JPH07167586A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH07167586A
JPH07167586A JP5312274A JP31227493A JPH07167586A JP H07167586 A JPH07167586 A JP H07167586A JP 5312274 A JP5312274 A JP 5312274A JP 31227493 A JP31227493 A JP 31227493A JP H07167586 A JPH07167586 A JP H07167586A
Authority
JP
Japan
Prior art keywords
heat exchange
fins
heat exchanger
exchange section
sub
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
Application number
JP5312274A
Other languages
Japanese (ja)
Inventor
Kazuo Yagi
和男 八木
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=18027272&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JPH07167586(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Rinnai Corp filed Critical Rinnai Corp
Priority to JP5312274A priority Critical patent/JPH07167586A/en
Priority to KR1019940033997A priority patent/KR0132742B1/en
Publication of JPH07167586A publication Critical patent/JPH07167586A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H8/00Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation
    • F24H8/006Means for removing condensate from the heater
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/10Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
    • F24H1/12Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium
    • F24H1/14Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form
    • F24H1/145Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form using fluid fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/047Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/084Heat exchange elements made from metals or metal alloys from aluminium or aluminium alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/085Heat exchange elements made from metals or metal alloys from copper or copper alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/082Heat exchange elements made from metals or metal alloys from steel or ferrous alloys
    • F28F21/083Heat exchange elements made from metals or metal alloys from steel or ferrous alloys from stainless steel

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To make compact the whole structure of a heat exchanger device by forming fins of a heat exchanger unit with a high thermal conductivity material, such as copper and constituting water flow tubes or fins in a sub-heat exchanger unit with highly corrosion resistant materials, such as aluminum alloy. CONSTITUTION:Water flow tubes 11 in a main heat exchanger unit 1a are constructed with three stages where each stage is meanderingly laid out laterally in two or three rows. The water flow tubes 11 and fins 12a into which the water flow tubes are penetrated are formed with copper which is a high conductivity material. The water flow tubes 11 in the other sub-heat exchanger unit 1b are meanderingly laid out laterally in three rows under one stage structure. The water flow tubes 11 and the fins 12b into which the tubes are penetrated are formed with aluminum alloy which is excellent in corrosion resistance. The adoption of the fins 12 of a highly thermal conductivity material makes it possible to reduce the size of the main heat exchanger unit 1a, and compact the whole structure of the heat exchanger device.

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、熱交換装置、特に、燃
焼排気中の水蒸気を凝縮させ、その潜熱を熱交換部に吸
熱させることによって、熱交換効率の向上を図る形式の
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 exchanging device, and more particularly to a heat exchanging device for condensing water vapor in combustion exhaust gas and absorbing the latent heat in the heat exchanging portion to improve heat exchanging efficiency. It is about.

【0002】[0002]

【従来技術及びその課題】前記形式の熱交換装置とし
て、図3に示すように、ガスバーナ(3) と熱交換器(1)
とが組み合わされたものがある。この熱交換器(1) は、
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)は通水管
(11)とその外周に設けられた多数のフィン(12a)(12a)と
から成り、他方の副熱交換部(1b)は上記通水管(11)にお
ける前記主熱交換部(1a)より上流側部分とその外周に設
けられた多数のフィン(12b)(12b)とから成る。そして、
前記主熱交換部(1a)及び副熱交換部(1b)を構成する上記
通水管(11)やフィン(12a)(12b)は、後述する腐食の問題
を考慮してアルミニウム合金で形成されている。
2. Description of the Related Art As a heat exchanger of the above type, as shown in FIG. 3, a gas burner (3) and a heat exchanger (1) are provided.
There is a combination of and. This heat exchanger (1)
Main heat exchange part (1a) which mainly absorbs sensible heat of combustion exhaust gas of the gas burner (3), and sub heat exchange part (1b) which is arranged below it and mainly absorbs latent heat of combustion exhaust gas of the gas burner (3).
The main heat exchange part (1a) on one side is a water pipe.
(11) and a large number of fins (12a) and (12a) provided on the outer periphery thereof, and the other sub heat exchange section (1b) is upstream of the main heat exchange section (1a) in the water pipe (11). It is composed of a side portion and a large number of fins (12b) (12b) provided on the outer periphery thereof. And
The water pipe (11) and fins (12a) (12b) constituting the main heat exchange part (1a) and the sub heat exchange part (1b) are formed of an aluminum alloy in consideration of the corrosion problem described later. There is.

