JP2010175103A - Heat exchanger - Google Patents

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JP2010175103A
JP2010175103A JP2009016329A JP2009016329A JP2010175103A JP 2010175103 A JP2010175103 A JP 2010175103A JP 2009016329 A JP2009016329 A JP 2009016329A JP 2009016329 A JP2009016329 A JP 2009016329A JP 2010175103 A JP2010175103 A JP 2010175103A
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water
pipe
heat exchanger
pipe end
end opening
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JP5030981B2 (en
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Hidekatsu Naruse
英克 成瀬
Yoichi Kojima
洋一 小島
Shinya Otsubo
伸也 大坪
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Rinnai Corp
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Rinnai Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat exchanger properly draining a heat absorption pipe with a simple structure even when the heat absorption pipe is thinned. <P>SOLUTION: In this heat exchanger 5 in which the heat absorption pipe 52 is disposed in a case 50 where a combustion exhaust flows, one end section and the other end section of the heat absorption pipe 52 are connected with an inflow header 6a and an outflow header 6b disposed on a side plate 51 of the case 50, and the water flowing into the heat absorption pipe 52 is heated by the combustion exhaust, the inflow header 6a the height position of which is on a low position side, is provided with a drainage plate 7 opposed to pipe end openings 52a to form a drainage flow channel for the water reaching the pipe end openings 52a in draining the heat absorption pipe 52, the drainage flow channel is formed by a recessed groove 70 formed on an opposite face to the pipe end openings 52a, of the drainage plate 7 and extending in the vertical direction, and the recessed groove 70 has a groove width narrower than a diameter of the pipe end openings 52a, and is disposed in opposition to the pipe end openings 52a, and continuously opposed to the plurality of pipe end openings 52a arranged in the vertical direction. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、流入ヘッダと流出ヘッダとを介して吸熱管内に流す水を燃焼排気により熱交換加熱する熱交換器に関する。   The present invention relates to a heat exchanger that heats and heats water flowing into a heat absorption pipe via an inflow header and an outflow header by combustion exhaust.

高効率給湯装置に搭載される潜熱熱交換器は、燃焼排気が流れるケース内に複数本の吸熱管を配置し、これら吸熱管の一端部と他端部とをケース側板の流入ヘッダと流出ヘッダとに接続し、この吸熱管に水を流して燃焼排気中の水蒸気を凝縮させて潜熱を回収するように構成されている(特許文献1)。   A latent heat heat exchanger mounted on a high-efficiency hot water supply apparatus has a plurality of heat absorption tubes arranged in a case through which combustion exhaust flows, and one end portion and the other end portion of these heat absorption tubes are connected to an inflow header and an outflow header of a case side plate. And is configured to collect the latent heat by allowing water to flow through the heat absorption tube to condense the water vapor in the combustion exhaust (Patent Document 1).

このような潜熱熱交換器おいて、更なる小型化、高効率化を実現するため吸熱管の細管化が図られている。つまり、吸熱管の細管化を図ることで、ケースの限られたスペース内により多くの吸熱管を配置でき、吸熱管全体の伝熱面積を大きくできるからである。しかし、吸熱管の細管化を図った場合、冬季における吸熱管内の凍結防止のため吸熱管から水抜きを行う際、水の表面張力に起因して吸熱管のパイプ端開口に水膜が張って吸熱管内の流水方向下流部に水が残ってしまうことがあった。従って、吸熱管の細管化を図る場合には、吸熱管内の水抜き作業が円滑に行われることも望まれる。   In such a latent heat exchanger, the heat absorption tube is made narrower in order to realize further downsizing and higher efficiency. That is, by reducing the size of the heat absorption tube, more heat absorption tubes can be arranged in the limited space of the case, and the heat transfer area of the entire heat absorption tube can be increased. However, if the endothermic tube is made thinner, when water is drained from the endothermic tube to prevent freezing in the endothermic tube in winter, a water film is stretched at the end of the endothermic tube due to the surface tension of the water. Water sometimes remained in the downstream portion of the heat absorption pipe in the flowing direction. Therefore, when the heat absorption tube is made thin, it is also desired that the water draining operation in the heat absorption tube is smoothly performed.

ところで、図8に示すように、従来の潜熱熱交換器805として、吸熱管850の端部に延設管体部851を接続し、この延設管体部851は、ケース870の外部に露出して先端部にヘッダ806Aを取付け、先端寄りほど高さが低くなる曲げ部851aを形成するものがある(特許文献2)。これによると、吸熱管850の細管化を図った場合でも、延設管体部851の曲げ部851aに存在する水の水頭圧が延設管体部851の先端に作用し、水抜き作業時に延設管体部851の先端開口に水膜が張ることを防止し円滑な水抜きが可能となるとしている。   By the way, as shown in FIG. 8, as a conventional latent heat exchanger 805, an extended tube portion 851 is connected to the end of the heat absorption tube 850, and this extended tube portion 851 is exposed to the outside of the case 870. Then, there is a type in which a header 806A is attached to the tip, and a bent portion 851a whose height decreases toward the tip (Patent Document 2). According to this, even when the endothermic tube 850 is narrowed, the water head pressure of the water existing in the bent portion 851a of the extended tube portion 851 acts on the tip of the extended tube portion 851, and during draining work. It is supposed that a water film is prevented from being stretched at the distal end opening of the extended tube portion 851 and smooth drainage is possible.

しかし、図8に示す従来の潜熱熱交換器805は、延設管体部851を新たに設けることにより熱交換器805の小型化を阻害し、また、複数本の吸熱管850のそれぞれに対して延設管体部851が必要なため、部品点数の増加及びロー付け等の接続箇所の増加等という問題があった。   However, the conventional latent heat exchanger 805 shown in FIG. 8 prevents the downsizing of the heat exchanger 805 by newly providing the extended tube body portion 851, and also prevents each of the plurality of heat absorption tubes 850. Therefore, there is a problem that the number of parts is increased and the number of connecting portions such as brazing is increased.

