JP5523400B2 - Heat exchanger and air conditioner equipped with the heat exchanger - Google Patents

Heat exchanger and air conditioner equipped with the heat exchanger Download PDF

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JP5523400B2
JP5523400B2 JP2011141505A JP2011141505A JP5523400B2 JP 5523400 B2 JP5523400 B2 JP 5523400B2 JP 2011141505 A JP2011141505 A JP 2011141505A JP 2011141505 A JP2011141505 A JP 2011141505A JP 5523400 B2 JP5523400 B2 JP 5523400B2
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fin
heat exchanger
notch
heat transfer
transfer tube
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JP2013007540A (en
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孝彦 河合
光裕 石川
浩招 牧野
隆 金谷
晃 石橋
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Mitsubishi Electric Corp
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本発明は、熱交換器及びこの熱交換器を備えた空気調和機に関する。   The present invention relates to a heat exchanger and an air conditioner equipped with the heat exchanger.

従来より、扁平伝熱管が嵌入する切欠きが長手方向に櫛歯状に並設されたフィンを、空気が通過する隙間を置いて複数積層し、これらフィンの切欠きには扁平伝熱管を嵌入し、扁平伝熱管の内部を作動流体が通過する熱交換器が知られている。   Conventionally, a plurality of fins in which notches into which flat heat transfer tubes are inserted are arranged in a comb-like shape in the longitudinal direction are stacked with a gap through which air passes, and flat heat transfer tubes are inserted into the notches of these fins A heat exchanger in which a working fluid passes through a flat heat transfer tube is known.

このようなものにおいて、フィンの切欠きの幅は、これに嵌入される扁平伝熱管との密着性を考慮して、扁平伝熱管よりも狭くなるように設定されている。そのため、切欠きの末端円弧の半径も、切欠きに嵌入される扁平伝熱管の嵌入末端円弧の半径よりも小さくなっている。従って、フィンの切欠きに扁平伝熱管を嵌入する際、切欠きの開口側が扁平伝熱管により押し開かれてフィンに反りが発生する。この反りは、扁平伝熱管を切欠きの末端円弧に押し込んで行くに従って大きくなる。これは扁平伝熱管を押し込む際のくさび作用によるものと思われる。フィンに反りが発生すると、扁平伝熱管間の間隔が乱れ、接続するための配管のロウ付け及びユニット収納に支障が出る。さらに管とフィンとの密着性が悪化し、伝熱性能が低下する。   In such a thing, the width of the notch of the fin is set so as to be narrower than that of the flat heat transfer tube in consideration of adhesion to the flat heat transfer tube inserted therein. For this reason, the radius of the end arc of the notch is also smaller than the radius of the end arc of the flat heat transfer tube inserted into the notch. Accordingly, when the flat heat transfer tube is fitted into the notch of the fin, the opening side of the notch is pushed open by the flat heat transfer tube, and the fin is warped. This warp increases as the flat heat transfer tube is pushed into the notch end arc. This seems to be due to the wedge effect when pushing in the flat heat transfer tube. When the fin is warped, the interval between the flat heat transfer tubes is disturbed, which causes troubles in brazing of the piping for connection and housing of the unit. Furthermore, the adhesiveness between the tube and the fin is deteriorated, and the heat transfer performance is lowered.

このような問題を、従来は、フィンにおける切欠きの無い側に強度を増すためのビードを設けてフィンの剛性を高めることで、対処している(例えば、特許文献1,2参照)。   Conventionally, such a problem has been dealt with by increasing the rigidity of the fin by providing a bead for increasing the strength on the side of the fin not having a notch (for example, see Patent Documents 1 and 2).

特開2008−002746号公報(図3)JP 2008-002746 A (FIG. 3) 実開平5−090173号公報(図2)Japanese Utility Model Publication No. 5-090173 (FIG. 2)

このように、従来の熱交換器は、フィンの剛性を高めることで、切欠きの開口側が扁平伝熱管により押し開かれることにより発生するフィンの反りに対処しており、反りの発生そのものを抑制するものではなかった。   As described above, the conventional heat exchanger copes with the warping of the fin that occurs when the opening side of the notch is pushed open by the flat heat transfer tube by increasing the rigidity of the fin, and suppresses the occurrence of the warping itself. It wasn't something to do.