【0003】前記ガスバーナ(3) は、これの炎孔部が下
向きに設定され、その炎形成域近傍に前記主熱交換部(1
a)が位置するように配設されている。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(12a)(12b)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、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、主熱交換部(1a)で顕熱が奪
われて冷却された燃焼排気をその露点温度以下の該副熱
交換部(1b)における通水管(11)やフィン(12b)(12b)に接
触させることによってドレンを発生させ、そのときの潜
熱を該通水管(11)内の通水に吸熱させることにより熱効
率の向上を図っているのである。
In the gas burner (3), the flame hole portion is set downward, and the main heat exchange portion (1) is provided in the vicinity of the flame forming region.
It is arranged so that a) is located. In this case, when the gas burner (3) is combusted and tap water is supplied from the water pipe (11) located on the side of the sub heat exchange section (1b), the water in the water pipe (11) flows through the gas burner (3). ) Heat is absorbed from the water pipe (11) and fins (12a) and (12b) to become hot water, and the main heat exchange part (1a)
Of the gas burner (3), the sensible heat of the combustion exhaust gas of the gas burner (3) is absorbed mainly by the main heat exchange section (1a). Department
In (1b), the action of mainly condensing the steam in 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 flue gas deprived of the sensible heat in the main heat exchange section (1a) to cool the combustion exhaust gas, the water pipe (11) in the sub heat exchange section (1b) below the dew point temperature. The drain is generated by contacting the fins (12b) (12b) with each other, and the latent heat at that time is absorbed by the water passing through the water pipe (11) to improve the thermal efficiency.

【0004】一方、前記副熱交換部(1b)には上記の如く
ドレンが付着し、然も該ドレンには燃焼排気中の腐食性
成分(窒素酸化物等)が溶融しているが、該副熱交換部
(1b)は耐食性に優れたアルミニウム合金で形成されてい
ることから、該副熱交換部(1b)は腐食し難いものになっ
ている。しかしながら、このものでは、装置全体が大型
化するという問題があった。
On the other hand, the drain adheres to the sub heat exchange section (1b) as described above, and the corrosive component (nitrogen oxide etc.) in the combustion exhaust gas is melted to the drain. Sub heat exchange section
Since (1b) is formed of an aluminum alloy having excellent corrosion resistance, the sub heat exchange section (1b) is resistant to corrosion. However, this has a problem that the entire device becomes large.

【0005】このものでは、腐食の原因となるドレンの
発生が著しい副熱交換部(1b)と、前記ドレンが殆ど発生
しない主熱交換部(1a)とが画一的に、耐食性の優れたア
ルミニウム合金で形成されている。ところが、アルミニ
ウム合金は、熱伝導率が比較的小さい(約0.52cal/
℃cm・sec)ことから、所定の熱効率を得るには、通水管
(11)やフィン(12a)(12b)の表面積を大きくしなければな
らない。従って、上記したドレンが殆ど発生しない主熱
交換部(1a)に位置する通水管(11)やフィン(12a)(12a)の
表面積も大きくしなければならなくなって、装置全体が
大きくなるのである。
In this case, the auxiliary heat exchange part (1b) in which the drainage which causes the corrosion is remarkable and the main heat exchange part (1a) in which the drainage is hardly generated are uniformly excellent in corrosion resistance. It is made of aluminum alloy. However, aluminum alloy has a relatively low thermal conductivity (about 0.52 cal /
℃ cm · sec), to obtain the specified thermal efficiency, water pipe
The surface area of (11) and fins (12a) (12b) must be increased. Therefore, the surface area of the water passage pipe (11) and the fins (12a) (12a) located in the main heat exchange part (1a) where the above-mentioned drain is hardly generated also has to be increased, and the entire device becomes large. .

