JPH10103784A - Combustion device - Google Patents
Combustion deviceInfo
- Publication number
- JPH10103784A JPH10103784A JP28011996A JP28011996A JPH10103784A JP H10103784 A JPH10103784 A JP H10103784A JP 28011996 A JP28011996 A JP 28011996A JP 28011996 A JP28011996 A JP 28011996A JP H10103784 A JPH10103784 A JP H10103784A
- Authority
- JP
- Japan
- Prior art keywords
- water
- heat exchanger
- heated
- main heat
- supply
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Details Of Fluid Heaters (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は給湯機などの燃焼装
置に関し、特に燃焼ガスの潜熱を利用して熱効率の向上
を図った燃焼装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion apparatus such as a water heater, and more particularly, to a combustion apparatus in which latent heat of combustion gas is used to improve thermal efficiency.
【0002】[0002]
【従来の技術】従来から熱交換器の熱効率を向上するた
めに燃焼ガスの潜熱を利用する方法があり、例えば特公
昭62−2671号公報に記載されているものは、ガス
バーナとその真上の燃焼ガス流路の上流と下流に2つの
熱交換器を設け、下流側の補助熱交換器から上流側の主
熱交換器に直列に通水する構成となっている。2. Description of the Related Art Conventionally, there has been a method of utilizing the latent heat of a combustion gas to improve the heat efficiency of a heat exchanger. Two heat exchangers are provided upstream and downstream of the combustion gas flow path, and water is passed in series from the downstream auxiliary heat exchanger to the upstream main heat exchanger.
【0003】[0003]
【本発明が解決しようとする課題】ところが、上記従来
のように2つの熱交換器に対して直列に通水する構成と
すると、熱効率を低下させることなく補助熱交換器を小
型化し、燃焼装置全体の小型化を図るために補助熱交換
器を構成する水管の径を細くして、それら水管を密に配
置する、例えば主熱交換器の水管径を20mm、補助熱
交換器の水管径を10mmとすると、水管の細径化によ
り通水抵抗が増加するために十分な出湯量が得られない
という問題点がある。However, if water is passed in series to the two heat exchangers as in the prior art described above, the size of the auxiliary heat exchanger can be reduced without lowering the thermal efficiency and the combustion apparatus can be reduced. In order to reduce the overall size, the diameter of the water tubes constituting the auxiliary heat exchanger is reduced, and the water tubes are densely arranged. For example, the water pipe diameter of the main heat exchanger is 20 mm, and the water tubes of the auxiliary heat exchanger are When the diameter is 10 mm, there is a problem that a sufficient tapping amount cannot be obtained because the water flow resistance increases due to the reduction in the diameter of the water pipe.
【0004】そこで本発明は、上記従来の問題を解消
し、熱交換器をできるだけ小さくしても、効率よく熱交
換を行い、十分な出湯量を得ることができる燃焼装置の
提供を目的とする。Accordingly, an object of the present invention is to solve the above-mentioned conventional problems and to provide a combustion apparatus capable of efficiently performing heat exchange and obtaining a sufficient amount of hot water even if the heat exchanger is made as small as possible. .
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
に、請求項1の燃焼装置は、主熱交換器と補助熱交換器
とバーナとを備えた燃焼装置であって、主熱交換器への
給水管を分岐し、補助熱交換器に至る分岐管を設け、前
記分岐管は補助熱交換器を経てその終端が前記給水管と
の分岐部より下流側かつ主熱交換器より上流側に接続さ
れたことを特徴としている。さらに請求項2の燃焼装置
は、主熱交換器と補助熱交換器とバーナとを備えた燃焼
装置であって、少なくとも補助熱交換器へ至るまでは給
水管に被加熱部分を設けないことを特徴としている。According to one aspect of the present invention, there is provided a combustion apparatus including a main heat exchanger, an auxiliary heat exchanger, and a burner. A water supply pipe to the water supply pipe, and a branch pipe to an auxiliary heat exchanger is provided.The branch pipe passes through the auxiliary heat exchanger, and the end thereof is located downstream of the branch with the water supply pipe and upstream of the main heat exchanger. It is characterized by being connected to. Further, the combustion device according to claim 2 is a combustion device provided with a main heat exchanger, an auxiliary heat exchanger, and a burner, wherein at least the auxiliary water exchanger is not provided with a heated portion in a water supply pipe. Features.
