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JP2729461B2 - Heat exchange equipment - Google Patents
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JP2729461B2 - Heat exchange equipment - Google Patents

Heat exchange equipment

Info

Publication number
JP2729461B2
JP2729461B2 JP5305093A JP30509393A JP2729461B2 JP 2729461 B2 JP2729461 B2 JP 2729461B2 JP 5305093 A JP5305093 A JP 5305093A JP 30509393 A JP30509393 A JP 30509393A JP 2729461 B2 JP2729461 B2 JP 2729461B2
Authority
JP
Japan
Prior art keywords
exhaust
water pipe
heat exchange
exhaust gas
combustion
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.)
Expired - Fee Related
Application number
JP5305093A
Other languages
Japanese (ja)
Other versions
JPH07159079A (en
Inventor
雅昭 中浦
和男 八木
宏治 矢野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Rinnai Corp
Original Assignee
Rinnai Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Rinnai Corp filed Critical Rinnai Corp
Priority to JP5305093A priority Critical patent/JP2729461B2/en
Publication of JPH07159079A publication Critical patent/JPH07159079A/en
Application granted granted Critical
Publication of JP2729461B2 publication Critical patent/JP2729461B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Details Of Fluid Heaters (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、燃焼装置からの排気通
路に吸熱用の通水管を配置した熱交換装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger in which a water absorption pipe is disposed in an exhaust passage from a combustion device.

【0002】[0002]

【従来技術及びその課題】燃焼排気からの熱交換効率の
向上を図った熱交換装置として、図7に示すように、ガ
スバーナ(3) と二段式の熱交換器(1) とが組み合わされ
たものがある。前記熱交換器(1) は、通水管(11)とその
外周に設けられた多数のフィン(12)(12)とこれらを収容
する缶体(6) とから構成されており、該熱交換器(1) は
通水管(11)の下流側の主としてガスバーナ(3) の燃焼排
気の顕熱を吸熱する主熱交換部(1a)と、その下方に配設
された通水管(11)の上流側の主としてガスバーナ(3) の
燃焼排気の潜熱を吸熱する副熱交換部(1b)とから構成さ
れる。そして、熱交換器(1) の下方には、該熱交換器
(1) に付着するドレンを外部に排出するためのドレン排
出口(8) が設けられている。
2. Description of the Related Art As shown in FIG. 7, a gas burner (3) and a two-stage heat exchanger (1) are combined as a heat exchange device for improving heat exchange efficiency from combustion exhaust gas. There are things. The heat exchanger (1) is composed of a water pipe (11), a number of fins (12) (12) provided on the outer periphery thereof, and a can (6) for accommodating these. The heat exchanger (1) has a main heat exchange section (1a) downstream of the water pipe (11), which mainly absorbs the sensible heat of the combustion exhaust gas from the gas burner (3), and a water pipe (11) arranged below it. The upstream side mainly comprises a sub heat exchange section (1b) for absorbing the latent heat of the combustion exhaust gas of the gas burner (3). Then, below the heat exchanger (1), the heat exchanger
A drain outlet (8) is provided for discharging drain adhering to (1) to the outside.

【0003】前記ガスバーナ(3) の炎孔部は下向きに設
定され、その炎形成域近傍に前記主熱交換部(1a)が位置
するように配設されている。そして、前記ガスバーナ
(3) にはファン(4) によって強制的に燃焼用空気が押し
込み供給されるようになっており、これにより、ガスバ
ーナの燃焼排気は主・副熱交換部(1a)(1b)を通過した
後、これの下方の排気筒(21)を介して外部に排出される
ようになっている。
[0003] The flame hole of the gas burner (3) is set downward so that the main heat exchange part (1a) is located near the flame formation area. And the gas burner
Combustion air is forcibly supplied to (3) by the fan (4), so that the combustion exhaust gas from the gas burner passes through the main and sub heat exchange sections (1a) and (1b). Thereafter, the air is discharged to the outside through an exhaust pipe (21) below the exhaust pipe (21).

