JPS61270592A - cryogenic transfer tube - Google Patents

cryogenic transfer tube

Info

Publication number
JPS61270592A
JPS61270592A JP60110430A JP11043085A JPS61270592A JP S61270592 A JPS61270592 A JP S61270592A JP 60110430 A JP60110430 A JP 60110430A JP 11043085 A JP11043085 A JP 11043085A JP S61270592 A JPS61270592 A JP S61270592A
Authority
JP
Japan
Prior art keywords
tube
heat shield
holder
heat
cryogenic
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
JP60110430A
Other languages
Japanese (ja)
Other versions
JPH0338476B2 (en
Inventor
典英 佐保
松田 紀元
今村 実
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP60110430A priority Critical patent/JPS61270592A/en
Publication of JPS61270592A publication Critical patent/JPS61270592A/en
Publication of JPH0338476B2 publication Critical patent/JPH0338476B2/ja
Granted legal-status Critical Current

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  • Thermal Insulation (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の分野〕 本発明は極低温移送管に係り、特に液体ヘリウム等の極
低温流体を移送するのに好適な極低温移送管に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Field of the Invention] The present invention relates to a cryogenic transfer tube, and more particularly to a cryogenic transfer tube suitable for transferring a cryogenic fluid such as liquid helium.

〔発明の背景〕[Background of the invention]

液体ヘリウム等の極低温流体を移送する低温流体移送管
としては、例えば、実公昭56−32707号に記載の
ように極低温流体が内部を流通する内管と、該内管の外
側で内管外面と真空断熱空間を形成して配設された高温
の外管との間には、内管と外管が直接に接触しないよう
、熱伝導率の小さい例えば、高分子材のホルダーを内管
長手方向に所定間隔毎にらせん状に設けている。
As a cryogenic fluid transfer pipe for transferring a cryogenic fluid such as liquid helium, for example, as described in Japanese Utility Model Publication No. 56-32707, there is an inner pipe through which the cryogenic fluid flows, and an inner pipe outside the inner pipe. A holder made of a polymer material with low thermal conductivity, such as a polymer material, is placed between the outer surface and the high-temperature outer tube, which is placed in a vacuum-insulated space, to prevent direct contact between the inner tube and the outer tube. They are provided in a spiral shape at predetermined intervals in the hand direction.

夕1 しかし、このような極低温移送管では、ポルイー間に内
管と外管が直接対面する空間ができ、屈曲性を有する極
低温移送管では、移送管を曲げた場合、該空間で、内管
と外管とが直接接触し、外管から内管への侵入熱により
、極低温流体の移送効率が著しく低下する一因となって
いる。これは、内管と外管との間に中間温度の熱シール
ド管が存在する場合、内管と熱シールド管の間のボルダ
ーに関しても同様である。また、ホルダーを長手方向に
所定の間隔で設けられているため、その製造がめんどう
であり、移送管製造コス)・高の一因となっている。
E1 However, in such a cryogenic transfer tube, there is a space between the polyurethane tubes where the inner tube and the outer tube directly face each other, and in a cryogenic transfer tube with flexibility, when the transfer tube is bent, in this space, The inner tube and the outer tube are in direct contact, and heat intrusion from the outer tube to the inner tube causes a significant decrease in the transfer efficiency of the cryogenic fluid. This also applies to the boulder between the inner tube and the heat shield tube when there is a heat shield tube at an intermediate temperature between the inner tube and the outer tube. Furthermore, since the holders are provided at predetermined intervals in the longitudinal direction, their manufacture is troublesome, which is one of the reasons for the high cost of manufacturing the transfer tube.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、内情と熱シールド管との開に筒状ホル
ダーを配設して、極低温移送管を屈曲させた際に、内管
と熱シールド管との直接接触を防いで熱伝達をおさえ、
極低温流体の移送効率を向」−できる極低温移送管を提
供することにある。
An object of the present invention is to dispose a cylindrical holder between the inner tube and the heat shield tube to prevent direct contact between the inner tube and the heat shield tube and to transfer heat when the cryogenic transfer tube is bent. hold down,
An object of the present invention is to provide a cryogenic transfer tube that can improve the transfer efficiency of cryogenic fluid.

