JP2011242023A - Liquid fuel water heater - Google Patents

Liquid fuel water heater Download PDF

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JP2011242023A
JP2011242023A JP2010112969A JP2010112969A JP2011242023A JP 2011242023 A JP2011242023 A JP 2011242023A JP 2010112969 A JP2010112969 A JP 2010112969A JP 2010112969 A JP2010112969 A JP 2010112969A JP 2011242023 A JP2011242023 A JP 2011242023A
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heat exchanger
latent heat
bottom plate
combustion gas
liquid fuel
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JP5610841B2 (en
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Hiroyuki Takahama
浩之 高濱
Shunsuke Inoue
俊輔 井上
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Chofu Seisakusho Co Ltd
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Chofu Seisakusho Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To solve a problem that a conventional latent heat recovery heat exchanger in a tube and header method requires a combustion gas passage and a casing having airtightness for the latent heat recovery heat exchanger, and thus, has a complicated shape requiring a considerable skillful technique and accuracy during manufacturing.SOLUTION: A latent heat heat-exchanger 30 comprises: a top plate 41; a bottom plate 43; a side plate 42 covering peripheries of the top plate 41 and the bottom plate 43; and combustion gas passages 33 penetrating the top plate 41 and the bottom plate 43. Combustion gas is brought into contact with the top late 41, the bottom plate 43 and the combustion gas passages 33 penetrating the top plate 41 and the bottom plate 43.

Description

本発明は、液体燃料を燃焼させる給湯機で、顕熱を回収する熱交換器だけではなく、潜熱も回収する熱交換器を有する給湯機に関する。   The present invention relates to a hot water heater that burns liquid fuel, and relates to a hot water heater having not only a heat exchanger that recovers sensible heat but also a heat exchanger that recovers latent heat.

従来、液体燃料燃焼装置を備え、液体燃料燃焼装置の燃焼ガスを熱交換して温水に換える給湯機としては、熱交換率の向上を目的として潜熱の回収が可能な液体燃料給湯機が知られていた。潜熱の回収が可能な液体燃料給湯機は、顕熱回収用熱交換器と潜熱回収用熱交換器の二つの熱交換器を備えており、液体燃料を燃焼させた燃焼ガスを前記顕熱回収用熱交換器に接触させて熱交換し、顕熱を奪った後の燃焼ガスを潜熱回収用熱交換器に接触させて潜熱も奪う方式となっていた。また、燃焼ガスが流れる順序としては、顕熱回収用熱交換器を通過させた後に、潜熱回収用熱交換器を通過させるようになっていた。   Conventionally, as a water heater provided with a liquid fuel combustion device and exchanging heat with the combustion gas of the liquid fuel combustion device for hot water, a liquid fuel water heater capable of recovering latent heat for the purpose of improving the heat exchange rate is known. It was. A liquid fuel water heater capable of recovering latent heat includes two heat exchangers, a sensible heat recovery heat exchanger and a latent heat recovery heat exchanger, and recovers the combustion gas obtained by burning liquid fuel into the sensible heat recovery system. The heat exchange was performed by contacting the heat exchanger and the combustion gas after depriving sensible heat was brought into contact with the latent heat recovery heat exchanger to deprive the latent heat. Further, the combustion gas flows through the sensible heat recovery heat exchanger and then the latent heat recovery heat exchanger.

潜熱回収用熱交換器は、潜熱を回収するためできるだけ低い温度の水を給水する必要があり、給水される水道水は、潜熱回収用熱交換器を通過させた後に、顕熱回収用熱交換器を通過させる構成となっていた。この場合、潜熱回収用熱交換器は、燃焼ガスに含まれる水蒸気からも熱回収するため、潜熱回収用熱交換器の表面に強酸性の凝縮水が付着し、この凝縮水を給湯機の外部に排出する必要があり、潜熱回収用熱交換器の下部に凝縮水を受ける凝縮水受け皿を設けて、凝縮水受け皿に受けた凝縮水を凝縮水排出管により潜熱回収用熱交換器の外部に排出するようにしていた。(特許文献1参照)   The latent heat recovery heat exchanger needs to supply water at the lowest possible temperature to recover the latent heat, and the supplied tap water passes through the latent heat recovery heat exchanger, and then the sensible heat recovery heat exchange. It was configured to pass the vessel. In this case, since the latent heat recovery heat exchanger also recovers heat from the water vapor contained in the combustion gas, strongly acidic condensate adheres to the surface of the latent heat recovery heat exchanger, and this condensate is A condensate tray that receives condensed water is installed at the bottom of the latent heat recovery heat exchanger, and the condensed water received in the condensate tray is placed outside the latent heat recovery heat exchanger through the condensate discharge pipe. I was trying to discharge. (See Patent Document 1)

液体燃料給湯機の液体燃料燃焼装置で発生する燃焼ガスは、排気口で液体燃料給湯機の外部に排出される。この燃焼ガスの発生源から排気口までの液体燃料給湯機内部における燃焼ガスの通路において、燃焼ガスが途中で漏れることは、液体燃料燃焼装置に二酸化炭素濃度の高い空気が供給されて前記液体燃料燃焼装置の燃焼状態が悪くなり、時間が経過すると煤の発生や熱交換器の詰まりを生じる原因の一つ、所謂ショートサイクルとなる。よって、液体燃料燃焼装置の燃焼ガスの発生源(液体燃料燃焼装置)から排気口までの燃焼ガスの通路は、気密性を有する必要があった。そして燃焼ガスの通路には、顕熱回収用熱交換器、潜熱回収用熱交換器、凝縮水受け皿、および顕熱回収用熱交換器と潜熱回収用熱交換器を繋ぐ通路等もこれに該当していた。   Combustion gas generated in the liquid fuel combustion apparatus of the liquid fuel water heater is discharged to the outside of the liquid fuel water heater at the exhaust port. In the combustion gas passage inside the liquid fuel water heater from the combustion gas generation source to the exhaust port, the leakage of the combustion gas in the middle means that the liquid fuel combustion apparatus is supplied with air having a high carbon dioxide concentration and supplies the liquid fuel. When the combustion state of the combustion device becomes worse and time elapses, it becomes a so-called short cycle, which is one of the causes of generation of soot and clogging of the heat exchanger. Therefore, the passage of the combustion gas from the combustion gas generation source (liquid fuel combustion device) of the liquid fuel combustion device to the exhaust port needs to be airtight. The combustion gas passages also include sensible heat recovery heat exchangers, latent heat recovery heat exchangers, condensate trays, and passages connecting the sensible heat recovery heat exchanger and latent heat recovery heat exchangers. Was.