【0004】このものでは、ガスバーナ(3) を燃焼させ
て副熱交換部(1b)側に位置する通水管(11)から水道水を
供給すると、該通水管(11)内の通水は、ガスバーナ(3)
の発生熱量を通水管(11)やフィン(12)(12)から吸熱し
て、湯となって主熱交換部(1a)から外部に取り出される
が、そのための吸熱作用の中で、主熱交換部(1a)では主
として、ガスバーナ(3) の燃焼排気の顕熱を吸熱する作
用が行われ、副熱交換部(1b)では、主として、ガスバー
ナ(3) の燃焼排気中の水蒸気を凝縮させてその潜熱を吸
熱する作用が行われる。即ち、副熱交換部(1b)では、顕
熱が奪われて冷却された燃焼排気をその露点温度以下に
冷却させることによってドレンを発生させ、そのときの
潜熱を該副熱交換部(1b)における通水管(11)内の通水に
吸熱させているのである。そして、前記副熱交換部(1b)
に付着したドレンは、その自重によって該副熱交換部(1
b)の下方に滴下し、ドレン排出口(8) から外部に排出さ
れる。このものでは、燃焼排気の顕熱だけでなく潜熱を
も積極的に熱交換部に吸収させるので、熱効率が向上す
るという利点がある。
In this apparatus, when the gas burner (3) is burned to supply tap water from the water pipe (11) located on the side of the sub heat exchange section (1b), the water flow in the water pipe (11) becomes Gas burner (3)
The heat generated is absorbed by the water pipe (11) and the fins (12) and (12), and is taken out as hot water from the main heat exchange section (1a). The exchange section (1a) mainly absorbs the sensible heat of the combustion exhaust gas from the gas burner (3), and the sub heat exchange section (1b) mainly condenses the water vapor in the combustion exhaust gas from the gas burner (3). The latent heat is absorbed. That is, in the sub heat exchange section (1b), sensible heat is deprived and the cooled combustion exhaust is cooled to a temperature equal to or lower than its dew point to generate drain, and the latent heat at that time is used as the sub heat exchange section (1b). In this case, heat is absorbed by the water flowing in the water pipe (11). And the sub heat exchange section (1b)
The drain adhering to the sub heat exchange section (1
It is dropped below b) and discharged outside through the drain outlet (8). In this case, since not only the sensible heat of the combustion exhaust gas but also the latent heat is positively absorbed in the heat exchange section, there is an advantage that the thermal efficiency is improved.

【0005】しかしながら、このものでは、熱効率を未
だ十分に向上させることができない。熱交換器(1) に送
り込まれる燃焼排気は、該熱交換器(1) における通水管
(11)の部分及びこれら通水管の相互間の間隔に対して均
等に流入するために、ガスバーナ(3) からの燃焼排気の
全てが通水管(11)の上面に接触しない。又、通水管(11)
の下面側は排気流の流れにおいて背後にあたるために、
該下面側では燃焼排気が淀んだ状態になり、当該部分に
新鮮な燃焼排気が流れ込まない。これらのことから、燃
焼排気の全てが通水管(11)に有効に接触して熱交換する
こととはならず、この点で熱効率を十分には向上させる
ことができない。
[0005] However, in this case, the thermal efficiency cannot be sufficiently improved yet. The combustion exhaust gas sent to the heat exchanger (1) passes through the water pipe in the heat exchanger (1).
All of the combustion exhaust gas from the gas burner (3) does not come into contact with the upper surface of the water pipe (11) because the gas flows equally into the portion (11) and the distance between the water pipes. In addition, water pipe (11)
Because the lower side of the
On the lower surface side, the combustion exhaust becomes stagnant, and fresh combustion exhaust does not flow into this portion. From these facts, all of the combustion exhaust does not effectively contact the water pipe (11) to exchange heat, and in this respect, the thermal efficiency cannot be sufficiently improved.

【0006】尚、上記と同様の不都合は、図8に示すよ
うに、ガスバーナ(3)上方の燃焼排気通路の下流側に
熱交換器山が配設される形式のものでも発生する。本発
明は、このような、『下方向に延在する燃焼装置からの
排気通路の幅方向複数の吸熱用の通水管(11)を間隔
をあけて並列に設けた構成の熱交換装置』において、熱
効率を向上させ、かつ発生したドレンの排出を容易にす
ることをその課題とする。
[0008] The same disadvantage as described above also occurs in a type in which a heat exchanger mountain is disposed downstream of a combustion exhaust passage above a gas burner (3), as shown in FIG. 8. The present invention relates to such a “heat exchange device having a configuration in which a plurality of heat-absorbing water pipes (11) are provided in parallel at intervals in the width direction of an exhaust passage from a combustion device extending downward”. It is an object of the present invention to improve thermal efficiency and facilitate discharge of generated drain.

