JPS6262243B2 - - Google Patents
Info
- Publication number
- JPS6262243B2 JPS6262243B2 JP1858877A JP1858877A JPS6262243B2 JP S6262243 B2 JPS6262243 B2 JP S6262243B2 JP 1858877 A JP1858877 A JP 1858877A JP 1858877 A JP1858877 A JP 1858877A JP S6262243 B2 JPS6262243 B2 JP S6262243B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- heat exchanger
- heat exchange
- sleeve
- tubes
- 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
Links
- 229910052751 metal Inorganic materials 0.000 claims description 12
- 239000002184 metal Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000005219 brazing Methods 0.000 claims description 9
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 6
- 229910045601 alloy Inorganic materials 0.000 claims description 5
- 239000000956 alloy Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 230000003014 reinforcing effect Effects 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 230000000295 complement effect Effects 0.000 claims description 3
- 229910001338 liquidmetal Inorganic materials 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims 1
- 239000011261 inert gas Substances 0.000 claims 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 13
- 229910052708 sodium Inorganic materials 0.000 description 13
- 239000011734 sodium Substances 0.000 description 13
- 239000000463 material Substances 0.000 description 8
- 230000004927 fusion Effects 0.000 description 7
- 230000013011 mating Effects 0.000 description 7
- 238000010276 construction Methods 0.000 description 6
- 230000001413 cellular effect Effects 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000002955 isolation Methods 0.000 description 4
- 229910000599 Cr alloy Inorganic materials 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000000788 chromium alloy Substances 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009760 electrical discharge machining Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- -1 sodium Chemical class 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/163—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
- F28D7/1669—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing the conduit assemblies having an annular shape; the conduits being assembled around a central distribution tube
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
本発明は、胴型熱交換器、主として、溶融金属
と水との間で熱交換を行うための熱交換器及びそ
の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a shell-type heat exchanger, primarily a heat exchanger for exchanging heat between molten metal and water, and a method for manufacturing the same.
例えばナトリウムなどの溶融金属は主としてそ
の熱容量が大きいことにより、高速増殖炉の冷却
媒体として原子炉技術に使用されている。溶融金
属は作動温度が高く且つ浸食性を有しているの
で、加熱器や再熱器に使用する熱交換器はオース
テナイト鋼で作るが、それにも拘らずこれらのユ
ニツトには可成りの障害が発見されている。製作
時、最高度に厳重な品質管理を行うにも拘らず、
管対管板接手が破損した。 Molten metals, such as sodium, are used in nuclear reactor technology as cooling media in fast breeder reactors, primarily due to their high heat capacity. Due to the high operating temperatures and corrosive nature of molten metals, heat exchangers used in heaters and reheaters are made of austenitic steel, but these units nevertheless present considerable damage. has been discovered. Despite the strictest quality control during production,
The tube-to-tube plate joint was damaged.
この発明の目的は、溶融金属と水の熱交換に用
いてしかもナトリウムと水の反応を惹起すること
になるような破損の傾向が少い改良された胴型熱
交換器を提供することにある。 SUMMARY OF THE INVENTION It is an object of the present invention to provide an improved shell heat exchanger for use in heat exchange between molten metal and water, which is less prone to failure which could lead to reactions between sodium and water. .
本発明によれば、溶融金属を使用する胴型熱交
換器に於いて、各熱交換管は、管と管板との間に
すきまをもたせて管板の個々の開口を通つて延
び、管は、管板面から直立し管外壁面にその自由
端を封着したスリーブによつて管板に封着され、
管とスリーブとは、封着を行うよう介在させた結
合金属によつて結合してあり、しかもこの結合金
属は、融接による接合の作製に必要とされるよう
な高温の処理を接合の作製に全く必要としない種
類のものである。好ましい構造では、スリーブは
管にろう付けしてありまた管板には融接してあ
り、熱交換管は胴内では継目のない連続した長さ
の管となるように作られている。 According to the present invention, in a shell heat exchanger using molten metal, each heat exchange tube extends through a respective opening in the tube sheet with a gap between the tube and the tube sheet; is sealed to the tube sheet by a sleeve that stands upright from the tube sheet surface and has its free end sealed to the tube outer wall surface,
The tube and sleeve are joined by an intervening bonding metal that provides a seal, and the bonding metal does not require high-temperature processing such as that required to create a fusion welded joint. This is the type of thing that is not needed at all. In a preferred construction, the sleeve is brazed to the tube and fusion welded to the tubesheet, and the heat exchange tube is constructed as a continuous length of tube within the shell.
管にろう付けしたスリーブを用いて管を管板に
適合させ且つ胴内の管を継目のない連続した長さ
の管から作ることによつて、この熱交換器のナト
リウムと水の障壁には融接は使用されていない。
かくして、別の解釈によれば、本発明は、胴側に
溶融金属を使用し、すべての管が個々の管板の開
口に対してすきまを伴つて貫通することにより胴
内に入り且つ胴内にある全長に亘つて継目がなく
連続した長さをもち、各管の管板面から直立し管
外壁面との接合をその自由端に有するスリーブに
よつて各開口で封着されてあつて、しかもこの接
合が管壁のしたがつてまた溶融金属と管内の伝熱
媒体との間の障壁との完全な状態の劣化を軽減す
るよう融接による接合の作製に必要とされるよう
な高温の処理を接合の作製に全く必要としない種
類の結合金属を介在させることによつて形成され
ている胴型の熱交換器に関する。 By fitting the tubes to the tubesheet using sleeves brazed to the tubes and by making the tubes in the shell from continuous, seamless lengths of tube, the sodium and water barriers in this heat exchanger are achieved. No fusion welding was used.
