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JP7789726B2 - Heat exchanger coil fin structure - Google Patents
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JP7789726B2 - Heat exchanger coil fin structure - Google Patents

Heat exchanger coil fin structure

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JP7789726B2
JP7789726B2 JP2023121630A JP2023121630A JP7789726B2 JP 7789726 B2 JP7789726 B2 JP 7789726B2 JP 2023121630 A JP2023121630 A JP 2023121630A JP 2023121630 A JP2023121630 A JP 2023121630A JP 7789726 B2 JP7789726 B2 JP 7789726B2
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slit
slits
rib
section
coil
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JP2025018153A (en
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一人 星野
智彦 竹内
隆介 中村
書▲かい▼ 范
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Sinko Industries Ltd
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Sinko Industries Ltd
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Description

本発明は、熱交換器のコイルのフィン構造に関し、特に、熱交換性能を良くする熱交換器のフィン構造に関する。 The present invention relates to a fin structure for a heat exchanger coil, and in particular to a fin structure for a heat exchanger that improves heat exchange performance.

従来の熱交換器のコイル(所謂フィンアンドチューブ)は、図1に示すように、コイルの主管にフィンを装着し、熱交換性能を高めるためにフィン表面に切り起こしたスリットを設けている。このスリットフィンは、例えば、特許文献1に示すように、コイル主管間の距離よりも短い切り込みによるスリットを並列して数本設け、スリットとフィン材との間には隙間を設けて空気が通過するようにフィン表面に形成し、スリットは通常コイル主管の段方向(長手方向)及び、左右のコイル主管の複数の列方向(左右方向)に並列に連続形成されている。このスリット表面や隙間を空気が通過することによって熱交換される。 As shown in Figure 1, conventional heat exchanger coils (so-called fin and tube) have fins attached to the main tubes of the coil, with raised slits cut into the fin surface to enhance heat exchange performance. As shown in Patent Document 1, for example, these slit fins have several parallel slits cut shorter than the distance between the main tubes of the coil, with gaps formed between the slits and the fin material on the fin surface to allow air to pass through. The slits are usually formed in parallel in the row direction (longitudinal direction) of the main tubes of the coil and in multiple row directions (left-right direction) of the left and right main tubes of the coil. Heat is exchanged as air passes through the slit surfaces and gaps.

意匠登録第1137226号公報Design Registration No. 1137226

従来のコイルとフィンからなるフィンアンドチューブ型の熱交換器には、熱交換性能を高めるためにフィン表面に切り起こしたスリットを設け、このスリットは空気が通る主管と主管の間のフィン表面に形成され、このスリットが段方向(長手方向)、列方向(左右方向)に連続形成されたフィンを積層している。
このスリットフィンは、主管内を流れる熱媒体の熱を空気に伝達する伝熱板として機能し、スリットフィンのフィン表面に設けたスリット(切り起こし)の前縁部で温度境界層を更新し、温度境界層の発達を抑えることで熱伝達率を向上させている(前縁効果)ため、その結果、スリットの長さが長いほど(スリット前縁が長いほど)熱伝達率を上げることができる。コイルの主管間にスリットを配置する場合、スリット長さを長くすることで、熱伝達率の高いスリット前縁部が主管に近づくため、さらに熱伝達率を向上させることにもつながる。
このため、スリットフィンでは、スリットの長さが長いほど(スリット前縁が長いほど)熱伝達率を上げることができるが、スリットの長さが長くなるほどスリット成形(プレス成形)後の残留応力により、スリットにたわみが発生するという問題があり、スリット長さ拡大による性能向上の阻害要因となっていた。
In conventional fin-and-tube heat exchangers consisting of coils and fins, slits are cut into the fin surface to improve heat exchange performance. These slits are formed on the fin surface between the main pipes through which air passes, and the fins are stacked with these slits formed continuously in the row direction (longitudinal direction) and column direction (left and right direction).
These slit fins function as heat transfer plates that transfer the heat of the heat medium flowing inside the main pipe to the air, and the leading edges of the slits (raised cuts) on the fin surface of the slit fins update the thermal boundary layer, suppressing its development and improving the heat transfer coefficient (leading edge effect).As a result, the longer the slit length (the longer the slit leading edge), the higher the heat transfer coefficient can be.When slits are placed between the main pipes of the coil, increasing the slit length brings the slit leading edge, which has a high heat transfer coefficient, closer to the main pipe, further improving the heat transfer coefficient.
For this reason, in slit fins, the longer the slit (the longer the leading edge of the slit), the higher the heat transfer coefficient can be. However, the longer the slit, the more residual stress after slit forming (press forming) occurs, which causes the slit to warp, which is an obstacle to improving performance by increasing the slit length.

