JPH11108570A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH11108570A
JPH11108570A JP28212797A JP28212797A JPH11108570A JP H11108570 A JPH11108570 A JP H11108570A JP 28212797 A JP28212797 A JP 28212797A JP 28212797 A JP28212797 A JP 28212797A JP H11108570 A JPH11108570 A JP H11108570A
Authority
JP
Japan
Prior art keywords
heat
heat medium
heat exchange
exchange
heat source
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
JP28212797A
Other languages
Japanese (ja)
Inventor
Junichi Shitamachi
順一 下町
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP28212797A priority Critical patent/JPH11108570A/en
Publication of JPH11108570A publication Critical patent/JPH11108570A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • F28D7/085Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently heat-exchange a medium to be heat-exchanged such as oxygen-containing gas for combustion with a heat source heat medium such as exhaust gas for combustion. SOLUTION: This heat exchanger is provided with a lead-in chamber 2 and a lead-out chamber 3 for a heat medium to be heat-exchanged in the direction of the flow of the heat source heat medium in a heat source heat medium passage 1. A plurality of heat exchangers 5 and 15, which make heat media to be heat-exchanged flow in the direction of the flow of the heat source heat medium flowing in the heat source heat medium passage 1, are juxtaposed in the heat source heat medium passage. For the heat exchangers 5 and 15, both their ends lead to the lead-in chamber 2 and the lead-out chamber 3, respectively, of the said heat medium to be heat-exchanged. For each heat exchange pipe 5 and 15, straight pipe parts 7 continuous to both ends connected to the lead-in chamber 2 and the lead-out chamber 3 and turn parts 8 in the middles being continuous to both straight pipes 7 and having turn bent pipe parts are arranged on the same plane orthogonal to the flow direction of the heat source heat medium flowing in the heat source heat medium passage 1.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、鉄鋼加熱炉、熱処
理炉、アルミニューム溶融炉などにおいて、例えば、燃
焼排ガスによって燃焼用酸素含有ガスを熱交換により予
熱するなど熱源熱媒体と被熱交換熱媒体とを熱交換する
熱交換装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steel heating furnace, a heat treatment furnace, an aluminum melting furnace, and the like, for example, heat exchange between a heat source heat medium and a heat source such as preheating an oxygen-containing gas for combustion by heat exchange with combustion exhaust gas. The present invention relates to a heat exchange device that exchanges heat with a medium.

【0002】[0002]

【従来の技術】従来のこの種のバーナ装置における燃焼
用酸素含有ガスを予熱する熱交換装置は、例えば、特公
昭53−20139号公報または実公昭53−5210
7号公報に記載されているように、燃焼排ガスの排ガス
通路に中間部を略W字状または略U字状に屈曲した複数
の熱交換管体をこの排ガス通路を流動する排ガスの流動
方向と平行方向に配設し、この各熱交換管体の一端を燃
焼用酸素含有ガスの導入室に連通させるとともに他端を
燃焼用酸素含有ガスの導出室に連通させる構造が採られ
ていた。
2. Description of the Related Art A conventional heat exchanger for preheating an oxygen-containing gas for combustion in a burner of this type is disclosed, for example, in Japanese Patent Publication No. 53-20139 or Japanese Utility Model Publication No. 53-5210.
As described in Japanese Patent Application Publication No. 7, a plurality of heat exchange pipes having an intermediate portion bent in a substantially W-shape or a substantially U-shape in an exhaust gas passage of a combustion exhaust gas and a flow direction of the exhaust gas flowing through the exhaust gas passage. The heat exchange tubes are arranged in parallel, and one end of each of the heat exchange tubes is communicated with a chamber for introducing the oxygen-containing gas for combustion, and the other end is communicated with a chamber for extracting the oxygen-containing gas for combustion.

【0003】そして、この従来の熱交換装置は導入室か
ら流入された燃焼用酸素含有ガスは排ガス通路を流動す
る燃焼排ガスと熱交換により加熱されて高温の燃焼用酸
素含有ガスとなって導出室に流出し、高温の燃焼用酸素
含有ガスをバーナの燃焼部に供給するようになってい
る。
In this conventional heat exchange apparatus, the combustion oxygen-containing gas flowing from the introduction chamber is heated by heat exchange with the combustion exhaust gas flowing through the exhaust gas passage to become a high-temperature combustion oxygen-containing gas, and the outlet chamber is heated. And the hot oxygen-containing gas for combustion is supplied to the combustion section of the burner.

【0004】[0004]

【発明が解決しようとする課題】上記従来の熱交換装置
では、燃焼用酸素含有ガスは熱交換管体の中間の屈曲部
では熱源熱源熱媒体の燃焼排ガスとの流動方向は平行流
となり、熱回収効率を高めることに限界があった。
In the above conventional heat exchange apparatus, the flow direction of the oxygen-containing gas for combustion is parallel to the flow direction of the combustion exhaust gas of the heat source heat source heat medium at the middle bent portion of the heat exchange tube. There was a limit to improving the recovery efficiency.

【0005】本発明は上記問題点に鑑みなされたもの
で、燃焼用酸素含有ガスなどの被熱交換熱媒体を熱効率
よく燃焼排ガスなどの熱源熱媒体と熱交換ができる熱交
換装置を提供するものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and provides a heat exchanger capable of efficiently exchanging a heat exchange heat medium such as an oxygen-containing gas for combustion with a heat source heat medium such as combustion exhaust gas. It is.

【0006】[0006]

【課題を解決するための手段】請求項1に記載の発明の
熱交換装置は、熱源熱媒体通路と、この熱媒体通路の熱
源熱媒体の流動方向に沿って設けられた被熱交換熱媒体
の導入室および導出室と、前記熱源熱媒体通路内にこの
熱源熱媒体通路を流動する熱源熱媒体の流動方向に並設
されかつ両端部をそれぞれ前記被熱交換熱媒体の導入室
および導出室に連通された被熱交換熱媒体を流動させる
複数の熱交換管体とを備え、前記各熱交換管体は、前記
被熱交換熱媒体の導入室および導出室に両端部を接続す
るとともにこの両端部に連続する直管部とこの両側直管
部に連続する中間部の折り返し部とを有し、この各熱交
換管体の折り返し部は、両側直管部にそれぞれ連続する
折り返し屈曲管部と、この折り返し屈曲管部にそれぞれ
連続した中間直管部と、この両中間直管部に連続する折
り返し屈曲管部とにて形成し、前記各熱交換管体の直管
部と折り返し部とを前記熱源熱媒体通路を流動する熱源
熱媒体の流動方向と直交する同一面に配設したものであ
る。
According to a first aspect of the present invention, there is provided a heat exchange apparatus, wherein a heat source heat medium passage and a heat exchange heat medium provided along the flow direction of the heat source heat medium in the heat medium passage. And the introduction chamber and the extraction chamber of the heat exchange heat medium which are arranged in the heat source heat medium passage in the flow direction of the heat source heat medium flowing through the heat source heat medium passage, and have both ends thereof. A plurality of heat exchange pipes for flowing the heat exchange heat medium that is communicated with the heat exchange heat medium, and each of the heat exchange pipes has both ends connected to the introduction chamber and the discharge chamber of the heat exchange heat medium. It has a straight pipe portion continuous to both ends and an intermediate folded portion continuous to both straight pipe portions, and the folded portion of each heat exchange pipe body is a folded bent pipe portion respectively continuous to both straight pipe portions. And intermediate straight pipes respectively connected to this folded pipe section And a folded bent tube portion that is continuous with both intermediate straight tube portions, and the straight tube portion and the folded portion of each of the heat exchange tubes are flow direction of the heat source heat medium flowing through the heat source heat medium passage. It is arranged on the same plane orthogonal to.

【0007】そして、被熱交換熱媒体の導入室に導入さ
れた被熱交換熱媒体は、複数の熱交換管体を流動して熱
源熱媒体通路を流動する熱源熱媒体と熱交換し、被熱交
換熱媒体は加熱されて導出室に流出される。この熱交換
管体を流れる被熱交換熱媒体は熱交換管体の両側直管部
とこの両側直管部にそれぞれ連通する折り返し部の両側
直管部にそれぞれ連続する折り返し屈曲管部と、この折
り返し屈曲管部にそれぞれ連続した中間直管部と、この
両中間直管部に連続する折り返し屈曲管部とを流動する
間に熱源熱媒体通路を流動する熱源熱媒体と熱交換さ
れ、しかも、この両側直管部、この両側直管部とそれぞ
れ連続する折り返し屈曲管部と、この折り返し屈曲管部
にそれぞれ連続した中間直管部、この両中間直管部に連
続する折り返し屈曲管部を流れる被熱交換熱媒体と熱源
熱媒体通路を流れる熱源熱媒体とは全域において直交流
となり、熱交換効率が高められ、熱効率が向上する。
The heat-exchange heat medium introduced into the heat-exchange heat-medium introduction chamber exchanges heat with the heat-source heat medium flowing through the plurality of heat-exchange tubes and the heat-source heat-medium passages. The heat exchange heat medium is heated and flows out to the outlet chamber. The heat exchange heat medium flowing through the heat exchange tube is a straight bent portion that is continuous with both straight portions on both sides of the heat exchange tube and straight portions on both sides of the folded portion that respectively communicate with the straight portions on both sides. The intermediate straight pipe portions respectively connected to the folded bent pipe portions, and the heat source heat medium flowing in the heat source heat medium passage while flowing through the folded bent pipe portions continuous to both the intermediate straight pipe portions, are heat-exchanged, and The straight pipe sections on both sides, the folded bent pipe sections respectively connected to the both straight pipe sections, the intermediate straight pipe sections respectively connected to the folded bent pipe sections, and the folded bent pipe sections connected to the both intermediate straight pipe sections flow. The heat-exchanged heat medium and the heat-source heat medium flowing through the heat-source heat medium passage form a direct flow in the entire region, so that the heat exchange efficiency is improved and the heat efficiency is improved.

