JPH1163859A - Heat exchanger and burner - Google Patents

Heat exchanger and burner

Info

Publication number
JPH1163859A
JPH1163859A JP9226258A JP22625897A JPH1163859A JP H1163859 A JPH1163859 A JP H1163859A JP 9226258 A JP9226258 A JP 9226258A JP 22625897 A JP22625897 A JP 22625897A JP H1163859 A JPH1163859 A JP H1163859A
Authority
JP
Japan
Prior art keywords
heat
heat exchange
heat medium
section
combustion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP9226258A
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 JP9226258A priority Critical patent/JPH1163859A/en
Publication of JPH1163859A publication Critical patent/JPH1163859A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Abstract

PROBLEM TO BE SOLVED: To effect heat exchange with a good thermal efficiency between a heating medium to be heat-exchanged such as gas containing oxygen for combustion and a heat source heating medium such as a combustion exhaust gas. SOLUTION: An introduction chamber 2 for a heating medium to be heat-exchanged and a discharge chamber 3 therefor are parallely formed along a heat source heating medium passage 1 on an outer periphery of the heat source heating medium passage. Introduction side vertical heat-exchanger pipe parts 4 composed of a plurality of pipe bodies 6 to be heat-exchanged, which are respectively allowed to communicate with the introduction chamber 2 at one end of each of them, and a plurality of discharge side vertical heat-exchanger pipe parts 5, which are respectively allowed to communicate with the discharge chamber 3 at one end of each of them, are provided parallely in a direction in which the heating medium in the heating medium passage 1 flows. The other end of each introduction side heat-exchanger pipe part 4 and the other end of each discharge side heat-exchanger pipe part 5 communicate with each other in such a manner that the heat-exchanger pipe parts 4 positioned on the downstream side are allowed to communicate in the order of position from the upstream side of the heat source heating medium passage 1 toward the downstream side thereof, and that the discharge side heat-exchanger pipe parts 5 are allowed to communicate in the order of position from the downstream side of the heating medium passage 1 toward the upstream side thereof.

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、ガラス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
置およびバーナ装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat medium for heat exchange with a heat medium for heat exchange, for example, in a steel heating furnace, a heat treatment furnace, a glass melting furnace, etc. The present invention relates to a heat exchange device and a burner device for exchanging heat with heat.

【0002】[0002]

【従来の技術】従来のこの種のバーナ装置において、燃
焼用酸素含有ガスを予熱する熱交換器は、燃焼排ガスの
排ガス通路に複数本の直線状熱交換管体を燃焼排ガスに
対して向流方向に配設し、この熱交換管体を流動する燃
焼用酸素含有ガスを燃焼排ガスと熱交換により加熱して
予熱された酸素含有ガスを燃焼部に供給する構造が採ら
れていた。
2. Description of the Related Art In a conventional burner apparatus of this type, a heat exchanger for preheating an oxygen-containing gas for combustion comprises a plurality of straight heat exchange tubes flowing in a flue gas passage of the flue gas in a counterflow direction with respect to the flue gas. In this configuration, the combustion oxygen-containing gas flowing through the heat exchange tube is heated by heat exchange with the combustion exhaust gas to supply a preheated oxygen-containing gas to the combustion section.

【0003】[0003]

【発明が解決しようとする課題】上記従来のバーナ装置
における熱交換器は、直線状熱交換管体は燃焼排ガスの
流動方向の上流側と下流側とでは温度分布が異なり、熱
交換管体が熱損傷され易い問題があった。
In the heat exchanger of the above-mentioned conventional burner device, the linear heat exchange tube has a different temperature distribution between the upstream side and the downstream side in the flow direction of the combustion exhaust gas. There was a problem of being easily damaged by heat.

【0004】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
換装置およびバーナ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 has an object to provide a heat exchange device and a burner device capable of efficiently exchanging a heat exchange heat medium such as oxygen-containing gas for combustion with a heat source heat medium such as combustion exhaust gas. To provide.

【0005】[0005]

【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、この熱源熱媒体通路
の外周に沿ってこの熱源熱媒体通路を流動する熱源熱媒
体の流動方向に対して並設された被熱交換熱媒体の導入
室および導出室と、前記被熱交換熱媒体の導入室と導出
室とに両端部を連通接続して前記熱源熱媒体通路に配設
され被熱交換熱媒体が流動する複数の被熱交換管体とを
備えている。
According to a first aspect of the present invention, there is provided a heat exchange apparatus comprising: a heat source heat medium passage; and a heat source heat medium flowing along the outer periphery of the heat source heat medium passage. Both ends of the heat exchange heat medium introduction chamber and discharge chamber, which are arranged in parallel with the flow direction, and the heat exchange heat medium introduction chamber and the discharge chamber are connected to each other at the heat source heat medium passage. And a plurality of heat exchange tubes through which the heat exchange heat medium flows.

【0006】また、前記各被熱交換管体は、前記被熱交
換熱媒体の導入室にそれぞれ外周側端部を連通接続し前
記熱源熱媒体通路の熱源熱媒体の流動方向に対して直交
する面に配設される渦巻状の導入側熱交換管部と、前記
被熱交換熱媒体の導出室にそれぞれ外周側端部を連通接
続し前記熱源熱媒体通路の熱源熱媒体の流動方向に対し
て直交する面に配設される渦巻状の導出側熱交換管部
と、前記導入側熱交換管部と導出側熱交換管部との内周
側端部を互いに連通接続し前記熱源熱媒体通路を流動す
る熱源熱媒体の流動方向に配設される直線状の連通管部
とを有している。
[0006] Each of the heat exchange pipes has an outer peripheral end connected to the introduction chamber of the heat exchange heat medium, and is orthogonal to the flow direction of the heat source heat medium in the heat source heat medium passage. A spiral inlet-side heat exchange tube portion disposed on the surface, and an outer peripheral end portion connected to the outlet chamber of the heat-exchanged heat medium, respectively, and connected to the flow direction of the heat-source heat medium in the heat-source heat medium passage. A spiral outlet-side heat exchange tube portion, which is disposed on a surface orthogonal to the bottom surface, and inner peripheral ends of the inlet-side heat exchange tube portion and the outlet-side heat exchange tube portion, which are connected to each other to connect the heat source heat medium. And a linear communication pipe disposed in the flow direction of the heat source heat medium flowing through the passage.

【0007】さらに、前記各被熱交換管体の導入側熱交
換管部と導出側熱交換管部とを連通接続する連通管部の
長さをそれぞれ異なる長さとし、この連通管部の長さが
長い被熱交換管体の導入側熱交換管部と導出側熱交換管
部との間に連通管部の長さが短い被熱交換管体の導入側
熱交換管部と導出側熱交換管部を順次に配設して複数の
被熱交換管体の導入側熱交換管部と導出側熱交換管部と
を前記熱媒体通路の熱源熱媒体の流動方向に並設したも
のである。
Further, the lengths of the communicating pipes for connecting and connecting the inlet side heat exchanging pipes and the outlet side heat exchanging pipes of the respective heat exchanged pipes are different from each other, and the lengths of the communicating pipes are different. Between the inlet and outlet heat exchange pipe sections of the heat exchange pipe section having a longer length, and the inlet and outlet heat exchange sections of the heat exchange pipe section having a shorter length. The pipe sections are sequentially arranged, and the inlet-side heat exchange pipe section and the outlet-side heat exchange pipe section of the plurality of heat exchange pipes are arranged in parallel with the flow direction of the heat source heat medium in the heat medium passage. .

【0008】そして、導入室に導入された被熱交換熱媒
体は、それぞれこの導入室に外周側端部を連通した複数
の熱交換管体の渦巻状の導入側熱交換管部にそれぞれ流
入して熱媒体通路を流動する熱源熱媒体と熱交換され、
さらに、各導出側熱交換管部の内周側端部に連通された
各連通管部を経て熱源熱媒体と熱交換されながら導出側
熱交換管部に流動して導出部に流出される。
The heat-exchange heat medium introduced into the introduction chamber flows into the spiral introduction-side heat exchange pipe sections of a plurality of heat exchange pipe bodies each having an outer peripheral end communicating with the introduction chamber. Heat exchange with the heat source heat medium flowing through the heat medium passage,
Further, the heat is exchanged with the heat source heat medium via the communication pipes connected to the inner peripheral end of each of the outlet side heat exchange pipes, and flows into the outlet side heat exchange pipes while flowing out to the outlet.

【0009】各熱交換管体の渦巻状の導入側熱交換部と
導出側熱交換管部は熱源熱媒体通路の熱源熱媒体の流動
方向に対して熱媒体通路の下流側から上流側に位置する
順序で互いに順次に各連通管部にて連通されているた
め、被熱交換熱媒体は熱源熱媒体の温度が比較的に低い
かまたは高い導入側熱交換管部から熱源熱媒体の温度が
比較的に高いかまたは低い導出側被熱交換管部に流入
し、各熱交換管体を流動する被熱交換熱媒体の熱交換熱
量は略均等化され、各熱交換管体の温度を従来の熱源熱
媒体通路に熱源熱媒体の流動方向に直線状に配設した熱
交換管体に比して温度上昇を低くでき、熱交換管体の熱
損傷を低減できるため、耐久性を高め、また、熱交換管
体の熱計算が容易となる。
The spiral inlet-side heat exchange portion and the outlet-side heat exchange tube portion of each heat exchange tube are located from the downstream side of the heat medium passage to the upstream side with respect to the flow direction of the heat source heat medium in the heat source heat medium passage. The heat exchange heat medium has a relatively low or high temperature of the heat source heat medium, and the temperature of the heat source heat medium from the introduction side heat exchange tube part is relatively low or high. The heat exchange heat of the heat exchange heat medium flowing into the relatively high or low outlet side heat exchange pipe section and flowing through each heat exchange pipe body is substantially equalized, and the temperature of each heat exchange pipe body is conventionally reduced. Since the temperature rise can be reduced and the heat damage of the heat exchange tube can be reduced as compared with the heat exchange tube arranged linearly in the flow direction of the heat source heat medium in the heat source heat medium passage, the durability can be increased. Further, heat calculation of the heat exchange tube is facilitated.