【0006】本発明は、このような、『通水管(11)の外
周に多数のフィン(12a)(12a)を設けて主熱交換部(1a)を
構成し、上記通水管(11)における前記主熱交換部(1a)よ
り上流側部分の外周に多数のフィン(12b)(12b)を設けて
副熱交換部(1b)を構成し、排気通路における燃焼装置の
下流側に主熱交換部(1a)と副熱交換部(1b)をこの順序で
順次配設することにより前者の主熱交換部(1a)で燃焼排
気の顕熱を吸収し、後者の副熱交換部(1b)で燃焼排気を
通水管(11)やフィン(12b)(12b)に接触させて該燃焼排気
から顕熱及び潜熱を吸収するようにした熱交換装置』に
おいて、熱交換装置全体をコンパクトにできるようにす
ることをその課題とする。
According to the present invention, the main heat exchange section (1a) is constructed by providing a large number of fins (12a) (12a) on the outer periphery of the water pipe (11) as described above. A large number of fins (12b) (12b) are provided on the outer periphery of the upstream side of the main heat exchange section (1a) to form the auxiliary heat exchange section (1b), and the main heat exchange is performed downstream of the combustion device in the exhaust passage. By arranging the section (1a) and the sub heat exchange section (1b) in this order, the sensible heat of the combustion exhaust is absorbed by the former main heat exchange section (1a), and the latter sub heat exchange section (1b). In order to make the entire heat exchange device compact, it is possible to make the heat exchange device in contact with the water passage pipe (11) or the fins (12b) (12b) by absorbing the sensible heat and latent heat from the combustion exhaust gas. The task is to

【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、『主熱交換部(1a)のフィン(12a)(12a)
を銅等の熱伝導率の高い材料で形成すると共に、副熱交
換部(1b)における通水管(11)やフィン(12b)(12b)をアル
ミニウム合金等の耐食性に富む材料で構成した』ことで
ある。
[Technical Means] The technical means of the present invention taken to solve the above-mentioned problem is "fins (12a) (12a) of the main heat exchange part (1a)".
Is made of a material with high thermal conductivity such as copper, and the water pipes (11) and fins (12b) (12b) in the sub heat exchange section (1b) are made of a material with high corrosion resistance such as an aluminum alloy. Is.

【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。主熱交換部(1a)におけるフィン(12a)(12a)は銅等の
熱伝導率の高い材料で形成されていることから、既述従
来のものと同じ熱効率を確保しながら、その表面積を小
さくでき、前記主熱交換部(1a)を小さくすることができ
る。尚、上記のものでは、主熱交換部(1a)におけるフィ
ン(12a)(12a)の材料を選択するに当って、その耐食性を
考慮していないが、該主熱交換部(1a)は専ら顕熱を吸収
するだけでドレンが殆ど発生しないから、上記フィン(1
2a)(12a)が腐食する心配がない。又、腐食性成分が溶融
したドレンが既述従来例で説明したように副熱交換部(1
b)にて発生するが、該副熱交換部(1b)の通水管(11)やフ
ィン(12b)(12b)は、既述従来のものと同様にアルミニウ
ム合金等の耐食性の良好な材料で形成されていることか
ら、該副熱交換部(1b)の腐食に対処することができる。
The above technical means of the present invention operates as follows. Since the fins (12a) and (12a) in the main heat exchange part (1a) are made of a material having a high thermal conductivity such as copper, the surface area is small while ensuring the same thermal efficiency as the conventional one. Therefore, the main heat exchange section (1a) can be downsized. In the above, in selecting the material of the fins (12a) (12a) in the main heat exchange part (1a), the corrosion resistance is not taken into consideration, but the main heat exchange part (1a) is exclusively used. Since the drain is hardly generated only by absorbing sensible heat, the fin (1
There is no concern about corrosion of 2a) and (12a). In addition, as described in the above-mentioned conventional example, the drainage in which the corrosive component is melted causes the sub heat exchange part (1
Although it occurs in b), the water passage pipe (11) and the fins (12b) (12b) of the sub heat exchange part (1b) are made of a material having a good corrosion resistance such as an aluminum alloy like the conventional one. Since it is formed, it is possible to cope with the corrosion of the sub heat exchange portion (1b).

【0009】[0009]

【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。熱伝導率の高い材料のフィン(12a)(12a)を
採用することにより、主熱交換部(1a)を小型化できるの
で、その分、熱交換装置全体をコンパクトなものにでき
る。
[Effect] The present invention having the above-mentioned structure has the following unique effects. Since the main heat exchange section (1a) can be downsized by adopting the fins (12a) (12a) made of a material having a high heat conductivity, the heat exchange apparatus as a whole can be made compact accordingly.