【0006】請求項1の燃焼装置において、供給水は分
岐した入水回路から主熱交換器と補助熱交換器とに通水
される。補助熱交換器で加熱された温水は補助熱交換器
から出た後、主熱交換器に供給される水と合流して主熱
交換器に入り、再び加熱されて出湯される。したがって
補助熱交換器を構成する水管の径を細くしても全体の通
水抵抗が大きくなることはない。さらに請求項2の燃焼
装置においては、補助熱交換器に供給される水は補助熱
交換器に至るまでは加熱されないので、温度の低いまま
補助熱交換器に通水される。通水温度が低いほどバーナ
からの燃焼ガスとの温度差が大きくなり、効率よく熱交
換を行うことができる。[0006] In the combustion apparatus of the first aspect, the supply water is passed from the branched water inlet circuit to the main heat exchanger and the auxiliary heat exchanger. The hot water heated by the auxiliary heat exchanger exits the auxiliary heat exchanger, merges with the water supplied to the main heat exchanger, enters the main heat exchanger, is heated again, and is heated. Therefore, even if the diameter of the water pipe constituting the auxiliary heat exchanger is reduced, the overall water flow resistance does not increase. Further, in the combustion apparatus according to the second aspect, since the water supplied to the auxiliary heat exchanger is not heated until reaching the auxiliary heat exchanger, the water is passed through the auxiliary heat exchanger at a low temperature. The lower the passing water temperature, the greater the temperature difference from the combustion gas from the burner, and the more efficient the heat exchange.
【0007】[0007]
【発明の実施形態】図1は本発明の第1の実施形態を示
す燃焼装置の側断面図、図2は本発明の第2の実施形態
を示す燃焼装置の側断面図である。FIG. 1 is a side sectional view of a combustion apparatus showing a first embodiment of the present invention, and FIG. 2 is a side sectional view of a combustion apparatus showing a second embodiment of the present invention.
【0008】図1において、第1の実施形態における燃
焼装置は、バーナ1の上方の排ガス流路7の上流側に主
熱交換器2、下流側に補助熱交換器4をドレン受け6を
挟んで配置している。補助熱交換器4を構成する水管5
の径は主熱交換器2を構成する水管3の径より細く、例
えば水管3の径は20mm、水管5の径は10mmと
し、水管5を密に配置することで補助熱交換器4を小型
化することができる。供給水は図示しない給水管から分
岐され、水管3と水管5とに通水される。水管5に入っ
た供給水は補助熱交換器4で加熱された後、給水管の分
岐部より下流側かつ主熱交換器2より上流側において、
主熱交換器2へ供給される水と合流し、主熱交換器2で
加熱された後、図示しない給湯管から出湯される。ま
た、水管3と水管5とに通水された供給水は、主熱交換
器2で高温の排ガスによって加熱される一方、補助熱交
換器4では主熱交換器2において加熱作用した後の排ガ
スによって、すなわち排熱を利用して加熱される。In FIG. 1, the combustion apparatus according to the first embodiment has a main heat exchanger 2 upstream of an exhaust gas flow path 7 above a burner 1 and an auxiliary heat exchanger 4 downstream of a drain receiver 6. It is arranged in. Water tube 5 constituting auxiliary heat exchanger 4
Is smaller than the diameter of the water tube 3 constituting the main heat exchanger 2, for example, the diameter of the water tube 3 is 20 mm, the diameter of the water tube 5 is 10 mm, and the auxiliary heat exchanger 4 is compact by disposing the water tubes 5 densely. Can be The supply water is branched from a water supply pipe (not shown), and flows through the water pipes 3 and 5. After the supply water entering the water pipe 5 is heated by the auxiliary heat exchanger 4, on the downstream side of the branch of the water supply pipe and upstream of the main heat exchanger 2,
After joining with the water supplied to the main heat exchanger 2 and being heated by the main heat exchanger 2, the hot water is discharged from a hot water supply pipe (not shown). The supply water passed through the water pipe 3 and the water pipe 5 is heated by the high-temperature exhaust gas in the main heat exchanger 2, while the auxiliary heat exchanger 4 is heated by the main heat exchanger 2. , That is, using the exhaust heat.