【0010】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、熱源熱媒体通路の熱源
熱媒体が流動する下流側に第1の熱交換部を形成すると
ともに上流側に第2の熱交換部を形成し、前記第1の熱
交換部は前記熱源熱媒体通路の熱源熱媒体が流動する下
流側に被熱交換熱媒体の導入室を形成するとともに前記
熱源熱媒体通路の熱源熱媒体が流動する上流側に被熱交
換熱媒体の導出室を形成し、前記第2の熱交換部は前記
熱源熱媒体通路の熱源熱媒体が流動する上流側に被熱交
換熱媒体の導入室を形成するとともに前記熱源熱媒体通
路の熱源熱媒体が流動する下流側に被熱交換熱媒体の導
出室を形成し、前記第1の熱交換部の被熱交換熱媒体の
導出室に前記第2の熱交換部の被熱交換熱媒体の導入室
を連通し、前記第1の熱交換部と第2の熱交換部とにそ
れぞれ両端部を被熱交換熱媒体の導入室と導出室とに接
続した被熱交換熱媒体が流動する複数の被熱交換管体を
熱源熱媒体通路に配設したものである。
According to a second aspect of the present invention, in the heat exchange apparatus according to the first aspect, a first heat exchange portion is formed on a downstream side of the heat source heat medium passage where the heat source heat medium flows, and the first heat exchange portion is formed upstream. A second heat exchange section on the side of the heat source heat medium passage, the first heat exchange section forms an inlet chamber for the heat exchange heat medium on the downstream side of the heat source heat medium passage where the heat source heat medium flows, and forms the heat source heat medium. An outlet chamber for the heat exchange heat medium is formed on the upstream side of the medium passage where the heat source heat medium flows, and the second heat exchange section is provided on the upstream side of the heat source heat medium passage where the heat source heat medium flows. Forming an introduction chamber for the heat medium and forming an outlet chamber for the heat exchange heat medium on the downstream side of the heat source heat medium passage where the heat source heat medium flows, and forming the heat exchange heat medium of the first heat exchange section. The introduction chamber for the heat exchange heat medium of the second heat exchange section communicates with the outlet chamber, A plurality of heat exchange tubes in which both ends of the heat exchange unit and the second heat exchange unit are connected to the inlet and outlet chambers of the heat exchange heat medium through which the heat exchange heat medium flows are used as heat source heat sources. It is arranged in the medium passage.

【0011】そして、被熱交換熱媒体は第1の熱交換部
と第2の熱交換部とで熱媒体通路を流動する熱源熱媒体
にて熱交換され、熱源熱媒体の熱回収率が高められ、熱
源熱媒体と効率よく熱交換され、熱源熱媒体の熱回収率
が高められ、しかも、第1の熱交換部の熱交換管体と第
2の熱交換部の熱交換管体とは熱媒体通路の熱源熱媒体
の流動方向に対して各導入側熱交換管部と各導出側熱交
換管部とは互いに反対位置となるため、熱源熱媒体と被
熱交換熱媒体との熱交換効率が高められるとともに各熱
交換管体を流動する被熱交換熱媒体の熱交換熱量は略均
等化され、各熱交換管体の温度を熱交換効率に比して温
度上昇を低くでき、熱交換管体の熱損傷を低減できるた
め、耐久性を高め、また、熱交換管体の熱計算が容易と
なる。
Then, the heat exchange heat medium is exchanged with the first heat exchange section and the second heat exchange section by the heat source heat medium flowing through the heat medium passage, so that the heat recovery rate of the heat source heat medium is increased. Heat is efficiently exchanged with the heat source heat medium, the heat recovery rate of the heat source heat medium is increased, and the heat exchange pipes of the first heat exchange section and the second heat exchange section are Since each inlet-side heat exchange tube and each outlet-side heat exchange tube are located at positions opposite to each other with respect to the flow direction of the heat source heat medium in the heat medium passage, heat exchange between the heat source heat medium and the heat exchange heat medium is performed. The efficiency is increased and the heat exchange heat of the heat exchange heat medium flowing through each heat exchange tube is substantially equalized, so that the temperature rise of each heat exchange tube can be reduced as compared with the heat exchange efficiency. Since the heat damage of the exchange tube can be reduced, the durability is enhanced, and the heat calculation of the heat exchange tube is facilitated.

【0012】請求項3記載の発明のバーナ装置は、燃焼
部と、この燃焼部の燃焼排ガスが流動する熱源熱媒体通
路と、この熱源熱媒体通路の外周に沿ってこの熱源熱媒
体通路を流動する燃焼排ガスの流動方向に対して並設さ
れた燃焼用酸素含有ガスの導入室および前記燃焼部の燃
焼用酸素含有ガス導入部に連通された燃焼用酸素含有ガ
スの導出室と、前記燃焼用酸素含有ガスの導入室と導出
室とに両端部を連通接続して前記熱源熱媒体通路に配設
され燃焼用酸素含有ガスが流動する複数の被熱交換管体
とを備えている。
According to a third aspect of the present invention, there is provided a burner device, comprising: a combustion section; a heat source heat medium passage through which flue gas from the combustion section flows; and the heat source heat medium passage flowing along the outer periphery of the heat source heat medium passage. A combustion oxygen-containing gas introduction chamber and a combustion oxygen-containing gas discharge chamber communicated with the combustion oxygen-containing gas introduction section of the combustion section. A plurality of heat exchange tubes are provided in the heat source heat medium passage, the plurality of heat exchange tubes through which the combustion oxygen-containing gas flows, the ends being connected to the oxygen-containing gas introduction chamber and the discharge chamber.

【0013】また、前記各被熱交換管体は、前記燃焼用
酸素含有ガスの導入室にそれぞれ外周側端部を連通接続
し前記熱源熱媒体通路の燃焼排ガスの流動方向に対して
直交する面に配設される渦巻状の導入側熱交換管部と、
前記燃焼用酸素含有ガスの導出室にそれぞれ外周側端部
を連通接続し前記熱源熱媒体通路の燃焼排ガスの流動方
向に対して直交する面に配設される渦巻状の導出側熱交
換管部と、前記導入側熱交換管部と導出側熱交換管部と
の内周側端部を互いに連通接続し前記熱源熱媒体通路を
流動する燃焼排ガスの流動方向に配設される直線状の連
通管部とを有している。
Each of the heat exchange pipes has an outer peripheral end connected to the introduction chamber for the oxygen-containing gas for combustion, and a surface orthogonal to the flow direction of the combustion exhaust gas in the heat source heat medium passage. A spiral inlet-side heat exchange tube section disposed in the
A spiral outlet-side heat exchange pipe section which is connected to an outer peripheral end of each of the outlet chambers for the combustion oxygen-containing gas and is disposed on a surface orthogonal to the flow direction of the combustion exhaust gas in the heat source heat medium passage; And linear communication arranged in the flow direction of the combustion exhaust gas flowing through the heat source heat medium passage by connecting the inner peripheral ends of the inlet side heat exchange pipe portion and the outlet side heat exchange tube portion to each other. And a tube portion.

【0014】さらに、前記各被熱交換管体の導入側熱交
換管部と導出側熱交換管部とを連通接続する連通管部の
長さをそれぞれ異なる長さとし、この連通管部の長さが
長い被熱交換管体の導入側熱交換管部と導出側熱交換管
部との間に連通管部の長さが短い被熱交換管体の導入側
熱交換管部と導出側熱交換管部を順次に配設して複数の
被熱交換管体の導入側熱交換管部と導出側熱交換管部と
を前記熱媒体通路の熱源熱媒体の流動方向に並設したも
のである。
Further, the lengths of the communication pipes for connecting and connecting the inlet-side heat exchange pipes and the outlet-side heat exchange pipes of the respective heat-exchanged pipes are different, and the lengths of the communication pipes are different. Between the inlet and outlet heat exchange pipe sections of the heat exchange pipe section having a longer length, and the inlet and outlet heat exchange sections of the heat exchange pipe section having a shorter length. The pipe sections are sequentially arranged, and the inlet-side heat exchange pipe section and the outlet-side heat exchange pipe section of the plurality of heat exchange pipes are arranged in parallel with the flow direction of the heat source heat medium in the heat medium passage. .

【0015】そして、導入室に導入された被熱交換熱媒
体の燃焼用酸素含有ガスは、それぞれこの導入室に外周
側端部を連通した複数の熱交換管体の渦巻状の導入側熱
交換管部にそれぞれ流入して熱媒体通路を流動する熱源
熱媒体の燃焼排気ガスと熱交換され、さらに、各導出側
熱交換管部の内周側端部に連通された各連通管部を経て
燃焼排ガスと熱交換されながら導出側熱交換管部に流動
して導出部に流出され、燃焼排ガスの廃熱を有効に回収
して熱を燃焼用酸素含有ガスを予熱できる。
The combustion-containing oxygen-containing gas of the heat exchange heat medium introduced into the introduction chamber receives the spiral introduction heat exchange of a plurality of heat exchange tubes each having an outer peripheral end communicating with the introduction chamber. The heat is exchanged with the combustion exhaust gas of the heat source heat medium flowing into the pipes and flowing through the heat medium passages, and further through the respective communication pipes connected to the inner peripheral end of each of the outlet side heat exchange pipes. The heat-exchanged heat-exchanger flows into the outlet-side heat exchange pipe portion and flows out to the outlet portion while being exchanged with the flue gas. The waste heat of the flue gas can be effectively recovered to preheat the combustion oxygen-containing gas.

【0016】各熱交換管体の渦巻状の導入側熱交換部と
導出側熱交換管部は熱源熱媒体通路の燃焼排ガスの流動
方向に対して熱媒体通路の下流側から上流側に位置する
順序で互いに順次に各連通管部にて連通されているた
め、燃焼用酸素含有ガスは燃焼排ガスの温度が比較的に
低いかまたは高い導入側熱交換管部から燃焼排ガスの温
度が比較的に高いかまたは低い導出側被熱交換管部に流
入し、各熱交換管体を流動する燃焼用酸素含有ガスの熱
交換熱量は略均等化され、各熱交換管体の温度を従来の
熱源熱媒体通路に燃焼排ガスの流動方向に直線状に配設
した熱交換管体に比して温度上昇を低くでき、熱交換管
体の熱損傷を低減できるため、耐久性を高め、また、熱
交換管体の熱計算が容易となる。
The spiral inlet-side heat exchange portion and the outlet-side heat exchange tube portion of each heat exchange tube are located from the downstream side to the upstream side of the heat medium passage with respect to the flow direction of the combustion exhaust gas in the heat source heat medium passage. Since each of the communication pipes is sequentially communicated with each other in order, the combustion oxygen-containing gas has a relatively low or high temperature of the combustion exhaust gas and a relatively high temperature of the combustion exhaust gas from the inlet heat exchange pipe section. The heat exchange heat of the oxygen-containing gas for combustion flowing into the high or low outlet side heat exchange pipe section and flowing through each heat exchange pipe body is substantially equalized, and the temperature of each heat exchange pipe body is reduced by the conventional heat source heat. Since the temperature rise can be reduced and heat damage to the heat exchange tube can be reduced as compared with the heat exchange tube arranged linearly in the flow direction of the combustion exhaust gas in the medium passage, durability can be improved and heat exchange can be performed. Heat calculation of the tube becomes easy.

