JPS6064187A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS6064187A
JPS6064187A JP17196183A JP17196183A JPS6064187A JP S6064187 A JPS6064187 A JP S6064187A JP 17196183 A JP17196183 A JP 17196183A JP 17196183 A JP17196183 A JP 17196183A JP S6064187 A JPS6064187 A JP S6064187A
Authority
JP
Japan
Prior art keywords
fluid
ceramic
heated
heat exchanger
tube
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.)
Granted
Application number
JP17196183A
Other languages
Japanese (ja)
Other versions
JPH0319474B2 (en
Inventor
Kazuhiko Ito
一彦 伊藤
Jun Yonehara
米原 潤
Minoru Yamaguchi
実 山口
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP17196183A priority Critical patent/JPS6064187A/en
Publication of JPS6064187A publication Critical patent/JPS6064187A/en
Publication of JPH0319474B2 publication Critical patent/JPH0319474B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/04Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone

Landscapes

  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To eliminate the possibility of breakage by a method wherein a ceramic pipe, communicating the supplying port of a fluid to be heated with the outflow port thereof, is suspended in parallel to the axial direction by a compression spring cooled by the fluid to be heated. CONSTITUTION:When high-temperature exhaust gas is flowed into the flow path of heat transfer fluid in a frame body 1 and the normal-temperature fluid to be heated is sent into a plurality of ceramic pipes 5, provided with supporting pipes 8, 9 communicated with the through holes 10, 10' of opposing wall surfaces 2, 2', from a supplying port 3, heat exchange is effected between the high-temperature exhaust gas and the fluid to be heated through the walls of the ceramic pipes. The ceramic pipes 5 can be slid slightly into the axial direction thereof by the compression springs 14 provided between the supporting pipe 8 of one side and the wall surface 2. According to this method, heat may be retrieved efficiently from the high-temperature exhaust gas or corrosive gas of 1,000 deg.C or more, further, ununiform thermal ecpansions or contractions, generated in respective ceramic pipes, may be absorbed and the breakage of the ceramic pipes may be prevented.

Description

【発明の詳細な説明】 (M業上の利用分野) 本発明は各種工業炉から排出される排熱の回収をするシ
ェルアンドチューブ型の熱交換器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of industrial application) The present invention relates to a shell-and-tube heat exchanger for recovering waste heat discharged from various industrial furnaces.

(従来技術) 各種工業炉の排熱を熱交換器により回収して慾焼用空気
を予熱することは最も効果的な省エネルギー対策として
広く行なわれているところであって、従来よりこの種の
用徐にはシェルアンドチューブ型の熱交換器が実用化さ
iしている。ところが従来のこの種熱交換器では被加熱
流体を原曲させる伝熱管としてステンレスm管が使用さ
れているため、その耐熱許容温度は約800°Cであり
、空気流による内部冷却を考慮しても/ OQ O”(
S以上の高温の排ガスとの熱交換には用いることができ
ず、また、ステンレス鋼管は排ガスによる腐食を受け易
いために排ガス組成によって利用範囲が大幅に限定され
る欠点があった。でこで、耐熱性及び耐腐食性に優れた
セラミックス管を伝熱管に用いる試みもなされてきたが
、セラミックス9f+よ金属管のように支持壁に溶接す
ることかできないうえしこ金属管に比較して製造上の寸
法誤差が大きいので支持壁に密接保持させ難く、また、
何らかの手段で支持壁1こ強固に取付Gjた場合には金
属管よりも脆いために熱応力により破損し易いC?i 
JIll々の問題点がある。
(Prior art) Recovering waste heat from various industrial furnaces using a heat exchanger to preheat air for burning is widely used as the most effective energy-saving measure. A shell-and-tube heat exchanger has been put into practical use. However, in conventional heat exchangers of this type, stainless steel m-tubes are used as heat transfer tubes to bend the heated fluid, so the allowable heat resistance temperature is approximately 800°C, which takes into account internal cooling by air flow. Mo / OQ O” (
Stainless steel pipes cannot be used for heat exchange with exhaust gas at temperatures higher than S or higher, and stainless steel pipes are easily corroded by exhaust gas, so they have the disadvantage that their range of use is severely limited depending on the composition of the exhaust gas. Attempts have been made to use ceramic tubes, which have excellent heat resistance and corrosion resistance, as heat transfer tubes, but compared to ceramic 9F+ metal tubes, which cannot be welded to support walls like metal tubes. Due to large dimensional errors during manufacturing, it is difficult to hold the support wall closely, and
If the support wall is firmly attached by some means, it is more brittle than a metal tube and is more likely to be damaged by thermal stressC? i
There are many problems.