【0010】[0010]

【実施例】以下本発明の実施例を図面に従って説明す
る。図1に示す実施例は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)
を収容する缶体(6) を設け、該缶体(6) の上部にガスバ
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、該給気箱(7) の上部にファン(4) を設
け、前記熱交換器(1) の燃焼排気の流れにおける下流側
に配設される排気通路(21)が給湯器本体を上下に走行す
る態様で設けられたものである。
Embodiments of the present invention will be described below with reference to the drawings. The embodiment shown in FIG. 1 is one in which the present invention is applied to a water heater. This one has a heat exchanger (1) at the bottom of the water heater body.
An air supply box provided with a can body (6) for accommodating a gas, a gas burner (3) being provided on an upper part of the can body (6), and an air supply chamber (42) being provided on an upper part.
(7) is provided, a fan (4) is provided in the upper part of the air supply box (7), and an exhaust passage (21) is provided downstream of the combustion exhaust flow of the heat exchanger (1). Is provided so as to run up and down the water heater main body.

【0011】前記熱交換器(1) は、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)とから構成されてい
る。一方の主熱交換部(1a)は環状のフィン(12a)(12a)を
具備させた通水管(11)から成り、他方の副熱交換部(1b)
は通水経路における主熱交換部(1a)の上流側に位置し且
つ環状のフィン(12b)(12b)を具備させた通水管(11)から
成る。尚、前記缶体(6) の下端は、開放しており、副熱
交換部(1b)に発生するドレンは、該缶体(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) is mainly a gas burner.
From the main heat exchange part (1a) that absorbs the sensible heat of the combustion exhaust of (3), and the sub heat exchange part (1b) that is arranged below it and that mainly absorbs the latent heat of the combustion exhaust of the gas burner (3). It is configured. One main heat exchange part (1a) consists of a water pipe (11) equipped with annular fins (12a) (12a), and the other sub heat exchange part (1b)
Consists of a water pipe (11) located upstream of the main heat exchange part (1a) in the water passage and equipped with annular fins (12b) (12b). The lower end of the can body (6) is open, and the drain generated in the auxiliary heat exchange section (1b) is discharged to the outside from the drain discharge port (8) below the can body (6). .

【0012】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
状に配設されており、この主熱交換部(1a)の通水管(11)
とこれが貫通するフィン(12a)(12a)は、熱伝導率の高い
銅(銅の熱伝導率は約0.93cal/℃cm・sec)で形成さ
れている。他方の副熱交換部(1b)の通水管(11)は、横三
列に蛇行状に配設された一段構成であり、副熱交換部(1
b)における通水管(11)とこれが貫通するフィン(12b)(12
b)は耐食性の良好なアルミニウム合金で形成されてい
る。そして、熱交換器(1) の主熱交換部(1a)は既述従来
のものと比べてコンパクトに構成されている。即ち、主
熱交換部(1a)における通水管(11)とフィン(12a)(12a)の
吸熱面積が、構成材料の熱伝導率の関係から、既述従来
のものと同等の熱効率を確保しながら、該従来のものよ
り小さく設定されているのである。
A water pipe (11) in the main heat exchange section (1a)
Is composed of three stages, and each stage is arranged in two rows or three rows in a meandering shape, and the water pipe (11) of the main heat exchange section (1a) is
The fins (12a) (12a) penetrating therethrough are formed of copper having a high thermal conductivity (the thermal conductivity of copper is about 0.93 cal / ° C cm · sec). The water pipe (11) of the other sub heat exchange section (1b) has a one-stage structure in which the sub heat exchange section (1) is arranged in three rows in a meandering manner.
The water pipe (11) and the fins (12b) (12b)
b) is made of an aluminum alloy with good corrosion resistance. Further, the main heat exchange part (1a) of the heat exchanger (1) is made compact as compared with the above-mentioned conventional one. That is, the heat absorption area of the water pipe (11) and the fins (12a) (12a) in the main heat exchange part (1a) ensures the same thermal efficiency as the above-mentioned conventional one from the relationship of the thermal conductivity of the constituent materials. However, it is set smaller than the conventional one.

【0013】上記ガスバーナ(3) は全一次空気燃焼方式
であり、多孔プレート(31)とこれの上方の混合室(32)と
から構成されており、該混合室(32)にはガスノズル(33)
が臨んでいる。上記排気通路(21)は、給湯器の上記缶体
(6) の下端開口部から引き出されており、その下流端の
排気口(2) は給湯器の上部に開口している。
The gas burner (3) is of the all primary air combustion type and comprises a perforated plate (31) and a mixing chamber (32) above the porous plate (31). The mixing chamber (32) has a gas nozzle (33). )
Is facing. The exhaust passage (21) is the can body of the water heater.
It is pulled out from the lower end opening of (6), and the exhaust port (2) at its downstream end opens to the upper part of the water heater.