このように、コイルの主管間のフィンにスリットを配置する場合に、スリット長さを長くすることで、熱伝達率の高いスリット前縁部が主管に近づくため、さらに熱伝達率を向上させることにもつながるが、しかしながら、コイルの主管に用いるスリットフィンの厚さは、通常、0.1mmから0.2mmであって非常に薄い。したがって、スリットの長さが長くなると、図6に示すようにたわみが生じこれにより空気がスリットフィンに沿って移動する場合に、たわみによりスリットが形成する隙間が狭くなり空気の移動が制限されて結果として熱交換効率が低下する。 When slits are placed in the fins between the main pipes of the coil, increasing the slit length brings the leading edge of the slit, which has a high heat transfer coefficient, closer to the main pipe, further improving the heat transfer coefficient. However, the thickness of the slit fins used in the main pipes of the coil is typically very thin, ranging from 0.1 mm to 0.2 mm. Therefore, when the slit length is increased, deflection occurs as shown in Figure 6. As air moves along the slit fin, the deflection narrows the gap formed by the slit, restricting the movement of air and resulting in reduced heat exchange efficiency.

この発明は、前記のスリットフィンの熱交換効率を高めるためにスリットをなるべく長くするが、このための不都合を解決しようとするもので、熱交換器のコイルのフィンに設けたスリットにおいて、長いスリットを設けたために生じるスリットのたわみを防止して熱交換効率を向上させることを目的とするものである。 This invention aims to solve the inconvenience of making the slits as long as possible to increase the heat exchange efficiency of the slit fins mentioned above, and aims to improve heat exchange efficiency by preventing the deflection of the slits that occurs when long slits are provided in the fins of the heat exchanger coil.

上記の目的を達成するために、熱交換器のコイルに設けたスリットフィンでコイルの主管の段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造であって、少なくとも主管間の距離よりも大きくしたスリットにおいて、長手方向の剛性を高めるリブを設けたコイルのスリットフィン構造であり、前記リブは断面V字状(又は溝)、または、断面円弧状(又は溝)、または、断面台形状(又は溝)であれば良く、要は剛性を大きくしたものであれば良い。 To achieve the above objective, the slit fins provided on the coil of a heat exchanger have a slit fin structure that is larger than the distance between adjacent main pipes in the direction of the number of stages of the coil's main pipes, and the slits, which are at least larger than the distance between the main pipes, have ribs that increase longitudinal rigidity.The ribs may have a V-shaped cross section (or groove), an arc-shaped cross section (or groove), or a trapezoidal cross section (or groove), and the key is to increase rigidity.

本発明は、熱交換器のコイルに設けたスリットフィンで、段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造であるので、従来のようにコイルの主管間の距離よりも短いスリットとは異なり、スリットの長さ方向の長さを主管間よりも長くしたので(図4:X2×2)、長くした分だけ熱交換に関与するので熱交換効率が向上する。
また、隣り合う主管間の距離よりも大きくしたスリットは、スリット上面が平坦だとたわみが生じるので、スリットの上面にリブを設けることで剛性が増し、たわみが少なくなる。このリブ形状は断面V字状(又は溝)、または、断面円弧状(又は溝)、または、断面台形状(又は溝)としたもので、加工が簡単であるにも拘わらず顕著な効果が得られる。
The present invention has a slit fin structure in which the slit fins provided on the coil of a heat exchanger are longer than the distance between adjacent main pipes in the row direction. Therefore, unlike conventional slits which are shorter than the distance between the main pipes of the coil, the length of the slits in the longitudinal direction is longer than the distance between the main pipes (Figure 4: X2 x 2). As the slits are involved in heat exchange by the increased length, the heat exchange efficiency is improved.
Furthermore, since slits that are larger than the distance between adjacent main pipes will bend if the top surface of the slit is flat, providing ribs on the top surface of the slit increases rigidity and reduces bending. The rib shape is a V-shaped (or groove) cross section, an arc-shaped (or groove) cross section, or a trapezoidal (or groove) cross section, and although it is easy to process, it produces a remarkable effect.