【0017】請求項4記載の発明のバーナ装置は、請求
項3記載のバーナ装置において、熱源熱媒体通路の燃焼
排ガスが流動する下流側に第1の熱交換部を形成すると
ともに上流側に第2の熱交換部を形成し、前記第1の熱
交換部は前記熱源熱媒体通路の燃焼排ガスが流動する下
流側に燃焼用酸素含有ガスの導入室を形成するとともに
前記熱源熱媒体通路の燃焼排ガスが流動する上流側に燃
焼部の燃焼用酸素含有ガス導入部に連通された被熱交換
熱媒体の導出室を形成し、前記第2の熱交換部は前記熱
源熱媒体通路の燃焼排ガスが流動する上流側に燃焼用酸
素含有ガスの導入室を形成するとともに前記熱源熱媒体
通路の燃焼排ガスが流動する下流側に燃焼用酸素含有ガ
スの導出室を形成し、前記第1の熱交換部の燃焼用酸素
含有ガスの導出室に前記第2の熱交換部の燃焼用酸素含
有ガスの導入室を連通し、前記第1の熱交換部と第2の
熱交換部とにそれぞれ両端部を燃焼用酸素含有ガスの導
入室と導出室とに接続した燃焼用酸素含有ガスが流動す
る複数の被熱交換管体を熱源熱媒体通路に配設したもの
である。
According to a fourth aspect of the present invention, there is provided the burner device according to the third aspect, wherein a first heat exchange section is formed on the downstream side of the heat source heat medium passage where the combustion exhaust gas flows, and the first heat exchange section is formed on the upstream side. The first heat exchange section forms an introduction chamber for an oxygen-containing gas for combustion on the downstream side of the heat source heat medium passage where the combustion exhaust gas flows, and forms the combustion chamber in the heat source heat medium passage. On the upstream side where the exhaust gas flows, an outlet chamber for the heat exchange heat medium that is communicated with the combustion oxygen-containing gas introduction section of the combustion section is formed, and the second heat exchange section is configured so that the combustion exhaust gas of the heat source heat medium passage is formed. An inlet chamber for the oxygen-containing gas for combustion is formed on the upstream side where the gas flows, and an outlet chamber for the oxygen-containing gas for combustion is formed on the downstream side where the combustion exhaust gas of the heat source heat medium passage flows; Of oxygen-containing gas for combustion The introduction chamber for the oxygen-containing gas for combustion of the second heat exchange section is communicated, and both ends of the first heat exchange section and the second heat exchange section are led out to the introduction chamber for the oxygen-containing gas for combustion. A plurality of heat exchange pipes connected to a chamber and through which a combustion oxygen-containing gas flows are disposed in a heat source heat medium passage.

【0018】そして、被熱交換熱媒体の燃焼用酸素含有
ガスは第1の熱交換部と第2の熱交換部とで熱媒体通路
を流動する燃焼排ガスにて熱交換され、燃焼排ガスの熱
回収率が高められ、燃焼排ガスと効率よく熱交換され、
燃焼排ガスの熱回収率が高められ、燃焼排ガスの廃熱を
有効に回収して熱を燃焼用酸素含有ガスを予熱できる。
The combustion-containing oxygen-containing gas of the heat exchange heat medium is exchanged with the combustion exhaust gas flowing through the heat medium passage between the first heat exchange section and the second heat exchange section. Recovery rate is increased, heat exchange with combustion exhaust gas efficiently,
The heat recovery rate of the flue gas is increased, and the waste heat of the flue gas can be effectively recovered to preheat the oxygen-containing gas for combustion.

【0019】しかも、第1の熱交換部の熱交換管体と第
2の熱交換部の熱交換管体とは熱媒体通路の燃焼排ガス
の流動方向に対して各導入側熱交換管部と各導出側熱交
換管部とは互いに反対位置となるため、各熱交換管体を
流動する燃焼用酸素含有ガスの熱交換熱量は略均等化さ
れ、各熱交換管体の温度を熱交換効率に比して温度上昇
を低くでき、熱交換管体の熱損傷を低減できるため、耐
久性を高め、また、熱交換管体の熱計算が容易となる。
Furthermore, the heat exchange pipes of the first heat exchange section and the heat exchange pipes of the second heat exchange section are connected to each of the inlet side heat exchange pipes in the flow direction of the combustion exhaust gas in the heat medium passage. Since the heat exchange pipes are located at positions opposite to each other, the heat exchange heat of the oxygen-containing gas flowing through each heat exchange pipe is substantially equalized, and the temperature of each heat exchange pipe is reduced by the heat exchange efficiency. Since the temperature rise can be reduced and the heat damage of the heat exchange tube can be reduced as compared with the above, the durability can be increased and the heat calculation of the heat exchange tube can be easily performed.

【0020】[0020]

【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.

【0021】図1および図2において、熱源熱媒体通路
1は、熱源熱媒体、例えばバーナの燃焼部に連通され燃
焼排ガスが流動する略円筒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上半部の外周に沿
って形成した被熱交換熱媒体、例えば、燃焼用酸素含有
ガスの導入室2と、この熱媒体通路1の上流側に位置す
る下半部の外周に沿って形成した被熱交換熱媒体の導出
室3とが、この熱源熱媒体通路1を流動する熱源熱媒体
の流動方向に並設されている。この導出室3は、例え
ば、バーナの燃焼部に連通されている。
In FIG. 1 and FIG. 2, a heat source heat medium passage 1 is a substantially cylindrical heat source heat medium passage which communicates with a heat source heat medium, for example, a combustion portion of a burner and through which flue gas flows. The heat exchange heat medium, for example, the introduction chamber 2 for the oxygen-containing gas for combustion formed along the outer periphery of the upper half located on the downstream side, and the lower half located on the upstream side of the heat medium passage 1. An outlet chamber 3 for the heat exchange heat medium formed along the outer periphery is arranged in parallel with the flow direction of the heat source heat medium flowing through the heat source heat medium passage 1. The outlet chamber 3 is communicated with, for example, a combustion section of a burner.

【0022】また、前記被熱交換熱媒体の導入室2と導
出室3とに被熱交換熱媒体が流動する複数の被熱交換管
体6の両端部がそれぞれ連通接続され、この各被熱交換
管体6は前記熱源熱媒体通路1に配設されている。
Further, both ends of a plurality of heat exchange tubes 6 through which the heat exchange heat medium flows are respectively connected to the introduction chamber 2 and the discharge chamber 3 for the heat exchange heat medium. The exchange pipe 6 is disposed in the heat source heat medium passage 1.

【0023】そして、前記各被熱交換管体6は、図3に
示すように渦巻状の導入側熱交換管部4と渦巻状の導出
側熱交換管部5およびこの導入側熱交換管部4と導出側
熱交換管部5との内周側端部を互いに連通接続する直線
状の連通管部9が一体的に形成されている。この連通管
部9の長さは各被熱交換管体6ごとにそれぞれ異なる長
さを有している。
As shown in FIG. 3, each of the heat exchange pipes 6 includes a spiral inlet heat exchanger tube 4, a spiral outlet heat exchanger tube 5, and the inlet heat exchanger tube. A linear communication pipe portion 9 that connects the inner peripheral ends of the heat exchange pipe portion 4 and the outlet side heat communication tube portion 5 to each other is integrally formed. The length of the communication pipe section 9 is different for each heat exchange pipe body 6.

【0024】また、前記各被熱交換管体6の導入側熱交
換管部4のそれぞれの外周側端部は前記被熱交換熱媒体
の導入室2に連通接続され、導出側熱交換管部5のそれ
ぞれの外周側端部は導出室3に連通接続され、前記渦巻
状の導入側熱交換管部4と導出側熱交換管部5は前記熱
源熱媒体通路1に熱源熱媒体の流動方向に対してそれぞ
れ直交する面に配設されるとともに直線状の連通管部9
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
向に配設される。
Each of the heat-exchanger tubes 6 has an inlet-side heat-exchange tube 4 having an outer peripheral end connected to the heat-exchanger-medium introduction chamber 2 and connected to the outlet-side heat-exchanger tube. 5 are connected to the outlet chamber 3 in communication with each other, and the spiral inlet-side heat exchange pipe section 4 and the outlet-side heat exchange pipe section 5 are connected to the heat source heat medium passage 1 in the flow direction of the heat source heat medium. Communication pipe portions 9 which are arranged on surfaces orthogonal to
Are disposed in the flow direction of the heat source heat medium flowing through the heat source heat medium passage 1.

【0025】なお、前記各被熱交換管体6の導入側熱交
換管部4は導出側熱交換管部5より前記熱源熱媒体通路
1の下流側に接続されている。
The inlet-side heat exchange tube portion 4 of each of the heat-exchanged tubes 6 is connected to the downstream side of the heat-source heat medium passage 1 from the outlet-side heat exchange tube portion 5.

【0026】また、前記導入室2には被熱交換媒体の導
入口7が形成され、前記導出室3には導出口8が形成さ
れている。
Further, an inlet 7 for the heat exchange medium is formed in the introduction chamber 2, and an outlet 8 is formed in the outlet chamber 3.