【0014】したがって、ファン(4) を作動させて混合
室(32)に一次空気を供給すると共にガスノズル(33)から
ガスを供給してガスバーナ(3) を燃焼させて、通水管(1
1)に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)→排気通路(21)と流れ
て排気口(2) から外部に排出される。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) の発生熱量を上記フィン(12a)(12b)や通水管(1
1)から吸収して、上段の通水管(11)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
の露点温度以下の該副熱交換部(1b)に位置する通水管(1
1)やフィン(12b)(12b)に接触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通水管(11)内の通水に
吸収させているのである。このとき、副熱交換部(1b)に
はドレンが発生するが、該副熱交換部(1b)は耐食性の高
いアルミニウム合金で形成されていることから、該副熱
交換部(1b)が腐食することはない。尚、主熱交換部(1a)
はコンパクトに形成するために熱伝導率の良い銅で形成
されており、そのため耐食性は劣るが、該主熱交換部(1
a)にはドレンが発生しないので、腐食の問題は発生しな
い。
Therefore, the fan (4) is operated to supply the primary air to the mixing chamber (32), and the gas is supplied from the gas nozzle (33) to burn the gas burner (3), so that the water passage (1
When tap water is supplied to (1), the combustion exhaust gas generated in the gas burner (3) is discharged from the main heat exchange section (1a) of the heat exchanger (1) → the sub heat exchange section ( It flows from 1b) to the exhaust passage (21) and is discharged to the outside from the exhaust port (2). On the other hand, the main heat exchange section
(1a) and the water in the water pipe (11) of the sub heat exchange part (1b), the generated heat of the gas burner (3) is the same as the above fins (12a) (12b) and water pipe (1).
It is absorbed from 1) and made hot water from the upper water pipe (11) and taken out to the outside. Among the endothermic action at this time, the action of absorbing the sensible heat of the combustion exhaust of the gas burner (3) is mainly performed in the main heat exchange section (1a), and in the sub heat exchange section (1b), Mainly, the combustion exhaust gas of the gas burner (3) is condensed and the latent heat is absorbed. That is, in the sub heat exchange section (1b), mainly the sensible heat is taken away and the cooled combustion exhaust gas is placed in the water pipe (1b) located in the sub heat exchange section (1b) below the dew point temperature.
Drain is generated by bringing it into contact with 1) or the fins (12b) (12b), and the latent heat at that time is absorbed by the water flow in the water flow pipe (11). At this time, drain is generated in the sub heat exchange section (1b), but since the sub heat exchange section (1b) is formed of an aluminum alloy having high corrosion resistance, the sub heat exchange section (1b) is corroded. There is nothing to do. The main heat exchange section (1a)
Is formed of copper with good thermal conductivity in order to form a compact structure, and therefore the corrosion resistance is poor, but the main heat exchange part (1
No drainage occurs in a), so there is no problem of corrosion.

【0015】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、副熱交換部(1b)をアルミニウム合
金で形成したが、これをステンレス鋼で形成してもよ
い。又、主熱交換部(1a)における通水管(11)とフィン(1
2a)(12a)とを銅で形成したが、該通水管(11)をアルミニ
ウム合金等で形成し、フィン(12a)(12a)を銅で形成して
もよい。
The above embodiment can be modified as follows. . Although the sub heat exchange part (1b) is made of an aluminum alloy in the above embodiment, it may be made of stainless steel. In addition, the water pipe (11) and the fins (1) in the main heat exchange section (1a)
Although 2a) and (12a) are formed of copper, the water pipe (11) may be formed of an aluminum alloy or the like and the fins (12a) and (12a) may be formed of copper.

【0016】尚、上記何れの場合でも、銅に替えて銅合
金を用いることも可能である。 .上記実施例では、通水管(11)を蛇行状に曲成させて
四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)とし他の三段を主熱交換部(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)は、下から二段・三段等の複数段となる。こ
の場合、当該副熱交換部(1b)における各段の通水管(11)
及びフィン(12b)(12b)をアルミニウム合金等で形成す
る。
In any of the above cases, a copper alloy may be used instead of copper. . In the above embodiment, the water pipe (11) is bent in a meandering manner to form a four-stage structure, in which the lowermost stage is the auxiliary heat exchange section (1b) and the other three stages are the main heat exchange section. Although (1a) is used, depending on the sensible heat absorbing capacity of the main heat exchange section (1a), the sub heat exchange section (1b) that absorbs latent heat has a plurality of stages such as two stages and three stages from the bottom. In this case, the water pipe (11) at each stage in the sub heat exchange section (1b)
Also, the fins (12b) (12b) are formed of an aluminum alloy or the like.

