JPH0195290A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH0195290A
JPH0195290A JP25223187A JP25223187A JPH0195290A JP H0195290 A JPH0195290 A JP H0195290A JP 25223187 A JP25223187 A JP 25223187A JP 25223187 A JP25223187 A JP 25223187A JP H0195290 A JPH0195290 A JP H0195290A
Authority
JP
Japan
Prior art keywords
heat
pipe
heat transfer
heat pipe
transfer medium
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
JP25223187A
Other languages
Japanese (ja)
Inventor
Takeshi Terada
武 寺田
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP25223187A priority Critical patent/JPH0195290A/en
Publication of JPH0195290A publication Critical patent/JPH0195290A/en
Pending legal-status Critical Current

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  • Central Heating Systems (AREA)

Abstract

PURPOSE:To alleviate the effect of dispersion of thermal stress as well as to enable heating to a heat transfer medium at a uniform temperature, by covering a heat pipe with a heat- insulating material, by positioning the evaporation part on the lower end of a heat pipe in a part confronting a heating source such as combustion gas, and by piercing a heat transfer pipe which flows the heat transfer medium through it through a condensation part on the upper end of a heat pipe. CONSTITUTION:The inlet side of a heat transfer medium is formed by inserting a heat transfer pipe 1 in a heat pipe 3 from the middle body of a pipe, piercing through its pipe wall. The heat transfer pipe 1 is a piping formed in a 'U' shape, extending in the direction to the top end of a condensation part 3b along the axis of a heat pipe 3, passing through the condensation part 3b, going outside piercing through the top end, forming an outlet side. A structure is such that the heat transfer pipe 1 is heated by the evaporating latent heat in the condensation part 3b of a heat pipe 3. The middle body of a heat pipe 3 is held by the wall of a furnace 5 by the intermediary of a heat-insulating material 6, so that the evaporation part 3a of a heat pipe 3 is projected to a heating source 8 in high temperature, from a through hole 9 provided on the wall of a furnace 5. The side of a condensation part 3b through which the heat transfer pipe 1 is pierced is projected to the outside of a combustion furnace. The exposed part is covered with a warmth-keeping material 7.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、ヒートパイプを利用して均一加熱を行う熱交
換装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a heat exchange device that performs uniform heating using a heat pipe.

〔従来の技術〕[Conventional technology]

従来、熱交換器は金属管が伝熱壁となっているものが広
く使用され、金属管である伝熱壁を間に挟み、その外側
及び内側にそれぞれ伝熱媒体を通流させ、伝熱壁の熱伝
導によつて伝熱媒体の加熱又は冷却が行なわれるように
なされている。
Conventionally, heat exchangers with metal tubes as heat transfer walls have been widely used, and heat transfer is performed by sandwiching the heat transfer wall, which is a metal tube, and passing a heat transfer medium through the outside and inside of the wall. The heat transfer medium is heated or cooled by heat conduction through the walls.

数拾度ないし数百度という湿度領域において、低温域で
の熱交換は、金属管の外側における加熱流体の対流熱伝
達によって、管内の伝熱媒体への伝熱が行なわれるよう
になっており、一般の管板式熱交換器がこれである。一
方高温域での熱交換は、例えばボイラに見られる如く、
燃料の燃焼による火焔などの輻射と、燃焼ガスの対流熱
伝達とによって、伝熱管内の伝熱媒体を伝熱するように
なされており、加熱量のバランスを考慮して計画する必
要がある。
Heat exchange at low temperatures in the humidity range of several tens to hundreds of degrees is performed by convective heat transfer of the heated fluid on the outside of the metal tube to the heat transfer medium inside the tube. This is a common tube plate heat exchanger. On the other hand, heat exchange in high temperature ranges, as seen in boilers, for example,
Heat is transferred to the heat transfer medium in the heat transfer tube by radiation such as flames caused by combustion of fuel and convective heat transfer of combustion gas, and it is necessary to plan with the balance of heating amount in consideration.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

以下問題点を従来例の熱交換装置の図面に基づいて説明
する。
The problems will be explained below based on drawings of a conventional heat exchange device.