(発明の目的) 本発明はこのような問題点を解決して1000°C以上
の高温度の排ガスにもあるいは腐食性のtJlガスにも
使用することができるうえに支持壁に対し破損の虞れな
く伝熱管を適確容易に取イ11けることのできる熱交換
器を目的として完成されたものである。
(Object of the Invention) The present invention solves these problems and can be used for exhaust gas with a high temperature of 1000°C or more or corrosive tJl gas, and also eliminates the risk of damage to the support wall. This was completed with the aim of creating a heat exchanger that allows heat exchanger tubes to be easily and accurately removed without being damaged.

(発明の構成) 本発明は内部を伝熱流体流路に形成した枠体の対向する
壁面間に被加熱流体の供給口と流出口に連通される多数
のセラミックス管を前記供給口から供給される被加熱流
体により冷却される圧縮スプリングをもって該セラミッ
クス管の軸線方向への膨張、収縮が吸収できるように並
行に架設したことを特徴とするものである。
(Structure of the Invention) The present invention provides a plurality of ceramic tubes, which are connected to a supply port and an outlet port for a fluid to be heated, between opposing walls of a frame whose interior is formed into a heat transfer fluid flow path. A compression spring cooled by a heated fluid is installed in parallel to absorb the expansion and contraction of the ceramic tube in the axial direction.

次に、本発明を図示の実施例について詳細に説明する。Next, the present invention will be explained in detail with reference to the illustrated embodiments.

