JP2007064551A - Combustion apparatus - Google Patents

Combustion apparatus Download PDF

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JP2007064551A
JP2007064551A JP2005251162A JP2005251162A JP2007064551A JP 2007064551 A JP2007064551 A JP 2007064551A JP 2005251162 A JP2005251162 A JP 2005251162A JP 2005251162 A JP2005251162 A JP 2005251162A JP 2007064551 A JP2007064551 A JP 2007064551A
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heat
heat exchanger
heat transfer
latent
combustion gas
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Masatomo Yoshimura
昌知 吉村
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements

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  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a compact arrangement that recovers latent heat to enhance heat efficiency and achieve energy savings. <P>SOLUTION: A latent heat exchanger of a water-heating heat exchanger heated by a burner to exchange heat with hot water comprises a plurality of bellows pipes 27 and heat-transfer fin parts 25 mounted on the outsides of the plurality of bellows pipes. The heat-transfer fins are folded back and semicircular protrusions and cylindrical burring or the like are provided, whereby a high-efficiency heat exchange apparatus larger than an arrangement composed only of the bellows pipes 27 and the heat-transfer fins can be provided. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、家庭用又は業務用の燃焼装置において、顕熱だけでなく、特に燃焼ガス中の水蒸気潜熱までを回収し、熱効率の向上を図った熱交換システムに関するものである。   The present invention relates to a heat exchange system that recovers not only sensible heat but also water vapor latent heat in combustion gas and improves thermal efficiency in a household or commercial combustion apparatus.

従来、この種の潜熱回収熱交換装置として、例えば,特許文献1に記載されているようなものがあった。図9は、前記公報に記載された従来の潜熱回収熱交換装置を示すものである。   Conventionally, as this type of latent heat recovery heat exchange device, for example, there has been one described in Patent Document 1. FIG. 9 shows a conventional latent heat recovery heat exchange device described in the publication.

図9において、1はバーナ、2はバーナ1に燃料ガスを供給するガス管、3はバーナ1に燃焼用空気供給するファン、4はバーナ1の燃焼によって発生する燃焼ガスの下流に位置する給湯熱交換器、5は給湯熱交換器4と上下に重ね合わせて配設される追い焚き熱交換器、6は給湯熱交換器4を形成する給湯伝熱管、7は追い焚き熱交換器を形成する追い焚き伝熱管である。8は給湯熱交換器4の燃焼ガス下流側に設置される給湯潜熱回収熱交換器、9は給湯潜熱回収熱交換器を形成する給湯潜熱伝熱管、10は給湯潜熱伝熱管9の出口9bと給湯伝熱管6の入口6aとを結ぶ温水管である。また、11は給湯潜熱伝熱管9の入口9aに接続する給水管、12は給湯伝熱管6の出口6bに接続する給湯管、13は追い炊き伝熱管7の入口に接続する風呂戻り管、14は追い焚き伝熱管7の出口に接続する風呂往き管である。   In FIG. 9, 1 is a burner, 2 is a gas pipe for supplying fuel gas to the burner 1, 3 is a fan for supplying combustion air to the burner 1, and 4 is hot water supply located downstream of the combustion gas generated by the combustion of the burner 1 The heat exchanger 5 is a reheating heat exchanger that is disposed on top of and below the hot water supply heat exchanger 4, 6 is a hot water transfer tube that forms the hot water heat exchanger 4, and 7 is a reheating heat exchanger. It is a reheating heat transfer tube. 8 is a hot water latent heat recovery heat exchanger installed downstream of the combustion gas of the hot water heat exchanger 4, 9 is a hot water latent heat transfer tube that forms a hot water latent heat recovery heat exchanger, and 10 is an outlet 9 b of the hot water latent heat transfer tube 9. It is a hot water pipe that connects the inlet 6 a of the hot water supply heat transfer pipe 6. 11 is a water supply pipe connected to the inlet 9a of the hot water latent heat transfer pipe 9, 12 is a hot water pipe connected to the outlet 6b of the hot water heat transfer pipe 6, 13 is a bath return pipe connected to the inlet of the additional heat transfer pipe 7, Is a bath outlet pipe connected to the outlet of the reheating heat transfer pipe 7.