第3図は、多管式熱交換装置の概略を示す部分断面図で
符号10は燃焼装置である。燃焼装置10は、内部下方
にバーナー12を配備し、供給される重油等を燃焼させ
ることにより燃焼焔ならびに燃焼ガスとからなる燃焼域
11を装置10の内部に形成させる、そして廃ガスを装
置10の上方に設けられている煙道15から排出するよ
うになっている。燃焼装置lOの燃焼域11の側壁16
には、伝熱媒体(冷媒)が矢印のように通流する伝熱管
1が複数本、燃焼域の上方から側壁を外から貫通して入
り、側壁に沿って垂直に下方へ延伸し、燃焼域の下方か
ら側壁16を貫通して外部に接続されるように配備され
ている。
FIG. 3 is a partial sectional view schematically showing a multi-tubular heat exchange device, and numeral 10 is a combustion device. The combustion device 10 has a burner 12 disposed in the lower part of the interior, and burns supplied heavy oil etc. to form a combustion zone 11 consisting of combustion flame and combustion gas inside the device 10, and waste gas is transferred to the device 10. It is designed to be discharged from a flue 15 provided above. Side wall 16 of combustion zone 11 of combustion device IO
A plurality of heat transfer tubes 1 through which a heat transfer medium (refrigerant) flows in the direction of the arrow enter from above the combustion zone by penetrating the side wall from the outside, and extend vertically downward along the side wall. It is arranged so as to penetrate the side wall 16 from below the area and be connected to the outside.

このように構成された高温域の熱交換装置において、伝
熱管1は、燃焼焔及び燃焼装置内壁からの輻射伝達と、
燃焼ガスの対流熱伝達にさらされることによって加熱さ
れるので、燃焼域内の温度分布を一定に保持しうるよう
に、燃焼条件を整えるように計画することは極めて繁雑
な計算を伴うとともに、よしんば計画ができたとしても
伝熱管を均一な温度に加熱することは、実際上極めて困
難である。従って不均一な熱分布と熱移動のため伝熱管
の伸び曲がりにバラツキを生じ、熱応力的問題を生ずる
という不利を避は得なかった。
In the high-temperature region heat exchange device configured in this way, the heat transfer tubes 1 are capable of transmitting combustion flame and radiation from the inner wall of the combustion device,
Since the combustion gas is heated by being exposed to convective heat transfer, planning the combustion conditions to maintain a constant temperature distribution within the combustion zone requires extremely complicated calculations, and the Yoshiba Plan Even if it were possible, it is actually extremely difficult to heat the heat exchanger tube to a uniform temperature. Therefore, due to non-uniform heat distribution and heat transfer, the elongation and bending of the heat exchanger tubes becomes uneven, which inevitably causes thermal stress problems.

特に燃料電池プラントにおける燃料改質装置の熱交換器
において上記の問題は、重大な影響を及ぼし製作上の難
点となっている。
In particular, the above-mentioned problem has a serious effect on the heat exchanger of a fuel reformer in a fuel cell plant, and is a manufacturing difficulty.

本発明は上記の問題点に鑑みなされたもので、均一な温
度で伝熱媒体を加熱するとともに熱応力のバラツキの影
響を減少し、設計のための繁雑さを軽減するなどを目的
とするものである。
The present invention was made in view of the above problems, and aims to heat a heat transfer medium at a uniform temperature, reduce the influence of variations in thermal stress, and reduce complexity in design. It is.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は伝熱媒体(冷媒)が通流する伝熱管が、燃焼焔
や燃焼ガスあるいは廃ガス等の高温部に直接接触するこ
とにより生ずる、加熱の不均一性や応力のアンバランス
を避けるため、ヒートパイプを介在させて上記目的を達
成しようとするものである。
The present invention aims to avoid uneven heating and unbalanced stress caused by direct contact of heat transfer tubes through which a heat transfer medium (refrigerant) flows with high-temperature parts such as combustion flames, combustion gas, or waste gas. , attempts to achieve the above object by interposing a heat pipe.

