縮した空気中の水分が気流下流へ流
入するのを防ぐことにより、気流下流のフィンの熱交換
量の低下を防ぎ、フィン付交換器の熱交換量を維持する
ことができる。
Thus, when the evaporator functions as an evaporator during the heating operation, when the evaporating temperature of the refrigerant decreases, the moisture in the air condensed on the surfaces of the fins upstream of the airflow is prevented from flowing into the downstream of the airflow. In addition, it is possible to prevent a decrease in the amount of heat exchange of the fins downstream of the airflow and maintain the amount of heat exchange of the finned exchanger.

【0015】また本発明は、フィンの伝熱管の列相互間
に重量方向に連続する排水溝を設けるとともに、気流上
流のフィン前縁から排水溝までのフィン表面に撥水性表
面処理を施したものである。
Further, the present invention is characterized in that a drain groove continuous in the weight direction is provided between the rows of heat transfer tubes of the fins, and the fin surface from the leading edge of the fin upstream of the airflow to the drain groove is subjected to a water-repellent surface treatment. It is.

【0016】これにより、暖房運転時の蒸発器として機
能した場合、冷媒の蒸発温度が低下したとき、気流上流
のフィンの表面に凝縮した空気中の水分が、気流下流へ
流入するのを伝熱管の列相互間の排水溝によって防ぐ。
また、気流上流のフィン前縁から排水溝までのフィン表
面に撥水性表面処理を施したため、この凝縮水が水滴と
なり、気流に流され易くすることにより、気流上流のフ
ィンの表面において、凝縮水が多量に、かつ速やかに排
水溝より排水される。これらにより、気流上流と下流と
もに熱交換量の低下を防ぎ、フィン付熱交換器の熱交換
量を維持することができる。
When the evaporator functions as an evaporator during a heating operation, when the evaporating temperature of the refrigerant decreases, the moisture in the air condensed on the surface of the fin upstream of the airflow flows into the downstream of the airflow. Prevented by inter-row drains.
In addition, since the fin surface from the leading edge of the fin upstream of the airflow to the drainage groove is subjected to a water-repellent surface treatment, this condensed water becomes water droplets and is easily flown into the airflow, so that the condensed water is condensed on the surface of the fin upstream of the airflow. In large quantities and quickly drained from drains. Thus, it is possible to prevent a decrease in the amount of heat exchange both upstream and downstream of the airflow, and to maintain the amount of heat exchange of the finned heat exchanger.

【0017】さらに本発明は、フィンの伝熱管の列相互
間の重量方向に連続する排水溝を設け、気流上流のフィ
ン前縁から排水溝までのフィン表面に撥水性表面処理を
施し、さらにフィン前縁から排水溝までの部分をフラッ
トにしたものである。
Further, the present invention provides a drain groove which is continuous in the weight direction between the rows of heat transfer tubes of the fins, and performs a water-repellent surface treatment on the fin surface from the leading edge of the fin upstream of the airflow to the drain groove. The part from the leading edge to the drain is flat.

【0018】これにより、暖房運転時の蒸発器として機
能した場合、冷媒の蒸発温度が低下したとき、気流上流
のフィンの表面に凝縮した空気中の水分が、気流下流へ
流入するのを伝熱管の列相互間の排水溝によって防ぐ。
また、気流上流のフィン前縁から排水溝までのフィン表
面に撥水性表面処理を施したため、この凝縮水が水滴と
なり、気流に流され易くなるため、気流上流のフィンの
表面において、凝縮水が多量に、かつ速やかに排水され
る。これらにより、気流上流と下流ともに熱交換量の低
下を防ぎ、フィン付熱交換器の熱交換量を維持すること
ができる。さらに冷媒の蒸発温度が低下し、冷媒の蒸発
温度が0℃以下になったとき、切り起こしとベースのフ
ィンとの隙間の目詰まりをなくし、暖房運転時間延長が
できる。
When the evaporator functions as an evaporator during the heating operation, when the evaporating temperature of the refrigerant decreases, the moisture in the air condensed on the surface of the fin upstream of the airflow flows into the downstream of the airflow. Prevented by inter-row drains.
In addition, since the fin surface from the leading edge of the fin upstream of the airflow to the drainage groove has been subjected to a water-repellent surface treatment, the condensed water becomes water droplets and is easily flown into the airflow. It is drained in large quantities and quickly. Thus, it is possible to prevent a decrease in the amount of heat exchange both upstream and downstream of the airflow, and to maintain the amount of heat exchange of the finned heat exchanger. Further, when the evaporating temperature of the refrigerant decreases and the evaporating temperature of the refrigerant becomes 0 ° C. or less, clogging of the gap between the cut-and-raised portion and the fin of the base can be eliminated, and the heating operation time can be extended.