【0007】[0007]

【技術的手段】上記課題を解決するために講じた本発明
の技術的手段は、『前記通水管(11)の各々に対して
排気流の上流側の表面に燃焼排気を集めるための第1排
気集中手段(A)と、該第1排気集中手段(A)からの
燃焼排気を通水管(11)における排気流の下流側表面
に集めて排出するための第2排気集中手段(B)と、通
水管(11)の断面両側に対向配置され、第1排気集中
手段(A)と第2排気集中手段(B)との間に通水管
(11)の断面側壁に沿って燃焼排気を案内する排気案
内手段(C)とを備え、排気案内手段(C)の各々は、
排気通路の内壁又は他の排気案内手段(C)に対して所
定の部分で密接するように配置され、さらに排気案内手
段(C)の各々の前記所定の部分より上側の部分にドレ
ン排出用の透孔(55)が形成された』ことである。
The technical means of the present invention taken for solving the above-mentioned problem is as follows: The first means for collecting the combustion exhaust gas on the upstream surface of the exhaust flow for each of the water pipes (11). Exhaust concentrating means (A), and second exhaust concentrating means (B) for collecting and discharging the combustion exhaust from the first exhaust concentrating means (A) to the downstream surface of the exhaust flow in the water pipe (11). The combustion exhaust is guided along the sectional side wall of the water pipe (11) between the first exhaust concentrating means (A) and the second exhaust concentrating means (B). Exhaust guide means (C), and each of the exhaust guide means (C)
A predetermined portion is disposed so as to be in close contact with the inner wall of the exhaust passage or another exhaust guide means (C), and a portion for discharging drain is provided above each of the predetermined portions of the exhaust guide means (C). The through-hole (55) was formed. "

【0008】[0008]

【作用】本発明の上記技術的手段は、次のように作用す
る。燃焼装置で生成された燃焼排気が通水管(11)に
接触し、燃焼排気中の熱量が前記通水管(11)内の通
水に熱交換される。このとき、第1排気集中手段(A)
及び第2排気集中手段(B)に対応した図1の概念図に
示すように、各々の通水管(11)に向けて流れる燃焼
排気だけでなく、更にこれから外れた部分に供給される
燃焼排気が第1排気集中手段(A)によって通水管(1
1)の部分に集められる。即ち、排気流の上流側に面す
る通水管(11)の表面に向けて燃焼排気が集められ、
これにより前記通水管(11)の表面部分に燃焼排気が
集中的に吹き付けられる。そして、上記第1排気集中手
段(A)から通水管(11)の表面に吹き付けられた燃
焼排気は、該通水管(11)の側方を流れた後に第2排
気集中手段(B)によって通水管(11)の裏面部分、
即ち、通水管(11)における排気流の下流側表面に集
められた後に排出される。このように、燃焼装置からの
燃焼排気は、通水管(11)における上流側表面に吹き
つけられた後、その側方表面から下流側表面に沿って流
れ、その後排気流下流側の表面から集中的に排出される
こととなる。このことから、上記技術的手段によれば、
通水管(11)に接触する燃焼排気の量が多くなり、
又、排気流と通水管(11)との接触時間が長くなる。
The above technical means of the present invention operates as follows. The combustion exhaust gas generated by the combustion device comes into contact with the water pipe (11), and the amount of heat in the combustion exhaust gas is exchanged with the water in the water pipe (11). At this time, the first exhaust concentration means (A)
As shown in the conceptual view of FIG. 1 corresponding to the second exhaust concentration means (B), not only the combustion exhaust flowing toward each water pipe (11), but also the combustion exhaust supplied to a portion further away therefrom. By the first exhaust concentrating means (A)
Collected in part 1). That is, the combustion exhaust is collected toward the surface of the water pipe (11) facing the upstream side of the exhaust flow,
As a result, the combustion exhaust is intensively blown to the surface of the water pipe (11). The combustion exhaust blown from the first exhaust concentrating means (A) to the surface of the water pipe (11) flows through the water pipe (11) and then flows through the second exhaust concentrating means (B). The back of the water pipe (11),
That is, after being collected on the downstream surface of the exhaust flow in the water pipe (11), it is discharged. As described above, the combustion exhaust gas from the combustion device is blown to the upstream surface of the water pipe (11), flows from the side surface to the downstream surface, and then concentrates from the downstream surface of the exhaust flow. Will be discharged. From this, according to the above technical means,
The amount of combustion exhaust coming into contact with the water pipe (11) increases,
Further, the contact time between the exhaust stream and the water pipe (11) becomes longer.

【0009】[0009]