すなわち、ヒートパイプを断熱材で覆い、前記ヒートパ
イプの下端側の蒸発部を燃焼ガスあるいは高温部ガスな
どの加熱源に対応する部分に位置させ、前記ヒートパイ
プの上端側の凝縮部に伝熱媒体を通流させる伝熱管を貫
通させて熱交換装置を構成した。
That is, the heat pipe is covered with a heat insulating material, the evaporating part at the lower end of the heat pipe is located in a part corresponding to the heat source such as combustion gas or high temperature gas, and heat is transferred to the condensing part at the upper end of the heat pipe. A heat exchange device was constructed by passing a heat transfer tube through which a medium flows.

〔作用〕[Effect]

本発明は、高温熱源と伝熱管との熱の授受をヒートパイ
プを介在して行なうようにしたことにより、伝熱管が高
温熱源に直接さらされることがなくなるので、そのため
に起因する不都合が排除される。
In the present invention, heat is transferred between the high-temperature heat source and the heat transfer tube through the heat pipe, so that the heat transfer tube is no longer directly exposed to the high-temperature heat source, thereby eliminating the inconvenience caused by this. Ru.

すなわち、ヒートパイプの蒸発部を燃焼装置の燃焼域内
や廃ガス通路内に突出するように配備し、高温熱源の熱
でヒートパイプ内の作動液を蒸発させ、その蒸気はヒー
トパイプ内に生起される圧力差によってヒートパイプの
am部へ送られ蒸発潜熱を放出する。ヒートパイプの凝
縮部分には伝熱媒体(冷媒)が通流するようになってい
る伝熱管が挿置されているので、蒸発潜熱によって伝熱
管内の伝熱媒体(冷媒)が加熱される。従って伝熱管は
、常に均一な温度の作動液の蒸気によって加熱されるた
め、還流する伝熱媒体(冷媒)は均一な温度に加温され
るとともに熱分布の不均一がなくなるためそれに起因す
る問題に対する不安はなくなるのである。
In other words, the evaporation part of the heat pipe is arranged so as to protrude into the combustion zone of the combustion device or into the waste gas passage, and the working fluid in the heat pipe is evaporated by the heat of the high-temperature heat source, and the steam is generated in the heat pipe. Due to the pressure difference, the latent heat of vaporization is sent to the am section of the heat pipe and releases the latent heat of vaporization. Since a heat transfer tube through which a heat transfer medium (refrigerant) flows is inserted in the condensing portion of the heat pipe, the heat transfer medium (refrigerant) in the heat transfer tube is heated by the latent heat of vaporization. Therefore, the heat transfer tubes are always heated by the vapor of the working fluid at a uniform temperature, so the circulating heat transfer medium (refrigerant) is heated to a uniform temperature and uneven heat distribution is eliminated, thereby eliminating problems caused by this. The anxiety about it disappears.

高温熱源における温度分布の問題は、ヒートパイプの蒸
発部の加熱に係る問題であるので多少のバラツキは許容
されるので、その意味での計画上の難しさも緩和される
The problem of temperature distribution in a high-temperature heat source is a problem related to heating of the evaporation section of a heat pipe, so some variation is allowed, so the difficulty in planning in that sense is alleviated.

〔実施例〕〔Example〕

以下本発明の実施例の図面に基づいて説明する。 Embodiments of the present invention will be described below based on the drawings.

第1図は、本発明の第1実施例の構成を示す部分断面図
で、第2図は第2実施例の構成を示す部分断面図である
FIG. 1 is a partial sectional view showing the structure of a first embodiment of the present invention, and FIG. 2 is a partial sectional view showing the structure of a second embodiment.