【0027】そして、図1および図2に示すように、前
記連通管部9の長さが長い被熱交換管体6の導入側熱交
換管部4と導出側熱交換管部5との間に連通管部9の長
さが短い被熱交換管体6の導入側熱交換管部4と導出側
熱交換管部5を順次に配設して複数の被熱交換管体6の
導入側熱交換管部4と導出側熱交換管部5とを前記熱媒
体通路1の熱源熱媒体の流動方向に並設され、前記熱媒
体通路1を流れる熱源熱媒体の流動方向と前記導入側熱
交換管部4および導出側熱交換管部5を流れる被熱交換
熱媒体の流動方向とは直交流となり、導入側熱交換管部
4と導出側熱交換管部5の中央部に配設した各連通管部
9を熱媒体通路1を流れる被熱交換熱媒体の流動方向は
熱源熱媒体の流動方向と並流となる。
As shown in FIGS. 1 and 2, between the inlet side heat exchange pipe part 4 and the outlet side heat exchange pipe part 5 of the heat exchange pipe body 6 having the long communication pipe part 9 long. The inlet side heat exchange pipe section 4 and the outlet side heat exchange pipe section 5 of the heat exchange pipe section 6 having a short communication pipe section 9 are sequentially disposed on the inlet side of the plurality of heat exchange pipe sections 6. The heat exchange pipe section 4 and the outlet heat exchange pipe section 5 are arranged side by side in the flow direction of the heat source heat medium in the heat medium path 1, and the flow direction of the heat source heat medium flowing through the heat medium path 1 and the introduction side heat The flow direction of the heat-exchanged heat medium flowing through the exchange pipe section 4 and the outlet-side heat exchange pipe section 5 is a cross flow, and is disposed at the center of the inlet-side heat exchange pipe section 4 and the outlet-side heat exchange pipe section 5. The flow direction of the heat exchange heat medium flowing in the heat medium passage 1 through each communication pipe portion 9 is parallel to the flow direction of the heat source heat medium.

【0028】例えば、前記被熱交換管体6の各導入側熱
交換管部4を前記熱媒体通路1を流れる熱源熱媒体の下
流側に配設するとともに各導出側熱交換管部5を前記熱
媒体通路1を流れる熱源熱媒体の上流側に配設し、連通
管部9の長さが最も長い被熱交換管体6の導入側熱交換
管部4は熱源熱媒体の最も下流側に、導出側熱交換管部
5は熱源熱媒体の最も上流側に配設され、連通管部9の
長さが短かくなる順序で各導入側熱交換管部4は熱源熱
媒体の下流側から上流側に位置する順序で、導出側熱交
換管部5は前記排ガス通路1の上流側から下流側に位置
する順序で配設される。
For example, each of the inlet-side heat exchange tubes 4 of the heat-exchanged tube 6 is disposed downstream of the heat-source heat medium flowing through the heat medium passage 1, and each of the outlet-side heat exchange tubes 5 is connected to the heat-exchange tube 5. The inlet side heat exchange pipe part 4 of the heat exchange pipe body 6 having the longest length of the communication pipe part 9 is disposed on the upstream side of the heat source heat medium flowing through the heat medium passage 1 and is located at the most downstream side of the heat source heat medium. The outlet-side heat exchange pipes 5 are arranged at the most upstream side of the heat source heat medium, and each of the inlet-side heat exchange pipes 4 are arranged from the downstream side of the heat source heat medium in the order in which the length of the communication pipes 9 becomes shorter. In the order located on the upstream side, the outlet-side heat exchange pipe section 5 is disposed in the order located from the upstream side to the downstream side of the exhaust gas passage 1.

【0029】なお、前記導入室2と各導入側熱交換管部
4との連通部は図2に示すように順次円周方向に偏位さ
れるとともに、前記導出室3と各導出側熱交換管部5と
の連通部も順次円周方向に偏位されている。
The communicating portion between the introduction chamber 2 and each of the introduction side heat exchange pipe sections 4 is sequentially displaced in the circumferential direction as shown in FIG. The communicating part with the pipe part 5 is also deviated sequentially in the circumferential direction.

【0030】また、前記導入側熱交換管部4、導出側熱
交換管部5および連通管部9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一体的に
成形する。
The inlet-side heat exchange tube 4, the outlet-side heat exchange tube 5, and the communication tube 9 are integrally formed of a heat-resistant metal material such as Inconel or 70% nickel / 15% chromium alloy.

【0031】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.

【0032】熱媒体通路1の下流側に位置する導入室2
に導入口7から導入された被熱交換熱媒体は、それぞれ
この導入室2に一端を連通した複数の被熱交換管体6の
渦巻状の導入側熱交換管部4にそれぞれ流入して熱媒体
通路1を流動する熱源熱媒体とは直交流となって熱交換
される。
An introduction chamber 2 located downstream of the heat medium passage 1
The heat exchange heat medium introduced from the inlet 7 into each of the plurality of heat exchange pipes 6 having one ends communicating with the introduction chamber 2 respectively flows into the spiral introduction-side heat exchange pipe portions 4. The heat exchange between the heat source heat medium flowing through the medium passage 1 and the heat source heat medium is performed in a cross flow.

【0033】さらに、各導入側熱交換管部4にて熱源熱
媒体と熱交換されながら各導入側熱交換管部4の他端側
に流動した被熱交換熱媒体は各連通管部9にて熱媒体通
路1を流動する熱源熱媒体と熱交換されながら流動し、
この各連通管部9に連通された上流側に位置する各導出
側熱交換管部5にそれぞれ流入し、各導出側熱交換管部
5に流入した被熱交換熱媒体は熱媒体通路1を流動する
熱源熱媒体と直交流となってさらに熱交換されて導出室
3に流出され、この導出口8から流出される。
Further, the heat exchange heat medium flowing to the other end of each of the inlet side heat exchange tubes 4 while being exchanged with the heat source heat medium in each of the inlet side heat exchange tube portions 4 is transferred to each of the communication tube portions 9. Flow while being exchanged with the heat source heat medium flowing through the heat medium passage 1,
The heat-exchanged heat medium flowing into each of the outlet-side heat exchange pipe portions 5 located on the upstream side and communicated with each of the communication tube portions 9 flows into the heat-medium passage 1. The fluid flows in a cross flow with the flowing heat source heat medium, is further exchanged with heat, flows out to the outlet chamber 3, and flows out from the outlet 8.

【0034】そして、各導入側熱交換管部4にて熱源熱
媒体と熱交換された被熱交換熱媒体は、それぞれ熱媒体
通路1の下流側に位置する導入流側熱交換管部4から前
記熱媒体通路1の上流側に位置する導出側熱交換管部5
への順序で互いに順次に連通するため、被熱交換熱媒体
は熱源熱媒体の比較的温度の低い下流側に位置する導入
側熱交換管部4から熱源熱媒体の比較的温度の高い上流
側に位置する導出側熱交換管部5に流れ、また、被熱交
換熱媒体は熱源熱媒体の比較的温度の高い上流側に位置
する導入側熱交換管部4から熱源熱媒体の比較的温度の
低い下流側に位置する導出側熱交換管部5に流れ、各被
熱交換管体6を流動する被熱交換熱媒体の熱交換熱量は
各略均等化される。
The heat-exchanged heat medium that has been heat-exchanged with the heat-source heat medium in each of the inlet-side heat-exchange pipe sections 4 passes through the inlet-side heat-exchange pipe section 4 located downstream of the heat medium passage 1. Outlet-side heat exchange pipe portion 5 located upstream of the heat medium passage 1
, The heat exchange heat medium to be exchanged flows from the inlet side heat exchange pipe portion 4 located downstream of the heat source heat medium at a relatively low temperature to the upstream side of the heat source heat medium at a relatively high temperature. The heat exchange heat medium flows from the inlet side heat exchange tube part 4 located on the upstream side where the temperature of the heat source heat medium is relatively high, and the heat exchange heat medium flows into the outlet side heat exchange pipe part 5 The heat exchange heat quantity of the heat exchange heat medium flowing through the heat exchange pipes 6 flowing through the outlet heat exchange pipe portions 5 located on the downstream side of the lower heat exchange pipes is substantially equalized.

【0035】前記実施の形態では、略円筒状の熱媒体通
路1に配設した導入側熱交換管部4および導出流側熱交
換管部5を略渦巻き円環状に形成した構成について説明
したが、図4に示すように熱媒体通路1を断面矩形状に
形成し、導入側熱交換管部4および導出側熱交換管部5
を略渦巻き矩形形状とすることもでき、また、断面形状
を楕円形状など適宜の形状とすることもできる。
In the above-described embodiment, the configuration is described in which the inlet-side heat exchange tube portion 4 and the outlet-side heat exchange tube portion 5 disposed in the substantially cylindrical heat medium passage 1 are formed in a substantially spiral annular shape. As shown in FIG. 4, the heat medium passage 1 is formed in a rectangular shape in cross section, and the inlet side heat exchange tube portion 4 and the outlet side heat exchange tube portion 5 are formed.
May have a substantially spiral rectangular shape, and the cross-sectional shape may be an appropriate shape such as an elliptical shape.

【0036】さらに、前記各実施の形態では、熱源熱媒
体と被熱交換熱媒体は、燃焼排ガスと燃焼用酸素含有ガ
ス、例えば空気の気体について説明したが、熱源熱媒体
と被熱交換熱媒体の一方または両方を液体とすることも
できる。
Furthermore, in each of the above embodiments, the heat source heat medium and the heat exchange heat medium have been described as the combustion exhaust gas and the oxygen-containing gas for combustion, for example, air gas. One or both can be liquids.

【0037】次に前記実施の形態の熱交換装置を備えた
バーナ装置の一実施の形態の構成を図5に基いて説明す
る。
Next, a configuration of an embodiment of a burner device provided with the heat exchange device of the above embodiment will be described with reference to FIG.

【0038】10は燃焼装置の窯炉で、この窯炉10内の燃
焼部に連通した熱源熱媒体の燃焼排ガスの流出口11が形
成され、この流出口11に下側部を連通した上流側の排ガ
ス通路となる熱源熱媒体通路12が垂直状に形成され、こ
の上流側の熱源熱媒体通路12の上側部は水平方向の中間
熱源熱媒体通路13を介して垂直方向の下流側の燃焼排ガ
ス通路となる熱源熱媒体通路14の上端部が連通され、こ
の下流側の熱源熱媒体通路14の下端部は排ガス放出路に
連通され、前記中間燃焼排ガス流路13は断熱材にて覆わ
れている。
Reference numeral 10 denotes a kiln of the combustion apparatus, which is formed with an outlet 11 for a combustion exhaust gas of a heat source heat medium which communicates with a combustion section in the kiln 10, and an upstream side which communicates with the outlet 11 at a lower portion. A heat source heat medium passage 12 serving as an exhaust gas passage is vertically formed, and an upper portion of the upstream heat source heat medium passage 12 is vertically exhausted through a horizontal intermediate heat source heat medium passage 13. The upper end of the heat source heat medium passage 14 serving as a passage is communicated, the lower end of the downstream heat source heat medium passage 14 is communicated with an exhaust gas discharge passage, and the intermediate combustion exhaust gas passage 13 is covered with a heat insulating material. I have.