液体燃料給湯機には、給湯機能だけではなく、追焚き機能を有するものがある。一つの液体燃料燃焼装置を利用して給湯機能と追焚き機能を行う液体燃料給湯機には、給湯用の顕熱熱交換器の内部に追焚き用のチューブ式熱交換器が設けられることにより、給湯用の顕熱熱交換器が二重構造になっているものがあった。(特許文献2の図1参照)   Some liquid fuel water heaters have not only a hot water supply function but also a reheating function. In a liquid fuel water heater that uses a single liquid fuel combustion device to perform hot water supply and reheating functions, a reheating tube heat exchanger is provided inside the sensible heat exchanger for hot water supply. Some sensible heat exchangers for hot water supply have a double structure. (See FIG. 1 of Patent Document 2)

特開2008−170088号公報JP 2008-170088 A 特開2009−210203号公報JP 2009-210203 A

しかしながら、特許文献1に記載された潜熱回収用熱交換器は、チューブとヘッダーで構成されており、チューブとヘッダーの全表面に燃焼ガスが接触して熱交換が行われて、チューブとヘッダー全体を覆うケーシングが必要であった。そしてケーシングは燃焼ガスが通過する燃焼ガス通路に該当し、ケーシングに気密性を必要としていた。特許文献1に記載された熱交換器が設けられる給湯装置等の場合においては、潜熱回収用熱交換器と顕熱回収用熱交換器とは、略J形の長い燃焼ガス通路で結ばれる構造となっていた。そして、顕熱回収用熱交換器と潜熱回収用熱交換器を結ぶ燃焼ガス通路が長いということは、燃焼ガス通路で放熱が発生し、燃焼ガスの潜熱回収を妨げる原因となり好ましくないという問題があった。また、略J形の燃焼ガス通路や潜熱回収用熱交換器のために気密性を持たせたケーシングが必要になるということは、製造に多大に熟練や精度が要求される複雑な形状となるという問題があった。   However, the heat exchanger for latent heat recovery described in Patent Document 1 is composed of a tube and a header, and the entire surface of the tube and the header is in contact with the combustion gas to perform heat exchange. A casing was needed. The casing corresponds to a combustion gas passage through which combustion gas passes, and the casing needs to be airtight. In the case of a hot water supply apparatus or the like provided with a heat exchanger described in Patent Document 1, the latent heat recovery heat exchanger and the sensible heat recovery heat exchanger are connected by a substantially J-shaped long combustion gas passage. It was. And, the long combustion gas passage connecting the sensible heat recovery heat exchanger and the latent heat recovery heat exchanger is not preferable because it generates heat radiation in the combustion gas passage and hinders the latent heat recovery of the combustion gas. there were. Moreover, the fact that a casing having airtightness is required for the substantially J-shaped combustion gas passage and the heat exchanger for recovering latent heat requires a complicated shape that requires a great deal of skill and accuracy in manufacturing. There was a problem.

潜熱回収用熱交換器がチューブとヘッダー方式の場合、チューブおよびヘッダーで発生する凝縮水を受ける凝縮水受け皿は、チューブおよびヘッダーの全表面で発生する凝縮水を確実に受けるために、チューブおよびヘッダーの鉛直方向の投影面だけではなく、前記投影面の範囲から所定の幅で広げた範囲で凝縮水を受けなければならないという問題があった。なお、特許文献1の熱交換器の場合は、ケーシングの底部(カップ部)が凝縮水受け皿を兼ねて、チューブおよびヘッダーの鉛直方向の投影面から広い範囲を覆うようにして、この問題を解決している。また、この場合には、ケーシングの気密性と同時に、強酸性の凝縮水に耐え得るようにする必要があることになる。   When the latent heat recovery heat exchanger is of the tube and header type, the condensate tray that receives the condensate generated in the tube and header receives the condensate generated on the entire surface of the tube and header in order to reliably receive the condensate generated on the tube and header. There is a problem that the condensed water must be received not only in the vertical projection plane but also in a range widened by a predetermined width from the projection plane. In addition, in the case of the heat exchanger of patent document 1, this bottom is solved so that the bottom part (cup part) of the casing also serves as a condensate tray and covers a wide range from the vertical projection surface of the tube and the header. is doing. Further, in this case, it is necessary to be able to withstand strongly acidic condensed water as well as the airtightness of the casing.

特許文献2に記載されている、給湯用の顕熱熱交換器の内部に追焚き用のチューブ式熱交換器が設けられる給湯機に、チューブとヘッダー方式の潜熱回収用熱交換器を設けようとすると、給湯用潜熱回収用熱交換器と追焚き用潜熱回収用熱交換器を分けて設ける必要がある。給湯用と追焚き用に分けて潜熱回収用熱交換器を設ける場合には、ケーシングの構造が複雑になるという問題があった。また、チューブを2重構造にして、内側の管を追焚き用、外側の管を給湯用の潜熱回収用熱交換器にする場合には、潜熱回収用熱交換器の作成が困難となり、いずれの場合でも給湯機自体の構造が複雑になるという問題があった。そして、給湯に比較して追焚きは頻繁に行われないことから、追焚き用潜熱回収用熱交換器は設けず、追焚き時の潜熱回収は断念する場合もあった。   Let's provide a tube and header type heat exchanger for latent heat recovery in a hot water heater described in Patent Document 2 in which a tube heat exchanger for reheating is provided inside a sensible heat exchanger for hot water supply. Then, it is necessary to separately provide a heat exchanger for recovering latent heat for hot water supply and a heat exchanger for recovering latent heat for tracking. When the heat exchanger for recovering latent heat is provided separately for hot water supply and reheating, there is a problem that the structure of the casing becomes complicated. In addition, when the tube is made into a double structure and the inner tube is used for chasing and the outer tube is used as a latent heat recovery heat exchanger for hot water supply, it becomes difficult to create a latent heat recovery heat exchanger. Even in this case, there is a problem that the structure of the water heater itself is complicated. In addition, since reheating is not frequently performed as compared with hot water supply, there is a case in which a latent heat recovery heat exchanger for reheating is not provided and latent heat recovery during reheating is abandoned.

上記の課題を解決するため、本発明では、次の技術的手段が講じられている。   In order to solve the above problems, the following technical means are taken in the present invention.