特開2007−163096JP2007-163096

特開2007−333343JP2007-333343

本発明は、上記事情に鑑みてなされたものであり、吸熱管の細管化を図った場合でも、簡易な構造で吸熱管の水抜きが適切に行われる熱交換器を提供することを課題とする。   The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a heat exchanger in which drainage of an endothermic tube is appropriately performed with a simple structure even when the endothermic tube is narrowed. To do.

本発明に係る熱交換器は、
燃焼排気が流れるケース内に吸熱管を配置し、吸熱管の一端部と他端部とをケースの側板に設けた流入ヘッダと流出ヘッダとに接続して吸熱管内に流す水を燃焼排気により熱交換加熱する熱交換器において、
高さ位置が低位置側に配置されるヘッダには、吸熱管内の水抜き時にパイプ端開口に達した水の水抜き流路を形成させるための水抜き板を、上下方向に並設された複数のパイプ端開口に対して連続して対向配置したものである。
The heat exchanger according to the present invention is
An endothermic tube is arranged in the case through which the combustion exhaust flows, and one end and the other end of the endothermic tube are connected to an inflow header and an outflow header provided on the side plate of the case, and the water flowing in the endothermic tube is heated by the combustion exhaust. In heat exchangers that exchange heat,
On the header whose height position is located on the low position side, a drainage plate is arranged in parallel in the vertical direction to form a drainage channel that reaches the pipe end opening when draining the heat absorption pipe. A plurality of pipe end openings are continuously arranged to face each other.

これにより、吸熱管の水抜き時にパイプ端開口に水の表面張力に起因した水膜が保持されようとしても、このパイプ端開口に達した水は、水抜き板によって形成される水抜き流路に導かれてパイプ端開口から水抜き流路へ流出される。このパイプ端開口から水抜き流路への水の流出によってパイプ端開口における水の表面張力に起因した水膜の形成が阻止される。従って、吸熱管の細管化により口径を小さくした場合でも、吸熱管のパイプ端開口での水の表面張力に起因して吸熱管の流水方向下流部に水が残されることがなく吸熱管内の水抜きが確実に行われる。また、水抜き板は、ヘッダ内に設けられるため、熱交換器の小型化を阻害することもない。   As a result, even if a water film due to the surface tension of water is held in the pipe end opening when draining the heat absorption pipe, the water reaching the pipe end opening is drained by the drain plate. To flow out from the pipe end opening to the drainage channel. Formation of a water film due to the surface tension of water at the pipe end opening is prevented by the outflow of water from the pipe end opening to the drain passage. Therefore, even when the diameter is reduced by reducing the endothermic tube, the water in the endothermic tube does not remain in the downstream portion of the endothermic tube in the flowing direction due to the surface tension of the water at the pipe end opening of the endothermic tube. Unplugging is performed reliably. Moreover, since the drainage plate is provided in the header, it does not hinder downsizing of the heat exchanger.

上記水抜き流路は、水抜き板に形成された上下方向に延びる凹溝により構成され、
上記凹溝は、パイプ端開口の口径よりも溝幅が狭く且つパイプ端開口に連通されていることが望ましい。
これにより、吸熱管の水抜き時にパイプ端開口に水の表面張力に起因した水膜が形成されようとしても、このパイプ端開口に達した水は、水抜き流路となる凹溝に導かれ、凹溝を伝って流下される。このパイプ端開口から凹溝へ水が流下することによってパイプ端開口における水の表面張力に起因した水膜の形成が阻止される。従って、吸熱管の細管化により口径を小さくした場合でも、吸熱管のパイプ端開口での水の表面張力に起因して吸熱管の流水方向下流部に水が残されることがなく吸熱管内の水抜きが確実に行われる。
The drainage channel is constituted by a concave groove formed in the drainage plate extending in the vertical direction,
The concave groove preferably has a groove width narrower than the diameter of the pipe end opening and communicates with the pipe end opening.
As a result, even when a water film due to the surface tension of the water is formed at the pipe end opening when draining the heat absorption pipe, the water reaching the pipe end opening is guided to the concave groove serving as the water drainage channel. , Will flow down the groove. Formation of a water film due to the surface tension of water at the pipe end opening is prevented by water flowing from the pipe end opening to the concave groove. Therefore, even when the diameter is reduced by reducing the endothermic tube, the water in the endothermic tube does not remain in the downstream portion of the endothermic tube in the flowing direction due to the surface tension of the water at the pipe end opening of the endothermic tube. Unplugging is performed reliably.

上記水抜き流路は、パイプ端開口と水抜き板との間の隙間により構成され、
上記隙間は、パイプ端開口に水の表面張力に起因して形成される水膜の盛り上がり量以下に設定されることが望ましい。
これにより、吸熱管の水抜き時にパイプ端開口に水の表面張力に起因した水膜が形成されようとしても、このパイプ端開口に達した水は、水抜き流路となる上記隙間に導かれ、その後は水抜き板を伝って流下される。このパイプ端開口から水抜き板を伝って水が流下することによってパイプ端開口における水の表面張力に起因した水膜の形成が阻止される。従って、吸熱管の細管化により口径を小さくした場合でも、吸熱管のパイプ端開口での水の表面張力に起因して吸熱管の流水方向下流部に水が残されることがなく吸熱管内の水抜きが確実に行われる。
The drainage channel is constituted by a gap between the pipe end opening and the drainage plate,
The gap is desirably set to be equal to or less than the rising amount of the water film formed in the pipe end opening due to the surface tension of water.
As a result, even when a water film due to the surface tension of water is formed at the pipe end opening when draining the heat absorption pipe, the water reaching the pipe end opening is guided to the gap serving as the water drainage channel. After that, it flows down the drainage plate. Formation of a water film due to the surface tension of the water at the pipe end opening is prevented by the water flowing down from the pipe end opening through the drain plate. Therefore, even when the diameter is reduced by reducing the endothermic tube, the water in the endothermic tube does not remain in the downstream portion of the endothermic tube in the flowing direction due to the surface tension of the water at the pipe end opening of the endothermic tube. Unplugging is performed reliably.

