JPH05164481A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH05164481A
JPH05164481A JP33323091A JP33323091A JPH05164481A JP H05164481 A JPH05164481 A JP H05164481A JP 33323091 A JP33323091 A JP 33323091A JP 33323091 A JP33323091 A JP 33323091A JP H05164481 A JPH05164481 A JP H05164481A
Authority
JP
Japan
Prior art keywords
fins
heat exchanger
fin
heat transfer
corrugated
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
JP33323091A
Other languages
Japanese (ja)
Inventor
Koji Terada
浩二 寺田
Toshio Hatada
敏夫 畑田
Takeo Tanaka
武雄 田中
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP33323091A priority Critical patent/JPH05164481A/en
Publication of JPH05164481A publication Critical patent/JPH05164481A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To enhance corrosion resistant and heat transfer properties by providing a corrugated fin between fins, since it is difficult to expect an improvement of a cross fin tube type heat exchanger adopted in the field of air conditioner heat exchangers due to their corrosion problems. CONSTITUTION:Corrugated fins 4 are mounted between a large number of plate fins 1 having a louver part laid out in parallel to each other with a span so as to reduce the load of the louver part in the plate fins 1 and increase their heat transfer areas. This construction makes it possible to enhance their corrosion resistant and heat transfer properties so that the heat exchangers may be used for a long time in a stabilized manner.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、空気調和装置,冷凍機
あるいは除湿機等、空気との熱交換を行うのに適した熱
交換器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger suitable for exchanging heat with air, such as an air conditioner, a refrigerator or a dehumidifier.

【0002】[0002]

【従来の技術】従来の技術をクロスフィンチューブ式熱
交換器を引用して説明する。従来のクロスフィンチュー
ブ式熱交換器は、適宜面積を有するアルミ板等で形成さ
れたフィンに銅製伝熱管を挿入する複数個の孔が開口さ
れ、このフィンは数mmピッチで多数個並設され、この並
設フィンに複数本の伝熱管がこの孔を貫通して配設され
拡管時等の手段により伝熱管とフィンを密着して形成
し、伝熱管端部をU字形のベント管で接続し、蛇行状に
延長した適数本の伝熱通路を形成している。フィンの上
面にはルーバと呼ぶ多数の切り起しを設け新鮮な空気と
できるだけ多く触れさせることで高性能化を図ってい
る。また、一般にフィン表面には表面処理剤がほどこさ
れ、水切り性及び耐食性を考慮してあるが、クロスフィ
ンチューブ式熱交換器はアルミ性フィンと銅製伝熱管の
電位差の大きな異種金属で接触しているため、フィンカ
ラー部に腐食が生じ、フィンの脱落へと発展していく。
また、特開平1−208698 号公報,特開平2−37293号公報
によるフィンはルーバ占有面積を増加させて、熱伝達率
を向上させるというもので、ルーバ切り起し部からの腐
食を考慮した例はみあたらない。このように、熱交換器
の高性能化にともない、フィンの薄板化とルーバの微細
化のため、表面処理がなされてない切り起し断面からの
腐食が熱交換器の耐久性にかかわるという問題が生じて
いる。しかも、今後、熱交換器の高性能化を図る上で、
さらにフィンが微細化すると、耐食性という面から従来
のクロスフィンチューブ式熱交換器では高性能化が困難
となってきていることを示している。
2. Description of the Related Art A conventional technique will be described with reference to a cross fin tube type heat exchanger. In the conventional cross fin tube type heat exchanger, a plurality of holes for inserting a copper heat transfer tube are opened in a fin formed of an aluminum plate or the like having an appropriate area, and the fins are arranged in parallel at a pitch of several mm. , A plurality of heat transfer tubes are arranged in this parallel fin so as to pass through this hole, the heat transfer tube and the fin are formed in close contact with each other by means such as expansion, and the end of the heat transfer tube is connected by a U-shaped vent tube. However, a suitable number of heat transfer passages extending in a meandering shape are formed. A large number of louvers, called louvers, are provided on the upper surface of the fins to improve the performance by exposing the fins to fresh air as much as possible. In general, the fin surface is treated with a surface treatment agent to consider drainage and corrosion resistance.However, in the cross fin tube type heat exchanger, aluminum fins and copper heat transfer tubes are contacted with different metals with large potential difference. As a result, the fin collar is corroded and the fins fall off.
Further, the fins disclosed in JP-A-1-208698 and JP-A-2-37293 increase the louver occupying area to improve the heat transfer coefficient. It doesn't hit. In this way, as the performance of heat exchangers has improved, the fins have become thinner and the louvers have become finer, so corrosion from the cut-and-raised cross section that has not been surface-treated affects the durability of the heat exchanger. Is occurring. Moreover, in order to improve the performance of the heat exchanger in the future,
Further, it is shown that as the fins become finer, it is becoming difficult to improve the performance of the conventional cross fin tube type heat exchanger in terms of corrosion resistance.

