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JP2012122663A - Heat exchanger and water heater using the same - Google Patents

Heat exchanger and water heater using the same Download PDF

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JP2012122663A
JP2012122663A JP2010273657A JP2010273657A JP2012122663A JP 2012122663 A JP2012122663 A JP 2012122663A JP 2010273657 A JP2010273657 A JP 2010273657A JP 2010273657 A JP2010273657 A JP 2010273657A JP 2012122663 A JP2012122663 A JP 2012122663A
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heat exchanger
heat exchange
exchange unit
heated liquid
heated
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Hiroki Kanazawa
広輝 金澤
Yoshio Ando
芳生 安藤
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Paloma Co Ltd
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Paloma Co Ltd
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  • Details Of Fluid Heaters (AREA)
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Abstract

PROBLEM TO BE SOLVED: To provide a heat exchanger and a water heater using the heat exchanger having a high degree of freedom in setting positions to provide an inflow port and an outflow port of a heated liquid.SOLUTION: A heat exchange unit 64 is formed by joining the outer peripheral edges of two plate-like members 66 to each other, and the heat exchange units 64 are stacked to constitute the heat exchanger. Communicating parts 68 serving for communication between heated liquid passages 220 of the heat exchange units 64 are formed at two parts between the adjacent heat exchange units 64. A transverse part 76 formed by the contact or approach of recesses 74 provided at the two plate-like members 66 interrupts a flow of bath water that flows into the heated liquid passage 220 from one of the communicating parts 68 and is going to short-circuit to the other of the communicating parts 68. The heated liquid passage 220 is thereby formed in annular shape. The passage width L of the heated liquid passage 220 on both sides of a transverse direction of the transverse part 76 with the transverse part 76 held in between is equal to the passage width L of heated liquid passage 220 on both sides of a direction orthogonal to the transverse direction with the transverse part 76 held in between.

Description

本発明は、積層型の熱交換器およびそれを用いた給湯器に関する。   The present invention relates to a stacked heat exchanger and a water heater using the same.

従来の熱交換器として、特許文献1に開示されているように、2枚のチューブプレートを接合して形成したチューブを複数積層し、熱交換器を形成するものが知られている。
特許文献1の熱交換器では、U字状または直線状に形成されたチューブとチューブとの間に、隣接するチューブの流路を連通する連通部を2箇所設けており、積層方向の一端側のチューブにおいて、2箇所設けられた連通部と同じ積層方向上に、被加熱液である給湯水の給湯口と出湯口とが設けられている。
As a conventional heat exchanger, as disclosed in Patent Document 1, a heat exchanger is formed by stacking a plurality of tubes formed by joining two tube plates.
In the heat exchanger of Patent Document 1, two communication portions that communicate the flow paths of adjacent tubes are provided between the tubes formed in a U shape or a straight line, and one end side in the stacking direction. In the tube, hot water supply hot water outlets and hot water outlets are provided on the same stacking direction as the two communicating portions.

給湯口から熱交換器内に流入した給湯水は、チューブ間においては、給湯口と同じ積層方向上の連通部を通り、出湯口と同じ積層方向上の連通部を通って出湯口から流出する。各チューブ内においては、2箇所設けられた連通部の一方から流入した給湯水は他方の連通部に向けて流れる。   Hot water flowing into the heat exchanger from the hot water supply port passes through the communication portion in the same stacking direction as the hot water supply port between the tubes, and flows out from the hot water outlet through the communication portion in the same stacking direction as the hot water outlet. . In each tube, hot water supplied from one of the two communication portions is directed toward the other communication portion.

特開2004−125189号公報JP 2004-125189 A

しかしながら、特許文献1の熱交換器のように、両端が閉塞したU字状または直線状のチューブでは、チューブが形成する流路にデッドスペースができないように、2箇所の連通部をチューブの両端側に設け、連通部に合わせて熱交換器の給湯口および出湯口をチューブの両端側に形成する必要がある。   However, as in the heat exchanger of Patent Document 1, in a U-shaped or linear tube whose both ends are closed, two communicating portions are connected to both ends of the tube so that there is no dead space in the flow path formed by the tube. It is necessary to form the hot water supply port and the hot water outlet of the heat exchanger on both ends of the tube in accordance with the communication portion.

このように、チューブの両端側に被加熱液が流入する流入口と被加熱液が流出する流出口とを設ける熱交換器の構成では、流入口および流出口を設ける位置が固定されるので、熱交換器を設置するスペース、ならびに熱交換器の周囲に設置される部品に合わせて、熱交換器に流入口および流出口を設ける位置を自由に設定できない。   Thus, in the configuration of the heat exchanger that provides the inlet into which the liquid to be heated flows in and the outlet from which the liquid to be heated flows out at both ends of the tube, the positions where the inlet and the outlet are provided are fixed. In accordance with the space where the heat exchanger is installed and the parts installed around the heat exchanger, the positions where the inlet and the outlet are provided in the heat exchanger cannot be freely set.

その結果、配管を熱交換器の流入口および流出口に接続する位置が固定されるので、熱交換器に配管を接続するときの配管の取り回しの自由度が低いという問題が生じる。
本発明は、上記問題を解決するためになされたものであり、被加熱液の流入口および流出口を設ける位置の自由度が高い熱交換器およびそれを用いた給湯器を提供することを目的とする。
As a result, the position where the pipe is connected to the inlet and the outlet of the heat exchanger is fixed, which causes a problem that the degree of freedom of the piping when connecting the pipe to the heat exchanger is low.
The present invention has been made to solve the above-described problem, and an object of the present invention is to provide a heat exchanger having a high degree of freedom in positions where the inlet and outlet of the liquid to be heated are provided, and a water heater using the heat exchanger. And

請求項1から7に記載の発明では、2枚の板状部材の外周縁部同士を接合して各熱交換ユニットが形成されて各熱交換ユニットが内部に扁平な被加熱液流路を有し、熱交換ユニットの厚み方向に積層されており、隣接する熱交換ユニットの間に、バーナにより発生する燃焼ガスが通過するガス流路を形成している熱交換ユニット群と、ガス流路を横切って2箇所に設けられ、隣接する熱交換ユニットの被加熱液流路同士を連通する連通部と、を備え、積層方向の一端側の熱交換ユニットにおいて、積層方向に対して連通部が設けられている側と反対側の板状部材に、被加熱液の流入口と流出口とが設けられており、熱交換ユニットは、被加熱液流路において、2箇所に設けられた連通部の間を横断して設けられ、2箇所に設けられた連通部の間を短絡しようとする被加熱液の流れを妨害することにより被加熱液流路を環状に形成する横断部を有している。   In the invention according to any one of claims 1 to 7, the heat exchange units are formed by joining the outer peripheral edge portions of the two plate-like members, and each heat exchange unit has a flat liquid flow path to be heated. A heat exchange unit group which is stacked in the thickness direction of the heat exchange unit, and forms a gas flow path through which the combustion gas generated by the burner passes between adjacent heat exchange units, and a gas flow path. And a communication portion that is provided at two locations across and communicates between the liquid flow paths to be heated of adjacent heat exchange units. In the heat exchange unit on one end side in the stacking direction, the communication portion is provided in the stacking direction. An inflow port and an outflow port for the liquid to be heated are provided on the plate-like member opposite to the side on which the heat is supplied, and the heat exchange unit is connected to the communication portion provided at two locations in the liquid flow path to be heated. Of the communication part provided in two places. And a heated liquid flow path has a cross section which forms the annular by interfering with the flow of the heated liquid to be short-circuited.

この構成によれば、2箇所に設けられた連通部の一方から被加熱液流路に流入した被加熱液は、連通部の間を短絡しようとする流れを横断部に妨害されるので、被加熱液流路を横断部の横断方向両側に分かれて環状に流れ、他方の連通部で合流する。   According to this configuration, the liquid to be heated that has flowed into the liquid flow path to be heated from one of the communication portions provided at two places is obstructed by the crossing portion in a flow that attempts to short-circuit between the communication portions. The heating liquid flow path is divided into both sides in the transverse direction of the transverse part and flows in an annular shape, and merges at the other communicating part.

