JP2005274028A - Combustion device - Google Patents

Combustion device Download PDF

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JP2005274028A
JP2005274028A JP2004088402A JP2004088402A JP2005274028A JP 2005274028 A JP2005274028 A JP 2005274028A JP 2004088402 A JP2004088402 A JP 2004088402A JP 2004088402 A JP2004088402 A JP 2004088402A JP 2005274028 A JP2005274028 A JP 2005274028A
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heat
heat exchanger
combustion
combustion gas
heat receiving
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JP2004088402A
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Inventor
Nobuhiro Takeda
信宏 竹田
Kazuhiro Kimura
和宏 木村
Akira Tsutsumi
明 堤
Hiroshi Asakura
宏 朝倉
Norihiro Hori
紀弘 堀
Ichiro Otomo
一朗 大友
Takayasu Fujita
貴康 藤田
Masakuni Morikawa
正邦 森川
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Noritz Corp
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Noritz Corp
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Priority to JP2004088402A priority Critical patent/JP2005274028A/en
Priority to PCT/JP2005/005241 priority patent/WO2005093335A1/en
Priority to US10/593,350 priority patent/US7647897B2/en
Priority to DE112005000642T priority patent/DE112005000642T5/en
Publication of JP2005274028A publication Critical patent/JP2005274028A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To develop a combustion device having improved heat efficiency without excessively increasing its whole shape. <P>SOLUTION: The combustion device 1 comprises a canned body 2, a primary heat exchanger 3 (a sensible heat recovery heat exchanger), and a combustion burner 5 (a combustion means) and a blowing means 6. A secondary heat exchanger 7 (a latent heat recovery heat exchanger) has a plurality of heat receiving tubes 18 arranged in parallel between a pair of headers 16, 17. In this embodiment, the heat receiving tubes 18 are mounted on a tube plate 20 on which the heat receiving tubes 18 are mounted. The heat receiving tubes 18 are bare tubes which are arranged in the direction of crossing the flow of combustion gas. The stack number of the receiving tubes 18 in the vertical direction is less than the stack number thereof in the lateral direction. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は燃焼装置に関するものであり、特に潜熱回収用の熱交換器を備えた燃焼装置に関するものである。   The present invention relates to a combustion apparatus, and more particularly to a combustion apparatus provided with a heat exchanger for recovering latent heat.

給湯器や風呂装置等の熱源として、ガスや液体燃料を燃焼する燃焼装置が多用されている。また近年、省エネルギーや環境保護の観点から、従来の燃焼装置よりもさらに熱効率の高い燃焼装置が切望されている。そこで、かかる要望を解決すべく複数の熱交換器を備えた燃焼装置や、燃焼ガスの顕熱に加えて潜熱も回収可能な潜熱回収型燃焼装置と称する燃焼装置が提案されている。
従来技術の潜熱回収型燃焼装置は、例えば下記特許文献1に開示されている様な構成を有するものであり、主として燃焼ガスの顕熱を回収する顕熱回収用熱交換器と、主として燃焼ガスの潜熱を回収する(残存する顕熱も回収する)潜熱回収用熱交換器を備えたものである。
特開平11−148642号公報
Combustion devices that burn gas or liquid fuel are often used as heat sources for water heaters, bath devices, and the like. In recent years, from the viewpoint of energy saving and environmental protection, a combustion apparatus having higher thermal efficiency than the conventional combustion apparatus is desired. In order to solve such a demand, a combustion apparatus provided with a plurality of heat exchangers and a combustion apparatus called a latent heat recovery type combustion apparatus capable of recovering latent heat in addition to sensible heat of combustion gas have been proposed.
A conventional latent heat recovery combustion apparatus has a configuration as disclosed in, for example, Patent Document 1 below, and mainly includes a sensible heat recovery heat exchanger that recovers sensible heat of combustion gas, and mainly combustion gas. It is provided with a latent heat recovery heat exchanger that recovers the latent heat (recovers the remaining sensible heat).
JP-A-11-148642

図11は、特許文献1に記載された燃焼装置のモデル図である。特許文献1に記載された潜熱回収型燃焼装置では、図11の様に潜熱回収用熱交換器としてフィン付き管100が使用されている。ここでフィン付き管100とは、受熱管の周囲にフィンが溶接されたものであり、フィンチューブとも称されるものである。
そして従来技術においては、フィン付き管100は燃焼ガス流路101の中に直接的に挿入されている。即ち従来技術では、図11の様に壁体102によって燃焼ガス流路101が構成されており、この壁体102によって構成された燃焼ガス流路101内にフィン付き管100が挿入されている。従来技術においては、燃焼ガス流路101内のフィン付き管100は図の様に直列的に配されている。
FIG. 11 is a model diagram of the combustion apparatus described in Patent Document 1. In the latent heat recovery combustion apparatus described in Patent Document 1, a finned tube 100 is used as a latent heat recovery heat exchanger as shown in FIG. Here, the finned tube 100 is a tube in which fins are welded around the heat receiving tube, and is also referred to as a fin tube.
In the prior art, the finned tube 100 is directly inserted into the combustion gas passage 101. That is, in the prior art, the combustion gas flow path 101 is configured by the wall body 102 as shown in FIG. 11, and the finned tube 100 is inserted into the combustion gas flow path 101 formed by the wall body 102. In the prior art, the finned tubes 100 in the combustion gas passage 101 are arranged in series as shown in the figure.

従来技術の潜熱回収型燃焼装置は、通常の燃焼装置に比べて熱効率が高い。しかしながら市場においては、熱効率のさらなる向上が望まれている。
ここで熱効率を向上させるための方策として、燃焼ガス流路101内に挿入されるフィン付き管100の全長を長くして潜熱回収用熱交換器の熱交換効率を高めることが考えられる。しかしフィン付き管100の全長を長くすると潜熱回収用熱交換器が占有する容積が大きくなってしまい、燃焼装置の全体形状が大きくなってしまうという弊害がある。
The conventional latent heat recovery type combustion apparatus has higher thermal efficiency than a normal combustion apparatus. However, further improvement in thermal efficiency is desired in the market.
Here, as a measure for improving the thermal efficiency, it is conceivable to increase the heat exchange efficiency of the latent heat recovery heat exchanger by lengthening the entire length of the finned tube 100 inserted into the combustion gas flow path 101. However, when the overall length of the finned tube 100 is increased, the volume occupied by the latent heat recovery heat exchanger increases, which has the disadvantage of increasing the overall shape of the combustion apparatus.

そこで本発明は、全体形状が過度に大きくならずに熱効率のさらなる向上を図ることができる燃焼装置の開発を課題とするものである。   Accordingly, an object of the present invention is to develop a combustion apparatus that can further improve thermal efficiency without excessively increasing the overall shape.

上記した課題を解決する為に鋭意研究したところ、潜熱回収用熱交換器の熱交換効率を低下させる要因として、ドレンの影響が大きいことが判明した。即ち潜熱回収型燃焼装置は、燃焼ガスの持つ潜熱まで回収するものであるため、燃焼ガスに含まれる水蒸気が液化して大量のドレンが発生する。このドレンは潜熱回収用熱交換器の表面に発生するので燃焼ガスは当該ドレンと接することとなり、燃焼ガスの熱エネルギーがドレンに奪われる。そのため燃焼ガスの熱はドレンの再気化に消費されてしまい、熱交換器内の湯水の昇温に寄与する熱エネルギーが減じてしまう。   As a result of diligent research to solve the above-mentioned problems, it has been found that the influence of the drain is large as a factor for reducing the heat exchange efficiency of the heat exchanger for recovering latent heat. That is, since the latent heat recovery type combustion apparatus recovers even the latent heat of the combustion gas, the water vapor contained in the combustion gas is liquefied and a large amount of drain is generated. Since this drain is generated on the surface of the heat exchanger for recovering latent heat, the combustion gas comes into contact with the drain, and the thermal energy of the combustion gas is taken away by the drain. Therefore, the heat of the combustion gas is consumed for re-evaporating the drain, and the thermal energy contributing to the temperature rise of the hot water in the heat exchanger is reduced.

