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JP4994402B2 - Latent heat exchanger - Google Patents
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JP4994402B2 - Latent heat exchanger - Google Patents

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JP4994402B2
JP4994402B2 JP2009036244A JP2009036244A JP4994402B2 JP 4994402 B2 JP4994402 B2 JP 4994402B2 JP 2009036244 A JP2009036244 A JP 2009036244A JP 2009036244 A JP2009036244 A JP 2009036244A JP 4994402 B2 JP4994402 B2 JP 4994402B2
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heat exchanger
exhaust
latent heat
casing
tube
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大十 榊原
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Rinnai Corp
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Description

本発明は、燃焼排気中に含まれる水蒸気を吸熱管の表面で凝縮させ、その燃焼排気から潜熱を回収する潜熱熱交換器、特に、給湯器や風呂釜等に組み込まれる潜熱熱交換器に関するものである。   The present invention relates to a latent heat exchanger that condenses water vapor contained in combustion exhaust gas on the surface of the heat absorption tube and recovers latent heat from the combustion exhaust gas, and more particularly to a latent heat heat exchanger incorporated in a water heater, a bath tub or the like. It is.

給湯器や風呂釜等に組み込まれる従来の熱交換器において、螺旋状の吸熱管を備えた顕熱回収型の熱交換器が知られている(例えば、特許文献1参照)。   As a conventional heat exchanger incorporated in a water heater, a bath tub, or the like, a sensible heat recovery type heat exchanger having a spiral heat absorption tube is known (for example, see Patent Document 1).

図5は、上記従来の顕熱熱交換器9を備えたガス湯沸器7の概略構成図である。このガス湯沸器7は、外装ケース70下端の開放部から排気するダウンフロー式のガス湯沸器であり、下端が開放する筒状の外装ケース70内に、ガスと空気の混合ガスを燃焼させるバーナ8と、バーナから放出された混合ガスの燃焼排気から顕熱を回収する顕熱熱交換器9とが収容されている。   FIG. 5 is a schematic configuration diagram of a gas water heater 7 provided with the conventional sensible heat exchanger 9. This gas water heater 7 is a downflow type gas water heater that exhausts from an open portion at the lower end of the outer case 70, and a mixed gas of gas and air is combusted in a cylindrical outer case 70 whose lower end is open. A burner 8 to be recovered and a sensible heat exchanger 9 for recovering sensible heat from the combustion exhaust gas of the mixed gas discharged from the burner are accommodated.

顕熱熱交換器9のケーシング90は、下端が開放する筒状に形成されており、このケーシング90内には、バーナ8の外周を覆う上端開放の排気導入筒93が設けられている。また、排気導入筒93の内部空間S1は、上端開放部932を介してケーシング90の内部空間S2へ繋がっており、ケーシング90の内部空間S2は、下端開放部902を介して外装ケース70外へ繋がっている。そして、この排気導入筒93およびケーシング90の各内周面に、燃焼排気から顕熱を回収する吸熱管91が螺旋状に配設されている。   The casing 90 of the sensible heat exchanger 9 is formed in a cylindrical shape whose lower end is opened, and an exhaust introduction cylinder 93 having an open upper end that covers the outer periphery of the burner 8 is provided in the casing 90. Further, the internal space S1 of the exhaust introduction tube 93 is connected to the internal space S2 of the casing 90 via the upper end opening portion 932, and the internal space S2 of the casing 90 is out of the exterior case 70 via the lower end opening portion 902. It is connected. A heat absorption pipe 91 for recovering sensible heat from the combustion exhaust is spirally disposed on the inner peripheral surfaces of the exhaust introduction cylinder 93 and the casing 90.

従って、バーナ8から放出された混合ガスの燃焼排気は、排気導入筒93の内部空間S1を通って上端開放部932へ導かれた後、さらにケーシング90の内部空間S2を通って下端開放部902から外装ケース70外へ放出され、その際、排気導入筒93およびケーシング90の各内周面に設けられた吸熱管91の表面から顕熱が回収される。   Accordingly, the combustion exhaust gas of the mixed gas discharged from the burner 8 is guided to the upper end opening portion 932 through the inner space S1 of the exhaust introduction cylinder 93 and then further passed through the inner space S2 of the casing 90 to the lower end opening portion 902. From the outer casing 70, and at that time, sensible heat is recovered from the surfaces of the heat absorption pipes 91 provided on the inner peripheral surfaces of the exhaust introduction cylinder 93 and the casing 90.

このものでは、吸熱管91が排気導入筒93の内周面からケーシング90の内周面に至る比較的広い範囲に配設されているから、吸熱管91の表面と燃焼排気との接触面積が広く、高い顕熱回収能力を発揮できる。   In this configuration, the heat absorption pipe 91 is disposed in a relatively wide range from the inner peripheral surface of the exhaust introduction cylinder 93 to the inner peripheral surface of the casing 90, so that the contact area between the surface of the heat absorption pipe 91 and the combustion exhaust is small. Wide and high sensible heat recovery capability.