したがって、環状の被加熱液流路の周上で連通部を設ける位置、つまり被加熱液の流入口および流出口を設ける位置を変更しても、被加熱液流路にデッドスペースが生じることなく、被加熱液が環状の被加熱液流路を流れる。これにより、被加熱液の流入口および流出口を熱交換器に設ける位置の自由度が高くなるので、熱交換器に接続する配管の取り回しの自由度が高くなる。   Therefore, even if the position where the communication portion is provided on the circumference of the annular heated liquid channel, that is, the position where the inlet and outlet of the heated liquid are changed, dead space does not occur in the heated liquid channel. The heated liquid flows through the annular heated liquid flow path. Thereby, since the freedom degree of the position which provides the inflow port and outflow port of a to-be-heated liquid in a heat exchanger becomes high, the freedom degree of the handling of piping connected to a heat exchanger becomes high.

請求項2に記載の発明では、横断部は、被加熱液流路の中心部に形成されている。
これにより、一方の連通部から被加熱液流路に流入し、横断部の横断方向両側の被加熱液流路に分かれて他方の連通部で合流する被加熱液の流量が、横断部の横断方向両側の被加熱液流路でほぼ等しくなる。その結果、横断部の横断方向両側の被加熱液流路を流れる被加熱液が熱交換ユニットにおいて均等に加熱される。
In the invention according to claim 2, the transverse portion is formed at the center of the heated liquid channel.
As a result, the flow rate of the liquid to be heated that flows into the heated liquid flow path from one communicating portion, is divided into the heated liquid flow paths on both sides in the transverse direction of the transverse portion, and merges at the other communicating portion is It becomes almost equal in the heated liquid flow path on both sides in the direction. As a result, the to-be-heated liquid which flows through the to-be-heated liquid flow path of the transverse direction both sides of a crossing part is heated equally in a heat exchange unit.

請求項3に記載の発明では、2箇所に設けられた連通部は横断部を中心として点対称の位置に配置されている。
この構成によれば、熱交換ユニットを180°回転しても2箇所に設けられた連通部の位置は変化しないので、熱交換ユニットを半回転しても連通部の位置を一致させて熱交換ユニットを積層できる。これにより、熱交換ユニットの回転位置を考慮せずに熱交換ユニットを積層できるので、熱交換器を容易に製造できる。
According to the third aspect of the present invention, the communication portions provided at two places are arranged at point-symmetrical positions with the crossing portion as the center.
According to this configuration, even if the heat exchange unit is rotated by 180 °, the positions of the communication portions provided at the two positions do not change. Therefore, even if the heat exchange unit is rotated halfway, the positions of the communication portions are matched to perform heat exchange. Units can be stacked. Thereby, since a heat exchange unit can be laminated | stacked without considering the rotation position of a heat exchange unit, a heat exchanger can be manufactured easily.

請求項4に記載の発明では、2箇所の各箇所に設けられた連通部と、各箇所の連通部と同じ積層方向上にそれぞれ設けられた流入口および流出口とは、被加熱液流路を形成する熱交換ユニットの内壁面の内周縁と接している。   In the invention according to claim 4, the communicating portion provided at each of the two locations, and the inlet and the outlet provided on the same stacking direction as the communicating portions at each location are the heated liquid channel. Is in contact with the inner peripheral edge of the inner wall surface of the heat exchange unit.

この構成によれば、流入口または流出口の一方が下、他方が上になるように熱交換器を取り付ける場合、下側に位置する流入口または流出口の一方と、流入口または流出口の一方と同じ積層方向上に設けられた連通部と、被加熱液流路との下端位置が一致する。   According to this configuration, when the heat exchanger is mounted so that one of the inlet or the outlet is on the lower side and the other is on the upper side, one of the inlet or the outlet located on the lower side and the inlet or the outlet are arranged. The lower end positions of the communicating portion provided on the same stacking direction as the one and the heated liquid flow path coincide with each other.

これにより、熱交換器を取付けた機器から被加熱液を抜く操作、例えば給湯器の場合には周知の水抜き操作を実行すると、被加熱液流路の被加熱液は連通部および被加熱液流路に溜まらず、下側に位置する流入口または流出口の一方から熱交換器の外部に流れ出る。その結果、熱交換器内で被加熱液が凍結することを防止できる。さらに、被加熱液に含まれる異物および汚れが被加熱液とともに熱交換器から流れ出るので、熱交換器内に異物および汚れが堆積することを防止できる。   As a result, when an operation for extracting the liquid to be heated from the device to which the heat exchanger is attached, for example, in the case of a water heater, a well-known water draining operation is performed, the liquid to be heated in the liquid channel to be heated It does not accumulate in the flow path but flows out of the heat exchanger from one of the inlet or outlet located on the lower side. As a result, the liquid to be heated can be prevented from freezing in the heat exchanger. Furthermore, since the foreign material and dirt contained in the liquid to be heated flow out of the heat exchanger together with the liquid to be heated, it is possible to prevent the foreign material and dirt from accumulating in the heat exchanger.

請求項5に記載の発明では、2箇所のうち一方に設けられた連通部および流入口、ならびに2箇所のうち他方に設けられた連通部および流出口にそれぞれ接している熱交換ユニットの内壁面は、連通部と内壁面の内周縁とが接する箇所を通る接線に対して接する箇所の両側の内壁面をそれぞれ所定角度傾斜させることにより凹部を形成している。   In the invention according to claim 5, the inner wall surface of the heat exchange unit that is in contact with the communication portion and the inlet provided in one of the two locations, and the communication portion and the outlet provided in the other of the two locations, respectively. Has a concave portion formed by inclining the inner wall surfaces on both sides of a portion in contact with a tangent passing through a portion where the communication portion and the inner peripheral edge of the inner wall surface are in contact with each other by a predetermined angle.

この構成によれば、流入口または流出口の一方が下、他方が上になるように熱交換器を取り付けるときに、熱交換ユニットの積層方向を軸として熱交換器の回転方向の取付け位置が多少ずれても、熱交換器を取付けた機器から被加熱液を抜く操作を実行すると、下側に位置する連通部と流入口または流出口の一方とに向けて被加熱液が集まる。その結果、熱交換器の回転方向の取付け位置が多少ずれても、被加熱液流路の被加熱液は連通部を通り下側に位置する流入口または流出口の一方から熱交換器の外部に流れ出る。   According to this configuration, when the heat exchanger is mounted so that one of the inlet or the outlet is on the lower side and the other is on the upper side, the mounting position in the rotation direction of the heat exchanger is centered on the stacking direction of the heat exchange units. Even if there is a slight deviation, when the operation of extracting the liquid to be heated from the device to which the heat exchanger is attached is performed, the liquid to be heated gathers toward the communication portion located on the lower side and one of the inflow port or the outflow port. As a result, even if the mounting position of the heat exchanger in the rotational direction is slightly deviated, the liquid to be heated in the liquid flow path to be heated passes through the communicating portion and is located outside the heat exchanger from one of the inlet or outlet located below. Flows out.

請求項6に記載の発明では、横断部を挟んで横断部による横断方向の両側、ならびに横断部を挟んで横断方向と直交する方向の両側にそれぞれ形成されている被加熱液流路の幅は等しい。   In the invention according to claim 6, the width of the heated liquid channel formed on both sides in the transverse direction by the transverse part across the transverse part and on both sides in the direction orthogonal to the transverse direction across the transverse part is equal.

この構成によれば、横断部を中心として環状に形成される被加熱液流路の流路断面積が周上でほぼ等しくなる。これにより、被加熱液流路を流れる被加熱液の流速が周上で等しくなるとともに、流路断面において等しくなる。その結果、被加熱液流路を流れる被加熱液を均等に加熱することができる。   According to this configuration, the channel cross-sectional area of the heated liquid channel formed in an annular shape centering on the transverse portion is substantially equal on the circumference. As a result, the flow rates of the liquid to be heated flowing in the liquid flow path to be heated are equal on the circumference and are equal in the cross section of the flow path. As a result, the liquid to be heated flowing through the liquid flow path to be heated can be heated evenly.

請求項7に記載の発明では、給湯側加熱回路と、給湯側加熱回路の通水を加熱する主バーナと、主加熱回路である給湯側加熱回路とは別に設けられ、1次熱交換器、ならびに1次熱交換器を通過した燃焼ガスの潜熱を回収する2次熱交換器を有する副加熱回路と、副加熱回路の通水を加熱する副バーナと、を備え、副加熱回路の2次熱交換器として請求項1から6のいずれか一項に記載の熱交換器を使用する。   In the invention according to claim 7, a primary heat exchanger provided separately from the hot water supply side heating circuit, the main burner for heating the water passing through the hot water supply side heating circuit, and the hot water supply side heating circuit as the main heating circuit, And a secondary heating circuit having a secondary heat exchanger that recovers the latent heat of the combustion gas that has passed through the primary heat exchanger, and a secondary burner that heats water through the secondary heating circuit. The heat exchanger according to any one of claims 1 to 6 is used as a heat exchanger.