【0039】また、前記下流側の熱源熱媒体通路14の下
流側に位置する下半部の外周に被熱交換熱媒体の燃焼用
酸素含有ガス、例えば空気の導入室15が形成され、この
下流側の熱源熱媒体通路14の上流側に位置する上半部の
外周に燃焼用酸素含有ガスの導出室16が形成されてい
る。さらに、前記上流側の熱源熱媒体通路12の下流側に
位置する下半部の外周に前記導出室16に接続管17にて連
通された燃焼用酸素含有ガスの導入室18が形成され、こ
の下流側の排ガス通路12の上流側に位置する上半部の外
周に燃焼用酸素含有ガスの導出室19が形成されている。
Further, an oxygen-containing gas for combustion of the heat exchange heat medium, for example, an air introduction chamber 15 is formed on the outer periphery of the lower half located on the downstream side of the heat source heat medium passage 14 on the downstream side. A discharge chamber 16 for the oxygen-containing gas for combustion is formed on the outer periphery of the upper half located on the upstream side of the heat source heat medium passage 14 on the side. Furthermore, an introduction chamber 18 for a combustion oxygen-containing gas communicated with a connection pipe 17 to the outlet chamber 16 is formed on the outer periphery of a lower half located on the downstream side of the upstream heat source heat medium passage 12. A discharge chamber 19 for the oxygen-containing gas for combustion is formed on the outer periphery of the upper half located on the upstream side of the exhaust gas passage 12 on the downstream side.

【0040】そして、前記下流側の被熱交換熱媒体の導
入室15と導出室16とに被熱交換熱媒体が流動する複数の
被熱交換管体20の両端部がそれぞれ連通接続され、この
各被熱交換管体20が下流側の熱源熱媒体通路14に配設さ
れて第1の熱交換部21が形成されている。
Both ends of a plurality of heat exchange tubes 20 through which the heat exchange heat medium flows are respectively connected to the inlet chamber 15 and the discharge chamber 16 of the heat exchange heat medium on the downstream side. Each of the heat exchange tubes 20 is disposed in the heat source heat medium passage 14 on the downstream side to form a first heat exchange unit 21.

【0041】また、前記上流側の被熱交換熱媒体の導入
室18と導出室19とに被熱交換熱媒体が流動する複数の被
熱交換管体22の両端部がそれぞれ連通接続され、この各
被熱交換管体22が上流側の熱源熱媒体通路12に配設され
て第2の熱交換部23が形成されている。
Further, both ends of a plurality of heat exchange pipes 22 through which the heat exchange heat medium flows are connected to the upstream side heat exchange heat medium introduction chamber 18 and the discharge chamber 19, respectively. Each of the heat exchange tubes 22 is disposed in the heat source heat medium passage 12 on the upstream side to form a second heat exchange portion 23.

【0042】そして、前記第1および第2の熱交換部2
1,23の各被熱交換管体20,22は、前記図1ないし図3
に示す実施の形態と同一構成で、渦巻状の導入側熱交換
管部25,26と渦巻状の導出側熱交換管部27,28およびこ
の導入側熱交換管部25,26と導出側熱交換管部27,28と
の内周側端部を互いに連通接続する直線状の連通管部2
9,30が一体的に形成されている。この連通管部29,30
の長さは各被熱交換管体20,22ごとにそれぞれ異なる長
さを有している。
The first and second heat exchange units 2
Each of the heat exchange tubes 20 and 22 shown in FIGS.
With the same configuration as that of the embodiment shown in FIG. 3, the spiral inlet-side heat exchange pipe sections 25 and 26, the spiral outlet-side heat exchange pipe sections 27 and 28, and the inlet-side heat exchange pipe sections 25 and 26 and the outlet-side heat exchanger pipes. A linear communication pipe 2 that connects the inner peripheral ends of the exchange pipes 27 and 28 to each other.
9 and 30 are integrally formed. These communication pipe sections 29, 30
Has a different length for each of the heat exchange tubes 20, 22.

【0043】また、前記各被熱交換管体20,22の導入側
熱交換管部25,26のそれぞれの外周側端部は前記被熱交
換熱媒体の導入室15,18に連通接続され、導出側熱交換
管部27,28のそれぞれの外周側端部は導出室16,19に連
通接続され、前記渦巻状の導入側熱交換管部25,26と導
出側熱交換管部27,28は前記下流側の熱源熱媒体通路14
に熱源熱媒体の流動方向に対してそれぞれ直交する面に
配設されるとともに直線状の連通管部29,30は前記下流
側および上流側の熱源熱媒体通路14,12を流動する熱源
熱媒体の流動方向に配設される。
The outer peripheral ends of the inlet-side heat exchange pipe portions 25 and 26 of the heat-exchanger tubes 20 and 22 are connected to the introduction chambers 15 and 18 for the heat-exchange heat medium. Outer peripheral end portions of the outlet-side heat exchange tube portions 27 and 28 are connected to the outlet chambers 16 and 19, respectively, and the spiral inlet-side heat exchange tube portions 25 and 26 and the outlet-side heat exchange tube portions 27 and 28 are connected. Is the heat source heat medium passage 14 on the downstream side.
The heat source heat medium flowing through the heat source heat medium passages 14 and 12 on the downstream side and the upstream side, respectively, are disposed on the surfaces orthogonal to the flow direction of the heat source heat medium. In the direction of flow.

【0044】なお、前記第1の熱交換部21の各被熱交換
管体20の渦巻状の導入側熱交換管部25は導出側熱交換管
部27より前記下流側の熱源熱媒体通路14の下流側に配設
され、第2の熱交換部22の各被熱交換管体22の渦巻状の
導入側熱交換管部26は導出側熱交換管部28より前記上流
側の熱源熱媒体通路12の上流側に配設される。
The spiral inlet-side heat exchange tube section 25 of each heat-exchanged pipe body 20 of the first heat exchange section 21 is connected to the heat-source heat medium passage 14 on the downstream side of the outlet-side heat exchange pipe section 27. The spiral inlet-side heat exchange tube portion 26 of each heat-exchanged tube body 22 of the second heat exchange portion 22 is disposed on the downstream side of the heat source heat medium on the upstream side of the outlet-side heat exchange tube portion 28. It is arranged on the upstream side of the passage 12.

【0045】また、前記下流側の熱源熱媒体通路14の外
周に形成した導入室15には被熱交換媒体の導入口31が形
成され、前記上流側の熱源熱媒体通路12の導出室19には
導出口32が形成されている。
An inlet 31 for the heat exchange medium is formed in the introduction chamber 15 formed on the outer periphery of the heat source heat medium passage 14 on the downstream side, and is connected to the outlet chamber 19 of the heat source heat medium passage 12 on the upstream side. Has an outlet 32 formed therein.

【0046】そして、前記第1および第2の熱交換部2
1,23の各被熱交換管体20,22の連通管部29,30の長さ
が長い被熱交換管体20,23の導入側熱交換管部25,26と
導出側熱交換管部27,28との間に連通管部29,30の長さ
が短い被熱交換管体20,22の導入側熱交換管部25,26と
導出側熱交換管部27,28を順次に配設して複数の被熱交
換管体20,23の導入側熱交換管部25,26と導出側熱交換
管部27,28とを前記下流側および上流側熱媒体通路14,
12の熱源熱媒体の流動方向に並設され、この熱媒体通路
14,12を流れる熱源熱媒体の流動方向と前記導入側熱交
換管部25,26および導出側熱交換管部27,28を流れる被
熱交換熱媒体の流動方向とは直交流となり、導入側熱交
換管部25,26と導出側熱交換管部27,28の中央部に配設
した各連通管部29,30を熱媒体通路14,12を流れる被熱
交換熱媒体の流動方向は熱源熱媒体の流動方向と並流と
なる。
The first and second heat exchange units 2
Introducing the heat exchange pipes 25 and 26 and the outlet heat exchange pipes of the heat exchange pipes 20 and 23 having long communication pipe sections 29 and 30 of the heat exchange pipes 20 and 22 of 1 and 23, respectively. Introducing the heat exchange pipe sections 25, 26 and the discharge heat pipe sections 27, 28 of the heat exchange pipe bodies 20, 22 having short communication pipe sections 29, 30 between the pipes 27, 28 in that order. And the inlet-side heat exchange pipe sections 25, 26 and the outlet-side heat exchange pipe sections 27, 28 of the plurality of heat exchange pipe bodies 20, 23 are connected to the downstream and upstream heat medium passages 14,
The heat medium passages are arranged side by side in the flow direction of the 12 heat source heat media.
The flow direction of the heat source heat medium flowing through the heat exchange tubes 14 and 12 and the flow direction of the heat exchange heat medium flowing through the inlet-side heat exchange tube portions 25 and 26 and the outlet-side heat exchange tube portions 27 and 28 have a cross flow. The direction of flow of the heat exchange heat medium flowing through the heat medium passages 14 and 12 flows through the communication pipes 29 and 30 disposed at the center of the heat exchange pipe sections 25 and 26 and the outlet side heat exchange pipe sections 27 and 28, respectively. It is co-current with the flow direction of the heat medium.

【0047】例えば、前記第1の熱交換部21の被熱交換
管体20の各導入側熱交換管部25を前記熱媒体通路14を流
れる熱源熱媒体の下流側に配設するとともに各導出側熱
交換管部27を前記熱媒体通路14を流れる熱源熱媒体の下
流側に配設し、連通管部29の長さが最も長い被熱交換管
体20の導入側熱交換管部25は熱源熱媒体の最も下流側
に、導出側熱交換管部27は熱源熱媒体の最も上流側に配
設され、連通管部29の長さが短かくなる順序で各導入側
熱交換管部25は熱源熱媒体の下流側から上流側に位置す
る順序で、導出側熱交換管部27は前記熱源熱媒体通路14
の上流側から下流側に位置する順序で配設される。
For example, each inlet-side heat exchange pipe section 25 of the heat exchange pipe body 20 of the first heat exchange section 21 is disposed downstream of the heat source heat medium flowing through the heat medium passage 14, and each of the heat exchange pipe sections 25 is led out. The side heat exchange tube 27 is disposed downstream of the heat source heat medium flowing through the heat medium passage 14, and the introduction side heat exchange tube 25 of the heat exchange tube 20 having the longest length of the communication tube 29 is At the most downstream side of the heat source heat medium, the outlet side heat exchange pipe section 27 is disposed at the most upstream side of the heat source heat medium, and the introduction side heat exchange pipe sections 25 are arranged in the order of decreasing the length of the communication pipe section 29. Are in the order from the downstream side to the upstream side of the heat source heat medium, and the outlet side heat exchange pipe portion 27 is connected to the heat source heat medium passage 14.
Are arranged in order from the upstream side to the downstream side.