特開昭60−48442号公報JP 60-48442 A 特開昭59−63449号公報JP 59-63449 A

ところで、一般的に、燃焼排気から潜熱を回収する潜熱回収型の熱交換器では、吸熱管の間隙を通過する燃焼排気の流速が低いほど、吸熱管と燃焼排気との接触時間が長くなるから、その分、吸熱管の表面に凝縮し得る水蒸気の量が多くなり、吸熱効率が向上する。
しかしながら、上記従来の顕熱熱交換器9では、吸熱管91が排気導入筒93およびケーシング90の各内周面に沿って螺旋状に設けられており、燃焼排気がその吸熱管91の表面をスムーズに通過する構成であるから、単にこの構成を潜熱回収型の熱交換器に採用しても、吸熱効率の向上が見込めない。
By the way, in general, in a latent heat recovery type heat exchanger that recovers latent heat from combustion exhaust, the lower the flow rate of the combustion exhaust that passes through the gap between the heat absorption tubes, the longer the contact time between the heat absorption tube and the combustion exhaust Accordingly, the amount of water vapor that can be condensed on the surface of the endothermic tube is increased, and the endothermic efficiency is improved.
However, in the conventional sensible heat exchanger 9, the heat absorption pipe 91 is provided in a spiral shape along the inner peripheral surfaces of the exhaust introduction cylinder 93 and the casing 90, and the combustion exhaust covers the surface of the heat absorption pipe 91. Since the structure passes smoothly, even if this structure is simply adopted in a latent heat recovery type heat exchanger, improvement in heat absorption efficiency cannot be expected.

本発明は係る点に鑑みてなされたものであり、吸熱効率の高い潜熱熱交換器を提供することを課題とする。   This invention is made in view of the point which concerns, and makes it a subject to provide a latent heat heat exchanger with high heat absorption efficiency.

本発明に係る潜熱熱交換器は、
底部に排気入口を有するケーシングと、排気入口へ送り込まれたガスの燃焼排気をケーシング内の上域へ導く上下開放の排気導入筒と、排気導入筒を通ってケーシング内へ送り込まれた燃焼排気から潜熱を回収する吸熱管とを備え、
吸熱管は、排気導入筒を中心として渦巻状に形成された複数の渦状部を、上下に層を成して並設した構成であることを特徴とするものである。
The latent heat exchanger according to the present invention is
A casing having an exhaust inlet at the bottom, a vertically open exhaust introduction pipe for guiding the combustion exhaust gas sent to the exhaust inlet to the upper region in the casing, and a combustion exhaust sent into the casing through the exhaust introduction pipe An endothermic tube that collects latent heat,
The endothermic tube is characterized in that a plurality of spiral portions formed in a spiral shape centering on the exhaust introduction tube are arranged side by side in layers.

上記構成によれば、排気導入筒からケーシング内へ導かれた燃焼排気は、上下に層を成して並設された各渦状部の周囲で乱流となり、流速を低下させつつそれら渦状部を通過するから、吸熱管の表面と燃焼排気との接触時間が比較的長くなる。これにより、吸熱管の表面に多くの水蒸気を凝縮させ、潜熱を回収することが可能である。   According to the above configuration, the combustion exhaust led from the exhaust introduction cylinder into the casing becomes a turbulent flow around the spirals arranged in parallel in the upper and lower layers, and the spirals are reduced while reducing the flow velocity. Since it passes, the contact time between the surface of the heat absorption tube and the combustion exhaust becomes relatively long. Thereby, it is possible to condense a lot of water vapor on the surface of the endothermic tube and recover the latent heat.

上記潜熱熱交換器において、所定の間隙をもって排気導入筒の外周を覆い、ケーシング内の上域へ送り込まれた燃焼排気をケーシングの下域へ導く下端開放の筒カバーを備え、
排気導入筒の外周面と筒カバーの内周面とで挟まれた空間内に吸熱管を配設するのが望ましい。
In the latent heat exchanger, the outer periphery of the exhaust introduction cylinder is covered with a predetermined gap, and a lower end open cylinder cover is provided to guide the combustion exhaust sent to the upper area in the casing to the lower area of the casing,
It is desirable to dispose the heat absorption tube in a space sandwiched between the outer peripheral surface of the exhaust introduction cylinder and the inner peripheral surface of the cylinder cover.

吸熱管の表面で多量のドレンが発生し、水膜となって残留した場合には、その管体への熱伝達が妨げられて、吸熱効率を低下させる恐れがある。これに対して、上記構成のものでは、ケーシング内の上域から下域へ流れる燃焼排気によって、吸熱管の表面に付着したドレンの流下が促されるから、その表面に水膜が形成され難い。これにより、安定して高い吸熱効率を発揮できる。   If a large amount of drainage is generated on the surface of the endothermic tube and remains as a water film, heat transfer to the tube may be hindered and the endothermic efficiency may be reduced. On the other hand, in the thing of the said structure, since the flow of the drain which adhered to the surface of the heat absorption pipe | tube is promoted by the combustion exhaust gas flowing from the upper region to the lower region in the casing, it is difficult to form a water film on the surface. Thereby, high heat absorption efficiency can be exhibited stably.