この構成によれば、被加熱液である水の流入口および流出口を熱交換器に設ける位置の自由度が高いので、副加熱回路の2次熱交換器として使用される請求項1から6のいずれか一項に記載の熱交換器を給湯器に取り付けるときに、給湯器内における副加熱回路の2次熱交換器の設置スペースおよび周囲に設置される部品に応じて、副加熱回路の2次熱交換器に設ける流入口および流出口の位置を適切に設定できる。その結果、副加熱回路の2次熱交換器に接続する配管の取り回しの自由度が高くなる。   According to this structure, since the freedom degree of the position which provides the inflow port and the outflow port of the water which is a to-be-heated liquid in a heat exchanger is high, it is used as a secondary heat exchanger of a subheating circuit. When the heat exchanger according to any one of the above is attached to the water heater, the sub-heating circuit of the sub-heating circuit depends on the installation space of the secondary heat exchanger of the sub-heating circuit in the water heater and the components installed around it. The positions of the inlet and outlet provided in the secondary heat exchanger can be appropriately set. As a result, the degree of freedom of the piping connected to the secondary heat exchanger of the sub-heating circuit is increased.

第1実施形態による給湯器を示す模式図。The schematic diagram which shows the water heater by 1st Embodiment. 給湯側および風呂側の2次熱交換器を組み付けた状態を示す斜視図。The perspective view which shows the state which assembled | attached the secondary heat exchanger of the hot water supply side and the bath side. (A)は風呂側の2次熱交換器の斜視図を示し、(B)はその分解斜視図。(A) shows the perspective view of the secondary heat exchanger by the side of a bath, and (B) is the exploded perspective view. (A)は風呂側の2次熱交換器の正面図、(B)は(A)のB−B線断面図、(C)は(A)のC−C線断面図。(A) is a front view of the secondary heat exchanger on the bath side, (B) is a cross-sectional view taken along line BB in (A), and (C) is a cross-sectional view taken along line CC in (A). (A)は(B)のA方向矢視図、(B)は図4の(C)において1個の熱交換ユニットを取り出した模式的断面図。(A) is a view in the direction of arrow A in (B), and (B) is a schematic cross-sectional view of one heat exchange unit taken out in (C) of FIG. 4. 隣接する熱交換ユニットの間のガス流路を説明するために図4の(B)の一部を取り出した模式的断面図。FIG. 5 is a schematic cross-sectional view in which a part of FIG. 4B is taken out in order to explain a gas flow path between adjacent heat exchange units. (A)は突部によるガス流れの均等化作用を説明する模式図、(B)は突部による空気膜の除去作用を説明する模式図。(A) is a schematic diagram explaining the equalization effect | action of the gas flow by a protrusion, (B) is a schematic diagram explaining the removal effect | action of the air film by a protrusion. 第2実施形態による風呂側の2次熱交換器の被加熱液流路を示す模式図。The schematic diagram which shows the to-be-heated liquid flow path of the secondary heat exchanger by the side of the bath by 2nd Embodiment. 第3実施形態による風呂側の2次熱交換器の被加熱液流路を示す模式図。The schematic diagram which shows the to-be-heated liquid flow path of the secondary heat exchanger by the side of the bath by 3rd Embodiment.

次に、本発明の実施形態を図に基づいて説明する。
[第1実施形態]
本発明の第1実施形態による給湯器の模式図を図1に示す。
Next, embodiments of the present invention will be described with reference to the drawings.
[First Embodiment]
The schematic diagram of the water heater by 1st Embodiment of this invention is shown in FIG.

(給湯器10の構造)
給湯器10は、ファンモータ12と、ファンモータ12によって回転駆動されるファン14と、給湯栓や浴槽などの出湯箇所へ湯を供給する給湯部20と、浴槽内の湯の保温および追い焚きを行う保温部50と、給湯部20および保温部50の作動を制御する図示しない制御部とを備えている。また、給湯部20の配管と保温部50の配管とは図示を省略する連通管で連通されており、給湯部20および保温部50を介し、浴槽内に湯水を供給できる構成になっている。
(Structure of the water heater 10)
The water heater 10 includes a fan motor 12, a fan 14 that is rotationally driven by the fan motor 12, a hot water supply unit 20 that supplies hot water to hot water outlets such as a hot water tap and a bathtub, and the warming and reheating of hot water in the bathtub. A heat retaining unit 50 is provided, and a controller (not shown) that controls the operation of the hot water supply unit 20 and the heat retaining unit 50 is provided. Moreover, the piping of the hot water supply unit 20 and the piping of the heat retaining unit 50 are communicated with each other through a communication pipe (not shown) so that hot water can be supplied into the bathtub through the hot water supplying unit 20 and the heat retaining unit 50.

給湯器10において、給湯部20は、燃焼室200に収納されたバーナ22、24と、顕熱回収用の1次熱交換器26と、潜熱回収用の2次熱交換器30とが、下方から上方にかけて順次配設されて構成されている。   In the water heater 10, the hot water supply unit 20 includes a burner 22, 24 accommodated in the combustion chamber 200, a sensible heat recovery primary heat exchanger 26, and a latent heat recovery secondary heat exchanger 30. Are arranged sequentially from top to bottom.

また、給湯器10において、保温部50は、燃焼室202に収納されたバーナ52と、顕熱回収用の1次熱交換器54と、潜熱回収用の2次熱交換器60とが、下方から上方にかけて順次配設されて構成されている。   In the water heater 10, the heat retaining unit 50 includes a burner 52 housed in the combustion chamber 202, a sensible heat recovery primary heat exchanger 54, and a latent heat recovery secondary heat exchanger 60. Are arranged sequentially from top to bottom.

給湯部20と保温部50とは互いに連通した構造になっており、ファンモーター12によってファン14を回転駆動することにより、給湯部20側の燃焼室200と、保温部50側の燃焼室202とのそれぞれに空気を供給可能になっている。   The hot water supply unit 20 and the heat retaining unit 50 are in communication with each other, and the fan 14 is rotationally driven by the fan motor 12, whereby the combustion chamber 200 on the hot water supply unit 20 side, the combustion chamber 202 on the heat retaining unit 50 side, and Air can be supplied to each of these.

バーナ22、24とバーナ52とにそれぞれガスを供給するガス供給管の支管、ならびに支管にガスを供給するガス供給管の本管には電磁弁が設置されている。これら電磁弁を開閉することにより、バーナ22、24とバーナ52へのガスの供給が制御される。   Solenoid valves are installed in the branch pipes of the gas supply pipes that supply gas to the burners 22 and 24 and the burner 52, respectively, and in the main pipe of the gas supply pipe that supplies gas to the branch pipes. By opening and closing these solenoid valves, gas supply to the burners 22 and 24 and the burner 52 is controlled.

図2に示すように、給湯部20の2次熱交換器30と、保温部50の2次熱交換器60とは、共通の枠体40に取り付けられた構造となっている。枠体40には、1次熱交換器26を通過したバーナ22、24の燃焼ガスを2次熱交換器30に導入する燃焼ガス導入口210と、1次熱交換器54を通過したバーナ52の燃焼ガスを2次熱交換器60に導入する燃焼ガス導入口212とが形成されている。   As shown in FIG. 2, the secondary heat exchanger 30 of the hot water supply unit 20 and the secondary heat exchanger 60 of the heat retaining unit 50 are attached to a common frame body 40. The frame body 40 includes a combustion gas inlet 210 through which the combustion gas of the burners 22 and 24 that has passed through the primary heat exchanger 26 is introduced into the secondary heat exchanger 30, and a burner 52 that has passed through the primary heat exchanger 54. The combustion gas inlet 212 for introducing the combustion gas into the secondary heat exchanger 60 is formed.

そして、燃焼ガス導入口210、212からそれぞれ導入された燃焼ガスは、2次熱交換器30、60をそれぞれ通過し、排気口214から排出される。燃焼ガスは、2次熱交換器30、60を通過するときに、内部の水と熱交換を行うことにより、水を加熱する。   The combustion gases introduced from the combustion gas inlets 210 and 212 respectively pass through the secondary heat exchangers 30 and 60 and are discharged from the exhaust port 214. When the combustion gas passes through the secondary heat exchangers 30 and 60, it heats the water by exchanging heat with the internal water.