【0048】前記第2の熱交換部23の被熱交換管体22の
各導入側熱交換管部26を前記熱媒体通路12を流れる熱源
熱媒体の上流側に配設するとともに各導出側熱交換管部
28を前記熱媒体通路12を流れる熱源熱媒体の下流側に配
設し、連通管部30の長さが最も長い被熱交換管体22の導
入側熱交換管部26は熱源熱媒体の最も上流側に、導出側
熱交換管部28は熱源熱媒体の最も下流側に配設され、連
通管部30の長さが短かくなる順序で各導入側熱交換管部
26は熱源熱媒体の上流側から下流側に位置する順序で、
導出側熱交換管部28は前記熱源熱媒体通路12の下流側か
ら上流側に位置する順序で配設される。
Each of the inlet-side heat exchange tubes 26 of the heat-exchanged tube 22 of the second heat exchange unit 23 is disposed upstream of the heat source heat medium flowing through the heat medium passage 12, and each of the outlet-side heat exchangers 26 is provided. Exchange pipe
28 is disposed downstream of the heat source heat medium flowing through the heat medium passage 12, and the introduction side heat exchange tube portion 26 of the heat exchange tube 22 having the longest communication tube portion 30 is the most heat source heat medium. On the upstream side, the outlet-side heat exchange pipe section 28 is disposed at the most downstream side of the heat source heat medium, and the introduction-side heat exchange pipe sections are arranged in the order in which the length of the communication pipe section 30 becomes shorter.
26 is the order from upstream to downstream of the heat source heat medium,
The outlet-side heat exchange tubes 28 are arranged in the order from the downstream side to the upstream side of the heat source heat medium passage 12.

【0049】なお、前記第1および第2の熱交換部21,
23の導入室15,18と各導入側熱交換管部25,26との連通
部は順次円周方向に偏位されるとともに、前記導出室1
6,19と各導出側熱交換管部27,28との連通部も順次円
周方向に偏位されている。
The first and second heat exchange sections 21 and
The communication sections between the introduction chambers 15 and 18 of 23 and the introduction side heat exchange pipe sections 25 and 26 are sequentially displaced in the circumferential direction, and
The communicating portions between 6, 19 and the respective outlet-side heat exchange tube portions 27, 28 are also sequentially displaced in the circumferential direction.

【0050】さらに、第1の熱交換部21の下流側の熱媒
体通路14の下流側に位置する導入室15に導入口31が形成
され、また、第2の熱交換部23の下流側の熱媒体通路12
の下流側に位置する導出室19に導出口32が連通され、こ
の導出口32は導出路にて燃焼装置10の窯炉10の燃焼部に
連通されている。
Further, an introduction port 31 is formed in the introduction chamber 15 located on the downstream side of the heat medium passage 14 on the downstream side of the first heat exchange section 21, and the introduction port 31 is provided on the downstream side of the second heat exchange section 23. Heat medium passage 12
The outlet 32 is connected to the outlet chamber 19 located downstream of the furnace, and the outlet 32 is connected to the combustion section of the kiln 10 of the combustion device 10 through the outlet path.

【0051】また、前記被熱交換管体20,22の導入側熱
交換管部25,26、導出側熱交換管部27,28および連通管
部29,30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一体的に成形する。
The inlet-side heat exchange pipe sections 25, 26, the outlet-side heat exchange pipe sections 27, 28, and the communication pipe sections 29, 30 of the heat exchange pipes 20, 22 are made of Inconel or 70% nickel.15%. Molded integrally with heat-resistant metal material such as chrome 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】窯炉10内の燃焼部からの熱源熱媒体の燃焼
排ガスは、流入口11の上流側の熱源熱媒体通路12を流動
して第2の熱交換部23の熱交換管体22の導入側熱交換管
部26および導出側熱交換管部27を流動する空気と向流と
なって熱交換し、中間熱源熱媒体通路13を経て下流側の
熱源熱媒体通路14を流動して第1の熱交換部21の導出側
熱交換管部27および導入側熱交換管部25を流れる被熱交
換熱媒体の燃焼用酸素含有ガス、例えば空気と直交流と
なって熱交換し、排ガス放出路に放出される。
The flue gas of the heat source heat medium from the combustion part in the kiln 10 flows through the heat source heat medium passage 12 on the upstream side of the inflow port 11 and flows through the heat exchange pipe 22 of the second heat exchange part 23. The air flowing through the inlet-side heat exchange pipe section 26 and the outlet-side heat exchange pipe section 27 exchanges heat in a counterflow manner, flows through the intermediate heat source heat medium passage 13, flows through the downstream heat source heat medium passage 14, and The oxygen-containing gas for combustion of the heat exchange heat medium, such as air, flowing through the heat exchange pipe section 27 and the heat exchange pipe section 25 of the heat exchange section 21 of the first heat exchange section 21 undergoes heat exchange in a cross flow to release exhaust gas. Released into the road.

【0054】また、第1の熱交換部21の下流側の熱媒体
通路14の下流側に位置する導入室15に導入口31から導入
された被熱交換熱媒体は、それぞれこの導入室15に一端
を連通した複数の被熱交換管体20の渦巻状の導入側熱交
換管部25にそれぞれ流入して熱媒体通路14を流動する熱
源熱媒体とは直交流となって熱交換される。
The heat exchange heat medium introduced from the introduction port 31 into the introduction chamber 15 located downstream of the heat medium passage 14 downstream of the first heat exchange section 21 is supplied to the introduction chamber 15 respectively. The heat source heat medium flowing into the heat medium passage 14 by flowing into the spiral introduction side heat exchange pipe portions 25 of the plurality of heat exchange pipe bodies 20 having one ends communicating therewith is exchanged with heat.

【0055】さらに、各被熱交換管体20の導入側熱交換
管部25にて熱源熱媒体と熱交換されながら各導入側熱交
換管部25の他端側に流動した被熱交換熱媒体は各連通管
部29にて熱媒体通路14を流動する熱源熱媒体と熱交換さ
れながら流動し、この各連通管部29に連通された上流側
に位置する各導出側熱交換管部27にそれぞれ流入し、各
導出側熱交換管部27に流入した被熱交換熱媒体は熱媒体
通路14を流動する熱源熱媒体と直交流となってさらに熱
交換されて導出室16に流出され、この導出室16から接続
管17を経て第2の熱交換部23の導入室18に流入される。
Further, the heat-exchanged heat medium flowing to the other end of each of the inlet-side heat exchange tubes 25 while exchanging heat with the heat source heat medium in the inlet-side heat-exchange tubes 25 of each heat-exchanged tube 20. Flows while being exchanged with the heat source heat medium flowing through the heat medium passage 14 in each communication pipe section 29, and flows into each outlet side heat exchange pipe section 27 located on the upstream side connected to each communication pipe section 29. The heat-exchanged heat medium that has flowed in and has flowed into each outlet-side heat exchange pipe portion 27 has a cross flow with the heat source heat medium flowing through the heat medium passage 14, is further heat-exchanged, and flows out to the outlet chamber 16. It flows into the introduction chamber 18 of the second heat exchange unit 23 from the outlet chamber 16 via the connection pipe 17.

【0056】また、第2の熱交換部23の各被熱交換管体
22の導入側熱交換管部26にて熱源熱媒体と熱交換されな
がら各導入側熱交換管部26の他端側に流動した被熱交換
熱媒体は各連通管部30にて熱媒体通路12を流動する熱源
熱媒体と熱交換されながら流動し、この各連通管部30に
連通された下流側に位置する各導出側熱交換管部28にそ
れぞれ流入し、各導出側熱交換管部28に流入した被熱交
換熱媒体は熱媒体通路12を流動する熱源熱媒体と直交流
となってさらに熱交換されて導出室19に流出され、この
導出室19から燃焼装置10の窯炉10の燃焼部に供給され
る。
Each heat exchange pipe of the second heat exchange section 23
The heat-exchanged heat medium flowing to the other end of each of the inlet-side heat exchange tubes 26 while being exchanged with the heat source heat medium at the inlet-side heat exchange tubes 26 of the heat medium passages at the respective communication tubes 30. 12 flows while being heat-exchanged with the heat source heat medium flowing therethrough, flows into each outlet side heat exchange tube portion 28 located on the downstream side communicated with each communication tube portion 30, and each outlet side heat exchange tube portion The heat-exchanged heat medium flowing into the heat source heat medium flowing through the heat medium passage 12 is further exchanged with heat as a direct flow with the heat source heat medium flowing through the heat medium passage 12 and flows out to the discharge chamber 19. Is supplied to the combustion section.

【0057】そして、各導入側熱交換管部25,26にて熱
源熱媒体と熱交換された被熱交換熱媒体は、それぞれ熱
媒体通路14,12の導入流側熱交換管部25,26から導出側
熱交換管部27,28への順序で互いに順次に連通するた
め、第1の熱交換部21では、被熱交換熱媒体は熱源熱媒
体の下流側に位置する導入側熱交換管部25から熱源熱媒
体の上流側に位置する導出側熱交換管部27に流れるとと
もに、熱源熱媒体の上流側に位置する導入側熱交換管部
25から熱源熱媒体の下流側に位置する導出側熱交換管部
27に流れ、各被熱交換管体20を流動する被熱交換熱媒体
の熱交換熱量は各略均等化される。
Then, the heat exchange heat medium that has been heat-exchanged with the heat source heat medium in each of the inlet side heat exchange pipe sections 25 and 26 is introduced into the inlet flow side heat exchange pipe sections 25 and 26 of the heat medium passages 14 and 12, respectively. In the first heat exchange section 21, the heat exchange heat medium to be exchanged is the introduction side heat exchange pipe positioned downstream of the heat source heat medium. From the section 25 to the outlet side heat exchange pipe section 27 located upstream of the heat source heat medium, and to the inlet side heat exchange pipe section located upstream of the heat source heat medium
Outlet heat exchange tube located downstream of heat medium from 25
27, the heat exchange heat of the heat exchange heat medium flowing through each heat exchange tube 20 is substantially equalized.

