JPS6339572Y2 - - Google Patents

Info

Publication number
JPS6339572Y2
JPS6339572Y2 JP1983119861U JP11986183U JPS6339572Y2 JP S6339572 Y2 JPS6339572 Y2 JP S6339572Y2 JP 1983119861 U JP1983119861 U JP 1983119861U JP 11986183 U JP11986183 U JP 11986183U JP S6339572 Y2 JPS6339572 Y2 JP S6339572Y2
Authority
JP
Japan
Prior art keywords
outer cylinder
baffle plate
donut
shaped baffle
chamber
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.)
Expired
Application number
JP1983119861U
Other languages
Japanese (ja)
Other versions
JPS6027267U (en
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 filed Critical
Priority to JP11986183U priority Critical patent/JPS6027267U/en
Publication of JPS6027267U publication Critical patent/JPS6027267U/en
Application granted granted Critical
Publication of JPS6339572Y2 publication Critical patent/JPS6339572Y2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Details Of Heat-Exchange And Heat-Transfer (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【考案の詳細な説明】 本考案はレキユペレータに係り、さらに詳しく
は熱伝導効率を上げることにより小型化すること
ができるように構成したレキユペレータに関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a recuperator, and more particularly to a requiperator configured to be miniaturized by increasing heat conduction efficiency.

従来のレキユペレータの構造を第1図に示す。 The structure of a conventional recuperator is shown in FIG.

第1図に示す例は多管式のレキユペレータで、
図において符号1は外筒を示し、その外側は耐熱
材1aによつて覆われている。この外筒1は直円
筒状に形成されており、上部より加熱ガス室5、
熱交換室8、ガス排出室7とに分けられている。
The example shown in Figure 1 is a multi-tube recuperator.
In the figure, reference numeral 1 indicates an outer cylinder, the outside of which is covered with a heat-resistant material 1a. This outer cylinder 1 is formed into a right cylindrical shape, and from the top, a heating gas chamber 5,
It is divided into a heat exchange chamber 8 and a gas discharge chamber 7.

加熱ガス室5と熱交換室8との間には上部の管
板13が、また、熱交換室8とガス排出室7との
間にも下部の管板14がそれぞれ設けられてい
る。
An upper tube sheet 13 is provided between the heating gas chamber 5 and the heat exchange chamber 8, and a lower tube sheet 14 is provided between the heat exchange chamber 8 and the gas discharge chamber 7, respectively.

加熱ガス室8の一側には加熱ガス導管6が開口
しており、ここから加熱ガスが導入される。
A heating gas conduit 6 is opened on one side of the heating gas chamber 8, and heating gas is introduced from here.

熱交換室8の内部には外筒1と平行に多数の伝
熱管2a及び冷却管2が配置されている。
Inside the heat exchange chamber 8, a large number of heat transfer tubes 2a and cooling tubes 2 are arranged parallel to the outer cylinder 1.

少数の冷却管2は、上下の管板13と14との
間に、上下端を閉鎖して取付けられており、上下
の管板13,14に近くスリツト15,16が開
口している。
A small number of cooling pipes 2 are installed between upper and lower tube sheets 13 and 14 with their upper and lower ends closed, and slits 15 and 16 are open near the upper and lower tube sheets 13 and 14.

また、多数の伝熱管2aは上下の管板13,1
4を貫通し、加熱ガス室5とガス排出室7との間
に開口している。
In addition, a large number of heat exchanger tubes 2a are arranged in upper and lower tube sheets 13, 1.
4 and opens between the heating gas chamber 5 and the gas discharge chamber 7.

そして、これらの伝熱管2a及び冷却管2を利
用して大直径のドーナツ型の邪魔板3と小直径の
邪魔板4とが交互に、かつ伝熱管2a及び冷却管
2と直交した状態で所定間隔離して配置されてい
る。ドーナツ型の邪魔板3と小直径の邪魔板4と
は互い違いに伝熱管2a及び冷却管2を取付けた
状態で、外筒1の内部に収容されている。
Using these heat transfer tubes 2a and cooling tubes 2, large-diameter donut-shaped baffle plates 3 and small-diameter baffle plates 4 are arranged alternately and perpendicularly to the heat transfer tubes 2a and cooling tubes 2 at predetermined positions. are placed in isolation. The donut-shaped baffle plate 3 and the small-diameter baffle plate 4 are housed inside the outer cylinder 1 with heat transfer tubes 2a and cooling tubes 2 attached alternately.

符号9は被加熱ガスの供給管、また符号12は
被加熱ガスの排出管である。
Reference numeral 9 is a supply pipe for heated gas, and reference numeral 12 is a discharge pipe for heated gas.