上記水抜き板は、水透過部材により構成される。
これにより、水が水抜き板を円滑に通過することができるので、熱交換器の通常使用時においてヘッダを介した吸熱管への水の流通を妨げることがなく円滑に行うことができる。
The drain plate is constituted by a water permeable member.
Thereby, since water can pass smoothly through the drain plate, it can be smoothly performed without disturbing the flow of water to the heat absorption pipe via the header during normal use of the heat exchanger.

以上のように、本発明に係る熱交換器によれば、吸熱管の細管化を図った場合でも、パイプ端開口に水抜き板を配置させるといった簡単な構成で吸熱管の水抜きを確実に行うことができる。従って、水抜き作業を行ったにもかかわらず吸熱管内に残水が存在して冬季に凍結し吸熱管を破損させるなどの不具合を起こすこともない。よって、小型化、高効率化を実現すると共に、吸熱管の水抜きを適切に行える熱交換器の提供が可能となる。   As described above, according to the heat exchanger of the present invention, even when the endothermic tube is made thin, it is possible to reliably drain the endothermic tube with a simple configuration in which a drainage plate is arranged at the pipe end opening. It can be carried out. Therefore, there is no problem such as remaining water in the endothermic tube even though the drainage operation is performed, and freezing in the winter and damaging the endothermic tube. Therefore, it is possible to provide a heat exchanger that can achieve miniaturization and high efficiency and can appropriately drain water from the heat absorption pipe.

実施形態における熱交換器を備えた給湯装置の構成を示す断面図である。It is sectional drawing which shows the structure of the hot water supply apparatus provided with the heat exchanger in embodiment. 副熱交換器の流入ヘッダの部分を分解した斜視図である。It is the perspective view which decomposed | disassembled the part of the inflow header of a subheat exchanger. 副熱交換器における流入ヘッダの内部構成を示す横断面図である。It is a cross-sectional view which shows the internal structure of the inflow header in a subheat exchanger. 副熱交換器における流入ヘッダの内部構成を示す縦断面図である。It is a longitudinal cross-sectional view which shows the internal structure of the inflow header in a subheat exchanger. 水抜き板を示す図である。It is a figure which shows the drain plate. 他の実施形態による副熱交換器の流入ヘッダの内部構成を示す横断面図である。It is a cross-sectional view which shows the internal structure of the inflow header of the subheat exchanger by other embodiment. 他の実施形態による副熱交換器の流入ヘッダの内部構成を示す縦断面図である。It is a longitudinal cross-sectional view which shows the internal structure of the inflow header of the subheat exchanger by other embodiment. 従来例として、吸熱管内の水抜き構造を備えた潜熱熱交換器を示す側面図である。It is a side view which shows the latent-heat heat exchanger provided with the water draining structure in an endothermic tube as a prior art example.

以下に、本発明の実施形態について添付図面を参照しながら説明する。
図1に示す給湯装置1は、潜熱回収型給湯装置1であり、外装ケース2内に、ガスバーナ31を内蔵する燃焼筐3と、燃焼筐3の上方の主熱交換器4と、主熱交換器4の上方の副熱交換器5とを備えている。燃焼筐3の下側には、燃焼筐3内に燃焼用空気を供給する給気ファン11が設置されている。
Embodiments of the present invention will be described below with reference to the accompanying drawings.
A hot water supply apparatus 1 shown in FIG. 1 is a latent heat recovery type hot water supply apparatus 1, and includes a combustion housing 3 containing a gas burner 31 in an outer case 2, a main heat exchanger 4 above the combustion housing 3, and main heat exchange. The auxiliary heat exchanger 5 above the unit 4 is provided. An air supply fan 11 that supplies combustion air into the combustion housing 3 is installed below the combustion housing 3.

主熱交換器4は、ガスバーナ31の燃焼排気が流れる胴部40内に間隔を存して並設した多数の吸熱フィン41と、これら吸熱フィン41を蛇行形状に貫通する吸熱管42とを備えている。副熱交換器5は、潜熱熱交換器であり、ケース50内に横向き蛇行形状に配置した複数本の吸熱管52を備えている。吸熱管52は、耐食性金属、例えば、ステンレス製、チタン製等のコルゲート管を蛇行形状に曲げ加工して形成される。ケース50の横方向一側の側板51には、流入ヘッダ6aと流出ヘッダ6bとが設けられ、複数本の吸熱管52の一端部が流入ヘッダ6aに接続され、他端部が流出ヘッダ6bに接続されている。流入ヘッダ6aには給水管81が接続され、流出ヘッダ6bには主熱交換器4の吸熱管52の上流端に繋がる接続管83が接続されている。主熱交換器4の吸熱管52の下流端には出湯管82が接続されている。副熱交換器5は、底板53の後部には主熱交換器4を通過した燃焼排気の排気導入口54が開設され、ケース50の前面には副熱交換器5を通過した燃焼排気を排出する排気口55が設けられている。   The main heat exchanger 4 includes a large number of endothermic fins 41 arranged in parallel in the body 40 through which the combustion exhaust gas of the gas burner 31 flows, and an endothermic pipe 42 penetrating the endothermic fins 41 in a meandering shape. ing. The auxiliary heat exchanger 5 is a latent heat exchanger, and includes a plurality of heat absorption tubes 52 arranged in a meandering manner in the case 50. The endothermic tube 52 is formed by bending a corrugated tube made of a corrosion-resistant metal such as stainless steel or titanium into a meandering shape. The side plate 51 on one side of the case 50 is provided with an inflow header 6a and an outflow header 6b. One end of a plurality of heat absorption tubes 52 is connected to the inflow header 6a, and the other end is connected to the outflow header 6b. It is connected. A water supply pipe 81 is connected to the inflow header 6a, and a connection pipe 83 connected to the upstream end of the heat absorption pipe 52 of the main heat exchanger 4 is connected to the outflow header 6b. A tapping pipe 82 is connected to the downstream end of the heat absorption pipe 52 of the main heat exchanger 4. The auxiliary heat exchanger 5 has an exhaust inlet 54 for combustion exhaust that has passed through the main heat exchanger 4 at the rear of the bottom plate 53, and exhausts the combustion exhaust that has passed through the auxiliary heat exchanger 5 on the front surface of the case 50. An exhaust port 55 is provided.