第1図、第2図に示す第1の実施例において、(1)は
上下両面に開口部を有し、その内部を高温の排ガス等の
伝熱流体流路に形成した金属製の枠体であって、該枠体
(1)の対向する壁面(2)と壁面(2)の外側には被
加熱流体の供給口(3)を備えた流体流入室(3)と、
流出口(4)を備えた流体流出室(4)が設けられてい
る。(5)は炭化珪素のような耐熱性と耐腐食るための
フィン(6)が形成され、これらのセラミックス管(5
)は6角柱状の壁面構成体(7)、<rfn+]に挾持
させるとともに該壁面構成体(7)、(7)の外側をn
iJ記壁而壁面)、 (2)に多数配設された透孔01
、θ0に一端が取付けら力で前記供給口(3)と流出口
(4)V一連通ずる金属製の支持管(8)及び支持管(
9ンに接続させ、このようにして壁面T2)、(2)間
には多数のセラミックス管(5)が並行して架設される
。また、壁面構成体(7)/ 、(7)はセラミックス管(5)と同様に炭化珪素のよ
うなセラミックス材料からなり、その中央をこはセラミ
ックス管(5)の内径に等しい通孔0υ、0υが軸線方
向に設けられており、各壁面構成体(7)、(7)とセ
ラミックス管(5)との接合面μ4、Ga及び壁面(イ
へ成体(7)、(7fと支持管(8)、(9)との接合
面(1,1、θ)はいずれも球面に形成され、また、流
入側の支持’t’i’ 01)の内部には前記供給口(
3)から供給された被加熱流体に曝されて冷却される圧
縮スプリング04)が設置Jられている。この支持管(
8)は第2図に示さil、る↓つに壁面(2)の透孔θ
Qのまわりに溶接された金属製の外管(、ra)と、こ
の外管(J a)の内周向をこ密接しつつ軸方向tこ摺
動可能な内管(Jb)とからなり、外管(JR)の内部
には後端を壁面(2)に支承させるとともに前端を内W
 (Jb)に当接させて前記圧縮スフ゛リング0荀が設
けられており、内管G!rb)tよこの圧縮スプリング
041により押出されてその凸球面状の先端部を前記1
8 rJii itM m 仕1ワ+ /7)1111
 1番 iiF 44’ 6)fiハ iMi 1 1
j; 鋲 (jト −r lx ス、0また、他方の壁
面構成体(7)゛の外方の支持管(9)はその後部に抜
止めフランジ・(9)を有していて壁面構成体(7)を
移動不能に支持しており、セラミックス管(5)はこれ
らの壁面構成体(7)、(7)に両端が挾持された状態
で圧縮スプリング041の弾発力により壁面(2)、(
2)間に弾発的に架設されて軸線方向への膨張、Il、
V縮がこの14う縮スプリングθ勺によって吸収され、
このセラミックス管(5)は前記壁面構成体(7)、(
7)支持管(8)、(9)および壁面(2)、(2)の
透孔01、Q[Jを介して流体流入室(3)及び流体流
出室(4)に連通させることによりセラミックス管(5
)の内部を貫流する被加熱流体の流路を形成している。
In the first embodiment shown in FIGS. 1 and 2, (1) is a metal frame having openings on both upper and lower surfaces, and the inside thereof is formed as a flow path for heat transfer fluid such as high-temperature exhaust gas. a fluid inflow chamber (3) provided with an opposing wall surface (2) of the frame (1) and a supply port (3) for heated fluid on the outside of the wall surface (2);
A fluid outlet chamber (4) is provided with an outlet (4). (5) is formed with fins (6) for heat resistance and corrosion resistance such as silicon carbide, and these ceramic tubes (5)
) is sandwiched between the hexagonal columnar wall structure (7), <rfn+], and the outside of the wall structure (7), (7) is n
iJ wall and wall surface), (2) many through holes 01
, a metal support tube (8) and a support tube (
In this way, a large number of ceramic tubes (5) are installed in parallel between the wall surfaces T2) and (2). In addition, the wall structure (7)/ (7) is made of a ceramic material such as silicon carbide like the ceramic tube (5), and has a through hole 0υ equal to the inner diameter of the ceramic tube (5) in the center. 0υ is provided in the axial direction, and the joint surface μ4 between each wall structure (7), (7) and the ceramic tube (5), Ga and the wall surface (A), (7f) and the support tube ( The joint surfaces (1, 1, θ) with 8) and (9) are all formed into spherical surfaces, and the supply port (
A compression spring 04) is installed which is cooled by being exposed to the heated fluid supplied from 3). This support tube (
8) is shown in Fig. 2, and the through hole θ in the wall (2) is
It consists of a metal outer tube (, ra) welded around Q, and an inner tube (Jb) that can slide in the axial direction while keeping the inner circumferential direction of this outer tube (Ja) in close contact. Inside the outer tube (JR), the rear end is supported on the wall surface (2), and the front end is supported by the inner W.
The compression ring 0 is provided in contact with the inner pipe G! rb) It is pushed out by the compression spring 041 on the side of t and its convex spherical tip is
8 rJii itM m 1 wa + /7) 1111
No. 1 iiF 44' 6) fiha iMi 1 1
In addition, the outer support pipe (9) of the other wall structure (7) has a retaining flange (9) at its rear, and the wall structure The ceramic tube (5) supports the wall surface (2) immovably by the elastic force of the compression spring 041 while its both ends are held between the wall surface structures (7), (7). ), (
2) axial expansion, Il, elastically constructed between
V compression is absorbed by these 14 compression springs θ,
This ceramic tube (5) includes the wall structure (7), (
7) By communicating with the fluid inflow chamber (3) and fluid outflow chamber (4) through the support tubes (8), (9) and the through holes 01 and Q[J of the walls (2) and (2), Pipe (5
) forms a flow path for the heated fluid to flow through the inside of the tube.