実施例1の熱交換器の全体外観の斜視図、FIG. 1 is a perspective view of the overall appearance of a heat exchanger according to a first embodiment; 図1のスリットフィンの拡大部分の斜視図、FIG. 2 is a perspective view of an enlarged portion of the slit fin of FIG. 1; 図3は主管とスリットフィンの関係を示す正面断面図、Figure 3 is a front cross-sectional view showing the relationship between the main pipe and the slit fins. 図3のスリットの平面図、4 is a plan view of the slit of FIG. 3; 図5(a)は図4の長辺スリットの平面図、図5(b)は図5(a)の側面図、5(a) is a plan view of the long-side slit of FIG. 4, FIG. 5(b) is a side view of FIG. 5(a), スリットフィンのスリットの上面が平坦のたわみが生じた状態の側面図、A side view of the slit fin with the top surface of the slit flat and deflected. 図7(a)はスリット表面に断面V字状のリブを設けた平面図、図7(b)はその断側面図、図7(c)はその正面図、FIG. 7(a) is a plan view of a slit surface provided with a V-shaped cross-section rib, FIG. 7(b) is a cross-sectional side view thereof, and FIG. 7(c) is a front view thereof. 図8(a)はスリット表面に断面円弧状のリブを設けた平面図、図8(b)はその断側面図、図8(c)はその正面図、図8(d)はその斜視図、FIG. 8(a) is a plan view of a slit surface provided with a rib having an arcuate cross section, FIG. 8(b) is a cross-sectional side view thereof, FIG. 8(c) is a front view thereof, and FIG. 8(d) is a perspective view thereof. 図9(a)はスリット表面に断面台形状のリブを設けた平面図、図9(b)はその断側面図、図9(c)はその正面図、図9(d)はその斜視図、FIG. 9(a) is a plan view of a rib having a trapezoidal cross section provided on the surface of a slit, FIG. 9(b) is a cross-sectional side view thereof, FIG. 9(c) is a front view thereof, and FIG. 9(d) is a perspective view thereof. スリット幅2.7mmの平坦(フラット)及び各リブ形状毎のたわみ量を表す棒グラフ、A bar graph showing the amount of deflection for a flat surface with a slit width of 2.7 mm and for each rib shape. 従来のリブなしフィンの圧力損失と熱交換効率を基準(100%)としたときの断面V字形状リブの圧力損失比率と熱交換率の関係を示す解析結果である。10 shows the results of an analysis showing the relationship between the pressure loss ratio and heat exchange rate of a V-shaped cross-section rib when the pressure loss and heat exchange efficiency of a conventional fin without ribs are taken as the reference (100%).

本発明は、熱交換器のコイルに設けたスリットフィンで、段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造として、熱交換器での熱交換性能を高め、さらに、段数方向の主管間のスリットにおいて、少なくとも主管間の距離よりも長いスリットの断面形状を単なる平面ではなく、剛性を高めるためにスリットのたわみを抑制するためにリブを備えた形状とすることである。 The present invention provides slit fins on the coils of a heat exchanger with a slit fin structure that is larger than the distance between adjacent main pipes in the row direction, thereby improving the heat exchange performance of the heat exchanger. Furthermore, the cross-sectional shape of the slits between the main pipes in the row direction, which are at least longer than the distance between the main pipes, is not simply flat, but has ribs that suppress deflection of the slits to increase rigidity.