また、上記潜熱熱交換器において、渦状部相互が上下に密接しているのが望ましい。これによれば、吸熱管の表面に付着したドレンがそれら各渦状部の表面を伝って流れ落ち易いから、その表面に水膜が一層形成され難い。これにより、一層安定して高い吸熱効率を発揮できる。   In the latent heat exchanger, it is desirable that the spiral portions are in close contact with each other. According to this, since the drain adhering to the surface of the endothermic tube easily flows down along the surface of each of the spiral portions, it is difficult to form a water film on the surface. Thereby, high heat absorption efficiency can be exhibited more stably.

また、上記潜熱熱交換器において、排気導入筒の周壁を二重構造としたものとしても良い。これによれば、排気導入筒の内周面に燃焼排気中の水蒸気が凝縮し難いから、燃焼排気が吸熱管へ到達するまでの間に、その燃焼排気中の熱が奪われてしまうのを抑制できる。   In the latent heat exchanger, the peripheral wall of the exhaust introduction cylinder may have a double structure. According to this, since the water vapor in the combustion exhaust is difficult to condense on the inner peripheral surface of the exhaust introduction cylinder, the heat in the combustion exhaust is taken away until the combustion exhaust reaches the heat absorption pipe. Can be suppressed.

本発明は、上記構成であるから次の特有の効果を有する。
吸熱管の間隙を通過する燃焼排気の流速を低下させ、吸熱管の表面と燃焼排気との接触時間を長くしたことによって、吸熱管の表面に多くの水蒸気を凝縮させることが可能であるから、吸熱効率が向上する。
Since the present invention has the above configuration, the present invention has the following specific effects.
Because it is possible to condense a lot of water vapor on the surface of the endothermic tube by reducing the flow rate of the combustion exhaust passing through the gap between the endothermic tubes and increasing the contact time between the surface of the endothermic tube and the combustion exhaust, The endothermic efficiency is improved.

本発明の実施の形態に係る潜熱熱交換器を備えた給湯器の概略構成図である。It is a schematic block diagram of the water heater provided with the latent heat exchanger which concerns on embodiment of this invention. 本発明の実施の形態に係る潜熱熱交換器の縦断面概略図である。It is a longitudinal section schematic diagram of a latent heat exchanger concerning an embodiment of the invention. 本発明の実施の形態に係る潜熱熱交換器の吸熱管の分解斜視図である。It is a disassembled perspective view of the heat sink tube of the latent heat exchanger which concerns on embodiment of this invention. 本発明の実施の形態に係る潜熱熱交換器の分解斜視図である。It is a disassembled perspective view of the latent heat exchanger which concerns on embodiment of this invention. 従来の熱交換器を備えた風呂釜の縦断面概略図である。It is a longitudinal cross-sectional schematic diagram of the bathtub provided with the conventional heat exchanger.

次に、上記した本発明を実施するための形態について、添付図面を参照しながら詳述する。
図1は、本発明の実施の形態に係る潜熱熱交換器4を備えた給湯器1であり、主として、ガスと空気の混合ガスを燃焼させるバーナ2と、バーナ2から放出された混合ガスの燃焼排気から顕熱を回収する顕熱熱交換器3と、燃焼排気から潜熱を回収する潜熱熱交換器4と、バーナ2へ器外の空気を送り込む給気ファン5とで構成されている。
Next, embodiments for carrying out the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 shows a water heater 1 provided with a latent heat exchanger 4 according to an embodiment of the present invention, which mainly includes a burner 2 for burning a mixed gas of gas and air, and a mixed gas released from the burner 2. A sensible heat exchanger 3 that recovers sensible heat from the combustion exhaust, a latent heat exchanger 4 that recovers latent heat from the combustion exhaust, and an air supply fan 5 that sends outside air to the burner 2 are configured.

バーナ2は、上端が開放する矩形箱状の燃焼ケース10内に収容されており、給気ファン5から燃焼ケース10内へ送り込まれた空気と、ガス配管LGから送り込まれた燃料ガスとの混合ガスの燃焼排気を、後述する缶体30内へ放出する。   The burner 2 is housed in a rectangular box-like combustion case 10 whose upper end is open, and is a mixture of air sent from the supply fan 5 into the combustion case 10 and fuel gas sent from the gas pipe LG. Gas combustion exhaust is discharged into a can 30 described later.

顕熱熱交換器3は、上下に開放する矩形筒状の缶体30内に、上記燃焼排気から顕熱を回収する吸熱管31を収容したものであり、この缶体30の下端に燃焼ケース10の上端が接続されている。   The sensible heat exchanger 3 has a rectangular tube-shaped can body 30 that opens up and down, and a heat absorption pipe 31 that collects sensible heat from the combustion exhaust. The combustion case is disposed at the lower end of the can body 30. The upper end of 10 is connected.