Thus, according to another interpretation, the invention uses molten metal on the shell side, and all the tubes enter and exit the shell by passing through the individual tubesheet openings with clearance. having a seamless and continuous length over the entire length of each tube, and being sealed at each opening by a sleeve that stands upright from the tube sheet surface of each tube and has a connection with the outer wall surface of the tube at its free end; , and also at the high temperatures required to create a joint by fusion welding, such that this joint reduces the deterioration of the integrity of the tube wall and thus also the barrier between the molten metal and the heat transfer medium within the tube. The present invention relates to a shell-type heat exchanger formed by interposing a bonding metal of a type that does not require any processing to make the joint.
この構造体はろう付け個所やスリーブと管板間
の融接接合の応力除去が容易であり、従つて管及
び管板の何れも応力腐食による亀裂発生を増進す
るような大きい張力状態に置かれることがないよ
うになつている。 This structure facilitates stress relief at braze points and fusion joints between the sleeve and tubesheet, so that both the tube and tubesheet are placed under high tension, which can increase cracking due to stress corrosion. It seems like it never happens.
本発明による胴型熱交換器に於いては、各管と
補完スリーブは各端で管とスリーブとに夫々ろう
付けした管状の嵌合片を設けて間接的に結合でき
る。この場合、スリーブは組立てを容易にするよ
う十分にすきまを設けて管上に伸長するU字管を
横方向から支持するための手段と、囲い板の内側
室に沿つて延び熱交換器の第1の管板を形成する
延長部の端壁を貫通する各管の長い方の脚と、囲
い板の外側室に沿つて延び熱交換器の第2の管板
を形成する延長部のフランジを貫通する各管の短
い方の脚とを含み、各管の各脚が管と管板との間
にすきまを伴つて個々の開口を通り補足管板を貫
通しており、管が管板面から直立し管の外壁面に
その自由端で封着せるスリーブを通るよう配置す
ることができる。嵌合片はろう付けを行うのに適
当な管及びスリーブの外面と締り嵌めするよう作
製してある。 In the barrel heat exchanger according to the invention, each tube and the complementary sleeve can be indirectly coupled by providing a tubular mating piece at each end that is brazed to the tube and sleeve, respectively. In this case, the sleeve is provided with means for lateral support of the U-tube extending over the tube with sufficient clearance to facilitate assembly, and with means for lateral support of the U-tube extending along the inner chamber of the shroud and with sufficient clearance to facilitate assembly. the longer leg of each tube passing through the end wall of the extension forming one tubesheet and the flange of the extension extending along the outer chamber of the shroud forming the second tubesheet of the heat exchanger; a shorter leg of each tube passing therethrough, each leg of each tube passing through the complementary tubesheet through a respective opening with a gap between the tube and the tubesheet, and the tube passing through the supplementary tubesheet with a gap between the tube and the tubesheet. The tube can be placed through a sleeve which is sealed at its free end to the outer wall of the upright tube. The mating piece is constructed to provide an interference fit with the outer surface of the tube and sleeve suitable for brazing.
本発明は溶融金属用入口及び出口を備え取外し
自在の熱交換管組立体を収容する長い容器を具備
し、熱交換管組立体は、容器の閉鎖体を形成する
フランジ付延長部と、該延長部から不等長の脚を
懸吊させたU字状の熱交換管群と、容器と同軸に
配置されるフランジ付延長部と、該延長部から不
等長の脚を懸吊させたU字状の熱交換管群と、容
器と同軸に配置され且つU字状の管群を包む環状
囲い板と前記延長部から懸吊され且つ前記囲い板
中に内側および外側の環状室を形成する円筒状の
邪魔板と、容器の長手方向軸線に平行に延びるU
字状の管を横方向に支持する装置とから構成さ
れ、各管の長い方の管は熱交換器の第1の管板を
形成する延長部の端壁を貫通するよう囲い板の内
側の室に沿つて延び、各管の短い方の管は、熱交
換器の第2の管板を形成する延長部のフランジを
貫通するよう囲い板の外側の室に沿つて延び、各
管の各脚は、管と管板との間にすき間を伴つて
個々の開口を貫通し、管は管板の面から直立する
スリーブによつて管板に封着され且つスリーブの
自由端によつて管の外壁面に封着され、管とスリ
ーブとは共にろう付けされている胴型熱交換器を
提供することにある。 The present invention comprises an elongated vessel containing a removable heat exchange tube assembly with an inlet and an outlet for molten metal, the heat exchange tube assembly having a flanged extension forming a closure for the vessel; A group of U-shaped heat exchange tubes with legs of unequal length suspended from the U-shaped heat exchange tube group, a flanged extension section disposed coaxially with the container, and a U-shaped heat exchange tube group with legs of unequal length suspended from the extension section. a set of heat exchange tubes in the shape of a shape, an annular shroud arranged coaxially with the vessel and surrounding the U-shaped set of tubes, and suspended from the extension and forming inner and outer annular chambers in the shroud. A cylindrical baffle plate and a U extending parallel to the longitudinal axis of the container.
and a device for laterally supporting the tubes in the shape of a tube, with the longer tube of each tube extending inside the shroud so as to pass through the end wall of the extension forming the first tubesheet of the heat exchanger. the shorter tube of each tube extends along the outer chamber of the shroud so as to pass through the flange of the extension forming the second tube sheet of the heat exchanger; The legs pass through respective openings with gaps between the tubes and the tubesheet, and the tubes are sealed to the tubesheet by sleeves that stand upright from the face of the tubesheet and are secured to the tubes by the free ends of the sleeves. The object of the present invention is to provide a shell-type heat exchanger which is sealed to the outer wall surface of the tube and the sleeve are brazed together.