加えて、大量のドレンが潜熱回収用熱交換器の表面に付着すると、当該ドレンが潜熱回収用熱交換器内部への熱の移行を妨げ、熱交換効率を大幅に低下させてしまう。
また全体形状を過度に大きくすることなく、燃焼ガスとの大きな接触面積を確保するためには、多数の受熱管を並列的に並べた構造の熱交換器を採用することが望ましいことが判明した。なお多数の受熱管を並列的に並べた構造の熱交換器は、一般的に小型化が困難であるとされ、燃焼装置の潜熱回収用熱交換器として採用された例はない。一般的にコンパクトで高効率の熱交換器が必要な機器に対しては、積層式熱交換器が採用される場合が多いが、本発明者らの研究によると、積層式熱交換器はドレンの排出性能が劣り、燃焼装置の潜熱回収用熱交換器として採用するには前記した多数の受熱管を並列的に並べた構造の熱交換器の方が適する。
In addition, if a large amount of drain adheres to the surface of the latent heat recovery heat exchanger, the drain hinders the transfer of heat into the latent heat recovery heat exchanger, thereby greatly reducing the heat exchange efficiency.
It was also found that it is desirable to use a heat exchanger with a structure in which a large number of heat receiving tubes are arranged in parallel in order to ensure a large contact area with the combustion gas without excessively increasing the overall shape. . A heat exchanger having a structure in which a large number of heat receiving tubes are arranged in parallel is generally difficult to downsize, and there is no example of adopting it as a heat exchanger for recovering latent heat of a combustion apparatus. In general, a stack type heat exchanger is often used for a device that requires a compact and highly efficient heat exchanger, but according to the study of the present inventors, the stack type heat exchanger is a drain. Therefore, a heat exchanger having a structure in which a large number of heat receiving tubes are arranged in parallel is more suitable for use as a heat exchanger for recovering latent heat of a combustion apparatus.

また多数の受熱管を並列的に並べた構造の熱交換器は、積層式熱交換器に比べて設計の自由度も高い。即ち多数の受熱管を並列的に並べた構造の熱交換器は、管の長さや縦横の配列を適宜選定することにより、外形形状の設計変更が可能であり、燃焼装置に合わせた形状に設計することが容易である。そのため燃焼装置に余分な空隙が生じ難く、結果的に燃焼装置の小型化に寄与する。   Further, a heat exchanger having a structure in which a large number of heat receiving tubes are arranged in parallel has a higher degree of design freedom than a stacked heat exchanger. In other words, heat exchangers with a structure in which a large number of heat receiving tubes are arranged in parallel can be changed in external shape design by appropriately selecting the length and vertical and horizontal arrangement of the tubes, and are designed to match the combustion equipment. Easy to do. For this reason, it is difficult for an extra air gap to be generated in the combustion apparatus, and as a result, it contributes to downsizing of the combustion apparatus.

上記した知見に基づく請求項1に記載の発明は、燃焼手段と、主として燃焼手段において発生した燃焼ガスの顕熱を回収して湯水を加熱する顕熱回収用熱交換器と、当該顕熱回収用熱交換器に対して燃焼ガス流路の下流側に配置され、主として前記燃焼ガスの潜熱を回収して湯水を加熱する潜熱回収用熱交換器を備え、前記潜熱回収用熱交換器を通過した湯水が前記顕熱回収用熱交換器に流れる様に配管された燃焼装置において、前記潜熱回収用熱交換器は多数の受熱管が並列的に並べられたものであることを特徴とする燃焼装置である。   The invention according to claim 1 based on the above-described knowledge includes a combustion means, a sensible heat recovery heat exchanger that recovers sensible heat of combustion gas generated mainly in the combustion means and heats hot water, and the sensible heat recovery. A heat exchanger for latent heat recovery, which is disposed downstream of the combustion gas flow path with respect to the heat exchanger for heat and mainly recovers the latent heat of the combustion gas and heats the hot water, and passes through the heat exchanger for latent heat recovery In the combustion apparatus piped so that the hot and cold water flows to the sensible heat recovery heat exchanger, the latent heat recovery heat exchanger is composed of a large number of heat receiving tubes arranged in parallel. Device.

本発明の燃焼装置では、潜熱回収用熱交換器として多数の受熱管を並列的に並べたものが採用されている。そのため本発明の燃焼装置では、燃焼ガスと受熱管との接触機会が多く、熱効率が高い。   In the combustion apparatus of the present invention, a heat exchanger for latent heat recovery in which a large number of heat receiving tubes are arranged in parallel is employed. Therefore, in the combustion apparatus of the present invention, there are many opportunities for contact between the combustion gas and the heat receiving pipe, and the thermal efficiency is high.

また請求項2に記載の発明は、潜熱回収用熱交換器の受熱管は、裸管であることを特徴とする請求項1に記載の燃焼装置である。   The invention according to claim 2 is the combustion apparatus according to claim 1, wherein the heat receiving pipe of the heat exchanger for recovering latent heat is a bare pipe.

気・液間の熱交換を行う熱交換器では、一般に、燃焼ガス等との接触機会を増大させることを目的としてフィン付きの受熱管が使用される。逆に気・液間の熱交換を行う熱交換器では、受熱管として裸管が使用されることは稀である。
しかしながら本発明者らの研究によると、潜熱回収用熱交換器の受熱管に、フィンの無い裸管を使用した場合でも十分高い熱効率が得られることが判明した。
即ち潜熱回収型燃焼装置は、燃焼ガスの持つ潜熱まで回収するものであるため、燃焼ガスに含まれる水蒸気が液化して大量のドレンが発生する。従来技術で採用していた潜熱回収用熱交換器では受熱管にフィンが設けられていたので、フィンにドレンが付着し、受熱管にドレンの皮膜ができてしまう。
そのため燃焼ガスの熱エネルギーの多くがドレンの再気化に消費され、熱交換器内の湯水の昇温に寄与する熱エネルギーが減じてしまう。特にフィンとフィンの間にドレンが溜まると、受熱管の周囲をドレンが大きく取り巻くこととなり、熱交換効率が著しく低下する。
また従来技術で採用していた潜熱回収用熱交換器では受熱管にフィンがあるためにドレンの離脱が困難であり、熱交換効率が低下する。
これに対して本発明では、受熱管が裸管であるため、ドレンの離脱が円滑であり、受熱管に形成されるドレンの皮膜が薄く、熱交換効率の低下が少ない。
In heat exchangers that exchange heat between gas and liquid, finned heat receiving tubes are generally used for the purpose of increasing the chance of contact with combustion gas and the like. In contrast, in a heat exchanger that performs heat exchange between gas and liquid, bare tubes are rarely used as heat receiving tubes.
However, according to the study by the present inventors, it has been found that a sufficiently high thermal efficiency can be obtained even when a bare tube without fins is used as the heat receiving tube of the latent heat recovery heat exchanger.
That is, since the latent heat recovery type combustion apparatus recovers even the latent heat of the combustion gas, the water vapor contained in the combustion gas is liquefied and a large amount of drain is generated. In the heat exchanger for recovering latent heat employed in the prior art, the fins are provided on the heat receiving pipe, so that the drain adheres to the fins and a drain film is formed on the heat receiving pipe.
Therefore, most of the heat energy of the combustion gas is consumed for re-evaporating the drain, and the heat energy contributing to the temperature rise of the hot water in the heat exchanger is reduced. In particular, when the drain is accumulated between the fins, the drain is greatly surrounded around the heat receiving tube, and the heat exchange efficiency is significantly reduced.
Further, in the heat exchanger for latent heat recovery employed in the prior art, it is difficult to remove the drain due to the fins in the heat receiving pipe, and the heat exchange efficiency is lowered.
On the other hand, in the present invention, since the heat receiving pipe is a bare pipe, the drain is smoothly detached, the drain film formed on the heat receiving pipe is thin, and the heat exchange efficiency is hardly lowered.