また、顕熱熱交換器3の吸熱管31の一端には、カランやシャワー等の温水供給先へ繋がる往き配管L2が接続されている一方、他端は、後述する潜熱熱交換器4の吸熱管41の一端側へ繋がっている。   One end of the heat absorption pipe 31 of the sensible heat exchanger 3 is connected to an outgoing pipe L2 connected to a hot water supply destination such as a currant or a shower, and the other end is the heat absorption of the latent heat exchanger 4 described later. It is connected to one end side of the tube 41.

潜熱熱交換器4は、矩形箱状のケーシング40内に、上記燃焼排気から潜熱を回収する吸熱管41を収容したものであり、このケーシング40の底部に缶体30の上端が接続されている。   The latent heat exchanger 4 has a rectangular box-shaped casing 40 in which a heat absorption pipe 41 for recovering latent heat from the combustion exhaust is accommodated, and the upper end of the can 30 is connected to the bottom of the casing 40. .

ケーシング40の底部には、缶体30内を通過した燃焼排気の排気入口401が設けられている一方、ケーシング40の上部には、ケーシング40内を通過した燃焼排気の排気出口402が設けられている。   An exhaust inlet 401 for combustion exhaust gas that has passed through the can 30 is provided at the bottom of the casing 40, while an exhaust outlet 402 for combustion exhaust gas that has passed through the casing 40 is provided at the top of the casing 40. Yes.

また、潜熱熱交換器4の吸熱管41の一端側は、上記顕熱熱交換器3の吸熱管31の一端へ繋がっている一方、他端側には、図示しない給水配管へ繋がる戻り配管L1が接続されている。   One end side of the heat absorption pipe 41 of the latent heat exchanger 4 is connected to one end of the heat absorption pipe 31 of the sensible heat exchanger 3, while the other end side is a return pipe L1 connected to a water supply pipe (not shown). Is connected.

従って、図示しない給水配管から戻り配管L1を通って潜熱熱交換器4の吸熱管41へ送り込まれた水は、燃焼排気の潜熱によって加熱された後、顕熱熱交換器3の吸熱管31へ導かれ、さらに燃焼排気の顕熱によって加熱され、往き配管L2から温水供給先へ送り出される。   Therefore, the water sent from the water supply pipe (not shown) through the return pipe L1 to the heat absorption pipe 41 of the latent heat exchanger 4 is heated by the latent heat of the combustion exhaust gas, and then to the heat absorption pipe 31 of the sensible heat exchanger 3. Further, it is further heated by the sensible heat of the combustion exhaust, and sent out from the forward piping L2 to the hot water supply destination.

潜熱熱交換器4について詳述すると、図2に示すように、ケーシング40の底板42の中央には、ケーシング40内上方へ隆起する断面逆V字状の隆起部420が形成されており、さらにこの隆起部420の頂部には、ケーシング40の内部上域まで延びる筒体(以下、「排気導入筒」という)43が立設されている。尚、上記底板42上面の最下部には、給湯器1に設けられたドレン中和器へ繋がる排水孔(図示しない)が開設されている。   The latent heat exchanger 4 will be described in detail. As shown in FIG. 2, a raised portion 420 having an inverted V-shaped cross section is formed at the center of the bottom plate 42 of the casing 40 and is raised upward in the casing 40. A cylindrical body (hereinafter referred to as “exhaust gas introducing cylinder”) 43 extending up to the upper area inside the casing 40 is provided upright on the top of the raised portion 420. In addition, a drainage hole (not shown) connected to a drain neutralizer provided in the water heater 1 is opened at the bottom of the upper surface of the bottom plate 42.

また、底板42の裏面は、中央部に上記隆起部420と略同一形状の隆起部440を有する底カバー44で覆われており、その底板42と底カバー44との間に空気の層が形成されている。   The back surface of the bottom plate 42 is covered with a bottom cover 44 having a raised portion 440 having substantially the same shape as the raised portion 420 at the center, and an air layer is formed between the bottom plate 42 and the bottom cover 44. Has been.

一方、排気導入筒43の内周面は、上下に開放する内筒45で覆われており、その排気導入筒43と内筒45との間に空気の層が形成されている。尚、内筒45の下端開放部451は、底カバー44の隆起部440の頂部を貫通してケーシング40の下方へ臨んでおり、この下端開放部451が上述した排気入口401に相当する。   On the other hand, the inner peripheral surface of the exhaust introduction cylinder 43 is covered with an inner cylinder 45 that opens up and down, and an air layer is formed between the exhaust introduction cylinder 43 and the inner cylinder 45. The lower end opening portion 451 of the inner cylinder 45 passes through the top of the raised portion 440 of the bottom cover 44 and faces the casing 40, and the lower end opening portion 451 corresponds to the exhaust inlet 401 described above.