本発明の技術的課題は、切欠きの開口側が扁平伝熱管により押し開かれることにより発生する反りそのものを抑制できるようにすることにある。   The technical problem of the present invention is to be able to suppress the warpage itself that occurs when the opening side of the notch is pushed open by a flat heat transfer tube.

本発明に係る熱交換器は、内部を作動流体が通過する扁平伝熱管と、切欠きが長手方向に櫛歯状に並設されたフィンとを有し、フィンは、隙間を置いて複数積層されており、切欠きには、扁平伝熱管が嵌入された熱交換器において、フィン長手方向の中央部よりも両端側の切欠きの深さが深くなるようにしたものである。   A heat exchanger according to the present invention has a flat heat transfer tube through which a working fluid passes and fins in which notches are juxtaposed in a comb-like shape in the longitudinal direction, and the fins are stacked with a gap. In the heat exchanger in which the flat heat transfer tubes are fitted, the notches are formed so that the notches on both ends are deeper than the center portion in the fin longitudinal direction.

本発明に係る熱交換器においては、フィン長手方向の中央部よりも両端側の切欠きの深さが深くなるようにしているので、フィン長手方向の両端側の切欠きに嵌入される扁平伝熱管の嵌入先端と切欠きの末端円弧との間に遊びを設けることができ、その分、フィン長手方向の中央部よりも両端側の切欠きに対する扁平伝熱管の押し込み圧力を小さくすることができる。このため、各切欠きの開口側が扁平伝熱管により押し開かれることにより発生する反りそのものを抑制することができ、配管部品の取付性及び伝熱性能が向上し、ユニット収納時の変形分を考慮した無駄な空間を無くすことができる。   In the heat exchanger according to the present invention, since the depth of the notches on both end sides is deeper than the center portion in the fin longitudinal direction, the flat transmission fitted into the notches on both end sides in the fin longitudinal direction. A play can be provided between the insertion tip of the heat tube and the end arc of the notch, and accordingly, the pushing pressure of the flat heat transfer tube against the notch on both ends of the fin in the longitudinal direction can be reduced. . For this reason, it is possible to suppress the warping itself that occurs when the opening side of each notch is pushed open by a flat heat transfer tube, improving the mounting properties and heat transfer performance of piping parts, and taking into account deformation during unit storage The wasted space can be eliminated.

本発明の実施形態1に係る熱交換器の要部の外観を示す斜視図である。It is a perspective view which shows the external appearance of the principal part of the heat exchanger which concerns on Embodiment 1 of this invention. 本発明の実施形態1に係る熱交換器のフィンと扁平伝熱管との関係を示す断面図である。It is sectional drawing which shows the relationship between the fin of the heat exchanger which concerns on Embodiment 1 of this invention, and a flat heat exchanger tube. 比較例の熱交換器のフィンと扁平伝熱管との関係を示す断面図である。It is sectional drawing which shows the relationship between the fin of the heat exchanger of a comparative example, and a flat heat exchanger tube. 本発明の実施形態2に係る空気調和機の冷凍サイクルの冷媒回路図である。It is a refrigerant circuit figure of the refrigerating cycle of the air conditioner concerning Embodiment 2 of the present invention.

実施形態1.
図1は本発明の実施形態1に係る熱交換器の要部の外観を示す斜視図、図2はそのフィンと扁平伝熱管との関係を示す断面図である。
本発明の実施形態1に係る熱交換器10は、図1及び図2のように空気が通過する隙間を置いて複数積層された矩形状のフィン2と、これらフィン2のそれぞれに直交し、内部を作動流体が通過する扁平伝熱管1とを備えている。
Embodiment 1. FIG.
FIG. 1 is a perspective view showing the appearance of the main part of a heat exchanger according to Embodiment 1 of the present invention, and FIG. 2 is a cross-sectional view showing the relationship between the fins and flat heat transfer tubes.
The heat exchanger 10 according to Embodiment 1 of the present invention includes rectangular fins 2 stacked in a plurality of gaps through which air passes as shown in FIGS. 1 and 2, and orthogonal to each of these fins 2. A flat heat transfer tube 1 through which the working fluid passes is provided.