給湯部20の2次熱交換器30は、1次熱交換器26を通過したバーナ22、24の燃焼ガスの潜熱を回収し、保温部50の2次熱交換器60は、1次熱交換器54を通過したバーナ52の燃焼ガスの潜熱を回収するために設置されている。   The secondary heat exchanger 30 of the hot water supply unit 20 recovers the latent heat of the combustion gas of the burners 22 and 24 that has passed through the primary heat exchanger 26, and the secondary heat exchanger 60 of the heat retaining unit 50 performs primary heat exchange. It is installed to recover the latent heat of the combustion gas of the burner 52 that has passed through the vessel 54.

給湯部20においては、上水道から供給された給湯水は、まず2次熱交換器30に供給され、2次熱交換器30で加熱された給湯水が1次熱交換器26に供給されてさらに加熱される。給湯部20で加熱された湯は、キッチンの給湯栓等から出湯される他、給湯部20の配管と保温部50の配管とを連通する前述した連通管および保温部50の配管を介して、浴槽内に出湯される。尚、給湯部20から加熱された給湯水を浴槽に供給する連通管には、浴槽への出湯を行うときに開弁される電磁弁が設けられている。   In the hot water supply unit 20, hot water supplied from the water supply is first supplied to the secondary heat exchanger 30, and hot water heated by the secondary heat exchanger 30 is supplied to the primary heat exchanger 26. Heated. The hot water heated in the hot water supply unit 20 is discharged from a hot water tap or the like of the kitchen, and also through the above-described communication pipe that connects the piping of the hot water supply unit 20 and the piping of the heat retaining unit 50 and the piping of the heat retaining unit 50. Hot water is poured into the bathtub. In addition, the communication pipe which supplies the hot water heated from the hot water supply part 20 to the bathtub is provided with an electromagnetic valve which is opened when the hot water is discharged to the bathtub.

保温部50においても、風呂の浴槽からポンプ等で汲み上げられた風呂水が、まず2次熱交換器60に供給され、2次熱交換器60で加熱された風呂水が1次熱交換器54に供給されてさらに加熱される。1次熱交換器54で加熱された風呂水は、浴槽に戻される。   Also in the heat retaining unit 50, the bath water pumped up from the bath tub by a pump or the like is first supplied to the secondary heat exchanger 60, and the bath water heated by the secondary heat exchanger 60 is the primary heat exchanger 54. To be further heated. The bath water heated by the primary heat exchanger 54 is returned to the bathtub.

図示しない制御部は、CPU、ROM、RAM等を備えたマイクロコンピュータを内蔵しており、バーナ用イグナイタ、および前述した各種電磁弁、モータ、ポンプ等の作動を制御する。   A control unit (not shown) incorporates a microcomputer including a CPU, a ROM, a RAM, and the like, and controls operations of the burner igniter and the various electromagnetic valves, motors, pumps, and the like described above.

(保温部50の2次熱交換器60)
次に、保温部50の2次熱交換器60について説明する。
図3に示すように、2次熱交換器60は、扁平な熱交換ユニット64を積層した熱交換ユニット群62から主に構成されている。各熱交換ユニット64は、プレス加工で成型された2枚の板状部材66の外周縁部同士をろう付けにより接合して形成されている。
(Secondary heat exchanger 60 of the heat retaining unit 50)
Next, the secondary heat exchanger 60 of the heat retaining unit 50 will be described.
As shown in FIG. 3, the secondary heat exchanger 60 is mainly composed of a heat exchange unit group 62 in which flat heat exchange units 64 are stacked. Each heat exchange unit 64 is formed by joining the outer peripheral edge portions of two plate-like members 66 formed by press working by brazing.

図3の(B)において、符号222は隣接する熱交換ユニット64の間を積層方向に流れる風呂水の流れを示し、符号224は熱交換ユニット64内を流れる風呂水の流れを示している。   In FIG. 3B, reference numeral 222 indicates a flow of bath water flowing in the stacking direction between adjacent heat exchange units 64, and reference numeral 224 indicates a flow of bath water flowing in the heat exchange unit 64.

図4の(A)に示すように、熱交換ユニット64の外形は長方形である。2次熱交換器60は、熱交換ユニット64の長辺を水平方向に向け、短辺を鉛直方向に向けて枠体40に取付けられるので、給湯器10の高さを極力低くすることができる。   As shown to (A) of FIG. 4, the external shape of the heat exchange unit 64 is a rectangle. Since the secondary heat exchanger 60 is attached to the frame body 40 with the long side of the heat exchange unit 64 in the horizontal direction and the short side in the vertical direction, the height of the water heater 10 can be made as low as possible. .

図4の(B)、(C)に示すように、熱交換ユニット64の内部には、風呂水が流れる扁平な被加熱液流路220が形成されており、隣接する熱交換ユニット64の間には、バーナ52の燃焼ガスが通過するガス流路230が形成されている。   As shown in FIGS. 4B and 4C, a flat heated liquid flow path 220 through which bath water flows is formed inside the heat exchange unit 64, and between adjacent heat exchange units 64. Is formed with a gas passage 230 through which the combustion gas of the burner 52 passes.

尚、図3および図4では、図の煩雑さを避けるために一部の符号を省略している。
熱交換ユニット64には、2枚の板状部材66のそれぞれに、隣接する熱交換ユニット64の被加熱液流路220を連通する連通部68が、ガス流路230を横切って2箇所形成されている。尚、積層方向の一端側の熱交換ユニット64Aにおいて、隣接する熱交換ユニット64に面する板状部材66に対して反対側の板状部材66に形成された連通部の一方は風呂水の流入口70として機能し、連通部の他方は風呂水の流出口72として機能する。流入口70および流出口72には、配管と接続する接続継手80が補強板82を介してろう付けされている。
In FIGS. 3 and 4, some symbols are omitted in order to avoid complexity of the drawings.
In the heat exchange unit 64, two plate-like members 66 are formed with two communicating portions 68 that communicate with the heated liquid passage 220 of the adjacent heat exchange unit 64 across the gas passage 230. ing. In the heat exchange unit 64A on one end side in the stacking direction, one of the communicating portions formed on the plate member 66 on the opposite side to the plate member 66 facing the adjacent heat exchange unit 64 is the flow of bath water. It functions as an inlet 70, and the other of the communicating portions functions as an outlet 72 for bath water. A connection joint 80 connected to the pipe is brazed to the inflow port 70 and the outflow port 72 via a reinforcing plate 82.

流入口70および流出口72が設けられている積層方向の一端側の熱交換ユニット64Aに対して、積層方向の他端側の熱交換ユニット64Bにおいて、隣接する熱交換ユニット64に面する板状部材66と反対側の板状部材66には、連通部68が形成されていないか、形成された連通部68が栓で封止されている。   In the heat exchange unit 64B on the other end side in the stacking direction with respect to the heat exchange unit 64A on the one end side in the stacking direction in which the inlet 70 and the outlet 72 are provided, a plate shape facing the adjacent heat exchange unit 64 The plate-like member 66 opposite to the member 66 is not formed with a communication portion 68 or the formed communication portion 68 is sealed with a stopper.

熱交換ユニット64を形成する2枚の板状部材66の中心部には、熱交換ユニット64の内部に向けて積層方向に凹む凹部74が形成されている。2枚の板状部材66を接合した状態で2個の凹部74が接触または接近することにより、横断部76が形成されている。横断部76は、被加熱液流路220において、2箇所に設けられた連通部68の間を横断して設けられている。   A concave portion 74 that is recessed in the stacking direction toward the inside of the heat exchange unit 64 is formed at the center of the two plate-like members 66 that form the heat exchange unit 64. When the two concave portions 74 are brought into contact with or approach each other in a state where the two plate-like members 66 are joined, the transverse portion 76 is formed. The crossing part 76 is provided across the communication parts 68 provided at two places in the heated liquid channel 220.

図5の(A)に示すように、板状部材66の2箇所に設けられた連通部68は、横断部76の中心位置76aを中心として点対称の位置に配置されている。
図5の(A)は、図5の(B)をA方向から見た図であり、熱交換ユニット64を構成する2枚の板状部材66の一方を取り除いて熱交換ユニット64の内部を模式的に示した図である。図5の(B)は、図4の(C)における1個の熱交換ユニット64を取り出した熱交換ユニット64の模式的断面図である。
As shown in FIG. 5A, the communication portions 68 provided at two locations of the plate-like member 66 are arranged at point-symmetrical positions around the center position 76 a of the transverse portion 76.
FIG. 5A is a view of FIG. 5B as viewed from the A direction. One of the two plate-like members 66 constituting the heat exchange unit 64 is removed, and the inside of the heat exchange unit 64 is shown. It is the figure shown typically. FIG. 5B is a schematic cross-sectional view of the heat exchange unit 64 in which one heat exchange unit 64 in FIG. 4C is taken out.