そして、出湯管82の下流端の出湯栓(図示せず)が開かれると給水管81から副熱交換器5の吸熱管52、主熱交換器4の吸熱管42へと通水され、また、ガスバーナ31が燃焼される。主熱交換器4では、ガスバーナ31の燃焼による燃焼排気中から主に顕熱を吸収して吸熱管42内を流れる水を熱交換加熱する。副熱交換器5では、燃焼排気中の水蒸気を凝縮して潜熱を吸収して吸熱管52内の水を熱交換加熱する。これにより、副熱交換器5及び主熱交換器4で加熱された温水が出湯管82から出湯される。   When a hot water tap (not shown) at the downstream end of the hot water pipe 82 is opened, water is passed from the water supply pipe 81 to the heat absorption pipe 52 of the sub heat exchanger 5 and the heat absorption pipe 42 of the main heat exchanger 4. The gas burner 31 is burned. In the main heat exchanger 4, sensible heat is mainly absorbed from the combustion exhaust gas generated by the combustion of the gas burner 31, and the water flowing in the heat absorption pipe 42 is heat exchange heated. The auxiliary heat exchanger 5 condenses the water vapor in the combustion exhaust and absorbs latent heat to heat and heat the water in the heat absorption pipe 52. As a result, the hot water heated by the sub heat exchanger 5 and the main heat exchanger 4 is discharged from the hot water discharge pipe 82.

なお、副熱交換器5は、後上がりに僅かに傾斜(約5°)して設置されている。副熱交換器5において燃焼排気中の水蒸気の凝縮により発生した酸性のドレン水は、傾斜した底板53に滴下され、低位置のドレン回収部56からドレン排水管57を通り中和器58で中和された後、下水に排水される。   The auxiliary heat exchanger 5 is installed with a slight inclination (about 5 °) in the rearward direction. Acidic drain water generated by the condensation of water vapor in the combustion exhaust gas in the auxiliary heat exchanger 5 is dropped on the inclined bottom plate 53, and passes through the drain drain pipe 57 from the drain recovery portion 56 at the lower position and is neutralized in the neutralizer 58. After being summed, it is drained into the sewer.

図2、図3、図4に示すように、副熱交換器5における流入ヘッダ6aと流出ヘッダ6bは、側板51の所定位置を絞り加工することによりケース50の内方へ凹ませた凹部よりなるヘッダ本体61と、ケース50の外側から配設されてヘッダ本体61との間に閉鎖空間60を画成するヘッダ蓋62とを備えている。ヘッダ本体61には、吸熱管52用の差込口63が複数本の吸熱管52に対応して複数開設され、ヘッダ蓋62には、給水管81や接続管83用の単一のジョイント部64が設けられている。ヘッダ蓋62は、ジョイント部64を設けない裏側が全周囲に周壁65を形成する浅い器状に形成されている。ヘッダ蓋62の裏側をヘッダ本体61の凹部に向けてヘッダ本体61の凹部内にヘッダ蓋62を嵌め込み、ヘッダ本体61の凹部内壁とヘッダ蓋62の周壁65外面とを重ね合わせた状態でロー付けして各ヘッダ6a,6bが形成される。   As shown in FIGS. 2, 3, and 4, the inflow header 6 a and the outflow header 6 b in the sub heat exchanger 5 are formed from a recess recessed inward of the case 50 by drawing a predetermined position of the side plate 51. And a header lid 62 which is disposed from the outside of the case 50 and defines a closed space 60 between the header body 61 and the header body 61. The header body 61 has a plurality of insertion openings 63 for the heat absorption pipes 52 corresponding to the plurality of heat absorption pipes 52, and the header lid 62 has a single joint portion for the water supply pipe 81 and the connection pipe 83. 64 is provided. The header lid 62 is formed in a shallow vessel shape in which the back side where the joint portion 64 is not provided forms a peripheral wall 65 on the entire periphery. The header lid 62 is fitted in the recess of the header body 61 with the back side of the header lid 62 facing the recess of the header body 61, and brazing is performed with the inner wall of the recess of the header body 61 and the outer surface of the peripheral wall 65 of the header lid 62 overlapped. Thus, the headers 6a and 6b are formed.

流入ヘッダ6aと流出ヘッダ6bとは、ジョイント部64の位置は、流入ヘッダ6aが下側に設けられ、流出ヘッダ6bが上側に設けられている(図2参照)。副熱交換器5を傾けて設置することから、高さ位置は、流入ヘッダ6aの方が低位置に配置されている。   As for the inflow header 6a and the outflow header 6b, the position of the joint part 64 is such that the inflow header 6a is provided on the lower side and the outflow header 6b is provided on the upper side (see FIG. 2). Since the auxiliary heat exchanger 5 is installed at an angle, the height of the inflow header 6a is arranged at a lower position.