本発明による多管式熱交換器の構造を添付図面
を参照して説明する。 The structure of the shell-and-tube heat exchanger according to the present invention will be explained with reference to the accompanying drawings.
添付図面に示した胴型熱交換器は、液体金属冷
却型高速増殖炉装置の蒸気発生回路に使用され
る。開示の熱交換器は過熱器に使用することを意
図せるものであるが、この発明による熱交換器で
蒸発器及び再熱器として使用するものも概ね類似
の構造である。図示した熱交換器は下端が閉じ、
フランジ付の上端が開放した概ね円筒形の胴1を
具備している。 The barrel heat exchanger shown in the accompanying drawings is used in a steam generation circuit of a liquid metal cooled fast breeder reactor device. Although the disclosed heat exchanger is intended for use in a superheater, heat exchangers according to the present invention for use as evaporators and reheaters are of generally similar construction. The illustrated heat exchanger is closed at the bottom end;
It has a generally cylindrical body 1 with a flange and an open upper end.
胴は基部のナトリウム入口2、側部の出口3、
ドレン口4及びナトリウムと水の反応が発生した
場合に胴内の圧力を逃がすための圧力解放用接続
部5を備えている。胴の開放端は、上端が閉じた
フランジ付の円筒形延長部6を有し、胴のフラン
ジと延長部のフランジはボルト止めしてあり且つ
周縁部は軽い溶接7で封着してある。熱交換管8
は不等長の脚を有するU字形状をなし、胴内で延
長部6から懸吊してある。長い方の脚8aは延長
部に沿つて延び、内側管板9を形成する端部カバ
ーを貫通し、短い方の脚8bは環状外側管板10
を形成する延長部フランジを貫通している。これ
らの管は、同軸状に配設された2つの円筒形部材
11a,11bによつて結合され環状囲い板11
によつて包囲されており、(第3図に示したよう
に)内側管板に架設された円筒形邪魔板12があ
り、この邪魔板は、囲い板11内で管の長脚と短
脚間を同軸状に延びている。ナトリウムの流路
は、胴基部の入口から上方に向い、囲い板の内側
円筒形部材11bを通つて延長部6内の分配器1
3に至り、そこから管の長脚上を下向きに流れ、
短脚上を上向きに流れて出口3を通つて胴から出
る。U字管の長脚と短脚は第1及び2図に示した
ように外部の出口と入口蒸気ヘツダ14,15と
に夫々接続されている。U字管8は9%クロム合
金鋼であるが、この材料は現場で溶接、液処理が
困難であるので、1%クロム合金鋼の移行部16
を管板とヘツダとの間に配設してある。1%クロ
ム合金の尾部は、9%合金鋼製の管端とヘツダの
尾管とに取付けでき、その(尾部の)製造中に熱
処理することができるものである。相互の連結は
現場で容易に行うことができ、更に熱処理を行う
必要はない。アルゴンのカバーガスは、円筒形邪
魔板12の各側部上でナトリウム液面上部に配置
し、且つ例えば17で示したようなプランチが、
カバーガスの水素含量を検査できるようまたナト
リウムの液面高さを検知できるよう設けてある。 The body has a sodium inlet 2 at the base, an outlet 3 at the side,
It is equipped with a drain port 4 and a pressure release connection 5 for releasing the pressure inside the shell when a reaction between sodium and water occurs. The open end of the barrel has a flanged cylindrical extension 6 with a closed top end, the flange of the barrel and the flange of the extension being bolted together and sealed around the periphery with a light weld 7. heat exchange tube 8
is U-shaped with legs of unequal length and is suspended from an extension 6 within the torso. The longer leg 8a extends along the extension and passes through the end cover forming the inner tubesheet 9, and the shorter leg 8b extends along the annular outer tubesheet 10.
passing through an extension flange forming an extension flange. These tubes are connected by two coaxially arranged cylindrical members 11a, 11b and are connected to an annular shroud 11.
There is a cylindrical baffle 12 surrounded by and suspended in the inner tubesheet (as shown in FIG. It extends coaxially between the two. The flow path for the sodium is directed upwardly from the inlet at the base of the barrel and through the inner cylindrical member 11b of the shroud to the distributor 1 in the extension 6.
3 and from there flows downward on the long leg of the tube,
It flows upwards over the short legs and exits the torso through outlet 3. The long and short legs of the U-tube are connected to external outlet and inlet steam headers 14 and 15, respectively, as shown in FIGS. 1 and 2. The U-shaped tube 8 is made of 9% chromium alloy steel, but since this material is difficult to weld and process in the field, the transition section 16 is made of 1% chromium alloy steel.
is placed between the tube plate and the header. The 1% chromium alloy tail can be attached to the 9% alloy steel tube end and tail tube of the header and can be heat treated during its manufacture. Interlocking can be easily done in situ and requires no further heat treatment. A cover gas of argon is placed above the sodium liquid level on each side of the cylindrical baffle 12, and a plant such as that shown at 17 is
It is equipped to test the hydrogen content of the cover gas and to detect the sodium level.
