JPH03293784A - Cryostat - Google Patents
CryostatInfo
- Publication number
- JPH03293784A JPH03293784A JP2095152A JP9515290A JPH03293784A JP H03293784 A JPH03293784 A JP H03293784A JP 2095152 A JP2095152 A JP 2095152A JP 9515290 A JP9515290 A JP 9515290A JP H03293784 A JPH03293784 A JP H03293784A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- piping
- cryostat
- refrigerant
- section
- 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
Links
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- Containers, Films, And Cooling For Superconductive Devices (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は、超電導機器等に使用されるクライオスタット
に関する。Detailed Description of the Invention [Object of the Invention] (Industrial Application Field) The present invention relates to a cryostat used in superconducting equipment and the like.
(従来の技術)
従来、超電導マグネット等を極低温に保持するためのク
ライオスタットは、極低温冷媒の蒸発を極力少なくする
ため以下のような構成となっている。即ち、極低温冷媒
を収容する冷媒容器と。(Prior Art) Conventionally, a cryostat for maintaining a superconducting magnet or the like at a cryogenic temperature has the following configuration in order to minimize evaporation of a cryogenic refrigerant. That is, a refrigerant container containing cryogenic refrigerant.
この冷媒容器を覆うとともに、上記冷媒容器との間に真
空断熱層を形成する真空容器と、上記断熱層内に設けら
れた熱シールドと、一端側が前記冷媒容器に通じるとと
もに、他端側か前記真空断熱層、熱シールドおよび真空
容器の壁を貫通して常温部に位置するように設けられ、
極低温冷媒の注入、蒸発気体の回収、電流リードの案内
等に供される配管とで構成されている。a vacuum container that covers the refrigerant container and forms a vacuum insulation layer between it and the refrigerant container; a heat shield provided within the insulation layer; one end communicates with the refrigerant container; It is installed so that it penetrates the vacuum insulation layer, heat shield and wall of the vacuum container and is located in the room temperature area.
It consists of piping used for injection of cryogenic refrigerant, collection of evaporated gas, guidance of current leads, etc.
上記のように構成されたクライオスタットにあっては、
前記配管を介する以外の冷媒容器への侵入熱は、小型冷
凍機等の設置により数mWまで押えることができる。し
かし、前記配管に関わる侵入熱は、一般に数十mWであ
り、冷媒の蒸発量を低減する上で大きな問題となる。こ
の配管に関わる侵入熱は、配管内の蒸発気体の対流によ
るものが大きな要因となっている。例えば、垂直配管の
場合、前記配管からの侵入熱によって、前記配管内の管
壁近傍では上昇流が、配管中央部では下降流が生じ、こ
の対流現象によって常温部の暖かいガスが低温部に持ち
込まれ蒸発量が増加する。In a cryostat configured as above,
The heat that enters the refrigerant container other than through the piping can be suppressed to several milliwatts by installing a small refrigerator or the like. However, the intrusion heat related to the piping is generally several tens of mW, which poses a big problem in reducing the amount of evaporation of the refrigerant. A major factor in the intrusion heat related to this piping is due to convection of evaporated gas within the piping. For example, in the case of vertical piping, the heat intruding from the pipe causes an upward flow near the pipe wall and a downward flow in the center of the pipe, and this convection phenomenon brings warm gas from the normal temperature area to the low temperature area. The amount of evaporation increases.
この蒸発気体の対流による蒸発量の増加は、前記配管の
断面積を小さくすれば、それに応じて対流も抑制される
ため、抑えられる。しかしながら、超電導マグネットの
クエンチによる冷媒容器の内圧上昇を抑えるために、配
管径をある程度以下に出来ない。このため、従来のクラ
イオスタットでは、特開昭64−59911号公報に示
されるように管軸方向に多数の小孔を有する筒状体を配
置するものが提案されている。This increase in the amount of evaporation due to the convection of the evaporated gas can be suppressed by reducing the cross-sectional area of the piping, since the convection is also suppressed accordingly. However, in order to suppress an increase in the internal pressure of the refrigerant container due to quenching of the superconducting magnet, the pipe diameter cannot be reduced to a certain level. For this reason, a conventional cryostat has been proposed in which a cylindrical body having a large number of small holes is arranged in the tube axis direction, as shown in Japanese Patent Laid-Open No. 64-59911.
しかしながら、上述のような構成では、それ程大きな効
果は得られない。このことは以下のように説明される。However, such a configuration as described above does not provide such a great effect. This is explained as follows.
前記配管内に前述のような筒状体を挿入することで、対
流による侵入熱は減少するものの、挿入した多数の小孔
を有する筒状体の伝導による侵入熱が増加するため侵入
熱はそれ程減少しない。Inserting a cylindrical body like the one described above into the pipe reduces the amount of heat intrusion due to convection, but the amount of heat intrusion due to conduction through the inserted cylindrical body, which has a large number of small holes, increases, so the amount of heat intrusion is not that much. Does not decrease.
さらに、小孔を多数設ける構造は大気などの混入による
配管の閉塞を促進することになる。Furthermore, a structure with a large number of small holes promotes clogging of the piping due to intrusion of air and the like.