【0008】さらに、各熱交換管体は折り返し部の折り
返し屈曲部が多くなり、熱膨脹による撓み変形が生じに
くく、熱交換管体が折損することがなく超高温の熱交換
が可能となる。
Further, each heat exchange tube body has a large number of folded portions at the folded portions, so that bending deformation due to thermal expansion hardly occurs, and heat exchange at an extremely high temperature can be performed without breakage of the heat exchange tube body.

【0009】請求項2記載の発明の熱交換装置は、請求
項1記載の熱交換装置において、被熱交換熱媒体の導入
室を両側にそれぞれ配設し、この両側の導入室の中間部
に被熱交換熱媒体の導出室を形成し、この両側の被熱交
換熱媒体の導入室にそれぞれ熱交換管体の一端部を連通
させるとともに中間部の導出室にそれぞれこの熱交換管
体の他端部を接続し、この一対の熱交換管体を熱源熱媒
体通路にこの熱源熱媒体通路を流動する熱源熱媒体の流
動方向と直交する同一面にそれぞれ配設したものであ
る。
According to a second aspect of the present invention, there is provided the heat exchange apparatus according to the first aspect, wherein the introduction chambers for the heat exchange heat medium are disposed on both sides, respectively, and at an intermediate portion between the introduction chambers on both sides. An outlet chamber for the heat exchange heat medium is formed, and one end of the heat exchange tube is connected to each of the introduction chambers for the heat exchange heat medium on both sides of the heat exchange heat medium. The ends are connected, and the pair of heat exchange tubes are arranged in the heat source heat medium passage on the same plane orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage.

【0010】そして、両側の被熱交換熱媒体の導入室に
流入した被熱交換熱媒体はそれぞれ熱交換管体を流動
し、熱源熱媒体通路を流動する熱源熱媒体と熱交換し、
被熱交換熱媒体は加熱されて両導入室の中間に配設され
た導出室に流出され、熱源熱媒体の流動方向と直交する
同一面にそれぞれ配設した複数対の熱交換管体にそれぞ
れ流動する被熱交換熱媒体は熱交換管体の直管部とこの
両側直管部に連続する中間部を折り返し部とを流動する
ときに熱源熱媒体と直交流となり、熱交換効率が高めら
れ、熱効率が向上する。
The heat-exchange heat mediums flowing into the heat-exchange heat-medium introduction chambers on both sides flow through the heat-exchange tubes and exchange heat with the heat-source heat medium flowing through the heat-source heat medium passages.
The heat-exchanged heat medium is heated and flows out to an outlet chamber arranged between the two introduction chambers, and is transferred to a plurality of pairs of heat exchange pipes respectively arranged on the same surface orthogonal to the flow direction of the heat source heat medium. The flowing heat exchange heat medium flows in the straight pipe portion of the heat exchange tube body and the intermediate portion continuous with the straight pipe portions on both sides, and when flowing therethrough, there is a direct exchange with the heat source heat medium, thereby increasing the heat exchange efficiency. , Improve thermal efficiency.

【0011】請求項3記載の発明の熱交換装置は、請求
項1記載の熱交換装置において、被熱交換熱媒体の導出
室を両側にそれぞれ配設し、この両側の導出室の中間部
に被熱交換熱媒体の導入室を形成し、この中間の被熱交
換熱媒体の導入室にそれぞれ熱交換管体の一端部を連通
させるとともに両側の導出室にそれぞれこの熱交換管体
の他端部を接続し、この一対の熱交換管体を熱源熱媒体
通路にこの熱源熱媒体通路を流動する熱源熱媒体の流動
方向と直交する同一面にそれぞれ配設したものである。
According to a third aspect of the present invention, there is provided the heat exchange apparatus according to the first aspect, wherein the outlet chambers for the heat exchange heat medium are disposed on both sides, respectively, and the outlet chambers on the both sides are provided at an intermediate portion. An introduction chamber for the heat exchange heat medium is formed, and one end of the heat exchange tube is connected to the intermediate heat exchange heat medium introduction chamber, and the other end of the heat exchange tube is respectively connected to the outlet chambers on both sides. And a pair of heat exchange tubes are disposed in the heat source heat medium passage on the same plane orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage.

【0012】そして、被熱交換熱媒体の導入室に流入し
た被熱交換熱媒体はそれぞれ熱交換管体を流動し、熱源
熱媒体通路を流動する熱源熱媒体と熱交換し、被熱交換
熱媒体は加熱されて導入室の両側に配設された導出室に
流出され、熱源熱媒体の流動方向と直交する同一面にそ
れぞれ配設した複数対の熱交換管体にそれぞれ流動する
被熱交換熱媒体は熱交換管体の直管部とこの両側直管部
に連続する中間部を折り返し部とを流動するときに熱源
熱媒体と直交流となり、熱交換効率が高められ、熱効率
が向上する。
The heat exchange heat medium flowing into the introduction chamber of the heat exchange heat medium flows through the heat exchange tube, exchanges heat with the heat source heat medium flowing through the heat source heat medium passage, and generates heat exchange heat. The medium is heated and flows out to the outlet chambers disposed on both sides of the introduction chamber, and flows through the plurality of pairs of heat exchange pipes respectively disposed on the same surface orthogonal to the flow direction of the heat source heat medium. When the heat medium flows through the straight pipe portion of the heat exchange tube and the folded portion of the intermediate portion continuous with the straight pipe portions on both sides, the heat medium forms a direct flow with the heat source heat medium, thereby increasing the heat exchange efficiency and improving the heat efficiency. .

【0013】請求項4記載の発明の熱交換装置は、請求
項1記載の熱交換装置において、被熱交換熱媒体の導入
室の両側にそれぞれ被熱交換熱媒体の導出室を形成し、
この中間の被熱交換熱媒体の導入室にそれぞれ熱交換管
体の一端部を連通させるとともに両側の導出室にそれぞ
れこの熱交換管体の他端部を接続し、この一対の熱交換
管体を熱源熱媒体通路にこの熱源熱媒体通路を流動する
熱源熱媒体の流動方向と直交する同一面にそれぞれ配設
して第1の熱交換部を形成し、この両側の導出室に連通
する導入室を両側にそれぞれ配設し、この導入室の中間
部に被熱交換熱媒体の導出室を形成し、この両側の被熱
交換熱媒体の導入室にそれぞれ熱交換管体の一端部を連
通させるとともに中間部の導出室にそれぞれこの熱交換
管体の他端部を接続し、この複数対の熱交換管体を前記
熱源熱媒体通路にこの熱源熱媒体通路を流動する熱源熱
媒体の流動方向と直交する同一面にそれぞれ配設して第
2の熱交換部を形成し、前記熱源熱媒体通路にこの熱源
熱媒体通路を流動する熱源熱媒体の下流側に前記第1の
熱交換部を配設するとともに前記第2の熱交換部をこの
熱源熱媒体通路を流動する熱源熱媒体の上流側に配設し
たものである。
According to a fourth aspect of the present invention, there is provided the heat exchange apparatus according to the first aspect, wherein a heat exchange heat medium outlet chamber is formed on each side of the heat exchange heat medium introduction chamber.
One end of the heat exchange tube is communicated with each of the intermediate chambers for introducing the heat exchange heat medium, and the other end of the heat exchange tube is connected to each of the outlet chambers on both sides. Are arranged on the same surface orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage in the heat source heat medium passage to form a first heat exchange portion, and the first heat exchange portion communicates with the outlet chambers on both sides thereof. Chambers are arranged on both sides, and an outlet for the heat exchange heat medium is formed in the middle of the introduction chamber. One end of the heat exchange pipe is connected to each of the heat exchange heat medium introduction chambers on both sides. At the same time, the other ends of the heat exchange tubes are respectively connected to the outlet chambers in the intermediate portion, and the plurality of pairs of heat exchange tubes are connected to the heat source heat medium passage so that the heat source heat medium flows through the heat source heat medium passage. The second heat exchange section is formed by arranging them on the same plane orthogonal to the direction. The first heat exchange unit is disposed downstream of the heat source heat medium flowing through the heat source heat medium passage in the heat source heat medium passage, and the second heat exchange unit flows through the heat source heat medium passage. It is disposed upstream of the heat source heat medium.

【0014】そして、被熱交換熱媒体の導入室に流入し
た第1の熱交換部の被熱交換熱媒体はそれぞれ各熱交換
管体を流動し、熱源熱媒体通路を流動する熱源熱媒体と
熱交換し、被熱交換熱媒体は中温に加熱されて導入室の
両側に配設された導出室に流出され、さらに、この両導
出室にそれぞれ連通する導入室から第2の熱交換部の各
熱交換管体を流動し、熱源熱媒体通路の第1の熱交換部
の配設位置より上流側で熱源熱媒体通路を流動する熱源
熱媒体と熱交換し、被熱交換熱媒体はさらに高温に加熱
されて両導入室の間に配設された導出室に流出され、第
1および第2の熱交換部にて、熱源熱媒体の流動方向と
直交する同一面にそれぞれ配設した一対の熱交換管体に
それぞれ流動する被熱交換熱媒体は熱交換管体の直管部
とこの両側直管部に連続する中間部の折り返し部とを流
動するときに熱源熱媒体と直交流となり、熱交換効率が
高められ、熱効率が向上する。
The heat exchange heat medium of the first heat exchange section that has flowed into the heat exchange heat medium introduction chamber flows through each heat exchange tube, and the heat source heat medium flowing through the heat source heat medium passage. After the heat exchange, the heat exchange heat medium is heated to a medium temperature and flows out to the outlet chambers disposed on both sides of the inlet chamber. Each heat exchange pipe flows and exchanges heat with the heat source heat medium flowing in the heat source heat medium passage on the upstream side of the position of the first heat exchange part of the heat source heat medium passage. It is heated to a high temperature and flows out to an outlet chamber arranged between the two introduction chambers, and a pair of first and second heat exchanging sections are respectively arranged on the same plane orthogonal to the flow direction of the heat source heat medium. The heat exchange heat medium flowing through the heat exchange tubes of the two tubes is the straight tube of the heat exchange tube and the straight tubes on both sides. Consecutive becomes a heat source heat medium and the cross when flowing through the folded portion of the intermediate portion, the heat exchange efficiency is increased, thereby improving the thermal efficiency.