【0010】さらに、各々の通水管(11)の断面側壁
に沿って燃焼排気を案内する排気案内手段(C)を第1
排気集中手段(A)と第2排気集中手段(B)との間で
通水管(11)の断面両側に対向配置したことから、図
2の概念図に示すように、前記第1排気集中手段(A)
からの燃焼排気は、排気案内手段(C)の上流端部に供
給され、通水管(11)の側方表面に沿って確実に接触
しながら、該排気案内手段(C)と通水管(11)との
間を下流端に向けて流れることとなる。しかも、排気案
内手段(C)の各々は、排気通路の内壁又は他の排気案
内手段(C)に対して密接するように配置されるので、
排気流はすべて排気案内手段(C)によって各々の通水
管(11)の側方表面に案内される。
Further, an exhaust guide means (C) for guiding the combustion exhaust gas along the sectional side wall of each water pipe (11) is provided as a first means.
Since the exhaust gas concentrating means (A) and the second exhaust gas concentrating means (B) are disposed on opposite sides of the cross section of the water pipe (11), as shown in the conceptual diagram of FIG. (A)
Is supplied to the upstream end of the exhaust guide means (C), and the exhaust guide means (C) and the water pipe (11) are reliably contacted along the side surface of the water pipe (11). ) Flows toward the downstream end. Moreover, since each of the exhaust guide means (C) is disposed so as to be in close contact with the inner wall of the exhaust passage or the other exhaust guide means (C),
All exhaust streams are guided by the exhaust guide means (C) to the lateral surfaces of each water pipe (11).

【0011】[0011]

【効果】本発明は、上記構成であるから、次の特有の効
果を有する。通水管(11)に燃焼排気がすべて接触
し、又、排気流と通水管(11)との接触時間が長くな
るから、当該熱交換装置の熱効率が向上する。さらに、
排気案内手段(C)の各々には透孔(55)が形成され
ているので、発生したドレンが滞留する恐れはない。
According to the present invention having the above-described configuration, the present invention has the following specific effects. Since all the combustion exhaust gas comes into contact with the water pipe (11) and the contact time between the exhaust stream and the water pipe (11) becomes longer, the heat efficiency of the heat exchange device is improved. further,
Since the exhaust holes (55) are formed in each of the exhaust guides (C), there is no danger that the generated drain will stay.

【0012】[0012]

【実施例】以下本発明の実施例を図面に従って説明す
る。図3に示す実施例は、燃焼排気を凝縮させてその潜
熱を吸熱する機能を備えた熱交換器(1) を具備する給湯
器に本発明を実施したものである。このものは、給湯器
本体の下部に熱交換器(1) を構成する缶体(6) を設け、
該缶体(6) の上部に多孔プレート式のガスバーナ(3) を
具備し且つ上部に給気室(42)を備える給気箱(7) を配設
したものである。そして、前記給気室(42)にはガスノズ
ル(31)を臨ませており、該給気室(42)の上部にはファン
(4) が設けられている。又、前記熱交換器(1) の下端開
口部には排気筒(21)を接続させている。
Embodiments of the present invention will be described below with reference to the drawings. In the embodiment shown in FIG. 3, the present invention is applied to a water heater provided with a heat exchanger (1) having a function of condensing combustion exhaust gas and absorbing the latent heat. In this device, a can body (6) constituting a heat exchanger (1) is provided at the bottom of the water heater body,
An air supply box (7) having a gas burner (3) of a perforated plate type on the upper part of the can body (6) and an air supply chamber (42) on the upper part is provided. A gas nozzle (31) faces the air supply chamber (42), and a fan is provided above the air supply chamber (42).
(4) is provided. An exhaust pipe (21) is connected to the lower end opening of the heat exchanger (1).

【0013】前記熱交換器(1) は、主にガスバーナ(3)
の燃焼排気の顕熱を吸熱する主熱交換部(1a)と、その下
方に配設され且つ主としてガスバーナ(3) の燃焼排気の
潜熱を吸熱する副熱交換部(1b)とから構成されており、
一方の主熱交換部(1a)は環状のフィン(12)(12)を具備さ
せた通水管(11)から成り、他方の副熱交換部(1b)は前記
通水管(11)における主熱交換部(1a)より上流側部分に環
状のフィン(12)(12)を具備させた構成である。尚、副熱
交換部(1b)に発生するドレンは、缶体(6) 下方のドレン
排出口(8) から外部に排出される。
The heat exchanger (1) mainly includes a gas burner (3)
A main heat exchange section (1a) that absorbs the sensible heat of the combustion exhaust gas, and a sub heat exchange section (1b) that is disposed below and mainly absorbs the latent heat of the combustion exhaust gas from the gas burner (3). Yes,
One main heat exchange section (1a) is composed of a water pipe (11) provided with annular fins (12), (12), and the other sub heat exchange section (1b) is a main heat exchange section of the water pipe (11). The configuration is such that annular fins (12) and (12) are provided on the upstream side of the exchange part (1a). The drain generated in the sub heat exchange section (1b) is discharged to the outside from a drain outlet (8) below the can (6).