このように、2箇所に設けられた連通部68が、横断部76の中心位置76aを中心として点対称の位置に配置されているので、熱交換ユニット64を180°回転しても、2箇所に設けられた連通部68の位置は変化しない。その結果、熱交換ユニット64の回転位置を考慮せずに熱交換ユニット64を積層できるので、熱交換ユニット64を積層して2次熱交換器60を容易に製造できる。   As described above, since the communication portions 68 provided at two places are arranged at point-symmetrical positions around the center position 76a of the crossing portion 76, even if the heat exchange unit 64 is rotated by 180 °, two places are provided. The position of the communication portion 68 provided in the position does not change. As a result, since the heat exchange unit 64 can be laminated without considering the rotational position of the heat exchange unit 64, the secondary heat exchanger 60 can be easily manufactured by laminating the heat exchange unit 64.

また、図3および図4に示すように、熱交換ユニット64を形成する2枚の板状部材66の表面には、凹部74の周囲に突部78が複数設けられている。突部78は、プレス加工により板状部材66に形成されてもよいし、各板状部材66に溶接等で接合してもよい。隣接する熱交換ユニット64の互いに向き合う突部78は、熱交換ユニット64を積層してろう付けするときに隣接する熱交換ユニット64を支持するので、熱交換ユニット64を積層するときに熱交換ユニット64が傾くことを防止する。これにより、2次熱交換器60を製造するときに、熱交換ユニット64を容易に積層できる。   As shown in FIGS. 3 and 4, a plurality of protrusions 78 are provided around the recess 74 on the surface of the two plate-like members 66 forming the heat exchange unit 64. The protrusion 78 may be formed on the plate-like member 66 by press working, or may be joined to each plate-like member 66 by welding or the like. The protrusions 78 facing each other of the adjacent heat exchange units 64 support the adjacent heat exchange units 64 when the heat exchange units 64 are laminated and brazed, so that when the heat exchange units 64 are laminated, the heat exchange units 64 64 prevents tilting. Thereby, when manufacturing the secondary heat exchanger 60, the heat exchange unit 64 can be laminated easily.

(被加熱液流路220)
図5に示すように、熱交換ユニット64において、2箇所に設けられた連通部68の一方から被加熱液流路220に流入した風呂水は、連通部68の他方に短絡しようとする流れを横断部76により妨害される。その結果、連通部68の一方から流入した風呂水は、被加熱液流路220を横断部76の横断方向の両側に分かれて流れ、他方の連通部68で合流する。その結果、熱交換ユニット64の内部に、横断部76を中心として、環状の被加熱液流路220が形成される。
(Heating liquid flow path 220)
As shown in FIG. 5, in the heat exchange unit 64, the bath water that has flowed into the heated liquid flow path 220 from one of the communicating portions 68 provided at two locations has a flow that tends to be short-circuited to the other of the communicating portions 68. It is obstructed by the crossing 76. As a result, the bath water flowing in from one of the communicating portions 68 flows separately on both sides of the transverse portion 76 in the transverse direction of the liquid to be heated 220 and merges at the other communicating portion 68. As a result, an annular heated liquid flow path 220 is formed in the heat exchange unit 64 with the cross section 76 as the center.

横断部76を挟んで横断部76の横断方向の両側の被加熱液流路220の流路幅L、ならびに横断部76を挟んで横断方向と直交する方向の両側の被加熱液流路220の流路幅Lは等しい。つまり、環状の被加熱液流路220の流路断面積はほぼ等しい。   The channel width L of the heated liquid channel 220 on both sides of the transverse part 76 across the transverse part 76 and the heated liquid channel 220 on both sides in the direction perpendicular to the transverse direction across the transverse part 76. The channel width L is equal. That is, the channel cross-sectional areas of the annular heated liquid channel 220 are substantially equal.

これにより、被加熱液流路220を流れる風呂水の流量が横断部76の横断方向両側と横断方向と直交する直交方向両側とで等しくなるとともに、風呂水の流速が被加熱液流路220の周上および流路断面において等しくなる。その結果、隣接する熱交換ユニット64の間に形成されたガス流路230を通過する燃焼ガスにより、被加熱液流路220を流れる風呂水が均等に加熱される。   As a result, the flow rate of the bath water flowing through the heated liquid channel 220 becomes equal on both sides in the transverse direction of the transverse portion 76 and on both sides in the orthogonal direction perpendicular to the transverse direction, and the flow rate of the bath water is increased in the heated liquid channel 220. It becomes equal on the circumference and the channel cross section. As a result, the bath water flowing through the heated liquid channel 220 is evenly heated by the combustion gas passing through the gas channel 230 formed between the adjacent heat exchange units 64.

また、環状の被加熱液流路220の流路断面積がほぼ等しいので、被加熱液流路220における圧力損失を軽減し、風呂水の通水量を確保できる。
(拡幅部232)
図6は、隣接する熱交換ユニット64の間に形成されるガス流路230を説明するために、図4の(B)の一部を取り出した模式的断面図である。隣接する熱交換ユニット64の間のガス流路230には、板状部材66に形成された凹部74により、ガス流路230の中心部に、ガス流れ方向に沿って拡幅部232が形成されている。拡幅部232は、拡幅部232の周囲よりもガス流路230の流路幅が積層方向に拡幅されているので、拡幅部232の周囲よりも流路抵抗が小さくなっている。
In addition, since the channel cross-sectional area of the annular heated liquid passage 220 is substantially equal, the pressure loss in the heated liquid passage 220 can be reduced, and the amount of bath water flowing can be ensured.
(Widened portion 232)
FIG. 6 is a schematic cross-sectional view in which a part of FIG. 4B is taken out in order to explain the gas flow path 230 formed between the adjacent heat exchange units 64. In the gas flow path 230 between the adjacent heat exchange units 64, a widened portion 232 is formed in the center of the gas flow path 230 along the gas flow direction by the recess 74 formed in the plate member 66. Yes. In the widened portion 232, the flow path width of the gas flow channel 230 is wider in the stacking direction than the periphery of the widened portion 232, and thus the flow path resistance is smaller than that of the widened portion 232.

ここで、拡幅部232が設けられておらず、ガス流路230の積層方向の幅が均一な場合、ガス流路230の一方側(図4の(A)では左側)から流入した燃焼ガスは、ガス流路230を図4の(A)の上下間を均等に流れて他方側(図4の(A)では右側)から流出するのではなく、流路抵抗の小さい2次熱交換器60の外側に引き寄せられるので、ガス流路230の中心部よりも外側(図4の(A)では上側および下側)を流れる傾向にある。   Here, when the widened portion 232 is not provided and the width of the gas flow path 230 in the stacking direction is uniform, the combustion gas flowing in from one side of the gas flow path 230 (left side in FIG. 4A) is In addition, the secondary heat exchanger 60 having a small flow path resistance is used instead of flowing through the gas flow path 230 between the upper and lower portions of FIG. 4A and flowing out from the other side (the right side in FIG. 4A). Therefore, it tends to flow outside the center of the gas flow path 230 (upper and lower sides in FIG. 4A).

これに対し、本実施形態では、ガス流路230の中心部に拡幅部232が形成されているので、ガス流路230に流入した燃焼ガスは、2次熱交換器60の外側だけでなく、ガス流路230の中心部に設けられた流路抵抗の小さい拡幅部232にも引き寄せられる。さらに、拡幅部232はガス流れ方向に沿って形成されているので、拡幅部232に向かうガス流れは、ガス流れ方向に沿った拡幅部232の長さ分、ガス流路230の中心部に向かって引き寄せられる。これにより、燃焼ガスはガス流路230を均等に流れる。   On the other hand, in this embodiment, since the widened portion 232 is formed at the center of the gas flow path 230, the combustion gas that has flowed into the gas flow path 230 is not only outside the secondary heat exchanger 60, It is also attracted to the widened portion 232 having a small flow resistance provided at the center of the gas flow channel 230. Further, since the widened portion 232 is formed along the gas flow direction, the gas flow toward the widened portion 232 is directed toward the center of the gas flow path 230 by the length of the widened portion 232 along the gas flow direction. Attracted. Thereby, the combustion gas flows through the gas flow path 230 evenly.