【0019】[0019]

【発明の実施の形態】本発明の請求項1に記載の発明
は、一定間隔で平行に並べられ、相互間を気体が流動す
るフィンと、フィンを貫通し、気流方向に複数列配置さ
れた伝熱管とから構成され、フィンの伝熱管の列相互間
に重量方向に連続する排水溝を設けたフィン付熱交換器
であり、フィンの伝熱管の列相互間に重力方向に連続す
る排水溝を設けることにより、気流上流のフィンの表面
に凝縮した空気中の水分が気流下流へ流入するのを防
ぎ、気流下流のフィンの熱交換量の低下を防ぎ、フィン
付熱交換器の熱交換量を維持することができるという作
用を有する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention according to claim 1 of the present invention is arranged in parallel at regular intervals, and fins in which gas flows between the fins and a plurality of fins penetrating the fins and arranged in the gas flow direction. A heat exchanger with fins comprising a heat transfer tube and a drainage groove continuous in the weight direction between rows of heat transfer tubes of fins, and a drainage groove continuous in the direction of gravity between the rows of heat transfer tubes of fins. Prevents the water in the air condensed on the surface of the fins upstream of the airflow from flowing into the downstream of the airflow, prevents the heat exchange amount of the fins downstream of the airflow from decreasing, and reduces the heat exchange amount of the finned heat exchanger. Can be maintained.

【0020】本発明の請求項2に記載の発明は、気流上
流のフィン前縁から排水溝までのフィン表面に撥水性表
面処理を施した請求項1に記載のフィン付熱交換器であ
り、フィンの伝熱管の列相互間に重力方向に連続する排
水溝を設け、かつ気流上流のフィン前縁から排水溝まで
のフィン表面に撥水性表面処理を施すことで、気流上流
のフィンの表面に凝縮した空気中の水分が、気流下流へ
流入するのを防ぐとともに、この凝縮水が水滴となり、
気流に流され易くすることにより、気流上流のフィンの
表面において、凝縮した水分が速やかに排水溝により排
水され、気流上流と下流ともに熱交換量の低下を防ぎ、
フィン付熱交換器の熱交換量を維持することができると
いう作用を有する。
According to a second aspect of the present invention, there is provided the finned heat exchanger according to the first aspect, wherein the fin surface from the leading edge of the fin upstream of the airflow to the drain is subjected to a water-repellent surface treatment. By providing a drainage groove that is continuous in the direction of gravity between the rows of heat transfer tubes of the fins, and applying a water-repellent surface treatment to the fin surface from the leading edge of the fin upstream of the airflow to the drainage groove, the surface of the fins upstream of the airflow While preventing the water in the condensed air from flowing downstream of the airflow, this condensed water becomes water droplets,
By facilitating the flow in the air flow, the condensed water is quickly drained by the drainage grooves on the surface of the fins upstream of the air flow, preventing a decrease in the amount of heat exchange both upstream and downstream of the air flow,
This has the effect that the heat exchange amount of the finned heat exchanger can be maintained.