【0014】この実施例では、前記主熱交換部(1a)にお
ける通水管(11)は、三段で構成されて各段が横二列若し
くは三列に蛇行状に曲成されており、他方の副熱交換部
(1b)の通水管(11)は、横三列に蛇行状に曲成された一段
構成である。そして、副熱交換部(1b)側の通水管(11)
(通水管(11)の最下段部分)から水道水を供給して主熱
交換部(1a)側の通水管(11)(通水管(11)の最上段部分)
から湯を取り出すようにしている。
In this embodiment, the water pipe (11) in the main heat exchange section (1a) is composed of three stages, each stage being curved in a meandering manner in two rows or three rows. Secondary heat exchange section
The water pipe (11) of (1b) has a single-stage configuration curved in a meandering manner in three horizontal rows. And the water pipe (11) on the side of the sub heat exchange section (1b)
Tap water is supplied from the (bottom part of the water pipe (11)) and the water pipe (11) on the main heat exchange part (1a) side (the top part of the water pipe (11)).
I try to take hot water out of it.

【0015】副熱交換部(1b)における通水管(11)の断面
両側には、断面円弧状の案内板(5)(5)が、該通水管(11)
のフィン(12)(12)と同芯状に配設されており、これらフ
ィン(12)(12)と案内板(5)(5)との間には、所定の間隔が
形成されている。そして、図4に示すように、当該通水
管(11)を包囲する一対の案内板(5)(5)の上端相互及び下
端相互は、該通水管(11)の外径より小さな間隔を置いて
対向しており、これにより、通水管(11)の上方に開放部
(51)(51)が形成されると共に、該通水管(11)下方に開放
部(52)(52)が形成される。尚、断面円弧状に形成された
各案内板(5) の上下方向の中央部相互と、該中央部と缶
体(6) の内壁とは、燃焼排気の流れを実質的に遮断でき
るように密接させている。又、各案内板(5) には、その
上下方向の中央部の若干上方に複数の透孔(55)(55)が穿
設されている。
Guide plates (5) (5) having an arc-shaped cross section are provided on both sides of the cross section of the water pipe (11) in the sub heat exchange section (1b).
Are arranged concentrically with the fins (12) and (12), and a predetermined interval is formed between the fins (12) and (12) and the guide plates (5) and (5). . Then, as shown in FIG. 4, the upper end and the lower end of a pair of guide plates (5) surrounding the water pipe (11) are spaced apart from each other by a distance smaller than the outer diameter of the water pipe (11). So that the opening is located above the water pipe (11).
(51) and (51) are formed, and open portions (52) and (52) are formed below the water pipe (11). The vertical center portions of the guide plates (5) formed into an arc-shaped cross section, and the center portions and the inner wall of the can (6) are designed to substantially block the flow of combustion exhaust gas. Close. Each guide plate (5) is provided with a plurality of through holes (55) (55) slightly above the center in the vertical direction.

【0016】したがって、ファン(4) から強制給気を行
なうと共にガスノズル(31)からガスを供給してガスバー
ナ(3) を燃焼させて、通水管(11)の最下段部分から水道
水を供給すると、既述従来のものと同様に、ガスバーナ
(3) で生成された燃焼排気は熱交換器(1) の主熱交換部
(1a)→副熱交換部(1b)→排気筒(21)と流れて外部に排出
される。一方、主熱交換部(1a)や副熱交換部(1b)の通水
管(11)内の通水は、ガスバーナ(3) の発生熱量を通水管
(11)やフィン(12)(12)から吸収して、通水管(11)の最上
段部分から湯となって外部に取り出される。このときの
吸熱作用の中で、ガスバーナ(3) の燃焼排気の顕熱を吸
熱する作用は、主に、主熱交換部(1a)で行われており、
副熱交換部(1b)では、主として、ガスバーナ(3) の燃焼
排気を凝縮させてその潜熱を吸熱する作用が行われる。
即ち、副熱交換部(1b)では、主として、顕熱が奪われて
冷却された燃焼排気をその露点温度以下に冷却させるこ
とによってドレンを発生させ、そのときの潜熱を副熱交
換部(1b)に位置する通水管(11)内の通水に吸収させてい
るのである。
Therefore, when forced air is supplied from the fan (4) and gas is supplied from the gas nozzle (31) to burn the gas burner (3), tap water is supplied from the lowermost part of the water pipe (11). Gas burner similar to the conventional one
The combustion exhaust gas generated in (3) is the main heat exchange section of the heat exchanger (1).
(1a) → the sub heat exchange section (1b) → the exhaust pipe (21) and discharged to the outside. On the other hand, the water flow in the water pipe (11) of the main heat exchange section (1a) and the sub heat exchange section (1b) is based on the heat generated by the gas burner (3).
The water is absorbed from (11) and the fins (12) and (12), and is taken out from the uppermost part of the water pipe (11) as hot water. In this endothermic action, the action of absorbing the sensible heat of the combustion exhaust gas from the gas burner (3) is mainly performed in the main heat exchange section (1a).
In the sub heat exchange section (1b), the action of mainly condensing the combustion exhaust gas of the gas burner (3) and absorbing the latent heat thereof is performed.
That is, in the sub heat exchange section (1b), the sensible heat is deprived and the cooled combustion exhaust is cooled below its dew point temperature to generate drain, and the latent heat at that time is converted into the sub heat exchange section (1b). ) Is absorbed by the water flowing in the water pipe (11).