(突部78の作用)
突部78は、前述したように、熱交換ユニット64を積層するときに隣接する熱交換ユニット64を支持するだけでなく、図7の(A)に示すように、ガス流路230の中心部よりも外側に向かおうとする燃焼ガスの流れを妨害し、中心部に向かう流れを形成する。これにより、ガス流路230の中心部よりも外側を流れようとする燃焼ガスが中心部側にも向かおうとするので、燃焼ガスはガス流路230を均等に流れる。
(Operation of the protrusion 78)
As described above, the protrusion 78 not only supports the adjacent heat exchange unit 64 when the heat exchange units 64 are stacked, but also includes a central portion of the gas flow path 230 as shown in FIG. This obstructs the flow of the combustion gas going outward, and forms a flow toward the center. As a result, the combustion gas that tends to flow outside the central portion of the gas flow path 230 tends to move toward the central portion side, so that the combustion gas flows evenly through the gas flow path 230.

また、被加熱液流路220を風呂水が流れると、熱交換ユニット64の表面の空気が冷却されるので、図7の(B)に示すように、燃焼ガスに対して温度の低い空気膜240が熱交換ユニット64の表面に形成される。熱交換ユニット64の表面が空気膜240で覆われたままでは、燃焼ガスは熱交換ユニット64に直接接触できなくなるとともに、空気膜240が断熱膜となるので、燃焼ガスによる風呂水の加熱効率が低下する。   Further, when bath water flows through the heated liquid flow path 220, the air on the surface of the heat exchange unit 64 is cooled, so that an air film having a lower temperature than the combustion gas as shown in FIG. 240 is formed on the surface of the heat exchange unit 64. If the surface of the heat exchange unit 64 is covered with the air film 240, the combustion gas cannot directly contact the heat exchange unit 64, and the air film 240 becomes a heat insulation film. descend.

そこで、本実施形態では、板状部材66の表面に突部78を設けているので、燃焼ガスが突部78に衝突し、空気膜240を除去する。これにより、燃焼ガスが熱交換ユニット64に直接接触するので、燃焼ガスによる風呂水の加熱効率が向上する。   Therefore, in the present embodiment, since the protrusion 78 is provided on the surface of the plate-like member 66, the combustion gas collides with the protrusion 78, and the air film 240 is removed. Thereby, since combustion gas contacts the heat exchange unit 64 directly, the heating efficiency of the bath water by combustion gas improves.

以上説明した第1実施形態によれば、2箇所に設けられた連通部68の一方から環状の被加熱液流路220に流入した風呂水は、連通部68の間を短絡しようとする流れを横断部76に妨害されるので、被加熱液流路220を横断部76の横断方向の両側に分かれて流れ、他方の連通部68で合流する。   According to 1st Embodiment demonstrated above, the bath water which flowed in into the cyclic | annular to-be-heated liquid flow path 220 from one of the communication parts 68 provided in two places has the flow which tries to short-circuit between the communication parts 68. Since it is obstructed by the crossing part 76, the heated liquid flow path 220 flows separately on both sides in the transverse direction of the crossing part 76, and merges at the other communication part 68.

したがって、環状の被加熱液流路220の周上で連通部68を設ける位置、つまり風呂水の流入口70および流出口72を設ける位置を変更しても、被加熱液流路220にデッドスペースが生じることなく、風呂水が環状の被加熱液流路220を流れる。これにより、風呂水の流入口70および流出口72を熱交換器に設ける位置の自由度が高いので、熱交換器に接続する配管の取り回しの自由度が高くなる。   Therefore, even if the position where the communication portion 68 is provided on the circumference of the annular heated liquid flow path 220, that is, the position where the bath water inlet 70 and the outlet 72 are provided is changed, a dead space is formed in the heated liquid flow path 220. The bath water flows through the annular heated liquid passage 220 without the occurrence of water. Thereby, since the freedom degree of the position which provides the inflow port 70 and the outflow port 72 of bath water in a heat exchanger is high, the freedom degree of the management of piping connected to a heat exchanger becomes high.

第1実施形態では、給湯部20の1次熱交換器26および2次熱交換器30が本発明の給湯側加熱回路を形成し、保温部50の1次熱交換器54および2次熱交換器60が本発明の副加熱回路を形成している。   In the first embodiment, the primary heat exchanger 26 and the secondary heat exchanger 30 of the hot water supply unit 20 form the hot water supply side heating circuit of the present invention, and the primary heat exchanger 54 and the secondary heat exchange of the heat retaining unit 50. The vessel 60 forms the subheating circuit of the present invention.

また、第1実施形態では、バーナ22、24が本発明の主バーナに相当し、バーナ52が本発明の副バーナに相当する。
また、第1実施形態では、2次熱交換器60が本発明の熱交換器に相当し、熱交換ユニット群62が本発明の熱交換ユニット群に相当し、熱交換ユニット64が本発明の熱交換ユニットに相当し、板状部材66が本発明の板状部材に相当し、連通部68が本発明の連通部に相当し、流入口70が本発明の流入口に相当し、流出口72が本発明の流出口に相当し、横断部76が本発明の横断部に相当し、被加熱液流路220が本発明の被加熱液流路に相当し、ガス流路230が本発明のガス流路に相当する。
In the first embodiment, the burners 22 and 24 correspond to the main burner of the present invention, and the burner 52 corresponds to the auxiliary burner of the present invention.
In the first embodiment, the secondary heat exchanger 60 corresponds to the heat exchanger of the present invention, the heat exchange unit group 62 corresponds to the heat exchange unit group of the present invention, and the heat exchange unit 64 of the present invention. The plate-like member 66 corresponds to the plate-like member of the present invention, the communication portion 68 corresponds to the communication portion of the present invention, the inlet 70 corresponds to the inlet of the present invention, and the outlet 72 corresponds to the outlet of the present invention, the cross section 76 corresponds to the cross section of the present invention, the heated liquid flow path 220 corresponds to the heated liquid flow path of the present invention, and the gas flow path 230 corresponds to the present invention. This corresponds to the gas flow path.

[第2実施形態]
本発明の第2実施形態による熱交換器を図8に示す。第1実施形態と実質的に同一構成部分には同一符号を付す。図8は、図5の(A)と同様に、熱交換ユニット90を構成する2枚の板状部材92の一方を取り除いて熱交換ユニット90の内部を模式的に示した図である。
[Second Embodiment]
A heat exchanger according to a second embodiment of the present invention is shown in FIG. Components that are substantially the same as those in the first embodiment are denoted by the same reference numerals. FIG. 8 is a diagram schematically showing the inside of the heat exchange unit 90 by removing one of the two plate-like members 92 constituting the heat exchange unit 90, as in FIG.

第1実施形態の2次熱交換器60では、四角形状に形成された熱交換ユニット64において横断部76を挟んで横断方向と直交する方向の両側の長辺に沿った中心部に連通部68を設けた。   In the secondary heat exchanger 60 of the first embodiment, in the heat exchange unit 64 formed in a quadrangular shape, the communicating portion 68 is connected to the central portion along the long side on both sides in the direction orthogonal to the transverse direction across the transverse portion 76. Was provided.

これに対し、第2実施形態の熱交換ユニット90では、四角形状に形成された熱交換ユニット90において、2個の凹部94により形成される横断部96を挟んで対角線上に連通部68を設けている。   On the other hand, in the heat exchange unit 90 of the second embodiment, in the heat exchange unit 90 formed in a square shape, the communication portion 68 is provided diagonally across the transverse portion 96 formed by the two concave portions 94. ing.

この場合にも、横断部96は被加熱液流路220の中心部に形成されることが望ましく、2箇所に設けられた連通部68は、横断部96の中心位置96aを中心として、横断部96に対して点対称の位置に配置されていることが望ましい。   Also in this case, it is desirable that the crossing portion 96 is formed at the center portion of the heated liquid flow path 220, and the communication portions 68 provided at two places are crossing portions around the center position 96 a of the crossing portion 96. It is desirable that they are arranged at point-symmetrical positions with respect to 96.