〔発明の概要〕[Summary of the invention]

低温流体を流通させる屈曲可能な内管と、該内情の外側
に配設された屈曲可能な熱シールド管と、該熱シールド
管の外側に配設された屈曲可能な外管と、iffff管
内管記熱シールド管との間に配設された屈曲可能な筒状
ホルダーとから成ることを特徴とし、1i7I Me筒
状ホルダーとして熱伝導率の小さな高分子材で製作し、
連続波形管にして屈曲可能にするとともに、小さな曲げ
半径で移送管を曲げても、内管と熱シールド管が直接接
触しないようにして、筒状ボルダ−を介しての内管と熱
シールド管の接触部の伝導伝熱の移動距離を長(して、
熱シールド管から内管へ侵入する熱量を極小にし、極低
温流体の断熱効果を十分に上げるようにしたものである
。
A bendable inner tube through which low-temperature fluid flows, a bendable heat shield tube disposed outside the inner tube, a bendable outer tube disposed outside the heat shield tube, and an iffff tube inner tube. The 1i7I Me cylindrical holder is made of a polymer material with low thermal conductivity, and is characterized by a bendable cylindrical holder disposed between the heat recording shield tube and the 1i7I Me cylindrical holder.
The continuous corrugated pipe is made bendable, and even if the transfer pipe is bent with a small bending radius, the inner pipe and heat shield pipe do not come into direct contact with each other. Increase the travel distance of conductive heat transfer at the contact area (by
This minimizes the amount of heat that enters the inner tube from the heat shield tube and sufficiently increases the heat insulation effect of the cryogenic fluid.

〔発明の実施例〕[Embodiments of the invention]

本発明の一実施例を第1図により説明する。第1図で屈
曲性を有する極低温移送管1は、例えば液体ヘリウム等
の極低温流体が内部を流通する内管2と、内管2の外側
に配置された筒状ホルダーである波形管ホルダー3と、
波形ボルダ−3の外側に配設された熱シールド管4と、
熱シールド管4の外側で熱シールド管4外面と熱伝導媒
体雰囲気5を形成して配設された他の熱シールド管6と
、熱伝導媒体雰囲気5内にスパイラル状に配設された冷
却管7と、他の熱シールド管6の外側に配設された外管
8と、他の熱シールド管6の外側と外管8の内側の空間
に巻き付けられた多層断熱材9とで構成されている。ま
た、内管2と熱シールド管4の間には真空断熱空間10
、他の熱シールド管6と外管の間には真空断熱空間11
が形成されている。
An embodiment of the present invention will be explained with reference to FIG. In FIG. 1, a cryogenic transfer tube 1 having flexibility includes an inner tube 2 through which a cryogenic fluid such as liquid helium flows, and a corrugated tube holder which is a cylindrical holder placed outside the inner tube 2. 3 and
a heat shield tube 4 disposed outside the corrugated boulder 3;
Another heat shield tube 6 is arranged outside the heat shield tube 4 to form a heat conduction medium atmosphere 5 with the outer surface of the heat shield tube 4, and a cooling tube is arranged in a spiral shape in the heat conduction medium atmosphere 5. 7, an outer tube 8 disposed outside the other heat shield tube 6, and a multilayer insulation material 9 wrapped around the outside of the other heat shield tube 6 and the space inside the outer tube 8. There is. Furthermore, a vacuum insulation space 10 is provided between the inner tube 2 and the heat shield tube 4.
, a vacuum insulation space 11 is provided between the other heat shield tube 6 and the outer tube.
is formed.