本発明の実施例で図面に沿って説明する。
先ず、熱交換率を高めるために熱交換器の通常のスリットフィンのスリットよりも長くしたスリットフィン321(図4:X4+X3又はX1+X2)について説明する。図3から図5、特に、図4において、2点鎖線の内側部分が従来の通常の短い短辺スリット322の切り起こした部分(図4:X1)であるが、本発明の前提となるのは、図4での2点鎖線の外側の斜線部分(図4:X2)がそれよりも長くした長辺スリット321が通常よりも長い部分(X2或いはX3)である。
ところで、熱交換器のコイル2のフィン3のフィン材自体は、厚さが0.1mmから0.2mmと薄いが、本実施例では0.15mmであり、スリットの長さが約31mm、フィンピッチ(FP)は2mmから4mmであるから、このスリット形状に加工するとなると、スリットの長さが長いほど(スリット前縁が長いほど)熱伝達率を上げることができる反面、スリットの長さが長くなるほどスリット成形(プレス成形)後の残留応力により、スリットに図6に示すような「たわみ」3212が発生するという問題があり、長辺スリット321の長さ拡大による性能向上の阻害要因となっていた。
そこで、切り起こすスリットの断面形状を、単なる平面40ではなく、剛性を高めるためのリブを備えた形状とすることでリブの長手方向の剛性を高め、「たわみ3212」を抑えたもので、図7のスリット形状をV型溝のリブ、図8の円溝のリブ、図9の台形溝のリブを作成して解析した。
An embodiment of the present invention will be described with reference to the drawings.
First, we will explain the slit fin 321 (X4+X3 or X1+X2 in FIG. 4) that is longer than the slits of a normal slit fin of a heat exchanger in order to increase the heat exchange efficiency. In FIGS. 3 to 5, and particularly in FIG. 4, the inside of the two-dot chain line is the cut-up portion (X1 in FIG. 4) of the normal short short-side slit 322 of the conventional art. However, the premise of the present invention is that the diagonally shaded portion (X2 in FIG. 4) outside the two-dot chain line in FIG. 4 is the longer-than-normal portion (X2 or X3) of the long-side slit 321.
Incidentally, the fin material itself of the fins 3 of the heat exchanger coil 2 is thin, having a thickness of 0.1 mm to 0.2 mm, but in this embodiment it is 0.15 mm, the slit length is approximately 31 mm, and the fin pitch (FP) is 2 mm to 4 mm. Therefore, when processing into this slit shape, the longer the slit length (the longer the slit leading edge), the higher the heat transfer coefficient can be. However, the longer the slit length, the more residual stress after slit forming (press forming) will cause the slit to develop a ``deflection'' 3212 as shown in Figure 6, which is a problem that hinders performance improvement by increasing the length of the long side slit 321.
Therefore, by making the cross-sectional shape of the cut and raised slit not simply a flat surface 40 but a shape equipped with ribs to increase rigidity, the rigidity in the longitudinal direction of the rib is increased and the "deflection 3212" is suppressed, and the slit shapes of Figure 7 were created and analyzed using V-shaped groove ribs, Figure 8 circular groove ribs, and Figure 9 trapezoidal groove ribs.

[リブの形状]
図6から図9でリブ4の形状について説明する。
図6は、スリットフィン32の長辺スリット321の表面にリブ4がなく平坦40であるが、後述するように長辺スリット321は「たわみ部3212」が生じることが多い。
図7は、長辺スリット321の表面には図7(b)に示すように断面V字状リブ41を設けたものである。
図8は、長辺スリット321の表面には図8(b)に示すように断面円弧状リブ42を設けたものである。円弧状も寸法によっては、断面V字形状とほぼ変わらなくなるので図8(b)に示すようにフィン3自体の円弧のリブ深さは0.26mmで曲率半径R1.65mmであり、フィン3とスリット表面3211との隙間(高さ)は1.3mmであり、十分に円弧状が確認できる形状である。
図9は、長辺スリット321の表面には図9(b)に示すように断面台形状リブ43を設けたものである。台形状も寸法によっては、断面円弧状形状や断面V字状形状とほぼ変わらなくなるので、図9(b)に示すように、台形の深さは0.2mmで、左右の巾は底辺が1.2mm、上辺が1.6mmであり、フィン3とスリット表面3211との隙間(高さ)は1.3mmであり、十分に台形が確認できる形状である。
[Rib Shape]
The shape of the rib 4 will be described with reference to FIGS.
In FIG. 6, the surfaces of the long side slits 321 of the slit fin 32 are flat 40 without ribs 4, but as will be described later, the long side slits 321 often have "flexed portions 3212".
In FIG. 7, a rib 41 having a V-shaped cross section is provided on the surface of the long side slit 321 as shown in FIG. 7(b).
8(b), a rib 42 having an arc-shaped cross section is provided on the surface of the long-side slit 321. Depending on the dimensions, the arc shape can become almost the same as a V-shaped cross section, so as shown in FIG. 8(b), the arc rib depth of the fin 3 itself is 0.26 mm, the radius of curvature R is 1.65 mm, and the gap (height) between the fin 3 and the slit surface 3211 is 1.3 mm, making the arc shape clearly recognizable.
9(b), a rib 43 having a trapezoidal cross section is provided on the surface of the long side slit 321. Depending on the dimensions, the trapezoidal shape can be almost the same as an arc-shaped cross section or a V-shaped cross section, so as shown in FIG. 9(b), the depth of the trapezoid is 0.2 mm, the width on the left and right sides is 1.2 mm at the base and 1.6 mm at the top, and the gap (height) between the fin 3 and the slit surface 3211 is 1.3 mm, making the trapezoidal shape clearly recognizable.