そして、連通部68の一方から流入した風呂水は、被加熱液流路220を横断部96の横断方向の両側に分かれて流れ、他方の連通部68で合流する。その結果、熱交換ユニット90の内部に、横断部96を中心として環状の被加熱液流路220が形成される。   Then, the bath water flowing in from one of the communication portions 68 flows separately on both sides in the transverse direction of the transverse portion 96 through the heated liquid flow path 220, and merges at the other communication portion 68. As a result, an annular liquid passage 220 to be heated is formed inside the heat exchange unit 90 with the transverse portion 96 as the center.

第2実施形態では、熱交換ユニット90が本発明の熱交換ユニットに相当し、板状部材92が本発明の板状部材に相当し、横断部96が本発明の横断部に相当する。
[第3実施形態]
本発明の第3実施形態による熱交換器を図9に示す。第1実施形態と実質的に同一構成部分には同一符号を付す。図9は、図5の(A)および図8と同様に、熱交換ユニット100を構成する2枚の板状部材102の一方を取り除いて熱交換ユニット100の内部を模式的に示した図である。
In the second embodiment, the heat exchange unit 90 corresponds to the heat exchange unit of the present invention, the plate-like member 92 corresponds to the plate-like member of the present invention, and the transverse portion 96 corresponds to the transverse portion of the present invention.
[Third Embodiment]
A heat exchanger according to a third embodiment of the present invention is shown in FIG. Components that are substantially the same as those in the first embodiment are denoted by the same reference numerals. FIG. 9 is a diagram schematically showing the inside of the heat exchange unit 100 by removing one of the two plate-like members 102 constituting the heat exchange unit 100, as in FIG. 5A and FIG. is there.

横断部76は被加熱液流路220の中心部に形成されており、2箇所に設けられた連通部68は、横断部76の中心位置76aを中心として、横断部76に対して点対称の位置に配置されている。   The crossing part 76 is formed at the center of the heated liquid flow path 220, and the communication parts 68 provided at two places are point-symmetric with respect to the crossing part 76 around the center position 76 a of the crossing part 76. Placed in position.

熱交換ユニット100においても、横断部76を中心として、環状の被加熱液流路220が形成されている。
2箇所に設けられた連通部68は、被加熱液流路220を形成する熱交換ユニット100の内壁面104の内周縁106と接している。したがって、2箇所の各箇所に形成された連通部68と同じ積層方向上に形成されている熱交換器の流入口70および流出口72も、熱交換ユニット100の内壁面104の内周縁106と接している。
Also in the heat exchange unit 100, an annular heated liquid channel 220 is formed around the crossing 76.
The communication portions 68 provided at two locations are in contact with the inner peripheral edge 106 of the inner wall surface 104 of the heat exchange unit 100 that forms the heated liquid flow path 220. Therefore, the inlet 70 and the outlet 72 of the heat exchanger formed in the same stacking direction as the communication portions 68 formed at the two locations are also connected to the inner peripheral edge 106 of the inner wall surface 104 of the heat exchange unit 100. It touches.

そして、流入口70および流入口70と同じ積層方向上の連通部68、ならびに流出口72および流出口72と同じ積層方向上の連通部68のそれぞれと内壁面104の内周縁106とが接している箇所300の内壁面104は、接している箇所300を通る接線302に対して、接している箇所300を挟んで両側の内壁面104を所定角度θ傾斜させることにより、凹部108を形成している。   The inflow port 70 and the communication portion 68 in the same stacking direction as the inflow port 70 and the outflow port 72 and the communication portion 68 in the same stacking direction as the outflow port 72 are in contact with the inner peripheral edge 106 of the inner wall surface 104. The inner wall surface 104 of the location 300 has a recess 108 formed by inclining the inner wall surfaces 104 on both sides with a predetermined angle θ with respect to the tangent line 302 passing through the contact location 300. Yes.

これにより、流入口70または流出口72が鉛直方向下側になるように熱交換器を取り付けるときに、熱交換ユニット100の積層方向を軸として熱交換器を多少回転して取り付けても、周知の水抜き操作を実行すると、鉛直方向下側に位置する流入口70または流出口72と連通部68とに向けて、つまり凹部108の底に向けて風呂水が集まる。その結果、熱交換器の回転方向の組み付け位置が多少ずれていても、被加熱液流路220の風呂水は連通部68を通り鉛直方向下側に位置する流入口70または流出口72から熱交換器の外部に流れ出る。   Thus, when the heat exchanger is attached so that the inlet 70 or the outlet 72 is on the lower side in the vertical direction, the heat exchanger may be attached with a slight rotation about the stacking direction of the heat exchange unit 100 as an axis. When the water draining operation is performed, bath water gathers toward the inflow port 70 or the outflow port 72 positioned on the lower side in the vertical direction and the communication portion 68, that is, toward the bottom of the recess 108. As a result, even if the assembly position in the rotational direction of the heat exchanger is slightly shifted, the bath water in the heated liquid flow path 220 passes through the communication portion 68 and is heated from the inlet 70 or the outlet 72 located on the lower side in the vertical direction. It flows out of the exchanger.

したがって、熱交換ユニット100内に風呂水が残り、冬期に凍結することを防止できる。また、風呂水内の異物および汚れが熱交換ユニット100内に溜まることを防止できる。   Therefore, it is possible to prevent the bath water from remaining in the heat exchange unit 100 and freezing in the winter. Further, foreign substances and dirt in the bath water can be prevented from accumulating in the heat exchange unit 100.

第3実施形態では、熱交換ユニット100が本発明の熱交換ユニットに相当し、板状部材102が本発明の板状部材に相当し、内壁面104が本発明の内壁面に相当し、内周縁106が本発明の内周縁に相当し、凹部108が本発明の内壁面の凹部に相当し、接している箇所300が本発明の接している箇所に相当し、接線302が本発明の接線に相当する。   In the third embodiment, the heat exchange unit 100 corresponds to the heat exchange unit of the present invention, the plate member 102 corresponds to the plate member of the present invention, the inner wall surface 104 corresponds to the inner wall surface of the present invention, The peripheral edge 106 corresponds to the inner peripheral edge of the present invention, the concave portion 108 corresponds to the concave portion of the inner wall surface of the present invention, the contacting portion 300 corresponds to the contacting portion of the present invention, and the tangent 302 is the tangent of the present invention. It corresponds to.

[他の実施形態]
上記実施形態では、横断部を中心として連通部を点対称に設置した。これに対し、2箇所に設けられた連通部の一方から流入した被加熱液が他方の連通部に短絡して流れることを横断部が妨害し、横断部を中心として環状の被加熱液流路が形成されるのであれば、2箇所に設けられた連通部は横断部を中心とした点対称の位置に設置されている必要はない。また、横断部は被加熱液流路の中心部からずれた位置に設けられてもよい。
[Other Embodiments]
In the above-described embodiment, the communication part is installed point-symmetrically with the crossing part as the center. On the other hand, the liquid to be heated that has flowed in from one of the two communication portions provided at two locations is prevented from flowing short-circuited to the other communication portion, and the transverse portion prevents the liquid to be heated to have an annular shape around the transverse portion. If it is formed, the communication part provided in two places does not need to be installed in the point symmetrical position centering on the crossing part. Further, the crossing portion may be provided at a position shifted from the central portion of the heated liquid channel.

また、上記実施形態では、被加熱液の流入口が上方になり、流出口が下方になるように本発明の熱交換器を取付けた。これに対し、流出口が上方になり、流入口が下方になるように本発明の熱交換器を取付けてもよい。   Moreover, in the said embodiment, the heat exchanger of this invention was attached so that the inflow port of a to-be-heated liquid might become an upper direction and an outflow port might become a downward direction. On the other hand, you may attach the heat exchanger of this invention so that an outflow port may become upper and an inflow port may become downward.

また、上記実施形態では、2枚の板状部材の外周縁部を接合して形成され、内部に扁平な環状の被加熱液流路を有する熱交換ユニットを積層して製造した本発明の熱交換器を、給湯器の浴槽用の保温部においてバーナの燃料ガスの潜熱を回収する2次熱交換器として使用した。これに対し、本発明の熱交換器は、浴槽用の保温部以外に、例えば床暖房用の保温部の2次熱交換器に適用してもよい。そして、本発明の熱交換器は、水に限らず内部を流れる被加熱液を加熱するのであれば、どのような用途に適用してもよい。   Moreover, in the said embodiment, the heat | fever of this invention manufactured by laminating | stacking the heat exchange unit which joins the outer periphery part of two plate-shaped members, and has a flat cyclic | annular to-be-heated liquid flow path inside. The exchanger was used as a secondary heat exchanger for recovering the latent heat of the burner fuel gas in the heat retaining section for the bathtub of the water heater. On the other hand, you may apply the heat exchanger of this invention to the secondary heat exchanger of the heat retention part for floor heating, for example besides the heat retention part for bathtubs. And if the heat exchanger of this invention heats the to-be-heated liquid which flows not only in water but the inside, you may apply to what kind of use.