供給管9から導かれた被加熱ガスは、外筒1の
円周方向に沿つて所定間隔であけられた開口部1
0内に導かれ、外筒1内に入る。そして、ドーナ
ツ型の邪魔板3の中央部の開口部と、小直径の邪
魔板4の外側との間をジグザグに通過して伝熱管
2aに導かれる高温の加熱ガスとの間で熱交換が
行なわれる。また、被加熱ガスの一部は、冷却管
2の下部のスリツト16より冷却管2内にも導か
れ、上昇して上部の管板13を冷却する。そし
て、熱交換を終了した被加熱ガスは外筒1の加熱
ガス室5の端部近傍において円周方向に沿つてあ
けられた開口部11から排出管12へと導かれ
る。
The gas to be heated led from the supply pipe 9 is passed through the openings 1 formed at predetermined intervals along the circumferential direction of the outer cylinder 1.
0 and enters the outer cylinder 1. Heat exchange occurs between the opening in the center of the donut-shaped baffle plate 3 and the high-temperature heated gas that passes in a zigzag pattern between the outside of the small-diameter baffle plate 4 and is guided to the heat transfer tube 2a. It is done. A part of the heated gas is also guided into the cooling pipe 2 through the slit 16 at the lower part of the cooling pipe 2, rises, and cools the upper tube plate 13. The heated gas that has completed the heat exchange is guided to the discharge pipe 12 through an opening 11 formed along the circumferential direction near the end of the heated gas chamber 5 of the outer cylinder 1.

また、熱交換を終了した加熱ガスはガス排出室
7に入り、さらに下部に設けたガス排出口17よ
り外筒1外に排出される。
Further, the heated gas that has undergone heat exchange enters the gas discharge chamber 7 and is further discharged to the outside of the outer cylinder 1 through the gas discharge port 17 provided at the lower part.

ところで以上のような構造を採用すると、外筒
1およびドーナツ型の邪魔板3の製作誤差および
外筒1の円周方向の溶接による縮みを見込んで製
作しなければならず、外筒の内径とドーナツ型の
邪魔板3の外径との間のすきまは5〜10mm程度と
する必要がある。
By the way, if the above structure is adopted, manufacturing errors in the outer cylinder 1 and the donut-shaped baffle plate 3 and shrinkage due to welding in the circumferential direction of the outer cylinder 1 must be taken into consideration, and the inner diameter of the outer cylinder and The gap between the outer diameter of the donut-shaped baffle plate 3 needs to be about 5 to 10 mm.

このようにすきまが10mm程度になると、ドーナ
ツ型の邪魔板3の穴の面積に対しすきまの面積が
30%〜50%程度となつてしまう。この傾向は小さ
なサイズのもの程大きくなる。
When the gap is about 10mm like this, the area of the gap is smaller than the area of the hole in the donut-shaped baffle plate 3.
It will be around 30% to 50%. This tendency becomes larger as the size becomes smaller.

このようにすきま面積が大きくなると被加熱ガ
スは邪魔板間をジグザグに通過せず、外筒とドー
ナツ型邪魔板との間のすきまを直進してしまう。
このため伝熱管2aと接触して通過する被加熱ガ
ス量が減少するため、被加熱ガスの出口温度が設
定値以上にオーバヒートされることになり、部材
の耐熱対策を講じなければならなくなる。
When the gap area becomes large in this way, the heated gas does not pass between the baffle plates in a zigzag pattern, but instead travels straight through the gap between the outer cylinder and the donut-shaped baffle plate.
As a result, the amount of gas to be heated that comes into contact with and passes through the heat transfer tube 2a is reduced, so that the outlet temperature of the gas to be heated is overheated to a set value or higher, and it is necessary to take measures for heat resistance of the member.

また、伝熱効果が悪いため、レキユペレータの
サイズを大きくしなければならないという欠点が
ある。
Another disadvantage is that the size of the recuperator must be increased due to the poor heat transfer effect.

本考案は、以上のような従来の欠点を除去する
ためになされたもので、外筒と大直径のドーナツ
型の邪魔板との間のすきまを著しく小さくするこ
とにより製作誤差に大きな自由度をもたせ、全体
として小型化することができるように構成したレ
キユペレータを提供することを目的としている。
The present invention was developed in order to eliminate the above-mentioned drawbacks of the conventional technology, and by significantly reducing the gap between the outer cylinder and the large-diameter donut-shaped baffle plate, it provides a greater degree of freedom for manufacturing errors. It is an object of the present invention to provide a recuperator configured so that it can be made more compact and smaller as a whole.

以下、図面に示す実施例に基いて本考案を詳細
に説明する。
Hereinafter, the present invention will be explained in detail based on embodiments shown in the drawings.