ケーシング40内には、排気導入筒43の上端から外周にかけて覆う下端開放箱状の筒カバー46が設けられており、吸熱管41は、この筒カバー46の内周面と排気導入筒43の外周面とで挟まれた空間(以下、「吸熱室」という)S2内に収容されている。   In the casing 40, a lower end open box-shaped tube cover 46 is provided to cover from the upper end to the outer periphery of the exhaust introduction tube 43, and the heat absorption tube 41 includes an inner peripheral surface of the tube cover 46 and an outer periphery of the exhaust introduction tube 43. It is accommodated in a space (hereinafter referred to as “endothermic chamber”) S2 sandwiched between the surfaces.

筒カバー46の内側上面の中央部には、断面逆V字状の凹部460が形成されており、内筒45の内部空間(以下「排気導入路」という)S1は、この凹部460下方の空間を介して吸熱室S2の上域へ繋がっている。   A concave portion 460 having an inverted V-shaped cross section is formed at the center of the inner upper surface of the tube cover 46, and an internal space (hereinafter referred to as “exhaust introduction path”) S <b> 1 of the inner tube 45 is a space below the concave portion 460. Is connected to the upper region of the endothermic chamber S2.

また、筒カバー46の下端開放部462は、上記隆起部420の傾斜面R2の上方位置にあり、吸熱室S2は、この隆起部420上方の空間を介して筒カバー46の外周面とケーシング40の内周面とで囲まれた空間(以下、「排気導出路」という)S3の下域へ繋がっている。   The lower end opening 462 of the tube cover 46 is located above the inclined surface R2 of the raised portion 420, and the heat absorption chamber S2 is connected to the outer peripheral surface of the tube cover 46 and the casing 40 via the space above the raised portion 420. Is connected to a lower area of a space (hereinafter referred to as “exhaust lead-out path”) S3 surrounded by the inner peripheral surface.

さらに、ケーシング40の天板47の中央上部には、そのケーシング40内の空気を器外へ排出するための排気筒48が立設されている。排気筒48の下端開放部481は、上記凹部460の裏面側(筒カバー46の上面側)に形成された傾斜面R3の上方位置にあり、排気導出路S3は、この凹部460裏面の空間から排気筒48の内部空間を介して器外へ繋がっている。   Further, an exhaust cylinder 48 for discharging the air in the casing 40 to the outside of the container is provided upright at the center upper portion of the top plate 47 of the casing 40. The lower end opening 481 of the exhaust cylinder 48 is located above the inclined surface R3 formed on the back surface side of the recess 460 (upper surface side of the tube cover 46), and the exhaust lead-out path S3 extends from the space on the back surface of the recess 460. The exhaust pipe 48 is connected to the outside through the internal space.

従って、バーナ2から缶体30内へ放出された混合ガスの燃焼排気は、底カバー44の隆起部440の裏面に沿って排気入口401へ導かれ、排気導入路S1内を上昇する。そして、内筒45の上方へ送り出された燃焼排気は、凹部460の傾斜面R1に沿って燃焼室S2の上域へ導かれ、吸熱管41の間隙を通って燃焼室S2内を降下する。その際、吸熱管41の表面では燃焼排気中の水蒸気が凝縮し、潜熱が回収される。   Therefore, the combustion exhaust gas of the mixed gas discharged from the burner 2 into the can 30 is guided to the exhaust inlet 401 along the back surface of the raised portion 440 of the bottom cover 44 and ascends in the exhaust introduction path S1. Then, the combustion exhaust sent to the upper side of the inner cylinder 45 is guided to the upper region of the combustion chamber S2 along the inclined surface R1 of the recess 460 and descends in the combustion chamber S2 through the gap of the heat absorption pipe 41. At this time, water vapor in the combustion exhaust is condensed on the surface of the heat absorption pipe 41, and latent heat is recovered.

さらに、筒カバー46の下方へ送り出された燃焼排気は、隆起部420の傾斜面R2に沿って排気導出路S3の下域へ導かれ、排気導出路S3を上昇する。そして、凹部460裏面の傾斜面R3に沿って排気筒48内へ導かれ、器外上方へ排出される。   Further, the combustion exhaust sent to the lower side of the tube cover 46 is guided to the lower region of the exhaust lead-out path S3 along the inclined surface R2 of the raised portion 420, and ascends the exhaust lead-out path S3. And it guide | induces into the exhaust pipe 48 along the inclined surface R3 of the back surface of the recessed part 460, and is discharged | emitted upwards outside the container.

一方、吸熱管41の表面で凝縮した強酸性のドレンは、隆起部420の傾斜面R2へ滴下し、その傾斜面R2を伝って図示しない排水孔からドレン中和器へ回収される。   On the other hand, the strongly acidic drain condensed on the surface of the endothermic tube 41 is dropped onto the inclined surface R2 of the raised portion 420, and is collected to the drain neutralizer through the inclined surface R2 through a drain hole (not shown).