これらを形成した平面(フラット)40、及び、断面形状V字状の溝41、断面形状円孔円弧形状の溝(リブ)42、断面形状台形状のリブの溝43(リブ)のスリット幅2.7mm、長さが約31mmの長辺スリット321でたわみを解析した。この結果を図10の[棒グラフ]で説明する。
図10の[グラフ1]は、長辺スリット321が左からリブ4がないスリット40、断面V字状形状のリブ41、断面円弧状形状のリブ42、断面台形状のリブ43でありこれらのリブ4付き長辺スリットのたわみ量を解析し、リブなしのフラット40の表面のたわみ部3212との割合を算出して棒グラフにしたものである。
この解析結果から、フラットの表面のたわみを0%とした場合に、フィン3自体の厚さが0.15mmと薄いにも拘わらず、リブ断面V字形状のリブ41では-34%しかたわまず、断面円弧状形状のリブ42では-39%しかたわまず、断面台形形状のリブ43では-48%しかたわまなかった。すなわち、全般にかなり剛性が得られるが、断面V字形状のリブ43、断面円弧状形状のリブ42、断面台形形状のリブ41の順で剛性が強くなる。
The deflection was analyzed for the flat surface 40 on which these were formed, the V-shaped groove 41, the circular-hole arc-shaped groove (rib) 42, and the trapezoidal rib groove 43 (rib) with a slit width of 2.7 mm and a long-side slit 321 with a length of approximately 31 mm. The results are explained using the bar graph in Figure 10.
In [Graph 1] of Figure 10, the long side slits 321 are, from left to right, a slit 40 without a rib 4, a rib 41 with a V-shaped cross section, a rib 42 with an arc-shaped cross section, and a rib 43 with a trapezoidal cross section.The amount of deflection of these long side slits with ribs 4 was analyzed, and the ratio to the deflected portion 3212 on the surface of a flat 40 without a rib was calculated and plotted as a bar graph.
The analysis results show that when the deflection of the flat surface is 0%, and despite the thickness of the fin 3 itself being as thin as 0.15 mm, the rib 41 with a V-shaped cross section deflects only -34%, the rib 42 with a circular arc cross section deflects only -39%, and the rib 43 with a trapezoidal cross section deflects only -48%. In other words, while a considerable degree of rigidity is obtained overall, the rigidity increases in the order of the rib 43 with a V-shaped cross section, the rib 42 with a circular arc cross section, and the rib 41 with a trapezoidal cross section.