第1図において、1は伝熱管で、伝熱媒体(冷媒)が矢
印のように通流するように形成されているU字管である
(なお伝熱媒体の供給、排出の詳細は本発明の説明に直
接関与しないので割愛することとする)、すなわちヒー
トパイプ3の中間胴部分から管壁を貫通してその内部に
入り伝熱媒体の流入側を形成し、それがヒートパイプ3
の軸心に沿って凝縮部3bの終端方向へ延伸して凝縮部
3b内を通り抜け、その終端部を貫通して外部へ出、流
出側を形成するようにU字形に形成されている管路であ
る。したがって伝熱管1は、ヒートパイプ3の凝縮部3
bにおける蒸発潜熱によって加熱されるのである。
In FIG. 1, reference numeral 1 denotes a heat transfer tube, which is a U-shaped tube formed so that a heat transfer medium (refrigerant) flows as shown by the arrow. In other words, it penetrates the pipe wall from the intermediate body part of the heat pipe 3 and enters the inside thereof, forming the inflow side of the heat transfer medium, which forms the inflow side of the heat transfer medium.
A conduit formed in a U-shape so as to extend along the axis of the condensing part 3b toward the terminal end of the condensing part 3b, pass through the condensing part 3b, pass through the terminal end, go out to the outside, and form an outflow side. It is. Therefore, the heat exchanger tube 1 is the condensing section 3 of the heat pipe 3.
It is heated by the latent heat of vaporization at b.

ヒートパイプ3は、燃焼装置壁5に設けられている貫通
孔9から、その蒸発部3aを高温熱源8中に突出するよ
うに、中間胴部分が断熱材6を介して燃焼装置壁5によ
って保持されている。そして伝熱管1を挿置している凝
縮部3b側は燃焼装置の外方へ出されている。その露出
部分は保温材7にて覆われている。なお、第1の実施例
は、1本の伝熱管しか示していないが、複数にすること
は何隻差支えはない。
The heat pipe 3 has an intermediate body portion held by the combustion device wall 5 via a heat insulating material 6 so that its evaporating portion 3a projects into the high-temperature heat source 8 from a through hole 9 provided in the combustion device wall 5. has been done. The condensing section 3b side in which the heat exchanger tube 1 is inserted is exposed to the outside of the combustion device. The exposed portion is covered with a heat insulating material 7. Note that although the first embodiment shows only one heat exchanger tube, it does not matter how many there are.

次に第2実施例は、第2図に示されるように、上記例の
伝熱管にかえ、伝熱管として作用するとともに伝熱媒体
の流出路となる外被管2aと、伝熱媒体の流入路として
外被管2aと同心にその中に挿入される内被管2bとか
らなる、2重管形式のバヨネット管2を用い、ヒートパ
イプ3゛の凝縮部3b内に挿置して形成している点が第
1の実施例と異なるが作用、効果は全(同じである。な
お、第2図において外被管2aと内被管2bとの間に触
媒層17を図示しであるがこれは単に伝熱のみでなく、
化学反応(吸熱反応)の場合にも利用できることを示し
ているのである。
Next, as shown in FIG. 2, in the second embodiment, instead of the heat transfer tube of the above example, a jacket tube 2a that acts as a heat transfer tube and serves as an outflow path for the heat transfer medium, and a jacket tube 2a for the inflow of the heat transfer medium. A double-tube type bayonet tube 2 consisting of an outer jacket tube 2a and an inner jacket tube 2b inserted concentrically therein is used as a channel, and is inserted into the condensing part 3b of the heat pipe 3. Although it differs from the first embodiment in that it is different from the first embodiment, the operation and effect are the same.Although the catalyst layer 17 is shown between the outer jacket tube 2a and the inner jacket tube 2b in FIG. This is not just about heat transfer;
This shows that it can also be used in chemical reactions (endothermic reactions).