【0017】このとき、通水管(11)上方の開放部(51)(5
1)以外は、案内板(5)(5)同士等が密接状態にされている
ことから、副熱交換部(1b)に送り込まれる燃焼排気は、
該開放部(51)(51)から集中的に流入して通水管の上面に
接触せしめられ、案内板(5)(5)と、通水管(11)及びフィ
ン(12)(12)との間に流入する。すると、案内板(5)(5)の
形状は断面円弧状としてあることから、案内板(5)(5)と
通水管(11)等との間の空間は、通水管(11)等の外形に倣
った形状に形成されているので、当該燃焼排気は通水管
(11)等の外周面に確実に沿って流れることとなる。そし
て、この燃焼排気は通水管(11)の下方の開放部(52)(52)
から排出され、このときに該通水管(11)の下面に集中的
に接触する。したがって、この実施例のものでは、前記
したような、燃焼排気の通水管(11)やフィン(12)(12)の
全周にわたる有効的な接触作用によって、当該副熱交換
部(1b)においては、燃焼ガスが無駄なく凝縮されて、こ
れにより熱効率が向上する。この凝縮作用によって、副
熱交換部(1b)にはドレンが発生するが、通水管(11)やフ
ィン(12)(12)に付着したドレンは上記開放部(52)(52)を
通ってその下方に滴下し、又、案内板(5)(5)の外壁の上
部に付着したドレンは透孔(55)(55)を通って中に入り、
開放部(52)(52)から下方に流下することから、該ドレン
が副熱交換部(1b)に滞留することはない。尚、上記実施
例では、缶体(6) 内に架設される案内板(5)(5)の上半分
が既述技術的手段の項に記載の第1排気集中手段(A) に
相当すると共に、案内板(5)(5)の下半分が第2排気集中
手段(B) に相当する一方、この案内板(5)(5)の全体が排
気案内手段(C) に相当する。
At this time, the open portions (51) (5) above the water pipe (11)
Except for 1), since the guide plates (5) and (5) are in close contact with each other, the combustion exhaust gas sent to the sub heat exchange unit (1b) is:
The water flows intensively from the open portions (51) and (51), is brought into contact with the upper surface of the water pipe, and is formed between the guide plates (5) and (5), the water pipe (11) and the fins (12) and (12). Flows in between. Then, since the shapes of the guide plates (5) and (5) are arc-shaped in cross section, the space between the guide plates (5) and (5) and the water pipe (11) is the same as that of the water pipe (11). Since it is formed in a shape that follows the external shape, the combustion exhaust is
It will surely flow along the outer peripheral surface such as (11). Then, the combustion exhaust gas is supplied to the open portion (52) (52) below the water pipe (11).
At this time, and intensively contacts the lower surface of the water pipe (11). Therefore, in the embodiment, the auxiliary heat exchange section (1b) in the auxiliary heat exchange section (1b) by the effective contact action over the entire circumference of the combustion exhaust water pipe (11) and the fins (12) (12) as described above. In this method, the combustion gas is condensed without waste, thereby improving the thermal efficiency. Due to this condensation, drain is generated in the sub heat exchange section (1b), but the drain attached to the water pipe (11) and the fins (12) (12) passes through the open sections (52) and (52). Drain dripped below it, and the drain attached to the upper part of the outer wall of the guide plates (5) (5) enters through the through holes (55) (55),
Since the water flows downward from the open portions (52) and (52), the drain does not stay in the sub heat exchange portion (1b). In the above embodiment, the upper half of the guide plates (5) and (5) installed in the can body (6) corresponds to the first exhaust concentration means (A) described in the section of the technical means described above. At the same time, the lower half of the guide plates (5) and (5) corresponds to the second exhaust concentrating means (B), while the entire guide plates (5) and (5) correspond to the exhaust guide means (C).

【0018】尚、上記実施例は、以下のように変更が可
能である。 .上記実施例では、各案内板(5) を断面円弧状に形成
したが、これを、図5に示す如く断面「く字状」に形成
してもよい。かかる場合も、缶体(6) 内に架設される案
内板(5)(5)の上半分が既述技術的手段の項に記載の第1
排気集中手段(A)に、案内板(5)(5)の下半分が第2排気
集中手段(B) に相当する一方、案内板(5)(5)全体が排気
案内手段(C) に相当する。
The above embodiment can be modified as follows. . In the above embodiment, each guide plate (5) is formed in an arc-shaped cross section. However, it may be formed in a "L-shaped" cross section as shown in FIG. In such a case as well, the upper half of the guide plates (5) and (5) installed in the can body (6) is the first half of the technical means described above.
The lower half of the guide plates (5) and (5) correspond to the second exhaust concentrator (B), while the entire guide plates (5) and (5) correspond to the exhaust guide (C). Equivalent to.