【0009】図2において、第2の実施形態における燃
焼装置は、バーナ1の上方の排ガス流路7の上流側に主
熱交換器2、下流側に補助熱交換器4をドレン受け6を
挟んで配置している。補助熱交換器4を構成する水管5
の径は主熱交換器2を構成する水管3の径より細く、例
えば水管3の径は20mm、水管5の径は10mmとな
っており、水管5を密に配置することで補助熱交換器4
を小型化することができる。供給水は給水管の分岐部で
分岐し、一方は加熱されないまま補助熱交換器4の水管
5に通水され、他方は排ガス流路外壁9の周囲に旋回し
て配設された水管10に通水され、給水管の分岐部より
下流側かつ主熱交換器2より上流側において双方が再び
合流して主熱交換器2の水管3に至る。また、水管3と
水管5とに通水された供給水は、主熱交換器2で高温の
排ガスによって加熱される一方、補助熱交換器4では主
熱交換器2において加熱作用した後の排ガスによって、
すなわち排熱を利用して加熱され、図示しない給湯管か
ら出湯される。なお、高温の燃焼ガスで加熱された排ガ
ス流路外壁9は、その周囲に旋回して配設された水管1
0へ通水された供給水により冷却される。言い換える
と、給水管から分岐して水管10に通水された供給水は
主熱交換器2に供給される前に加熱されることになる
が、補助熱交換器4へ供給される前の供給水は何ら加熱
されることはない。In FIG. 2, the combustion apparatus according to the second embodiment has a main heat exchanger 2 upstream of an exhaust gas flow path 7 above a burner 1 and an auxiliary heat exchanger 4 downstream of a drain receiver 6. It is arranged in. Water tube 5 constituting auxiliary heat exchanger 4
Is smaller than the diameter of the water pipe 3 constituting the main heat exchanger 2, for example, the diameter of the water pipe 3 is 20 mm and the diameter of the water pipe 5 is 10 mm. 4
Can be reduced in size. The supply water branches at the branch of the water supply pipe, one of which is passed through the water pipe 5 of the auxiliary heat exchanger 4 without being heated, and the other of which is supplied to the water pipe 10 which is swirled around the outer wall 9 of the exhaust gas passage. Water is passed, and the two join again again downstream of the branch of the water supply pipe and upstream of the main heat exchanger 2 to reach the water pipe 3 of the main heat exchanger 2. The supply water passed through the water pipe 3 and the water pipe 5 is heated by the high-temperature exhaust gas in the main heat exchanger 2, while the auxiliary heat exchanger 4 is heated by the main heat exchanger 2. By
That is, the hot water is heated by using the exhaust heat and is discharged from a hot water supply pipe (not shown). The outer wall 9 of the exhaust gas passage heated by the high-temperature combustion gas is provided around the water pipe 1 which is swirled around it.
It is cooled by the supply water that has been passed through to zero. In other words, the supply water branched from the water supply pipe and passed through the water pipe 10 is heated before being supplied to the main heat exchanger 2, but is supplied before being supplied to the auxiliary heat exchanger 4 The water is not heated at all.
【0010】補助熱交換器4で排熱を利用して水を加熱
すると、排ガス中の水分が凝縮することによってドレン
が生じる。このドレンは強い酸性であり、そのまま排水
すると排水経路や構造物が腐食される恐れがあるため、
ドレン受け6で回収した後に中和装置8で中和処理され
る。When water is heated using the exhaust heat in the auxiliary heat exchanger 4, the water in the exhaust gas is condensed to generate drain. This drain is strongly acidic, and if drained as it is, the drainage channels and structures may be corroded.