さて、背景技術でも述べたとおり、熱交換器の更なる小型化、高熱効率化の要請より、副熱交換器5の吸熱管52の細管化が図られる。本実施形態における副熱交換器5では、吸熱管52の口径をφ10mmとし、8本の吸熱管52を配設する。これにより、限られたスペース内に多くの吸熱管52を配置し、小型化が図られ且つ吸熱管52の伝熱面積が増して高熱効率化を達成している。ところが、吸熱管52を細管化すると、吸熱管52内の水抜きに際して水の表面張力に起因してパイプ端開口52aに水膜が形成され吸熱管52の流水方向下流部に水が残ることがある。そこで、本実施形態では、吸熱管52を細管化しても、水抜きが円滑に行われるようにするため、以下のように構成する。   As described in the background art, the heat absorption pipe 52 of the auxiliary heat exchanger 5 can be made narrower in response to a request for further miniaturization and higher thermal efficiency of the heat exchanger. In the auxiliary heat exchanger 5 in the present embodiment, the diameter of the heat absorption tube 52 is φ10 mm, and eight heat absorption tubes 52 are disposed. Thereby, many heat absorption pipes 52 are arranged in a limited space, the size is reduced, and the heat transfer area of the heat absorption pipes 52 is increased to achieve high thermal efficiency. However, if the endothermic tube 52 is narrowed, a water film is formed in the pipe end opening 52a due to the surface tension of water when water is drained from the endothermic tube 52, and water may remain in the downstream portion of the endothermic tube 52 in the flowing direction. is there. Therefore, in the present embodiment, in order to smoothly drain water even if the heat absorption tube 52 is narrowed, it is configured as follows.

低位置側に配置された流入ヘッダ6aには、パンチングメタルで形成する水抜き板7がパイプ端開口52aに対向してヘッダ本体61内の底部66に配置されている。水抜き板7の多数のパンチ孔75は、パイプ端開口52aよりも小径である。水抜き板7は、吸熱管52の水抜き時にパイプ端開口52aに達した水の水抜き流路を形成させるものである。水抜き板7は、パイプ端開口52aの対向面側に上下方向に延びる凹溝70が2箇所に形成されており、これら凹溝70が上記水抜き流路となる。各凹溝70は、左右位置に4つずつ上下方向に並設された各吸熱管52のパイプ端開口52aに対して連続して対向されている。これら凹溝70の溝幅は、パイプ端開口52aの口径よりも狭く形成されている。例えば、パイプ端開口52aの口径が10mmで、凹溝70の溝幅は、約1mmに設定される。   In the inflow header 6a disposed on the low position side, a drain plate 7 formed of punching metal is disposed on the bottom 66 in the header body 61 so as to face the pipe end opening 52a. Many punch holes 75 of the drain plate 7 have a smaller diameter than the pipe end opening 52a. The drain plate 7 forms a drain channel for the water that has reached the pipe end opening 52 a when draining the heat absorption pipe 52. In the drain plate 7, two concave grooves 70 extending in the vertical direction are formed on the opposite surface side of the pipe end opening 52 a, and these concave grooves 70 serve as the drain channel. Each concave groove 70 is continuously opposed to the pipe end opening 52a of each heat absorption pipe 52 arranged in parallel in the vertical direction by four at the left and right positions. The groove widths of these concave grooves 70 are narrower than the diameter of the pipe end opening 52a. For example, the diameter of the pipe end opening 52a is 10 mm, and the groove width of the groove 70 is set to about 1 mm.

図5を参照して、水抜き板7は、凹溝70を形成させるためのリブ山71が形成され、また、両端のそれぞれにリブ山71の側に曲げられた曲げ部73が形成されている。水抜き板7は、この曲げ部73の先端にヘッダ蓋62の周壁65の上端面が当接され、リブ山71の頂部72がヘッダ蓋62の底面67に当接される大きさに設定されている。水抜き板7は、外形がヘッダ本体61の底部66に略沿った大きさを有する。従って、リブ山71が水抜き板7の強度確保に寄与すると共に、ヘッダ蓋62をヘッダ本体61に嵌め込むとヘッダ蓋62の底面67にリブ山71が当接されて水抜き板7がパイプ端開口52aに接して保持される。水抜き板7の両側の曲げ部73もヘッダ蓋62の周壁65の上端面に当接されて水抜き板7の保持がなされる。このようにして、水抜き板7がパイプ端開口52aに接するように配置されることで、凹溝70の開口部がパイプ端開口52aに当接されている。   Referring to FIG. 5, the drain plate 7 has rib peaks 71 for forming the concave grooves 70, and bent portions 73 bent toward the rib peaks 71 at both ends. Yes. The drainage plate 7 is set to a size such that the upper end surface of the peripheral wall 65 of the header lid 62 is brought into contact with the tip of the bent portion 73 and the top portion 72 of the rib crest 71 is brought into contact with the bottom surface 67 of the header lid 62. ing. The drainage plate 7 has a size such that the outer shape is substantially along the bottom 66 of the header body 61. Therefore, the rib crest 71 contributes to securing the strength of the drain plate 7 and when the header lid 62 is fitted into the header body 61, the rib crest 71 is brought into contact with the bottom surface 67 of the header lid 62 so that the drain plate 7 is connected to the pipe. It is held in contact with the end opening 52a. The bent portions 73 on both sides of the drain plate 7 are also brought into contact with the upper end surface of the peripheral wall 65 of the header lid 62 to hold the drain plate 7. In this way, the drain plate 7 is disposed so as to contact the pipe end opening 52a, so that the opening of the groove 70 is in contact with the pipe end opening 52a.