なお、壁面構成体(7)、(7)は全部のセラミックス
管(5)が壁面(2)、(2)間に取付けらIしたとき
にその外面が互いに覆着して枠体(1)の内部の両側に
気密な壁体を構成するものであり、これらの壁体に囲ま
れた内側を高温の排ガス等が流れる伝熱流体流路とする
ことにより排ガスのリークを防止するとともに圧縮スゲ
リンクQ41の断熱壁として作用して圧縮119270
勺の弾性低下を防止している。さらにまた、図示のよう
にセラミックス管(5)及びm面構成体(7)、(7j
の内部には放射状の隔壁を備えた七うミックス製の分流
体0119が嵌入されていてセラミックス管(5)の内
部を流れる空気流を細かく分流させることによりセラミ
ックス管内の境膜伝熱係数を増大させている。なお、前
記実施例では流入側の支持?? (8)と壁rhj(2
)との間にのみ圧縮スゲリングo4を配設したが、排出
側の支持管(9)と壁面(2)との間にも14:、縮ス
プリングを配設してもよく、また、回申tmは外?!′
。a)と内管σb)との接合面に設けられたグランドパ
ツキンである。さらに、本実施例の壁面構成体(7)、
(7)は全てのセラミックス管(5)を枠体(1)の対
向する壁面(2)、(2)間に並設したとき、壁面構成
体(7)、(7)の外表面か互いに密着して枠体く1〕
の内部1に気密な壁面を構成することにより枠体(1)
の内部を流れる排ガスのリークを防止するようにしたも
のであるが、これを省略してセラミックス管(5)の両
端を直接に支持W(8)、(9)で支承させることも可
能であり、また、支持管(8)及び圧縮スプリングθψ
の形態についても種々の液形が可能であって、例えば@
3図に示されるように内管(Jc)を壁面(2)に溶接
し、外管σのにより壁面構成体(7)を押圧させたり、
第1A7に示されるように、支持管(8)ヲ単−管とな
しその後端を壁面(2)の透孔四に貫通させたうえその
外部に圧縮スプリングQ41を取付けてもよい。この場
合、圧縮ヌグリングa膏は支持管(8ンのn11部に突
設されたフランジ(8)と壁面(2)の透孔の周囲に溶
接された受台Q樟との間に設けられ、支持管(8)を介
して壁面構成体(7)をセラミックス管(5)に向って
押圧する。−七して、透孔(IIの内径を支持’ii!
−(8)の外径よりも大としてその1t(1に02〜/
問程度の幅の細隙aυを形成し、この細1IIoT)を
介して供給口(3)がら分流される被加熱流体により圧
縮スプリングQ41を冷却各種の工業炉からrJt出さ
れた高温の排ガスを流すとともに対向する壁面(2)、
(2fの透孔□0%aL/に連通される支持管(3)、
(9)を両端に備えた多数のセラミックス管(5)に供
給1月3)から支持管(8)を介して常温の被加熱流体
を送り込めば、これらのセラミックス管(5)の管壁を
介d〒v屹゛スl加熱流体との間に熱交換が行なわれる
ことは従来のこの種熱交換器と同様であるが、本発明で
は伝熱管として耐熱性及び耐腐食性tこ優れたセラミッ
クス管(5)を使用しているために1ooo°Cを越え
る高温の排ガスとの間で熱交換を行なわせることができ
、1OOO″C以下の排ガスにしか用いることのできな
かった従来の熱交換器に比較してはるかに優れた温度効
率を得ることができるうえに金属製の伝熱管を使用した
熱交換器によっては行なうこともできなかった腐食性の
ガスからの熱回収をも行なうことができる。また、この
ような高温の排ガスが枠体(1)内に導入されると各セ
ラミックス管(5)は著しく熱膨張し、しかも、その膨
張景ii被加熱流体の流入側において大きく、流出側に
おいて小さい不均一なものとなるが、本発明において各
セラミックス管(5)が少なくとも片側の支持管(8)
と壁面(2)との間に設けた圧縮スプリング0勺により
軸線方向へ伜かに摺動できるので、各セラミックス! 
(5)の不均一な熱膨張は各圧縮スラブりングU〜によ
り個別に吸収されて熱応力によるセラミックス管(6)
の破損を防止でき、しかも、これらの圧縮スプリング0
勺による押圧力がセラミックス管(5)と壁面構成体(
7)、ノ (7)との間あるいは壁面構成体(7)、(7)と支持
管(8)、(9)との間に作用してこれらを互いに密着
させて加熱された流体が外部へリークすることを防止で
きる。しかも、圧縮スプリング0勺は供給口(3)から
供給される被加熱流体の流れに曝されて常時冷却されて
いるため、長期間にわたり使用しても高温の排ガスtこ
よる弾性劣化がなく壁面(2)、(2)間tこセラミッ
クス管(5)が適確に密接保持されることとなり、効率
的な熱交換を続lJることかできる。
In addition, when all the ceramic tubes (5) are installed between the wall surfaces (2), (2), the outer surfaces of the wall structures (7), (7) cover each other and form the frame (1). This system has airtight walls on both sides of the inside of the pipe, and the inside surrounded by these walls is used as a heat transfer fluid flow path through which high-temperature exhaust gas flows, thereby preventing exhaust gas leakage and compressed sedge links. Compression 119270 acting as a heat insulating wall of Q41
This prevents the elasticity of the straw from decreasing. Furthermore, as shown in the figure, a ceramic tube (5) and m-plane structures (7), (7j
A dividing fluid 0119 made by Nanau Mix with radial partition walls is fitted inside the ceramic tube (5), which finely divides the air flow flowing inside the ceramic tube (5) to increase the film heat transfer coefficient inside the ceramic tube. I'm letting you do it. In addition, in the above embodiment, support on the inflow side? ? (8) and wall rhj (2
), but a compression spring may also be provided between the support pipe (9) on the discharge side and the wall surface (2). Is tm outside? ! ′
. This is a gland packing provided on the joint surface between a) and the inner pipe σb). Furthermore, the wall structure (7) of this embodiment,
(7) When all the ceramic tubes (5) are arranged in parallel between the opposing walls (2), (2) of the frame (1), the outer surfaces of the wall structures (7), (7) Closely fit the frame 1]