第2図および第3図は本考案の一実施例を説明
するものであり、本図中、第1図と同一部分には
同一符号を付し、その説明は省略する。
FIGS. 2 and 3 illustrate one embodiment of the present invention. In the figures, the same parts as in FIG. 1 are designated by the same reference numerals, and their explanation will be omitted.

本実施例にあつては外筒1を所定のテーパをも
つて形成してある。すなわち加熱ガス室5側が小
直径でガス排出室7側が大直径となるように形成
されている。
In this embodiment, the outer cylinder 1 is formed with a predetermined taper. That is, it is formed so that the heating gas chamber 5 side has a small diameter and the gas discharge chamber 7 side has a large diameter.

また、ドーナツ型の邪魔板3の外径も外筒1の
テーパに合わせてガス排出室7側に至るに従い、
次第に直径が大きくなるように形成されている。
Also, the outer diameter of the donut-shaped baffle plate 3 is adjusted to the taper of the outer cylinder 1 as it reaches the gas discharge chamber 7 side.
It is formed so that the diameter gradually increases.

このような構造を採用すると、伝熱管2ととも
に邪魔板を外筒1内に組込むとき、ガス排出室7
側の大直径側の端部から挿入し、ドーナツ型の邪
魔板3と外筒1との間のすきまが最小となるよう
に組立てることができる。
If such a structure is adopted, when the baffle plate is assembled into the outer cylinder 1 together with the heat exchanger tube 2, the gas discharge chamber 7
It can be inserted from the end on the large diameter side of the side, and assembled so that the gap between the donut-shaped baffle plate 3 and the outer cylinder 1 is minimized.

また、このように外筒1をテーパ状にし、ドー
ナツ型の邪魔板の外形もこれに応じて変化させる
構造を採用しているので、外筒1の製作誤差とド
ーナツ型の邪魔板3の製作誤差とがあつても、伝
熱管2aと邪魔板3,4の組立体を軸線方向に沿
つて相対的に位置ずれさせることにより吸収する
ことができ、製作に大きな自由度が生じる。
In addition, since the outer cylinder 1 is tapered and the outer shape of the donut-shaped baffle plate is changed accordingly, manufacturing errors in the outer cylinder 1 and manufacturing errors in the donut-shaped baffle plate 3 are avoided. Even if there is an error, it can be absorbed by relatively shifting the assembly of the heat exchanger tube 2a and the baffle plates 3, 4 along the axial direction, resulting in a large degree of freedom in manufacturing.

このようにして外筒1とドーナツ型の邪魔板3
との間のすきまを著しく小さくすることができ、
従来のレキユペレータと比較し、その大きさを20
〜30%縮小することが可能となり、大幅なコスト
ダウンが実現できる。
In this way, the outer cylinder 1 and the donut-shaped baffle plate 3 are
The gap between the
Compared to the conventional requiperator, its size is 20
It is possible to reduce the size by ~30%, resulting in significant cost reductions.

ところで、ここで外筒1のテーパについて付言
すると以下のとおりである。
By the way, the following is an additional comment regarding the taper of the outer cylinder 1.

すなわち、第3図に示すように外筒1の溶接縮
小代をA、大直径の邪魔板のピツチをBとする
と、ドーナツ型の邪魔板3と邪魔板4間のピツチ
をB/2としてテーパを決定すればよい。
That is, as shown in FIG. 3, if the welding reduction allowance of the outer cylinder 1 is A, and the pitch of the large-diameter baffle plate is B, then the pitch between the donut-shaped baffle plate 3 and the baffle plate 4 is B/2, and the taper is All you have to do is decide.

以上の説明から明らかなように本考案によれ
ば、レキユペレータの外筒をテーパ状とするとと
もに、内部に取付けられるドーナツ型の邪魔板と
して形成された邪魔板を外筒のテーパに合わせて
一方から他方にかけて大直径となるようにした構
造を採用しているので、外筒と、ドーナツ型の邪
魔板との間のすきまを著しく小さくすることがで
き、伝熱効率を大幅に改善できるとともに製作誤
差があつても、これを吸収することができ、組立
てが容易となる。
As is clear from the above description, according to the present invention, the outer cylinder of the requiperator is tapered, and the baffle plate formed as a donut-shaped baffle plate attached to the inside is aligned with the taper of the outer cylinder. Since the structure has a large diameter towards the other end, it is possible to significantly reduce the gap between the outer cylinder and the donut-shaped baffle plate, greatly improving heat transfer efficiency and reducing manufacturing errors. Even if there is such a problem, it can be absorbed and assembly becomes easy.

また、外筒と大直径のドーナツ型の邪魔板との
間のすきまを小さくすることができるため、全体
として小型化することができ、大幅なコストダウ
ンを実現することができる。
Furthermore, since the gap between the outer cylinder and the large-diameter donut-shaped baffle plate can be reduced, the overall size can be reduced, and significant cost reductions can be achieved.