そして、水抜き作業に際して、給水管81及び出湯管82における水抜き栓(図示せず)を開くと、最初は、吸熱管52の一端部と他端部との高低差により吸熱管52内の水がパイプ端開口52aから円滑に流出される。このとき、水抜き板7は、パンチングメタルで形成されているので、吸熱管52内の水は、パイプ端開口52aから水抜き板7の多数のパンチ孔75を通って排水される。そして、吸熱管52内の水が吸熱管52の流水方向下流部まで抜けると、吸熱管52の高低差による水の水頭圧が小さくなることから、水抜き板7を配しない場合は、水の表面張力に起因してパイプ端開口52aに水膜が形成されて吸熱管52の流水方向下流部に水が残ってしまうことがある。本実施形態では、吸熱管52の流水方向下流部まで水が抜けると、パイプ端開口52aに達した水は、水抜き板7の凹溝70内に進入し凹溝70内に沿って流下されて行く。従って、吸熱管52の流水方向下流部の水は、凹溝70を通じて排水される。   Then, when draining work, when a drain plug (not shown) in the water supply pipe 81 and the hot water discharge pipe 82 is opened, initially, the heat absorption pipe 52 has a difference in height between one end and the other end. Water flows out smoothly from the pipe end opening 52a. At this time, since the drain plate 7 is made of punching metal, the water in the heat absorption pipe 52 is drained from the pipe end opening 52a through the numerous punch holes 75 of the drain plate 7. And if the water in the endothermic pipe 52 passes to the downstream part in the flowing direction of the endothermic pipe 52, the water head pressure due to the difference in height of the endothermic pipe 52 becomes smaller. A water film may be formed in the pipe end opening 52a due to the surface tension, and water may remain in the downstream portion of the heat absorption pipe 52 in the flowing direction. In the present embodiment, when water is drained to the downstream portion in the flowing direction of the heat absorption pipe 52, the water that has reached the pipe end opening 52 a enters the concave groove 70 of the drain plate 7 and flows down along the concave groove 70. Go. Therefore, the water in the downstream portion of the heat absorption pipe 52 in the flowing direction is drained through the concave groove 70.

この排水の原理は、以下のように考えられる。
パイプ端開口52aに達した水は、凹溝70での毛細管現象に基づいて凹溝70内に浸透され、この凹溝70に浸透した水は、その自重と凹溝70での毛細管現象とが相まって凹溝70内に沿って流下されると考えられる。このようにしてパイプ端開口52aに達した水が順次に凹溝70を通じて流されて行くことで、吸熱管52の高低差による水の水頭圧が小さくなっても、パイプ端開口52aには水の表面張力に起因した水膜が形成されることがなく、吸熱管52の流水方向下流部の水は、残らず凹溝70を通じて排水される。
The principle of this drainage is considered as follows.
The water that has reached the pipe end opening 52 a is permeated into the concave groove 70 based on the capillary phenomenon in the concave groove 70, and the water that has permeated the concave groove 70 has its own weight and the capillary phenomenon in the concave groove 70. In combination, it is considered that it flows down along the concave groove 70. In this way, the water that has reached the pipe end opening 52a is sequentially flowed through the concave groove 70, so that even if the water head pressure due to the height difference of the heat absorption pipe 52 is reduced, the pipe end opening 52a has no water. A water film due to the surface tension of the heat absorption pipe 52 is not formed, and water in the downstream portion of the heat absorption pipe 52 in the flowing direction is not drained through the concave groove 70.

従って、吸熱管52の細管化により口径を小さくした場合でも、吸熱管52のパイプ端開口52aでの水の表面張力に起因して吸熱管52の流水方向下流部に水が残されることがなく吸熱管52内の水抜きが確実に行われる。このように、本実施形態における副熱交換器5によれば、吸熱管52の細管化を図った場合でも、パイプ端開口52aに水抜き板7を配置させるといった簡単な構成で吸熱管52の水抜きを確実に行うことができる。従って、水抜き作業を行ったにもかかわらず吸熱管52内に残水が存在して冬季に凍結し吸熱管52を破損させるなどの不具合を起こすこともない。よって、小型化、高効率化を実現すると共に、吸熱管52の水抜きを適切に行える潜熱熱交換器5の提供が可能となる。   Therefore, even when the diameter is reduced by reducing the endothermic tube 52, water does not remain in the downstream portion of the endothermic tube 52 in the flowing direction due to the surface tension of the water at the pipe end opening 52a of the endothermic tube 52. The drainage of the heat absorption pipe 52 is reliably performed. As described above, according to the auxiliary heat exchanger 5 in the present embodiment, even when the heat absorption tube 52 is narrowed, the heat absorption tube 52 can be configured with a simple configuration in which the drainage plate 7 is disposed in the pipe end opening 52a. Water can be drained reliably. Therefore, there is no problem such as remaining water in the endothermic tube 52 in spite of the draining operation, freezing in the winter and damaging the endothermic tube 52. Therefore, it is possible to provide the latent heat exchanger 5 that can achieve downsizing and high efficiency and can appropriately drain the heat absorption pipe 52.

水抜き板7は、パンチングメタルにより構成されているので、水が水抜き板7を円滑に通過することができ、潜熱熱交換器5の通常使用時において流入ヘッダ6aを介した吸熱管52への水の流通を妨げることがなく円滑に行うことができる。なお、水抜き板7は、パンチングメタルで構成するが、これに限らず、エキスパンドメタル、網、メッシュ、フィルター等の種々の水透過部材により構成することができる。また、水抜き板7は、金属板が好適に使用されるが、プラスチック、セラミック等の材質が用いられてもよい。   Since the water drain plate 7 is made of punching metal, water can smoothly pass through the water drain plate 7 and to the heat absorption pipe 52 via the inflow header 6a when the latent heat exchanger 5 is normally used. Can be carried out smoothly without obstructing the flow of water. In addition, although the draining plate 7 is comprised with a punching metal, it can comprise not only this but various water permeable members, such as an expanded metal, a net | network, a mesh, and a filter. Moreover, although the metal plate is used suitably for the water draining plate 7, materials, such as a plastic and a ceramic, may be used.

(他の実施形態)
図6、図7に示すように、他の実施形態では、パンチングメタルより形成された水抜き板7xがパイプ端開口52aと隙間70aを設けるように配置される。この水抜き板7xとパイプ端開口52aとの間の隙間70aは、パイプ端開口52aに水の表面張力に起因して形成される水膜の盛り上がり量以下に設定され、この隙間70aにより吸熱管52内の水抜き時の水抜き流路を形成する。例えば、パイプ端開口52aの口径が10mmで、隙間70aは、約1mmに設定される。
(Other embodiments)
As shown in FIGS. 6 and 7, in another embodiment, a drain plate 7x formed of a punching metal is disposed so as to provide a pipe end opening 52a and a gap 70a. The gap 70a between the drain plate 7x and the pipe end opening 52a is set to be less than the rising amount of the water film formed in the pipe end opening 52a due to the surface tension of water. A drainage flow path is formed at the time of draining in 52. For example, the diameter of the pipe end opening 52a is 10 mm, and the gap 70a is set to about 1 mm.