After being collected by the drain receiver 6, it is neutralized by the neutralizer 8.
【0011】通水量は、第1、第2の実施形態とも任意
であり、例えば水管3と水管5に8:2の割合で通水
し、補助熱交換器4で加熱された温水が主熱交換器2に
供給される前の水と合流し、主熱交換器2で加熱された
後、図示しない給湯管から出湯されるので補助熱交換器
4を構成する水管5を細径化しても全体としては通水抵
抗の増加はない。The amount of water passing is arbitrary in both the first and second embodiments. For example, hot water heated by the auxiliary heat exchanger 4 is passed through the water pipe 3 and the water pipe 5 at a ratio of 8: 2. Water before being supplied to the exchanger 2 is merged, heated by the main heat exchanger 2 and then discharged from a hot water supply pipe (not shown). Therefore, even if the water pipe 5 constituting the auxiliary heat exchanger 4 is reduced in diameter. There is no increase in water flow resistance as a whole.
【0012】さらに主熱交換器2への通水量は従来と変
わらないため、主熱交換器2の熱効率が低下することも
ない。Further, since the amount of water passing through the main heat exchanger 2 is not different from the conventional case, the heat efficiency of the main heat exchanger 2 does not decrease.
【0013】[0013]
【発明の効果】以上説明したような構成にしたことで本
発明の燃焼装置は次のような効果を奏する。すなわち請
求項1の燃焼装置では、補助熱交換器と主熱交換器とに
分岐通水するとともに、補助熱交換器において加熱され
た温水を再度、主熱交換器に至る前の供給水と合流する
ことによって、補助熱交換器を構成する水管径を細くし
ても全体の通水抵抗が増加することはないので、十分な
出湯量を得ることができる。したがって径の細い水管を
より密に配置することによって補助熱交換器の小型化が
可能となるとともに、主熱交換器の通水量は従来と変わ
らず、熱効率が低下することもないため、主熱交換器を
大型化する必要もない。その結果燃焼装置全体としても
小型化できる。また、請求項2の燃焼装置では供給水が
何ら加熱作用を受けることなく、温度の低いまま補助熱
交換器に供給されることによって、補助熱交換器の熱効
率を向上することができるので、補助熱交換器の小型化
が可能となり、燃焼装置全体としても小型化できるとい
う効果がある。With the above-described configuration, the combustion apparatus of the present invention has the following effects. That is, in the combustion device of the first aspect, while branching and passing water to the auxiliary heat exchanger and the main heat exchanger, the hot water heated in the auxiliary heat exchanger is again joined with the supply water before reaching the main heat exchanger. By doing so, even if the diameter of the water pipe constituting the auxiliary heat exchanger is reduced, the overall water flow resistance does not increase, so that a sufficient amount of hot water can be obtained. Therefore, by arranging the water pipes with smaller diameters more densely, it is possible to reduce the size of the auxiliary heat exchanger, and the flow rate of water in the main heat exchanger is the same as before and the thermal efficiency does not decrease. There is no need to increase the size of the exchanger. As a result, the size of the entire combustion apparatus can be reduced. Further, in the combustion device according to the second aspect, since the supply water is supplied to the auxiliary heat exchanger at a low temperature without receiving any heating action, the heat efficiency of the auxiliary heat exchanger can be improved. There is an effect that the heat exchanger can be reduced in size, and the entire combustion device can be reduced in size.
【図1】本発明の第1の実施形態を示す燃焼装置の側断
面図である。FIG. 1 is a side sectional view of a combustion device showing a first embodiment of the present invention.
【図2】本発明の第2の実施形態を示す燃焼装置の側断
面図である。FIG. 2 is a side sectional view of a combustion apparatus showing a second embodiment of the present invention.