【0019】又、図6に示す如く、波形板(5a)(5a)を、
副熱交換部(1b)における通水管(11)の断面両側に配設し
てもよい。この場合、波形板(5a)(5a)の凹凸表面に燃焼
排気が衝突してこれが通水管(11)側に集められ、これに
より、熱効率が向上する。そして、このものでは、波形
板(5a)(5a)の上半分が第1排気集中手段(A) に、下半分
が第2排気集中手段(B) に相当する。 .本発明は、主熱交換部(1a)にて主として顕熱を吸収
し、副熱交換部(1b)にて主として潜熱を吸収する形式の
熱交換器はもちろん、主熱交換部(1a)にて顕熱のみを吸
収し、副熱交換部(1b)にて主として潜熱を吸収する形式
のものにも採用できる。何れの場合でも、主熱交換部(1
a)に本発明を実施してもよい。 .上記実施例では、通水管(11)を蛇行状に曲成させて
4段構成となるようにしてその中で、最下段を副熱交換
部(1b)とし他の3段を主熱交換部(1a)としたが、主熱交
換部(1a)の顕熱吸収能力によっては潜熱を吸収する副熱
交換部(1b)の副通水管(11b) は、下から2段・3段等の
複数段となる。
As shown in FIG. 6, the corrugated plates (5a) and (5a) are
It may be provided on both sides of the cross section of the water pipe (11) in the sub heat exchange section (1b). In this case, the combustion exhaust collides with the uneven surfaces of the corrugated plates (5a), (5a) and is collected on the water pipe (11) side, thereby improving the thermal efficiency. In this case, the upper half of the corrugated plates (5a) and (5a) corresponds to the first exhaust concentrating means (A), and the lower half corresponds to the second exhaust concentrating means (B). . The present invention is a heat exchanger of the type mainly absorbing sensible heat in the main heat exchange section (1a) and mainly absorbing latent heat in the sub heat exchange section (1b), as well as the main heat exchange section (1a). It is also applicable to a type that absorbs only sensible heat and absorbs mainly latent heat in the sub heat exchange section (1b). In any case, the main heat exchange section (1
The present invention may be implemented in a). . In the above embodiment, the water pipe (11) is bent in a meandering shape so as to have a four-stage configuration, in which the lowest stage is the sub heat exchange unit (1b) and the other three stages are the main heat exchange unit. (1a), but depending on the sensible heat absorption capacity of the main heat exchange part (1a), the sub-flow pipe (11b) of the sub heat exchange part (1b), which absorbs latent heat, There are multiple stages.

【0020】このように、副熱交換部(1b)が複数段に構
成される場合は、下から2段目若しくは3段目等の通水
管(11)から給水してもよい。又、上記実施例の場合も含
めて、湯の取り出しは上から2段目若しくは3段目等か
ら行ってもよい。 .上記実施例では、ファン(4) を給気通路側に設けた
が、これを排気通路(21)側に設けてもよい。 .上記実施例では、給湯器に本発明を実施したが、給
湯器以外にも、加熱された水を循環させる方式の暖房器
等の熱交換装置にも本発明を採用することは可能であ
る。上記何れの場合でも、熱交換装置が具備する熱交換
器は、燃焼排気中の顕熱を吸熱する機能のみを備える形
式でもよい。 .開放部(52)(52)からドレンを円滑に落下させるた
め、該開放部(52)(52)周縁における案内板(5)(5)の下端
縁から、垂下片を垂下させてもよい。
When the sub heat exchange section (1b) is constructed in a plurality of stages as described above, water may be supplied from the water pipe (11) of the second or third stage from the bottom. Also, including the case of the above embodiment, the hot water may be taken out from the second or third stage from the top. . In the above embodiment, the fan (4) is provided on the side of the air supply passage, but may be provided on the side of the exhaust passage (21). . In the above embodiment, the present invention is applied to a water heater, but the present invention can also be applied to a heat exchanger such as a heater that circulates heated water, in addition to the water heater. In any of the above cases, the heat exchanger included in the heat exchange device may be a type having only a function of absorbing sensible heat in the combustion exhaust gas. . In order to allow the drain to smoothly fall from the open portions (52), (52), a hanging piece may be hung from the lower edge of the guide plates (5), (5) around the open portions (52), (52).