【0003】[0003]

【発明が解決しようとする課題】上記従来技術は、クロ
スフィンチューブ式熱交換器の腐食では、銅伝熱管とフ
ィンにおけるスリットつけ根間の距離を十分とることに
よって、腐食に際してのフィン脱落までの寿命を長くし
て対処してきたが、微細化したルーバの腐食に関しては
考慮されておらず、近年、熱交換器の小形・軽量化に伴
う高性能化が求められる点において、フィンの薄板化及
びルーバの微細化による腐食が問題となってきている。
従来、熱交換器は腐食に備えてフィンに表面処理剤を施
しているが、プレス成形で複数のルーバを切り起すため
表面処理剤がなされてない切り起し断面が生じてくる。
ルーバの微細化に伴いフィンの切り起し断面の面積が増
加し、フィンの耐食性に影響を及ぼすようになり、高性
能化への障害となっている。
In the above-mentioned prior art, in the corrosion of the cross-fin tube type heat exchanger, by ensuring a sufficient distance between the copper heat transfer tube and the slit root of the fin, the life until the fin falls off during the corrosion. However, in consideration of the corrosion of the miniaturized louvers, and in recent years, the heat exchangers are required to have higher performance as they become smaller and lighter. Corrosion due to miniaturization has become a problem.
Conventionally, in heat exchangers, fins are provided with a surface treatment agent in preparation for corrosion, but since a plurality of louvers are cut and raised by press molding, a cut and raised cross section without the surface treatment agent is produced.
With the miniaturization of the louver, the area of the cut and raised cross section of the fin increases, which affects the corrosion resistance of the fin, which is an obstacle to higher performance.

【0004】本発明の目的は、プレートフィン間にコル
ゲートフィンを備えることにより、プレートフィンにお
けるルーバの負荷を少なくしてやり、フィンの耐食性を
向上させ、熱交換器の高性能化を達成することである。
An object of the present invention is to provide a corrugated fin between plate fins to reduce the load of the louvers on the plate fins, improve the corrosion resistance of the fins, and achieve high performance of the heat exchanger. ..

【0005】[0005]

【課題を解決するための手段】上記目的は、流体の流れ
を剪断する方向にプレートフィンを流れ方向と交差する
方向に積層し、プレートフィンを貫通する複数の伝熱管
を備えた熱交換器において、伝熱管をはさんで流れ方向
上流部と下流部にコルゲートフィンを備えることによっ
て達成される。
SUMMARY OF THE INVENTION The above object is to provide a heat exchanger having a plurality of heat transfer tubes which are formed by stacking plate fins in a direction intersecting the flow direction in a direction of shearing a fluid flow and penetrating the plate fins. This is achieved by providing corrugated fins in the upstream and downstream portions of the heat transfer tube in the flow direction.

【0006】[0006]

【作用】プレートフィン間にコルゲートフィンを備える
ことにより、プレートフィンにおけるルーバの数を減ら
すことができるため、フィンの耐食性が向上するととも
に、拡管時など製造過程におけるフィンの変形からくる
性能低下への影響を防ぐことができる。
By providing the corrugated fins between the plate fins, the number of louvers in the plate fins can be reduced, so that the corrosion resistance of the fins is improved and the performance is deteriorated due to the deformation of the fins during the manufacturing process such as pipe expansion. The impact can be prevented.