【0017】このように、副熱交換部(1b)が複数段に構
成される場合は、下から二段目若しくは三段目等の通水
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二段目若しくは三段目等か
ら行ってもよい。又、図2に示すように、缶体(6) と排
気通路(21)との間に、通水管(11)の最上流端に連通接続
させ且つ多数のフィン(12b)(12b)を具備させた扁平な矩
形状断面を有する補助通水管(11a) を介在させて、該補
助通水管(11a) に水道水を供給するようにしてもよい。
そして、該補助通水管(11a) とフィン(12b)(12b)とを副
熱交換部(1b)とし、他を主熱交換部(1a)とするのであ
る。かかる場合、該補助通水管(11a) 及びフィン(12b)
(12b)をアルミニウム合金等で形成する。 .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。。
As described above, when the sub heat exchange section (1b) is formed in a plurality of stages, water may be supplied from the water pipes (11) at 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 addition, as shown in FIG. 2, a large number of fins (12b) (12b) are provided between the can body (6) and the exhaust passage (21) so as to communicate with the most upstream end of the water pipe (11). Tap water may be supplied to the auxiliary water pipe (11a) by interposing the auxiliary water pipe (11a) having a flat rectangular cross section.
Then, the auxiliary water flow pipe (11a) and the fins (12b) and (12b) are used as a sub heat exchange section (1b), and the other are used as a main heat exchange section (1a). In such a case, the auxiliary water pipe (11a) and fins (12b)
(12b) is formed of an aluminum alloy or the like. . In the above embodiment, the fan (4) is provided on the air supply passage side, but it may be provided on the exhaust passage (21) side. . Although the present invention is applied to the water heater in the above-described embodiments, the present invention can be applied to a heat exchange device such as a heater that circulates heated water in addition to the water heater. .

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

【図1】本発明の実施例の説明図FIG. 1 is an explanatory diagram of an embodiment of the present invention.

【図2】他の実施例の説明図FIG. 2 is an explanatory diagram of another embodiment.

【図3】従来例の説明図FIG. 3 is an explanatory diagram of a conventional example.

【符号の説明】[Explanation of symbols]

(11) ・・・通水管 (1a) ・・・主熱交換部 (1b) ・・・副熱交換部 (12a)、(12b) ・・・フィン (11) ・ ・ ・ Water pipe (1a) ・ ・ ・ Main heat exchange part (1b) ・ ・ ・ Sub heat exchange part (12a), (12b) ・ ・ ・ Fin

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 通水管(11)の外周に多数のフィン(12a)
(12a)を設けて主熱交換部(1a)を構成し、上記通水管(1
1)における前記主熱交換部(1a)より上流側部分の外周に
多数のフィン(12b)(12b)を設けて副熱交換部(1b)を構成
し、排気通路における燃焼装置の下流側に主熱交換部(1
a)と副熱交換部(1b)をこの順序で順次配設することによ
り前者の主熱交換部(1a)で燃焼排気の顕熱を吸収し、後
者の副熱交換部(1b)で燃焼排気を通水管(11)やフィン(1
2b)(12b)に接触させて該燃焼排気から顕熱及び潜熱を吸
収するようにした熱交換装置において、主熱交換部(1a)
のフィン(12a)(12a)を銅等の熱伝導率の高い材料で形成
すると共に、副熱交換部(1b)における通水管(11)やフィ
ン(12b)(12b)をアルミニウム合金等の耐食性に富む材料
で構成した熱交換装置。
1. A large number of fins (12a) on the outer circumference of the water pipe (11).
(12a) is provided to form the main heat exchange section (1a), and the water pipe (1
A large number of fins (12b) (12b) are provided on the outer circumference of the upstream side of the main heat exchange section (1a) in 1) to form the sub heat exchange section (1b), and the exhaust passage is provided on the downstream side of the combustion device. Main heat exchange part (1
By arranging a) and the sub heat exchange part (1b) in this order in sequence, the sensible heat of the combustion exhaust is absorbed by the former main heat exchange part (1a) and burned by the latter sub heat exchange part (1b). Exhaust pipes (11) and fins (1
2b) In the heat exchange device in contact with (12b) so as to absorb sensible heat and latent heat from the combustion exhaust gas, the main heat exchange section (1a)
The fins (12a) and (12a) are made of a material with high thermal conductivity such as copper, and the water pipes (11) and fins (12b) and (12b) in the sub heat exchange section (1b) are made of aluminum alloy or other corrosion resistant material. Heat exchanger composed of rich materials.
【請求項2】 主熱交換部(1a)における通水管(11)を銅
等の熱伝導率の高い材料で形成した請求項1に記載の熱
交換装置。
2. The heat exchange device according to claim 1, wherein the water passage pipe (11) in the main heat exchange portion (1a) is made of a material having a high thermal conductivity such as copper.
JP5312274A 1993-12-13 1993-12-13 Heat exchanger Pending JPH07167586A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP5312274A JPH07167586A (en) 1993-12-13 1993-12-13 Heat exchanger
KR1019940033997A KR0132742B1 (en) 1993-12-13 1994-12-13 Heat exchanger apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5312274A JPH07167586A (en) 1993-12-13 1993-12-13 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH07167586A true JPH07167586A (en) 1995-07-04