また、第3実施形態において、流入口70および流入口70と同じ積層方向上の連通部68、ならびに流出口72および流出口72と同じ積層方向上の連通部68のそれぞれと接している箇所の内壁面を、凹状ではなく直線状に形成してもよい。   Further, in the third embodiment, the inlet 70 and the communication portion 68 in the same stacking direction as the inlet 70, and the portions in contact with the outlet 72 and the communication portion 68 in the same stacking direction as the outlet 72, respectively. The inner wall surface may be formed in a straight line instead of a concave shape.

このように、本発明は、上記実施形態に限定されるものではなく、その要旨を逸脱しない範囲で種々の実施形態に適用可能である。   As described above, the present invention is not limited to the above-described embodiment, and can be applied to various embodiments without departing from the gist thereof.

10:給湯器、20:給湯部、22、24:バーナ(主バーナ)、26:1次熱交換器(給湯側加熱回路、主加熱回路)、30:2次熱交換器(給湯側加熱回路、主加熱回路)、50:保温部、52:バーナ(副バーナ)、54:1次熱交換器(副加熱回路)、60:2次熱交換器(副加熱回路)、62:熱交換ユニット群、64、90、100:熱交換ユニット、66、92、102:板状部材、68:連通部、70:流入口、72:流出口、74、94:凹部、76、96:横断部、78:突部、104:内壁面、106:内周縁、108:凹部、220:被加熱液流路、300:接している箇所、302:接線、θ:所定角度 10: Hot water heater, 20: Hot water supply section, 22, 24: Burner (main burner), 26: Primary heat exchanger (hot water supply side heating circuit, main heating circuit), 30: Secondary heat exchanger (hot water supply side heating circuit) , Main heating circuit), 50: heat retaining section, 52: burner (sub-burner), 54: primary heat exchanger (sub-heating circuit), 60: secondary heat exchanger (sub-heating circuit), 62: heat exchange unit Group, 64, 90, 100: heat exchange unit, 66, 92, 102: plate-like member, 68: communication portion, 70: inflow port, 72: outflow port, 74, 94: recess, 76, 96: crossing portion, 78: Projection, 104: Inner wall surface, 106: Inner peripheral edge, 108: Recess, 220: Heated liquid flow path, 300: Touched part, 302: Tangent, θ: Predetermined angle

Claims (7)

2枚の板状部材の外周縁部同士を接合して各熱交換ユニットが形成されて各熱交換ユニットが内部に扁平な被加熱液流路を有し、前記熱交換ユニットの厚み方向に積層されており、隣接する前記熱交換ユニットの間に、バーナにより発生する燃焼ガスが通過するガス流路を形成している熱交換ユニット群と、
前記ガス流路を横切って2箇所に設けられ、隣接する前記熱交換ユニットの前記被加熱液流路同士を連通する連通部と、
を備え、
積層方向の一端側の前記熱交換ユニットにおいて、前記積層方向に対して前記連通部が設けられている側と反対側の前記板状部材に、被加熱液の流入口と流出口とが設けられており、
前記熱交換ユニットは、前記被加熱液流路において、2箇所に設けられた前記連通部の間を横断して設けられ、2箇所に設けられた前記連通部の間を短絡しようとする被加熱液の流れを妨害することにより前記被加熱液流路を環状に形成する横断部を有している、
ことを特徴とする熱交換器。
Each heat exchange unit is formed by joining the outer peripheral edge portions of two plate-like members, each heat exchange unit has a flat heated liquid passage inside, and is laminated in the thickness direction of the heat exchange unit A heat exchange unit group forming a gas flow path through which combustion gas generated by a burner passes between the adjacent heat exchange units;
A communication portion provided at two locations across the gas flow path, and communicating the heated liquid flow paths of the adjacent heat exchange units;
With
In the heat exchange unit on one end side in the stacking direction, an inlet and an outlet for the liquid to be heated are provided on the plate-like member on the side opposite to the side on which the communication portion is provided in the stacking direction. And
The heat exchange unit is provided across the communication portions provided at two locations in the heated liquid flow path, and is to be heated to short-circuit between the communication portions provided at two locations. It has a cross section that forms the heated liquid passage in an annular shape by obstructing the flow of the liquid,
A heat exchanger characterized by that.
前記横断部は、前記被加熱液流路の中心部に形成さ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 crossing portion is formed at a central portion of the heated liquid channel. 2箇所に設けられた前記連通部は前記横断部を中心として点対称の位置に配置されていることを特徴とする請求項2に記載の熱交換器。   3. The heat exchanger according to claim 2, wherein the communication portions provided at two locations are arranged at point-symmetric positions with respect to the transverse portion. 2箇所の各箇所に設けられた前記連通部と、各箇所の前記連通部と同じ前記積層方向上に設けられた前記流入口および前記流出口とは、前記被加熱液流路を形成する前記熱交換ユニットの内壁面の内周縁と接していることを特徴とする請求項1から3のいずれか一項に記載の熱交換器。   The communication portion provided at each of the two locations, and the inlet and the outlet provided on the same stacking direction as the communication portion at each location form the heated liquid flow path. The heat exchanger according to any one of claims 1 to 3, wherein the heat exchanger unit is in contact with an inner peripheral edge of an inner wall surface of the heat exchange unit. 2箇所のうち一方に設けられた前記連通部および前記流入口、ならびに2箇所のうち他方に設けられた前記連通部および前記流出口に前記内周縁がそれぞれ接している箇所の前記内壁面は、前記接している箇所を通る接線に対して前記接している箇所の両側の前記内壁面をそれぞれ所定角度傾斜させることにより凹部を形成していることを特徴とする請求項4に記載の熱交換器。   The communication portion and the inlet provided at one of the two locations, and the inner wall surface of the location where the inner peripheral edge is in contact with the communication portion and the outlet provided at the other of the two locations, 5. The heat exchanger according to claim 4, wherein a concave portion is formed by inclining the inner wall surfaces on both sides of the contacting portion with a predetermined angle with respect to a tangent line passing through the contacting portion. . 前記横断部を挟んで前記横断部による横断方向の両側、ならびに前記横断部を挟んで前記横断方向と直交する方向の両側にそれぞれ形成されている前記被加熱液流路の幅は等しいことを特徴とする請求項1から5のいずれか一項に記載の熱交換器。   The widths of the heated liquid passages formed on both sides in the transverse direction by the transverse part across the transverse part and on both sides in the direction perpendicular to the transverse direction across the transverse part are equal. The heat exchanger according to any one of claims 1 to 5. 給湯側加熱回路と、
前記給湯側加熱回路の通水を加熱する主バーナと、
主加熱回路である前記給湯側加熱回路とは別に設けられ、1次熱交換器、ならびに前記1次熱交換器を通過した燃焼ガスの潜熱を回収する2次熱交換器を有する副加熱回路と、
前記副加熱回路の通水を加熱する副バーナと、
を備え、
前記副加熱回路の前記2次熱交換器として請求項1から6のいずれか一項に記載の熱交換器を使用する、
ことを特徴とする給湯器。
A hot water supply side heating circuit;
A main burner for heating the water flow of the hot water supply side heating circuit;
A sub heating circuit provided separately from the hot water supply side heating circuit, which is a main heating circuit, and having a primary heat exchanger and a secondary heat exchanger that recovers the latent heat of the combustion gas that has passed through the primary heat exchanger; ,
A sub-burner for heating the water passing through the sub-heating circuit;
With
The heat exchanger according to any one of claims 1 to 6 is used as the secondary heat exchanger of the sub-heating circuit.
A water heater characterized by that.
JP2010273657A 2010-12-08 2010-12-08 Heat exchanger and water heater using the same Pending JP2012122663A (en)

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KR20190123206A (en) * 2018-04-23 2019-10-31 린나이코리아 주식회사 Heat exchange device

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JPH0433865U (en) * 1990-06-29 1992-03-19
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WO2017135730A1 (en) * 2016-02-05 2017-08-10 주식회사 경동나비엔 Heat exchanger
US11054188B2 (en) 2016-02-05 2021-07-06 Kyungdong Navien Co., Ltd. Heat exchanger
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