給湯熱交換器4と追い焚き熱交換器5は共通のバーナ1によって加熱され、給水管11からの給水が給湯潜熱回収熱交換器8に入り、給湯熱交換器4と追い焚き熱交換器を経た燃焼ガスによって加熱され、温水管10を通じて、給湯熱交換器4に入り、バーナ1によって発生する燃焼ガスにさらに加熱され、所定の温度になって、給湯管12から流出する。この給湯潜熱回収熱交換器8では、主に燃焼ガス中の水蒸気に含まれる凝縮潜熱を回収することになる。また、風呂戻り管13から風呂水槽(図示せず)風呂水などが追い焚き熱交換器5に入り、燃焼ガスによって加熱された後、風呂往き管14を通じて、風呂水槽(図示せず)へ流れる。このように、給湯潜熱回収熱交換器8を設けたことにより、給湯運転時、燃焼ガス中の水蒸気の凝縮潜熱まで回収でき、高い熱効率が得られる(例えば、特許文献1参照)。
特開平10−267414号公報
The hot water supply heat exchanger 4 and the reheating heat exchanger 5 are heated by the common burner 1, and the water supplied from the water supply pipe 11 enters the hot water supply latent heat recovery heat exchanger 8, and the hot water supply heat exchanger 4 and the reheating heat exchanger are connected. The heated combustion gas is heated, enters the hot water supply heat exchanger 4 through the hot water pipe 10, further heated by the combustion gas generated by the burner 1, reaches a predetermined temperature, and flows out of the hot water supply pipe 12. In this hot water supply latent heat recovery heat exchanger 8, the condensation latent heat mainly contained in the water vapor in the combustion gas is recovered. Also, bath water (not shown) from the bath return pipe 13 enters the reheating heat exchanger 5 and is heated by the combustion gas, and then flows to the bath water tank (not shown) through the bath outlet pipe 14. . Thus, by providing the hot water supply latent heat recovery heat exchanger 8, it is possible to recover even the condensation latent heat of the water vapor in the combustion gas during the hot water supply operation, and high thermal efficiency is obtained (for example, see Patent Document 1).
JP-A-10-267414

しかしながら、上記従来の構成では潜熱回収用熱交換器の伝熱管に用いられる蛇腹管の機械加工上の制約から大きな伝熱面積をとることが困難であり、その為、蛇腹管の使用長さを増やして伝熱面積を増やすため必然的に潜熱回収用熱交換器が大きくなり、結果として給湯器筐体が大きくなるという課題があった。   However, in the above conventional configuration, it is difficult to take a large heat transfer area due to the machining restriction of the bellows tube used for the heat transfer tube of the latent heat recovery heat exchanger. In order to increase the heat transfer area by increasing the size, the heat exchanger for recovering latent heat is inevitably increased, resulting in an increase in the size of the water heater casing.

本発明は前記従来の課題を解決するもので、高効率で省スペースとした潜熱回収熱交換器を構成し、燃焼ガス通路の適正な場所に設置することで、燃焼効率の向上を図った燃焼装置を提供することを目的とする。   The present invention solves the above-described conventional problems, and constitutes a high-efficiency and space-saving latent heat recovery heat exchanger and is installed at an appropriate location in the combustion gas passage to improve combustion efficiency. An object is to provide an apparatus.

上記目的を達成するために本発明の燃焼装置は、潜熱回収熱交換器は複数の蛇腹状内管の外周に伝熱フィンを一体的に取り付けて構成するとともに、燃焼ガスの流れが上方から下方に偏向する燃焼ガス通路内に設置するようにしたものである。   In order to achieve the above object, in the combustion apparatus of the present invention, the latent heat recovery heat exchanger is configured by integrally attaching heat transfer fins to the outer circumferences of the plurality of bellows-shaped inner tubes, and the flow of combustion gas flows downward from above. It is designed to be installed in the combustion gas passage that is deflected to the right.

上記発明によれば、蛇腹管と伝熱フィンにより伝熱面積を増大させた高効率で省スペースとした潜熱回収熱交換器を提供することができるとともに、燃焼ガス経路を迂回させることで燃焼ガス中の潜熱回収を効率的に行うことができ、総合的な燃焼効率の向上と、結露水の処理構成を簡単に行うことができる。   According to the above invention, it is possible to provide a highly efficient and space-saving latent heat recovery heat exchanger having a heat transfer area increased by a bellows tube and a heat transfer fin, and by bypassing the combustion gas path, the combustion gas It is possible to efficiently recover the latent heat therein, and to improve the overall combustion efficiency and easily perform the dew condensation treatment configuration.