第3図及び4図に示したように、管8の各々は
すきま開口を通つて関連する管板9,10を貫通
し、スリーブ18によつて管板に封着されてい
る。封着を行うため、各スリーブの下端は管板上
面の開口の境界をなす外方に突出した差し込み口
19に突合せ溶接してあり、直立スリーブの自由
端は管の外壁面にろう付けしてある。各管板の
夫々の差し込み口へのスリーブの溶接は、管を通
す前にスリーブの内側から行い得るようになつて
おり、溶接部は管板全体を過熱することによつて
すべて同時に応力除去される。ろう付け接合は
個々に作られるが、ろう付け接合を作るため、管
の外側面とスリーブ自由端の内側面とは初めに接
合領域を綿密にきれいにしておく。各接合を連続
して作製するため、20で示したストリツプ形フ
イラー材料(第4図)をスリーブの孔に取付け
る。管はスリーブを通つて、スリーブと管との間
に作られた接合のすぐ上の位置まで通されてお
り、且つ管は、スリーブの自由端と密着締り嵌め
させるべく、内部で作動するロール手段によつて
外方に変形される。次いで、管の拡張部分がスリ
ーブの自由端と係合するように、管をスリーブ内
に引入れる。高周波誘導加熱コイル(第4図に於
いて21で示してある)をスリーブの周囲に配置
して、フイラーを溶融するため約1分間加熱を行
うが、接手個所は材料の酸化を防ぐためアルゴン
を充満させた22で示す密封カバーで包囲して置
く。 As shown in FIGS. 3 and 4, each tube 8 passes through an associated tube sheet 9, 10 through a clearance opening and is sealed thereto by a sleeve 18. As shown in FIGS. To effect the seal, the lower end of each sleeve is butt welded to an outwardly projecting spigot 19 bounding the opening in the top of the tubesheet, and the free end of the upright sleeve is brazed to the outside wall of the tube. be. Welding of the sleeve to the respective spigot in each tubesheet can be done from the inside of the sleeve before threading the tube, and the welds are all stress relieved at the same time by heating the entire tubesheet. Ru. The braze joints are made individually, but in order to make the braze joint, the outer surface of the tube and the inner surface of the free end of the sleeve are first carefully cleaned of the joint area. To make each joint in succession, a strip of filler material, indicated at 20 (FIG. 4), is attached to the hole in the sleeve. The tube is threaded through the sleeve to a position just above the joint made between the sleeve and the tube, and the tube is moved by internally actuated rolling means to bring the tube into a tight interference fit with the free end of the sleeve. is deformed outwardly by The tube is then pulled into the sleeve such that the expanded portion of the tube engages the free end of the sleeve. A high frequency induction heating coil (designated 21 in Figure 4) is placed around the sleeve and heated for about 1 minute to melt the filler, but the joints are heated with argon to prevent oxidation of the material. Surround with a filled sealed cover shown at 22.
フイラー材料はニツケルベース合金のニクロブ
ラズ(Nicrobraz)135(ニクロブラズ
(Nicrobraz)は登録商標であり、この材料の融
点は代表的には1065℃程度である)であり、ろう
付け操作は1050℃〜1200℃の範囲内の温度で行な
う。接合は続いて応力除去が行なわれる。 The filler material is the nickel-based alloy Nicrobraz 135 (Nicrobraz is a registered trademark; the melting point of this material is typically around 1065°C), and the brazing operation is performed at temperatures between 1050°C and 1200°C. Perform the test at a temperature within the range of . The bond is then stress relieved.
各ろう付けの結合個所は超音波検査、ヘリウム
漏洩試験及び視覚調査を行い満足できる封着接合
が必ず得られるようにする。スリーブの最外端の
フイラー材料の外観は、結合が有効であるかどう
かの証拠になる。管8は長く連続した管から作ら
れているので、欠陥が発生した場合ナトリウムが
水と接触する原因となるような継目が胴内には存
在しないようになつている。 Each braze joint is subjected to ultrasonic inspection, helium leak testing, and visual inspection to ensure a satisfactory seal. The appearance of the filler material on the outermost edge of the sleeve provides evidence of whether the bond is effective. The tube 8 is made from a long continuous tube so that there are no seams in the shell that could cause the sodium to come into contact with the water in the event of a defect.