【0021】本発明の請求項3に記載の発明は、気流上
流のフィン前縁から排水溝までの部分をフラットにした
請求項2記載のフィン付熱交換器であり、フィンの伝熱
管の列相互間に重力方向に連続する排水溝を設け、かつ
気流上流のフィン前縁から排水溝までのフィン表面に撥
水性表面処理を施し、かつ気流上流のフィン前縁から排
水溝までの部分をフラットにすることにより、切り起こ
しとベースのフィンとの隙間の目詰まりをなくし、暖房
運転時間の延長ができるという作用を有する。また、気
流上流のフィンの表面に凝縮した空気中の水分が、気流
下流へ流入するのを防ぐとともに、気流上流のフィンの
表面に凝縮した空気中の水分が水滴となり、気流に流さ
れ易くなるため、気流上流のフィンの表面において、凝
縮した水分が速やかに排水され、気流上流と下流ともに
熱交換量の低下を防ぎ、フィン付熱交換器の熱交換量を
維持することができるという作用を有する。
According to a third aspect of the present invention, there is provided the heat exchanger with fins according to the second aspect, wherein a portion from the leading edge of the fin upstream of the airflow to the drainage groove is flattened. Provide drainage grooves that are continuous in the direction of gravity between each other, apply a water-repellent surface treatment to the fin surface from the fin leading edge to the drainage groove upstream of the airflow, and flatten the part from the fin leading edge to the drainage groove upstream of the airflow. By doing so, clogging of the gap between the cut-and-raised and the fins of the base is eliminated, and the heating operation time can be extended. In addition, while preventing the moisture in the air condensed on the surface of the fin upstream of the airflow from flowing into the downstream of the airflow, the moisture in the air condensed on the surface of the fin upstream of the airflow becomes a water droplet and is easily flowed into the airflow. Therefore, on the surface of the fins upstream of the airflow, the condensed water is quickly drained, preventing a decrease in the amount of heat exchange both upstream and downstream of the airflow, and maintaining the heat exchange amount of the finned heat exchanger. Have.

【0022】[0022]

【実施例】以下、本発明によるフィン付熱交換器の実施
例について、図面を参照しながら説明する。なお、従来
と同一構成については、同一付号を付して詳細な説明を
省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a finned heat exchanger according to the present invention will be described below with reference to the drawings. Note that the same components as those in the related art are denoted by the same reference numerals, and detailed description is omitted.

【0023】(実施例1)図1は本発明の実施例1によ
るフィン付熱交換器の断面図であり、図2は図1のB−
B断面図である。
(Embodiment 1) FIG. 1 is a sectional view of a finned heat exchanger according to Embodiment 1 of the present invention, and FIG.
It is B sectional drawing.

【0024】図において2は伝熱管であり、従来の構成
と同じものである。4は一定間隔で平行に並べられたフ
ィンで、5はフィン4の伝熱管2の列相互間に力量方向
に連続して続けられた排水溝である。
In the figure, reference numeral 2 denotes a heat transfer tube, which is the same as a conventional structure. Reference numeral 4 denotes fins arranged in parallel at regular intervals, and reference numeral 5 denotes a drainage groove which is continuously provided between the rows of the heat transfer tubes 2 of the fins 4 in the force direction.

【0025】以上のように構成されたフィン付熱交換器
について、以下暖房運転時の蒸発器として機能した場合
の動作を説明する。
The operation of the finned heat exchanger configured as described above when it functions as an evaporator during a heating operation will be described below.

【0026】このフィン付熱交換器では、フィン4の間
を流れる気流と伝熱管2の管内を流れる冷媒との間で、
フィン4及び伝熱管2を介して熱交換が行なわれる。こ
の際、冷媒の蒸発温度が低下すると、気流上流のフィン
4aの表面に空気中の水分が凝縮する。
In this heat exchanger with fins, the airflow flowing between the fins 4 and the refrigerant flowing in the heat transfer tubes 2
Heat exchange is performed via the fins 4 and the heat transfer tubes 2. At this time, when the evaporation temperature of the refrigerant decreases, moisture in the air condenses on the surface of the fin 4a upstream of the airflow.