【0015】請求項5記載の発明の熱交換装置は、請求
項1ないし4のいずれかに記載の熱交換装置において、
熱源熱媒体通路を流動する熱源熱媒体の流動方向を水平
方向とするとともに、熱交換管体の両端部を上側にして
この熱交換管体を熱源熱媒体の流動方向と直交する縦方
向の同一面に配設したものである。
According to a fifth aspect of the present invention, there is provided a heat exchanger according to any one of the first to fourth aspects.
The flow direction of the heat source heat medium flowing through the heat source heat medium passage is horizontal, and the heat exchange pipe body is positioned at both ends of the heat exchange pipe body at an upper side, and the heat exchange pipe body is the same in the vertical direction orthogonal to the flow direction of the heat source heat medium. It is arranged on the surface.

【0016】そして、熱源熱媒体通路は高さを低くで
き、建造物の天井近傍に吊り下げ配置でき、設置スペー
スを必要とせず、各熱交換管体は中間部が熱膨脹変形し
ても支障がなく、各熱交換管体を支持する梁などを必要
としない。
The heat source heat medium passage can be reduced in height, can be suspended near the ceiling of the building, does not require an installation space, and each heat exchange pipe does not hinder even if the intermediate portion is thermally expanded and deformed. There is no need for a beam or the like for supporting each heat exchange tube.

【0017】請求項6記載の発明の熱交換装置は、請求
項1ないし4のいずれかに記載の熱交換装置において、
熱源熱媒体通路を流動する熱源熱媒体の流動方向を縦方
向とするとともに、熱交換管体を熱源熱媒体の流動方向
と直交する水平方向の同一面に配設したものである。
According to a sixth aspect of the present invention, there is provided a heat exchanger according to any one of the first to fourth aspects.
The flow direction of the heat source heat medium flowing through the heat source heat medium passage is set to the vertical direction, and the heat exchange tubes are arranged on the same horizontal plane orthogonal to the flow direction of the heat source heat medium.

【0018】そして、熱源熱媒体通路を流動する熱源熱
媒体の流動方向を縦方向としたため、据付面積が少なく
ても容易に設置でき、また、各熱交換管体は両端部を同
一側の導入室および導出室に連通して中間部は固定され
ないためが熱膨脹変形しても支障がない。
Further, since the flow direction of the heat source heat medium flowing through the heat source heat medium passage is set to the vertical direction, the heat source heat medium can be easily installed even if the installation area is small. Since the intermediate portion is not fixed in communication with the chamber and the outlet chamber, there is no problem even if the thermal expansion deformation occurs.

【0019】請求項7記載の発明の熱交換装置は、請求
項6記載の熱交換装置において、各熱交換管体は熱源熱
媒体通路に配設した冷却用空気を流動させるパイプにて
それぞれ支持したものである。
According to a seventh aspect of the present invention, in the heat exchange apparatus of the sixth aspect, each of the heat exchange tubes is supported by a pipe provided in the heat source heat medium passage for flowing cooling air. It was done.

【0020】そして、各熱交換管体は中間部が熱膨脹変
形してもパイプに支持され、中間部が湾曲することがな
く、また、パイプは冷却用空気の流動によって冷却さ
れ、パイプが熱変形されることがなく、各熱交換管体は
確実に支持される。
Each of the heat exchange tubes is supported by the pipe even if the intermediate portion is thermally expanded and deformed, the intermediate portion is not bent, and the pipe is cooled by the flow of cooling air, and the pipe is thermally deformed. Therefore, each heat exchange tube is securely supported.

【0021】[0021]

【発明の実施の形態】本発明の熱交換装置の一実施の形
態の構成を図1ないし図3に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The configuration of an embodiment of the heat exchanger of the present invention will be described with reference to FIGS.

【0022】1は水平方向に配設され縦断面が略矩形形
状の熱源熱媒体通路で、この熱源熱媒体通路1の下流側
に位置する外周上面にこの熱源熱媒体通路1を熱源熱媒
体が流動する水平方向に沿って被熱交換熱媒体の導入室
2が形成され、この導入室2より前記熱源熱媒体通路1
を流動する熱源熱媒体の上流側に位置する外周上面に被
熱交換熱媒体の導出室3が形成されている。
Reference numeral 1 denotes a heat source heat medium passage which is disposed in a horizontal direction and has a substantially rectangular longitudinal section. The heat source heat medium passage 1 is formed on the outer peripheral upper surface located downstream of the heat source heat medium passage 1. An introduction chamber 2 for the heat exchange heat medium is formed along the flowing horizontal direction, and the heat source heat medium passage 1 is formed from the introduction chamber 2.
A heat-exchange heat-medium outlet chamber 3 is formed on the outer peripheral upper surface located upstream of the heat-source heat medium flowing through the heat-exchange medium.

【0023】さらに、前記被熱交換熱媒体の導入室2と
導出室3の両側に位置して熱源熱媒体通路1の外周上面
にこの熱源熱媒体通路1を熱源熱媒体が流動する水平方
向に沿って下流側が導出室となるとともに上流側が導入
室となる導出入室4,4が平行に形成されている。
Further, the heat source heat medium passage 1 is located on both sides of the inlet and outlet chambers 2 and 3 for the heat exchange heat medium in the horizontal direction in which the heat source heat medium flows. Outlet entry chambers 4 and 4 are formed in parallel along the downstream side as the outlet chamber and the upstream side as the inlet chamber.

【0024】また、前記導入室2に一端を連通するとと
もに他端を導出室となる導出入室4,4に連通した一対
の下流側の熱交換管体5,5が前記熱源熱媒体通路1を
流動する熱源熱媒体の流動方向と直交する縦方向の同一
面に垂下して配設され、この各対をなす熱交換管体5,
5が前記熱源熱媒体通路1の熱源熱媒体の流動方向に複
数対が並設され、第1の熱交換部6を形成している。
A pair of downstream heat exchange pipes 5 and 5 having one end communicating with the introduction chamber 2 and the other end communicating with the outlet chambers 4 and 4 serving as outlet chambers, respectively, are connected to the heat source heat medium passage 1. The heat exchange pipes 5, which are vertically suspended on the same plane in the vertical direction orthogonal to the flowing direction of the flowing heat source heat medium,
A plurality of pairs 5 are arranged side by side in the flow direction of the heat source heat medium in the heat source heat medium passage 1 to form a first heat exchange part 6.

【0025】この第1の熱交換部6の各熱交換管体5,
5は前記被熱交換熱媒体の導入室2および導出室となる
導出入室4,4にそれぞれ両端部を接続するとともにこ
の両端部に連続する両側直管部7とこの両側直管部7に
連続する中間部の折り返し部8とを有し、この折り返し
部8は、前記両側直管部7にそれぞれ連続する折り返し
屈曲管部9と、この折り返し屈曲管部9にそれぞれ連続
した中間直管部10,10と、この両中間直管部10,10に連
続する折り返し屈曲管部11とにて略W字状に形成され、
この一対の熱交換管体5,5は前記熱源熱媒体通路1を
流動する熱源熱媒体の流動方向と直交する縦方向の同一
面に垂下して配設されている。
Each of the heat exchange tubes 5, 5 of the first heat exchange section 6
Reference numeral 5 denotes both ends connected to the inlet and outlet chambers 4 and 4 serving as the inlet and outlet chambers 2 and 4 for the heat exchange heat medium, and both straight pipes 7 continuous with the both ends and continuous straight pipes 7 on both sides. And a folded portion 8 which is continuous with the straight tube portions 7 on both sides, and an intermediate straight tube portion 10 which is respectively continuous with the folded tube portion 9. , 10 and a folded tube portion 11 which is continuous with the intermediate straight tube portions 10, 10, and is formed in a substantially W shape.
The pair of heat exchange pipes 5 and 5 are disposed so as to hang down on the same plane in the vertical direction orthogonal to the flow direction of the heat source heat medium flowing in the heat source heat medium passage 1.

【0026】また、前記導入室となる導出入室4,4に
一端を連通するとともに他端を導出室となる導出室3に
連通した一対の上流側の熱交換管体15,15が前記熱源熱
媒体通路1を流動する熱源熱媒体の流動方向と直交する
縦方向の同一面に垂下して配設され、この各対をなす熱
交換管体15,15が前記熱源熱媒体通路1の熱源熱媒体の
流動方向に複数対並設され、第2の熱交換部16を形成し
ている。
A pair of upstream heat exchange tubes 15, 15 having one end communicating with the outlet chambers 4, 4 serving as the introduction chambers and the other end communicating with the outlet chamber 3 serving as the outlet chamber, are connected to the heat source heat source. The heat source heat medium flowing through the medium passage 1 is disposed so as to hang down on the same plane in the vertical direction orthogonal to the flow direction of the heat source heat medium, and the pair of heat exchange tubes 15 A plurality of pairs are arranged in parallel in the flow direction of the medium to form a second heat exchange section 16.