また請求項3に記載の発明は、潜熱回収用熱交換器の受熱管は、天地方向と横方向に積層された立体構造を構成しており、天地方向の積層数が横方向の積層数に比べて少ないことを特徴とする請求項1又は2に記載の燃焼装置である。   In the invention according to claim 3, the heat receiving pipe of the heat exchanger for recovering latent heat has a three-dimensional structure laminated in the vertical direction and the horizontal direction, and the number of laminations in the vertical direction is equal to the number of laminations in the horizontal direction. The combustion apparatus according to claim 1, wherein the combustion apparatus is less in number.

本発明の燃焼装置では、潜熱回収用熱交換器の受熱管は、天地方向と横方向に積層された立体構造を構成しているが、天地方向の積層数が横方向の積層数に比べて少ない。そのためドレンの離脱が円滑である。
即ち受熱管を立体的に積層すると、上段側で発生したドレンが下段に位置する受熱管に落下し、下断に位置する受熱管に付着するドレン量が増大して下段側に位置する受熱管の熱交換効率が低下してしまう。
これに対して本発明では、受熱管の積層数は、天地方向が横方向の積層数に比べて少ない。そのため本発明の燃焼装置では、受熱管の高さ方向の積層数が少なく、上段側で発生したドレンが下段の受熱管に与える影響が小さい。
In the combustion apparatus of the present invention, the heat receiving tube of the heat exchanger for recovering latent heat constitutes a three-dimensional structure laminated in the vertical direction and the horizontal direction, but the number of vertical layers is larger than the number of horizontal layers. Few. Therefore, draining is smooth.
That is, when the heat receiving pipes are three-dimensionally stacked, the drain generated on the upper stage falls to the heat receiving pipe located on the lower stage, and the amount of drain adhering to the heat receiving pipe located on the lower end increases, and the heat receiving pipe located on the lower stage side. The heat exchange efficiency will be reduced.
On the other hand, in the present invention, the number of stacked heat receiving tubes is smaller than the number of stacked layers in the vertical direction. Therefore, in the combustion apparatus of the present invention, the number of stacks in the height direction of the heat receiving tubes is small, and the influence of the drain generated on the upper stage side on the lower heat receiving tubes is small.

また請求項4に記載の発明は、潜熱回収用熱交換器の受熱管は、燃焼ガスの流れを横切る方向に配列されていることを特徴とする請求項1乃至3のいずれかに記載の燃焼装置である。   According to a fourth aspect of the present invention, in the combustion according to any one of the first to third aspects, the heat receiving tubes of the heat exchanger for recovering latent heat are arranged in a direction crossing the flow of the combustion gas. Device.

本発明の燃焼装置では、潜熱回収用熱交換器の受熱管が燃焼ガスの流れを横切る方向に配列されているので、受熱管に付着したドレンが燃焼ガスによって吹き飛ばされやすい。そのため受熱管に形成されるドレンの皮膜が薄く、熱交換効率の低下が少ない。   In the combustion apparatus of the present invention, since the heat receiving tubes of the latent heat recovery heat exchanger are arranged in a direction crossing the flow of the combustion gas, the drain adhering to the heat receiving tube is easily blown off by the combustion gas. Therefore, the drain film formed on the heat receiving tube is thin, and the heat exchange efficiency is hardly lowered.

また請求項5に記載の発明は、潜熱回収用熱交換器は、一対のヘッダ間に複数の受熱管が並列的に並べられたものであり、前記ヘッダは、受熱管が取り付けられる管板と当該管板の背面側に設けられた端室部材を備え、前記ヘッダが燃焼手段から排気部に至る一連の燃焼ガス流路の壁面の一部を構成していることを特徴とする請求項1乃至4のいずれかに記載の燃焼装置である。   In the invention according to claim 5, the heat exchanger for recovering latent heat has a plurality of heat receiving tubes arranged in parallel between a pair of headers, and the header includes a tube plate to which the heat receiving tubes are attached. 2. An end chamber member provided on the back side of the tube sheet, wherein the header constitutes a part of a wall surface of a series of combustion gas passages extending from the combustion means to the exhaust part. It is a combustion apparatus in any one of thru | or 4.

本発明の燃焼装置では、潜熱回収用熱交換器のヘッダが燃焼ガス流路の壁面の一部を構成しているので、燃焼装置の全体形状を小型化することができる。   In the combustion apparatus of the present invention, since the header of the latent heat recovery heat exchanger constitutes a part of the wall surface of the combustion gas flow path, the overall shape of the combustion apparatus can be reduced in size.

本発明の燃焼装置は、小型でありながら熱交換効率が優れるという効果がある。   The combustion apparatus of the present invention has an effect that heat exchange efficiency is excellent while being small.

続いて、本発明の一実施形態である燃焼装置について図面を参照しながら詳細に説明する。図1は、本実施形態の燃焼装置の構成図である。図2は、図1に示す燃焼装置の二次熱交換器近傍を示す分解斜視図である。図3は、二次熱交換器および排気部材を示す斜視図である。図4は、図3に示す二次熱交換器の分解斜視図である。図5は、図3に示す二次熱交換器のA−A断面図である。図6(a)は、図3に示す二次熱交換器における受熱管の配置を示す模式図であり、同(b),(c)は同(a)に示す受熱管の配置の変形例を示す模式図である。図7(a),図8(a)は、それぞれ図3に示す二次熱交換器のカップ部材を示す斜視図であり、図7(b),図8(b)は、図7(a),図8(a)のA−A断面図である。図9は、図3に示す熱交換器におけるカップ部材と管板の関係を示す断面図である。図10は、本実施形態の燃焼装置の外観図である。   Subsequently, a combustion apparatus according to an embodiment of the present invention will be described in detail with reference to the drawings. FIG. 1 is a configuration diagram of the combustion apparatus of the present embodiment. FIG. 2 is an exploded perspective view showing the vicinity of the secondary heat exchanger of the combustion apparatus shown in FIG. FIG. 3 is a perspective view showing the secondary heat exchanger and the exhaust member. FIG. 4 is an exploded perspective view of the secondary heat exchanger shown in FIG. FIG. 5 is a cross-sectional view of the secondary heat exchanger shown in FIG. Fig.6 (a) is a schematic diagram which shows arrangement | positioning of the heat receiving tube in the secondary heat exchanger shown in FIG. 3, (b), (c) is a modification of arrangement | positioning of the heat receiving tube shown to (a). It is a schematic diagram which shows. FIGS. 7A and 8A are perspective views showing the cup member of the secondary heat exchanger shown in FIG. 3, and FIGS. 7B and 8B are FIGS. ), An AA cross-sectional view of FIG. FIG. 9 is a cross-sectional view showing the relationship between the cup member and the tube sheet in the heat exchanger shown in FIG. FIG. 10 is an external view of the combustion apparatus of the present embodiment.

図1において、1は本実施形態の燃焼装置である。燃焼装置1は、缶体2と、一次熱交換器3(顕熱回収型熱交換器)と、燃焼バーナ5(燃焼手段)および送風手段6を設けた構成である。また、一次熱交換器3に対して燃焼ガス流路8の下流側(図1において上方側)には、主として燃焼ガス中から潜熱を回収する潜熱回収用の二次熱交換器7(潜熱回収用熱交換器)が配されている。   In FIG. 1, 1 is a combustion apparatus of this embodiment. The combustion apparatus 1 has a configuration in which a can body 2, a primary heat exchanger 3 (sensible heat recovery type heat exchanger), a combustion burner 5 (combustion means), and a blower means 6 are provided. Further, on the downstream side (upper side in FIG. 1) of the combustion gas flow path 8 with respect to the primary heat exchanger 3, a secondary heat exchanger 7 (latent heat recovery) for recovering latent heat mainly recovering latent heat from the combustion gas. Heat exchanger).