By configuring an airtight wall surface inside the frame (1)
Although this is designed to prevent leakage of exhaust gas flowing inside the ceramic tube, it is also possible to omit this and directly support both ends of the ceramic tube (5) with the supports W (8) and (9). , Also, the support tube (8) and the compression spring θψ
Various liquid forms are also possible, for example @
As shown in Figure 3, the inner tube (Jc) is welded to the wall surface (2), and the outer tube σ presses the wall structure (7),
As shown in 1A7, the support tube (8) may be a single tube, the rear end of which is passed through the through hole 4 of the wall surface (2), and the compression spring Q41 may be attached to the outside thereof. In this case, the compressed nugling a plaster is installed between the flange (8) protruding from the n11 part of the support tube (8) and the pedestal Q camphor welded around the through hole in the wall surface (2), Press the wall structure (7) towards the ceramic tube (5) via the support tube (8).
- 1t (1 to 02~/
The compressed spring Q41 is cooled by the heated fluid that is separated from the supply port (3) through this narrow gap aυ with a width of approximately A wall surface facing the flow (2),
(Support pipe (3) connected to the 2f through hole □0%aL/,
If a fluid to be heated at room temperature is sent from the supply pipe 3) to a large number of ceramic tubes (5) equipped with (9) at both ends through the support tube (8), the tube walls of these ceramic tubes (5) The fact that heat exchange is performed between the heating fluid and the dvd tube is the same as in conventional heat exchangers of this type, but in the present invention, the heat exchanger tube has excellent heat resistance and corrosion resistance. Because the ceramic tube (5) is used, it is possible to exchange heat with the exhaust gas at a temperature of over 100°C, compared to the conventional method that could only be used for exhaust gas at a temperature of 100"C or less. In addition to providing much better thermal efficiency than heat exchangers, it also recovers heat from corrosive gases, which is not possible with heat exchangers using metal heat transfer tubes. Furthermore, when such high-temperature exhaust gas is introduced into the frame (1), each ceramic tube (5) undergoes significant thermal expansion, and furthermore, the expansion pattern ii. However, in the present invention, each ceramic tube (5) has at least one support tube (8).
The compression spring installed between the wall surface (2) and the wall surface (2) allows it to slide upward in the axial direction, so each ceramic!
The non-uniform thermal expansion of (5) is absorbed individually by each compressed slab ring U~, causing thermal stress in the ceramic tube (6).
damage can be prevented, and these compression springs have 0
The pressing force from the shovel is applied to the ceramic tube (5) and the wall structure (
7), (7) or between the wall structure (7), (7) and the support tubes (8), (9) to bring them into close contact with each other, so that the heated fluid flows outside. It can prevent leakage. Moreover, since the compression springs are constantly cooled by being exposed to the flow of the heated fluid supplied from the supply port (3), there is no elastic deterioration due to high temperature exhaust gas even after long-term use, and the wall surface Between (2) and (2), the ceramic tube (5) is properly and closely held, and efficient heat exchange can continue.