次ぎに、本発明の実施例の効果を図11のグラフ2で説明する。
図11のグラフ2で、y1点の状態は従来のスリット表面が平坦である熱交換器のコイルのリブのないスリットフィン40で、フィン取り付けピッチ(FP)3.4mmのときの圧力損失と熱交換効率の関係で、この点を基準(100%)としたとき、スリット表面をV字形状のリブ41とした場合はy2点の状態すなわち圧力損失比率は120%、熱交換効率は128%となり、熱交換効率は28%アップするが、圧力損失も20%アップする。ここで圧力損失を抑えるためにスリット表面をV字形状のリブ41のままフィン取り付けピッチを4.1mmとしたときの状態がy3である。y3の状態では圧力損失はリブなしフィン40と同等で、熱交換効率のみ113%にアップできることが分かる。すなわちスリット表面をV字形状リブ41でフィンピッチを調整することで、圧力損失は従来と同等のまま熱交換効率をアップすることができる。
ここで、本発明の実施例の全体の効果を説明すると、熱交換器のコイルに設けたスリットフィンで、段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造であるので、従来のようにコイルの主管間の距離よりもの短いスリットとは異なり、スリットの長さ方向の長さを主管間よりも長くしたので(図4:X2×2)、長くした分だけ熱交換に関与するので熱交換効率が向上する。
また、隣り合う主管間の距離よりも大きくしたスリットは、スリット上面が平坦だとたわみが生じるので、フィン材3aが0.15mmと薄いにも拘わらずスリットの上面にリブを設けると剛性が増し、たわみが少なくなる。このリブ形状は断面V字状(又は溝)、または、断面円弧状(又は溝)、または、断面台形状(又は溝)としたので、加工が簡単であるにも拘わらず顕著な効果が得られるが、勿論これ以外にも前述した断面形状の組み合わせでも良く、断面波形状でも良く、剛性が増せばどのような形状のリブでも良い。
Next, the effect of the embodiment of the present invention will be explained with reference to graph 2 in FIG.
In graph 2 of Figure 11, point y1 represents the relationship between pressure loss and heat exchange efficiency when a ribbed slit fin 40 is used on a conventional heat exchanger coil with a flat slit surface and a fin mounting pitch (FP) of 3.4 mm. If this point is taken as the reference point (100%), the pressure loss ratio is 120% and the heat exchange efficiency is 128% when the slit surface is fitted with V-shaped ribs 41. This results in a 28% increase in heat exchange efficiency, but also a 20% increase in pressure loss. Here, y3 represents the state where the slit surface is left with V-shaped ribs 41 but the fin mounting pitch is set to 4.1 mm to reduce pressure loss. It can be seen that in the y3 state, pressure loss is equivalent to that of a ribbed fin 40, while heat exchange efficiency alone can be increased to 113%. In other words, by adjusting the fin pitch with V-shaped ribs 41 on the slit surface, heat exchange efficiency can be increased while maintaining the same pressure loss as the conventional system.
Here, the overall effect of the embodiment of the present invention will be explained. The slit fins provided on the coil of the heat exchanger have a slit fin structure that is larger than the distance between adjacent main pipes in the row direction. Therefore, unlike conventional slits that are shorter than the distance between the main pipes of the coil, the length of the slits in the longitudinal direction is longer than the distance between the main pipes (Figure 4: X2 x 2). Since the longer slits participate in heat exchange by the same amount, heat exchange efficiency is improved.
Furthermore, since slits that are larger than the distance between adjacent main pipes will bend if the top surface of the slit is flat, providing ribs on the top surface of the slit increases rigidity and reduces deflection, even though the fin material 3a is only 0.15 mm thin. The rib shape is a V-shaped (or groove) cross section, an arc-shaped (or groove) cross section, or a trapezoidal (or groove) cross section, so a remarkable effect can be obtained despite the simple processing, but of course other ribs may be used, such as a combination of the above cross sections, or a wave-shaped cross section, as long as they increase rigidity.

1・・熱交換器、
2・・コイル、21・・コイル枠体、
22・・ヘッダ、221・・冷温水入口側ヘッダ、222・・冷温水出口側ヘッダ、
23・・冷温水入口、24・・冷温水出口、
25・・主管、26・・Uベンド、
3・・フィン、3a・・フィン材、31・・コイル主管用の貫通孔、32・・スリットフィン、
321・・長辺スリット、3211・・スリット表面とフィンとのすき間(高さ)、
3212・・スリットのたわみ部、
322・・短辺スリット、33・・脚部、
4・・リブ、40・・リブなし(表面平坦)、41・・断面V字状リブ、
42・・断面円弧状リブ、43・・断面台形状リブ
1...Heat exchanger,
2... Coil, 21... Coil frame,
22...Header, 221...Cold and hot water inlet header, 222...Cold and hot water outlet header,
23: Cold and hot water inlet, 24: Cold and hot water outlet,
25...Main pipe, 26...U bend,
3. Fin, 3a. Fin material, 31. Through hole for coil main pipe, 32. Slit fin,
321...Long side slit, 3211...Gap between slit surface and fin (height),
3212...Slit deflection portion,
322... Short side slit, 33... Leg,
4. Rib, 40. No rib (flat surface), 41. V-shaped cross section rib,
42: Rib with arc-shaped cross section, 43: Rib with trapezoidal cross section