一次熱交換器3は、主要部分が銅製のいわゆるフィン・アンド・チューブ型の熱交換器である。一次熱交換器3は、燃焼バーナ5で発生する高温の燃焼ガスが流れる燃焼ガス流路8内に配置されている。一次熱交換器3は、主として燃焼ガスが持つ顕熱を回収する顕熱回収手段として機能するものであり、内部を流れる湯水を加熱するものである。   The primary heat exchanger 3 is a so-called fin-and-tube heat exchanger whose main part is made of copper. The primary heat exchanger 3 is disposed in a combustion gas flow path 8 through which high-temperature combustion gas generated in the combustion burner 5 flows. The primary heat exchanger 3 mainly functions as sensible heat recovery means for recovering sensible heat of the combustion gas, and heats hot water flowing inside.

一次熱交換器3は、入水口10と、出水口11とを備えている。入水口10は、二次熱交換器7の出水口13側に接続されている。一次熱交換器3には二次熱交換器7において熱交換された後の湯水が流入する。   The primary heat exchanger 3 includes a water inlet 10 and a water outlet 11. The water inlet 10 is connected to the water outlet 13 side of the secondary heat exchanger 7. Hot water after heat exchange in the secondary heat exchanger 7 flows into the primary heat exchanger 3.

一次熱交換器3は、燃焼バーナ5が配された缶体2の燃焼ガス流路8内を流れる燃焼ガスと熱交換を行うものであり、出水口11には図示しない暖房装置等の負荷端末や給湯栓が接続されている。   The primary heat exchanger 3 exchanges heat with the combustion gas flowing in the combustion gas flow path 8 of the can body 2 in which the combustion burner 5 is arranged, and the outlet 11 is a load terminal such as a heating device (not shown). Or a hot water tap is connected.

二次熱交換器7は、図1および図2に示すように、接続部材14を介して缶体2に接続されている。接続部材14は、図2に示すように缶体2の開口部分に接続される集合部14aと、接続部14bとが略「L」字型に配されており、内部に連通した流路を形成している。接続部14bは、二次熱交換器7のケース部材15(胴体部)の背面に対して面接触し、気密状態となる部分であり、ケース部材15の内部に燃焼ガスを導入するための開口14cが設けられている。   As shown in FIGS. 1 and 2, the secondary heat exchanger 7 is connected to the can body 2 via a connection member 14. As shown in FIG. 2, the connecting member 14 has a collecting portion 14a connected to the opening portion of the can body 2 and a connecting portion 14b arranged in a substantially “L” shape, and has a flow path communicating with the inside. Forming. The connection portion 14 b is a portion that comes into surface contact with the back surface of the case member 15 (body portion) of the secondary heat exchanger 7 and is in an airtight state. The connection portion 14 b is an opening for introducing combustion gas into the case member 15. 14c is provided.

二次熱交換器7は、図3および図4に示すように、中空で箱状のケース部材15の両端部に平行に配置されたヘッダ16,17に多数の受熱管18をろう付けして接続したものである。
ケース部材15は、金属板を折り曲げ加工して図4に示すような「コ」の字状を形成させ、さらに天面板70を取り付けて図3に示すような箱形を構成した部材である。即ちケース部材15は、天面板70、正面板71、背面板72及び底面板73を有し、側面部分74,75は開口している。ケース部材15の側面部分74,75は、後記する様にヘッダ16,17によって閉塞される。ケース部材15は、正面に排出口15a(排気部)があり、背面に導入口15bがある。
As shown in FIGS. 3 and 4, the secondary heat exchanger 7 is configured by brazing a large number of heat receiving tubes 18 to headers 16 and 17 arranged in parallel to both ends of a hollow box-shaped case member 15. Connected.
The case member 15 is a member in which a metal plate is bent to form a “U” shape as shown in FIG. 4, and a top plate 70 is attached to form a box shape as shown in FIG. 3. That is, the case member 15 includes a top plate 70, a front plate 71, a back plate 72, and a bottom plate 73, and the side portions 74 and 75 are open. The side surface portions 74 and 75 of the case member 15 are closed by the headers 16 and 17 as described later. The case member 15 has a discharge port 15a (exhaust part) on the front surface and an introduction port 15b on the back surface.

排出口15aは、二次熱交換器7から燃焼ガスを排出するための開口である。排出口15aの前面側には、図3に示すように4つの開口を有する排気部材19が装着される。また、導入口15bは、一次熱交換器3を通過した燃焼ガスを二次熱交換器7内に導入するためのものであり、接続部材14を介して二次熱交換器7を缶体2に接続した際に接続部材の開口14cに相当する位置に設けられている。導入口15bから導入された燃焼ガスは、ケース部材15内を横断する多数の受熱管18同士の隙間を通過し、受熱管18内の湯水と熱交換を行う。受熱管18内の湯水と熱交換を行った燃焼ガスは、排出口15aから二次熱交換器7の外部に排出される。   The discharge port 15 a is an opening for discharging combustion gas from the secondary heat exchanger 7. As shown in FIG. 3, an exhaust member 19 having four openings is mounted on the front side of the discharge port 15a. The inlet 15b is for introducing the combustion gas that has passed through the primary heat exchanger 3 into the secondary heat exchanger 7, and the secondary heat exchanger 7 is connected to the can body 2 via the connecting member 14. Is provided at a position corresponding to the opening 14c of the connection member. The combustion gas introduced from the inlet 15 b passes through the gaps between the many heat receiving pipes 18 that traverse the inside of the case member 15, and exchanges heat with the hot water in the heat receiving pipe 18. The combustion gas that has exchanged heat with the hot water in the heat receiving pipe 18 is discharged to the outside of the secondary heat exchanger 7 through the discharge port 15a.

受熱管18は、金属製の管体であり、それぞれ燃焼ガスが通過可能な程度の隙間を空けて平行に配置されている。二次熱交換器7は、各受熱管18を流れる湯水がヘッダ16,17において流れ方向を折り返し、ケース部材15に対して往復動してから排出される。本実施形態で採用する受熱管18は、ステンレススチール等の腐食に強い素材で作られている。また本実施形態で採用する受熱管18は、裸管であり、フィンを持たない。   The heat receiving pipes 18 are metal pipes, and are arranged in parallel with gaps that allow the combustion gas to pass therethrough. The secondary heat exchanger 7 is discharged after the hot water flowing through each heat receiving pipe 18 turns back in the flow direction in the headers 16 and 17 and reciprocates with respect to the case member 15. The heat receiving pipe 18 employed in the present embodiment is made of a corrosion resistant material such as stainless steel. Further, the heat receiving pipe 18 employed in the present embodiment is a bare pipe and does not have fins.

二次熱交換器7を構成する受熱管18は、図4に示す状態で配置した際に、本体ケース15の上下方向に4本の受熱管18が並び、本体ケース15の幅方向に8本の受熱管18が並んだ状態とされている。即ち本実施形態では、二次熱交換器7(潜熱回収用熱交換器)の受熱管18は、天地方向と横方向に積層された立体構造を構成しており、天地方向の積層数が横方向の積層数に比べて少ない。なお天地方向の積層数は横方向の積層数の1/2以下であることが望ましい。
二次熱交換器7は、図4の矢印P方向から観察すると図6(a)の様に受熱管18が錯列(千鳥状)に並べられた構成となっている。受熱管18の並べ方は、図6(a)の様に錯列であることが望ましいが、図6(b)の様な行列状であってもよい。
When the heat receiving pipes 18 constituting the secondary heat exchanger 7 are arranged in the state shown in FIG. 4, four heat receiving pipes 18 are arranged in the vertical direction of the main body case 15 and eight in the width direction of the main body case 15. The heat receiving pipes 18 are arranged side by side. That is, in the present embodiment, the heat receiving pipe 18 of the secondary heat exchanger 7 (latent heat recovery heat exchanger) has a three-dimensional structure laminated in the vertical direction and the horizontal direction, and the number of stacked layers in the vertical direction is horizontal. Less than the number of layers in the direction. It is desirable that the number of stacks in the vertical direction is not more than ½ of the number of stacks in the horizontal direction.
When the secondary heat exchanger 7 is observed from the direction of the arrow P in FIG. 4, the heat receiving tubes 18 are arranged in an array (staggered) as shown in FIG. 6A. The arrangement of the heat receiving tubes 18 is preferably a complex array as shown in FIG. 6A, but may be a matrix as shown in FIG. 6B.