【0007】[0007]

【実施例】本発明の実施例を図面をもとに説明する。図
1は、本発明の一実施例を示すフィンを積層した熱交換
器の一部で、図2は、熱交換器に供せられるプレートフ
ィンの平面図、図3は、熱交換器に供せられるコルゲー
トフィンの斜視図である。図2において、1はプレート
フィンの一部を示し、2はルーバ部、3は伝熱管挿入孔
を示す。また、図1において、4は図3で示すコルゲー
トフィンである。従来のクロスフィンチューブ式熱交換
器は一般に互いに間隔をおいて平行に並べた多数のプレ
ートフィンと、これらフィンを貫通する複数の伝熱管と
で構成されるが、本実施例は、このプレートフィン間に
伝熱管を境にして、流体の流れる方向の上流部と下流部
にコルゲートフィンを備えたものといえる。図2は積層
されたプレートフィンの一部を示しておりルーバ部は、
熱交換器の側面で見て伝熱管の投影断面積内で突出して
いる。フィンチューブ式熱交換器では、ルーバの変形が
高性能化を妨げる一要因でありルーバの変形はプレス加
工によるルーバ形成時及び、フィンと伝熱管を密着する
拡管時に生じ、フィン両端部で局所的に変形が大きくな
ることが判明している。また、高性能化を進める上で、
ルーバが微細化になり、それによって表面処理がなされ
てないルーバの切り起し断面の面積が増加し、フィンの
腐食の面から熱交換器の高性能化に限界がきている。こ
の理由から、各プレートフィン間に、コルゲートフィン
を備えることによって、プレートフィンにおけるルーバ
の数を減らしてルーバの負荷を少なくし、ルーバ部の耐
食性を向上させることができる。さらに、熱交換器全体
の剛性が増し、拡管時におけるフィンの変形を小さくす
ることができる。これによって、フィン変形による伝熱
性能の低下を防ぐとともに、コルゲートフィンに相当す
る伝熱面積が増加するため伝熱性能を向上させることが
できる。
Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a part of a heat exchanger in which fins according to an embodiment of the present invention are stacked, FIG. 2 is a plan view of plate fins used in the heat exchanger, and FIG. 3 is used in the heat exchanger. It is a perspective view of the corrugated fin which is put. In FIG. 2, 1 is a part of the plate fin, 2 is a louver portion, and 3 is a heat transfer tube insertion hole. Further, in FIG. 1, 4 is a corrugated fin shown in FIG. A conventional cross fin tube type heat exchanger is generally composed of a large number of plate fins arranged in parallel at intervals, and a plurality of heat transfer tubes penetrating the fins. It can be said that corrugated fins are provided on the upstream side and the downstream side in the fluid flow direction with the heat transfer tube as a boundary. FIG. 2 shows a part of the plate fins stacked, and the louver part is
It projects within the projected cross-sectional area of the heat transfer tube when viewed from the side of the heat exchanger. In the fin-tube heat exchanger, the deformation of the louver is one of the factors that hinders the performance improvement. It has been found that the deformation becomes large. Also, in order to improve performance,
The louver becomes finer, which increases the area of the cut and raised cross section of the louver that has not been surface-treated, and the performance of the heat exchanger is limited due to the corrosion of the fins. For this reason, by providing corrugated fins between the plate fins, it is possible to reduce the number of louvers in the plate fins, reduce the load on the louvers, and improve the corrosion resistance of the louver portion. Further, the rigidity of the entire heat exchanger is increased, and the deformation of the fins when expanding the pipe can be reduced. As a result, it is possible to prevent the heat transfer performance from being deteriorated due to the fin deformation and to improve the heat transfer performance because the heat transfer area corresponding to the corrugated fins is increased.

