JP2018112325A - Heat exchanger - Google Patents

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JP2018112325A
JP2018112325A JP2017001281A JP2017001281A JP2018112325A JP 2018112325 A JP2018112325 A JP 2018112325A JP 2017001281 A JP2017001281 A JP 2017001281A JP 2017001281 A JP2017001281 A JP 2017001281A JP 2018112325 A JP2018112325 A JP 2018112325A
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turbulent flow
heat transfer
heat exchanger
casing
shaped
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JP6867676B2 (en
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義生 鈴木
Yoshio Suzuki
義生 鈴木
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Paloma Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To effectively restrict a movement of a turbulence plate with a simple structure excellent in assembly workability.SOLUTION: A heat exchanger 1 includes a casing 2 through which combustion exhaust gas passes from a lower side to an upper side, a plurality of heat transfer pipe parts 4, 4 ... which linearly penetrate through the casing 2 in the horizontal direction, are equally spaced in parallel in a direction orthogonal to a penetration direction, and have respective turbulence plates 10 inside thereof, and a U-shaped connection pipe part (a bent part 5 and a U-shaped tube 6) which connects both ends of the heat transfer pipe parts 4, 4 adjacent to each other in the outside of the casing 2 such that both ends are alternately arranged in a plan view. A insertion end 6a of the U-shaped tube 6 is contacted to one end in a side of the turbulence plate 10 into which the U-shaped tube 6 is inserted and connected, so as to position the turbulence plate 10 in a longer direction.SELECTED DRAWING: Figure 3

Description

本発明は、給湯器等に設けられる熱交換器に関する。   The present invention relates to a heat exchanger provided in a water heater or the like.

給湯器等の熱交換器においては、水等の流体が流れ、外周に複数のフィンを等間隔で備えた蛇行状の配管(フィンパイプ)を有し、フィン間にバーナの燃焼排気を通過させることで、排気熱と配管内の流体との間で熱交換させる。配管内には、特許文献1〜3に開示されるように、配管内での局部沸騰による沸き上がり音の防止と熱効率アップを目的として、切り起こし片を形成したバッフルプレート(乱流板)が挿入されている。   In a heat exchanger such as a water heater, a fluid such as water flows, and has a meandering pipe (fin pipe) having a plurality of fins at equal intervals on the outer periphery, and allows combustion exhaust of a burner to pass between the fins. Thus, heat is exchanged between the exhaust heat and the fluid in the pipe. In the pipe, as disclosed in Patent Documents 1 to 3, a baffle plate (turbulent flow plate) in which cut and raised pieces are formed for the purpose of preventing boiling noise due to local boiling in the pipe and increasing thermal efficiency. Has been inserted.

特許第3678261号公報Japanese Patent No. 3678261 特許第3678262号公報Japanese Patent No. 3678262 特許第3687294号公報Japanese Patent No. 3687294

特許文献1〜3のバッフルプレートは、フィンパイプ内にしまり嵌めして装着しているため、バッフルプレートが流体の付勢により下流側へ移動することがある。また、流体の流量が少ない場合や流体が不凍液等の粘性が高いものである場合、配管内面と接触部分で流れが滞留したりして温度ムラが生じるおそれがある。
さらに、バッフルプレートは、下方からの燃焼排気の流れに対して水平に配設される配管の直線部分では、略水平姿勢(横向き姿勢)で挿入されるが、流れによって回転したバッフルプレートが配管のU字部分に入り込んで垂直姿勢(縦向き姿勢)になってしまうこともある。このように姿勢が変わってしまうと熱効率の向上が期待できない。かといって、バッフルプレートの移動を規制する別の部材を新たに設けると、構造が複雑化して組立作業性も悪くなってしまう。
Since the baffle plates of Patent Documents 1 to 3 are fitted and fitted in the fin pipes, the baffle plates may move downstream due to the urging of fluid. In addition, when the flow rate of the fluid is small or when the fluid has a high viscosity such as an antifreeze liquid, the flow may stay in contact with the inner surface of the pipe, resulting in temperature unevenness.
Further, the baffle plate is inserted in a substantially horizontal posture (lateral posture) in the straight portion of the piping arranged horizontally with respect to the flow of combustion exhaust from below, but the baffle plate rotated by the flow is not connected to the piping. It may enter the U-shaped part and become a vertical posture (vertical posture). If the posture changes in this way, improvement in thermal efficiency cannot be expected. However, if another member for restricting the movement of the baffle plate is newly provided, the structure becomes complicated and the assembling workability becomes worse.

そこで、本発明は、簡単且つ組立作業性の良好な構造で、乱流板の移動を効果的に規制できる熱交換器を提供することを目的としたものである。   SUMMARY OF THE INVENTION An object of the present invention is to provide a heat exchanger that can effectively regulate the movement of a turbulent plate with a simple structure and good assembly workability.