【0027】この第2の熱交換部16の各熱交換管体15,
15は前記被熱交換熱媒体の導入室となる導出入室4,4
と導出室3にそれぞれ両端部を接続するとともにこの両
端部に連続する直管部17とこの両側直管部17に連続する
中間部の折り返し部18とを有し、この折り返し部18は、
前記両側直管部17にそれぞれ連続する折り返し屈曲管部
19と、この折り返し屈曲管部19にそれぞれ連続した中間
直管部20,20と、この両中間直管部20,20に連続する折
り返し屈曲管部21とにて略W字状に形成され、この一対
の熱交換管体15,15は前記熱源熱媒体通路1を流動する
熱源熱媒体の流動方向と直交する同一面に垂下して配設
されている。
Each of the heat exchange tubes 15 of the second heat exchange section 16
15 is a lead-in / out chamber 4, 4 serving as an introduction chamber for the heat exchange heat medium.
Each of the two ends is connected to the outlet chamber 3 and has a straight pipe portion 17 continuing to the both ends and a middle folded portion 18 continuing to the straight pipe portions 17 on both sides.
Folded bent sections that are respectively continuous with the straight pipe sections 17 on both sides
19, an intermediate straight pipe portion 20 and 20 continuous with the folded bent pipe portion 19, and a folded bent pipe portion 21 continuous with the intermediate straight pipe portions 20 and 20 are formed in a substantially W shape. The pair of heat exchange tubes 15, 15 are disposed so as to hang down on the same plane orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage 1.

【0028】そして、この熱源熱媒体通路1にこの熱源
熱媒体通路1を流動する熱源熱媒体の下流側に前記第1
の熱交換部6は前記第2の熱交換部16よりもこの熱源熱
媒体通路1を流動する熱源熱媒体の下流側に配設し、前
記第2の熱交換部16が第1の熱交換部6よりも高温の上
流側に配置されるようになっている。
The first heat medium passage 1 is located downstream of the heat medium flowing through the heat medium passage 1.
The heat exchange section 6 is disposed on the downstream side of the heat source heat medium flowing through the heat source heat medium passage 1 with respect to the second heat exchange section 16, and the second heat exchange section 16 performs the first heat exchange. It is arranged on the upstream side at a higher temperature than the part 6.

【0029】また、前記下流側熱交換管体5、上流側熱
交換管体15はインコネルまたは70%ニッケル・15%クロ
ム合金などの耐熱金属材にて成形する。
The downstream heat exchange tube 5 and the upstream heat exchange tube 15 are formed of a heat-resistant metal material such as Inconel or 70% nickel / 15% chromium alloy.

【0030】次にこの実施の形態の作用を説明する。Next, the operation of this embodiment will be described.

【0031】図2に示すように、熱源熱媒体通路1を流
動する熱源熱媒体の下流側に位置する導入室2に導入さ
れた被熱交換熱媒体は、それぞれこの導入室2に一端を
連通した第1の熱交換部6の複数対の下流側熱交換管体
5にそれぞれ流入して熱源熱媒体通路1を流動する熱源
熱媒体と熱交換されて中温度に加熱された被熱交換熱媒
体となって導出室となる導出入室4,4に流出される。
As shown in FIG. 2, the heat exchange heat medium introduced into the introduction chamber 2 located on the downstream side of the heat source heat medium flowing through the heat source heat medium passage 1 has one end communicating with the introduction chamber 2. The heat exchange heat that has been exchanged with the heat source heat medium flowing into the plurality of pairs of downstream heat exchange tubes 5 of the first heat exchange unit 6 and flowing through the heat source heat medium passage 1 to be heated to an intermediate temperature. The medium flows out to the lead-in / out chambers 4 and 4 serving as the medium.

【0032】そして、熱源熱媒体の流動方向と直交する
同一面にそれぞれ配設した複数対の熱交換管体5,5に
それぞれ流動する被熱交換熱媒体は熱交換管体5,5の
直管部7,7と、この両側直管部7,7に連続する中間
部の折り返し部8の両側直管部7にそれぞれ連続する折
り返し屈曲管部9と、この折り返し屈曲管部9にそれぞ
れ連続した中間直管部10,10と、この両中間直管部10,
10に連続する折り返し屈曲管部11とを流動するときに、
熱源熱媒体と直交流となって熱交換管体5,5の被熱交
換熱媒体は熱交換される。
The heat exchange heat medium flowing in each of the plurality of pairs of heat exchange tubes 5, 5 disposed on the same plane orthogonal to the flow direction of the heat source heat medium is directly in the heat exchange tubes 5, 5. The pipes 7, 7, the folded bent pipes 9 that are respectively continuous with the straight pipes 7 on both sides of the intermediate folded part 8 that is continuous with the straight pipes 7 on both sides, and continuous with the folded bent pipe 9, respectively. Intermediate straight pipe sections 10, 10 and the two intermediate straight pipe sections 10,
When flowing through the bent tube portion 11 that is continuous with 10,
The heat exchange heat medium of the heat exchange tubes 5, 5 is exchanged with the heat source heat medium in a cross flow.

【0033】さらに、図3に示すように、導出室となる
導出入室4,4に流出した被熱交換熱媒体はこの導出入
室4,4に一端を連通した第2の熱交換部16の複数対の
上流側の熱交換管体15,15に流動し、熱源熱媒体通路1
を流動する熱源熱媒体と熱交換されて高温度に加熱され
た被熱交換熱媒体となって導出室3に流出される。
Further, as shown in FIG. 3, the heat-exchanged heat medium flowing out to the lead-in / out chambers 4 and 4 serving as the lead-out chambers is supplied to a plurality of second heat-exchange sections 16 having one ends communicating with the lead-in / out chambers 4 and 4. It flows to the heat exchange pipes 15 and 15 on the upstream side of the pair, and the heat source heat medium passage 1
The heat is exchanged with the heat source heat medium flowing through the heat source, and flows into the outlet chamber 3 as a heat exchange heat medium heated to a high temperature.

【0034】そして、第1の熱交換部6の各下流側熱交
換管体5と第2の熱交換管部16の各上流側熱交換管体15
を流動する被熱交換熱媒体に対し熱源熱媒体通路1を流
動する熱源熱媒体とは直交流となり、熱源熱媒体は各熱
交換管体5,15に接触すると熱交換管体5,15の熱源熱
媒体の上流側に沿った層流から下流側で乱流となり、ま
た、熱源熱媒体の流速が一定の速さ以上になると上流側
でも乱流となって熱交換部6,16での熱交換率が高めら
れる。
Then, each downstream heat exchange pipe 5 of the first heat exchange section 6 and each upstream heat exchange pipe 15 of the second heat exchange pipe 16
The heat exchange heat medium flowing through the heat source heat medium flowing through the heat source heat medium passage 1 has a cross flow with the heat exchange heat medium flowing through the heat exchange heat medium. The laminar flow along the upstream side of the heat source heat medium becomes turbulent on the downstream side, and when the flow velocity of the heat source heat medium exceeds a certain speed, the turbulent flow also occurs on the upstream side, and The heat exchange rate is increased.

【0035】前記熱交換装置をバーナ装置に実施する場
合には、熱源熱媒体は燃焼装置の窯炉内の燃焼部から発
生する燃焼排ガスとなり、被熱交換熱媒体は、予め予熱
される燃焼用酸素含有ガス、例えば空気となる。
When the heat exchange device is applied to a burner device, the heat source heat medium is combustion exhaust gas generated from a combustion portion in a kiln of the combustion device, and the heat exchange heat medium is a preheated combustion medium for combustion. It becomes an oxygen-containing gas, for example, air.

【0036】そして、熱源熱媒体通路1の上流側は燃焼
装置の窯炉内の燃焼部、例えばバーナーに連通され、被
熱交換熱媒体の導出室3は燃焼装置の窯炉内の燃焼部に
連通される。
The upstream side of the heat source heat medium passage 1 is communicated with a combustion part in the kiln of the combustion device, for example, a burner, and the outlet chamber 3 for the heat exchange heat medium is connected to the combustion part in the kiln of the combustion device. Communicated.

【0037】また、熱源熱媒体と被熱交換熱媒体とのい
ずれか一方または両方を液体とすることもできる。
Further, one or both of the heat source heat medium and the heat exchange heat medium can be liquid.

【0038】さらに、前記実施の形態では、被熱交換熱
媒体は第1の熱交換部6および第2の熱交換管部16を流
動して二段階で加熱されるが、一段階で熱交換する熱交
換装置とすることもできる。この一段階の熱交換装置で
は、第1の熱交換部6の一つの被熱交換熱媒体の導入室
2から二つの被熱交換熱媒体の導出室に流出させる構成
とし、または、第2の熱交換部16の二つの被熱交換熱媒
体の導入室2から一つの被熱交換熱媒体の導出室に流出
させる構成とすることもできる。
Furthermore, in the above embodiment, the heat exchange heat medium flows through the first heat exchange section 6 and the second heat exchange pipe section 16 and is heated in two stages. Heat exchange device. In this one-stage heat exchange device, the first heat exchange section 6 is configured to flow from one heat exchange heat medium introduction chamber 2 to two heat exchange heat medium outlet chambers, or It is also possible to adopt a configuration in which the two heat exchange heat transfer medium introduction chambers 2 of the heat exchange section 16 are allowed to flow out into one heat exchange heat transfer medium discharge chamber.