ケース部材15内に配されている受熱管18のうち、導入口15b側から1列目および2列目に配置されたものは、上流受熱管群23を構成し、これに隣接する3〜6列目のものは中流受熱管群24,25として分類される。また、導入口15b側から7列目および8列目、即ち排出口15a側から1列目および2列目に配された受熱管18は、下流受熱管群26を構成する。   Among the heat receiving pipes 18 arranged in the case member 15, those arranged in the first and second rows from the inlet 15 b side constitute the upstream heat receiving pipe group 23, and 3 to 6 adjacent thereto. The columns in the row are classified as the midstream heat receiving tube groups 24 and 25. Further, the heat receiving pipes 18 arranged in the seventh and eighth rows from the inlet 15b side, that is, the first and second rows from the outlet 15a side constitute a downstream heat receiving pipe group 26.

ヘッダ16は、図3、図4および図5に示すように、管板20に対して椀状のカップ部材30,31,32(端室部材)を3つ並べてろう付けした構成とされている。また、ヘッダ17は、管板20に対して椀状のカップ部材33,35(端室部材)を2つ並べてろう付けしたものである。   As shown in FIGS. 3, 4, and 5, the header 16 is configured such that three cup-shaped cup members 30, 31, and 32 (end chamber members) are aligned and brazed to the tube plate 20. . The header 17 is formed by brazing two cup-shaped cup members 33 and 35 (end chamber members) to the tube plate 20.

管板20は、金属製であり、平板状の平板部37の接続面37aに受熱管18の配列に合わせて多数の管差込孔38を設けると共に、四辺を折り曲げて段部40を形成したものである。段部40は、カップ部材30,31,32の接合側、即ち平板部37の接合面37b側に突出している。ヘッダ16側の管板20は、平板部37が大別して上流受熱管群23が接続される領域Aと、中流受熱管群24,25が接続される領域B、下流受熱管群26が接続される領域Cの3領域に分類される。また、ヘッダ17側の管板20の平板部37は、大別して上流受熱管群23および中流受熱管群24が接続される領域Dおよび中流受熱管群25および下流受熱管群26が接続される領域Eに分類される。管板20は、図4のようにケース部材15の両端部分を閉塞するようにろう付けされ、気密状態となるように接合されている。したがってケース部材15の側面部分74,75は、ヘッダ16,17の管板20によって閉塞される。   The tube plate 20 is made of metal, and a plurality of tube insertion holes 38 are provided on the connection surface 37a of the flat plate portion 37 in accordance with the arrangement of the heat receiving tubes 18, and the step portions 40 are formed by bending four sides. Is. The step portion 40 protrudes to the joining side of the cup members 30, 31, 32, that is, the joining surface 37 b side of the flat plate portion 37. The tube plate 20 on the header 16 side is divided into a region A where the flat plate portion 37 is roughly divided and the upstream heat receiving tube group 23 is connected, a region B where the midstream heat receiving tube groups 24 and 25 are connected, and a downstream heat receiving tube group 26. The region C is classified into three regions. Further, the flat plate portion 37 of the tube plate 20 on the header 17 side is roughly divided into a region D to which the upstream heat receiving tube group 23 and the midstream heat receiving tube group 24 are connected, and the midstream heat receiving tube group 25 and the downstream heat receiving tube group 26. The region E is classified. As shown in FIG. 4, the tube plate 20 is brazed so as to close both end portions of the case member 15 and joined so as to be in an airtight state. Therefore, the side portions 74 and 75 of the case member 15 are closed by the tube plates 20 of the headers 16 and 17.

カップ部材30,31は、それぞれ上記した接合面37bの領域A,Cに覆い被さるようにろう付けされた部材である。カップ部材30,31は、図5のように管板20の接合面37bとの間に流入室36および流出室39を形成する。カップ部材30,31は、図7のようにフランジ41と、これによって開口部の周囲を囲まれた水室部43とを有する。フランジ41は、ろう材を介して管板20の平板部37に対して略平行に接合される平行部45と、平行部45の外周端を水室部43の膨出方向に向けて略垂直に折り返した離反部46を有する。
水室部43には、カップ部材30,31と管板20によって構成される流入室36および流出室39の内外を連通し、配管を接続するための接続口47が設けられている。カップ部材30側の接続口47は、外部から二次熱交換器7に湯水を供給する流入口47aとして機能し、カップ部材31側の接続口47は、二次熱交換器7において熱交換された湯水を外部に排出する流出口47bとして機能する。
The cup members 30 and 31 are members brazed so as to cover the regions A and C of the joint surface 37b. As shown in FIG. 5, the cup members 30 and 31 form an inflow chamber 36 and an outflow chamber 39 with the joint surface 37 b of the tube plate 20. As shown in FIG. 7, the cup members 30 and 31 have a flange 41 and a water chamber portion 43 surrounded by the periphery of the opening. The flange 41 has a parallel part 45 joined substantially parallel to the flat plate part 37 of the tube sheet 20 via a brazing material, and a substantially vertical direction with the outer peripheral end of the parallel part 45 facing the bulging direction of the water chamber part 43. The separation portion 46 is folded back.
The water chamber portion 43 is provided with a connection port 47 for connecting the inside and outside of the inflow chamber 36 and the outflow chamber 39 constituted by the cup members 30 and 31 and the tube plate 20 to connect the pipe. The connection port 47 on the cup member 30 side functions as an inlet 47 a for supplying hot water to the secondary heat exchanger 7 from the outside, and the connection port 47 on the cup member 31 side is subjected to heat exchange in the secondary heat exchanger 7. It functions as an outlet 47b for discharging hot water to the outside.

カップ部材32,33,35は、図8のようにそれぞれカップ部材30,31に類似した構造を有するものであり、それぞれの大きさおよび形状は同一である。カップ部材32,33,35は、それぞれ、カップ部材30,31のフランジ41と同様の形状のフランジ50を有し、このフランジ50によって取り囲まれた位置にカップ部材30,31の水室部43よりも幅の大きな水室部51が設けられている。   The cup members 32, 33, and 35 have structures similar to the cup members 30 and 31, respectively, as shown in FIG. 8, and the sizes and shapes thereof are the same. The cup members 32, 33, and 35 each have a flange 50 having the same shape as the flange 41 of the cup members 30 and 31, and the water chamber portion 43 of the cup members 30 and 31 is located at a position surrounded by the flange 50. A large water chamber 51 is also provided.

カップ部材32は、図5のように水室部51がヘッダ16側の管板20の中央部にある領域Bの略全域に覆い被さり、中流迂回室55を形成している。また、ヘッダ17側に装着されるカップ部材33,35は、それぞれ管板20の領域D,Eの略全域に覆い被さり、上流迂回室56および下流迂回室57を形成している。   As shown in FIG. 5, the cup member 32 covers the substantially entire region B in the center portion of the tube plate 20 on the header 16 side to form a midstream bypass chamber 55. Further, the cup members 33 and 35 mounted on the header 17 side cover the substantially entire areas of the regions D and E of the tube plate 20 to form an upstream bypass chamber 56 and a downstream bypass chamber 57, respectively.

カップ部材30に設けられた流入口47aには、外部から湯水を供給する給水配管60が接続されている。また、カップ部材31に設けられた流出口47bには、二次熱交換器7と一次熱交換器3とを繋ぐ接続配管61が接続されている。二次熱交換器7は、ヘッダ16,17の管板20,20にろう付け接合されたカップ部材32,33,35により上流受熱管群23、中流受熱管群24,25および下流受熱管群26によって構成される流路同士が接続される。これにより、流入口47aから流出口47bに繋がり、ケース部材15の内部を湯水が往復動する一連の流路が形成されている。   A water supply pipe 60 for supplying hot water from the outside is connected to the inflow port 47 a provided in the cup member 30. A connection pipe 61 that connects the secondary heat exchanger 7 and the primary heat exchanger 3 is connected to the outlet 47 b provided in the cup member 31. The secondary heat exchanger 7 includes an upstream heat receiving tube group 23, a midstream heat receiving tube group 24, 25 and a downstream heat receiving tube group by cup members 32, 33, 35 brazed to the tube plates 20, 20 of the headers 16, 17. 26 are connected to each other. As a result, a series of flow paths are formed which connect the inflow port 47a to the outflow port 47b and allow the hot water to reciprocate inside the case member 15.