本発明の燃焼装置は、蛇腹管と伝熱フィンにより伝熱面積を増大させた高効率で省スペースとした潜熱回収熱交換器を提供することができるとともに、燃焼ガス経路を迂回させることで燃焼ガス中の潜熱回収を効率的に行うことができ、総合的な燃焼効率の向上と、結露水の処理構成を簡単に行うことができる。   The combustion apparatus of the present invention can provide a highly efficient and space-saving latent heat recovery heat exchanger with a heat transfer area increased by a bellows tube and heat transfer fins, and also burns by bypassing the combustion gas path The latent heat recovery in the gas can be efficiently performed, and the overall combustion efficiency can be improved and the dew condensation water treatment configuration can be easily performed.

第1の発明は、バーナと、前記バーナにより加熱され湯水と熱交換する給湯熱交換器と、前記給湯熱交換器の下流側の燃焼ガス通路に設け燃焼ガス中の水蒸気の凝縮潜熱を回収する潜熱回収熱交換器と、前記潜熱回収熱交換器を経由した燃焼ガスを排出する排気通路とを備え、前記潜熱回収熱交換器は、複数の蛇腹状内管の外周に伝熱フィンを一体的に取り付けて構成するとともに、前記燃焼ガスの流れが上方から下方に偏向する燃焼ガス通路内に設置するようにしたことを特徴とするものである。   The first invention is provided in a burner, a hot water heat exchanger that is heated by the burner and exchanges heat with hot water, and is provided in a combustion gas passage on the downstream side of the hot water heat exchanger to recover latent heat of condensation of water vapor in the combustion gas. A latent heat recovery heat exchanger; and an exhaust passage for discharging combustion gas via the latent heat recovery heat exchanger. The latent heat recovery heat exchanger has heat transfer fins integrally formed on the outer periphery of a plurality of bellows-shaped inner tubes. And is installed in a combustion gas passage in which the flow of the combustion gas is deflected downward from above.

そして、蛇腹管と伝熱フィンにより伝熱面積を増大させた高効率で省スペースとした潜熱回収熱交換器を提供することができるとともに、燃焼ガス経路を迂回させることで燃焼ガス中の潜熱回収を効率的に行うことができ、総合的な燃焼効率の向上と、結露水の処理構成を簡単に行うことができる。   In addition, it is possible to provide a highly efficient and space-saving latent heat recovery heat exchanger that increases the heat transfer area by means of a bellows tube and heat transfer fins, and also recovers latent heat in the combustion gas by bypassing the combustion gas path. Therefore, it is possible to improve the overall combustion efficiency and to easily perform the dew condensation water treatment configuration.

第2の発明は、潜熱回収熱交換器は複数の蛇腹管の外側に取り付けられた伝熱フィン部に折り返しを設けたことを特徴とするものである。   According to a second aspect of the present invention, the latent heat recovery heat exchanger is characterized in that folding is provided on the heat transfer fin portion attached to the outside of the plurality of bellows tubes.

そして、伝熱フィンの端面に折り返しを設けることにより伝熱面積をさらに増やすことができ、より有効に潜熱回収を行うことができる。   And the heat transfer area can be further increased by providing the end faces of the heat transfer fins, and the latent heat recovery can be performed more effectively.

第3の発明は、潜熱回収熱交換器は複数の蛇腹管の外側に取り付けられた伝熱フィン部に半円型の突起を設けたことを特徴とするものである。   A third invention is characterized in that the latent heat recovery heat exchanger is provided with a semicircular protrusion on a heat transfer fin portion attached to the outside of the plurality of bellows tubes.

そして、伝熱フィンの端面に半円型の突起を設けることにより伝熱面積をさらに増やすことができ、より有効に潜熱回収を行うことができる。   Further, by providing a semicircular projection on the end face of the heat transfer fin, the heat transfer area can be further increased, and latent heat recovery can be performed more effectively.

第4の発明は、潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部に円筒状のバーリングを設けたことを特徴とするものである。   The fourth invention is characterized in that the latent heat recovery heat exchanger is provided with a cylindrical burring in a heat transfer fin portion attached to the outside of the plurality of bellows tubes.

そして、伝熱フィンに円筒状のバーリングを設けることにより排気流れをより効率的に蛇腹管に導くことで、より有効に熱交換することが可能である。   Then, by providing a cylindrical burring on the heat transfer fin, the exhaust flow can be more efficiently guided to the bellows tube, so that heat can be exchanged more effectively.