第1図で内管2の内部を極低温流体、例えば、液体ヘリ
ウムが流動させられ、冷却管7には、冷却媒体、例えば
、液体窒素が供給されてその内部を流通させられる。熱
伝導媒体雰囲気5は、例えば、ヘリウムガス雰囲気であ
る。この状態で、熱シールド管4およびその他の熱シー
ルド管6は、ヘリウムガスの熱伝導により液体窒素温度
である77に付近に冷却される。移送管全体がどのよう
に曲げられても、内管2は、波形管ホルダー3で囲まれ
ており、熱シールド管4と直接に接触することはなく、
かつ、波形管ボルダ−3は熱伝導率の小さい高分子材で
製作され、波形管ホルダー3と内管2および熱シールド
w4との接触部は線接触で、しかも、その間の波形管ホ
ルダー3の熱移動距離は波形状に長(なり、熱シールド
管4がらの断熱効果は十分に発揮される。したがって、
内管2内を流動する液体ヘリウムの蒸発、すなわち熱損
失が小さく抑制される。
In FIG. 1, a cryogenic fluid such as liquid helium is made to flow inside the inner tube 2, and a cooling medium such as liquid nitrogen is supplied to the cooling pipe 7 and made to flow therein. The heat conduction medium atmosphere 5 is, for example, a helium gas atmosphere. In this state, the heat shield tube 4 and other heat shield tubes 6 are cooled to around 77, which is the liquid nitrogen temperature, by heat conduction of the helium gas. No matter how the entire transfer tube is bent, the inner tube 2 is surrounded by the corrugated tube holder 3 and does not come into direct contact with the heat shield tube 4.
In addition, the corrugated tube boulder 3 is made of a polymer material with low thermal conductivity, and the contact portions between the corrugated tube holder 3, the inner tube 2, and the heat shield w4 are line contact, and the corrugated tube holder 3 is in contact with the inner tube 2 and the heat shield w4. The heat transfer distance becomes long in the wave shape, and the heat insulation effect of the heat shield tube 4 is fully exhibited. Therefore,
Evaporation of the liquid helium flowing within the inner tube 2, that is, heat loss, is suppressed to a small level.

本実施例では、次のような効果を得ることができる。In this embodiment, the following effects can be obtained.

(1)  内管の外面と、熱シールド管の内側の真空空
間に、管長手方向に連続にホルダーを形成できるので、
極低温移送管をどのように曲げても、内管と熱シールド
管が01接接触せず、それによって断熱効果を十分に発
揮でき、内管内部を流動する液体ヘリウムの移送効率を
向上できる。
(1) The holder can be formed continuously in the longitudinal direction of the tube on the outer surface of the inner tube and in the vacuum space inside the heat shield tube.
No matter how the cryogenic transfer tube is bent, the inner tube and the heat shield tube do not come into direct contact with each other, thereby making it possible to sufficiently exhibit the heat insulation effect and improve the transfer efficiency of liquid helium flowing inside the inner tube.

(2)  ホルダーを波形管とすることにより、内管と
熱シールド管との間接接触熱移動距離を長くでき、断熱
効果を十分発揮でき、液体ヘリウムの移送効率を向上で
きる。
(2) By using a corrugated tube as the holder, the indirect contact heat transfer distance between the inner tube and the heat shield tube can be increased, the heat insulation effect can be sufficiently exhibited, and the transfer efficiency of liquid helium can be improved.

(3)  ホルダーを内管外側にスパイラル状に巻き付
ける必要がなく、ホルダー内に内管な軽く挿入するだけ
でよ(極低温移送管の製作工数を低減できる。
(3) There is no need to spirally wrap the holder around the outside of the inner tube, just insert the inner tube into the holder (reducing the number of man-hours required to manufacture the cryogenic transfer tube).

次に本発明の第2の実施例を第2図により説明する。第
2図で、上記した本発明の一実施例を示す第1図と異な
る点は、波形管ホルダー3の外側と熱シールド管4の内
側との真空空間10に、高分子材でできたひも状ホルダ
ー12をスパイラル状に形成した点である。(4(シー
ルド管4から外側は図示省略)本実施例によれば、波形
管ホルダー3と熱シールド管4との接触面積をさらに小
さく、かつ、内管2と熱シールド管との間接接触熱移動
距離をさら(こ長(でき、断熱効果をさらに発揮し、液
体ヘリウムの移送効果をさらに向上できる。この場合、
ひも状ホルダー12を、内管2の外側と波形管ホルダー
3の内側の真空空間暑こ配設しても同様な効果が生じ、
両真空空間に配設すれば、さらに断熱効果が同上する。
Next, a second embodiment of the present invention will be described with reference to FIG. The difference between FIG. 2 and FIG. 1, which shows an embodiment of the present invention described above, is that a string made of polymer material is placed in the vacuum space 10 between the outside of the corrugated tube holder 3 and the inside of the heat shield tube 4. This is because the shaped holder 12 is formed in a spiral shape. (4 (Outside of the shield tube 4 is omitted from illustration)) According to this embodiment, the contact area between the corrugated tube holder 3 and the heat shield tube 4 is further reduced, and the indirect contact heat between the inner tube 2 and the heat shield tube is The moving distance can be extended, the insulation effect can be further improved, and the liquid helium transfer effect can be further improved. In this case,
A similar effect can be obtained by placing the string-like holder 12 in a vacuum space between the outside of the inner tube 2 and the inside of the corrugated tube holder 3.
If it is placed in both vacuum spaces, the insulation effect will be further improved.