本実施形態の燃焼装置1の外観形状は、図10の通りであり、缶体2の下部に燃焼バーナ5があり、缶体2の上部に一次熱交換器3(顕熱回収型熱交換器)がある。そして缶体2の上端部に接続部材14が設けられ、接続部材14に二次熱交換器7が載置されている。
本実施形態では、二次熱交換器7のケース部材15及びヘッダ16,17が燃焼装置1の外壁の一部を構成する。そのため本実施形態の燃焼装置1は部品点数が少なく、組み立てが容易である。なお本実施形態では、二次熱交換器7のヘッダ16,17のカップ部材30,31,32,33,35(端室部材)が燃焼ガス流路8の外部側面に設けられた形状となっている。
燃焼装置1の内部においては、燃焼バーナ5から排気部材19に至る一連の燃焼ガス流路8が形成されている。
The external shape of the combustion apparatus 1 of the present embodiment is as shown in FIG. 10, the combustion burner 5 is provided at the lower part of the can body 2, and the primary heat exchanger 3 (sensible heat recovery type heat exchanger) is provided at the upper part of the can body 2. ) And the connection member 14 is provided in the upper end part of the can body 2, and the secondary heat exchanger 7 is mounted in the connection member 14. FIG.
In the present embodiment, the case member 15 and the headers 16 and 17 of the secondary heat exchanger 7 constitute a part of the outer wall of the combustion device 1. Therefore, the combustion apparatus 1 of this embodiment has few parts and is easy to assemble. In the present embodiment, the cup members 30, 31, 32, 33, and 35 (end chamber members) of the headers 16 and 17 of the secondary heat exchanger 7 are provided on the outer side surface of the combustion gas flow path 8. ing.
Inside the combustion apparatus 1, a series of combustion gas flow paths 8 extending from the combustion burner 5 to the exhaust member 19 are formed.

具体的に説明すると、燃焼バーナ5から接続部材14に至る間は、缶体2の内部によって燃焼ガス流路8が形成されている。接続部材14の内部では接続部材14自身によって燃焼ガス流路8が形成されている。また接続部材14から排気部材19に至る間は、二次熱交換器7自身が燃焼ガス流路8となっている。
即ち二次熱交換器7は、ケース部材15を有し、当該ケース部材15によって天面、正面、背面及び底面が囲まれている。またケース部材15の側面部分74,75は、ヘッダ16,17の管板20によって閉塞されている。そのため二次熱交換器7は、導入口15bと排出口15aを除く6面が囲まれ、内部が燃焼ガス流路8として機能する。
この様に本実施形態の燃焼装置1では、ヘッダ16,17の管板20が燃焼ガス流路8の壁面の一部を構成している。
More specifically, the combustion gas flow path 8 is formed by the inside of the can body 2 from the combustion burner 5 to the connecting member 14. Inside the connecting member 14, the combustion gas flow path 8 is formed by the connecting member 14 itself. Further, the secondary heat exchanger 7 itself serves as the combustion gas flow path 8 from the connection member 14 to the exhaust member 19.
That is, the secondary heat exchanger 7 includes a case member 15, and the top surface, the front surface, the back surface, and the bottom surface are surrounded by the case member 15. Further, the side surface portions 74 and 75 of the case member 15 are closed by the tube plates 20 of the headers 16 and 17. Therefore, the secondary heat exchanger 7 is surrounded by six surfaces except the inlet 15 b and the outlet 15 a, and the inside functions as the combustion gas flow path 8.
Thus, in the combustion apparatus 1 of the present embodiment, the tube plates 20 of the headers 16 and 17 constitute a part of the wall surface of the combustion gas flow path 8.

本実施形態では、ヘッダ16,17の管板20が燃焼ガス流路8の壁面の一部を構成しているので、燃焼ガス流路8内に受熱管18が密に配される。即ち二次熱交換器7は、一対のヘッダ16,17間に複数の受熱管18が並列的に並べられたものであり、本実施形態では、受熱管18が取り付けられた管板20に受熱管18が取り付けられている。そして本実施形態では、受熱管18が取り付けられた管板20が燃焼ガス流路8の側面側壁面を構成しているから、受熱管18は燃焼ガス流路8の両側壁を貫通している。そのため受熱管18は燃焼ガス流路8を横切り、流路内における表面積が大きい。   In this embodiment, since the tube plates 20 of the headers 16 and 17 constitute a part of the wall surface of the combustion gas flow path 8, the heat receiving pipes 18 are densely arranged in the combustion gas flow path 8. That is, the secondary heat exchanger 7 includes a plurality of heat receiving tubes 18 arranged in parallel between a pair of headers 16 and 17. In the present embodiment, the secondary heat exchanger 7 receives the heat receiving tubes 18 on the tube plate 20 to which the heat receiving tubes 18 are attached. A heat pipe 18 is attached. In this embodiment, since the tube plate 20 to which the heat receiving pipe 18 is attached constitutes the side wall surface of the combustion gas flow path 8, the heat receiving pipe 18 penetrates both side walls of the combustion gas flow path 8. . Therefore, the heat receiving pipe 18 crosses the combustion gas flow path 8 and has a large surface area in the flow path.

続いて、本実施形態の燃焼装置1における湯水の流れについて説明する。
外部から給水配管60を介して供給された湯水は、図5に矢印で示すように二次熱交換器7の流入口47aからヘッダ16の流入室36内に流れ込む。この湯水は、流入室36に連通し、上流受熱管群23を構成する各受熱管18に流入し、ヘッダ17側に向けて流れる。上流受熱管群23を流れる湯水は、上流迂回室56に流入して流れ方向を逆転し、上流迂回室56に開口した中流受熱管群24の受熱管18に流れ込む。その後、湯水は、同様にして中流迂回室55および下流迂回室57において迂回しながら中流受熱管群25および下流受熱管群26を構成する各受熱管18内を流れ、流出室39に流れ込む。各受熱管18内を流れる湯水は、ケース部材15内に導入された燃焼ガスとの熱交換加熱される。流出室39に至った湯水は、流出口47bから二次熱交換器7の外部に排出され、接続配管61を介して一次熱交換器3に供給される。一次熱交換器3に導入された湯水は、燃焼ガス流路8内を流れる高温の燃焼ガスとの熱交換により加熱され、出水口11から図示しない給湯栓や負荷端末に供給される。
Then, the flow of the hot water in the combustion apparatus 1 of this embodiment is demonstrated.
Hot water supplied from outside through the water supply pipe 60 flows into the inflow chamber 36 of the header 16 from the inlet 47a of the secondary heat exchanger 7 as indicated by an arrow in FIG. This hot water communicates with the inflow chamber 36, flows into each heat receiving pipe 18 constituting the upstream heat receiving pipe group 23, and flows toward the header 17. Hot water flowing through the upstream heat receiving pipe group 23 flows into the upstream detour chamber 56, reverses the flow direction, and flows into the heat receiving pipe 18 of the middle flow heat receiving pipe group 24 opened in the upstream detour chamber 56. Thereafter, the hot water flows in the heat receiving pipes 18 constituting the midstream heat receiving pipe group 25 and the downstream heat receiving pipe group 26 while being diverted in the middle flow bypass chamber 55 and the downstream bypass chamber 57 in the same manner, and flows into the outflow chamber 39. The hot and cold water flowing in each heat receiving pipe 18 is heat exchange heated with the combustion gas introduced into the case member 15. Hot water reaching the outflow chamber 39 is discharged from the outlet 47 b to the outside of the secondary heat exchanger 7 and supplied to the primary heat exchanger 3 through the connection pipe 61. The hot water introduced into the primary heat exchanger 3 is heated by heat exchange with the high-temperature combustion gas flowing in the combustion gas flow path 8 and supplied from a water outlet 11 to a hot water tap and a load terminal (not shown).