これを更に詳述すると、フィン2には、扁平伝熱管1が嵌入する切欠き2aが長手方向に櫛歯状に並設されている。切欠き2aの開口部2bの幅は、これに嵌入される扁平伝熱管1との密着性を考慮して、扁平伝熱管1よりも狭くなるように設定されている。また、図2のように切欠き2aは、それぞれの末端円弧2cを結んで形成される包絡線A1が、フィン2の切欠き形成側が凸となる円弧を描くように構成されている。これにより、切欠き2aは、フィン長手方向の中央部から両端側にいくにしたがって深さが滑らかに深くなる。但し、中央部に存在する所定個数の切欠き2aの深さが同じでもよい。   More specifically, the fin 2 is provided with a notch 2a into which the flat heat transfer tube 1 is fitted in a comb-like shape in the longitudinal direction. The width of the opening 2b of the notch 2a is set so as to be narrower than that of the flat heat transfer tube 1 in consideration of adhesiveness with the flat heat transfer tube 1 fitted therein. Further, as shown in FIG. 2, the notch 2a is configured such that the envelope A1 formed by connecting the respective end arcs 2c draws an arc in which the notch forming side of the fin 2 is convex. Thereby, the depth of the notch 2a increases smoothly from the center in the fin longitudinal direction toward both ends. However, the depth of the predetermined number of notches 2a existing in the center may be the same.

図3は比較例の熱交換器のフィンと扁平伝熱管との関係を示す断面図である。
この比較例の熱交換器のフィン(以下、これを「試験用フィン」という)3は、従来型のフィン(各切欠きの深さが、全てフィン長手方向の中央部の切欠きの深さと同じであるもの)である。このような試験用フィン3の各切欠き3aに扁平伝熱管1を嵌入し、末端円弧3cまで差し込むと、既述したように各切欠き3aの開口部3b側が扁平伝熱管1により押し開かれて試験用フィン3に反りA2が発生する。前述の包絡線A1が描く円弧の曲率は、この試験用フィン3に発生する反りA2の曲率に応じて設定されたものである。ここでは、包絡線A1が描く円弧の反り量が試験用フィン3の反り量B2の半分の反り量B1となるように、包絡線A1が描く円弧の曲率が設定されている。これにより、フィン2の反切欠き側つなぎ部の幅の確保が容易となっている。
FIG. 3 is a sectional view showing the relationship between the fins of the heat exchanger of the comparative example and the flat heat transfer tubes.
The fins (hereinafter referred to as “test fins”) 3 of the heat exchanger of this comparative example are conventional fins (the depth of each notch is the same as the depth of the notch at the center in the longitudinal direction of the fin). Are the same). When the flat heat transfer tube 1 is inserted into each notch 3a of such a test fin 3 and inserted to the end arc 3c, the opening 3b side of each notch 3a is pushed open by the flat heat transfer tube 1 as described above. As a result, the test fin 3 warps A2. The curvature of the arc drawn by the envelope A1 is set according to the curvature of the warp A2 generated in the test fin 3. Here, the curvature of the arc drawn by the envelope A1 is set so that the amount of warpage of the arc drawn by the envelope A1 becomes half the amount of warpage B1 of the warp B2 of the test fin 3. Thereby, it is easy to secure the width of the connecting portion on the opposite side of the fin 2.