【0027】この凝縮水は、気流により、フィン4aに
沿って気流下流へ流され、フィン4の伝熱管2の列相互
管の力量方向に連続する排水溝5に流入する。排水溝5
に流入した凝縮水は、重力方向に排水溝5に沿って排出
される。
The condensed water is caused to flow downstream of the air flow along the fins 4a by the air flow, and flows into the drain grooves 5 continuous in the direction of the force of the rows of the heat transfer tubes 2 of the fins 4. Drain 5
Is discharged along the drain 5 in the direction of gravity.

【0028】このため、気流とフィン4との熱交換を阻
害する気流上流のフィン4aで凝縮した凝縮水が、気流
下流のフィン4bへ流入するのを防ぎ、気流下流のフィ
ン4bと気流の熱交換量の低下を防ぎ、フィン付熱交換
器の熱交換量を維持することができる。
For this reason, the condensed water condensed by the fins 4a upstream of the airflow, which inhibits the heat exchange between the airflow and the fins 4, is prevented from flowing into the fins 4b downstream of the airflow. It is possible to prevent a decrease in the exchange amount and maintain the heat exchange amount of the finned heat exchanger.

【0029】以上のように本実施例のフィン付熱交換器
は、フィン4の伝熱管2の列相互間に重力方向に連続す
る排水溝5を設けることにより、気流上流のフィン4a
の表面に凝縮した空気中の水分が気流下流へ流入するの
を防ぎ、気流下流のフィン4bの熱交換量の低下を防
ぎ、フィン付熱交換器の熱交換量を維持することができ
る。
As described above, in the heat exchanger with fins of the present embodiment, by providing the drainage grooves 5 continuous in the direction of gravity between the rows of the heat transfer tubes 2 of the fins 4, the fins 4a on the upstream of the air flow are provided.
It is possible to prevent the moisture in the air condensed on the surface from flowing into the downstream of the air flow, prevent the heat exchange amount of the fins 4b downstream of the air flow from decreasing, and maintain the heat exchange amount of the finned heat exchanger.

【0030】(実施例2)図3は本発明の実施例2によ
るフィン付熱交換器の断面図であり、図4は図3のC−
C断面図である。
(Embodiment 2) FIG. 3 is a sectional view of a finned heat exchanger according to Embodiment 2 of the present invention, and FIG.
It is C sectional drawing.

【0031】同図において、2は伝熱管であり、従来の
構成と同じものである。6は一定間隔で平行に並べられ
たフィンで、7はフィン6の伝熱管2の列相互間に重力
方向に連続する排水溝である。8はフィン6の前縁から
排水溝7までの間の気流上流のフィン6aの表面に施さ
れた撥水性表面処理である。
In FIG. 1, reference numeral 2 denotes a heat transfer tube, which is the same as a conventional structure. Numeral 6 denotes fins arranged in parallel at regular intervals, and numeral 7 denotes a drainage groove continuous between rows of the heat transfer tubes 2 of the fins 6 in the direction of gravity. Reference numeral 8 denotes a water-repellent surface treatment applied to the surface of the fin 6a upstream of the airflow between the leading edge of the fin 6 and the drain groove 7.

【0032】以上のように構成されたフィン付熱交換器
について、以下暖房運転時の蒸発器として機能した場合
の動作を説明する。
The operation of the finned heat exchanger configured as described above when it functions as an evaporator during a heating operation will be described below.