【0039】さらに、前記実施の形態では、前記熱源熱
媒体通路1を流動する熱源熱媒体の流動方向と直交する
縦方向の同一面に一対の熱交換管体5,5または、一対
の熱交換管体15,15を配設したが、前記熱源熱媒体通路
1を流動する熱源熱媒体の流動方向と直交する縦方向の
同一面に一つの熱交換管体5または、一つの熱交換管体
15を配設した構造とすることもできる。
Further, in the above-described embodiment, a pair of heat exchange tubes 5, 5 or a pair of heat exchange tubes are provided on the same surface in the vertical direction orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage 1. Although the pipes 15 and 15 are provided, one heat exchange pipe 5 or one heat exchange pipe is provided on the same vertical surface orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage 1.
It is also possible to adopt a structure in which 15 are provided.

【0040】なお、前記の実施の形態の熱交換装置をバ
ーナ装置に実施する場合では、燃焼排ガスは、約1400℃
程度で、第2の熱交換部16では約1000〜1100℃程度、第
1の熱交換部6を流れるときは被熱交換熱媒体、例えば
燃焼用酸素含有ガスの空気の温度は約600 〜800 ℃程度
となり、窯炉の燃焼部に供給される被熱交換熱媒体の燃
焼用酸素含有ガスの空気の温度は1000〜1100℃程度とな
る。
In the case where the heat exchange device of the above embodiment is applied to a burner device, the combustion exhaust gas has a temperature of about 1400 ° C.
About 1000 to 1100 ° C. in the second heat exchange section 16, and the temperature of the heat exchange heat medium, for example, the air of the oxygen-containing gas for combustion when flowing through the first heat exchange section 6 is about 600 to 800 ° C. ° C, and the temperature of the air of the oxygen-containing gas for combustion of the heat exchange heat medium supplied to the combustion part of the kiln becomes about 1000 to 1100 ° C.

【0041】前記各実施の形態では、被熱交換熱媒体は
低温から高温になるように熱交換する例について説明し
たが、高温から低温に熱交換することもできる。
In each of the above embodiments, an example has been described in which the heat exchange heat medium exchanges heat from a low temperature to a high temperature. However, heat exchange may be performed from a high temperature to a low temperature.

【0042】次に本発明の他の実施の形態を図4ないし
図6について説明する。
Next, another embodiment of the present invention will be described with reference to FIGS.

【0043】30は縦方向に配設され横断面が略矩形形状
の熱源熱媒体通路で、断熱材31にて被覆されている。こ
の熱源熱媒体通路30の下流側に位置する外周前面にこの
熱源熱媒体通路30を熱源熱媒体が流動する縦方向に沿っ
て被熱交換熱媒体の導入室32が形成され、この導入室32
より前記熱源熱媒体通路30を流動する熱源熱媒体の上流
側に位置する外周前面に被熱交換熱媒体の導出室33が形
成されている。
Reference numeral 30 denotes a heat source heat medium passage which is disposed in the vertical direction and has a substantially rectangular cross section, and is covered with a heat insulating material 31. An introduction chamber 32 for the heat exchange heat medium is formed on the outer peripheral front face located downstream of the heat source heat medium path 30 along the longitudinal direction in which the heat source heat medium flows through the heat source heat medium path 30.
An outlet chamber 33 for the heat exchange heat medium is formed on the outer peripheral front surface located on the upstream side of the heat source heat medium flowing through the heat source heat medium passage 30.

【0044】さらに、前記被熱交換熱媒体の導入室32と
導出室33の両側に位置して熱源熱媒体通路30の外周前面
にこの熱源熱媒体通路30を熱源熱媒体が流動する水平方
向に沿って下流側が導出室となるとともに上流側が導入
室となる導出入室34,34が平行に形成されている。
Further, the heat source heat medium passage 30 is positioned on both sides of the heat exchange heat medium introduction chamber 32 and the discharge chamber 33 on the outer peripheral front surface of the heat source heat medium passage 30 in the horizontal direction in which the heat source heat medium flows. Outlet entry chambers 34, 34 are formed in parallel along the downstream side as outlet chambers and the upstream side as inlet chambers.

【0045】また、前記導入室32に一端を連通するとと
もに他端を導出室となる導出入室34,34に連通した一対
の下流側の熱交換管体35,35が前記熱源熱媒体通路30を
流動する熱源熱媒体の流動方向と直交する水平方向の同
一面に配設され、この各対をなす熱交換管体35,35が前
記熱源熱媒体通路30の熱源熱媒体の流動方向に複数対が
並設され、第1の熱交換部36を形成している。
A pair of downstream heat exchange pipes 35, 35, one end of which communicates with the introduction chamber 32 and the other end of which serves as an outlet chamber, communicates with the heat source heat medium passage 30. A plurality of pairs of heat exchange pipes 35, 35 are provided on the same horizontal plane orthogonal to the flowing direction of the flowing heat source heat medium, Are arranged side by side to form a first heat exchange section 36.

【0046】この第1の熱交換部36の各熱交換管体35,
35は前記被熱交換熱媒体の導入室32および導出室となる
導出入室34,34にそれぞれ両端部を接続するとともにこ
の両端部に連続する両側直管部37とこの両側直管部37に
連続する中間部の折り返し部38とを有し、この折り返し
部38は、前記両側直管部37にそれぞれ連続する折り返し
屈曲管部39と、この折り返し屈曲管部39にそれぞれ連続
した中間直管部40,40と、この両中間直管部40,40に連
続する折り返し屈曲管部41とにて略W字状に形成され、
この一対の熱交換管体35,35は前記熱源熱媒体通路30を
流動する熱源熱媒体の流動方向と直交する水平方向の同
一面に配設されている。
Each of the heat exchange tubes 35 of the first heat exchange section 36,
35 has both ends connected to the inlet and outlet chambers 34 and 34 serving as the inlet and outlet chambers 32 and 34 for the heat exchange heat medium, and both straight pipes 37 continuous with both ends and continuous straight pipes 37 on both sides. A folded portion 38 which is continuous with the straight pipe portions 37 on both sides, and an intermediate straight tube portion 40 which is respectively connected to the folded bent portion 39. , 40 and a folded tube portion 41 which is continuous with the intermediate straight tube portions 40, 40, and is formed in a substantially W shape.
The pair of heat exchange tubes 35 are disposed on the same plane in the horizontal direction orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage 30.

【0047】また、前記導入室となる導出入室34,34に
一端を連通するとともに他端を導出室となる導出室33に
連通した一対の上流側の熱交換管体45,45が前記熱源熱
媒体通路30を流動する熱源熱媒体の流動方向と直交する
水平方向の同一面に配設され、この各対をなす熱交換管
体45,45が前記熱源熱媒体通路30の熱源熱媒体の流動方
向に複数対並設され、第2の熱交換部46を形成してい
る。
Further, a pair of upstream heat exchange tubes 45, 45 having one ends communicating with the lead-in / out chambers 34, 34 serving as the introduction chambers and the other end communicating with the lead-out chambers 33 serving as the lead-out chambers, serve as the heat source heat source. The heat exchange pipes 45 are arranged on the same plane in the horizontal direction orthogonal to the flow direction of the heat source heat medium flowing through the medium passage 30, and each pair of heat exchange pipes 45, 45 A plurality of pairs are arranged side by side in the direction to form a second heat exchange section 46.

【0048】この第2の熱交換部46の各熱交換管体45,
45は前記被熱交換熱媒体の導入室となる導出入室34,34
と導出室33にそれぞれ両端部を接続するとともにこの両
端部に連続する直管部47とこの両側直管部47に連続する
中間部の折り返し部48とを有し、この折り返し部48は、
前記両側直管部47にそれぞれ連続する折り返し屈曲管部
49と、この折り返し屈曲管部49にそれぞれ連続した中間
直管部50,50と、この両中間直管部50,50に連続する折
り返し屈曲管部51とにて略W字状に形成され、この一対
の熱交換管体45,45は前記熱源熱媒体通路30を流動する
熱源熱媒体の流動方向と直交する水平方向の同一面に配
設されている。
Each heat exchange pipe 45 of the second heat exchange section 46,
45 is a lead-in / out chamber 34, 34 serving as an introduction chamber for the heat exchange heat medium.
And a straight pipe part 47 connected to both ends of the outlet chamber 33 and a middle folded part 48 continuous with the straight pipe parts 47 on both sides, and the folded part 48 is
Folded bent pipe sections that are respectively continuous with the straight pipe sections 47 on both sides
49, an intermediate straight pipe part 50, 50 continuous with the folded bent pipe part 49, and a folded bent pipe part 51 continuous with the intermediate straight pipe parts 50, 50 are formed in a substantially W shape. The pair of heat exchange tubes 45 are arranged on the same plane in the horizontal direction orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage 30.

【0049】そして、この熱源熱媒体通路30にこの熱源
熱媒体通路30を流動する熱源熱媒体の下流側に前記第1
の熱交換部36は前記第2の熱交換部46よりもこの熱源熱
媒体通路30を流動する熱源熱媒体の下流側に配設し、前
記第2の熱交換部46が第1の熱交換部36よりも高温の上
流側に配置されるようになっている。
The heat source heat medium passage 30 is provided downstream of the heat source heat medium flowing through the heat source heat medium passage 30.
The heat exchange section 36 is disposed on the downstream side of the heat source heat medium flowing through the heat source heat medium passage 30 with respect to the second heat exchange section 46, and the second heat exchange section 46 performs the first heat exchange. It is arranged on the upstream side where the temperature is higher than the part 36.

【0050】また、前記各熱交換管体35,35,45,45の
中間部は前記熱源熱媒体通路30の前後位置に各前記各熱
交換管体35,35,45,45に対応して熱源熱媒体の流動方
向に順次それぞれ配設したパイプ52にてそれぞれ支持さ
れている。この各パイプ52の両端は前記熱源熱媒体通路
30の両側に形成した冷却用空気流入室53と冷却用空気流
出室54とにそれぞれ連通されている。
An intermediate portion of each of the heat exchange tubes 35, 35, 45, 45 is located at a position before and after the heat source heat medium passage 30, corresponding to each of the heat exchange tubes 35, 35, 45, 45. The heat sources are supported by pipes 52 arranged sequentially in the flow direction of the heat medium. Both ends of each pipe 52 are connected to the heat source heat medium passage.
The cooling air inflow chamber 53 and the cooling air outflow chamber 54 formed on both sides of 30 are connected to each other.