次に、本発明の実施形態1に係る熱交換器のフィンの反り抑制原理について図2及び図3を用いて説明する。図3のように1枚目のフィンすなわち試験用フィン3に反りA2が発生している状態で、2枚目の試験用フィン3の各切欠き3aに扁平伝熱管1を嵌入する(又は扁平伝熱管1に2枚目の試験用フィン3を嵌入する)場合、まず1枚目の試験用フィン3の反りによって高位置となった両端に位置する扁平伝熱管1が2枚目の試験用フィン3の両端に位置する切欠き3aに嵌入する。そして、この状態から両端に位置する扁平伝熱管1を2枚目の試験用フィン3の両端に位置する切欠き3aの末端円弧3cまで差し込むわけであるが、これら両端に位置する扁平伝熱管1を2枚目の試験用フィン3の両端に位置する切欠き3aの末端円弧3cまで差し込んでも、2枚目の試験用フィン3の中央部の切欠き3aに後から差し込まれた扁平伝熱管1は、下位位置にあるために2枚目の試験用フィン3の中央部の切欠き3aの途中までしか嵌入しない。そのため、2枚目の試験用フィン3の長手方向の中央部を扁平伝熱管1側に無理に押し付けて、2枚目の試験用フィン3の中央部の切欠き3aの末端円弧3cまで扁平伝熱管1を差し込まなければならず、反りが更に悪化していく。   Next, the fin warpage suppression principle of the heat exchanger according to the first embodiment of the present invention will be described with reference to FIGS. As shown in FIG. 3, the flat heat transfer tube 1 is fitted into each notch 3a of the second test fin 3 (or flat) in a state where the warping A2 is generated in the first fin, that is, the test fin 3. When the second test fin 3 is inserted into the heat transfer tube 1), the flat heat transfer tubes 1 positioned at both ends, which are positioned higher due to warpage of the first test fin 3, are used for the second test. It fits in the notch 3a located in the both ends of the fin 3. FIG. Then, from this state, the flat heat transfer tubes 1 located at both ends are inserted to the end arcs 3c of the notches 3a located at both ends of the second test fin 3, but the flat heat transfer tubes 1 located at both ends are inserted. Is inserted into the notch 3c of the notch 3a located at both ends of the second test fin 3, and the flat heat transfer tube 1 is inserted later into the notch 3a in the center of the second test fin 3. Since it is in the lower position, it only fits in the middle of the notch 3a at the center of the second test fin 3. Therefore, the center portion of the second test fin 3 in the longitudinal direction is forcibly pressed against the flat heat transfer tube 1 side, and the flat transfer is made to the end arc 3c of the notch 3a in the center portion of the second test fin 3. The heat pipe 1 must be inserted, and the warpage is further deteriorated.

次に、図3のように1枚目のフィンすなわち試験用フィン3に反りA2が発生している状態で、本発明の実施形態1に係る熱交換器のフィン2を2枚目のフィンとして用い、各切欠き2aに扁平伝熱管1を差し込む(又は扁平伝熱管1に2枚目のフィン2を嵌入する)場合について考察する。この場合も、まず1枚目の試験用フィン3の反りによって高位置となった両端に位置する扁平伝熱管1が2枚目のフィン2の両端に位置する切欠き2aに嵌入する。そして、この状態から両端に位置する扁平伝熱管1を2枚目のフィン2の両端に位置する切欠き2aの末端円弧2cまで差し込む。この場合、2枚目のフィン2の各切欠き2aは、それぞれの末端円弧2cを結んで形成される包絡線A1が、フィン2の切欠き形成側が凸となる円弧を描くように構成され、これによって切欠き2aの深さが、フィン長手方向の中央部から両端側にいくにしたがって滑らかに深くなるように構成されているので、これら扁平伝熱管1を2枚目のフィン2の両端に位置する切欠き2aの末端円弧2cまで差し込めば、2枚目のフィン2の中央部の切欠き2aに後から差し込まれた扁平伝熱管1も切欠き2aの末端円弧2cまで差し込まれる。そのため、2枚目のフィン2を扁平伝熱管1側に無理に押し付ける必要がなくなって、反りの更なる悪化を防止することができる。   Next, as shown in FIG. 3, with the warping A2 occurring in the first fin, ie, the test fin 3, the fin 2 of the heat exchanger according to the first embodiment of the present invention is used as the second fin. The case where the flat heat transfer tube 1 is inserted into each notch 2a (or the second fin 2 is inserted into the flat heat transfer tube 1) will be considered. Also in this case, first, the flat heat transfer tubes 1 positioned at both ends which have become high due to warpage of the first test fin 3 are fitted into the notches 2 a positioned at both ends of the second fin 2. Then, from this state, the flat heat transfer tubes 1 positioned at both ends are inserted to the end arc 2c of the notch 2a positioned at both ends of the second fin 2. In this case, each notch 2a of the second fin 2 is configured such that the envelope A1 formed by connecting the respective terminal arcs 2c draws an arc in which the notch forming side of the fin 2 is convex. As a result, the depth of the notch 2a is configured to be smoothly deepened from the center in the longitudinal direction of the fin toward both ends, so that these flat heat transfer tubes 1 are disposed at both ends of the second fin 2 If it inserts to the end circular arc 2c of the notch 2a located, the flat heat exchanger tube 1 inserted afterwards into the notch 2a of the center part of the 2nd fin 2 will also be inserted to the terminal circular arc 2c of the notch 2a. Therefore, it is not necessary to force the second fin 2 to be pressed against the flat heat transfer tube 1 side, and further deterioration of warpage can be prevented.