〔発明の効果〕〔Effect of the invention〕

本発明は、上記のように高温熱源と伝熱管又はバヨネッ
ト管との間に、ヒートパイプを介在させ伝熱を行なうよ
うにしたことにより、従来的な加熱反応管特に内部に触
媒等が封入された改賀装置などの如く均一な加熱伝熱面
を必要とする熱交換装置として好適なものとすることが
できた。すなわち伝熱媒体(冷媒)が通流する伝熱管に
対する、従来見られる加熱温度の不均一性にもとづく諸
問題を、ヒートパイプを介在させることにより、その対
策をし易くするとともに、ヒートパイプの熱移転の特性
を生かし、伝熱管の適切な配置により均一な伝熱媒体の
加熱という難問をも容昌に克服することができるのであ
る。
As described above, the present invention interposes a heat pipe between the high-temperature heat source and the heat transfer tube or bayonet tube to perform heat transfer, thereby eliminating the need for a conventional heating reaction tube, especially a catalyst etc. sealed inside. It was possible to make it suitable for a heat exchange device that requires a uniform heating heat transfer surface, such as a converter device. In other words, by interposing a heat pipe, it is easier to solve various problems caused by non-uniform heating temperature of heat transfer tubes through which a heat transfer medium (refrigerant) flows. Taking advantage of the transfer characteristics, it is possible to easily overcome the difficult problem of uniformly heating the heat transfer medium by appropriately arranging the heat transfer tubes.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の第1実施例の構成を示す部分断面図、
第2図は第2実施例の構成を示す部分断面図で、第3図
は従来の多管式熱交換装置の概略を示す部分断面図であ
る。 1:伝熱管、2:バヨネット管、3:ヒートパイプ、3
a=蒸発部、3b:凝縮部、lO:燃焼装置、11:燃
焼域。
FIG. 1 is a partial sectional view showing the configuration of a first embodiment of the present invention;
FIG. 2 is a partial cross-sectional view showing the configuration of a second embodiment, and FIG. 3 is a partial cross-sectional view schematically showing a conventional multi-tubular heat exchanger. 1: heat transfer tube, 2: bayonet tube, 3: heat pipe, 3
a=evaporation section, 3b: condensation section, lO: combustion device, 11: combustion zone.

Claims (1)

【特許請求の範囲】[Claims] 1)内部に作動液を封入し立方向に配置されたヒートパ
イプを断熱材で覆い、前記ヒートパイプの下端側の蒸発
部の燃焼ガスあるいは高温廃ガスなどの加熱源に対応す
る部分に位置させ、前記ヒートパイプの上端側の凝縮部
に伝熱媒体を通流させる伝熱管を貫通させ、その際前記
ヒートパイプ内において作動液を蒸発させ前記伝熱管を
長手方向に均一温度に保つようにしたことを特徴とする
熱交換装置。
1) A heat pipe with a working fluid sealed inside and arranged vertically is covered with a heat insulating material, and the heat pipe is placed at the lower end of the evaporation part of the heat pipe in the part corresponding to the heating source such as combustion gas or high temperature waste gas. A heat transfer tube through which a heat transfer medium flows is passed through the condensation section on the upper end side of the heat pipe, and at this time, the working fluid is evaporated within the heat pipe to maintain a uniform temperature in the longitudinal direction of the heat transfer tube. A heat exchange device characterized by:
JP25223187A 1987-10-06 1987-10-06 Heat exchanger Pending JPH0195290A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25223187A JPH0195290A (en) 1987-10-06 1987-10-06 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25223187A JPH0195290A (en) 1987-10-06 1987-10-06 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH0195290A true JPH0195290A (en) 1989-04-13

Family

ID=17234341

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25223187A Pending JPH0195290A (en) 1987-10-06 1987-10-06 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH0195290A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4992232A (en) * 1987-08-31 1991-02-12 General Electric Company Method to control N-16 radiation levels in steam phase BWRs
US5171515A (en) * 1988-04-20 1992-12-15 Westinghouse Electric Corp. Process for inhibiting corrosion in a pressurized water nuclear reactor
JP2010534128A (en) * 2007-07-20 2010-11-04 イエフペ Bayonet tube exchanger-reactor enabling operation with a pressure difference of about 100 bar between the tube side and the shell side
CN107421365A (en) * 2017-07-31 2017-12-01 大连碧蓝节能环保科技有限公司 Adjust heat exchange area ratio formula heat pipe

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4992232A (en) * 1987-08-31 1991-02-12 General Electric Company Method to control N-16 radiation levels in steam phase BWRs
US5171515A (en) * 1988-04-20 1992-12-15 Westinghouse Electric Corp. Process for inhibiting corrosion in a pressurized water nuclear reactor
JP2010534128A (en) * 2007-07-20 2010-11-04 イエフペ Bayonet tube exchanger-reactor enabling operation with a pressure difference of about 100 bar between the tube side and the shell side
CN107421365A (en) * 2017-07-31 2017-12-01 大连碧蓝节能环保科技有限公司 Adjust heat exchange area ratio formula heat pipe

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