【0058】また、第2の熱交換部23では、被熱交換熱
媒体は熱源熱媒体の比較的温度の低い下流側に位置する
導入側熱交換管部26から熱源熱媒体の上流側に位置する
導出側熱交換管部28に流れるとともに、被熱交換熱媒体
は熱源熱媒体の上流側に位置する導入側熱交換管部26か
ら熱源熱媒体の下流側に位置する導出側熱交換管部28に
流れ、各被熱交換管体22を流動する被熱交換熱媒体の熱
交換熱量は各略均等化される。
In the second heat exchange section 23, the heat exchange medium to be heat-exchanged is positioned upstream from the heat-source heat medium from the inlet-side heat exchange pipe section 26 located downstream of the heat-source heat medium at a relatively low temperature. The heat exchange heat medium flows from the introduction side heat exchange tube section 26 located on the upstream side of the heat source heat medium to the discharge side heat exchange tube section located on the downstream side of the heat source heat medium. The heat exchange heat of the heat exchange heat medium flowing through the heat exchange tubes 22 flowing through the heat exchange tubes 22 is substantially equalized.

【0059】そして、第2の熱交換部23の導出室19に流
出された被熱交換熱媒体はの燃焼用酸素含有ガス導入部
35に流出し、窯炉10の燃焼部に供給される。
Then, the heat exchange heat medium flowing out to the outlet chamber 19 of the second heat exchange section 23 is a combustion oxygen-containing gas introduction section.
It flows out to 35 and is supplied to the combustion part of the kiln 10.

【0060】さらに、前記各実施の形態では、熱源熱媒
体と被熱交換熱媒体は、燃焼排ガスと燃焼用酸素含有ガ
ス、例えば空気の気体について説明したが、熱源熱媒体
と被熱交換熱媒体の一方または両方を液体とすることも
できる。
Further, in each of the above embodiments, the heat source heat medium and the heat exchange heat medium have been described as the combustion exhaust gas and the oxygen-containing gas for combustion, for example, air gas. One or both can be liquids.

【0061】[0061]

【発明の効果】請求項1記載の発明によれば、熱媒体通
路の導入室に導入された被熱交換熱媒体は、それぞれこ
の導入室に一端を連通した複数の被熱交換管体の略渦巻
状の導入側熱交換管部にそれぞれ流入して熱媒体通路を
流動する熱源熱媒体と熱交換され、さらに、各導入側熱
交換管部の他端に連通された各連通管部を経て熱源熱媒
体と熱交換されながら導出側熱交換管部に流動して導出
室に流出され、熱交換は直交流となって熱効率よく熱交
換され、各導入側熱交換管部と導出側熱交換管部とを流
動する被熱交換熱媒体の熱交換熱量は略均等化され、熱
交換率が高められても各被熱交換管体の温度上昇が低く
熱交換管体の熱損傷を低減できるため、耐久性を高め、
また、熱交換管体の熱計算が容易となる。
According to the first aspect of the present invention, the heat exchange heat medium introduced into the introduction chamber of the heat medium passage is substantially equivalent to a plurality of heat exchange pipes each having one end communicating with the introduction chamber. The heat is exchanged with the heat source heat medium flowing into the spiral heat introduction pipe portion and flowing through the heat medium passage, and further through each communication pipe portion connected to the other end of each introduction heat exchange tube portion. While being exchanged with the heat source heat medium, it flows into the outlet heat exchange pipe section and flows out to the outlet chamber.The heat exchange becomes a cross flow and is heat exchanged with high heat efficiency, and each inlet side heat exchange pipe section and the outlet side heat exchange. The heat exchange heat quantity of the heat exchange heat medium flowing through the pipe section is substantially equalized, so that even if the heat exchange rate is increased, the temperature rise of each heat exchange pipe body is low and the heat damage of the heat exchange pipe body can be reduced. To increase durability,
Further, heat calculation of the heat exchange tube is facilitated.

【0062】請求項2記載の発明によれば、熱源熱媒体
通路の下流側の第1の熱交換部にて熱交換された被熱交
換熱媒体は導出室から熱源熱媒体通路の上流側の第2の
熱交換部の導入室に導入されて再び熱交換され、熱源熱
媒体の熱を効率よく回収することができる。
According to the second aspect of the present invention, the heat-exchanged heat medium heat-exchanged in the first heat exchange section on the downstream side of the heat-source heat medium passage is transferred from the outlet chamber to the upstream side of the heat-source heat medium passage. The heat is introduced again into the introduction chamber of the second heat exchanging section and is exchanged again, so that the heat of the heat source heat medium can be efficiently recovered.

【0063】請求項3記載の発明によれば、燃焼排ガス
が流動する熱媒体通路の導入室に導入された被熱交換熱
媒体の燃焼用酸素含有ガス、例えば空気は、それぞれこ
の導入室に一端を連通した複数の被熱交換管体の略渦巻
状の導入側熱交換管部にそれぞれ流入して熱媒体通路を
流動する燃焼排ガスと熱交換され、さらに、各導入側熱
交換管部の他端に連通された各連通管部を経て燃焼排ガ
スと熱交換されながら導出側熱交換管部に流動して導出
室に流出され、熱交換は直交流となって熱効率よく熱交
換され、各導入側熱交換管部と導出側熱交換管部とを流
動する燃焼用酸素含有ガスの熱交換熱量は略均等化さ
れ、熱交換率が高められても各被熱交換管体の温度上昇
が低く熱交換管体の熱損傷を低減できるため、耐久性を
高め、また、熱交換管体の熱計算が容易となる。
According to the third aspect of the present invention, the oxygen-containing gas for combustion, for example, air of the heat exchange heat medium introduced into the introduction chamber of the heat medium passage through which the combustion exhaust gas flows, is supplied to the introduction chamber by one end. The plurality of heat exchange pipes communicates with each other, and heat exchanges with the combustion exhaust gas flowing into the substantially spiral introduction side heat exchange pipes and flowing through the heat medium passage. The heat is exchanged with the combustion exhaust gas through the communication pipes connected to the end and flows to the outlet side heat exchange pipe while flowing out to the outlet chamber.The heat exchange becomes a cross flow and heat is exchanged with high thermal efficiency. The heat exchange heat of the oxygen-containing gas for combustion flowing through the side heat exchange pipe section and the outlet side heat exchange pipe section is substantially equalized, and the temperature rise of each heat exchange pipe body is low even if the heat exchange rate is increased. Since heat damage to the heat exchange tube can be reduced, durability is improved and heat exchange Body heat calculation becomes easy.

【0064】請求項4記載の発明によれば、熱源熱媒体
通路の下流側の第1の熱交換部にて熱交換された被熱交
換熱媒体の燃焼用酸素含有ガスは導出室から熱源熱媒体
通路の上流側の第2の熱交換部の導入室に導入されて再
び熱交換され、燃焼排ガスの熱を効率よく予熱すること
ができる。
According to the fourth aspect of the present invention, the combustion-containing oxygen-containing gas of the heat exchange heat medium that has undergone heat exchange in the first heat exchange section on the downstream side of the heat source heat medium passage is supplied from the outlet chamber to the heat source heat exchange medium. The heat is introduced again into the introduction chamber of the second heat exchange section on the upstream side of the medium passage and heat is exchanged again, so that the heat of the combustion exhaust gas can be efficiently preheated.

【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縦断
面図である。
FIG. 1 is a longitudinal sectional view of a heat exchange device showing one embodiment of the present invention.

【図2】同上横断面図である。FIG. 2 is a cross-sectional view of the same.

【図3】同上熱交換管部の斜視図である。FIG. 3 is a perspective view of the heat exchange tube section.

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

【図5】本発明の他の実施の形態を示すバーナ装置の縦
断面図である。
FIG. 5 is a longitudinal sectional view of a burner device showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1,12,14 熱源熱媒体通路 2,15,18 導入室 3,16,19 導出室 4,25,26 導入側熱交換管部 5,27,28 導出側熱交換管部 6,20,22 被熱交換管体 9,29,30 連通管部 21 第1の熱交換部 23 第2の熱交換部 1,12,14 Heat source heat medium passage 2,15,18 Inlet chamber 3,16,19 Outlet chamber 4,25,26 Inlet side heat exchange tube 5,27,28 Outlet side heat exchange tube 6,20,22 Heat exchange pipes 9, 29, 30 Communication pipe section 21 First heat exchange section 23 Second heat exchange section