第5の発明は、潜熱回収熱交換器は複数の蛇腹管の外側に取り付けられた伝熱フィン部にブリッジ上の切り起こしを設けたことを特徴とするものである。   According to a fifth aspect of the present invention, the latent heat recovery heat exchanger is characterized in that the heat transfer fin portion attached to the outside of the plurality of bellows tubes is provided with a cut-and-raised portion on the bridge.

そして、伝熱フィンにブリッジ上の切り起こしを設けることにより排気流れを拡散しより効率的に蛇腹管に導くことで、より有効に熱交換することが可能である。
第6の発明は、潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン全体に波型の曲げを設けたことを特徴とするものである。
Then, by providing the heat transfer fins with the cut and raised portions on the bridge, it is possible to more effectively exchange heat by diffusing the exhaust flow and guiding it more efficiently to the bellows tube.
According to a sixth aspect of the present invention, the latent heat recovery heat exchanger is characterized in that a wave-shaped bend is provided on the entire heat transfer fin attached to the outside of the plurality of bellows tubes.

そして、伝熱フィンに波型の曲げを全体に設けたことである。波型の曲げを全体にを設けることにより吸熱面積を増やすことにより、より有効に熱交換することが可能である。   And, the heat transfer fin is provided with a corrugated bend throughout. It is possible to exchange heat more effectively by increasing the endothermic area by providing a corrugated bend as a whole.

第7の発明は、潜熱回収熱交換器は複数の蛇腹管の外側に取り付けられた伝熱フィン部にくさび状の切り起こしを設けたことを特徴とするものである。   According to a seventh aspect of the present invention, the latent heat recovery heat exchanger is characterized in that a wedge-shaped cut and raised portion is provided in a heat transfer fin portion attached outside the plurality of bellows tubes.

そして、伝熱フィンにV型の切り起こしを設けることにより排気流れを効率的に蛇腹管に導くことで、より有効に熱交換することが可能である。   Then, by providing a V-shaped cut and raised on the heat transfer fin, the exhaust flow can be efficiently guided to the bellows tube, so that heat can be exchanged more effectively.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、本実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the present embodiment.

(実施の形態1)
図1は本発明の実施例1における熱交換装置のシステム構成図、図2は熱交換装置を構成する熱交換ユニットの斜視図、図3は熱交換ユニットの断面図である。
(Embodiment 1)
FIG. 1 is a system configuration diagram of a heat exchange device according to Embodiment 1 of the present invention, FIG. 2 is a perspective view of a heat exchange unit constituting the heat exchange device, and FIG. 3 is a cross-sectional view of the heat exchange unit.

図1において、10は燃料ガスを燃焼するバーナで、バーナ10の下流側には燃焼室11を構成するドラム缶12が設けられており、ドラム缶12の外周にドラム水管13が密着して取り付けられている。燃焼室11の下流側にはフィン管14を内包する顕熱熱交換器15と、排気室16が互いに密接して設けられている。排気室16の下流側に排気通路調整板17が設けられ、排気通路調整板17によって、排気ガスAが曲がって燃焼ガス通路18へ導かれる。燃焼ガス通路18の下流側部分は下に向き、排出通路21と連通している。排出通路21において、排気ガスBが曲がって導出通路22へ導かれ排気口23から排出する。また、排出通路21には結露水排出部24が接続されている。ここで、燃焼ガス通路18には、熱交換ユニット19を多数接続した熱交換装置20が設けられている。この熱交換ユニット19は、図2に示すように、例えばステンレス鋼などの耐食性材料あるいは表面処理を施した材料を用いた蛇腹状内管27の外周に該蛇腹状内管27を固定する伝熱フィン25を一体形成した構成としている。   In FIG. 1, reference numeral 10 denotes a burner that burns fuel gas. A drum can 12 that constitutes a combustion chamber 11 is provided on the downstream side of the burner 10, and a drum water pipe 13 is attached to the outer periphery of the drum can 12 in close contact. Yes. On the downstream side of the combustion chamber 11, a sensible heat exchanger 15 containing the fin tube 14 and an exhaust chamber 16 are provided in close contact with each other. An exhaust passage adjusting plate 17 is provided on the downstream side of the exhaust chamber 16, and the exhaust gas A is bent by the exhaust passage adjusting plate 17 and guided to the combustion gas passage 18. A downstream portion of the combustion gas passage 18 faces downward and communicates with the discharge passage 21. In the discharge passage 21, the exhaust gas B is bent and guided to the lead-out passage 22 and is discharged from the exhaust port 23. Further, a dew condensation water discharge unit 24 is connected to the discharge passage 21. Here, the combustion gas passage 18 is provided with a heat exchange device 20 in which a large number of heat exchange units 19 are connected. As shown in FIG. 2, the heat exchanging unit 19 has a heat transfer mechanism for fixing the bellows-like inner tube 27 to the outer periphery of the bellows-like inner tube 27 using a corrosion-resistant material such as stainless steel or a surface-treated material. The fin 25 is integrally formed.