上記目的を達成するために、請求項1に記載の発明は、燃焼排気が下方から上方へ通過するケーシングと、ケーシング内を水平方向へ直線状に貫通して、当該貫通方向との直交方向へ等間隔で並設され、内部に乱流板をそれぞれ挿入した複数の伝熱管部と、ケーシングの外部で隣接する伝熱管部の端部同士を、平面視で両端が互い違いとなるように接続するU字状の接続管部と、を含み、伝熱管部と接続管部とによって、蛇行状に繋がる一連の管体を形成した熱交換器であって、
接続管部の少なくとも一箇所は、隣接する伝熱管部の端部に両端が差込接続される別体のU字管であり、乱流板におけるU字管が差込接続される側の端部に、U字管の差込端部が当接することで乱流板が長手方向に位置決めされていることを特徴とする。
請求項2に記載の発明は、請求項1の構成において、乱流板には、左右へ交互に切り起こし形成される複数の乱流片が設けられていることを特徴とする。
In order to achieve the above object, the invention according to claim 1 is directed to a casing in which combustion exhaust passes from below to above, and through the casing in a straight line in a horizontal direction, in a direction orthogonal to the penetration direction. Connect a plurality of heat transfer tube parts arranged side by side at equal intervals and having turbulent flow plates inserted therein, and the ends of adjacent heat transfer tube parts outside the casing so that both ends are alternated in plan view. A heat exchanger including a U-shaped connecting pipe part, and a heat transfer pipe part and a connecting pipe part forming a series of pipes connected in a meandering manner,
At least one part of the connecting pipe part is a separate U-shaped pipe whose both ends are inserted and connected to the end part of the adjacent heat transfer pipe part, and the end of the turbulent plate on the side where the U-shaped pipe is plugged and connected The turbulent flow plate is positioned in the longitudinal direction by abutting the insertion end portion of the U-shaped tube on the portion.
According to a second aspect of the present invention, in the configuration of the first aspect, the turbulent flow plate is provided with a plurality of turbulent flow pieces that are alternately cut and raised left and right.

請求項1に記載の発明によれば、U字管の差込端部で乱流板を位置決めするので、U字管を利用した簡単且つ組立作業性の良好な構造で、乱流板の移動を効果的に規制することができる。
請求項2に記載の発明によれば、請求項1の効果に加えて、乱流板には、複数の乱流片が設けられているので、温度ムラを抑えることができる。
According to the first aspect of the present invention, since the turbulent flow plate is positioned at the insertion end of the U-shaped tube, the turbulent flow plate can be moved with a simple structure using the U-shaped tube and good workability. Can be effectively regulated.
According to the second aspect of the present invention, in addition to the effect of the first aspect, the turbulent flow plate is provided with a plurality of turbulent pieces, so that temperature unevenness can be suppressed.

熱交換器の正面図である。It is a front view of a heat exchanger. 図1のA−A線断面図である。It is the sectional view on the AA line of FIG. 図1のB−B線断面図である。It is the BB sectional view taken on the line of FIG. 図3のC−C線断面図である。It is CC sectional view taken on the line of FIG. 乱流板の斜視図である。It is a perspective view of a turbulent flow board. 乱流板の説明図で、(A)は側面、(B)は底面をそれぞれ示す。It is explanatory drawing of a turbulent flow board, (A) shows a side surface, (B) shows a bottom face, respectively. 給湯器の概略図である。It is the schematic of a water heater. 乱流板に対する水の流れを示す説明図で、(A)が乱流板10A、(B)が乱流板10Bをそれぞれ示す。It is explanatory drawing which shows the flow of the water with respect to a turbulent flow board, (A) shows 10 A of turbulent flow boards, (B) shows the turbulent flow board 10B, respectively. 変更例の乱流板の斜視図である。It is a perspective view of the turbulent plate of the example of a change. 変更例の乱流板の説明図で、(A)は側面、(B)は底面をそれぞれ示す。It is explanatory drawing of the turbulent plate of the example of a change, (A) shows a side surface, (B) shows a bottom face, respectively. 変更例の乱流板を挿入した熱交換器における図1B−B線と同位置での断面図である。It is sectional drawing in the same position as FIG. 1B-B in the heat exchanger which inserted the turbulent flow board of the example of a change. 図10のD−D線断面図である。It is the DD sectional view taken on the line of FIG.