次に、本実施形態の燃焼装置1における燃焼ガスの流れについて説明する。
燃焼バーナ5の燃焼作動に伴って発生した燃焼ガスは、缶体2の燃焼ガス流路8内を下流側、即ち上方に向かって流れる。燃焼バーナ5において発生した高温の燃焼ガスは、燃焼ガス流路8の中途に設けられた一次熱交換器3を通過し、一次熱交換器3内を流れる湯水を加熱する。一次熱交換器3において主として顕熱が回収された燃焼ガスは、燃焼ガス流路8の最下流に配された接続部材14に至る。
Next, the flow of the combustion gas in the combustion apparatus 1 of the present embodiment will be described.
The combustion gas generated by the combustion operation of the combustion burner 5 flows in the combustion gas flow path 8 of the can 2 toward the downstream side, that is, upward. The high-temperature combustion gas generated in the combustion burner 5 passes through the primary heat exchanger 3 provided in the middle of the combustion gas flow path 8 and heats hot water flowing in the primary heat exchanger 3. The combustion gas from which sensible heat has been mainly recovered in the primary heat exchanger 3 reaches the connection member 14 disposed on the most downstream side of the combustion gas flow path 8.

一次熱交換器5を通過した燃焼ガスは、接続部材14の集合部14aに集まり、接続部14bの開口14cに気密状態に接続された導入口15bを通り、二次熱交換器7内に流入する。二次熱交換器7内では、燃焼ガスは、ケース部材15の背面に設けられた導入口15bからケース部材15の正面に設けられた排出口15a(排気部)に向かって水平方向(横方向)に流れる。これに対して二次熱交換器7は、ケース部材15の両側面に設けられたヘッダ16,17に多数の受熱管18が並列的に並べられたものであるから、燃焼ガスは受熱管18を横切る様に、平行に配された多数の受熱管18の間を流れる。これにより、二次熱交換器7において主として燃焼ガスの持つ潜熱が受熱管18内を流れる湯水に回収され、且つ受熱管18の表面に発生したドレンが燃焼ガスの送風によって受熱管18から離脱する。
その後、燃焼ガスは、二次熱交換器7の正面にある排出口15aに至り、ケース部材15の外部に排出される。
The combustion gas that has passed through the primary heat exchanger 5 gathers at the gathering portion 14a of the connecting member 14, and flows into the secondary heat exchanger 7 through the inlet 15b that is airtightly connected to the opening 14c of the connecting portion 14b. To do. In the secondary heat exchanger 7, the combustion gas flows in a horizontal direction (lateral direction) from an introduction port 15 b provided on the back surface of the case member 15 toward an exhaust port 15 a (exhaust part) provided on the front surface of the case member 15. ). On the other hand, since the secondary heat exchanger 7 has a large number of heat receiving pipes 18 arranged in parallel on headers 16 and 17 provided on both side surfaces of the case member 15, the combustion gas flows into the heat receiving pipe 18. Across the heat receiving pipes 18 arranged in parallel. Thereby, in the secondary heat exchanger 7, the latent heat of the combustion gas is mainly recovered in the hot water flowing in the heat receiving pipe 18, and the drain generated on the surface of the heat receiving pipe 18 is separated from the heat receiving pipe 18 by the blowing of the combustion gas. .
Thereafter, the combustion gas reaches the discharge port 15 a in front of the secondary heat exchanger 7 and is discharged to the outside of the case member 15.

本実施形態の燃焼装置1では、ヘッダ16,17の管板20が燃焼ガス流路8の側面側壁面を構成し、当該管板20に対して複数の受熱管18が並列的に並べられているから、燃焼ガス流路8内における受熱管18の収納が密である。そのため受熱管18の表面と燃焼ガスとの接触機会が多く、熱交換効率が高い。   In the combustion apparatus 1 of the present embodiment, the tube plates 20 of the headers 16 and 17 constitute the side wall surface of the combustion gas flow path 8, and a plurality of heat receiving tubes 18 are arranged in parallel with the tube plate 20. Therefore, the heat receiving pipe 18 is densely stored in the combustion gas flow path 8. Therefore, there are many contact opportunities between the surface of the heat receiving pipe 18 and the combustion gas, and the heat exchange efficiency is high.

また前記した様に、二次熱交換器7によって燃焼ガスの持つ潜熱が回収されるから、燃焼ガス中の水蒸気が凝縮し、ドレンが発生する。ドレンは、受熱管18の表面に発生することとなるが、本実施形態で採用する受熱管18は、裸管であってフィン等の突出物を持たない。またフィンが無いのでドレンが入り込む様な隙間もない。そのため本実施形態で採用する受熱管18は、ドレンが溜まりにくい。   Further, as described above, since the latent heat of the combustion gas is recovered by the secondary heat exchanger 7, water vapor in the combustion gas is condensed and drainage is generated. Drain is generated on the surface of the heat receiving tube 18, but the heat receiving tube 18 employed in the present embodiment is a bare tube and does not have protrusions such as fins. Also, since there are no fins, there is no gap for the drain to enter. Therefore, the heat receiving pipe 18 employed in the present embodiment is unlikely to accumulate drainage.

また本実施形態の燃焼装置1では、受熱管18は、燃焼ガスの流れを横切る方向に配列されている。そのため受熱管18に付着したドレンが燃焼ガスによって吹き飛ばされ、ドレンが溜まりにくい。   Moreover, in the combustion apparatus 1 of this embodiment, the heat receiving pipes 18 are arranged in a direction crossing the flow of the combustion gas. Therefore, the drain adhering to the heat receiving pipe 18 is blown off by the combustion gas, and the drain is not easily collected.

また上段側で発生したドレンが下段に位置する受熱管に落下するが、本実施形態の燃焼装置1では、天地方向の積層数が横方向の積層数に比べて少ないので、下段に位置する受熱管に落下するドレン量が少ない。   In addition, although the drain generated on the upper stage falls to the heat receiving pipe located on the lower stage, in the combustion apparatus 1 of the present embodiment, the number of stacks in the vertical direction is smaller than the number of stacks in the horizontal direction. The amount of drain falling on the heat pipe is small.

この様に本実施形態の燃焼装置1では、受熱管18に付着するドレン量が少ないので二次熱交換器7の熱交換効率が高い。本実施形態の燃焼装置1は、二次熱交換器7の熱交換効率が高いので、熱効率が高く、省エネルギーである。   Thus, in the combustion apparatus 1 of this embodiment, since the amount of drains adhering to the heat receiving pipe 18 is small, the heat exchange efficiency of the secondary heat exchanger 7 is high. Since the heat exchange efficiency of the secondary heat exchanger 7 is high, the combustion apparatus 1 of this embodiment has high heat efficiency and energy saving.