Family

ID=18027272

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5312274A Pending JPH07167586A (en) 1993-12-13 1993-12-13 Heat exchanger

Country Status (2)

Country Link
JP (1) JPH07167586A (en)
KR (1) KR0132742B1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1026454A2 (en) 1999-02-04 2000-08-09 Rinnai Kabushiki Kaisha Heat exchanger apparatus
EP1559965A1 (en) * 2004-01-28 2005-08-03 Jose Maria Vergara Uranga Condensing boiler with a two-stage heatexchanger
JP2006177623A (en) * 2004-12-22 2006-07-06 Noritz Corp Water heater
KR100893746B1 (en) * 2007-04-03 2009-04-17 엘지전자 주식회사 Air conditioner
JP2010096449A (en) * 2008-10-17 2010-04-30 Denso Corp Heat exchanger
JP2014095524A (en) * 2012-11-12 2014-05-22 Hitachi Appliances Inc Air conditioner
CN108489315A (en) * 2018-05-24 2018-09-04 浙江智海化工设备工程有限公司 A kind of heat exchanger core minor structure

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56168055A (en) * 1980-05-28 1981-12-24 Osaka Gas Co Ltd Hot water supplier
JPS60245787A (en) * 1984-05-18 1985-12-05 Matsushita Electric Ind Co Ltd Heat exchanger
JPS6115044A (en) * 1984-06-28 1986-01-23 Matsushita Electric Ind Co Ltd Heat exchanger
JPS635339B2 (en) * 1982-04-30 1988-02-03 Takara Standard Kk

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56168055A (en) * 1980-05-28 1981-12-24 Osaka Gas Co Ltd Hot water supplier
JPS635339B2 (en) * 1982-04-30 1988-02-03 Takara Standard Kk
JPS60245787A (en) * 1984-05-18 1985-12-05 Matsushita Electric Ind Co Ltd Heat exchanger
JPS6115044A (en) * 1984-06-28 1986-01-23 Matsushita Electric Ind Co Ltd Heat exchanger

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1026454A2 (en) 1999-02-04 2000-08-09 Rinnai Kabushiki Kaisha Heat exchanger apparatus
EP1026454A3 (en) * 1999-02-04 2002-10-16 Rinnai Kabushiki Kaisha Heat exchanger apparatus
EP1559965A1 (en) * 2004-01-28 2005-08-03 Jose Maria Vergara Uranga Condensing boiler with a two-stage heatexchanger
JP2006177623A (en) * 2004-12-22 2006-07-06 Noritz Corp Water heater
US7458340B2 (en) 2004-12-22 2008-12-02 Noritz Corporation Water heater
KR100893746B1 (en) * 2007-04-03 2009-04-17 엘지전자 주식회사 Air conditioner
JP2010096449A (en) * 2008-10-17 2010-04-30 Denso Corp Heat exchanger
JP2014095524A (en) * 2012-11-12 2014-05-22 Hitachi Appliances Inc Air conditioner
CN108489315A (en) * 2018-05-24 2018-09-04 浙江智海化工设备工程有限公司 A kind of heat exchanger core minor structure

Also Published As

Publication number Publication date
KR950019607A (en) 1995-07-24
KR0132742B1 (en) 1998-04-20

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