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の第1排気集中手段(A)及び第2排気
集中手段(B)の概念図
FIG. 1 is a conceptual diagram of a first exhaust concentration means (A) and a second exhaust concentration means (B) of the present invention.

【図2】本発明の第1排気集中手段(A)、第2排気集
中手段(B)及び排気案内手段(C)の概念図
FIG. 2 is a conceptual diagram of a first exhaust concentrating means (A), a second exhaust concentrating means (B) and an exhaust guiding means (C) of the present invention.

【図3】本発明の実施例の説明図FIG. 3 is an explanatory diagram of an embodiment of the present invention.

【図4】案内板(5)(5)の説明図FIG. 4 is an explanatory view of guide plates (5) and (5).

【図5】案内板(5)(5)の他の例の説明図FIG. 5 is an explanatory view of another example of the guide plates (5) and (5).

【図6】波形板(5a)(5a)の説明図FIG. 6 is an explanatory view of a corrugated plate (5a) (5a).

【図7】従来例の説明図FIG. 7 is an explanatory view of a conventional example.

【図8】他の従来例の説明図FIG. 8 is an explanatory view of another conventional example.

【符号の説明】[Explanation of symbols]

(11)・・・通水管 (A)・・・第1排気集中手段 (B)・・・第2排気集中手段 (C)・・・排気案内手段 (11) ... water pipe (A) ... first exhaust concentrating means (B) ... second exhaust concentrating means (C) ... exhaust guiding means

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F28F 17/00 501 F28F 17/00 501A ──────────────────────────────────────────────────続 き Continuation of the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical display location F28F 17/00 501 F28F 17/00 501A

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 下方向に延在する燃焼装置からの排気通
路の幅方向に複数の吸熱用の通水管(11)を間隔をあ
けて並列に設けた構成の熱交換装置において、前記通水
管(11)の各々に対して排気流の上流側の表面に燃焼
排気を集めるための第1排気集中手段(A)と、該第1
排気集中手段(A)からの燃焼排気を通水管(11)に
おける排気流の下流側表面に集めて排出するための第2
排気集中手段(B)と、通水管(11)の断面両側に対
向配置され、第1排気集中手段(A)と第2排気集中手
段(B)との間に通水管(11)の断面側壁に沿って燃
焼排気を案内する排気案内手段(C)とを備え、排気案
内手段(C)の各々は、排気通路の内壁又は他の排気案
内手段(C)に対して所定の部分で密接するように配置
され、さらに排気案内手段(C)の各々の前記所定の部
分より上側の部分にドレン排出用の透孔(55)が形成
された熱交換装置。
1. A heat exchanger according to claim 1, wherein a plurality of heat-absorbing water pipes (11) are provided in parallel in the width direction of an exhaust passage extending from a combustion apparatus extending downward. A first exhaust concentrating means (A) for collecting combustion exhaust gas on the upstream surface of the exhaust flow for each of (11);
A second means for collecting and discharging the combustion exhaust gas from the exhaust concentration means (A) on the downstream surface of the exhaust flow in the water pipe (11);
The exhaust gas concentrating means (B) is disposed on both sides of the cross section of the water pipe (11) so as to face each other, and the cross section side wall of the water pipe (11) is provided between the first exhaust gas concentrating means (A) and the second exhaust gas concentrating means (B). Exhaust guide means (C) for guiding the combustion exhaust along the exhaust gas passage, and each of the exhaust guide means (C) is in close contact with the inner wall of the exhaust passage or another exhaust guide means (C) at a predetermined portion. A heat exchange device, wherein a drain hole (55) for drain discharge is formed in a portion above each of the predetermined portions of the exhaust guide means (C).
JP5305093A 1993-12-06 1993-12-06 Heat exchange equipment Expired - Fee Related JP2729461B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5305093A JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5305093A JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Publications (2)

Publication Number Publication Date
JPH07159079A JPH07159079A (en) 1995-06-20
JP2729461B2 true JP2729461B2 (en) 1998-03-18

Family

ID=17941024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5305093A Expired - Fee Related JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Country Status (1)

Country Link
JP (1) JP2729461B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1292221C (en) * 1999-07-21 2006-12-27 斯通-韦伯斯特有限公司 Cross-flow heat transfer device and enhanced cross-flow heat transfer method
JP5612749B1 (en) * 2013-10-25 2014-10-22 増山 征男 Gas cooling device
CN118816586B (en) * 2024-08-02 2025-03-04 重庆帅豪机械有限公司 A dry air cooler

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60176367U (en) * 1984-04-24 1985-11-22 石川島播磨重工業株式会社 Heat exchanger
JPH0158039U (en) * 1987-10-06 1989-04-11

Also Published As

Publication number Publication date
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