以上のように構成された熱交換装置について、以下動作、作用を説明する。   The operation and action of the heat exchange apparatus configured as described above will be described below.

バーナ10の燃焼によって燃焼室11内で形成される高温燃焼ガスは顕熱熱交換器15でフィン管14内を流れる予熱水を加熱した後、低温燃焼ガスとなって、排気室16内に流入する。さらに排気室16の下流側において、この低温の排気ガスAが燃焼ガス通路18を通過しながら、下向きの流れ方向に偏向され、熱交換装置20を通過する。この時、熱交換装置20内において、伝熱フィン25、蛇腹状内管27を通じて蛇腹状内管27内を流れる水を予熱することによって排気ガスはさらに低温の排気ガスBとなり、燃焼排気ガス中の水蒸気は凝縮潜熱を奪われて外装部26の表面で凝縮水となる。この凝縮水にはCO2やNOxなどのガスが溶解しているため、酸性(pH=2〜4)を示す。発生した凝縮水は更に低温となった燃焼ガスとともに下向きに流れ、結露水排出部24から排出される。一方更に低温となった排気ガスBは排出通路21で偏向を受け、再び導出通路22を上方に流れ排気口23から大気に排出される。加熱流体である水は給水口(図示せず)から熱交換装置20の蛇腹状内管27へ導入され、低温の排気ガスAから水蒸気潜熱を奪い給水時よりやや温度が高い予熱水となって、熱交換装置20から導出される。そして、この予熱水はドラム缶12の外周を巻くドラム水管13へと導かれ、ドラム缶12の外周を冷却しながらフィン管14に至り、顕熱熱交換器15で所定の温度まで加熱された後出湯される。   The high-temperature combustion gas formed in the combustion chamber 11 by the combustion of the burner 10 heats the preheated water flowing in the fin tube 14 by the sensible heat exchanger 15 and then becomes low-temperature combustion gas and flows into the exhaust chamber 16. To do. Further, on the downstream side of the exhaust chamber 16, the low-temperature exhaust gas A is deflected in the downward flow direction while passing through the combustion gas passage 18 and passes through the heat exchange device 20. At this time, in the heat exchange device 20, by preheating the water flowing through the bellows-like inner tube 27 through the heat transfer fins 25 and the bellows-like inner tube 27, the exhaust gas becomes a lower temperature exhaust gas B, and the combustion exhaust gas The water vapor is deprived of condensation latent heat and becomes condensed water on the surface of the exterior portion 26. Since gas such as CO2 and NOx is dissolved in this condensed water, it shows acidity (pH = 2 to 4). The generated condensed water flows downward together with the combustion gas that has become lower in temperature, and is discharged from the condensed water discharge unit 24. On the other hand, the exhaust gas B having a lower temperature is deflected by the discharge passage 21, flows again through the outlet passage 22, and is discharged from the exhaust port 23 to the atmosphere. Water, which is a heating fluid, is introduced from a water supply port (not shown) into the bellows-like inner tube 27 of the heat exchange device 20, and takes steam latent heat from the low-temperature exhaust gas A to become preheated water having a slightly higher temperature than that at the time of water supply. , Derived from the heat exchange device 20. Then, the preheated water is led to a drum water pipe 13 that winds around the outer periphery of the drum can 12, reaches the fin pipe 14 while cooling the outer periphery of the drum can 12, and is heated to a predetermined temperature by the sensible heat exchanger 15 and then discharged from the hot water. Is done.

このように、複数の蛇腹状内管27を固定する伝熱フィン25と一体構成の蛇腹状内管
27を用いて構成された熱交換ユニット19は、蛇腹状内管27単独で構成された熱交換ユニットに対し、より多くの熱交換面積を得ることができる。
As described above, the heat exchange unit 19 configured using the bellows-shaped inner tube 27 integrally formed with the heat transfer fins 25 for fixing the plurality of bellows-shaped inner tubes 27 has the heat configured by the bellows-shaped inner tube 27 alone. More heat exchange area can be obtained for the exchange unit.