第1発明の液体燃料給湯機は、潜熱熱交換器と前記潜熱熱交換器の下部に顕熱熱交換器を備え、給水が前記潜熱熱交換器、前記顕熱熱交換器の順に供給される液体燃料給湯機で、前記潜熱熱交換器は、天板と、底板と、前記天板および前記底板の周囲を覆う側板と、前記天板および前記底板を貫通する燃焼ガス通路とより成り、前記天板、前記底板並びに前記天板および前記底板を貫通する燃焼ガス通路に、燃焼ガスが接触する様に構成されている。
第2発明の液体燃料給湯機は、請求項1記載の発明において、前記潜熱熱交換器の前記底板の下部には、前記底板の全面に対応させた凝縮水回収装置が備えられている。
第3発明の液体燃料給湯機は、請求項1記載の発明において、前記潜熱熱交換器の下面と、前記顕熱熱交換器の上面の外周形状が同一にされている。
第4発明の液体燃料給湯機は、請求項2または請求項3記載の発明において、前記潜熱熱交換器の内部には追い焚き用熱交換器が備えられている。
The liquid fuel water heater of the first invention includes a latent heat exchanger and a sensible heat exchanger at a lower portion of the latent heat exchanger, and water is supplied in the order of the latent heat exchanger and the sensible heat exchanger. In the liquid fuel water heater, the latent heat exchanger comprises a top plate, a bottom plate, a side plate covering the top plate and the periphery of the bottom plate, and a combustion gas passage penetrating the top plate and the bottom plate, Combustion gas is configured to contact the top plate, the bottom plate, and the combustion gas passage that penetrates the top plate and the bottom plate.
The liquid fuel water heater according to a second aspect of the present invention is the invention according to the first aspect, wherein a condensate recovery device corresponding to the entire surface of the bottom plate is provided below the bottom plate of the latent heat exchanger.
The liquid fuel water heater according to a third aspect of the present invention is the invention according to claim 1, wherein the outer peripheral shape of the lower surface of the latent heat exchanger and the upper surface of the sensible heat exchanger are the same.
According to a fourth aspect of the present invention, there is provided the liquid fuel water heater according to the second or third aspect, wherein a reheating heat exchanger is provided inside the latent heat exchanger.

以上のような、技術的手段が講じられていることにより、以下の効果を有する。
第1発明によれば、天板、底板並びに前記天板および前記底板を貫通する燃焼ガス通路に、排気が接触することにより、側板に燃焼ガスが通過しないので側板では結露し難いものとなる。これにより、潜熱熱交換器の外周での凝縮水回収装置が不要となり、凝縮水を集め易いという効果を有する。
第2発明によれば、第1発明を利用し、凝縮水回収装置を底板の全面に対応させていることで、凝縮水を簡単な構造でかつ確実に回収することができ、下部の顕熱熱交換器に結露水が落ちることがないという効果を有する。
第3発明によれば、第1発明を利用し、潜熱熱交換器と顕熱熱交換器の接続が容易となり、燃焼ガスに対する気密性を持たせる構成も容易となる。また、潜熱熱交換器と顕熱熱交換器が、連続した一体的な形状となるので、液体燃料給湯機として保温性や美観の向上に必要となる保温材や外装板で潜熱熱交換器と顕熱熱交換器の周囲を覆うことが容易にできる効果を有する。
第4発明によれば、第2発明または第3発明を利用し、製造時潜熱熱交換器の天板や底板を外した状態で潜熱回収時の追焚き用熱交換器を納めることが出来るので、組み立てが容易となる効果を有する。
By taking the technical means as described above, the following effects are obtained.
According to the first invention, the exhaust gas contacts the top plate, the bottom plate, and the combustion gas passage penetrating the top plate and the bottom plate, so that the combustion gas does not pass through the side plate, so that it is difficult for the side plate to condense. Thereby, the condensed water collection | recovery apparatus in the outer periphery of a latent-heat heat exchanger becomes unnecessary, and it has the effect that it is easy to collect condensed water.
According to the second invention, by utilizing the first invention, the condensed water recovery device is made to correspond to the entire surface of the bottom plate, so that the condensed water can be reliably recovered with a simple structure, and the sensible heat in the lower part There is an effect that the condensed water does not fall on the heat exchanger.
According to the third invention, the first invention is used, the connection between the latent heat exchanger and the sensible heat exchanger is facilitated, and the configuration for providing airtightness against the combustion gas is also facilitated. In addition, since the latent heat exchanger and sensible heat exchanger have a continuous and integrated shape, the latent heat heat exchanger and exterior plate are necessary for improving the heat retention and aesthetics as a liquid fuel water heater. This has the effect of easily covering the periphery of the sensible heat exchanger.
According to the fourth invention, since the second or third invention can be used and the heat exchanger for reheating at the time of latent heat recovery can be accommodated with the top plate and the bottom plate of the latent heat heat exchanger removed at the time of manufacture. This has the effect of facilitating assembly.

本発明に係る一実施形態を説明するための液体燃料給湯機の概略構成図である。It is a schematic block diagram of the liquid fuel water heater for demonstrating one Embodiment which concerns on this invention. 顕熱回収用熱交換器と潜熱回収用熱交換器の関係を説明する斜視図である。It is a perspective view explaining the relationship between the heat exchanger for sensible heat recovery, and the heat exchanger for latent heat recovery. 潜熱回収用熱交換器の分解図である。It is an exploded view of the heat exchanger for latent heat recovery. 凝縮水回収装置の分解図である。It is an exploded view of a condensed water collection | recovery apparatus. 本発明に係る他の実施形態を説明するための液体燃料給湯機の概略構成図である。It is a schematic block diagram of the liquid fuel water heater for demonstrating other embodiment which concerns on this invention. 他の実施形態の潜熱回収用熱交換器の分解図である。It is an exploded view of the heat exchanger for latent heat recovery of other embodiments.

発明を実施する形態について、図面に基づいて具体的に説明する。   Embodiments for carrying out the invention will be specifically described with reference to the drawings.

本発明の液体燃料給湯機の概略について図1を用いて説明する。液体燃料給湯機1は灯油や重油等の液体燃料を燃焼装置11で燃焼させ、この燃焼熱で熱交換器に通水された水を加熱するものであり。熱効率を向上させるため顕熱熱交換器20だけではなく、顕熱熱交換器20の上部、つまり排気側に給水温度を上昇させて熱効率の向上を可能とする潜熱熱交換器30を有している。   An outline of the liquid fuel water heater of the present invention will be described with reference to FIG. The liquid fuel water heater 1 burns liquid fuel such as kerosene or heavy oil in a combustion device 11 and heats water passed through the heat exchanger with this combustion heat. In order to improve thermal efficiency, not only the sensible heat exchanger 20, but also a latent heat heat exchanger 30 that can improve the thermal efficiency by raising the feed water temperature to the upper part of the sensible heat exchanger 20, that is, the exhaust side. Yes.