この水抜き板7xは、幅方向の中央部に上下方向に延びたリブ山71が1つ形成され、このリブ山71の頂部72がヘッダ蓋62の底面67に当接される大きさに設定されている。水抜き板7xの両端のそれぞれには、ヘッダ蓋62の周壁65の上端面が当接されリブ山71の側に曲げられた曲げ部73が形成されている。従って、リブ山71が水抜き板7の強度確保に寄与すると共に、ヘッダ蓋62をヘッダ本体61に嵌め込むとヘッダ蓋62の底面67にリブ山71が当接されて水抜き板7xがパイプ端開口52aに隙間70aを有して保持される。水抜き板7xの両側の曲げ部73もヘッダ蓋62の周壁65の上端面に当接されて水抜き板7xの保持がなされる。   The drain plate 7x is set to a size such that one rib crest 71 extending in the vertical direction is formed at the center in the width direction, and the top 72 of the rib crest 71 is in contact with the bottom surface 67 of the header lid 62. Has been. At both ends of the drainage plate 7x, a bent portion 73 is formed which is brought into contact with the upper end surface of the peripheral wall 65 of the header lid 62 and bent toward the rib crest 71. Therefore, the rib crest 71 contributes to securing the strength of the drain plate 7 and when the header lid 62 is fitted into the header body 61, the rib crest 71 is brought into contact with the bottom surface 67 of the header lid 62 and the drain plate 7x is connected to the pipe. The end opening 52a is held with a gap 70a. The bent portions 73 on both sides of the drain plate 7x are also brought into contact with the upper end surface of the peripheral wall 65 of the header lid 62 to hold the drain plate 7x.

そして、水抜き作業に際して、吸熱管52の流水方向下流部まで水が抜けると、パイプ端開口52aに達した水は、パイプ端開口52aと水抜き板7xとの間の隙間70aに誘導され水抜き板7xに沿って流下されて行く。従って、吸熱管52の流水方向下流部の水は、水抜き板7xに伝って排水される。   When water is drained to the downstream portion of the heat absorption pipe 52 in the direction of water flow, the water that has reached the pipe end opening 52a is guided to the gap 70a between the pipe end opening 52a and the water drain plate 7x. It flows down along the punch plate 7x. Therefore, the water in the downstream portion of the heat absorption pipe 52 in the flowing direction is drained through the drain plate 7x.

つまり、パイプ端開口52aに達した水は、パイプ端開口52aで外方へ盛り上がり水抜き板7xに接するとパイプ端開口52aと水抜き板7との間の隙間70aの毛細管現象によりパイプ端開口52aと水抜き板7xとの間の隙間70aに誘導され、この隙間70aに誘導された水は、その自重と隙間70aの毛細管現象とが相まって水抜き板7xに沿って流下されると考えられる。このようにしてパイプ端開口52aに達した水が順次に水抜き板7xを通じて流されて行くことで、吸熱管52の高低差による水の水頭圧が小さくなっても、パイプ端開口52aには水の表面張力に起因した水膜が形成されることがなく、吸熱管52の流水方向下流部の水は、残らず水抜き板7xを通じて排水される。従って、吸熱管52の細管化により口径を小さくした場合でも、吸熱管52のパイプ端開口52aでの水の表面張力に起因して吸熱管52の流水方向下流部に水が残されることがなく吸熱管52内の水抜きが確実に行われる。図6,図7に示す他の実施形態における上記以外の構成及び作用効果は、図3、図4に示す上記実施形態と同様である。   That is, when the water reaching the pipe end opening 52a rises outward at the pipe end opening 52a and comes into contact with the water drain plate 7x, the pipe end opening is caused by the capillary phenomenon of the gap 70a between the pipe end opening 52a and the water drain plate 7. It is considered that the water guided to the gap 70a between the water drain plate 7x and the water drain plate 7x flows down along the water drain plate 7x in combination with its own weight and the capillary phenomenon of the gap 70a. . Thus, the water that has reached the pipe end opening 52a is sequentially flowed through the drain plate 7x, so that even if the water head pressure due to the height difference of the heat absorption pipe 52 is reduced, the pipe end opening 52a has A water film due to the surface tension of the water is not formed, and the water in the downstream portion of the heat absorption pipe 52 in the flowing direction is not drained through the drain plate 7x. Therefore, even when the diameter is reduced by reducing the endothermic tube 52, water does not remain in the downstream portion of the endothermic tube 52 in the flowing direction due to the surface tension of the water at the pipe end opening 52a of the endothermic tube 52. The drainage of the heat absorption pipe 52 is reliably performed. Other configurations and operational effects of the other embodiments shown in FIGS. 6 and 7 are the same as those of the embodiment shown in FIGS. 3 and 4.

なお、本発明は、上記実施形態のみに限定されず、本発明の範囲内で種々の変更を施すことが可能である。
例えば、吸熱管52は、横置き蛇行形状でなく、渦巻状、螺旋状等に配設されるものでもよい。
また、熱交換器は、給湯装置に限らず、各種の熱交換装置に用いられるものでもよい。
In addition, this invention is not limited only to the said embodiment, A various change is possible within the scope of the present invention.
For example, the endothermic tube 52 may be arranged in a spiral shape, a spiral shape, or the like instead of a horizontal meandering shape.
The heat exchanger is not limited to the hot water supply device, and may be used for various heat exchange devices.