以下、本発明の実施の形態を図面に基づいて説明する。
図1は、熱交換器の一例を示す正面図、図2はA−A線断面図、図3はB−B線断面図、図4はC−C線断面図である。
この熱交換器1は、四角筒状のケーシング2を有し、ケーシング2内の上部には、左右方向に等間隔をおいて複数枚積層したフィン3,3・・(図3,4では中間部のフィンを省略)と、各フィン3を貫通してケーシング2内部で前後方向へ等間隔をおいて平行に配設される複数の伝熱管部4,4・・とを有する。前後に並ぶ伝熱管部4,4・・は、上下二段(ここでは上段に4本、下段に5本)配設されて、各段で前後に隣接する伝熱管部4,4同士は、一本の長いパイプを中間部位で折り曲げて、接続管部としてのU字状の折曲部5をケーシング2の右側の外部に突出させた状態でケーシング2及びフィン3,3・・を貫通して形成される。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
1 is a front view showing an example of a heat exchanger, FIG. 2 is a cross-sectional view taken along line AA, FIG. 3 is a cross-sectional view taken along line BB, and FIG. 4 is a cross-sectional view taken along line CC.
This heat exchanger 1 has a rectangular cylindrical casing 2 and a plurality of fins 3, 3... (In FIG. 3 and FIG. 4, intermediate layers) are stacked at equal intervals in the left-right direction. And a plurality of heat transfer tube portions 4, 4... That pass through the fins 3 and are arranged in parallel at equal intervals in the front-rear direction inside the casing 2. The heat transfer tube parts 4, 4 arranged in the front and rear are arranged in two upper and lower stages (here, four in the upper stage and five in the lower stage). A long pipe is bent at an intermediate portion, and the casing 2 and the fins 3, 3... Pass through the U-shaped bent part 5 as a connecting pipe part protruding outside the right side of the casing 2. Formed.

一方、ケーシング2の左側では、各段で前後に隣接する伝熱管部4,4同士は、接続管部としてのU字管6の両端を、伝熱管部4,4の端部に差込接続することで連結される。但し、U字管6は、平面視で折曲部5と左右が互い違いとなるように配置される。また、上段最奥の伝熱管部4と下段最奥の伝熱管部4同士は、縦向きのU字管6の両端を差込接続することで連結される。
これにより、ケーシング2内の上部には、上段最前方位置の伝熱管部4から、折曲部5及びU字管6を介して4本の伝熱管部4が蛇行状に連続し、最後方位置の伝熱管部4からU字管6を介して下段へ移り、下段最後方位置の伝熱管部4から折曲部5及びU字管6を介して5本の伝熱管部4が蛇行状に連続する一連の管体7が形成される。
On the other hand, on the left side of the casing 2, the heat transfer tube portions 4 and 4 adjacent to each other at each stage are connected by plugging both ends of the U-shaped tube 6 as a connection tube portion to the end portions of the heat transfer tube portions 4 and 4. To be connected. However, the U-shaped tube 6 is arranged so that the bent portion 5 and the left and right are alternated in plan view. The uppermost rearmost heat transfer tube portion 4 and the lowermost rearmost heat transfer tube portion 4 are connected to each other by plugging and connecting both ends of the vertical U-shaped tube 6.
As a result, the four heat transfer tube portions 4 continue to meander from the heat transfer tube portion 4 in the uppermost frontmost position via the bent portion 5 and the U-shaped tube 6 to the upper part in the casing 2, From the heat transfer tube portion 4 at the position to the lower stage via the U-shaped tube 6, the five heat transfer tube portions 4 meander from the heat transfer tube portion 4 at the rearmost position at the lower stage via the bent portion 5 and the U-shaped tube 6. A series of tube bodies 7 are formed.

そして、各伝熱管部4内には、乱流板10が挿入されている。この乱流板10は、図5に示すように、強度や熱伝導性が高く、耐食性や耐酸化性に優れた金属(例えばニッケル合金系のストリップ材)で、伝熱管部4の内径よりもやや小さい幅で帯板状に形成されている。乱流板10の長手方向の一方の端部は、終端が直線状の四角端部11となり、他方の端部は、終端が半円状の円形端部12となっている。円形端部12には、円形の透孔13,13が、長手方向に2つ並べて形成されている。   A turbulent flow plate 10 is inserted in each heat transfer tube portion 4. As shown in FIG. 5, the turbulent flow plate 10 is a metal (for example, a nickel alloy-based strip material) that has high strength and thermal conductivity and excellent corrosion resistance and oxidation resistance, and is larger than the inner diameter of the heat transfer tube portion 4. It is formed in a strip shape with a slightly smaller width. One end portion in the longitudinal direction of the turbulent flow plate 10 is a square end portion 11 having a linear end, and the other end portion is a circular end portion 12 having a semicircular end. Two circular through holes 13 are formed in the circular end portion 12 side by side in the longitudinal direction.

さらに、乱流板10には、図6にも示すように、四角端部11側が鋭角となり、円形端部12側へ行くに従って上下幅が大きくなる複数の三角孔14,14・・が、等間隔で形成されている。各三角孔14の傾斜縁には、鋭角部分を切り起こした格好で円形端部12側へ向けて幅が拡開する三角形状の乱流片15,15・・が、左右へ交互に突出するように、且つ下向き傾斜姿勢となるように折曲形成されている。各乱流片15の幅広側の先端外側には、小孔16が形成されている。   Further, as shown in FIG. 6, the turbulent flow plate 10 has a plurality of triangular holes 14, 14... That have an acute angle on the square end 11 side and increase in the vertical width toward the circular end 12. It is formed at intervals. Triangular turbulent flow pieces 15, 15... Are alternately projected to the left and right at the inclined edges of the respective triangular holes 14. Thus, it is bent so as to have a downward inclined posture. A small hole 16 is formed outside the wide end of each turbulent flow piece 15.