以上は本発明の実施形態1に係る熱交換器のフィン2を2枚目以降のフィンとして用いる場合の利点について述べたものであるが、1枚目のフィンに従来型の試験用フィン3(各切欠きの深さが、全てフィン長手方向の中央部の切欠きの深さと同じであるもの)を用いているので、反りA2の発生は抑制できないものである。   The above describes the advantages of using the fin 2 of the heat exchanger according to the first embodiment of the present invention as the second and subsequent fins. Since the depth of each notch is the same as the depth of the notch at the center in the fin longitudinal direction), the occurrence of warpage A2 cannot be suppressed.

本発明の実施形態1に係る熱交換器のフィン2は、1枚目から用いることで、有効に作用し、反り発生を抑制できるものである。すなわち、フィン2は、フィン長手方向の中央部よりも両端側の切欠き2aの深さが深くなるようにしているので、フィン長手方向の両端側の切欠き2aに嵌入される扁平伝熱管1の嵌入先端と切欠きの末端円弧との間に遊びを設けることができ、その分、フィン長手方向の中央部よりも両端側の切欠き2aに対する扁平伝熱管1の押し込み圧力を小さくすることができる。このため、各切欠き2aの開口部2bが扁平伝熱管1により押し開かれることにより発生する反りそのものを抑制することができ、配管部品の取付性及び伝熱性能が向上し、ユニット収納時の変形分を考慮した無駄な空間を無くすことができる。   By using the fin 2 of the heat exchanger according to the first embodiment of the present invention from the first sheet, the fin 2 can effectively act and suppress warpage. That is, since the fin 2 is formed so that the depth of the notch 2a at both ends is deeper than the center portion in the fin longitudinal direction, the flat heat transfer tube 1 fitted into the notch 2a at both ends in the fin longitudinal direction. Play can be provided between the insertion end of the flat plate and the end arc of the notch, and accordingly, the pushing pressure of the flat heat transfer tube 1 against the notch 2a on both ends of the fin in the longitudinal direction can be reduced. it can. For this reason, it is possible to suppress the warping itself that occurs when the opening 2b of each notch 2a is pushed open by the flat heat transfer tube 1, and the mounting property and heat transfer performance of the piping parts are improved. It is possible to eliminate a useless space in consideration of deformation.

また、切欠き2aは、それぞれの末端円弧2cを結んで形成される包絡線A1が、フィン2の切欠き形成側が凸となる円弧を描くように構成し、これにより切欠き2aの深さが、フィン長手方向の中央部から両端側にいくにしたがって深さが滑らかに深くなるようにすることで、フィン長手方向の両端側の切欠き2aの深さの最適化が図れる。これにより、切欠き2aの末端円弧2cと扁平伝熱管1の嵌入先端との間に隙間が発生することがあっても、これを極力小さなものとすることができて、伝熱性能を高めることができる。   Further, the notch 2a is configured such that the envelope A1 formed by connecting the respective end arcs 2c draws an arc in which the notch forming side of the fin 2 is convex, and the depth of the notch 2a is thereby increased. The depths of the notches 2a on both ends in the fin longitudinal direction can be optimized by smoothly increasing the depth from the center in the fin longitudinal direction toward both ends. Thereby, even if a gap is generated between the end arc 2c of the notch 2a and the insertion tip of the flat heat transfer tube 1, this can be made as small as possible to improve the heat transfer performance. Can do.

実施形態2.
図4は前述の熱交換器を備えた本発明の実施形態2に係る空気調和機の冷凍サイクルの冷媒回路図である。
Embodiment 2. FIG.
FIG. 4 is a refrigerant circuit diagram of a refrigeration cycle of an air conditioner according to Embodiment 2 of the present invention including the above-described heat exchanger.