1 給湯装置
2 外装ケース
3 燃焼筐
4 主熱交換器
5 副熱交換器
6a 流入ヘッダ
6b 流出ヘッダ
7,7x 水抜き板
42 吸熱管
50 ケース
51 側板
52 吸熱管
52a パイプ端開口
61 ヘッダ本体
60 閉鎖空間
62 ヘッダ蓋
63 差込口
64 ジョイント部
65 ヘッダ蓋の周壁
66 ヘッダ本体の底部
67 ヘッダ蓋の底面
70 凹溝
70a 隙間
71 リブ山
72 リブ山の頂部
73 曲げ部
DESCRIPTION OF SYMBOLS 1 Hot water supply apparatus 2 Exterior case 3 Combustion housing 4 Main heat exchanger 5 Sub heat exchanger 6a Inflow header 6b Outflow header 7, 7x Drain plate 42 Heat absorption pipe 50 Case 51 Side plate 52 Heat absorption pipe 52a Pipe end opening 61 Header main body 60 Closure Space 62 Header lid 63 Insertion port 64 Joint portion 65 Header cover peripheral wall 66 Header body bottom 67 Header lid bottom surface 70 Groove 70a Clearance 71 Rib crest 72 Rib crest top 73 Bending part

Claims (4)

燃焼排気が流れるケース内に吸熱管を配置し、吸熱管の一端部と他端部とをケースの側板に設けた流入ヘッダと流出ヘッダとに接続して吸熱管内に流す水を燃焼排気により熱交換加熱する熱交換器において、
高さ位置が低位置側に配置されるヘッダには、吸熱管内の水抜き時にパイプ端開口に達した水の水抜き流路を形成させるための水抜き板を、上下方向に並設された複数のパイプ端開口に対して連続して対向配置した熱交換器。
An endothermic tube is arranged in the case through which the combustion exhaust flows, and one end and the other end of the endothermic tube are connected to an inflow header and an outflow header provided on the side plate of the case, and the water flowing in the endothermic tube is heated by the combustion exhaust. In heat exchangers that exchange heat,
On the header whose height position is located on the low position side, a drainage plate is arranged in parallel in the vertical direction to form a drainage channel that reaches the pipe end opening when draining the heat absorption pipe. A heat exchanger arranged continuously opposite to a plurality of pipe end openings.
請求項1に記載の熱交換器において、
上記水抜き流路は、水抜き板に形成された上下方向に延びる凹溝により構成され、
上記凹溝は、パイプ端開口の口径よりも溝幅が狭く且つパイプ端開口に連通されている熱交換器。
The heat exchanger according to claim 1,
The drainage channel is constituted by a concave groove formed in the drainage plate extending in the vertical direction,
The concave groove is a heat exchanger in which the groove width is narrower than the diameter of the pipe end opening and communicates with the pipe end opening.
請求項1に記載の熱交換器において、
上記水抜き流路は、パイプ端開口と水抜き板との間の隙間により構成され、
上記隙間は、パイプ端開口に水の表面張力に起因して形成される水膜の盛り上がり量以下に設定される熱交換器。
The heat exchanger according to claim 1,
The drainage channel is constituted by a gap between the pipe end opening and the drainage plate,
The said clearance gap is a heat exchanger set below the amount of swelling of the water film formed in the pipe end opening resulting from the surface tension of water.
請求項1乃至3のいずれかに記載の熱交換器において、
上記水抜き板は、水透過部材により構成される熱交換器。
The heat exchanger according to any one of claims 1 to 3,
The water drain plate is a heat exchanger composed of a water permeable member.
JP2009016329A 2009-01-28 2009-01-28 Heat exchanger Active JP5030981B2 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011252661A (en) * 2010-06-02 2011-12-15 Rinnai Corp Heat exchanger
JP2015114003A (en) * 2013-12-09 2015-06-22 リンナイ株式会社 Heat exchanger
KR20160050730A (en) * 2014-10-30 2016-05-11 린나이코리아 주식회사 Heat exchanger and method of manufacturing thereof
JP2018031495A (en) * 2016-08-23 2018-03-01 株式会社ノーリツ Heat exchanger and water heater including the same
JP2018031532A (en) * 2016-08-25 2018-03-01 リンナイ株式会社 Heat exchanger and water heater using the same
JP2020176807A (en) * 2019-04-23 2020-10-29 リンナイ株式会社 Heat exchanger and combustion device including the same and drain auxiliary tool

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006177623A (en) * 2004-12-22 2006-07-06 Noritz Corp Water heater
JP2007010178A (en) * 2005-06-28 2007-01-18 Noritz Corp Heat exchanger and water heater comprising the same
JP2007333343A (en) * 2006-06-16 2007-12-27 Noritz Corp Heat exchanger, hot water device provided with same, and water pipe for heat exchanger

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006177623A (en) * 2004-12-22 2006-07-06 Noritz Corp Water heater
JP2007010178A (en) * 2005-06-28 2007-01-18 Noritz Corp Heat exchanger and water heater comprising the same
JP2007333343A (en) * 2006-06-16 2007-12-27 Noritz Corp Heat exchanger, hot water device provided with same, and water pipe for heat exchanger

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011252661A (en) * 2010-06-02 2011-12-15 Rinnai Corp Heat exchanger
JP2015114003A (en) * 2013-12-09 2015-06-22 リンナイ株式会社 Heat exchanger
KR20160050730A (en) * 2014-10-30 2016-05-11 린나이코리아 주식회사 Heat exchanger and method of manufacturing thereof
KR101636950B1 (en) 2014-10-30 2016-07-07 린나이코리아 주식회사 Heat exchanger and method of manufacturing thereof
JP2018031495A (en) * 2016-08-23 2018-03-01 株式会社ノーリツ Heat exchanger and water heater including the same
JP2018031532A (en) * 2016-08-25 2018-03-01 リンナイ株式会社 Heat exchanger and water heater using the same
JP2020176807A (en) * 2019-04-23 2020-10-29 リンナイ株式会社 Heat exchanger and combustion device including the same and drain auxiliary tool
JP7241595B2 (en) 2019-04-23 2023-03-17 リンナイ株式会社 Heat exchanger, combustion device provided with the same, and drain aid

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