この乱流板10は、上段の4本の伝熱管部4内へそれぞれ縦向きに挿入される。具体的には、U字管6を差込接続する前の伝熱管部4の左端から、乱流板10を、円形端部12を先にして挿入した後、U字管6を差込接続する。但し、4本の伝熱管部4,4・・間では、同じ縦向きの乱流板10でも、図8(A)に示すように、三角孔14の鋭角部分が上側に位置する向き(乱流片15が左から右に向けて下り傾斜姿勢となる向き、以下、区別する際には「10A」と表記する。)と、同図(B)に示すように、鋭角部分が下側に位置する向き(乱流片15が右から左に向けて下り傾斜姿勢となる向き、以下、区別する際には「10B」と表記する。)とが交互になるように向きを変えて挿入されている。   This turbulent flow plate 10 is inserted vertically into each of the upper four heat transfer tube portions 4. Specifically, after inserting the turbulent flow plate 10 with the circular end 12 first from the left end of the heat transfer tube portion 4 before the U-tube 6 is plugged in, the U-tube 6 is plugged in. To do. However, between the four heat transfer tube portions 4, 4..., Even in the same vertical turbulent flow plate 10, as shown in FIG. The direction in which the flow piece 15 is inclined downward from the left to the right, hereinafter referred to as “10A” when distinguished from each other), and the acute angle portion is on the lower side as shown in FIG. Inserted by changing the orientation so that the orientation (the orientation in which the turbulent flow piece 15 is in a downward inclined posture from right to left, hereinafter referred to as “10B” when distinguished) is alternated. ing.

すると、図3,4に示すように、各U字管6の差込端部6a,6aがそれぞれ四角端部11,11に当接して乱流板10,10を、円形端部12,12が右側の折曲部5内に差し込まれる位置まで押し込む。これにより、各乱流板10は、円形端部12が折曲部5の内面に近接し、四角端部11がU字管6の差込端部6aに当接した状態となって長手方向の移動が規制される。このとき乱流板10の下縁は、伝熱管部4の下側の内面に当接し、各乱流片15は、先端が伝熱管部4の左右の内面に当接した状態となるため、乱流板10の回転も規制される。   Then, as shown in FIGS. 3 and 4, the insertion end portions 6 a and 6 a of the U-tubes 6 abut against the square end portions 11 and 11, respectively, so that the turbulent flow plates 10 and 10 are replaced with the circular end portions 12 and 12. Is pushed to the position where it is inserted into the bent portion 5 on the right side. Thereby, each turbulent flow plate 10 is in a state where the circular end portion 12 is close to the inner surface of the bent portion 5 and the square end portion 11 is in contact with the insertion end portion 6a of the U-shaped tube 6 in the longitudinal direction. Movement is restricted. At this time, the lower edge of the turbulent flow plate 10 is in contact with the lower inner surface of the heat transfer tube portion 4, and each turbulent flow piece 15 is in a state of being in contact with the left and right inner surfaces of the heat transfer tube portion 4, The rotation of the turbulent plate 10 is also restricted.

以上の如く構成された熱交換器1は、例えば図7に示すように、給湯器20の筐体21内において、複数のバーナ群を内設するバーナユニット22の上部に組み付けられる。熱交換器1の上部には、排気フード23が組み付けられる。これにより、バーナユニット22内のバーナ群の燃焼排気が、熱交換器1のケーシング2内を上昇して各フィン3,3間を通過して排気フード23に至る燃焼室(内胴)が形成される。また、熱交換器1の管体7の上流端には、外部の水道管と接続される入水管24が接続され、管体7の下流端には、給湯栓に繋がる配管が接続される出湯管25が接続される。26はバーナユニット22への給気ファン、27はコントローラである。   For example, as shown in FIG. 7, the heat exchanger 1 configured as described above is assembled in an upper portion of a burner unit 22 in which a plurality of burner groups are provided in a housing 21 of a water heater 20. An exhaust hood 23 is assembled on the top of the heat exchanger 1. As a result, a combustion chamber (inner cylinder) is formed in which the combustion exhaust from the burner group in the burner unit 22 rises in the casing 2 of the heat exchanger 1 and passes between the fins 3 and 3 to reach the exhaust hood 23. Is done. In addition, an inlet pipe 24 connected to an external water pipe is connected to the upstream end of the pipe body 7 of the heat exchanger 1, and a hot water outlet connected to a pipe connected to the hot water tap is connected to the downstream end of the pipe body 7. A tube 25 is connected. 26 is a fan for supplying air to the burner unit 22, and 27 is a controller.