本発明の実施形態2に係る空気調和機は、図4のように圧縮機33、凝縮器34、絞り装置35、蒸発器36、凝縮器用送風機37a及びその駆動用モーター38a、蒸発器用送風機37b及びその駆動用モーター38bにより構成され、圧縮機33と、凝縮器34と、絞り装置35と、蒸発器36とが環状に接続されている。前述の実施形態1に係る熱交換器を凝縮器34または蒸発器36、もしくは両方に用いることにより、エネルギー効率の高い空調冷凍装置を実現することができる。ここで、エネルギー効率は、次式(1)(2)で求められるものである。
暖房エネルギー効率=室内熱交換器(凝縮器)能力/全入力‥‥‥‥‥‥(1)
冷房エネルギー効率=室内熱交換器(蒸発器)能力/全入力‥‥‥‥‥‥(2)
As shown in FIG. 4, the air conditioner according to the second embodiment of the present invention includes a compressor 33, a condenser 34, a throttling device 35, an evaporator 36, a condenser blower 37a and its driving motor 38a, an evaporator blower 37b, and The compressor 33, the condenser 34, the expansion device 35, and the evaporator 36 are connected in a ring shape. By using the heat exchanger according to the first embodiment for the condenser 34, the evaporator 36, or both, an air-conditioning refrigeration apparatus with high energy efficiency can be realized. Here, energy efficiency is calculated | required by following Formula (1) (2).
Heating energy efficiency = indoor heat exchanger (condenser) capacity / all inputs (1)
Cooling energy efficiency = indoor heat exchanger (evaporator) capacity / all inputs (2)

なお、前述の実施形態1で述べた熱交換器及びこの熱交換器を備えた空気調和機については、HCFC(R22)やHFC(R116、R125、R134a、R14、R143a、R152a、R227ea、R23、R236ea、R236fa、R245ca、R245fa、R32、R41、RC318などや、これら冷媒の数種の混合冷媒R407A、R407B、R407C、R407D、R407E、R410A、R410B、R404A、R507A、R508A、R508Bなど)、HC(ブタン、イソブタン、エタン、プロパン、プロピレンなどや、これら冷媒の数種混合冷媒)、自然冷媒(空気、炭酸ガス、アンモニアなどや、これら冷媒の数種の混合冷媒)、HFO1234yf等の低GWP冷媒、またこれら冷媒の数種の混合冷媒など、どんな種類の冷媒を用いても、その効果を達成することができる。   In addition, about the heat exchanger described in above-mentioned Embodiment 1, and an air conditioner provided with this heat exchanger, HCFC (R22) and HFC (R116, R125, R134a, R14, R143a, R152a, R227ea, R23, R236ea, R236fa, R245ca, R245fa, R32, R41, RC318, etc., and several types of these refrigerants R407A, R407B, R407C, R407D, R407E, R410A, R410B, R404A, R507A, R508A, HCB, etc. Low GWP refrigerants such as butane, isobutane, ethane, propane, propylene, etc., some mixed refrigerants of these refrigerants, natural refrigerants (air, carbon dioxide, ammonia, etc., several mixed refrigerants of these refrigerants), HFO1234yf, These refrigerants A mixed refrigerant type, be used any type of refrigerant, can achieve its effect.

また、作動流体として、ここでは空気と冷媒の例を示したが、他の気体、液体、気液混合流体を用いても、同様の効果を奏する。   Moreover, although the example of air and a refrigerant | coolant was shown here as a working fluid, even if it uses other gas, liquid, and gas-liquid mixed fluid, there exists the same effect.

扁平伝熱管1とフィン2は、異なった材料を用いることが一般的である。しかし、扁平伝熱管1とフィン2の材料として、銅やアルミ等、同じ材料を用いることで、フィン2と扁平伝熱管1のロウ付けが可能となる。この場合には、フィン2と扁平伝熱管1の接触熱伝達率が飛躍的に向上し、熱交換能力が大幅に向上する。また、リサイクル性も向上させることができる。   The flat heat transfer tubes 1 and the fins 2 are generally made of different materials. However, it is possible to braze the fins 2 and the flat heat transfer tubes 1 by using the same material such as copper or aluminum as the material of the flat heat transfer tubes 1 and the fins 2. In this case, the contact heat transfer coefficient between the fin 2 and the flat heat transfer tube 1 is dramatically improved, and the heat exchange capability is greatly improved. Moreover, recyclability can also be improved.

また、扁平伝熱管1とフィン2を密着させる方法として、炉中ロウ付けを行う場合、炉中ロウ付けの後に、フィン2に親水材を塗布するようにすれば、親水材の焼け落ちを防ぐことができる。   Further, as a method of bringing the flat heat transfer tube 1 and the fin 2 into close contact, when brazing in the furnace, if the hydrophilic material is applied to the fin 2 after brazing in the furnace, the burning of the hydrophilic material is prevented. be able to.

また、前述の実施形態1で説明した熱交換器を室外機で用いた場合においても同様な効果を奏する。   Further, the same effect can be obtained when the heat exchanger described in the first embodiment is used in an outdoor unit.