上記した実施形態は、燃焼バーナ5が下部にあり、その上部に熱交換器(一次熱交換器3、二次熱交換器7)が設けられた構造に本発明を活用したものであるが、当業者の間で「逆燃方式」と称される燃焼装置に本発明を適用することも可能である。ここで「逆燃方式」とは、燃焼バーナ5の下部に熱交換器が設けられた構成を言う。
しかしながら本発明の作用効果は、「逆燃方式」を採用する場合よりも実施形態に示した様な燃焼バーナ5の上部に熱交換器が設けられた構造を採用する場合の方が顕著である。即ち逆燃方式を採用すると、燃焼ガスは重力方向に流れることとなり、ドレンの落下方向に対して順方向に燃焼ガスが流れる。そのためドレンの剥離は比較的円滑であり、ドレンによる悪影響が少ない。これに対して燃焼バーナ5の上部に熱交換器が設けられた構造を採用する場合、従来技術の構造によればドレンの落下方向に対して逆方向に燃焼ガスが流れることとなり、ドレンが溜まりやすかったものが、本発明の採用によってドレンの排出が円滑に行われる様になった。
In the embodiment described above, the present invention is applied to a structure in which the combustion burner 5 is in the lower part and the heat exchanger (the primary heat exchanger 3 and the secondary heat exchanger 7) is provided in the upper part. It is also possible to apply the present invention to a combustion apparatus called “reverse combustion system” by those skilled in the art. Here, the “reverse combustion method” refers to a configuration in which a heat exchanger is provided in the lower part of the combustion burner 5.
However, the effect of the present invention is more conspicuous in the case of adopting the structure in which the heat exchanger is provided on the upper part of the combustion burner 5 as shown in the embodiment than in the case of employing the “reverse combustion method”. . That is, when the reverse combustion method is adopted, the combustion gas flows in the direction of gravity, and the combustion gas flows in the forward direction with respect to the drain falling direction. Therefore, the separation of the drain is relatively smooth and the adverse effect of the drain is small. On the other hand, when adopting a structure in which a heat exchanger is provided in the upper part of the combustion burner 5, according to the structure of the prior art, the combustion gas flows in the direction opposite to the direction in which the drain falls, and the drain accumulates. What was easy was that drainage was smoothly discharged by adopting the present invention.

上記した実施形態では、ヘッダ16,17部分の構造としてろう付け構造を例示したが、本発明はこの構造に限定されるものではなく、例えばネジ締め構造やリベット構造であってもよい。ネジ締め構造やリベット構造を採用する場合にはパッキンが併用される。   In the above-described embodiment, the brazing structure is exemplified as the structure of the headers 16 and 17, but the present invention is not limited to this structure, and may be, for example, a screw fastening structure or a rivet structure. When a screw tightening structure or a rivet structure is adopted, packing is used together.

本発明の一実施形態である燃焼装置の構成図である。It is a block diagram of the combustion apparatus which is one Embodiment of this invention. 図1に示す燃焼装置の二次熱交換器近傍を示す分解斜視図である。It is a disassembled perspective view which shows the secondary heat exchanger vicinity of the combustion apparatus shown in FIG. 二次熱交換器および排気部材を示す斜視図である。It is a perspective view which shows a secondary heat exchanger and an exhaust member. 図3に示す二次熱交換器の分解斜視図である。It is a disassembled perspective view of the secondary heat exchanger shown in FIG. 図3に示す二次熱交換器のA−A断面図である。It is AA sectional drawing of the secondary heat exchanger shown in FIG. (a)は、図3に示す二次熱交換器における受熱管の配置を示す模式図であり、同(b),(c)は同(a)に示す受熱管の配置の変形例を示す模式図である。(A) is a schematic diagram which shows arrangement | positioning of the heat receiving tube in the secondary heat exchanger shown in FIG. 3, (b), (c) shows the modification of arrangement | positioning of the heat receiving tube shown to (a). It is a schematic diagram. (a)は、図3に示す二次熱交換器のカップ部材を示す斜視図であり、(b)は、(a)のA−A断面図である。(A) is a perspective view which shows the cup member of the secondary heat exchanger shown in FIG. 3, (b) is AA sectional drawing of (a). (a)は、図3に示す二次熱交換器のカップ部材を示す斜視図であり、(b)は、(a)のA−A断面図である。(A) is a perspective view which shows the cup member of the secondary heat exchanger shown in FIG. 3, (b) is AA sectional drawing of (a). 図3に示す熱交換器におけるカップ部材と管板の関係を示す断面図である。It is sectional drawing which shows the relationship between the cup member and tube sheet in the heat exchanger shown in FIG. 本実施形態の燃焼装置の外観図である。It is an external view of the combustion apparatus of this embodiment. 特開平11−148642号公報に記載された燃焼装置のモデル図である。It is a model figure of the combustion apparatus described in Unexamined-Japanese-Patent No. 11-148642.

符号の説明Explanation of symbols

1 燃焼装置
2 缶体
3 一次熱交換器(顕熱回収型熱交換器)
5 燃焼バーナ(燃焼手段)
7 二次熱交換器(潜熱回収用熱交換器)
15 ケース部材
16,17 ヘッダ
18 受熱管
30,31,32,33,35 カップ部材(端室部材)
DESCRIPTION OF SYMBOLS 1 Combustion apparatus 2 Can body 3 Primary heat exchanger (sensible heat recovery type heat exchanger)
5 Combustion burner (combustion means)
7 Secondary heat exchanger (heat exchanger for latent heat recovery)
15 Case member 16, 17 Header 18 Heat receiving pipe 30, 31, 32, 33, 35 Cup member (end chamber member)

Claims (5)

燃焼手段と、主として燃焼手段において発生した燃焼ガスの顕熱を回収して湯水を加熱する顕熱回収用熱交換器と、当該顕熱回収用熱交換器に対して燃焼ガス流路の下流側に配置され、主として前記燃焼ガスの潜熱を回収して湯水を加熱する潜熱回収用熱交換器を備え、前記潜熱回収用熱交換器を通過した湯水が前記顕熱回収用熱交換器に流れる様に配管された燃焼装置において、前記潜熱回収用熱交換器は多数の受熱管が並列的に並べられたものであることを特徴とする燃焼装置。 Combustion means, a sensible heat recovery heat exchanger that recovers sensible heat of combustion gas generated mainly in the combustion means and heats hot water, and a downstream side of the combustion gas flow path with respect to the sensible heat recovery heat exchanger And a latent heat recovery heat exchanger that mainly recovers the latent heat of the combustion gas and heats the hot water, and the hot water that has passed through the latent heat recovery heat exchanger flows to the sensible heat recovery heat exchanger. In the combustion apparatus piped, the heat exchanger for latent heat recovery includes a large number of heat receiving tubes arranged in parallel. 潜熱回収用熱交換器の受熱管は、裸管であることを特徴とする請求項1に記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the heat receiving pipe of the heat exchanger for recovering latent heat is a bare pipe. 潜熱回収用熱交換器の受熱管は、天地方向と横方向に積層された立体構造を構成しており、天地方向の積層数が横方向の積層数に比べて少ないことを特徴とする請求項1又は2に記載の燃焼装置。 The heat receiving pipe of the heat exchanger for latent heat recovery has a three-dimensional structure laminated in a vertical direction and a horizontal direction, and the number of vertical layers is smaller than the number of horizontal layers. The combustion apparatus according to 1 or 2. 潜熱回収用熱交換器の受熱管は、燃焼ガスの流れを横切る方向に配列されていることを特徴とする請求項1乃至3のいずれかに記載の燃焼装置。 The combustion apparatus according to any one of claims 1 to 3, wherein the heat receiving pipes of the latent heat recovery heat exchanger are arranged in a direction crossing the flow of the combustion gas. 潜熱回収用熱交換器は、一対のヘッダ間に複数の受熱管が並列的に並べられたものであり、前記ヘッダは、受熱管が取り付けられる管板と当該管板の背面側に設けられた端室部材を備え、前記ヘッダが燃焼手段から排気部に至る一連の燃焼ガス流路の壁面の一部を構成していることを特徴とする請求項1乃至4のいずれかに記載の燃焼装置。 The heat exchanger for latent heat recovery has a plurality of heat receiving tubes arranged in parallel between a pair of headers, and the header is provided on a tube plate to which the heat receiving tubes are attached and on the back side of the tube plate. The combustion apparatus according to any one of claims 1 to 4, further comprising an end chamber member, wherein the header constitutes a part of a wall surface of a series of combustion gas passages extending from the combustion means to the exhaust portion. .
JP2004088402A 2004-03-25 2004-03-25 Combustion device Pending JP2005274028A (en)

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PCT/JP2005/005241 WO2005093335A1 (en) 2004-03-25 2005-03-23 Heating device
US10/593,350 US7647897B2 (en) 2004-03-25 2005-03-23 Heating apparatus
DE112005000642T DE112005000642T5 (en) 2004-03-25 2005-03-23 heater

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