図3に示すように、吸熱管41は、一本の蛇腹管を用いて、排気導入筒43を中心として同一平面上で外側から内側へ巻回して第一の渦状部411を形成し、さらに一段上がった同一平面上で内側から外側へ巻回して第二の渦状部412を形成した渦状管体410を、上下に複数(ここでは、四つ)重ね合わせて構成されている。   As shown in FIG. 3, the endothermic tube 41 uses a single bellows tube and is wound from the outside to the inside on the same plane around the exhaust introduction tube 43 to form the first spiral portion 411. A plurality of (in this case, four) spiral tubes 410, which are wound from the inside to the outside on the same plane that has been raised one step to form the second spiral portion 412, are configured to overlap each other.

また、上記渦状管体410の各渦状部411,412は、横方向に所定の間隔(例えば、1mm)を有しているとともに、それら各渦状部411,412相互は、上下に密接した状態で層を成して並設されている(図2参照)。   Further, the spiral portions 411 and 412 of the spiral tube 410 have a predetermined interval (for example, 1 mm) in the lateral direction, and the spiral portions 411 and 412 are in close contact with each other. They are arranged side by side (see FIG. 2).

従って、吸熱室S2内へ導かれた燃焼排気は、上記各渦状部411,412の周囲で乱流となり、流速を低下させつつ渦状部411,412を通過し、排気導出路S3側へ送り出される。   Accordingly, the combustion exhaust gas introduced into the heat absorption chamber S2 becomes turbulent around the spiral portions 411 and 412, passes through the spiral portions 411 and 412 while reducing the flow velocity, and is sent to the exhaust lead-out path S3 side. .

また、図4に示すように、ケーシング40の側壁400には、複数の吸熱管接続口40a,40bが開設されており、渦状管体410の各入水側管端41aおよび出水側管端41bは、上記側壁400の内側面からこの吸熱管接続口40a,40bに接続固定されている。   As shown in FIG. 4, a plurality of heat absorption pipe connection ports 40 a and 40 b are formed in the side wall 400 of the casing 40, and each water inlet side pipe end 41 a and water outlet side pipe end 41 b of the spiral tube 410 are The heat absorption pipe connection ports 40 a and 40 b are connected and fixed from the inner side surface of the side wall 400.

さらに、上記側壁400の外側面には、入水側の吸熱管接続口40aを覆う入水ヘッダ49Aと、出水側の吸熱管接続口40bを覆う出水ヘッダ49Bが接続されており、各渦状管体410の入水側管端41aは、この入水ヘッダ49Aを介して戻り配管L1へ繋がり、出水側管端41bは、出水ヘッダ49Bを介して顕熱熱交換器3の吸熱管31へ繋がっている。   Furthermore, a water inlet header 49A covering the water inlet side heat absorbing pipe connection port 40a and a water outlet header 49B covering the water outlet side heat absorbing pipe connection port 40b are connected to the outer surface of the side wall 400. The water inlet side pipe end 41a is connected to the return pipe L1 via the water inlet header 49A, and the water outlet side pipe end 41b is connected to the heat absorption pipe 31 of the sensible heat exchanger 3 via the water outlet header 49B.

従って、戻り配管L1を通って入水ヘッダ49Aへ送り込まれた水は、入水ヘッダ49A内で各入水側管端41aへ分散され、渦状管体410内へ並列的に流れ込む。その際、渦状管体410内へ送り込まれた水は、その下段外側から中心へ向かって渦巻状に流れた後、さらに上段内側から外側へ向かって流れ、各出水側管端41bから出水ヘッダ49Bへ送り出される。そして、出水ヘッダ49B内で集約され、顕熱熱交換器3の吸熱管31へ至る。   Accordingly, the water sent to the incoming water header 49A through the return pipe L1 is dispersed to each incoming water side pipe end 41a in the incoming water header 49A and flows into the spiral tube 410 in parallel. At that time, the water fed into the spiral tube 410 flows spirally from the lower outer side to the center, and further flows from the upper inner side to the outer side, and flows out from each outlet side pipe end 41b to the outlet header 49B. Sent out. And it collects in the outflow header 49B and reaches the heat absorption pipe 31 of the sensible heat exchanger 3.

このものでは、渦状管体410の各渦状部411,412を吸熱室S2内で層を成して並設したことによって、吸熱室S2内へ導かれた燃焼排気は、各渦状部411,412の周囲で乱流となってその流速を低下させつつ、渦状部411,412を通過するから、吸熱管41の表面と燃焼排気との接触時間が比較的長くなる。その結果、吸熱管41の表面に多くの水蒸気が凝縮し、潜熱が回収される。これにより、吸熱効率が向上する。   In this configuration, by arranging the spiral portions 411 and 412 of the spiral tube body 410 in layers in the endothermic chamber S2, the combustion exhaust introduced into the endothermic chamber S2 is converted into the respective spiral portions 411 and 412. Since it passes through the spiral portions 411 and 412 while reducing the flow velocity as a turbulent flow around, the contact time between the surface of the heat absorption tube 41 and the combustion exhaust gas becomes relatively long. As a result, a large amount of water vapor is condensed on the surface of the heat absorption tube 41, and latent heat is recovered. Thereby, endothermic efficiency improves.