液体燃料給湯機1は、水道より給水配管12で結ばれ、減圧弁13を介して給水されている。減圧された水道水は、潜熱熱交換器30の下部の潜熱熱交入接続口31から入り、潜熱熱交換器30の内部を通過して潜熱熱交換器30の上部の潜熱熱交出接続口32に至る。これにより、水道水は顕熱熱交換器20で一部熱を奪われた燃焼ガスより更に熱を奪い、昇温する。潜熱熱交出接続口32は内部配管14で、顕熱熱交換器20の高さ方向中間部の顕熱熱交入接続口21に接続されている。潜熱熱交換30でやや昇温された水道水は、顕熱熱交入接続口21から入り、顕熱熱交換器20の内部を通過して顕熱熱交換器20の上部の顕熱熱交出接続口22に至り、給湯配管15により風呂場等の給湯栓(図示せず)に接続されている。これにより、潜熱熱交換器30でやや昇温された水道水は、顕熱熱交換器20で燃焼ガスにより、設定されている所望の温度まで昇温されて給湯栓で利用される。なお、給水配管12や給湯配管15には、顕熱熱交換器20と潜熱熱交換器30を保護する目的で、逃がし弁(図示せず)が設けられている。   The liquid fuel water heater 1 is connected from a water supply by a water supply pipe 12 and is supplied with water through a pressure reducing valve 13. The depressurized tap water enters from the latent heat exchange inlet 31 at the bottom of the latent heat exchanger 30, passes through the inside of the latent heat exchanger 30, and the latent heat exchange outlet at the top of the latent heat exchanger 30. 32. As a result, the tap water is deprived of heat from the combustion gas partially deprived of heat by the sensible heat exchanger 20 and is heated up. The latent heat exchange port 32 is an internal pipe 14 and is connected to the sensible heat exchange connection port 21 at the intermediate portion in the height direction of the sensible heat exchanger 20. The tap water slightly heated in the latent heat exchange 30 enters from the sensible heat exchange connection port 21, passes through the inside of the sensible heat exchanger 20, and sensible heat exchange in the upper part of the sensible heat exchanger 20. The outlet connection port 22 is reached and connected to a hot water tap (not shown) such as a bathroom by a hot water supply pipe 15. Thereby, the tap water slightly heated in the latent heat exchanger 30 is heated to the set desired temperature by the combustion gas in the sensible heat exchanger 20 and used in the hot water tap. The water supply pipe 12 and the hot water supply pipe 15 are provided with a relief valve (not shown) for the purpose of protecting the sensible heat exchanger 20 and the latent heat exchanger 30.

燃焼ガスの流れで説明すると、燃焼装置11が燃焼することで発生する燃焼ガスは、顕熱熱交換器20の内部に有る複数の煙管23を上方に向かって移動する。複数の煙管23には、顕熱熱交換器20の熱効率を上昇させるため燃焼ガスの流れを屈曲させる整流板24が、それぞれ設けられている。これにより、顕熱熱交換器20では潜熱熱交換器30でやや昇温された水道水が所望の温度に熱交換される。   If it demonstrates with the flow of combustion gas, the combustion gas which generate | occur | produces when the combustion apparatus 11 will burn will move upwards the some smoke pipe 23 which exists in the inside of the sensible heat exchanger 20. FIG. Each of the plurality of smoke pipes 23 is provided with a rectifying plate 24 that bends the flow of the combustion gas in order to increase the thermal efficiency of the sensible heat exchanger 20. Thereby, in the sensible heat exchanger 20, the tap water slightly heated in the latent heat exchanger 30 is heat-exchanged to a desired temperature.

顕熱熱交換器20で熱交換された燃焼ガスは、凝縮水受け皿50の下面から、凝縮水受け皿50中央部の孔52を通過し、孔52の上側に一定間隔の隙間を設けた傘板53の周囲より、上部の潜熱熱交換器30に入る。燃焼ガスは、潜熱熱交換器30の内部に有る複数の煙管33を上方に向かって移動する。複数の煙管33には、潜熱熱交換器30の熱効率を上昇させるため燃焼ガスの流れを屈曲させる整流板34が、それぞれ設けられている。燃焼ガスは潜熱熱交換器30を通過した後、排気部60の排気口61より、液体燃料給湯機1の外部に排出される。   The combustion gas heat-exchanged in the sensible heat exchanger 20 passes through the hole 52 in the center of the condensate tray 50 from the lower surface of the condensate tray 50, and the umbrella plate is provided with gaps at regular intervals above the holes 52. From the periphery of 53, it enters the upper latent heat exchanger 30. The combustion gas moves upward through a plurality of smoke pipes 33 in the latent heat exchanger 30. The plurality of smoke pipes 33 are each provided with a rectifying plate 34 for bending the flow of the combustion gas in order to increase the thermal efficiency of the latent heat exchanger 30. After passing through the latent heat exchanger 30, the combustion gas is discharged from the exhaust port 61 of the exhaust unit 60 to the outside of the liquid fuel water heater 1.

燃焼ガスは潜熱熱交換器30に接触することにより潜熱が奪われ、燃焼ガスの温度はさらに下がる。この場合、燃焼ガスには燃料に含まれる水素成分の燃焼により生じた水蒸気が含まれているので、潜熱熱交換器30の表面に凝縮水が発生する。凝縮水の発生する量は燃料の種類や燃焼量、給水温度、更には外気の湿度等により異なり一定ではないが、多かれ少なかれ凝縮水は発生し、凝縮水には燃焼によって生成された窒素酸化物や硫黄酸化物が溶解するため強酸性の液体となる。この強酸性の液体が発生するため、潜熱熱交換器30については、強酸性に耐え得る材料により構成されている。   When the combustion gas comes into contact with the latent heat exchanger 30, the latent heat is taken away, and the temperature of the combustion gas further decreases. In this case, since the combustion gas contains water vapor generated by the combustion of the hydrogen component contained in the fuel, condensed water is generated on the surface of the latent heat exchanger 30. The amount of condensed water generated varies depending on the type of fuel, the amount of combustion, the feed water temperature, the humidity of the outside air, etc. and is not constant, but more or less condensed water is generated, and the condensed water contains nitrogen oxides generated by combustion. It becomes a strongly acidic liquid because sulfur oxides dissolve. Since this strongly acidic liquid is generated, the latent heat exchanger 30 is made of a material that can withstand strong acidity.