次に本発明の第3の実施例を第3図により説明する。第
3図が前記した本発明の一実施例を示す第1図と異なる
点は、第1図に示す波形管ホルダー3の片面もしくは両
面に、例えばふ4射の小さいアルミニウム等の薄膜を蒸
41゛シた波形管ホルダー13を使用している点である
。(熱シールド管4から外側は図示省略)本実施例によ
れば、波形管ホルダー13の素地のふく射率08〜0.
9を0.02程度まで小さくすることができ、熱シール
ド管4から波形管ホルダー13へのふく射熱による熱侵
入を小さくすることができ、断熱効果をさらに発揮し、
液体ヘリウムの移送効率をさらに向上できる。
Next, a third embodiment of the present invention will be described with reference to FIG. The difference between FIG. 3 and FIG. 1, which shows an embodiment of the present invention described above, is that a thin film of aluminum or the like with low radiation radiation is coated on one or both sides of the corrugated tube holder 3 shown in FIG. The point is that a corrugated tube holder 13 is used. (External parts from the heat shield tube 4 are omitted from illustration) According to this embodiment, the radiation rate of the material of the corrugated tube holder 13 is 08 to 0.
9 can be reduced to about 0.02, the heat intrusion due to radiant heat from the heat shield tube 4 to the corrugated tube holder 13 can be reduced, and the heat insulation effect is further exhibited.
Liquid helium transfer efficiency can be further improved.

二の場合、第2図に示した如(、C・も状ボルダ−12
を併用することによって、さらに断熱効果を向上させる
ことができる。
In the case of 2, as shown in Fig. 2,
By using together, the heat insulation effect can be further improved.

次に本発明の第4の実施例を第4図により説明する。第
4図が前記した本発明の一実施例を示す第1図と異なる
点は、第1図に示す波形管ホルダー3の表裏に、貫通す
る穴14を1個以上設けた点である。(熱シールド管4
から外側は図示省略)本実施例によれば、内管2の外側
と熱シールド管4の内側の間の真空空間10が穴14を
通じて局部的昏こ導通されるので、移送管の真空排気を
良好に行なえ、真空断熱の効果を十分発揮することがで
きる。
Next, a fourth embodiment of the present invention will be described with reference to FIG. The difference between FIG. 4 and FIG. 1, which shows an embodiment of the present invention described above, is that one or more penetrating holes 14 are provided on the front and back sides of the corrugated tube holder 3 shown in FIG. 1. (Heat shield tube 4
According to this embodiment, the vacuum space 10 between the outside of the inner tube 2 and the inside of the heat shield tube 4 is locally communicated through the hole 14, so that the transfer tube can be evacuated. It can be carried out well and the effect of vacuum insulation can be fully demonstrated.

〔うむ明の効果〕[Effect of Umu Ming]

本発明は、以上説明したように、極低温流体が内部を流
通する内管と熱シールド管の間の真空空間内を、長手方
向に連続的にホルダーで仕切ることができるので、移送
管全体をどのように曲げても内情と熱シールド管が直接
接触することはなく、熱シールド管から内管への熱侵入
を極小にすることができ、断熱効果を十分に発揮でき、
極低温流体の移送効率を向上できるという効果がある。
As explained above, the present invention allows the vacuum space between the inner tube and the heat shield tube, through which the cryogenic fluid flows, to be partitioned continuously in the longitudinal direction by the holder, so that the entire transfer tube can be separated. No matter how you bend it, the inner tube and the heat shield tube do not come into direct contact with each other, minimizing heat intrusion from the heat shield tube to the inner tube, and fully demonstrating the insulation effect.
This has the effect of improving the transfer efficiency of cryogenic fluid.