この給湯器20において、給湯栓を開栓して器具内に通水させると、水が入水管24を通って熱交換器1の管体7に至り、各伝熱管部4.4・・を順番に通過する。一方、コントローラ27が通水を検知してバーナユニット22内のバーナ群に点火すると共に、給気ファン26を回転させてバーナ群に燃焼用空気を供給する。バーナ群の燃焼排気は、熱交換器1のケーシング2内を上昇してフィン3,3間を通過することで伝熱管部4を通過する水と熱交換される。よって、出湯管25から所定温度の湯が出湯され、給湯栓から供給される。   In this water heater 20, when the hot water tap is opened and water is passed through the appliance, the water passes through the water inlet pipe 24 to the tube body 7 of the heat exchanger 1, and each heat transfer pipe section 4.4. Pass in order. On the other hand, the controller 27 detects water flow and ignites the burner group in the burner unit 22 and rotates the air supply fan 26 to supply combustion air to the burner group. The combustion exhaust of the burner group is exchanged with the water passing through the heat transfer pipe section 4 by rising in the casing 2 of the heat exchanger 1 and passing between the fins 3 and 3. Therefore, hot water of a predetermined temperature is discharged from the hot water discharge pipe 25 and supplied from the hot water tap.

各伝熱管部4では、図3に示す実線矢印方向に水が通過することになるが、ここで、水がU字管6を通って四角端部11側から流入した場合、乱流板10Aの左右を通りつつ乱流片15,15と当接した水の一部は、図8(A)に二点鎖線矢印で示すように、乱流片15の下向き傾斜姿勢によって下方へ導かれる。よって、伝熱管部4の下側内面に衝突して乱流を生じさせる。各乱流片15の小孔16を通ることでも流速が部分的に変化して乱流を生じさせる。また、水の一部は三角孔14を通過することで乱流板10Aの左右に行き来して乱流を生じさせる。
また、水が折曲部5を通って円形端部12側から流入した場合、水は、乱流板10Bの円形端部13の外側若しくは透孔13,13を通って伝熱管部4内に流れる。そして、乱流板10Bの左右を流れつつ乱流片15,15と当接した水の一部は、図8(B)に二点鎖線矢印で示すように、乱流片15の下向き傾斜姿勢によって下方へ導かれ、伝熱管部4の下側内面に衝突して乱流を生じさせる。各乱流片15の小孔16を通ることでも流速が部分的に変化して乱流を生じさせる。また、水の一部は三角孔14を通過することで乱流板10Bの左右に行き来して乱流を生じさせる。
In each heat transfer tube portion 4, water passes in the direction of the solid arrow shown in FIG. 3. Here, when water flows from the square end 11 side through the U-shaped tube 6, the turbulent flow plate 10 </ b> A. A part of the water that has contacted the turbulent flow pieces 15 and 15 while passing through the left and right sides of the turbulent flow is guided downward by a downward inclined posture of the turbulent flow pieces 15 as indicated by a two-dot chain line arrow in FIG. Therefore, it collides with the lower inner surface of the heat transfer tube portion 4 to generate turbulent flow. Even through the small holes 16 of the turbulent flow pieces 15, the flow velocity is partially changed to generate turbulent flow. Further, part of the water passes through the triangular hole 14 so as to go to the left and right of the turbulent flow plate 10A to generate turbulent flow.
Further, when water flows from the circular end 12 side through the bent portion 5, the water enters the heat transfer tube portion 4 outside the circular end portion 13 of the turbulent flow plate 10 </ b> B or through the through holes 13 and 13. Flowing. Then, a part of the water that is in contact with the turbulent flow pieces 15 and 15 while flowing on the left and right of the turbulent flow plate 10B is inclined downward as shown by a two-dot chain line arrow in FIG. Is caused to collide with the lower inner surface of the heat transfer tube section 4 to generate turbulent flow. Even through the small holes 16 of the turbulent flow pieces 15, the flow velocity is partially changed to generate turbulent flow. Further, a part of the water passes through the triangular hole 14 so as to go to the left and right of the turbulent flow plate 10B to generate turbulent flow.

このように水が下向き傾斜した乱流片15によって常に下方へ向けられるので、流量が少ない場合でも下方から上昇する燃焼排気との熱交換が効率よく行われ、伝熱管部4の長手方向での温度ムラが抑えられる。
一方、このように伝熱管部4内を水が乱流片15に当接しながら通過することで、乱流板10は水の下流側へ付勢されるが、四角端部11側から流入した場合、乱流板10は円形端部12が折曲部5の内面に当接して移動規制され、円形端部12側から流入した場合、乱流板10は四角端部11がU字管6の差込端部6aに当接することで移動規制される。よって、乱流板10が伝熱管部4内で移動したり回転したりすることがない。
Since the water is always directed downward by the turbulent flow piece 15 inclined downward in this way, even when the flow rate is small, heat exchange with the combustion exhaust rising from below is efficiently performed, and the heat transfer tube portion 4 in the longitudinal direction Temperature unevenness can be suppressed.
On the other hand, as the water passes through the heat transfer tube portion 4 in contact with the turbulent flow piece 15 in this way, the turbulent flow plate 10 is urged to the downstream side of the water, but flows in from the square end portion 11 side. In this case, the turbulent flow plate 10 has its circular end 12 abutted against the inner surface of the bent portion 5 and is restricted from moving. When the turbulent flow plate 10 flows from the circular end 12 side, the square end 11 of the turbulent flow plate 10 has a U-shaped tube 6. The movement is restricted by coming into contact with the insertion end 6a. Therefore, the turbulent flow plate 10 does not move or rotate in the heat transfer tube portion 4.