そして、強酸性の凝縮水を液体燃料給湯機1の内部に留めておくことは、製品の劣化等の要因になるため、潜熱熱交換器30で発生した強酸性の凝縮水は、潜熱熱交換器30の下部に設けた凝縮水回収装置である凝縮水受け皿50により集められ、潜熱熱交換器30の外部に設けられた凝縮水管接続口54より排出される。強酸性の凝縮水を強酸性のまま排出させると環境に悪影響を及ぼすので、これを中和するための中和槽55が設けられている。凝縮水管接続口54には凝縮水管56が連通しており、凝縮水管56は中和槽55に接続されている。中和槽55内に流入した凝縮水は中和され、ほぼ中性になった凝縮水は凝縮水排出管57により外部の下水等に排出される。   Since keeping strong acid condensate in the liquid fuel water heater 1 causes deterioration of the product, the strong acid condensate generated in the latent heat exchanger 30 is latent heat exchange. It is collected by a condensate tray 50, which is a condensate recovery device provided at the lower part of the vessel 30, and discharged from a condensate pipe connection port 54 provided outside the latent heat exchanger 30. If strong acid condensate is discharged with strong acidity, it has an adverse effect on the environment, so a neutralization tank 55 is provided to neutralize this. A condensed water pipe 56 communicates with the condensed water pipe connection port 54, and the condensed water pipe 56 is connected to the neutralization tank 55. The condensed water that has flowed into the neutralization tank 55 is neutralized, and the condensed water that has become almost neutral is discharged to the external sewage or the like through the condensed water discharge pipe 57.

顕熱熱交換器20と潜熱熱交換器30は装置外面から放熱することを防ぐ目的で、保温材62が設けられている。図1では保温材62に、斜線を付している。なお、保温材61を付けた顕熱熱交換器20、潜熱熱交換器30、燃焼装置11、中和槽55等は、設置上や美観上の目的から外装板(図示せず)の中に納められている。   The sensible heat exchanger 20 and the latent heat exchanger 30 are provided with a heat insulating material 62 for the purpose of preventing heat radiation from the outer surface of the apparatus. In FIG. 1, the heat insulating material 62 is hatched. Note that the sensible heat exchanger 20, the latent heat exchanger 30, the combustion device 11, the neutralization tank 55, and the like, to which the heat insulating material 61 is attached, are placed in an exterior plate (not shown) for installation and aesthetic purposes. It is paid.

顕熱熱交換器20と潜熱熱交換器30との大きさや位置による取り付けの関係について、図2を用いて説明する。顕熱熱交換器20と、潜熱熱交換器30は、共に外観が円筒形である。顕熱熱交換器20の上面には天板25と一体に成形された顕熱熱交フランジ26が設けられている。天板25には複数の孔があり、複数の煙管23が溶接されている。顕熱熱交換器20の側面には顕熱熱交入接続口21、顕熱熱交出接続口22、燃焼装置11の取付け口27および排水口28が設けられている。なお、液体燃料給湯機1を設置する場合には排水口28には排水弁が設けられる。(図1参照)   The attachment relationship between the sensible heat exchanger 20 and the latent heat exchanger 30 depending on the size and position will be described with reference to FIG. Both the sensible heat exchanger 20 and the latent heat exchanger 30 are cylindrical in appearance. A sensible heat exchange flange 26 formed integrally with the top plate 25 is provided on the upper surface of the sensible heat exchanger 20. The top plate 25 has a plurality of holes, and a plurality of smoke pipes 23 are welded. On the side surface of the sensible heat exchanger 20, there are provided a sensible heat inlet / outlet port 21, a sensible heat outlet / outlet port 22, a mounting port 27 and a drain port 28 for the combustion device 11. In addition, when installing the liquid fuel water heater 1, the drain port 28 is provided with a drain valve. (See Figure 1)

潜熱熱交換器30の上面には天板41と一体に成形された潜熱熱交上部フランジ35が設けられている。天板41には複数の孔があり、複数の煙管33が溶接されている。潜熱熱交換器30の側面には、潜熱熱交入接続口31、潜熱熱交出接続口32および凝縮水管接続口54が設けられている。潜熱熱交換器30の下面には底板43(図1参照)があり、底板43の下部には凝縮水受け皿50(図1参照)が取付けられている。凝縮水受け皿50には、一体に成形された潜熱熱交下部フランジ36が設けられており、潜熱熱交換器30の下部の周囲に張り出している。   On the upper surface of the latent heat exchanger 30, a latent heat heat exchange upper flange 35 formed integrally with the top plate 41 is provided. The top plate 41 has a plurality of holes, and a plurality of smoke pipes 33 are welded. On the side surface of the latent heat exchanger 30, a latent heat input / output connection port 31, a latent heat exchange port 32, and a condensed water pipe connection port 54 are provided. A bottom plate 43 (see FIG. 1) is provided on the lower surface of the latent heat exchanger 30, and a condensate tray 50 (see FIG. 1) is attached to the lower portion of the bottom plate 43. The condensate tray 50 is provided with an integrally formed latent heat exchange lower flange 36 and extends around the lower portion of the latent heat exchanger 30.

顕熱熱交フランジ26と潜熱熱交下部フランジ36は、互いに対向する面が平面であり、該平面同士が所定幅のシール面となって、シール部材を用いることで容易に気密性を保てる構造となっている。なお、好ましくは、顕熱熱交換器20と潜熱熱交換器30の円筒形の直径は同一である方が、顕熱熱交フランジ26と潜熱熱交下部フランジ36の互いに対向する所定幅の接触面を形成する上では容易となる。なお、顕熱熱交換器20と潜熱熱交換器30の円筒形の直径が同一の方が好ましいが、円筒形の直径が同一でない場合であっても、顕熱熱交フランジ26と潜熱熱交下部フランジ36との間に有効なシール面が保たれるよう加工することも可能である。   The sensible heat heat exchange flange 26 and the latent heat heat exchange lower flange 36 have a structure in which surfaces facing each other are flat surfaces, and the flat surfaces become a seal surface having a predetermined width, so that airtightness can be easily maintained by using a seal member. It has become. Preferably, when the sensible heat exchanger 20 and the latent heat exchanger 30 have the same cylindrical diameter, the sensible heat exchange flange 26 and the latent heat exchange lower flange 36 contact each other with a predetermined width. It is easy to form the surface. The sensible heat exchanger 20 and the latent heat exchanger 30 preferably have the same cylindrical diameter, but even if the cylindrical diameters are not the same, the sensible heat exchange flange 26 and the latent heat exchange It is also possible to process such that an effective sealing surface is maintained between the lower flange 36 and the lower flange 36.