また、上流側の低温の加熱流体を、下流側の低温の燃焼ガスで熱交換装置20によって熱交換させ、下流側の高温の加熱流体を、上流側の高温の燃焼ガスで顕熱熱交換器15によって熱交換させる対向型熱交換システムとすることで加熱流体と燃焼ガスとの温度差を確保し効果的な伝熱を行なわせ小型の熱交換システムを実現することができる。   Further, the heat exchange device 20 exchanges heat with the low-temperature heating fluid on the upstream side by the low-temperature combustion gas on the downstream side, and the sensible heat exchanger uses the high-temperature heating fluid on the downstream side with the high-temperature combustion gas on the upstream side. By adopting the opposed heat exchange system in which heat is exchanged by 15, a temperature difference between the heating fluid and the combustion gas is ensured, and effective heat transfer is performed to realize a small heat exchange system.

(実施の形態2)
図3は、本発明の第2の実施の形態における熱交換ユニット断面図を示す。
(Embodiment 2)
FIG. 3 shows a cross-sectional view of the heat exchange unit in the second embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図4に示すごとく熱交換ユニット19は伝熱フィン25の端面に折り返しを設けたことである。   In the present embodiment, the difference from the first embodiment is that the heat exchange unit 19 is provided with a turn on the end face of the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、端面に折り返し25bを設けた伝熱フィン25で構成される熱交換ユニットは端面に折り返し25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積が大きく取れるとともに、上方への排気流れ25Cに抵抗となり伝熱時間を長くすることができる。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型化な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the folded back 25b on the end face is in contact with the combustion gas as compared with the heat exchange unit constituted by the heat transfer fins not provided with the folded back 25b on the end face. As a result, a large heat transfer area can be obtained and resistance to the upward exhaust flow 25 </ b> C can be increased, thereby extending the heat transfer time. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a heat exchange device that is smaller than that of the first embodiment can be realized.

(実施の形態3)
図4は、本発明の第3の実施の形態における熱交換ユニット断面図を示す。
(Embodiment 3)
FIG. 4 shows a cross-sectional view of the heat exchange unit in the third embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図6に示すごとく熱交換ユニット19は伝熱フィン25の端面に端面に半円型の突起25bを設けたことである。   In the present embodiment, the difference from the first embodiment is that the heat exchange unit 19 is provided with a semicircular protrusion 25b on the end face of the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、端面に半円型の突起25bを設けた伝熱フィン25で構成される熱交換ユニットは端面に半円型の突起25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積は大きく取れる。また、半円型の突起25bに排気が攪拌される。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the semicircular protrusions 25b on the end face is heat exchange constituted by the heat transfer fins not provided with the semicircular protrusions 25b on the end face. Compared to the unit, the heat transfer area in contact with the combustion gas can be increased. Further, the exhaust gas is agitated by the semicircular protrusion 25b. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a smaller heat exchange device than that of the first embodiment can be realized.

(実施の形態4)
図5(a)(b)は、本発明の第4の実施の形態の熱交換ユニット断面図及び斜視図である。
(Embodiment 4)
5A and 5B are a cross-sectional view and a perspective view of a heat exchange unit according to the fourth embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図5に示すごとく熱交換ユニット19は伝熱フィン25に円形のバーリング25bを設けたことである。   The present embodiment is different from the first embodiment in that the heat exchange unit 19 is provided with a circular burring 25b on the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、円形のバーリング25bを設けた伝熱フィン25で構成される熱交換ユニットは円形のバーリング25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積は大きく取れる。また、円形のバーリング25bにより排気をより効率的に蛇腹状内管27に導くことができる。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the circular burring 25b is in contact with the combustion gas as compared with the heat exchange unit constituted by the heat transfer fins not having the circular burring 25b. A large heat transfer area can be obtained. Further, the exhaust can be more efficiently guided to the bellows-like inner tube 27 by the circular burring 25b. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a smaller heat exchange device than that of the first embodiment can be realized.