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

第1図は従来構造を説明する縦断側面図、第2
図は本考案の一実施例を説明する縦断側面図、第
3図は第2図の一部拡大図である。 1は外筒、1aは耐熱材、2は冷却管、2aは
伝熱管、3はドーナツ型の邪魔板、4は小直径の
邪魔板、5は加熱ガス室、6は加熱ガス導管、7
はガス排出室、8は熱交換室、9は被加熱ガスの
供給管、10は外筒下部の開口部、11は外筒上
部の開口部、12は被加熱ガスの排出管、13,
14は上下の管板、15は冷却管上部のスリツ
ト、16は冷却管下部のスリツト、17はガス排
出口である。
Figure 1 is a vertical cross-sectional side view explaining the conventional structure, Figure 2
The figure is a vertical side view illustrating an embodiment of the present invention, and FIG. 3 is a partially enlarged view of FIG. 2. 1 is an outer cylinder, 1a is a heat-resistant material, 2 is a cooling pipe, 2a is a heat exchanger tube, 3 is a donut-shaped baffle plate, 4 is a small diameter baffle plate, 5 is a heating gas chamber, 6 is a heating gas conduit, 7
1 is a gas discharge chamber, 8 is a heat exchange chamber, 9 is a supply pipe for heated gas, 10 is an opening at the bottom of the outer cylinder, 11 is an opening at the top of the outer cylinder, 12 is a discharge pipe for heated gas, 13,
14 is an upper and lower tube plate, 15 is a slit in the upper part of the cooling pipe, 16 is a slit in the lower part of the cooling pipe, and 17 is a gas discharge port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 加熱ガス室が小直径、ガス排出室が大直径とな
るようにテーパをつけて形成した外筒の内部に、
外筒のテーパに合わせて加熱ガス室側よりガス排
出側に至るに従い次第に直径が大きくなるように
形成したドーナツ型の邪魔板を取付けたことを特
徴とするレキユペレータ。
Inside the outer cylinder is tapered so that the heating gas chamber has a small diameter and the gas discharge chamber has a large diameter.
A recuperator characterized in that a donut-shaped baffle plate is attached whose diameter gradually increases from the heating gas chamber side to the gas discharge side in accordance with the taper of the outer cylinder.
JP11986183U 1983-08-02 1983-08-02 requiturer Granted JPS6027267U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11986183U JPS6027267U (en) 1983-08-02 1983-08-02 requiturer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11986183U JPS6027267U (en) 1983-08-02 1983-08-02 requiturer

Publications (2)

Publication Number Publication Date
JPS6027267U JPS6027267U (en) 1985-02-23
JPS6339572Y2 true JPS6339572Y2 (en) 1988-10-18

Family

ID=30274916

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11986183U Granted JPS6027267U (en) 1983-08-02 1983-08-02 requiturer

Country Status (1)

Country Link
JP (1) JPS6027267U (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5866278U (en) * 1981-10-17 1983-05-06 ダイキン工業株式会社 Heat exchanger

Also Published As

Publication number Publication date
JPS6027267U (en) 1985-02-23

Similar Documents

Publication Publication Date Title
WO2014044208A1 (en) Forced spiral finned coil condensation heat-supplying heat exchanger
WO2014044205A1 (en) Forced spiral finned coil and finned serpentine coil condensation heat-supplying heat exchanger
JP7357208B2 (en) Heat exchanger and water heating equipment equipped with the same
JPS58150794A (en) Concentric pipe type recuperative heat exchanger
JPS6339572Y2 (en)
US4694896A (en) Heat exchanger
CN109114815A (en) A kind of heat exchanger
CN208983626U (en) A kind of heat exchanger
JPH0665759U (en) Bayonet type heat exchanger
JP2000146464A (en) Heat exchanger
JP4247462B2 (en) Heat exchanger for exhaust heat recovery
JPH0630603U (en) Multi-tube once-through boiler
JP2694894B2 (en) Heat exchanger
CN216204350U (en) Heat exchange fin, heat exchanger and gas water heating equipment
JPS6222994A (en) Multi-tubular heat exchanger
JPH0684167U (en) Heat exchanger
CN217715033U (en) Heat exchange device with crossed smoke and air ducts
JPH09303875A (en) Hot water boiler for heating
CN214039662U (en) Full-premixing condensing heat exchanger
JP3041263U (en) Simplified heat exchanger core
JPH0220626Y2 (en)
JP2522856Y2 (en) Heat exchanger
JP2714904B2 (en) Spiral heat exchanger
JPH029272Y2 (en)
JPH0318864Y2 (en)