複合管体は、内側の管板9の下面から懸吊して
いる円筒形邪魔板12によつて横方向に支持され
ている。邪魔板はこれを通る離伝導を減少するた
め二重壁となつており、取扱い作業時に内壁と外
壁を隔置するようなパツド23(第5図に示して
ある)が内壁と外壁間に所定間隔をおいて配設し
てある。パツド23は内壁には溶接してあるが、
軸線方向に於ける壁の熱線膨張差を調整するため
外壁とは摺動接触している。熱交換管8を横方向
に支持するための内壁及び外壁の環状セル形格子
板24,25が、環状の囲い板で軸線方向に間隔
を隔てて固定してある。各格子板は、内側セル形
格子板24の断片を示す第6図に示されたような
セル形スポーク35によつて相互連結された内側
及び外側リム33,34を具備している。スポー
ク35は、各々1本の管をゆるく収容するための
開口を備えている。スポーク間に可動の防振板2
6が配設してあり、この防振板は管に対するすき
ま開口を備えている。防振板26は、2つの(垂
直方向に間隔をおいて設けられた)半径方向に突
出する合釘(dowel)37で外側のリム34から
摺動自在に支持され、且つこの防振板を半径方向
に内側または外側に動くよう調節できるセツトボ
ルト27によつて内側リム33に固定してある。
格子は、各管脚がスポーク35と防振板26とを
交互に貫通するように囲い板に順次に配設されて
いる。防振板を半径方向に変位させることによつ
て、管の振動を制止するよう横方向に負荷をかけ
ることができる。別の構造では、内側及び外側の
環状セル形格子板24,25が、円筒形邪魔板1
2の内外壁に軸線方向に間隔を隔てて固定してあ
り、この格子板は管を通すための大きいすきま開
口またはスロツトを備えている。この格子板の
各々は、角度を隔てて設けられた一群の防振板を
支持し、管が同じくこの防振板をすきまを設けて
貫通している。防振板は、囲い板の円筒部材8
a,8bを貫通して伸長するセツトボルトによつ
て格子板に関して半径方向に運動自在に設けら
れ、振動を防ぐため管8に対して半径方向に引出
しまたは押し込め得るようになつている。管に負
荷をかけるために行なわれる運動の方向は、内側
及び外側方向のいずれの方向にもできる。囲い板
の円筒形部材8a,8bは防振板に接近できるよ
う着脱自在の部分(図示してない)を有してお
り、この防振板も同じく熱交換器の作動後の点検
に際して管の接触部分の損傷調査を可能にするた
め軸線方向に移動自在であるよう且つ必要が生じ
た場合には管との接触部分を新らしくするために
取り替え得るよう配置してある。 The composite tube is laterally supported by a cylindrical baffle plate 12 suspended from the underside of the inner tubesheet 9. The baffle plate is double-walled to reduce conduction through it, and a pad 23 (shown in Figure 5) is provided between the inner and outer walls to separate the inner and outer walls during handling operations. They are placed at intervals. The pad 23 is welded to the inner wall,
It is in sliding contact with the outer wall to adjust the difference in thermal linear expansion of the wall in the axial direction. Annular cell-shaped grid plates 24, 25 on the inner and outer walls for laterally supporting the heat exchange tubes 8 are fixed at intervals in the axial direction by annular shroud plates. Each grid plate has inner and outer rims 33, 34 interconnected by cellular spokes 35 as shown in FIG. 6, which shows a fragment of the inner cellular grid plate 24. The spokes 35 each have an opening for loosely accommodating a tube. Movable vibration isolation plate 2 between spokes
6 is arranged, and this vibration isolation plate is provided with a clearance opening for the tube. The vibration isolation plate 26 is slidably supported from the outer rim 34 by two (vertically spaced) radially projecting dowels 37 and It is secured to the inner rim 33 by a set bolt 27 which is adjustable to move radially inward or outward.
The grids are sequentially arranged on the shroud so that each tube leg passes alternately through the spokes 35 and the vibration isolation plates 26. By radially displacing the vibration isolators, a lateral load can be applied to dampen the vibrations of the tube. In another construction, the inner and outer annular cellular grid plates 24, 25 have a cylindrical baffle plate 1.
The grid plate is axially spaced and fixed to the inner and outer walls of 2, and the grid plate is provided with large clearance openings or slots for passage of the tubes. Each of the lattice plates supports a group of angularly spaced vibration isolators, through which the tubes also pass with clearance. The vibration isolating plate is the cylindrical member 8 of the shrouding plate.
It is provided for radial movement with respect to the grid plate by means of set bolts extending through a, 8b, so that it can be pulled out or pushed in radially relative to the tube 8 to prevent vibrations. The direction of movement performed to load the tube can be either inward or outward. The cylindrical members 8a and 8b of the shroud have removable parts (not shown) to allow access to the vibration isolators, and the vibration isolators are also used to inspect the tubes after operation of the heat exchanger. It is arranged to be axially movable in order to allow damage investigation of the contact part and to be replaced in order to renew the contact part with the tube if the need arises.
下部格子板24,25下方のU字管8の脚の直
線部分は、第9,10図に示したように補強スリ
ーブ31によつて支持されている。このスリーブ
はその上下端で管を密着して包み、各スリーブの
上端は下方格子板24,25の管案内セル内にし
つかりと固定してある。スリーブは、その両端間
では管から間隔が隔つており、溶融ナトリウムが
管に接触できるよう窓32を備えている。補強ス
リーブ31は、振動や格子乱流による打撃によつ
て生じたクロスフローが原因となるU字管のふれ
を容認できるレベルまで減少する。 The straight portions of the legs of the U-shaped tube 8 below the lower grid plates 24, 25 are supported by reinforcing sleeves 31, as shown in FIGS. 9 and 10. The sleeves tightly enclose the tubes at their upper and lower ends, the upper ends of each sleeve being firmly fixed within the tube guiding cells of the lower grid plates 24,25. The sleeve is spaced apart from the tube between its ends and includes a window 32 to allow molten sodium to contact the tube. The reinforcing sleeve 31 reduces to an acceptable level the runout of the U-tube caused by cross-flow caused by vibration or impact from grid turbulence.
第11及び12図に示した別の支持スリーブ配
置では、U字管とスリーブ間にアルミニウム―ニ
ツケルベース合金製ブツシユ23が設けてある。
このブツシユのアルミニウム処理せる支持面は摩
擦係数が小さいので、熱膨張による管の長手方向
運動および振動による摩滅損傷が大巾に減少され
る。 In an alternative support sleeve arrangement shown in FIGS. 11 and 12, an aluminum-nickel based alloy bushing 23 is provided between the U-tube and the sleeve.