(円形端部による乱流板の移動及び回転規制に係る発明の効果)
このように、上記形態の熱交換器1によれば、乱流板10の一方の端部は、接続管部(折曲部5又はU字管6)内まで差し込まれて当該接続管部の内面に近接又は当接する半円形状の円形端部12となっているので、水の流れによって乱流板10が移動したり回転したりすることがない。また、これは乱流板10に円形端部12を形成して接続管部内に差し込むだけで足り、ロウ付け等の固定手段が不要となるため、部品点数の少ない簡単な構造となり、且つ組立作業性も良好な構造となる。
(Effect of invention relating to movement and rotation regulation of turbulent plate by circular end)
Thus, according to the heat exchanger 1 of the said form, one edge part of the turbulent flow board 10 is inserted in the connection pipe part (the bending part 5 or the U-shaped pipe 6), and the said connection pipe part is connected. Since it is the semicircular circular end portion 12 that is close to or in contact with the inner surface, the turbulent flow plate 10 is not moved or rotated by the flow of water. In addition, it is only necessary to form the circular end 12 on the turbulent flow plate 10 and insert it into the connecting pipe portion, and no fixing means such as brazing is required. The structure is also good.

特にここでは、乱流板10における接続管部内への差込部分には、透孔13,13が形成されているので、円形端部12を接続管部内へ差し込んでも水の流入を必要以上に妨げることがない。
また、乱流板10には、左右へ交互に切り起こし形成される複数の乱流片15,15が設けられているので、伝熱管部4の長手方向での温度ムラの発生を抑えることができる。
In particular, here, since the through holes 13 and 13 are formed in the insertion portion of the turbulent flow plate 10 into the connecting pipe portion, even if the circular end portion 12 is inserted into the connecting pipe portion, the inflow of water is more than necessary. There is no hindrance.
Moreover, since the turbulent flow plate 10 is provided with a plurality of turbulent flow pieces 15 and 15 which are alternately cut and raised to the left and right, the occurrence of temperature unevenness in the longitudinal direction of the heat transfer tube portion 4 can be suppressed. it can.

なお、上記形態では、乱流板の四角端部の移動規制にU字管の差込端部を利用しているが、これに限らず、伝熱管部やU字管の内面に突設した突起やリブ等を利用してもよい。伝熱管部の内面を利用した場合、四角端部側は別体のU字管である必要はなくなる。
但し、乱流板の一方の端部のみを円形端部とする構造に限らず、図9,10に示す乱流板10のように、両端を円形端部12,12として透孔13,13を設けてもよい。この場合、伝熱管部4では、図11,12に示すように、一方の円形端部12が折曲部5の内面に近接し、他方の円形端部12がU字管6の内面に近接するように挿入することで、伝熱管部4内での長手方向の移動規制は可能である。
この構造であれば、U字管6の差込端部を利用しなくても乱流板10の移動規制が可能となる。
In addition, in the said form, although the insertion end part of a U-shaped tube is utilized for the movement restriction | limiting of the square end part of a turbulent flow board, it protruded on the inner surface of not only this but a heat-transfer tube part or a U-shaped tube. A protrusion, a rib, or the like may be used. When the inner surface of the heat transfer tube portion is used, the square end portion side does not need to be a separate U-shaped tube.
However, it is not limited to a structure in which only one end of the turbulent flow plate is a circular end, but as in the turbulent flow plate 10 shown in FIGS. May be provided. In this case, in the heat transfer tube portion 4, as shown in FIGS. 11 and 12, one circular end portion 12 is close to the inner surface of the bent portion 5, and the other circular end portion 12 is close to the inner surface of the U-shaped tube 6. By inserting in such a manner, movement in the longitudinal direction within the heat transfer tube portion 4 can be regulated.
With this structure, the movement of the turbulent flow plate 10 can be restricted without using the insertion end of the U-shaped tube 6.