(発明の効果) 本発明は以上の説明からも明らかなように、金#4製の
伝熱管を使用した従来のシェルアンドチューブ型の熱交
換器によつ−Cは熱回収を行なうことができなかった1
ooo″C以上の高温の排ガスや腐食性のガスからも効
率良く熱回収を行なうことができ、しかも、各セラミッ
クス管に生ずる不均一な熱膨張や収縮を圧縮スプリング
により個別に吸収させることによりセラミックス管の熱
応力による破損を防止することができるうえに圧縮スフ
(Effects of the Invention) As is clear from the above description, the present invention is capable of recovering heat from the conventional shell-and-tube heat exchanger using heat transfer tubes made of #4 gold. I couldn't do it 1
It is possible to efficiently recover heat from exhaust gases and corrosive gases that are hotter than ooo''C, and in addition, by individually absorbing the uneven thermal expansion and contraction that occurs in each ceramic tube with a compression spring, It can prevent damage to pipes due to thermal stress and can also be compressed.

リングtこよる押圧力を利用してセラミックス管の両端
部を壁面間に密接保持させたもので、この圧縮スプリン
グが供給口から供給される被加熱流体により熱交換が行
われる間継続して冷却さiしることとなるので圧縮スプ
リングを長期間にわたり使用できるうえに特別な冷却機
構を何設する必要がないのでコストが安くなる等種々の
利点があり、在来のこの稲熱交換器の間融点を解消した
ものとして業界の発展に寄与するところ極めて大なもの
である。
Both ends of the ceramic tube are held closely between the walls using the pressing force of the ring t, and this compression spring continues to cool while heat exchange is performed by the heated fluid supplied from the supply port. This has various advantages such as the compression spring can be used for a long period of time and there is no need to install any special cooling mechanism, which reduces the cost. It is extremely useful in contributing to the development of the industry as a product that has solved the problem of melting point.

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

第1図は本発明の実施例を示す一部切欠正面図、第2図
は要部の一部切欠正面図、第3図、第7図は本発明の他
の実施例を示す要部の一部切欠11:面図である。 (02枠体、(2)、(2):壁面、(3):供給口、
(4):流出口、(5):セラミックス管、(8):支
持管、0勾:圧縮スプリング、α7):細隙。
Fig. 1 is a partially cutaway front view showing an embodiment of the present invention, Fig. 2 is a partially cutaway front view of the main part, and Figs. 3 and 7 are main parts showing other embodiments of the invention. Partial cutout 11: This is a side view. (02 frame body, (2), (2): wall surface, (3): supply port,
(4): Outlet, (5): Ceramic tube, (8): Support tube, 0 slope: Compression spring, α7): Slit.