【0033】このフィン付熱交換器では、フィン6の間
を流れる気流と伝熱管2の管内を流れる冷媒との間で、
フィン6及び伝熱管2を介して熱交換が行なわれる。こ
の際、冷媒の蒸発温度が低下すると、気流上流のフィン
6aの表面に空気中の水分が凝縮する。気流上流のフィ
ン6aには撥水性表面処理が施されているため、この凝
縮水は水滴となり、気流に流されやすくなる。このた
め、凝縮水は気流により排水溝7へ多量にかつ速やかに
導かれ、排水溝7によって重力方向に排出される。
In this heat exchanger with fins, the airflow flowing between the fins 6 and the refrigerant flowing in the heat transfer tubes 2
Heat exchange is performed via the fins 6 and the heat transfer tubes 2. At this time, when the evaporation temperature of the refrigerant decreases, moisture in the air condenses on the surface of the fin 6a upstream of the airflow. Since the water repellent surface treatment is applied to the fins 6a on the upstream side of the airflow, the condensed water becomes water droplets and is easily flowed into the airflow. Therefore, a large amount of the condensed water is guided to the drain 7 by the airflow, and is quickly discharged by the drain 7 in the direction of gravity.

【0034】これにより、気流上流のフィン6aの表面
と気流の熱交換を阻害する凝縮水が、多量にかつ速やか
に排出されることと、気流下流のフィン6bへの流入を
防ぐことにより、気流上流のフィン6aと気流下流のフ
ィン6bとの両方で気流との熱交換量の低下を防ぎ、フ
ィン付熱交換器の熱交換量を維持することができる。
Thus, a large amount of condensed water, which inhibits the heat exchange between the surface of the fin 6a upstream of the air flow and the air flow, is quickly discharged, and the flow of the condensed water into the fin 6b downstream of the air flow is prevented. Both the upstream fin 6a and the fin 6b downstream of the airflow can prevent a decrease in the amount of heat exchange with the airflow, and can maintain the heat exchange amount of the finned heat exchanger.

【0035】以上のように本実施例のフィン付熱交換器
は、フィン6の伝熱管2の列相互間に重力方向に連続す
る排水溝7を設け、かつ気流上流のフィン6aの前縁か
ら排水溝7までのフィン6a表面に撥水性表面処理8を
施したことにより、気流上流のフィン6aの表面に凝縮
した空気中の水分が、気流下流へ流入するのを防ぐとと
もに、この凝縮水が水滴となり、気流に流され易くする
ことにより、気流上流のフィン6aの表面において、凝
縮した水分が多量にかつ速やかに排水溝7により排水さ
れ、気流上流のフィン6aと気流下流のフィン6bとの
両方で熱交換量の低下を防ぎ、フィン付熱交換器の熱交
換量を維持することができる。
As described above, in the heat exchanger with fins of the present embodiment, the drain grooves 7 continuous in the direction of gravity are provided between the rows of the heat transfer tubes 2 of the fins 6, and the fins 6a are located upstream of the airflow from the front edge. By performing the water-repellent surface treatment 8 on the surface of the fin 6a up to the drain groove 7, the water in the air condensed on the surface of the fin 6a upstream of the air flow is prevented from flowing into the downstream of the air flow, and the condensed water is prevented from flowing. A large amount of condensed water is rapidly and rapidly drained by the drain groove 7 on the surface of the fin 6a upstream of the air flow by making it easy to be formed into a water droplet and flown to the air flow, so that the fin 6a upstream of the air flow and the fin 6b downstream of the air flow are condensed. In both cases, a decrease in the amount of heat exchange can be prevented, and the amount of heat exchange of the finned heat exchanger can be maintained.

【0036】(実施例3)図5は本発明の実施例3によ
るフィン付熱交換器の断面図であり、図6は図5のD−
D断面図である。
(Embodiment 3) FIG. 5 is a sectional view of a finned heat exchanger according to Embodiment 3 of the present invention, and FIG.
It is D sectional drawing.