図3は潜熱熱交換器30の組み立てを示す図であり、潜熱熱交換器30の主要な構成部品は、天板41、側板42、底板43と複数の煙管33である。天板41は、潜熱熱交上部フランジ35を外周に有して皿状に一体に成形されており、中央の円板には、複数の煙管33を溶接するための孔41aが開けられている。孔41aは煙管33との溶接を容易にするため、上向きにバーリングするのが好ましい。天板41の下側向きの凹み41bが燃焼ガスの通路となる。底板43の上側向きの凹み43bは燃焼ガスの通路となる。複数の煙管33は同一の径および同一の長さの中空の円筒(管)であり、内部が燃焼ガスの通路となる。側板42は天板41および底板43の垂直の壁41c、43cの外径に等しい内径となる円筒であり、外部に潜熱熱交入接続口31、潜熱熱交出接続口32および凝縮水管接続口54が取り付けられている。   FIG. 3 is a view showing assembly of the latent heat exchanger 30, and main components of the latent heat exchanger 30 are a top plate 41, a side plate 42, a bottom plate 43, and a plurality of smoke pipes 33. The top plate 41 has a latent heat heat exchange upper flange 35 on the outer periphery and is integrally formed in a dish shape, and a hole 41a for welding a plurality of smoke tubes 33 is formed in the central disc. . The hole 41a is preferably burred upward in order to facilitate welding with the smoke pipe 33. A depression 41b facing the lower side of the top plate 41 serves as a combustion gas passage. A recess 43b facing the upper side of the bottom plate 43 serves as a passage for combustion gas. The plurality of smoke pipes 33 are hollow cylinders (tubes) having the same diameter and the same length, and the inside serves as a passage for combustion gas. The side plate 42 is a cylinder having an inner diameter equal to the outer diameter of the vertical walls 41c and 43c of the top plate 41 and the bottom plate 43, and the latent heat input / output connection port 31, the latent heat / heat output connection port 32 and the condensed water tube connection port are provided outside. 54 is attached.

複数の煙管33の一端に、天板41または底板43のどちらからでも良いがここでは、底板43が溶接され、その後、他方の天板41が煙管33の他端に溶接される。天板41、複数の煙管33および底板43が溶接されたものを、側板42の中に底板43側から差込み、天板41の垂直の壁41cと側板42が溶接され、次に、底板43の垂直の壁43cと側板42が溶接される。次いで底板43の下部に凝縮水受け皿50を差し込み、凝縮水受け皿50の垂直の壁51cと側板42が溶接される。なお、凝縮水受け皿50の垂直の壁51cの外径も側板42の内径と等しい。   Although the top plate 41 or the bottom plate 43 may be connected to one end of the plurality of smoke tubes 33, the bottom plate 43 is welded here, and then the other top plate 41 is welded to the other end of the smoke tube 33. The top plate 41, the plurality of smoke pipes 33 and the bottom plate 43 welded are inserted into the side plate 42 from the bottom plate 43 side, the vertical wall 41c of the top plate 41 and the side plate 42 are welded, and then the bottom plate 43 The vertical wall 43c and the side plate 42 are welded. Next, the condensed water tray 50 is inserted into the bottom of the bottom plate 43, and the vertical wall 51c of the condensed water tray 50 and the side plate 42 are welded. Note that the outer diameter of the vertical wall 51 c of the condensate tray 50 is also equal to the inner diameter of the side plate 42.

凝縮水受け皿50について図4を用いて説明する。凝縮水受け皿50は、中央に孔52を有する皿板51、傘板53および複数の支持具58よりなる。皿板51は、周囲に垂直の壁51cでつながる潜熱熱交下部フランジ36を有している。また、皿板51の中央の孔52の周囲には立ち上げ部59があり、孔52から、顕熱熱交換器20側に凝縮水が流れ込まないようになっている。複数の支持具58は皿板51と傘板53の間に燃焼ガスが通過できる間隔を有するために設けられており、支持具58の両端を皿板51と傘板53とに溶接することで凝縮水受け皿50は形成されている。また、底板43から滴下した凝縮水が孔52を通過して顕熱熱交換器20に至らないようにするため傘板53は孔52の径よりも大きくしてある。なお、本実施例においては、皿板51に孔が一つの例を説明しているが、複数の孔を設け、燃焼ガスを分散させて潜熱熱交換器30に導く方法であっても良い。   The condensed water receiving tray 50 will be described with reference to FIG. The condensed water receiving tray 50 includes a tray plate 51 having a hole 52 in the center, an umbrella plate 53 and a plurality of supports 58. The dish plate 51 has a latent heat exchange lower flange 36 connected to the periphery by a vertical wall 51c. Further, a rising portion 59 is provided around the central hole 52 of the plate 51 so that condensed water does not flow from the hole 52 to the sensible heat exchanger 20 side. The plurality of support tools 58 are provided so as to have a space through which the combustion gas can pass between the dish plate 51 and the umbrella plate 53, and both ends of the support tool 58 are welded to the dish plate 51 and the umbrella plate 53. The condensed water receiving tray 50 is formed. The umbrella plate 53 is made larger than the diameter of the hole 52 so that the condensed water dropped from the bottom plate 43 does not pass through the hole 52 and reach the sensible heat exchanger 20. In the present embodiment, an example in which the plate plate 51 has one hole has been described. However, a method in which a plurality of holes are provided and combustion gas is dispersed and guided to the latent heat exchanger 30 may be used.

以上、実施例1は、図1から図4で説明した様に構成されているので、図1の燃焼装置11で発生した燃焼ガスは、顕熱熱交換器20の複数の煙管23を通過し天板25の上部に集められる。図2の様に顕熱熱交換器20と潜熱熱交換器30は接続されているので、全部の燃焼ガスは凝縮水受け皿50を通過して、潜熱熱交換器30の底板43に入る。図3の様に潜熱熱交換器30は構成されているので、燃焼ガスが潜熱熱交換器30で接触する部分は底板43、複数の煙管33および天板41の表面となる。そして、燃焼ガスが接触して発生する凝縮水も、底板43、複数の煙管33および天板41の表面だけでしか発生しない。   Since the first embodiment is configured as described with reference to FIGS. 1 to 4, the combustion gas generated in the combustion device 11 of FIG. 1 passes through the plurality of smoke pipes 23 of the sensible heat exchanger 20. Collected on top of the top plate 25. Since the sensible heat exchanger 20 and the latent heat exchanger 30 are connected as shown in FIG. 2, all the combustion gas passes through the condensate tray 50 and enters the bottom plate 43 of the latent heat exchanger 30. Since the latent heat exchanger 30 is configured as shown in FIG. 3, the portion where the combustion gas comes into contact with the latent heat exchanger 30 is the surface of the bottom plate 43, the plurality of smoke pipes 33, and the top plate 41. And the condensed water which generate | occur | produces when a combustion gas contacts is generated only on the surface of the bottom plate 43, the several smoke pipe 33, and the top plate 41. FIG.