Claims (1)

【特許請求の範囲】 /、内部を伝熱流体流路に形成しプこ枠体(1)の対向
する壁面(2)、(2)間に被加熱流体の供給[1(3
)と流出口(4)に連通される多数のセラミックス管(
5)を前記供給口(3)から供給される被加熱流体によ
り冷却される圧縮スプリングa41をもって該セラミッ
クス管(5)の軸線方向への膨張、収縮が吸11にでき
るように並行に架設置7たことを特徴とする熱交換器。 2、圧縮スプリングQ4)を被加熱流体の供紹Lit 
(3)と連通するように壁面(2)tこ取付りられた支
持’i’i’ (8)の内部に設けて該供給口(3)か
ら支持管(8)を通じてセラミックス管(5)に流れる
被加熱流体により冷却されるものとした特許請求の範囲
第7項記載の熱交換器。 3、圧縮スラブりングQ4を被加熱流体の供給口(3)
と連通ずるように壁面(2)に取イ(1けられた支持管
(8)に間装して該供給口(3)から細Rt、 07)
を通じて分流さ1−り&−1.J+言−シ赫さIeL4
−+フート湯11^、1llaJlブーl〆7)1−■
、−シ、+b+=−シ1請求の範囲@1項記載の熱交換
器。
[Scope of Claims] /, The interior is formed into a heat transfer fluid flow path, and the heated fluid is supplied between the opposing wall surfaces (2), (2) of the compressor frame (1) [1 (3)
) and a large number of ceramic tubes (
5) is mounted on a rack 7 in parallel so that the ceramic tube (5) can expand and contract in the axial direction with a compression spring a41 cooled by the heated fluid supplied from the supply port (3). A heat exchanger characterized by: 2. Introducing the compression spring Q4) to the fluid to be heated.
(3) is provided inside the support 'i'i' (8) attached to the wall surface (2) so as to communicate with the ceramic pipe (5) through the support pipe (8) from the supply port (3). 8. The heat exchanger according to claim 7, wherein the heat exchanger is cooled by a fluid to be heated flowing through the heat exchanger. 3. Connect the compressed slab ring Q4 to the heated fluid supply port (3)
It is installed on the wall surface (2) so as to be in communication with the supply port (3) and connected to the support pipe (8), which is connected to the wall surface (2) (07).
The flow is diverted through 1-ri &-1. J+Words IeL4
-+Footyu 11^, 1lla Jl Boo l〆7) 1-■
, -C, +b+=-C1 The heat exchanger according to claim 1.
JP17196183A 1983-09-16 1983-09-16 Heat exchanger Granted JPS6064187A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17196183A JPS6064187A (en) 1983-09-16 1983-09-16 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17196183A JPS6064187A (en) 1983-09-16 1983-09-16 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS6064187A true JPS6064187A (en) 1985-04-12
JPH0319474B2 JPH0319474B2 (en) 1991-03-15

Family

ID=15932971

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17196183A Granted JPS6064187A (en) 1983-09-16 1983-09-16 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS6064187A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0953894A (en) * 1995-08-14 1997-02-25 Sakushiyon Gas Kikan Seisakusho:Kk Double tube plate fixed heat exchanger and method for assembling the same
CN112594709A (en) * 2020-10-14 2021-04-02 安徽蓝风环保科技有限公司 Heat accumulation incineration pyrolysis waste gas treatment and utilization device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5546911U (en) * 1978-09-20 1980-03-27

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5546911U (en) * 1978-09-20 1980-03-27

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0953894A (en) * 1995-08-14 1997-02-25 Sakushiyon Gas Kikan Seisakusho:Kk Double tube plate fixed heat exchanger and method for assembling the same
CN112594709A (en) * 2020-10-14 2021-04-02 安徽蓝风环保科技有限公司 Heat accumulation incineration pyrolysis waste gas treatment and utilization device
CN112594709B (en) * 2020-10-14 2023-12-01 安徽蓝风环保科技有限公司 Heat accumulation burns schizolysis waste gas treatment and utilization device

Also Published As

Publication number Publication date
JPH0319474B2 (en) 1991-03-15

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