【0051】また、前記下流側熱交換管体35、上流側熱
交換管体45もインコネルまたは70%ニッケル・15%クロ
ム合金などの耐熱金属材にて成形する。
The downstream heat exchange tube 35 and the upstream heat exchange tube 45 are also formed of a heat-resistant metal material such as Inconel or 70% nickel / 15% chromium alloy.

【0052】次にこの実施の形態の作用を説明する。Next, the operation of this embodiment will be described.

【0053】図6に示すように、熱源熱媒体通路30を流
動する熱源熱媒体の下流側に位置する導入室32に導入さ
れた被熱交換熱媒体は、実線矢指で示すように、それぞ
れこの導入室32に一端を連通した第1の熱交換部36の複
数対の下流側熱交換管体35にそれぞれ流入して熱源熱媒
体通路30を流動する熱源熱媒体と熱交換されて中温度に
加熱された被熱交換熱媒体となって導出室となる導出入
室34,34に流出される。
As shown in FIG. 6, the heat-exchange heat medium introduced into the introduction chamber 32 located downstream of the heat-source heat medium flowing through the heat-source heat medium passage 30, as indicated by solid arrows, respectively. The heat exchange with the heat source heat medium flowing into the heat source heat medium passages 30 flowing into the heat source heat medium passages 30 by flowing into the plural pairs of downstream heat exchange pipes 35 of the first heat exchange part 36 having one ends communicating with the introduction chambers 32, respectively. The heated heat-exchanged heat medium flows out to the lead-in / out chambers 34, 34 serving as the outlet chambers.

【0054】そして、熱源熱媒体の流動方向と直交する
同一面にそれぞれ配設した複数対の熱交換管体35,35に
それぞれ流動する被熱交換熱媒体は熱交換管体35,35の
直管部37,37と、この両側直管部37,37に連続する中間
部の折り返し部38の両側直管部37にそれぞれ連続する折
り返し屈曲管部39と、この折り返し屈曲管部39にそれぞ
れ連続した中間直管部40,40と、この両中間直管部40,
40に連続する折り返し屈曲管部41とを流動するときに、
熱源熱媒体と直交流となって熱交換管体35,35の被熱交
換熱媒体は熱交換される。
The heat exchange heat medium flowing through the plurality of pairs of heat exchange tubes 35, 35 respectively disposed on the same plane orthogonal to the flow direction of the heat source heat medium is directly transferred to the heat exchange tubes 35, 35. The pipes 37, 37, the folded bent pipes 39 that are continuous with the straight pipes 37 on both sides of the intermediate folded part 38 that is continuous with the straight pipes 37, 37 on both sides, and the bent bent pipe 39 that is continuous with the folded bent pipe 39, respectively. Intermediate straight pipe sections 40, 40, and both intermediate straight pipe sections 40, 40
When flowing with the folded tube portion 41 continuous with 40,
The heat exchange heat medium of the heat exchange tubes 35 is exchanged with the heat source heat medium in a cross flow.

【0055】さらに、図6に鎖線矢指で示すように、導
出室となる導出入室34,34に流出した被熱交換熱媒体は
この導出入室34,34に一端を連通した第2の熱交換部46
の複数対の上流側の熱交換管体45,45に流動し、熱源熱
媒体通路30を流動する熱源熱媒体と熱交換されて高温度
に加熱された被熱交換熱媒体となって導出室33に流出さ
れる。
Further, as shown by a chain line arrow in FIG. 6, the heat-exchanged heat medium flowing out to the lead-in / out chambers 34, 34 serving as the lead-out chambers is supplied to the second heat-exchange section having one end communicating with the lead-in / out chambers 34, 34. 46
Flows into a plurality of pairs of heat exchange tubes 45, 45 on the upstream side, and exchanges heat with the heat source heat medium flowing through the heat source heat medium passage 30 to become a heat exchange heat medium heated to a high temperature to the outlet chamber. Spilled to 33.

【0056】そして、第1の熱交換部36の各下流側熱交
換管体35と第2の熱交換管部46の各上流側熱交換管体45
を流動する被熱交換熱媒体に対し熱源熱媒体通路30を流
動する熱源熱媒体とは直交流となり、熱源熱媒体は各熱
交換管体35,45に接触すると熱交換管体35,45の熱源熱
媒体の上流側に沿った層流から下流側で乱流となり、ま
た、熱源熱媒体の流速が一定の速さ以上になると上流側
でも乱流となって熱交換部36,46での熱交換率が高めら
れる。
Then, each downstream heat exchange pipe 35 of the first heat exchange section 36 and each upstream heat exchange pipe 45 of the second heat exchange pipe 46
The heat exchange heat medium flowing through the heat source heat medium flowing through the heat source heat medium passage 30 has a cross flow with the heat exchange heat medium, and when the heat source heat medium contacts the heat exchange tubes 35 and 45, the heat exchange tubes 35 and 45 The laminar flow along the upstream side of the heat source heat medium becomes turbulent on the downstream side, and when the flow velocity of the heat source heat medium exceeds a certain speed, it becomes turbulent on the upstream side as well, and The heat exchange rate is increased.

【0057】前記熱交換装置をバーナ装置に実施する場
合には、熱源熱媒体は燃焼装置の窯炉内の燃焼部から発
生する燃焼排ガスとなり、被熱交換熱媒体は、予め予熱
される燃焼用酸素含有ガス、例えば空気となる。
When the heat exchange device is applied to a burner device, the heat source heat medium is the combustion exhaust gas generated from the combustion portion in the kiln of the combustion device, and the heat exchange heat medium is a preheated combustion heat medium. It becomes an oxygen-containing gas, for example, air.

【0058】そして、熱源熱媒体通路30の上流側は燃焼
装置の窯炉内の燃焼部、例えばバーナーに連通され、被
熱交換熱媒体の導出室33は燃焼装置の窯炉内の燃焼部に
連通される。
The upstream side of the heat source heat medium passage 30 is communicated with a combustion section in the kiln of the combustion apparatus, for example, a burner, and the outlet chamber 33 for the heat exchange heat medium is connected to the combustion section in the kiln of the combustion apparatus. Communicated.

【0059】さらに、前記熱交換管体35,45をそれぞれ
支持したパイプ52には冷却用空気流入室53から流入した
冷却用空気が流動して冷却用空気流出室54に流出される
ため、パイプ52は熱変形することなく、確実に熱交換管
体35,45を支持する。
Further, the cooling air flowing from the cooling air inflow chamber 53 flows into the pipe 52 supporting the heat exchange pipes 35 and 45, respectively, and flows out to the cooling air outflow chamber 54. 52 reliably supports the heat exchange tubes 35 and 45 without thermal deformation.

【0060】また、熱源熱媒体と被熱交換熱媒体とのい
ずれか一方または両方を液体とすることもできる。
Further, one or both of the heat source heat medium and the heat exchange heat medium may be liquid.

【0061】さらに、前記実施の形態では、被熱交換熱
媒体は第1の熱交換部36および第2の熱交換管部46を流
動して二段階で加熱されるが、一段階で熱交換する熱交
換装置とすることもできる。この一段階の熱交換装置で
は、第1の熱交換部36の一つの被熱交換熱媒体の導入室
32から二つの被熱交換熱媒体の導出室に流出させる構成
とし、または、第2の熱交換部46の二つの被熱交換熱媒
体の導入室32から一つの被熱交換熱媒体の導出室に流出
させる構成とすることもできる。
Further, in the above embodiment, the heat exchange heat medium flows through the first heat exchange section 36 and the second heat exchange pipe section 46 and is heated in two stages. Heat exchange device. In this one-stage heat exchange apparatus, one of the first heat exchange units 36 has an introduction chamber for the heat exchange heat medium.
It is configured to flow out of the two heat exchange heat mediums to the outlet chambers of the two heat exchange heat mediums from the second heat exchange heat medium introduction chamber 32 of the second heat exchange unit 46. It is also possible to adopt a configuration in which the fluid is discharged to

【0062】なお、この実施の形態の熱交換装置をバー
ナ装置に実施する場合では、燃焼排ガスは、約1400℃程
度で、第2の熱交換部46では約1000〜1100℃程度、第1
の熱交換部36を流れるときは被熱交換熱媒体の温度は約
600 〜800 ℃程度となり、窯炉の燃焼部に供給される被
熱交換熱媒体の燃焼燃焼用酸素含有ガスの空気の温度は
1000〜1100℃程度となる。
When the heat exchange device of this embodiment is applied to a burner device, the combustion exhaust gas is about 1400 ° C., and the second heat exchange section 46 is about 1000 to 1100 ° C.
When flowing through the heat exchange section 36, the temperature of the heat exchange heat medium
The temperature of the oxygen-containing gas for combustion and combustion of the heat exchange heat medium supplied to the combustion part of the kiln is about 600 to 800 ° C.
It will be around 1000-1100 ° C.

【0063】前記各実施の形態では、被熱交換熱媒体は
低温から高温になるように熱交換する例について説明し
たが、高温から低温に熱交換することもできる。
In each of the above embodiments, an example has been described in which the heat exchange heat medium exchanges heat from a low temperature to a high temperature. However, heat exchange may be performed from a high temperature to a low temperature.