一方、吸熱管41の表面で多量のドレンが発生し、水膜となって残留した場合には、各渦状部411,412への熱伝達が妨げられ、吸熱効率を低下させる恐れがあるが、このものでは、吸熱室S2内に吸熱管41を設けたことによって、燃焼排気の下向きの流れが吸熱管41の表面に付着したドレンの流下を促すから、渦状部411,412の表面に水膜が形成され難い。これにより、安定して高い吸熱効率を発揮できる。   On the other hand, when a large amount of drainage is generated on the surface of the heat absorption tube 41 and remains as a water film, heat transfer to each of the spiral portions 411 and 412 may be hindered, which may reduce the heat absorption efficiency. In this case, since the endothermic tube 41 is provided in the endothermic chamber S2, the downward flow of the combustion exhaust promotes the flow of the drain adhering to the surface of the endothermic tube 41. Therefore, a water film is formed on the surfaces of the spiral portions 411 and 412. Is difficult to form. Thereby, high heat absorption efficiency can be exhibited stably.

尚、顕熱熱交換器3の吸熱管31は、銅材で形成されており、強酸性のドレンが付着すればその表面が腐食する恐れがあるが、このものでは、潜熱熱交換器4の吸熱管41を吸熱室S2内に設けたことによって、吸熱管41の表面に付着したドレンは、顕熱熱交換器3側へ滴下しない。これにより、ドレンによる顕熱熱交換器3の吸熱管31の腐食を防止できる。   The endothermic tube 31 of the sensible heat exchanger 3 is made of a copper material, and the surface of the heat absorption pipe 31 may corrode if strongly acidic drain adheres. By providing the endothermic tube 41 in the endothermic chamber S2, the drain adhering to the surface of the endothermic tube 41 does not drop to the sensible heat exchanger 3 side. Thereby, corrosion of the heat absorption pipe | tube 31 of the sensible heat exchanger 3 by a drain can be prevented.

さらに、渦状管体410相互が上下に密接した状態で重なり合っており、吸熱管41の表面に付着したドレンがそれら各渦状管体410の表面を伝って流れ落ち易いから、それら表面に水膜が一層形成され難い。これにより、一層安定して高い吸熱効率を発揮できる。   Further, since the spiral tube bodies 410 are overlapped with each other in close contact with each other, the drain adhering to the surface of the endothermic tube 41 easily flows down along the surface of each of the spiral tube bodies 410, so that a water film is further formed on the surfaces. It is difficult to form. Thereby, high heat absorption efficiency can be exhibited more stably.

また、底板42の裏面および排気導入筒43の内周面を二重構造にしたことによって、底カバー44の裏面や内筒45の内周面に燃焼排気中の水蒸気が凝縮し難いから、燃焼排気が吸熱管41へ到達するまでの間に、その燃焼排気中の熱が奪われてしまうのを抑制できる。これにより、吸熱効率が一層向上する。   Further, since the back surface of the bottom plate 42 and the inner peripheral surface of the exhaust introduction cylinder 43 have a double structure, water vapor in the combustion exhaust gas is unlikely to condense on the rear surface of the bottom cover 44 and the inner peripheral surface of the inner cylinder 45. It is possible to prevent the heat in the combustion exhaust from being taken away until the exhaust reaches the heat absorption pipe 41. Thereby, the endothermic efficiency is further improved.

さらに、底板42の裏面および排気導入筒43の内周面を二重構造にしたことによって、底カバー44の裏面や内筒45の内周面にドレンが付着し難いから、それら表面から顕熱熱交換器3側へドレンが滴下し難い。これにより、ドレンによる顕熱熱交換器3の吸熱管31の腐食を一層効果的に防止できる。   Furthermore, since the back surface of the bottom plate 42 and the inner peripheral surface of the exhaust introduction cylinder 43 have a double structure, it is difficult for the drain to adhere to the rear surface of the bottom cover 44 and the inner peripheral surface of the inner cylinder 45. It is difficult for the drain to drip to the heat exchanger 3 side. Thereby, corrosion of the heat absorption pipe | tube 31 of the sensible heat exchanger 3 by a drain can be prevented much more effectively.

また、吸熱管41を吸熱室S2内へ渦巻状に配設したことによって、潜熱熱交換器4全体の大きさを比較的コンパクトに構成できるから、潜熱回収型の給湯器1の小型化を図ることが可能である。   Further, since the endothermic pipe 41 is spirally arranged in the endothermic chamber S2, the overall size of the latent heat exchanger 4 can be made relatively compact, so that the latent heat recovery type water heater 1 can be downsized. It is possible.