なお、前述の実施形態1で述べた熱交換器及びそれを用いた実施形態2の空調冷凍装置については、鉱油系、アルキルベンゼン油系、エステル油系、エーテル油系、フッ素油系など、冷媒と油が溶ける溶けないに拘わらず、どんな冷凍機油についても、その効果を達成することができる。   For the heat exchanger described in the first embodiment and the air-conditioning refrigeration apparatus of the second embodiment using the heat exchanger, a mineral oil, an alkylbenzene oil, an ester oil, an ether oil, a fluorine oil, The effect can be achieved with any refrigeration oil, regardless of whether the oil is soluble or not.

1 扁平伝熱管、2,3 フィン、2a,3a 切欠き、2b,3b 開口部、2c,3c 末端円弧、3 試験用フィン、10 熱交換器、33 圧縮機、34 凝縮器、35 絞り装置、36 蒸発器、37a 凝縮器用送風機、37b 蒸発器用送風機、38a,38b 駆動用モーター、A1 包絡線、A2 反り、B1 包絡線が描く円弧の反り量、B2 従来型のフィンの反り量。   1 flat heat transfer tube, 2, 3 fin, 2a, 3a notch, 2b, 3b opening, 2c, 3c end arc, 3 test fin, 10 heat exchanger, 33 compressor, 34 condenser, 35 expansion device, 36 Evaporator, 37a Condenser blower, 37b Evaporator blower, 38a, 38b Drive motor, A1 envelope, A2 warp, B1 Warp amount of arc drawn by envelope, B2 Warp amount of conventional fin.

Claims (5)

内部を作動流体が通過する扁平伝熱管と、切欠きが長手方向に櫛歯状に並設されたフィンとを有し、前記フィンは、隙間を置いて複数積層されており、前記切欠きには、前記扁平伝熱管が嵌入された熱交換器において、
フィン長手方向の中央部よりも両端側の前記切欠きの深さが深くなるようにしたことを特徴とする熱交換器。
It has a flat heat transfer tube through which the working fluid passes, and fins in which notches are arranged in a comb-like shape in the longitudinal direction, and a plurality of the fins are stacked with a gap therebetween. Is a heat exchanger in which the flat heat transfer tube is inserted,
A heat exchanger characterized in that the depth of the notch on both end sides becomes deeper than the center portion in the fin longitudinal direction.
フィン長手方向の中央部から両端側にいくにしたがって前記切欠きの深さが深くなっていることを特徴とする請求項1記載の熱交換器。   The heat exchanger according to claim 1, wherein the depth of the notch becomes deeper from the center in the longitudinal direction of the fin toward both ends. 前記切欠きは、それぞれの末端円弧を結んで形成される包絡線が、前記フィンの切欠き形成側が凸となる円弧を描くように構成されていることを特徴とする請求項1又は請求項2記載の熱交換器。   The said notch is comprised so that the envelope formed by connecting each terminal circular arc may draw the circular arc from which the notch formation side of the said fin becomes convex. The described heat exchanger. 前記包絡線が描く円弧の曲率は、各切欠きの深さが、フィン長手方向の前記中央部の切欠きの深さと同じである試験用フィンに扁平伝熱管を嵌入した時に当該試験用フィンに発生する反りの曲率に応じて設定されていることを特徴とする請求項3記載の熱交換器。   The curvature of the arc drawn by the envelope is such that the depth of each notch is the same as the depth of the notch in the central portion in the longitudinal direction of the fin when the flat heat transfer tube is fitted into the test fin. The heat exchanger according to claim 3, wherein the heat exchanger is set according to a curvature of a warp to be generated. 圧縮機と、凝縮器と、絞り装置と、蒸発器とを環状に接続した空気調和機において、
作動流体に冷媒を用い、前記蒸発器及び前記凝縮器の両者又はいずれか一方に、前記請求項1乃至請求項4のいずれかの熱交換器を用いたことを特徴とする空気調和機。
In an air conditioner in which a compressor, a condenser, a throttling device, and an evaporator are connected in an annular shape,
An air conditioner using a refrigerant as a working fluid and using the heat exchanger according to any one of claims 1 to 4 for both or one of the evaporator and the condenser.
JP2011141505A 2011-06-27 2011-06-27 Heat exchanger and air conditioner equipped with the heat exchanger Expired - Fee Related JP5523400B2 (en)

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