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

第1図は本発明の一実施例である極低温移送管を示す斜
視断面図、第2図は本発明の第2の実施例である極低温
移送管を示す斜視断面図、第3図は本発明の第3の実施
例である極低温移送管を示す斜視断面図、第4図は本発
明の第4の実施例である極低温移送管を示す斜視断面図
で島る。
FIG. 1 is a perspective sectional view showing a cryogenic transfer tube which is an embodiment of the present invention, FIG. 2 is a perspective sectional view showing a cryogenic transfer tube which is a second embodiment of the present invention, and FIG. FIG. 4 is a perspective sectional view showing a cryogenic transfer tube according to a third embodiment of the present invention, and FIG. 4 is a perspective sectional view showing a cryogenic transfer tube according to a fourth embodiment of the present invention.

Claims (1)

【特許請求の範囲】 1、低温流体を流通させる屈曲可能な円管と、該内管の
外側に配設された屈曲可能な熱シールド管と、該熱シー
ルド管の外側に配設された屈曲可能な外管と、前記内管
と前記熱シールド管との間に配設された屈曲可能な筒状
ホルダーとから成ることを特徴とする極低温移送管。 2、前記筒状ホルダーが波形管である特許請求の範囲第
1項の極低温移送管。 3、前記筒状ホルダーと前記熱シールド管との間に、繊
維状のホルダーをスパイラル状に配設した特許請求の範
囲第1項の極低温移送管。 4、前記筒状ホルダーの片面もしくは両面に金属薄膜を
被着させた特許請求の範囲第1項の極低温移送管。 5、前記筒状ホルダーに表裏を貫通する穴を少なくとも
1個以上設けた特許請求の範囲第1項の極低温移送管。
[Claims] 1. A bendable circular tube through which low-temperature fluid flows, a bendable heat shield tube disposed outside the inner tube, and a bendable heat shield tube disposed outside the heat shield tube. A cryogenic transfer tube comprising a flexible outer tube and a bendable cylindrical holder disposed between the inner tube and the heat shield tube. 2. The cryogenic transfer tube according to claim 1, wherein the cylindrical holder is a corrugated tube. 3. The cryogenic transfer tube according to claim 1, wherein a fibrous holder is spirally arranged between the cylindrical holder and the heat shield tube. 4. The cryogenic transfer tube according to claim 1, wherein a metal thin film is coated on one or both sides of the cylindrical holder. 5. The cryogenic transfer tube according to claim 1, wherein the cylindrical holder is provided with at least one hole passing through the front and back sides.
JP60110430A 1985-05-24 1985-05-24 cryogenic transfer tube Granted JPS61270592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60110430A JPS61270592A (en) 1985-05-24 1985-05-24 cryogenic transfer tube

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60110430A JPS61270592A (en) 1985-05-24 1985-05-24 cryogenic transfer tube

Publications (2)

Publication Number Publication Date
JPS61270592A true JPS61270592A (en) 1986-11-29
JPH0338476B2 JPH0338476B2 (en) 1991-06-10

Family

ID=14535543

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60110430A Granted JPS61270592A (en) 1985-05-24 1985-05-24 cryogenic transfer tube

Country Status (1)

Country Link
JP (1) JPS61270592A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05263987A (en) * 1991-12-31 1993-10-12 Air Prod And Chem Inc Method and apparatus for insulating cryogenic devices
JP2017527754A (en) * 2014-08-08 2017-09-21 ネクサン Flexible conduit

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05263987A (en) * 1991-12-31 1993-10-12 Air Prod And Chem Inc Method and apparatus for insulating cryogenic devices
JP2017527754A (en) * 2014-08-08 2017-09-21 ネクサン Flexible conduit

Also Published As

Publication number Publication date
JPH0338476B2 (en) 1991-06-10

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