(実施の形態5)
図6(a)(b)は、本発明の第5の実施の形態の熱交換ユニット断面図及び斜視図である。
(Embodiment 5)
6A and 6B are a sectional view and a perspective view of a heat exchange unit according to the fifth embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図6に示すごとく熱交換ユニット19は伝熱フィン25に矩形のブリッジ25bを設けたことである。   In the present embodiment, the difference from the first embodiment is that the heat exchange unit 19 is provided with a rectangular bridge 25b on the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、矩形のブリッジ25bを設けた伝熱フィン25で構成される熱交換ユニットは矩形のブリッジ25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積は大きく取れる。また、矩形のブリッジ25bにより排気をより効率的に蛇腹状内管27に導くことができる。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the rectangular bridge 25b is in contact with the combustion gas as compared with the heat exchange unit constituted by the heat transfer fins not having the rectangular bridge 25b. A large heat transfer area can be obtained. Further, the exhaust can be more efficiently guided to the bellows-shaped inner tube 27 by the rectangular bridge 25b. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a smaller heat exchange device than that of the first embodiment can be realized.

(実施の形態6)
図7は、本発明の第6の実施の形態の熱交換ユニット断面図を示す。
(Embodiment 6)
FIG. 7 shows a sectional view of a heat exchange unit according to the sixth embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図7に示すごとく熱交換ユニット19は伝熱フィン25に波型の曲げ25bを全体に設けたことである。   In the present embodiment, the difference from the first embodiment is that the heat exchange unit 19 is provided with a wave-shaped bend 25b in the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、端面に波型の曲げ25bを設けた伝熱フィン25で構成される熱交換ユニットは端面に波型の曲げ25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積は大きく取れる。また、波型の曲げ25bに排気が攪拌される。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型化な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the corrugated bend 25b on the end face is changed to the heat exchange unit constituted by the heat transfer fin not having the corrugated bend 25b on the end face. In comparison, the heat transfer area in contact with the combustion gas can be increased. Further, the exhaust gas is agitated in the corrugated bend 25b. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a heat exchange device that is smaller than that of the first embodiment can be realized.

(実施の形態7)
図8(a)(b)は、本発明の第7の実施の形態の熱交換ユニット断面図及び斜視図である。
(Embodiment 7)
8A and 8B are a sectional view and a perspective view of a heat exchange unit according to the seventh embodiment of the present invention.

本実施の形態において、第1の実施の形態と異なる点は、図8に示すごとく熱交換ユニット19は伝熱フィン25にくさび状の切り起こし25bを設けたことである。   In the present embodiment, the difference from the first embodiment is that the heat exchanging unit 19 is provided with a wedge-shaped cut and raised portion 25b in the heat transfer fin 25 as shown in FIG.

次に作用を説明すると、くさび状の切り起こし25bを設けた伝熱フィン25で構成される熱交換ユニットはくさび状の切り起こし25bを持たない伝熱フィンで構成される熱交換ユニットに比べ、燃焼ガスと接触する伝熱面積は大きく取れる。また、くさび状の切り起こし25bにより排気をより効率的に蛇腹状内管27に導くことができる。すなわち、これによって、熱交換ユニット19の吸熱効果が向上し、実施例1と比べより小型な熱交換装置が実現できる。   Next, the operation will be described. The heat exchange unit constituted by the heat transfer fins 25 provided with the wedge-shaped cut and raised portions 25b is compared with the heat exchange unit constituted by the heat transfer fins not having the wedge-shaped cut and raised portions 25b. A large heat transfer area in contact with the combustion gas can be obtained. Further, the exhaust can be more efficiently guided to the bellows-like inner tube 27 by the wedge-shaped cut and raised portion 25b. That is, by this, the heat absorption effect of the heat exchange unit 19 is improved, and a smaller heat exchange device than that of the first embodiment can be realized.

以上のように、本発明の燃焼装置は、従来よりコンパクトかつ高効率な潜熱回収装置を提供することが可能となるため、ガス、石油給湯機の熱交換装置として適用できる。   As described above, the combustion apparatus of the present invention can provide a latent heat recovery apparatus that is more compact and highly efficient than conventional ones, and can therefore be applied as a heat exchange apparatus for gas and oil water heaters.

本発明の実施の形態1における燃焼装置の断面図Sectional drawing of the combustion apparatus in Embodiment 1 of this invention 同燃焼装置の熱交換ユニットの斜視図A perspective view of a heat exchange unit of the combustion apparatus 本発明の実施の形態2における熱交換ユニットの斜視図The perspective view of the heat exchange unit in Embodiment 2 of this invention 本発明の実施の形態3における熱交換ユニットの斜視図The perspective view of the heat exchange unit in Embodiment 3 of this invention (a)(b)本発明の実施の形態4における熱交換ユニットの断面図、斜視図(A) (b) Cross section and perspective view of a heat exchange unit according to Embodiment 4 of the present invention (a)(b)本発明の実施の形態5における熱交換ユニットの断面図、斜視図(A) (b) Cross-sectional view and perspective view of heat exchange unit according to Embodiment 5 of the present invention 本発明の実施例6における熱交換ユニットの斜視図The perspective view of the heat exchange unit in Example 6 of this invention (a)(b)本発明の実施の形態7における熱交換ユニットの断面図、斜視図(A) (b) Cross section and perspective view of a heat exchange unit in Embodiment 7 of the present invention 従来の燃焼装置の断面図Cross-sectional view of a conventional combustion device