また、複数の渦状管体410を重ね合わせて一つの吸熱管41を構成したことによって、ケーシング40内に組み込む渦状管体410の数を増減させるだけで、給湯器1の性能に合わせた潜熱熱交換器4を製造できる。   In addition, by forming a single heat absorption tube 41 by superimposing a plurality of spiral tubes 410, the latent heat heat that matches the performance of the water heater 1 can be obtained simply by increasing or decreasing the number of spiral tubes 410 incorporated in the casing 40. The exchanger 4 can be manufactured.

尚、上記実施の形態では、戻り配管L1から送り込まれた水が、各渦状管体410を並列的に流れて顕熱熱交換器3の吸熱管31へ送り出されるように構成されているが、各渦状管体410を直列的に接続し、戻り配管L1から一つの渦状管体410へ送り込まれた水が他の渦状管体410を順に流れた後、顕熱熱交換器3の吸熱管31へ送り出されるように構成しても良い。   In the above embodiment, the water sent from the return pipe L1 is configured to flow in parallel to the spiral tubes 410 and to the heat absorption pipe 31 of the sensible heat exchanger 3. Each spiral tube 410 is connected in series, and water sent from the return pipe L1 to one spiral tube 410 sequentially flows through the other spiral tube 410, and then the endothermic tube 31 of the sensible heat exchanger 3. You may comprise so that it may be sent out.

また、上記実施の形態では、本発明に係る潜熱熱交換器を給湯器1に組み込んだものを例示的に説明したが、本発明に係る潜熱熱交換器は、ガス湯沸器や風呂釜にも適用できる。   In the above embodiment, the latent heat exchanger according to the present invention incorporated in the water heater 1 has been exemplarily described. However, the latent heat exchanger according to the present invention can be used in a gas water heater or a bathtub. Is also applicable.

1・・・給湯器
2・・・バーナ
3・・・顕熱熱交換器
4・・・潜熱熱交換器
40・・・ケーシング
401・・・排気入口
41・・・吸熱管
410・・・渦状管体
411,412・・・渦状部
43・・・排気導入筒
DESCRIPTION OF SYMBOLS 1 ... Hot water heater 2 ... Burner 3 ... Sensible heat exchanger 4 ... Latent heat exchanger 40 ... Casing 401 ... Exhaust inlet 41 ... Heat absorption pipe 410 ... Spiral shape Tube bodies 411, 412 ... spiral portion 43 ... exhaust introduction cylinder

Claims (4)

底部に排気入口を有するケーシングと、排気入口へ送り込まれたガスの燃焼排気をケーシング内の上域へ導く上下開放の排気導入筒と、排気導入筒を通ってケーシング内へ送り込まれた燃焼排気から潜熱を回収する吸熱管とを備え、
吸熱管は、排気導入筒を中心として渦巻状に形成された複数の渦状部を、上下に層を成して並設した構成であることを特徴とする、潜熱熱交換器。
A casing having an exhaust inlet at the bottom, a vertically open exhaust introduction pipe for guiding the combustion exhaust gas sent to the exhaust inlet to the upper region in the casing, and a combustion exhaust sent into the casing through the exhaust introduction pipe An endothermic tube that collects latent heat,
The heat absorption pipe has a configuration in which a plurality of spiral portions formed in a spiral shape with the exhaust introduction cylinder as a center are arranged in parallel in a vertical layer.
請求項1に記載の潜熱熱交換器において、
所定の間隙をもって排気導入筒の外周を覆い、ケーシング内の上域へ送り込まれた燃焼排気をケーシングの下域へ導く下端開放の筒カバーを備え、
排気導入筒の外周面と筒カバーの内周面とで挟まれた空間内に前記吸熱管を配設したことを特徴とする、潜熱熱交換器。
The latent heat exchanger according to claim 1,
Covering the outer periphery of the exhaust introduction cylinder with a predetermined gap, and provided with a lower end open cylinder cover that guides the combustion exhaust sent to the upper area in the casing to the lower area of the casing,
A latent heat heat exchanger, wherein the heat absorption pipe is disposed in a space sandwiched between an outer peripheral surface of the exhaust introduction cylinder and an inner peripheral surface of the cylinder cover.
請求項1または2に記載の潜熱熱交換器において、
渦状部相互が上下に密接していることを特徴とする、潜熱熱交換器。
The latent heat exchanger according to claim 1 or 2,
A latent heat exchanger, characterized in that the vortex portions are in close contact with each other vertically.
請求項1から3のいずれかに記載の潜熱熱交換器において、
排気導入筒の周壁を二重構造としたことを特徴とする、潜熱熱交換器。
The latent heat exchanger according to any one of claims 1 to 3,
A latent heat heat exchanger characterized in that the peripheral wall of the exhaust introduction cylinder has a double structure.
JP2009036244A 2009-02-19 2009-02-19 Latent heat exchanger Expired - Fee Related JP4994402B2 (en)

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