【0037】同図において、2は伝熱管であり、従来の
構成と同じものである。9は一定間隔で平行に並べられ
たフィンで、10はフィン9の伝熱管2の列相互間の重
力方向に連続する排水溝である。11はフィン9の前縁
から排水溝10までの間の気流上流のフィン9aの表面
に施された撥水性表面処理である。また気流上流のフィ
ン9aは切り起こし等が無くフラットになっている。
In the figure, reference numeral 2 denotes a heat transfer tube, which is the same as a conventional structure. Reference numeral 9 denotes fins arranged in parallel at regular intervals, and reference numeral 10 denotes a drainage groove continuous between rows of the heat transfer tubes 2 of the fins 9 in the direction of gravity. Numeral 11 denotes a water-repellent surface treatment applied to the surface of the fin 9a upstream of the airflow between the leading edge of the fin 9 and the drain groove 10. Further, the fin 9a upstream of the airflow is flat without being cut or raised.

【0038】以上のように構成されたフィン付熱交換器
について、以下暖房運転時の蒸発器として機能した場合
の動作を説明する。
The operation of the finned heat exchanger configured as described above when it functions as an evaporator during a heating operation will be described below.

【0039】このフィン付熱交換器では、フィン9の間
を流れる気流と伝熱管2の管内を流れる冷媒との間で、
フィン9及び伝熱管2を介して熱交換が行なわれる。こ
の際、冷媒の蒸発温度が低下すると、気流上流のフィン
9aの表面に空気中の水分が凝縮する。
In this heat exchanger with fins, the airflow flowing between the fins 9 and the refrigerant flowing in the heat transfer tubes 2
Heat exchange is performed via the fins 9 and the heat transfer tubes 2. At this time, when the evaporation temperature of the refrigerant decreases, moisture in the air condenses on the surface of the fin 9a upstream of the airflow.

【0040】気流上流のフィン9aの表面には撥水性表
面処理11が施されているため、この凝縮水は水滴とな
り、かつ気流上流のフィン9aは抵抗となるスリット状
の切り起こしがなくフラットになっているため、非常に
気流に流されやすくなる。このため、凝縮水は気流によ
り、排水溝10へ多量に、かつ速やかに導かれ、排水溝
10によって重力方向に排出される。
Since the water repellent surface treatment 11 is applied to the surface of the fin 9a on the upstream side of the airflow, this condensed water becomes water droplets, and the fin 9a on the upstream side of the airflow is flat without any slit-shaped cut-and-raised portions. It is very easy to be swept away by the air current. For this reason, a large amount of the condensed water is guided to the drain 10 by the air current and quickly, and is discharged in the direction of gravity by the drain 10.

【0041】これにより、気流上流のフィン9aの表面
からフィン9aと気流の熱交換を阻害する凝縮水が、多
量にかつ速やかに排出されることと、気流下流のフィン
9bへの流入を防ぐことにより、フィン9と気流との熱
交換量の低下を防ぎ、フィン付熱交換器の熱交換量を維
持することができる。
Thus, a large amount of condensed water that inhibits the heat exchange between the fin 9a and the air flow is quickly and quickly discharged from the surface of the fin 9a upstream of the air flow, and the flow of the condensed water into the fin 9b downstream of the air flow is prevented. Accordingly, it is possible to prevent a decrease in the amount of heat exchange between the fins 9 and the airflow, and to maintain the amount of heat exchange of the finned heat exchanger.

【0042】さらに冷媒の蒸発温度が低下し、冷媒の蒸
発温度が0℃以下になったとき、気流上流のフィン9a
にスリット状の切り起こしがなくフラットなため、従来
例のように切り起こしとベースのフィン9との隙間が目
詰まりを起こすことはなく、通風抵抗の増大を抑えるこ
とができ、暖房運転時間を延長することができる。
When the evaporating temperature of the refrigerant further decreases and the evaporating temperature of the refrigerant becomes 0 ° C. or less, the fins 9a on the upstream of the airflow flow.
Since there is no slit-like cut-and-raised portion, the gap between the cut-and-raised portion and the base fin 9 does not become clogged as in the conventional example, the increase in ventilation resistance can be suppressed, and the heating operation time can be reduced. Can be extended.