天板41で生じた凝縮水は複数の煙管33を伝わり底板43に、複数の煙管33で生じた凝縮水も底板43にと、全ての凝縮水は底板43に集まる。底板43の下部には凝縮水受け皿50が底板43の全面を受ける様に取り付けられており、潜熱熱交換器30で生じた全部の凝縮水は凝縮水受け皿50に集められる。この凝縮水を凝縮水管接続口54に導き、凝縮水管56、中和槽55、凝縮水配管57を通過して外部に排出される。   Condensed water generated in the top plate 41 travels through the plurality of smoke pipes 33 to the bottom plate 43, condensed water generated in the plurality of smoke pipes 33 also flows into the bottom plate 43, and all condensed water collects in the bottom plate 43. A condensate tray 50 is attached to the bottom of the bottom plate 43 so as to receive the entire surface of the bottom plate 43, and all the condensed water generated in the latent heat exchanger 30 is collected in the condensate tray 50. This condensed water is guided to the condensed water pipe connection port 54, passes through the condensed water pipe 56, the neutralization tank 55, and the condensed water pipe 57 and is discharged to the outside.

実施例2の液体燃料給湯機2は、実施例1の液体燃料給湯機1に追焚き機能が追加されたものであり、追加された機能以外の部分については実施例1と同一であるので、実施例1と同一の構成部品には同一の符号を付けて説明を省略する。   The liquid fuel hot water heater 2 of the second embodiment is obtained by adding a tracking function to the liquid fuel hot water heater 1 of the first embodiment, and is the same as the first embodiment except for the added function. The same components as those in the first embodiment are denoted by the same reference numerals and description thereof is omitted.

図5は液体燃料給湯機2の概略説明図である。液体燃料給湯機2の外部には循環口3が取り付けられた浴槽4が設けられている。液体燃料給湯機2には、内部に顕熱追焚き熱交換器70が設けられた顕熱熱交換器20aと、内部に潜熱追焚き熱交換器80が設けられた潜熱熱交換器30aと、循環ポンプ19を有している。   FIG. 5 is a schematic explanatory diagram of the liquid fuel water heater 2. A bathtub 4 to which a circulation port 3 is attached is provided outside the liquid fuel water heater 2. The liquid fuel water heater 2 includes a sensible heat exchanger 20a provided with a sensible heat tracking heat exchanger 70 therein, a latent heat heat exchanger 30a provided with a latent heat tracking heat exchanger 80 therein, A circulation pump 19 is provided.

液体燃料給湯機2と循環口3で構成される追焚き循環回路について説明する。循環ポンプ19が駆動することにより、浴槽4内の湯水は、循環口3の吸い込み口より循環戻り配管17に流れる。循環戻り配管17は潜熱追焚き熱交換器80の潜熱追焚き入接続口81につながっており、潜熱追焚き熱交換器80で間接的に加熱され、潜熱追焚き出接続口82に至る。潜熱追焚き出接続口82は追焚き内部配管16を介して顕熱追焚き熱交換器70の顕熱追焚き入接続口71につながっており、顕熱追焚き熱交換器70で間接的に加熱され、顕熱追焚き出接続口72に至る。顕熱追焚き出接続口72には循環往き配管18がつながっており循環口3の吐出側へと至る。なお、循環ポンプ19は循環往き配管18の途中に設けられている。   A recirculation circuit constituted by the liquid fuel water heater 2 and the circulation port 3 will be described. When the circulation pump 19 is driven, hot water in the bathtub 4 flows from the suction port of the circulation port 3 to the circulation return pipe 17. The circulation return pipe 17 is connected to the latent heat tracking heat connection port 81 of the latent heat tracking heat exchanger 80 and is indirectly heated by the latent heat tracking heat exchanger 80 to reach the latent heat tracking output connection port 82. The latent heat tracking connection port 82 is connected to the sensible heat tracking input port 71 of the sensible heat tracking heat exchanger 70 via the tracking internal pipe 16, and indirectly through the sensible heat tracking heat exchanger 70. The sensible heat tracking connection port 72 is heated. A circulation outgoing pipe 18 is connected to the sensible heat outlet connection port 72 and reaches the discharge side of the circulation port 3. The circulation pump 19 is provided in the middle of the circulation outgoing pipe 18.

潜熱熱交換器30aの内部に潜熱追焚き熱交換器80を設ける方法について、図6を用いて説明する。潜熱熱交換器30aは、底板43に複数の煙管33が取り付けられた状態となっている。なお、潜熱熱交入接続口31、潜熱熱交出接続口32および凝縮水管接続口54は側板42aに取り付けられており、側板42aには、潜熱追焚き入接続口81と潜熱追焚き出接続口82が取り付けられる孔81a、82aが開けられている。   A method of providing the latent heat tracking heat exchanger 80 inside the latent heat exchanger 30a will be described with reference to FIG. The latent heat exchanger 30 a is in a state where a plurality of smoke pipes 33 are attached to the bottom plate 43. The latent heat input / output connection port 31, the latent heat / heat output connection port 32, and the condensed water pipe connection port 54 are attached to the side plate 42a. The latent heat input connection port 81 and the latent heat extraction connection are connected to the side plate 42a. Holes 81a and 82a to which the mouth 82 is attached are opened.

前述の潜熱熱交換器30aは、底板43に複数の煙管33が取り付けられた状態となっているものに、コイル状の潜熱追焚き熱交換器80を複数の煙管33の周囲の所定の位置に納め、複数の煙管33と天板41を溶接する。その後、潜熱追焚き熱交換器80を備えた、天板41、複数の煙管33および底板43が溶接されたものを、側板42aの中に底板43側から差込み、天板41の垂直の壁41cと側板42aが溶接され、次に、底板43の垂直の壁43cと側板42aが溶接される。次いで底板43の下部に凝縮水受け皿50を差し込み、凝縮水受け皿50の垂直の壁51cと側板42aが溶接される。なお、凝縮水受け皿50の垂直の壁51cの外径も側板42aの内径と等しい。   The above-described latent heat exchanger 30a has a plurality of smoke pipes 33 attached to the bottom plate 43, and a coiled latent heat tracking heat exchanger 80 is placed at a predetermined position around the plurality of smoke pipes 33. The plurality of smoke pipes 33 and the top plate 41 are welded. Thereafter, the top plate 41, the plurality of smoke pipes 33, and the bottom plate 43, each having a latent heat tracking heat exchanger 80, are inserted into the side plate 42a from the bottom plate 43 side, and the vertical wall 41c of the top plate 41 is inserted. And the side plate 42a are welded, and then the vertical wall 43c of the bottom plate 43 and the side plate 42a are welded. Next, the condensed water tray 50 is inserted into the bottom of the bottom plate 43, and the vertical wall 51c of the condensed water tray 50 and the side plate 42a are welded. The outer diameter of the vertical wall 51c of the condensate tray 50 is also equal to the inner diameter of the side plate 42a.