The aluminized support surface of this bushing has a low coefficient of friction, so wear damage due to longitudinal tube movement and vibration due to thermal expansion is greatly reduced.
スリーブ18を用いて熱交換管8を管板9,1
0に適合させることによつて、水とナトリウム間
に管板の境界ができることが避けられる。融接し
た管と管板の接合によつて通常生じる複雑な応力
は除かれているので、管板自体は応力腐食による
クラツク発生の傾向がない。スリーブと管との間
はろう付け接合であつてナトリウムと水の境界内
に融接を使用することは避けてあり、しかもろう
付け接合は製作及び応力除去が容易にできる。囲
い板の外側環状部分の頂部にあるカバーガスの空
間は内側管板に続いており、従つて外側管板の内
側端の温度を容認できるレベルに維持する。 The heat exchange tube 8 is attached to the tube plate 9,1 using the sleeve 18.
By adapting to 0, the formation of a tubesheet boundary between water and sodium is avoided. Because the complex stresses normally associated with fusion welded tube and tubesheet connections are eliminated, the tubesheet itself is not prone to cracking due to stress corrosion. The braze joint between the sleeve and the tube avoids the use of fusion welds within the sodium and water interface, and the braze joint is easy to fabricate and stress relieve. A cover gas space at the top of the outer annular portion of the shroud continues with the inner tubesheet, thus maintaining the temperature at the inner end of the outer tubesheet at an acceptable level.
この発明を実施する熱交換器の別の構造に於い
ては、各管と関連するスリーブとの間の封着を嵌
合片によつて行つている。第7図及び8図につい
て説明すると、管8はすきま開口によつて管板
9,10を貫通し、スリーブ18によつて管板に
封着される。管はスリーブの各端に対し十分なす
きまを保つてスリーブを貫通しており、且つスリ
ーブ上端と管外面とに締り嵌めするよう機械加工
したカラー形状の嵌合片28がある。スリーブ1
8はその下端で管板に溶接してあるが、上端は嵌
合片をスリーブと管とにろう付けすることにより
管8に封着される。ろう付け材料29は、第7図
に示したごとく、ろう付け材料を溶融するため加
熱する前に嵌合片と管との間に挿入でき、または
別の方法として第8図に示したように嵌合片に適
宜に位置決めした溝30内に置くことができる。
ろう付け作業は、前述の実施令に於けるごとく、
不活性雰囲気内で行ない、且つまた作業後応力除
去を行えばよい。このような構造は、ろう付けに
先立つて構造体を組立てる際、多数の管をスリー
ブにより容易に通し得ると言う経済的利益を有し
ている。 In another construction of a heat exchanger embodying the invention, the seal between each tube and its associated sleeve is provided by a mating piece. Referring to FIGS. 7 and 8, the tube 8 passes through the tube sheets 9, 10 by means of clearance openings and is sealed to the tube sheets by means of a sleeve 18. The tube extends through the sleeve with sufficient clearance to each end of the sleeve, and there is a collar-shaped mating piece 28 machined for an interference fit between the upper end of the sleeve and the outer surface of the tube. sleeve 1
8 is welded to the tube sheet at its lower end, while its upper end is sealed to the tube 8 by brazing a mating piece to the sleeve and tube. The brazing material 29 can be inserted between the mating piece and the tube before heating to melt the brazing material, as shown in FIG. 7, or alternatively, as shown in FIG. It can be placed in a suitably positioned groove 30 in the mating piece.
Brazing work shall be carried out as per the above-mentioned implementation order.
The process may be carried out in an inert atmosphere and the stress may be relieved after the process. Such a construction has the economic benefit of allowing multiple tubes to be easily threaded through the sleeve during assembly of the structure prior to brazing.
別の構造に於いては、管は熱交換器内方に向う
スリーブによつて管板に封着される。内方に向い
たスリーブをもつた熱交換器の製作はより複雑で
はあるが、このような熱交換器はナトリウム堆積
物の浄化が困難である多数のポケツトを一般に避
け得るという利益を有する。 In another construction, the tubes are sealed to the tubesheet by a sleeve facing inwardly into the heat exchanger. Although the fabrication of heat exchangers with inwardly facing sleeves is more complex, such heat exchangers have the advantage that they generally avoid multiple pockets that are difficult to clean of sodium deposits.
前述の構造のセル形格子板は、板素材から機械
加工するが、胴に於ける圧力降下が小さいことが
必要な場合には、より複雑な形状のセル形格子板
が必要となり、このような格子板は放電加工技術
を用いればより経済的に形成できるであろう。 Cellular lattice plates of the above structure are machined from plate stock, but if a small pressure drop in the shell is required, a cellular lattice plate with a more complex shape is required. The grid plate could be formed more economically using electrical discharge machining techniques.