また、この発明では、透孔の数や形状、三角孔及び乱流片の数や形状も適宜変更可能である。
さらに、上記形態では、水平方向で蛇行する管体の伝熱管部に乱流板を縦向きに挿入しているが、上下の伝熱管部を縦向きの接続管部で接続する場合、乱流板を横向きに挿入して長手方向の一端又は両端を接続管部に差し込むようにしてもよい。この場合も円形端部が縦向きの接続管部の内面に近接又は当接することで長手方向の移動規制が可能となる。
Moreover, in this invention, the number and shape of a through-hole and the number and shape of a triangular hole and a turbulent flow piece can also be changed suitably.
Furthermore, in the above embodiment, the turbulent flow plate is inserted vertically into the heat transfer tube portion of the tube meandering in the horizontal direction, but when the upper and lower heat transfer tube portions are connected by the vertical connection tube portion, the turbulent flow You may make it insert a board | plate sideways and insert one end or both ends of a longitudinal direction in a connection pipe part. Also in this case, the movement in the longitudinal direction can be restricted by the circular end portion approaching or abutting against the inner surface of the vertically connecting pipe portion.

(下向き傾斜姿勢の乱流片に係る発明の効果)
上記形態の熱交換器1によれば、乱流板10は、伝熱管部4へ縦向きに挿入され、乱流板10には、複数の乱流片15,15・・が左右へ交互に切り起こし形成されていると共に、各乱流片15は全て下流側への下向き傾斜姿勢で設けられているので、水が下向き傾斜した乱流片15によって常に下方へ向けられ、流量が少ない場合でも下方から上昇する燃焼排気との熱交換が効率よく行われる。よって、伝熱管部4の長手方向での温度ムラが抑えられて熱効率が向上する。
(Effect of the invention relating to the turbulent piece in the downward inclined posture)
According to the heat exchanger 1 of the said form, the turbulent flow plate 10 is inserted vertically into the heat exchanger tube part 4, and the turbulent flow plate 10 has a plurality of turbulent flow pieces 15, 15,. Since all the turbulent flow pieces 15 are provided in a downwardly inclined posture toward the downstream side, the water is always directed downward by the downwardly inclined turbulent flow pieces 15 even when the flow rate is small. Heat exchange with the combustion exhaust rising from below is efficiently performed. Therefore, the temperature unevenness in the longitudinal direction of the heat transfer tube portion 4 is suppressed, and the thermal efficiency is improved.

なお、上記形態では、同じ形態の乱流板10を用いて、各伝熱管部4内に交互に向きを変えて挿入しているが、水の流れを下向きに案内する乱流片を備えたものであれば、透孔の形状や三角孔及び乱流片の数や形状等が異なる乱流板を交互又は各伝熱管部ごとに用いてもよい。   In the above-described embodiment, the turbulent flow plate 10 having the same configuration is used, and the turbulent flow pieces 10 are alternately inserted into the respective heat transfer tube portions 4. As long as it is a thing, you may use the turbulent flow board from which the shape of a through-hole, a triangular hole, and the number and shape of a turbulent flow piece differ, or for every heat exchanger tube part.

(U字管による乱流板の移動規制に係る発明の効果)
上記形態の熱交換器1によれば、管体7における接続管部の複数箇所を、隣接する伝熱管部4,4の端部に両端が差込接続される別体のU字管6として、乱流板10におけるU字管6が差込接続される側の端部に、U字管6の差込端部6aが当接することで乱流板10が位置決めされているので、U字管6を利用した簡単且つ組立作業性の良好な構造で、乱流板10の移動を効果的に規制することができる。
(Effect of invention relating to movement restriction of turbulent plate by U-shaped tube)
According to the heat exchanger 1 of the said form, the several places of the connection pipe part in the pipe body 7 are set as the separate U-shaped pipe 6 by which both ends are inserted and connected to the edge part of the adjacent heat transfer pipe parts 4 and 4. The turbulent flow plate 10 is positioned by the contact of the insertion end 6a of the U-shaped tube 6 with the end of the turbulent flow plate 10 on the side where the U-shaped tube 6 is inserted and connected. The movement of the turbulent plate 10 can be effectively restricted with a simple structure using the tube 6 and good assembly workability.

なお、上記形態では、平面視左側にのみU字管を用いて伝熱管部同士を連結しているが、右側にもU字管を用いて連結し、乱流板の両端をU字管の差込端部で挟む格好として乱流板の移動規制を行うようにしてもよい。   In addition, in the said form, although the heat exchanger tube parts are connected only using the U-shaped tube on the left side in a plan view, the right side is also connected using the U-shaped tube, and both ends of the turbulent flow plate are connected to the U-shaped tube. You may make it perform movement restriction | limiting of a turbulent flow board as appearance put on an insertion edge part.