【0008】図4は、本発明の別実施例を示すフィンを
積層した熱交換器の一部であり、図5は、熱交換器に供
せられるコルゲートフィンの斜視図で図3で示した実施
例のコルゲートフィンに比べてフィンピッチの大きいも
のである。本実施例は、実施例において流体の流れ方向
の上流部のコルゲートフィンを下流部のコルゲートフィ
ンのフィンピッチよりも大きくしたもので、当前、実施
例に比べて、伝熱面積は小さくなる。しかし、着霜の面
からみると、ほとんどの着霜は流体の流れ方向の上流部
で発生するため、この着霜によって熱抵抗が増加し、通
風抵抗増加による風量の低下を招き、その結果、伝熱性
能が著しく低下することが知られている。一般には、着
霜量の多い熱交換器入口部のフィンピッチを大きくする
方法、または、着霜の進行につれて空気通路を変化させ
る方法などがあるが、本発明は、後者に基づくものであ
り、図4に示すように伝熱管を境に、空気の流れ方向の
上流部と下流部でフィンピッチの異なるコルゲートフィ
ンを備えることによって、空気通路を変化させ面積あた
りの着霜を減らし、除霜間隔を遅延することができる。
FIG. 4 is a part of a heat exchanger in which fins according to another embodiment of the present invention are laminated, and FIG. 5 is a perspective view of a corrugated fin used in the heat exchanger, which is shown in FIG. The fin pitch is larger than that of the corrugated fin of the embodiment. In this embodiment, the corrugated fins in the upstream portion in the fluid flow direction in the embodiment are made larger than the fin pitch of the corrugated fins in the downstream portion, so that the heat transfer area is smaller than that in the embodiment. However, from the viewpoint of frost formation, most frost formation occurs in the upstream part in the flow direction of the fluid, so the thermal resistance increases due to this frost formation, leading to a decrease in air volume due to an increase in ventilation resistance. It is known that heat transfer performance is significantly reduced. Generally, there is a method of increasing the fin pitch of the heat exchanger inlet with a large amount of frost, or a method of changing the air passage as the frost progresses, but the present invention is based on the latter, As shown in FIG. 4, by providing corrugated fins having different fin pitches in the upstream and downstream portions of the air flow direction with the heat transfer tube as a boundary, the air passage is changed to reduce frost formation per area, and defrosting interval is increased. Can be delayed.

【0009】本発明の他の実施例を図6を用いて説明す
る。図6は、フィンを積層した熱交換器の一部で、5は
図5で示したコルゲートフィン、6はルーバを有したコ
ルゲートフィンで、流体の流れ方向の上流部の5のフィ
ンピッチより小さいものである。これによって、ルーバ
率が増加するため伝熱性能が向上し、前述の実施例と同
様な着霜に対する作用効果を奏することができる。
Another embodiment of the present invention will be described with reference to FIG. FIG. 6 shows a part of a heat exchanger in which fins are laminated, 5 is a corrugated fin shown in FIG. 5, 6 is a corrugated fin having a louver, and is smaller than the fin pitch of 5 at the upstream portion in the fluid flow direction. It is a thing. As a result, the louver ratio is increased, so that the heat transfer performance is improved, and the same operational effect against frost formation as in the above-described embodiment can be obtained.

【0010】さらに、本発明の実施例を図7を用いて説
明する。図7は、フィンを積層した熱交換器の一部、7
はルーバをもったコルゲートフィンで、流体の流れ方向
の下流部の6のフィンピッチより大きいものである。こ
れによって、実施例よりもルーバ率が増加するため、よ
り伝熱性能は向上し、着霜に関しては実施例と同様な作
用効果を得ることができる。
Further, an embodiment of the present invention will be described with reference to FIG. FIG. 7 shows a part of a heat exchanger in which fins are stacked,
Is a corrugated fin having a louver, which is larger than the fin pitch of 6 at the downstream portion in the fluid flow direction. As a result, the louver ratio is increased as compared with the embodiment, so that the heat transfer performance is further improved, and it is possible to obtain the same action and effect as the embodiment with respect to frost formation.

【0011】また、これまで説明した各実施例は、通常
フィン材にはアルミニウム,伝熱管には銅を用いるが、
フィン材を銅とすることによって、はんだ付けによりプ
レートフィンとコルゲートフィンを容易に接合できると
ともに、電位差の大きな異種金属間の接触から生じる腐
食を防ぐことができるため、熱交換器のより安定した長
期使用が可能となる。
In each of the embodiments described above, aluminum is usually used as the fin material and copper is used as the heat transfer tube.
By using copper as the fin material, the plate fins and corrugated fins can be easily joined by soldering, and corrosion caused by contact between dissimilar metals with a large potential difference can be prevented, resulting in a more stable long-term heat exchanger. It can be used.

【0012】[0012]

【発明の効果】本発明によれば、クロスフィンチューブ
式熱交換器のフィン間にコルゲートフィンを備えること
により、熱交換器の耐食性を向上させ高性能化を可能に
することができる。
According to the present invention, by providing corrugated fins between the fins of the cross fin tube type heat exchanger, it is possible to improve the corrosion resistance of the heat exchanger and achieve high performance.