Claims (2)

熱交換器のコイルに設けたスリットフィンでコイルの主管の段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造であって、少なくとも主管間の距離よりも大きくしたスリットにおいて、スリットの表面の左右両側には平坦部を設け、スリットの表面の左右中央には長手方向に剛性を高める断面円弧状のリブを設け、断面円弧状のリブを設けるスリットは、そのスリット幅の寸法を2.7mm、スリット高さの寸法を1.3mmにし、断面円弧状のリブは、そのリブ深さの寸法を0.26mm、リブの曲率半径の寸法を1.65mmにしたことを特徴とする熱交換器のコイルのフィン構造。 A fin structure for a heat exchanger coil, characterized in that the slit fins provided on the coil of a heat exchanger are larger than the distance between adjacent main pipes in the direction of the number of stages of the coil, and in that the slits are larger than at least the distance between the main pipes, flat portions are provided on both the left and right sides of the slit surface, and ribs with arc-shaped cross sections are provided in the center of the left and right sides of the slit surface to increase rigidity in the longitudinal direction, the slits with the arc-shaped ribs have a slit width of 2.7 mm and a slit height of 1.3 mm, and the rib with the arc-shaped cross section has a rib depth of 0.26 mm and a rib radius of curvature of 1.65 mm . 熱交換器のコイルに設けたスリットフィンでコイルの主管の段数方向の隣り合う主管間の距離よりも大きくしたスリットフィン構造であって、少なくとも主管間の距離よりも大きくしたスリットにおいて、スリットの表面の左右両側には平坦部を設け、スリットの表面の左右中央には長手方向に剛性を高める断面台形状のリブを設け、断面台形状のリブを設けるスリットは、そのスリット幅の寸法を2.7mm、スリット高さの寸法を1.3mmにし、断面台形状のリブは、その断面台形の深さ寸法を0.2mm、断面台形の底辺の寸法を1.2mm、断面台形の上辺の寸法を1.6mmにしたことを特徴とする熱交換器のコイルのフィン構造。
A fin structure for a heat exchanger coil, characterized in that the slit fins provided on the coil of a heat exchanger are larger than the distance between adjacent main pipes in the direction of the number of stages of the coil, and in that the slits are larger than at least the distance between the main pipes, flat portions are provided on both the left and right sides of the surface of the slit , and ribs with trapezoidal cross sections are provided in the center of the left and right sides of the surface of the slit to increase rigidity in the longitudinal direction, the slits in which the trapezoidal cross section ribs are provided have a slit width of 2.7 mm and a slit height of 1.3 mm, and the trapezoidal cross section ribs have a trapezoidal cross section depth of 0.2 mm, a base dimension of 1.2 mm, and an upper dimension of 1.6 mm .
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Citations (2)

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Publication number Priority date Publication date Assignee Title
US20060005956A1 (en) 2001-06-28 2006-01-12 York International Corporation High-V plate fin heat exchanger and method of manufacturing
JP2006258383A (en) 2005-03-17 2006-09-28 Hitachi Ltd Finned tube heat exchanger

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JPS57100081U (en) * 1980-12-11 1982-06-19
JPS6027280U (en) * 1983-07-26 1985-02-23 株式会社東芝 air heat exchanger
JP2921227B2 (en) * 1990-11-30 1999-07-19 株式会社日立製作所 Finned tube heat exchanger
JPH10300375A (en) * 1997-04-28 1998-11-13 Hitachi Ltd Heat exchanger

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060005956A1 (en) 2001-06-28 2006-01-12 York International Corporation High-V plate fin heat exchanger and method of manufacturing
JP2006258383A (en) 2005-03-17 2006-09-28 Hitachi Ltd Finned tube heat exchanger

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