そして、各発明に共通して、熱交換器を設ける給湯器も、副熱交換器を有する潜熱回収型や、風呂の追い焚きや床暖房用の熱交換器を併設した二缶型等であっても本発明は適用できる。潜熱回収型では、少なくとも主熱交換器に本発明を適用すればよいし、二缶型であれば併設される双方の熱交換器に本発明を適用すればよい。
勿論給湯器に限らず、ロードヒータ等の他の器具であっても、流体と燃焼排気とを熱交換する熱交換器を有するものであれば、本発明の熱交換器は採用可能である。
In common with each invention, the water heater provided with a heat exchanger is also a latent heat recovery type having a sub-heat exchanger, a two-can type with a heat exchanger for bathing and floor heating, and the like. However, the present invention can be applied. In the latent heat recovery type, the present invention may be applied to at least the main heat exchanger, and in the case of a two-can type, the present invention may be applied to both heat exchangers provided side by side.
Of course, the heat exchanger of the present invention can be used not only for the water heater but also for other equipment such as a road heater as long as it has a heat exchanger for exchanging heat between the fluid and the combustion exhaust.

1・・熱交換器、2・・ケーシング、3・・フィン、4・・伝熱管部、5・・折曲部、6・・U字管、6a・・差込端部、7・・管体、10・・乱流板、11・・四角端部、12・・円形端部、13・・透孔、14・・三角孔、15・・乱流片、16・・小孔、20・・給湯器、21・・筐体、22・・バーナユニット、23・・排気フード、24・・入水管、25・・出湯管。   1. Heat exchanger 2. Casing 3. Fin 4. Heat transfer tube 5. Folding 6. U-tube 6a ... Insertion end 7. Tube Body 10 ... Turbulent plate 11, Square end 12 ... Circular end 13 ... Through hole 14 ... Triangular hole 15 ... Turbulent piece 16 ... Small hole 20 ... -Hot water heater, 21-Housing, 22-Burner unit, 23-Exhaust hood, 24-Water inlet pipe, 25-Hot water pipe.

Claims (2)

燃焼排気が下方から上方へ通過するケーシングと、
前記ケーシング内を水平方向へ直線状に貫通して、当該貫通方向との直交方向へ等間隔で並設され、内部に乱流板をそれぞれ挿入した複数の伝熱管部と、
前記ケーシングの外部で隣接する前記伝熱管部の端部同士を、平面視で両端が互い違いとなるように接続するU字状の接続管部と、を含み、前記伝熱管部と前記接続管部とによって、蛇行状に繋がる一連の管体を形成した熱交換器であって、
前記接続管部の少なくとも一箇所は、隣接する前記伝熱管部の端部に両端が差込接続される別体のU字管であり、前記乱流板における前記U字管が差込接続される側の端部に、前記U字管の差込端部が当接することで前記乱流板が長手方向に位置決めされていることを特徴とする熱交換器。
A casing through which combustion exhaust passes from below to above;
A plurality of heat transfer tube portions, which pass through the casing in a straight line in the horizontal direction, are arranged in parallel at equal intervals in a direction orthogonal to the penetration direction, and each has a turbulent flow plate inserted therein.
A U-shaped connecting pipe part that connects the ends of the heat transfer pipe parts adjacent to each other outside the casing so that both ends thereof are alternated in a plan view, and the heat transfer pipe part and the connecting pipe part And a heat exchanger that forms a series of pipes connected in a meandering manner,
At least one place of the connecting pipe part is a separate U-shaped pipe whose both ends are inserted and connected to the end part of the adjacent heat transfer pipe part, and the U-shaped pipe in the turbulent flow plate is plugged and connected. The heat exchanger is characterized in that the turbulent plate is positioned in the longitudinal direction by the end of the U-shaped tube coming into contact with the end of the U-tube.
前記乱流板には、左右へ交互に切り起こし形成される複数の乱流片が設けられていることを特徴とする請求項1に記載の熱交換器。   The heat exchanger according to claim 1, wherein the turbulent flow plate is provided with a plurality of turbulent pieces that are alternately cut and raised to the left and right.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2852042A (en) * 1951-04-07 1958-09-16 Garrett Corp Turbulator
US3036818A (en) * 1958-01-29 1962-05-29 Foster Wheeler Francaise Soc Heat exchanger
JPS648072U (en) * 1987-06-26 1989-01-17
JP3678261B2 (en) * 1997-08-29 2005-08-03 株式会社ノーリツ Fin pipe turbulence generator
JP2006052864A (en) * 2004-08-09 2006-02-23 Toshiba Kyaria Kk Heat exchanger
JP2015224804A (en) * 2014-05-26 2015-12-14 株式会社ノーリツ Heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2852042A (en) * 1951-04-07 1958-09-16 Garrett Corp Turbulator
US3036818A (en) * 1958-01-29 1962-05-29 Foster Wheeler Francaise Soc Heat exchanger
JPS648072U (en) * 1987-06-26 1989-01-17
JP3678261B2 (en) * 1997-08-29 2005-08-03 株式会社ノーリツ Fin pipe turbulence generator
JP2006052864A (en) * 2004-08-09 2006-02-23 Toshiba Kyaria Kk Heat exchanger
JP2015224804A (en) * 2014-05-26 2015-12-14 株式会社ノーリツ Heat exchanger

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