第1図は、本発明による多管式熱交換器構造体
の部分断面図、第2図は、平面図、第3図は、第
1図の部分の拡大部分断面図、第4図は、第3
図の部分の拡大部分断面図、第5図は、第1図
の部分の拡大部分断面図、第6図は、第1図の
線―に沿う部分平面図、第7及び8図は、別
の実施例の部分断面図、第9,10,11,12
図は、熱交換管の下端の2つの別の支持袋置の部
分図である。
1…円筒形胴、6…フランジ付円筒形延長部、
8…熱交換管、9…内側管板、10…外側管板、
11…囲い板、12…邪魔板、18…スリーブ、
23…パツド、24,25…格子板、26…防振
板。
FIG. 1 is a partial sectional view of a shell-and-tube heat exchanger structure according to the present invention, FIG. 2 is a plan view, FIG. 3 is an enlarged partial sectional view of the portion shown in FIG. 1, and FIG. Third
FIG. 5 is an enlarged partial sectional view of the part shown in FIG. 1, FIG. 6 is a partial plan view taken along the line of FIG. 1, and FIGS. 9th, 10th, 11th, 12th partial cross-sectional view of the embodiment of
The figure is a partial view of two separate support bags at the lower end of the heat exchange tube. 1... Cylindrical body, 6... Cylindrical extension with flanges,
8... Heat exchange tube, 9... Inner tube sheet, 10... Outer tube sheet,
11... Shrouding plate, 12... Baffle plate, 18... Sleeve,
23... Padded, 24, 25... Grid plate, 26... Vibration proof plate.
Claims (1)
熱交換器であつて、液体金属を導くようになつた
胴と、この胴内に設けられ、水又は蒸気を導くた
めの熱交換管の束とを有し、胴は熱交換管を通す
ための少くとも1つの管板を有し、各熱交換管
は、該熱交換管と管板との間に隙間をもつて管板
の個々の開口を貫通し、各熱交換管は管板の面か
ら直立する夫々のスリーブによつて管板に封着さ
れかつスリーブの自由端が熱交換管の外面に封着
結合され、スリーブは、該スリーブと熱交換管と
の連結部を除いて隙間をもつて管を取り囲んでい
る、熱交換器において、管8とスリーブ18がニ
ツケルベース合金からなるろう付け重ね接合によ
つて互に結合されていることを特徴とする液体金
属―水/蒸気熱交換器。 2 熱交換管8はすべて胴1内の管全体に亘つて
継目なしの連続長さであり、熱交換管の端は胴の
外部で水を導くヘツダ15および蒸気を導くヘツ
ダ14に夫々連結されている、特許請求の範囲第
1項に記載の熱交換器。 3 各スリーブ18は、その自由端として夫々の
熱交換管8の外面に重なる頚部分を形成するため
のテーパ部分を有し、ろう付け接合は前記頚部分
と、この頚部分で囲まれた管の部分との間に作ら
れる、特許請求の範囲第1項又は第2項に記載の
熱交換器。 4 各熱交換管はろう付け重ね接合領域で半径方
向に拡張される、特許請求の範囲第1項、第2項
又は第3項に記載の熱交換器。 5 熱交換管8とスリーブは、夫々熱交換管およ
びスリーブとのろう付け重ね接合を有する管状嵌
合片28を介して間接的に互に結合されている、
特許請求の範囲第1項、第2項又は第3項に記載
の熱交換器。 6 溶融金属用入口及び出口を備え且つ取外し自
在の熱交換管組立体を収容する長い容器を具備す
る熱交換器に於いて、前記熱交換管組立体は、容
器の閉鎖体を形成するフランジ付の延長部と、不
等長の脚を延長部から懸吊させたU字状の熱交換
管群と、該管群の長手方向軸線と同軸状に配置さ
れ且つU字状の管群を包囲する環状囲い板と、延
長部から懸吊され且つ囲い板内で内側及び外側の
環状室を形成する円筒形邪魔板と、上記U字管を
邪魔板から横方向に支持するための手段とを含
み、前記U字管の脚が容器の長手方向軸線に平行
に延び、各管の長い方の管は、熱交換器の第1の
管板を形成する延長部の端壁を貫通するよう囲い
板の内側の室に沿つて延び、各管の短い方の管
は、熱交換器の第2の管板を形成する延長部のフ
ランジを貫通するよう囲い板の外側の室に沿つて
延びることを特徴とする特許請求の範囲第1項〜
5項の何れかに記載の熱交換器。 7 U字管を邪魔板から横方向に支持するための
手段は、円筒形邪魔板によつて支持され且つ熱交
換管によつて貫通される一連の軸線方向に間隔を
隔てて設けられたセル形格子と、各格子に関連す
る一連の角度を隔てて設けた防振板とを含み、該
防振板は管が貫通する開口を備え、管を横方向か
ら支持すべく防振板を格子に関して半径方向に変
位させるための引出し手段とを有することを特徴
とする特許請求の範囲第6項記載の熱交換器。 8 少くともいくつかのU字管は、振動に対して
U字屈曲部を支持するための補強スリーブを備
え、該補強スリーブは、U字屈曲部に隣接する格
子から懸吊し且つU字屈曲部方向に延びているこ
とを特徴とする特許請求の範囲第7項記載の熱交
換器。 9 アルミニウム処理したニツケルベース合金が
各補強スリーブとその補完関係にある管との間に
配設してあることを特徴とする特許請求の範囲第
8項記載の熱交換器。 10 各スリーブ18の一端を管板9,10に先
ず溶接し、夫々の熱交換管8を、スリーブ18に
挿入し、スリーブをちよつと越える位置で熱交換
管を局部的に拡張させて、熱交換管の拡張部分が
スリーブの自由端と締まり嵌めするようにし、前
記拡張部分をスリーブの自由端と重なり関係をな
すように熱交換管を再び位置決めし、熱交換管お
よびスリーブを取り囲む高周波加熱誘導加熱器を
使つて、接合部を不活性ガス雰囲気で包みなが
ら、熱交換管およびスリーブの重なり表面間にニ
ツケルベース合金でろう付けを行うことを特徴と
する熱交換器の製造方法。[Scope of Claims] 1. A liquid metal-water/steam heat exchanger used in nuclear reactor equipment, comprising a shell configured to guide liquid metal, and a shell provided within the shell to guide water or steam. a bundle of heat exchange tubes, the shell having at least one tube sheet for passing the heat exchange tubes, each heat exchange tube having a gap between the heat exchange tube and the tube sheet. each tube through a respective opening in the tubesheet, each heat exchange tube being sealed to the tubesheet by a respective sleeve upright from the face of the tubesheet, the free ends of the sleeves being sealingly coupled to the outer surface of the heat exchange tube. In the heat exchanger, the sleeve 8 and the sleeve 18 are made of a nickel-based alloy and are joined together by a brazed lap joint. 1. A liquid metal-water/steam heat exchanger characterized in that the liquid metal-water/steam heat exchanger is 2. All of the heat exchange tubes 8 are of continuous length throughout the tubes in the shell 1, and the ends of the heat exchange tubes are connected outside the shell to a water-conducting header 15 and a steam-conducting header 14, respectively. A heat exchanger according to claim 1. 3. Each sleeve 18 has at its free end a tapered portion for forming a neck portion that overlaps the outer surface of the respective heat exchange tube 8, and the brazing joint is formed between the neck portion and the tube surrounded by this neck portion. 3. A heat exchanger according to claim 1 or 2, which is made between the heat exchanger and the heat exchanger. 4. A heat exchanger according to claim 1, 2 or 3, wherein each heat exchange tube is radially expanded in the region of the brazed lap joint. 5. The heat exchange tube 8 and the sleeve are indirectly connected to each other via a tubular fitting piece 28 having a brazed lap joint with the heat exchange tube and the sleeve, respectively.