1 バーナ 2 主熱交換器 3 水管 4 補助熱交換器 5 水管 6 ドレン受け 7 排ガス流路 8 中和装置 9 排ガス流路外壁 10 水管 DESCRIPTION OF SYMBOLS 1 Burner 2 Main heat exchanger 3 Water pipe 4 Auxiliary heat exchanger 5 Water pipe 6 Drain receiver 7 Exhaust gas flow path 8 Neutralization device 9 Outer wall of exhaust gas flow path 10 Water pipe
フロントページの続き (72)発明者 畑 秀典 兵庫県神戸市中央区江戸町93番地 株式会 社ノーリツ内 (72)発明者 永井 逸夫 兵庫県神戸市中央区江戸町93番地 株式会 社ノーリツ内 (72)発明者 忽那 良治 兵庫県神戸市中央区江戸町93番地 株式会 社ノーリツ内 (72)発明者 松田 隆広 兵庫県神戸市中央区江戸町93番地 株式会 社ノーリツ内Continued on the front page (72) Inventor Hidenori Hata 93, Edo-cho, Chuo-ku, Kobe-shi, Hyogo Pref. (72) Inventor Itsuo Nagai 93, Edo-cho, Chuo-ku, Kobe, Hyogo (72) ) Inventor, Ryoji Kutsuna 93, Edocho, Chuo-ku, Kobe, Hyogo Pref. (72) Inventor Takahiro Matsuda 93, Edocho, Chuo-ku, Kobe, Hyogo Pref.
Claims (2)
とを備えた燃焼装置であって、主熱交換器への給水管を
分岐し、補助熱交換器に至る分岐管を設け、前記分岐管
は補助熱交換器を経てその終端が前記給水管との分岐部
より下流側かつ主熱交換器より上流側に接続されたこと
を特徴とする燃焼装置。1. A combustion device comprising a main heat exchanger, an auxiliary heat exchanger, and a burner, wherein a branch pipe for branching a water supply pipe to the main heat exchanger and leading to the auxiliary heat exchanger is provided. A combustion apparatus, wherein the branch pipe is connected via an auxiliary heat exchanger to a terminal downstream of a branch with the water supply pipe and upstream of a main heat exchanger.
とを備えた燃焼装置であって、少なくとも補助熱交換器
へ至るまでは給水管に被加熱部分を設けないことを特徴
とする燃焼装置。2. A combustion device comprising a main heat exchanger, an auxiliary heat exchanger, and a burner, wherein at least a part to be heated is not provided in a water supply pipe up to the auxiliary heat exchanger. Burning device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28011996A JPH10103784A (en) | 1996-09-30 | 1996-09-30 | Combustion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28011996A JPH10103784A (en) | 1996-09-30 | 1996-09-30 | Combustion device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10103784A true JPH10103784A (en) | 1998-04-21 |
Family
ID=17620606
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28011996A Pending JPH10103784A (en) | 1996-09-30 | 1996-09-30 | Combustion device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10103784A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006177623A (en) * | 2004-12-22 | 2006-07-06 | Noritz Corp | Water heater |
JP2008039389A (en) * | 2007-09-21 | 2008-02-21 | Gastar Corp | Combustion device |
CN102734923A (en) * | 2011-04-15 | 2012-10-17 | 于忠顺 | Straw superconducting air hot blast stove |
CN103644645A (en) * | 2013-12-30 | 2014-03-19 | 北京老万生物质能科技有限责任公司 | Modular combined electric boiler |
-
1996
- 1996-09-30 JP JP28011996A patent/JPH10103784A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006177623A (en) * | 2004-12-22 | 2006-07-06 | Noritz Corp | Water heater |
JP2008039389A (en) * | 2007-09-21 | 2008-02-21 | Gastar Corp | Combustion device |
CN102734923A (en) * | 2011-04-15 | 2012-10-17 | 于忠顺 | Straw superconducting air hot blast stove |
CN103644645A (en) * | 2013-12-30 | 2014-03-19 | 北京老万生物质能科技有限责任公司 | Modular combined electric boiler |
CN103644645B (en) * | 2013-12-30 | 2016-08-17 | 北京老万生物质能科技有限责任公司 | A kind of modular combination electric boiler |
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