【0064】[0064]

【発明の効果】請求項1に記載の発明によれば、被熱交
換熱媒体の導入室に導入された被熱交換熱媒体は、複数
の熱交換管体を流動して熱源熱媒体通路を流動する熱源
熱媒体と熱交換し、被熱交換熱媒体は加熱されて導出室
に流出され、この熱交換管体を流れる被熱交換熱媒体は
熱交換管体の全域において熱源熱媒体通路を流れる熱源
熱媒体とは直交流となり、熱交換効率が高められ、熱効
率が向上する。さらに各熱交換管体は折り返し部の折り
返し屈曲部が多くなり、熱膨脹による撓み変形が生じに
くく、熱交換管体が折損することがなく、超高温の熱交
換に有利である。
According to the first aspect of the present invention, the heat-exchange heat medium introduced into the heat-exchange heat-medium introduction chamber flows through the plurality of heat exchange pipes and passes through the heat-source heat medium passage. The heat exchange heat medium exchanges heat with the flowing heat source heat medium, the heat exchange heat medium is heated and flows out to the outlet chamber, and the heat exchange heat medium flowing through the heat exchange tube passes through the heat source heat medium passage in the entire area of the heat exchange tube. The flowing heat source heat medium becomes a direct flow, the heat exchange efficiency is increased, and the heat efficiency is improved. Further, each heat exchange tube has a large number of folded portions in the folded portion, so that the heat exchange tube is less likely to be deformed by thermal expansion, and the heat exchange tube is not broken, which is advantageous for heat exchange at an ultra-high temperature.

【0065】請求項2記載の発明によれば、熱源熱媒体
の流動方向と直交する同一面にそれぞれ配設した複数対
の熱交換管体にそれぞれ流動する被熱交換熱媒体は熱交
換管体の直管部とこの両側直管部に連続する中間部を折
り返し部とを流動するときに熱源熱媒体と直交流とな
り、熱交換効率が高められ、熱効率が向上する。
According to the second aspect of the present invention, the heat exchange heat medium flowing through the plurality of pairs of heat exchange pipes respectively arranged on the same surface orthogonal to the flow direction of the heat source heat medium is a heat exchange pipe. When flowing through the straight pipe portion and the intermediate portion that is continuous with the straight pipe portions on both sides, the flow becomes a direct flow with the heat source heat medium, the heat exchange efficiency is increased, and the heat efficiency is improved.

【0066】請求項3記載の発明によれば、熱源熱媒体
の流動方向と直交する同一面にそれぞれ配設した複数対
の熱交換管体にそれぞれ流動する被熱交換熱媒体は熱交
換管体の直管部とこの両側直管部に連続する中間部を折
り返し部とを流動するときに熱源熱媒体と直交流とな
り、熱交換効率が高められ、熱効率が向上する。
According to the third aspect of the present invention, the heat exchange heat medium flowing through the plurality of pairs of heat exchange pipes respectively arranged on the same surface orthogonal to the flow direction of the heat source heat medium is a heat exchange pipe. When flowing through the straight pipe portion and the intermediate portion that is continuous with the straight pipe portions on both sides, the flow becomes a direct flow with the heat source heat medium, the heat exchange efficiency is increased, and the heat efficiency is improved.

【0067】請求項4記載の発明によれば、被熱交換熱
媒体の導入室に流入した第1の熱交換部の被熱交換熱媒
体はそれぞれ各熱交換管体を流動し、熱源熱媒体通路を
流動する熱源熱媒体と熱交換し、被熱交換熱媒体は中温
に加熱されて導入室の両側に配設された導出室に流出さ
れ、さらに、この両導出室にそれぞれ連通する導入室か
ら第2の熱交換部の各熱交換管体を流動し、熱源熱媒体
通路の第1の熱交換部の配設位置より上流側で熱源熱媒
体通路を流動する熱源熱媒体と熱交換し、被熱交換熱媒
体はさらに高温に加熱されて両導入室の間に配設された
導出室に流出され、第1および第2の熱交換部にて、熱
源熱媒体の流動方向と直交する同一面にそれぞれ配設し
た複数対の熱交換管体にそれぞれ流動する被熱交換熱媒
体は熱交換管体の直管部とこの両側直管部に連続する中
間部の折り返し部とを流動するときに熱源熱媒体と直交
流となり、熱交換効率が高められ、熱効率が向上する。
According to the fourth aspect of the present invention, the heat exchange heat medium of the first heat exchange section which has flowed into the introduction chamber of the heat exchange heat medium flows through each heat exchange tube, and the heat source heat medium The heat exchange medium exchanges heat with the heat source heat medium flowing through the passage, and the heat exchange heat medium is heated to a medium temperature and flows out to the outlet chambers arranged on both sides of the inlet chamber, and further, the inlet chambers communicating with the outlet chambers, respectively. Flows through the respective heat exchange tubes of the second heat exchange unit, and exchanges heat with the heat source heat medium flowing through the heat source heat medium passage at a position upstream of the position of the first heat exchange unit in the heat source heat medium passage. The heat exchange heat medium is further heated to a high temperature and flows out to the outlet chamber disposed between the two introduction chambers, and is orthogonal to the flow direction of the heat source heat medium in the first and second heat exchange units. The heat exchange heat medium flowing in each of a plurality of pairs of heat exchange tubes arranged on the same surface is a heat exchange tube. Becomes a heat source heat medium and the cross when flowing through the folded portion of the intermediate portion which is continuous with the tube portion to the both side straight pipe portion, the heat exchange efficiency is increased, thereby improving the thermal efficiency.

【0068】請求項5記載の発明によれば、熱源熱媒体
通路を流動する熱源熱媒体の流動方向を縦方向としたた
め、熱源熱媒体通路は高さを低くでき、建造物の天井近
傍に吊り下げ配置でき、熱交換装置の設置スペースを必
要とせず、各熱交換管体は中間部が熱膨脹変形しても支
障がなく、各熱交換管体を支持する梁などを必要としな
い。
According to the fifth aspect of the present invention, since the flow direction of the heat source heat medium flowing through the heat source heat medium passage is set to the vertical direction, the height of the heat source heat medium passage can be reduced, and the heat source heat medium passage can be suspended near the ceiling of the building. It can be placed down, does not require the installation space of the heat exchange device, does not hinder each heat exchange tube even if the middle part is thermally expanded and deformed, and does not need a beam for supporting each heat exchange tube.

【0069】請求項6記載の発明によれば、熱源熱媒体
通路を流動する熱源熱媒体の流動方向を縦方向としたた
め、据付面積が少なくても容易に設置でき、また、各熱
交換管体は両端部を同一側の導入室および導出室に連通
して中間部は固定されないためが熱膨脹変形しても支障
がない。
According to the sixth aspect of the present invention, since the flow direction of the heat source heat medium flowing through the heat source heat medium passage is set to the vertical direction, the heat source heat medium can be easily installed even if the installation area is small. Since both ends communicate with the introduction chamber and the extraction chamber on the same side and the intermediate part is not fixed, there is no problem even if the thermal expansion deformation occurs.

【0070】請求項7記載の発明によれば、各熱交換管
体は中間部が熱膨脹変形してもパイプに支持され、中間
部が湾曲することがなく、また、パイプは冷却用空気の
流動によって冷却され、パイプが熱変形されることがな
く、各熱交換管体は確実に支持される。
According to the seventh aspect of the present invention, each heat exchange tube is supported by the pipe even if the intermediate portion is thermally expanded and deformed, the intermediate portion does not bend, and the pipe is formed by the flow of cooling air. Thus, the pipes are not thermally deformed, and each heat exchange tube is securely supported.

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

【図1】本発明の一実施の形態を示す熱交換装置の一部
を切り欠いた斜視図である。
FIG. 1 is a partially cutaway perspective view of a heat exchange device according to an embodiment of the present invention.

【図2】同上第1の熱交換部の縦断面図である。FIG. 2 is a vertical cross-sectional view of the first heat exchange unit.

【図3】同上第2の熱交換部の縦断面図である。FIG. 3 is a longitudinal sectional view of a second heat exchange unit according to the first embodiment.

【図4】本発明の他の実施の形態を示す熱交換装置の横
断平面図である。
FIG. 4 is a cross-sectional plan view of a heat exchange device showing another embodiment of the present invention.

【図5】同上熱交換装置の正面図である。FIG. 5 is a front view of the heat exchange device.

【図6】同上熱交換装置の縦断正面図である。FIG. 6 is a vertical sectional front view of the same heat exchanger.