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

【図1】本発明の一実施例の斜視図。FIG. 1 is a perspective view of an embodiment of the present invention.

【図2】フィンの平面図。FIG. 2 is a plan view of a fin.

【図3】コルゲートフィンの斜視図。FIG. 3 is a perspective view of a corrugated fin.

【図4】本発明の一実施例を示す斜視図。FIG. 4 is a perspective view showing an embodiment of the present invention.

【図5】コルゲートフィンの斜視図。FIG. 5 is a perspective view of a corrugated fin.

【図6】本発明の一実施例を示す斜視図。FIG. 6 is a perspective view showing an embodiment of the present invention.

【図7】本発明の一実施例を示す斜視図。FIG. 7 is a perspective view showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…プレートフィン、2…ルーバ部、3…伝熱管挿入
孔、4〜7…コルゲートフィン。
1 ... Plate fin, 2 ... Louver part, 3 ... Heat transfer tube insertion hole, 4-7 ... Corrugated fin.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】流体の流れを剪断する方向に複数の切り起
し細片を有するプレートフィンを前記流体の流れ方向と
交差する方向に積層し、前記プレートフィンを貫通する
複数の伝熱管を備えた熱交換器において、前記ルーバ
は、いずれも前記積層方向の一方の側に突出し、前記熱
交換器の側面から見て前記伝熱管の投影断面積の内側に
突出しているルーバであり、さらに前記各プレートフィ
ン間にコルゲートフィンを備えたことを特徴とする熱交
換器。
1. A plurality of heat transfer tubes penetrating the plate fins, wherein plate fins having a plurality of cut-and-raised strips in a direction of shearing a fluid flow are laminated in a direction intersecting with the fluid flow direction. In the heat exchanger, each of the louvers is a louver that protrudes to one side in the stacking direction and protrudes inside the projected cross-sectional area of the heat transfer tube when viewed from the side surface of the heat exchanger. A heat exchanger having corrugated fins between plate fins.
JP33323091A 1991-12-17 1991-12-17 Heat exchanger Pending JPH05164481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33323091A JPH05164481A (en) 1991-12-17 1991-12-17 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33323091A JPH05164481A (en) 1991-12-17 1991-12-17 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH05164481A true JPH05164481A (en) 1993-06-29

Family

ID=18263780

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33323091A Pending JPH05164481A (en) 1991-12-17 1991-12-17 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH05164481A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114111389A (en) * 2022-01-27 2022-03-01 甘肃蓝科石化高新装备股份有限公司 Continuous H-shaped finned tube bundle with multiple parallel tubes and airflow partitions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114111389A (en) * 2022-01-27 2022-03-01 甘肃蓝科石化高新装备股份有限公司 Continuous H-shaped finned tube bundle with multiple parallel tubes and airflow partitions
CN114111389B (en) * 2022-01-27 2022-08-23 甘肃蓝科石化高新装备股份有限公司 Parallel multi-tube continuous H-shaped finned tube bundle forming airflow partition

Similar Documents

Publication Publication Date Title
US4365667A (en) Heat exchanger
US6401809B1 (en) Continuous combination fin for a heat exchanger
JP4952196B2 (en) Heat exchanger
JP2000179988A (en) Refrigerant evaporator
JP4930413B2 (en) Heat exchanger
WO2014167845A1 (en) Fin-and-tube heat exchanger and refrigeration cycle device
JPH0791873A (en) Fin and tube type heat exchanger
JPH0996497A (en) Fin tube type heat exchanger
JPH06221787A (en) Heat exchanger
JPS5995359A (en) Evaporator
JPH0829016A (en) Outdoor heat exchanger for heat pump
JP2009204277A (en) Heat exchanger
JPH05322478A (en) Heat exchanger
JP6706839B2 (en) Fin tube heat exchanger
JP4147731B2 (en) Heat exchanger for cooling
JP2568968Y2 (en) Heat exchanger
JP3048614B2 (en) Heat exchanger
JP4626422B2 (en) Finned tube heat exchanger
JP2002130973A (en) Heat exchanger
JPH05164481A (en) Heat exchanger
EP2224198A1 (en) Fin and tube type heat exchanger
JP2624336B2 (en) Finned heat exchanger
JPH1123179A (en) Heat exchanger with fin
JP2005201467A (en) Heat exchanger
JP2004317002A (en) Heat exchanger