【0043】以上のように本実施例のフィン付熱交換器
は、フィン9の伝熱管2の列相互間に重力方向に連続す
る排水溝10を設け、かつ気流上流のフィン9a前縁か
ら排水溝10までのフィン9a表面に撥水性表面処理1
1を施し、かつ気流上流のフィン9a前縁から排水溝1
0までの部分をフラットにすることにより、切り起こし
とベースのフィン9との隙間の目詰まりをなくし、暖房
運転時間の延長ができる。
As described above, in the heat exchanger with fins of the present embodiment, the drain grooves 10 continuous in the direction of gravity are provided between the rows of the heat transfer tubes 2 of the fins 9, and the drains are discharged from the front edge of the fin 9a upstream of the air flow. Water-repellent surface treatment 1 on fin 9a surface up to groove 10
1 and drain grooves 1 from the leading edge of the fin 9a upstream of the airflow.
By flattening the portion up to 0, clogging of the gap between the cut-and-raised portion and the fin 9 of the base can be eliminated, and the heating operation time can be extended.

【0044】また、気流上流のフィン9aの表面に凝縮
した空気中の水分が、気流下流のフィン9bへ流入する
のを防ぐとともに、気流上流のフィン9aの表面に凝縮
した空気中の水分が水滴となり、気流に流され易くなる
ため、気流上流のフィン9aの表面において、排水溝1
0により凝縮した水分が多量にかつ速やかに排水され、
気流上流のフィン9aと気流下流のフィン9bとの両方
で熱交換量の低下を防ぎ、フィン付熱交換器の熱交換量
を維持することができる。
In addition, the moisture in the air condensed on the surface of the fin 9a upstream of the air flow is prevented from flowing into the fin 9b downstream of the air flow, and the moisture in the air condensed on the surface of the fin 9a upstream of the air flow is removed by water droplets. Therefore, the drainage groove 1 is formed on the surface of the fin 9a upstream of the airflow.
A large amount of water condensed by 0 is quickly and quickly drained,
Both the fin 9a upstream of the airflow and the fin 9b downstream of the airflow can prevent a decrease in the amount of heat exchange, and can maintain the amount of heat exchange of the finned heat exchanger.

【0045】[0045]

【発明の効果】以上説明したように本発明は、一定間隔
で平行に並べられ、相互間を気体が流動するフィンと、
フィンを貫通し、気流方向に複数列配置された伝熱管と
から構成され、フィンの伝熱管の列相互間の重力方向に
連続する排水溝を設けたので、気流下流のフィンの熱交
換量の低下を防ぎ、フィン付熱交換器の熱交換量を維持
することができる。
As described above, according to the present invention, fins are arranged in parallel at regular intervals and gas flows between them.
The fins penetrate through the fins and are arranged in a plurality of rows in the airflow direction.The drainage grooves are continuous in the direction of gravity between the rows of the fins. It is possible to prevent the heat exchanger from lowering and maintain the heat exchange amount of the finned heat exchanger.

【0046】また、気流上流のフィン前縁から排水溝ま
でのフィン表面に撥水性表面処理を施したので、気流上
流と下流ともに熱交換量の低下を防ぎ、フィン付熱交換
器の熱交換量を維持することができる。
Further, since the fin surface from the leading edge of the fin upstream of the airflow to the drainage groove is subjected to a water-repellent surface treatment, the amount of heat exchange is prevented from decreasing both upstream and downstream of the airflow, and the heat exchange amount of the finned heat exchanger is reduced. Can be maintained.

【0047】さらに、気流上流のフィン前縁から排水溝
までの部分をフラットにしたので、気流下流での熱交換
量の低下を防ぐとともに、気流上流での着霜を抑制する
ことにより、フィン付熱交換器の熱交換量を低下させる
ことなく、暖房運転時間の延長を図ることができる。
Further, since the portion from the leading edge of the fin upstream of the airflow to the drainage groove is made flat, it is possible to prevent a decrease in the amount of heat exchange downstream of the airflow and to suppress frost formation upstream of the airflow, thereby providing a fin. The heating operation time can be extended without reducing the heat exchange amount of the heat exchanger.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明によるフィン付熱交換器の実施例1の断
面図
FIG. 1 is a sectional view of a finned heat exchanger according to a first embodiment of the present invention.