1、2:液体燃料給湯機
3:循環口
4:浴槽
11:燃焼装置
12:給水配管
13:減圧弁
14:内部配管
15:給湯配管
16:追焚き内部配管
17:循環戻り配管
18:循環往き配管
19:循環ポンプ
20、20a:顕熱熱交換器
21:顕熱熱交入接続口
22:顕熱熱交出接続口
23、33:煙管
24、34:整流板
25、41:天板
26:顕熱熱交フランジ
27:取付け口
30、30a:潜熱熱交換器
31:潜熱熱交入接続口
32:潜熱熱交出接続口
35:潜熱熱交上部フランジ
36:潜熱熱交下部フランジ
42、42a:側板
43:底板
50:凝縮水受け皿
51:皿板
52:孔
53:傘板
54:凝縮水管接続口
55:中和槽
56:凝縮水管
57:凝縮水排出管
58:支持具
59:立ち上げ部
60:排気部
61:排気口
62:保温材
70:顕熱追焚き熱交換器
71:顕熱追焚き入接続口
72:顕熱追焚き出接続口
80:潜熱追焚き熱交換器
81:潜熱追焚き入接続口
82:潜熱追焚き出接続口
1, 2: Liquid fuel water heater 3: Circulation port 4: Bathtub
11: Combustion device 12: Water supply pipe 13: Pressure reducing valve 14: Internal pipe 15: Hot water supply pipe 16: Reheating internal pipe 17: Circulation return pipe 18: Circulation return pipe 19: Circulation pump 20, 20a: Sensible heat exchanger 21 : Sensible heat inlet / outlet 22: Sensible heat outlet / outlet 23, 33: Smoke tube 24, 34: Rectifier plate 25, 41: Top plate 26: Sensible heat exchanger flange 27: Mounting port 30, 30a: Latent heat Heat exchanger 31: Latent heat exchange connection port 32: Latent heat exchange port 35: Latent heat exchange upper flange 36: Latent heat exchange lower flange 42, 42a: Side plate 43: Bottom plate 50: Condensate tray 51: Dish plate 52: Hole 53: Umbrella plate 54: Condensate water pipe connection port 55: Neutralization tank 56: Condensate water pipe 57: Condensate water discharge pipe 58: Support tool 59: Start-up part 60: Exhaust part 61: Exhaust part 62: Heat insulation material 70 : Sensible heat tracking heat exchanger 71: Sensible heat tracking connection 72: sensible heat reheating outgoing port 80: latent reheating heat exchanger 81: latent reheating incoming port 82: latent heat reheating outgoing port

Claims (4)

潜熱熱交換器と前記潜熱熱交換器の下部に顕熱熱交換器を備え、給水が前記潜熱熱交換器、前記顕熱熱交換器の順に供給される液体燃料給湯機において、前記潜熱熱交換器は、天板と、底板と、前記天板および前記底板の周囲を覆う側板と、前記天板および前記底板を貫通する燃焼ガス通路とより成り、前記天板、前記底板並びに前記天板および前記底板を貫通する燃焼ガス通路に、燃焼ガスが接触する様に構成されていることを特徴とする液体燃料給湯機。   In the liquid fuel water heater provided with a latent heat exchanger and a sensible heat exchanger below the latent heat exchanger, and water is supplied in the order of the latent heat exchanger and the sensible heat exchanger, the latent heat exchange The vessel comprises a top plate, a bottom plate, a side plate covering the top plate and the periphery of the bottom plate, and the top plate and a combustion gas passage penetrating the bottom plate, and the top plate, the bottom plate, and the top plate and A liquid fuel water heater, wherein the combustion gas is in contact with a combustion gas passage penetrating the bottom plate. 前記潜熱熱交換器の前記底板の下部には、前記底板の全面に対応させた凝縮水回収装置が備えられていることを特徴とする、請求項1記載の液体燃料給湯機。   The liquid fuel water heater according to claim 1, wherein a condensate recovery device corresponding to the entire surface of the bottom plate is provided below the bottom plate of the latent heat exchanger. 前記潜熱熱交換器の下面と、前記顕熱熱交換器の上面の外周形状が同一にされていることを特徴とする、請求項1記載の液体燃料給湯機。   The liquid fuel water heater according to claim 1, wherein the outer peripheral shape of the lower surface of the latent heat exchanger and the upper surface of the sensible heat exchanger are the same. 前記潜熱熱交換器の内部には追焚き用熱交換器が備えられていることを特徴とする、請求項2または請求項3記載の液体燃料給湯機。

The liquid fuel water heater according to claim 2 or 3, wherein a reheating heat exchanger is provided inside the latent heat exchanger.

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017172902A (en) * 2016-03-24 2017-09-28 株式会社ユタカ技研 Gas water heater
JP2019196852A (en) * 2018-05-08 2019-11-14 株式会社長府製作所 Water heater
CN112629008A (en) * 2020-11-25 2021-04-09 晏翠波 Hanging stove with flue gas is handled

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JP2008272654A (en) * 2007-04-27 2008-11-13 Chofu Seisakusho Co Ltd Neutralization apparatus for drain and neutralization system for drain
JP2010007983A (en) * 2008-06-27 2010-01-14 Noritz Corp Hot water supply device

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Publication number Priority date Publication date Assignee Title
JPS6144248A (en) * 1984-08-08 1986-03-03 Matsushita Electric Ind Co Ltd Hot water space heater
JPH11248250A (en) * 1998-02-25 1999-09-14 Hitachi Air Conditioning & Refrig Co Ltd Warm-water boiler
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JP2010007983A (en) * 2008-06-27 2010-01-14 Noritz Corp Hot water supply device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017172902A (en) * 2016-03-24 2017-09-28 株式会社ユタカ技研 Gas water heater
JP2019196852A (en) * 2018-05-08 2019-11-14 株式会社長府製作所 Water heater
CN112629008A (en) * 2020-11-25 2021-04-09 晏翠波 Hanging stove with flue gas is handled

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