A heat exchanger according to claim 1, 2 or 3. 6. In a heat exchanger comprising an elongated vessel having an inlet and an outlet for molten metal and containing a removable heat exchange tube assembly, said heat exchange tube assembly having a flanged tube forming a closure of the vessel. a U-shaped heat exchange tube group with legs of unequal length suspended from the extension, and a U-shaped heat exchange tube group arranged coaxially with the longitudinal axis of the tube group and surrounding the U-shaped tube group. a cylindrical baffle suspended from the extension and defining inner and outer annular chambers within the shroud; and means for laterally supporting the U-tube from the baffle. the legs of the U-tubes extending parallel to the longitudinal axis of the vessel, the longer tubes of each tube being enclosed so as to pass through the end wall of the extension forming the first tubesheet of the heat exchanger. extending along the inner chamber of the plate, with the shorter tube of each tube extending along the outer chamber of the shroud to pass through the flange of the extension forming the second tube sheet of the heat exchanger; Claims 1 to 1 are characterized by:
The heat exchanger according to any of Item 5. 7 The means for supporting the U-tube laterally from the baffle includes a series of axially spaced cells supported by the cylindrical baffle and penetrated by the heat exchange tubes. shaped gratings and vibration isolators spaced apart at a series of angles associated with each grating, the isolators having openings through which the tubes pass, the vibration isolators being connected to the gratings for laterally supporting the tubes. 7. A heat exchanger according to claim 6, further comprising extraction means for radially displacing the heat exchanger. 8. At least some U-tubes are provided with a reinforcing sleeve for supporting the U-bend against vibrations, the reinforcing sleeve suspending from the grid adjacent to the U-bend and extending from the U-bend. 8. The heat exchanger according to claim 7, wherein the heat exchanger extends in the direction of the heat exchanger. 9. The heat exchanger of claim 8, wherein an aluminized nickel-based alloy is disposed between each reinforcing sleeve and its complementary tube. 10 First, one end of each sleeve 18 is welded to the tube sheets 9 and 10, and each heat exchange tube 8 is inserted into the sleeve 18, and the heat exchange tube is expanded locally at a position slightly beyond the sleeve to release heat. repositioning the heat exchange tube so that the enlarged portion of the exchange tube is in an interference fit with the free end of the sleeve, and placing the enlarged portion in overlapping relationship with the free end of the sleeve; A method for manufacturing a heat exchanger, which comprises brazing the overlapping surfaces of a heat exchange tube and a sleeve with a nickel-based alloy using a heater while enveloping the joint in an inert gas atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1858877A JPS53104002A (en) | 1977-02-21 | 1977-02-21 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1858877A JPS53104002A (en) | 1977-02-21 | 1977-02-21 | Heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53104002A JPS53104002A (en) | 1978-09-09 |
| JPS6262243B2 true JPS6262243B2 (en) | 1987-12-25 |
Family
ID=11975781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1858877A Granted JPS53104002A (en) | 1977-02-21 | 1977-02-21 | Heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS53104002A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5308230B2 (en) * | 2009-05-19 | 2013-10-09 | 熱研産業株式会社 | Multi-tube heat exchanger |
| JP5676894B2 (en) * | 2010-03-17 | 2015-02-25 | 日本発條株式会社 | Fixing structure between metal plate and heat transfer tube |
-
1977
- 1977-02-21 JP JP1858877A patent/JPS53104002A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53104002A (en) | 1978-09-09 |
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