【符号の説明】[Explanation of symbols]

1,30 熱源熱媒体通路 2,32 導入室 3,33 導出室 4,34 導入室および導出室となる導出入室 5,15,35,45 熱交換管体 6,36 第1の熱交換部 7,17,37,47 直管部 8,18,38,48 折り返し部 9,19,39,49 折り返し屈曲管部 10,20,40,50 中間直管部 11,21,41,51 折り返し屈曲管部 16,46 第2の熱交換部 52 パイプ 1,30 Heat source heat medium passage 2,32 Inlet chamber 3,33 Outlet chamber 4,34 Outlet inlet and outlet chamber 5,15,35,45 Heat exchange tube 6,36 First heat exchange part 7 , 17,37,47 Straight pipe section 8,18,38,48 Folded section 9,19,39,49 Folded bent pipe section 10,20,40,50 Intermediate straight pipe section 11,21,41,51 Folded bent pipe Part 16, 46 Second heat exchange part 52 Pipe

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 熱源熱媒体通路と、この熱媒体通路の熱
源熱媒体の流動方向に沿って設けられた被熱交換熱媒体
の導入室および導出室と、前記熱源熱媒体通路内にこの
熱源熱媒体通路を流動する熱源熱媒体の流動方向に並設
されかつ両端部をそれぞれ前記被熱交換熱媒体の導入室
および導出室に連通された被熱交換熱媒体を流動させる
複数の熱交換管体とを備え、 前記各熱交換管体は、前記被熱交換熱媒体の導入室およ
び導出室に両端部を接続するとともにこの両端部に連続
する直管部とこの両側直管部に連続する中間部の折り返
し部とを有し、この各熱交換管体の折り返し部は、両側
直管部にそれぞれ連続する折り返し屈曲管部と、この折
り返し屈曲管部にそれぞれ連続した中間直管部と、この
両中間直管部に連続する折り返し屈曲管部とにて形成
し、前記各熱交換管体の直管部と折り返し部とを前記熱
源熱媒体通路を流動する熱源熱媒体の流動方向と直交す
る同一面に配設したことを特徴とする熱交換装置。
1. A heat source heat medium passage, an introduction chamber and a discharge chamber of a heat exchange heat medium provided along the flow direction of the heat source heat medium in the heat medium passage, and the heat source in the heat source heat medium passage. A plurality of heat exchange pipes which are arranged in parallel in the flow direction of the heat source heat medium flowing through the heat medium passage, and whose both ends flow through the heat exchange heat medium communicated with the introduction chamber and the discharge chamber of the heat exchange heat medium. And each of the heat exchange pipes has both ends connected to the introduction chamber and the discharge chamber of the heat exchange heat medium, and is connected to the straight pipes continuous with the both ends and the straight pipes on both sides. The intermediate portion has a folded portion, and the folded portion of each heat exchange tube body is a folded bent tube portion continuous to both straight tube portions, and an intermediate straight tube portion respectively continuous to the folded bent tube portion, A folded bent tube section that is continuous with both intermediate straight pipe sections Wherein the straight pipe portion and the folded portion of each of the heat exchange pipes are arranged on the same plane orthogonal to the flow direction of the heat source heat medium flowing through the heat source heat medium passage. .
【請求項2】 被熱交換熱媒体の導入室を両側にそれぞ
れ配設し、この両側の導入室の中間部に被熱交換熱媒体
の導出室を形成し、この両側の被熱交換熱媒体の導入室
にそれぞれ熱交換管体の一端部を連通させるとともに中
間部の導出室にそれぞれこの熱交換管体の他端部を接続
し、この一対の熱交換管体を熱源熱媒体通路にこの熱源
熱媒体通路を流動する熱源熱媒体の流動方向と直交する
同一面にそれぞれ配設したことを特徴とする請求項1記
載の熱交換装置。
2. An introduction chamber for a heat exchange heat medium is disposed on each side, and a discharge chamber for a heat exchange heat medium is formed at an intermediate portion between the introduction chambers on both sides. The other end of the heat exchange tube is connected to the intermediate chamber and the other end of the heat exchange tube is connected to the introduction chamber of the intermediate portion. The heat exchange device according to claim 1, wherein the heat source heat medium flowing in the heat source heat medium passage is disposed on the same surface orthogonal to the flow direction of the heat source heat medium.
【請求項3】 被熱交換熱媒体の導出室を両側にそれぞ
れ配設し、この両側の導出室の中間部に被熱交換熱媒体
の導入室を形成し、この中間の被熱交換熱媒体の導入室
にそれぞれ熱交換管体の一端部を連通させるとともに両
側の導出室にそれぞれこの熱交換管体の他端部を接続
し、この一対の熱交換管体を熱源熱媒体通路にこの熱源
熱媒体通路を流動する熱源熱媒体の流動方向と直交する
同一面にそれぞれ配設したことを特徴とする請求項1記
載の熱交換装置。
3. An outlet chamber for a heat-exchange heat medium is disposed on each side, and an inlet chamber for the heat-exchange heat medium is formed at an intermediate portion between the outlet chambers on both sides. One end of the heat exchange tube is communicated with each of the introduction chambers, and the other end of the heat exchange tube is connected to each of the outlet chambers on both sides, and the pair of heat exchange tubes are connected to the heat source heat medium passage with the heat source. The heat exchange device according to claim 1, wherein the heat source heat medium flowing in the heat medium passage is disposed on the same surface orthogonal to the flow direction of the heat source heat medium.
【請求項4】 被熱交換熱媒体の導入室の両側にそれぞ
れ被熱交換熱媒体の導出室を形成し、この中間の被熱交
換熱媒体の導入室にそれぞれ熱交換管体の一端部を連通
させるとともに両側の導出室にそれぞれこの熱交換管体
の他端部を接続し、この一対の熱交換管体を熱源熱媒体
通路にこの熱源熱媒体通路を流動する熱源熱媒体の流動
方向と直交する同一面にそれぞれ配設して第1の熱交換
部を形成し、 この両側の導出室に連通する導入室を両側にそれぞれ配
設し、この導入室の中間部に被熱交換熱媒体の導出室を
形成し、この両側の被熱交換熱媒体の導入室にそれぞれ
熱交換管体の一端部を連通させるとともに中間部の導出
室にそれぞれこの熱交換管体の他端部を接続し、この複
数対の熱交換管体を前記熱源熱媒体通路にこの熱源熱媒
体通路を流動する熱源熱媒体の流動方向と直交する同一
面にそれぞれ配設して第2の熱交換部を形成し、 前記熱源熱媒体通路にこの熱源熱媒体通路を流動する熱
源熱媒体の下流側に前記第1の熱交換部を配設するとと
もに前記第2の熱交換部をこの熱源熱媒体通路を流動す
る熱源熱媒体の上流側に配設したことを特徴とする請求
項1記載の熱交換装置。
4. An outlet chamber for a heat-exchange heat medium is formed on each side of the heat-exchange heat-medium introduction chamber, and one end of each heat-exchange tube is inserted into the intermediate heat-exchange heat-medium introduction chamber. The other ends of the heat exchange tubes are connected to the outlet chambers on both sides, respectively, and the pair of heat exchange tubes are connected to the heat source heat medium passage in the flow direction of the heat source heat medium flowing through the heat source heat medium passage. A first heat exchange portion is formed by arranging the first heat exchange portions on the same surface orthogonal to each other. Introducing chambers communicating with the outlet chambers on both sides are respectively disposed on both sides, and a heat exchange heat medium is provided in an intermediate portion of the introducing chambers. Are connected to one end of each heat exchange tube with the introduction chamber of the heat exchange heat medium on both sides, and the other end of each heat exchange tube is connected to the intermediate chamber. And passing the plurality of pairs of heat exchange tubes through the heat source heat medium passage. Are disposed on the same plane orthogonal to the flow direction of the heat source heat medium flowing therethrough to form a second heat exchange portion, and the heat source heat medium passage is downstream of the heat source heat medium flowing through the heat source heat medium passage. 2. The heat according to claim 1, wherein the first heat exchanging section is disposed on the upstream side of the heat source heat medium flowing through the heat source heat medium passage. Exchange equipment.
【請求項5】 熱源熱媒体通路を流動する熱源熱媒体の
流動方向を水平方向とするとともに、熱交換管体の両端
部を上側にしてこの熱交換管体を熱源熱媒体の流動方向
と直交する縦方向の同一面に配設したことを特徴とする
請求項1ないし4のいずれかに記載の熱交換装置。
5. The flow direction of the heat source heat medium flowing in the heat source heat medium passage is horizontal, and the heat exchange tube body is oriented orthogonally to the flow direction of the heat source heat medium with both ends of the heat exchange tube body facing upward. The heat exchange device according to any one of claims 1 to 4, wherein the heat exchange device is arranged on the same vertical surface.
【請求項6】 熱源熱媒体通路を流動する熱源熱媒体の
流動方向を縦方向とするとともに、熱交換管体を熱源熱
媒体の流動方向と直交する水平方向の同一面に配設した
ことを特徴とする請求項1ないし4のいずれかに記載の
熱交換装置。
6. A heat source heat medium flowing in a heat source heat medium passage, wherein the flow direction of the heat source heat medium is vertical, and the heat exchange tube is disposed on the same horizontal plane orthogonal to the flow direction of the heat source heat medium. The heat exchange device according to any one of claims 1 to 4, wherein:
【請求項7】 各熱交換管体は熱源熱媒体通路に配設し
た冷却用空気を流動させるパイプにてそれぞれ支持した
ことを特徴とする請求項6記載の熱交換装置。
7. The heat exchange apparatus according to claim 6, wherein each heat exchange pipe is supported by a pipe provided in the heat source heat medium passage for flowing cooling air.
JP28212797A 1997-08-04 1997-10-15 Heat exchanger Pending JPH11108570A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28212797A JPH11108570A (en) 1997-08-04 1997-10-15 Heat exchanger

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP20929997 1997-08-04
JP9-209299 1997-08-04
JP28212797A JPH11108570A (en) 1997-08-04 1997-10-15 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH11108570A true JPH11108570A (en) 1999-04-23

Family

ID=26517360

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28212797A Pending JPH11108570A (en) 1997-08-04 1997-10-15 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH11108570A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105021067A (en) * 2015-08-17 2015-11-04 杨胜东 Large-particle straight-through waste water heat exchanger and heat exchange system with same
CN105737182A (en) * 2016-04-25 2016-07-06 长沙为明节能科技有限公司 Smoke in-depth cooler
CN114199052A (en) * 2021-12-23 2022-03-18 北京瑞晨航宇能源科技有限公司 Pure countercurrent heat exchanger with working condition adaptability

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105021067A (en) * 2015-08-17 2015-11-04 杨胜东 Large-particle straight-through waste water heat exchanger and heat exchange system with same
CN105737182A (en) * 2016-04-25 2016-07-06 长沙为明节能科技有限公司 Smoke in-depth cooler
CN114199052A (en) * 2021-12-23 2022-03-18 北京瑞晨航宇能源科技有限公司 Pure countercurrent heat exchanger with working condition adaptability

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