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 熱源熱媒体通路と、この熱源熱媒体通路
の外周に沿ってこの熱源熱媒体通路を流動する熱源熱媒
体の流動方向に対して並設された被熱交換熱媒体の導入
室および導出室と、前記被熱交換熱媒体の導入室と導出
室とに両端部を連通接続して前記熱源熱媒体通路に配設
され被熱交換熱媒体が流動する複数の被熱交換管体とを
備え、 前記各被熱交換管体は、前記被熱交換熱媒体の導入室に
それぞれ外周側端部を連通接続し前記熱源熱媒体通路の
熱源熱媒体の流動方向に対して直交する面に配設される
渦巻状の導入側熱交換管部と、前記被熱交換熱媒体の導
出室にそれぞれ外周側端部を連通接続し前記熱源熱媒体
通路の熱源熱媒体の流動方向に対して直交する面に配設
される渦巻状の導出側熱交換管部と、前記導入側熱交換
管部と導出側熱交換管部との内周側端部を互いに連通接
続し前記熱源熱媒体通路を流動する熱源熱媒体の流動方
向に配設される直線状の連通管部とを有し、 前記各被熱交換管体の導入側熱交換管部と導出側熱交換
管部とを連通接続する連通管部の長さをそれぞれ異なる
長さとし、この連通管部の長さが長い被熱交換管体の導
入側熱交換管部と導出側熱交換管部との間に連通管部の
長さが短い被熱交換管体の導入側熱交換管部と導出側熱
交換管部を順次に配設して複数の被熱交換管体の導入側
熱交換管部と導出側熱交換管部とを前記熱媒体通路の熱
源熱媒体の流動方向に並設したことを特徴とした熱交換
装置。
1. A heat source heat medium passage, and an introduction chamber for a heat exchange heat medium which is arranged along the outer periphery of the heat source heat medium passage in a flow direction of the heat source heat medium flowing through the heat source heat medium passage. And a plurality of heat exchange tubes in which the heat exchange heat medium flows, the heat exchange heat medium flowing through the heat exchange heat medium passage, wherein the heat exchange heat medium flows through the heat exchange heat medium. Wherein each of the heat exchange pipes has an outer peripheral end connected to an introduction chamber of the heat exchange heat medium, and a surface orthogonal to the flow direction of the heat source heat medium in the heat source heat medium passage. And a spiral-shaped inlet-side heat exchange pipe portion, which is disposed at the outer peripheral end of the heat-exchanged heat medium outlet chamber. A spiral outlet-side heat exchange tube portion disposed on a surface orthogonal to the surface, A linear communication pipe portion connected to the inner peripheral end of the heat exchange pipe portion with each other and arranged in the flow direction of the heat source heat medium flowing through the heat source heat medium passage, and The lengths of the communication pipes that connect and connect the inlet-side heat exchange pipe section and the outlet-side heat exchange pipe section of the exchange pipe body are different from each other. The length of the communicating pipe section is short between the side heat exchange pipe section and the discharge side heat exchange pipe section, and the inlet side heat exchange pipe section and the discharge side heat exchange pipe section of the heat exchange pipe body are sequentially arranged. A heat exchange apparatus, wherein an inlet-side heat exchange pipe section and an outlet-side heat exchange pipe section of a plurality of heat exchange pipes are arranged in parallel in a flow direction of a heat source heat medium in the heat medium passage.
【請求項2】 熱源熱媒体通路の熱源熱媒体が流動する
下流側に第1の熱交換部を形成するとともに上流側に第
2の熱交換部を形成し、 前記第1の熱交換部は前記熱源熱媒体通路の熱源熱媒体
が流動する下流側に被熱交換熱媒体の導入室を形成する
とともに前記熱源熱媒体通路の熱源熱媒体が流動する上
流側に被熱交換熱媒体の導出室を形成し、 前記第2の熱交換部は前記熱源熱媒体通路の熱源熱媒体
が流動する上流側に被熱交換熱媒体の導入室を形成する
とともに前記熱源熱媒体通路の熱源熱媒体が流動する下
流側に被熱交換熱媒体の導出室を形成し、 前記第1の熱交換部の被熱交換熱媒体の導出室に前記第
2の熱交換部の被熱交換熱媒体の導入室を連通し、 前記第1の熱交換部と第2の熱交換部とにそれぞれ両端
部を被熱交換熱媒体の導入室と導出室とに接続した被熱
交換熱媒体が流動する複数の被熱交換管体を熱源熱媒体
通路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。
2. A first heat exchange section is formed on the downstream side of the heat source heat medium passage where the heat source heat medium flows, and a second heat exchange section is formed on the upstream side, wherein the first heat exchange section is A heat exchange heat medium introduction chamber is formed downstream of the heat source heat medium passage where the heat source heat medium flows, and a heat exchange heat medium outlet chamber is formed upstream of the heat source heat medium passage where the heat source heat medium flows. The second heat exchange unit forms an introduction chamber for the heat exchange heat medium on the upstream side of the heat source heat medium passage where the heat source heat medium flows, and the heat source heat medium of the heat source heat medium passage flows. A discharge chamber for the heat exchange heat medium is formed on the downstream side of the first heat exchange section, and an introduction chamber for the heat exchange heat medium of the second heat exchange section is formed in the discharge chamber for the heat exchange heat medium in the first heat exchange section. Both ends of the first heat exchange unit and the second heat exchange unit are connected to the heat exchange heat medium. Entry and heat exchange device according to claim 1, wherein the heat exchanger heat medium connected to the outlet chamber, characterized in that disposed in the heat source heat medium passage a plurality of the heat exchange tubes body flowing.
【請求項3】 燃焼部と、この燃焼部の燃焼排ガスが流
動する熱源熱媒体通路と、この熱源熱媒体通路の外周に
沿ってこの熱源熱媒体通路を流動する燃焼排ガスの流動
方向に対して並設された燃焼用酸素含有ガスの導入室お
よび前記燃焼部の燃焼用酸素含有ガス導入部に連通され
た燃焼用酸素含有ガスの導出室と、前記燃焼用酸素含有
ガスの導入室と導出室とに両端部を連通接続して前記熱
源熱媒体通路に配設され燃焼用酸素含有ガスが流動する
複数の被熱交換管体とを備え、 前記各被熱交換管体は、前記燃焼用酸素含有ガスの導入
室にそれぞれ外周側端部を連通接続し前記熱源熱媒体通
路の燃焼排ガスの流動方向に対して直交する面に配設さ
れる渦巻状の導入側熱交換管部と、前記燃焼用酸素含有
ガスの導出室にそれぞれ外周側端部を連通接続し前記熱
源熱媒体通路の燃焼排ガスの流動方向に対して直交する
面に配設される渦巻状の導出側熱交換管部と、前記導入
側熱交換管部と導出側熱交換管部との内周側端部を互い
に連通接続し前記熱源熱媒体通路を流動する燃焼排ガス
の流動方向に配設される直線状の連通管部とを有し、 前記各被熱交換管体の導入側熱交換管部と導出側熱交換
管部とを連通接続する連通管部の長さをそれぞれ異なる
長さとし、この連通管部の長さが長い被熱交換管体の導
入側熱交換管部と導出側熱交換管部との間に連通管部の
長さが短い被熱交換管体の導入側熱交換管部と導出側熱
交換管部を順次に配設して複数の被熱交換管体の導入側
熱交換管部と導出側熱交換管部とを前記熱媒体通路の熱
源熱媒体の流動方向に並設したことを特徴としたバーナ
装置。
3. A combustion section, a heat source heat medium passage through which flue gas from the combustion section flows, and a flow direction of the combustion exhaust gas flowing through the heat source heat medium passage along an outer periphery of the heat source heat medium passage. A combustion oxygen-containing gas introduction chamber and a combustion oxygen-containing gas discharge chamber communicated with the combustion oxygen-containing gas introduction section of the combustion section, and an introduction chamber and a discharge chamber of the combustion oxygen-containing gas. And a plurality of heat exchange pipes disposed in the heat source heat medium passage and having a flow of the oxygen-containing gas for combustion flowing therethrough. A spiral introduction-side heat exchange pipe section which is connected to an outer peripheral end of each of the introduction chambers for the contained gas and is disposed on a surface orthogonal to a flow direction of the combustion exhaust gas in the heat source heat medium passage; Outer end of each oxygen-containing gas communication chamber A spiral outlet-side heat exchange tube portion, which is disposed on a surface orthogonal to the flow direction of the combustion exhaust gas in the heat source heat medium passage, and the inlet-side heat exchange tube portion and the outlet-side heat exchange tube portion; And a linear communication pipe portion connected to the inner peripheral end portions of the heat exchange pipes and disposed in the flow direction of the combustion exhaust gas flowing in the heat source heat medium passage, and the introduction side of each of the heat exchange pipe bodies. The lengths of the communication pipes that connect and connect the heat exchange pipes and the outlet-side heat exchange pipes are different lengths, and the length of the communication pipes is longer than the length of the introduction-side heat exchange pipes of the heat exchange pipes. A plurality of heat exchange pipes are provided by sequentially arranging an inlet heat exchange pipe section and an outlet heat exchange pipe section of a heat exchange pipe body having a short communication pipe section with the outlet heat exchange pipe section. A burner device, wherein a heat-introducing tube portion and an outlet-side heat exchanging tube portion of a body are juxtaposed in a flow direction of a heat source heat medium in the heat medium passage.
【請求項4】 熱源熱媒体通路の燃焼排ガスが流動する
下流側に第1の熱交換部を形成するとともに上流側に第
2の熱交換部を形成し、 前記第1の熱交換部は前記熱源熱媒体通路の燃焼排ガス
が流動する下流側に燃焼用酸素含有ガスの導入室を形成
するとともに前記熱源熱媒体通路の燃焼排ガスが流動す
る上流側に燃焼部の燃焼用酸素含有ガス導入部に連通さ
れた被熱交換熱媒体の導出室を形成し、 前記第2の熱交換部は前記熱源熱媒体通路の燃焼排ガス
が流動する上流側に燃焼用酸素含有ガスの導入室を形成
するとともに前記熱源熱媒体通路の燃焼排ガスが流動す
る下流側に燃焼用酸素含有ガスの導出室を形成し、 前記第1の熱交換部の燃焼用酸素含有ガスの導出室に前
記第2の熱交換部の燃焼用酸素含有ガスの導入室を連通
し、 前記第1の熱交換部と第2の熱交換部とにそれぞれ両端
部を燃焼用酸素含有ガスの導入室と導出室とに接続した
燃焼用酸素含有ガスが流動する複数の被熱交換管体を熱
源熱媒体通路に配設したことを特徴とする請求項3記載
のバーナ装置。
4. A first heat exchange section is formed on the downstream side of the heat source heat medium passage where the combustion exhaust gas flows, and a second heat exchange section is formed on the upstream side, wherein the first heat exchange section is A combustion oxygen-containing gas introduction chamber is formed on the downstream side where the combustion exhaust gas of the heat source heat medium passage flows, and the combustion oxygen-containing gas introduction section of the combustion section is formed on the upstream side where the combustion exhaust gas of the heat source heat medium passage flows. The second heat exchange section forms an introduction chamber for the oxygen-containing gas for combustion on the upstream side where the combustion exhaust gas flows in the heat source heat medium passage. A discharge chamber for the oxygen-containing gas for combustion is formed on the downstream side of the heat source heat medium passage where the combustion exhaust gas flows, and a discharge chamber for the oxygen-containing gas for combustion in the first heat exchange section is provided in the second heat exchange section. Communicating the introduction chamber for the oxygen-containing gas for combustion, A plurality of heat exchange tubes through which the oxygen-containing gas for combustion flows are connected to the inlet and outlet chambers for the oxygen-containing gas for combustion, respectively. 4. The burner device according to claim 3, wherein the burner device is disposed in the medium passage.
JP9226258A 1997-08-22 1997-08-22 Heat exchanger and burner Pending JPH1163859A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9226258A JPH1163859A (en) 1997-08-22 1997-08-22 Heat exchanger and burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9226258A JPH1163859A (en) 1997-08-22 1997-08-22 Heat exchanger and burner

Publications (1)

Publication Number Publication Date
JPH1163859A true JPH1163859A (en) 1999-03-05

Family

ID=16842388

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9226258A Pending JPH1163859A (en) 1997-08-22 1997-08-22 Heat exchanger and burner

Country Status (1)

Country Link
JP (1) JPH1163859A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110423881A (en) * 2019-08-28 2019-11-08 浙江丰业集团有限公司 A kind of long-range roller-hearth solution annealing furnace
US11781940B2 (en) 2018-04-19 2023-10-10 Kairos Water, Inc. Fluid control system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11781940B2 (en) 2018-04-19 2023-10-10 Kairos Water, Inc. Fluid control system
CN110423881A (en) * 2019-08-28 2019-11-08 浙江丰业集团有限公司 A kind of long-range roller-hearth solution annealing furnace

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