符号の説明Explanation of symbols

10 バーナ
15 顕熱熱交換器(給湯熱交換器)
18 燃焼ガス通路
19 熱交換ユニット(潜熱回収熱交換器)
25 伝熱フィン(潜熱回収熱交換器)
27 蛇腹管(潜熱回収熱交換器)
10 Burner 15 Sensible heat exchanger (hot water heat exchanger)
18 Combustion gas passage 19 Heat exchange unit (latent heat recovery heat exchanger)
25 Heat transfer fin (latent heat recovery heat exchanger)
27 Bellows tube (latent heat recovery heat exchanger)

Claims (7)

バーナと、前記バーナにより加熱され湯水と熱交換する給湯熱交換器と、前記給湯熱交換器の下流側の燃焼ガス通路に設け燃焼ガス中の水蒸気の凝縮潜熱を回収する潜熱回収熱交換器と、前記潜熱回収熱交換器を経由した燃焼ガスを排出する排気通路とを備え、前記潜熱回収熱交換器は、複数の蛇腹状内管の外周に伝熱フィンを一体的に取り付けて構成するとともに、前記燃焼ガスの流れが上方から下方に偏向する燃焼ガス通路内に設置するようにした燃焼装置。 A burner, a hot water heat exchanger that is heated by the burner and exchanges heat with hot water, a latent heat recovery heat exchanger that is provided in a combustion gas passage on the downstream side of the hot water heat exchanger and recovers the latent heat of condensation of water vapor in the combustion gas; An exhaust passage for discharging combustion gas via the latent heat recovery heat exchanger, and the latent heat recovery heat exchanger is configured by integrally attaching heat transfer fins to the outer periphery of a plurality of bellows-shaped inner tubes. A combustion apparatus installed in a combustion gas passage in which the flow of the combustion gas is deflected downward from above. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部に折り返しを設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with folds on heat transfer fin portions attached to the outside of the plurality of bellows tubes. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部に半円型の突起を設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with a semicircular projection on a heat transfer fin portion attached to the outside of the plurality of bellows tubes. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部に円筒状のバーリングを設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with a cylindrical burring in a heat transfer fin portion attached to the outside of the plurality of bellows tubes. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部にブリッジ上の切り起こしを設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with a cut-and-raised portion on the bridge in a heat transfer fin portion attached to the outside of the plurality of bellows tubes. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン全体に波型の曲げを設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with a wave-shaped bend in the entire heat transfer fin attached to the outside of the plurality of bellows tubes. 潜熱回収熱交換器は、複数の蛇腹管の外側に取り付けられた伝熱フィン部にくさび状の切り起こしを設けた請求項1記載の燃焼装置。 The combustion apparatus according to claim 1, wherein the latent heat recovery heat exchanger is provided with a wedge-shaped cut and raised at a heat transfer fin portion attached to the outside of the plurality of bellows tubes.
JP2005251162A 2005-08-31 2005-08-31 Combustion apparatus Pending JP2007064551A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011233296A (en) * 2010-04-26 2011-11-17 Eneos Celltech Co Ltd Fuel cell system
JP2012117723A (en) * 2010-11-30 2012-06-21 T Rad Co Ltd Heat exchanger for hot-water supply
JP2022087576A (en) * 2020-12-01 2022-06-13 井上ヒーター株式会社 Heat exchanger fin and heat exchanger having the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011233296A (en) * 2010-04-26 2011-11-17 Eneos Celltech Co Ltd Fuel cell system
JP2012117723A (en) * 2010-11-30 2012-06-21 T Rad Co Ltd Heat exchanger for hot-water supply
JP2022087576A (en) * 2020-12-01 2022-06-13 井上ヒーター株式会社 Heat exchanger fin and heat exchanger having the same
JP7374066B2 (en) 2020-12-01 2023-11-06 井上ヒーター株式会社 Heat exchanger fins and heat exchangers equipped with the same

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