【図2】図1のB−B断面図FIG. 2 is a sectional view taken along line BB of FIG. 1;

【図3】本発明によるフィン付熱交換器の実施例2の断
面図
FIG. 3 is a sectional view of Embodiment 2 of the finned heat exchanger according to the present invention.

【図4】図3のC−C断面図FIG. 4 is a sectional view taken along the line CC of FIG. 3;

【図5】本発明によるフィン付熱交換器の実施例3の断
面図
FIG. 5 is a sectional view of a finned heat exchanger according to a third embodiment of the present invention.

【図6】図5のD−D断面図FIG. 6 is a sectional view taken along line DD of FIG. 5;

【図7】従来のフィン付熱交換器の斜視図FIG. 7 is a perspective view of a conventional finned heat exchanger.

【図8】従来のフィン付熱交換器の断面図FIG. 8 is a sectional view of a conventional finned heat exchanger.

【図9】図8のA−A断面図9 is a sectional view taken along line AA of FIG. 8;

【符号の説明】[Explanation of symbols]

2 伝熱管 4,4a,4b フィン 5 排水溝 6,6a,6b フィン 7 排水溝 8 撥水性表面処理 9,9a,9b フィン 10 排水溝 11 撥水性表面処理 2 Heat transfer tube 4, 4a, 4b fin 5 Drain groove 6, 6a, 6b fin 7 Drain groove 8 Water repellent surface treatment 9, 9a, 9b Fin 10 Drain groove 11 Water repellent surface treatment

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 一定間隔で平行に並べられ、相互間を気
体が流動するフィンと、前記フィンを貫通し、気流方向
に複数列配置された伝熱管とから構成され、前記フィン
の前記伝熱管の列相互間に重力方向に連続する排水溝を
設けたフィン付熱交換器。
1. A fin which is arranged in parallel at regular intervals and through which a gas flows, and a plurality of heat transfer tubes penetrating through the fins and arranged in a plurality of rows in a gas flow direction, wherein the heat transfer tubes of the fins are provided. Heat exchanger with fins provided with drainage grooves continuous in the direction of gravity between the rows of.
【請求項2】 気流上流のフィン前縁から排水溝までの
フィン表面に撥水性表面処理を施した請求項1に記載の
フィン付熱交換器。
2. The finned heat exchanger according to claim 1, wherein the fin surface from the leading edge of the fin upstream of the airflow to the drainage groove is subjected to a water-repellent surface treatment.
【請求項3】 気流上流のフィン前縁から排水溝までの
部分をフラットにした請求項2に記載のフィン付熱交換
器。
3. The heat exchanger with fins according to claim 2, wherein a portion from the leading edge of the fin upstream of the airflow to the drain groove is flattened.
JP5497A 1997-01-06 1997-01-06 Finned heat exchanger Pending JPH10197183A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5497A JPH10197183A (en) 1997-01-06 1997-01-06 Finned heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5497A JPH10197183A (en) 1997-01-06 1997-01-06 Finned heat exchanger

Publications (1)

Publication Number Publication Date
JPH10197183A true JPH10197183A (en) 1998-07-31

Family

ID=11463527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5497A Pending JPH10197183A (en) 1997-01-06 1997-01-06 Finned heat exchanger

Country Status (1)

Country Link
JP (1) JPH10197183A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008514897A (en) * 2004-09-30 2008-05-08 ベール ゲーエムベーハー ウント コー カーゲー Method of cooling a heat transfer body and supercharged air

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008514897A (en) * 2004-09-30 2008-05-08 ベール ゲーエムベーハー ウント コー カーゲー Method of cooling a heat transfer body and supercharged air

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