(発明が解決しようとする課題)
上述のごとく、配管内に前述のような筒状体を設けただ
けでは、前記配管からの侵入熱を押えることができない
上、配管の閉塞の可能性が高くなる。(Problems to be Solved by the Invention) As described above, simply providing the above-mentioned cylindrical body inside the pipe cannot suppress the heat intruding from the pipe, and there is a high possibility that the pipe will be blocked. Become.
そこで本発明は、配管内を通して極低温冷媒容器に入っ
てくる侵入熱を確実に抑制できると同時に、配管の閉塞
の可能性が少ないクライオスタットを提供することを目
的とする。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a cryostat that can reliably suppress the intrusion heat that enters the cryogenic refrigerant container through the inside of the pipe, and at the same time has a low possibility of clogging the pipe.
(課題を解決するための手段)
本発明のクライオスタットでは、極低温冷媒の注入、蒸
発気体の回収、電流リードの案内等に供される配管内に
1つあるいは複数の薄肉筒を。(Means for Solving the Problems) In the cryostat of the present invention, one or more thin-walled tubes are provided in the piping used for injection of cryogenic refrigerant, recovery of evaporated gas, guidance of current leads, etc.
同軸状に配置する。Arrange coaxially.
(作用)
前述のごとく、配管内に1つ以上の円筒を同軸状に設け
ることで、流路断面全体に自然対流による境界層が発達
し、流路断面全域にわたって上昇流が流れることになり
、配管内の対流現象を抑えることができる。即ち、常温
部の暖かいガスが低温部に持ち込まれることがなくなり
、配管部から侵入熱を抑えることができる。さらに、こ
のような同軸筒の構成では、配管内の流路断面を大きく
とることができるため閉塞の可能性が少なくなる。(Function) As mentioned above, by providing one or more cylinders coaxially within the pipe, a boundary layer due to natural convection develops over the entire cross section of the flow path, and an upward flow flows over the entire cross section of the flow path. It is possible to suppress the convection phenomenon inside the piping. That is, warm gas from the normal temperature section is not brought into the low temperature section, and heat intrusion from the piping section can be suppressed. Furthermore, with such a coaxial cylinder configuration, the cross section of the flow path within the pipe can be made large, reducing the possibility of blockage.
(実施例) 以下1本発明の実施例を図面を参照しながら説明する。(Example) An embodiment of the present invention will be described below with reference to the drawings.
第1図は、本発明の一実施例に係わるクライオスタット
を示すもので、基本的な構成は従来のクライオスタット
と同じであるが、本発明が従来のものと異なる点は、配
管7の内部にFRPなどの熱伝導率の低い材料からなる
円筒11を同軸状に配置したことである。FIG. 1 shows a cryostat according to an embodiment of the present invention. The basic configuration is the same as a conventional cryostat, but the present invention differs from the conventional cryostat in that the inside of the pipe 7 is made of FRP. The cylinders 11 made of a material with low thermal conductivity, such as, are arranged coaxially.
すなわち、この実施例に係わるクライオスタットでは、
極低温冷媒2の注入、蒸発気体の回収、電流リードの案
内等に供される配管7の内部に1つ、あるいは必要に応
じて複数の筒を配管7にたいして同軸上に配置する。That is, in the cryostat according to this embodiment,
One tube or a plurality of tubes as necessary are arranged coaxially with the tube 7 inside the tube 7 which is used for injecting the cryogenic refrigerant 2, recovering evaporated gas, guiding current leads, etc.
そもそも、配管7の内部に対流が生じる理由は次のとお
りである。第3図のごとく配管7を通して侵入する熱に
よって壁近傍に自然対流による上昇流が生じ、この上昇
流によって系外に持ち去られるガスの質量が、対流以外
の侵入熱によって蒸発するガスの質量よりも大きい場合
に、管路断面における質量流量のバランスを取るために
配管中央部に下降流が生じる。この下降流によって熱が
低温部に持ち込まれ冷媒の蒸発量が増加し系内がバラン
スする。The reason why convection occurs inside the pipe 7 is as follows. As shown in Figure 3, the heat penetrating through the pipe 7 causes an upward flow near the wall due to natural convection, and the mass of gas carried out of the system by this upward flow is greater than the mass of gas evaporated by intruding heat other than convection. If it is large, a downward flow occurs in the center of the pipe in order to balance the mass flow rate in the pipe cross section. This downward flow brings heat to the low-temperature part, increases the amount of evaporation of the refrigerant, and balances the system.
上述のような過程によって対流現象がおごるため、配管
7内に配置する円筒の個数、材質、直径、厚みなどは、
使用するクライオスタットの侵入熱に応じて最適値が存
在する。その−例を図2に示す1図中、横軸は円筒の数
、縦軸は冷媒蒸発量である1図2に示すように挿入する
円筒の数が増加するとある値までは、蒸発量が減少する
がそれ以降は逆に増加する。即ち、円筒の数が少ないと
きは対流の防止効果が小さく、円筒の数が増えると。Since the convection phenomenon occurs due to the above-mentioned process, the number, material, diameter, thickness, etc. of the cylinders placed in the pipe 7 are
There is an optimum value depending on the intrusion heat of the cryostat used. An example of this is shown in Figure 2. In the figure, the horizontal axis is the number of cylinders, and the vertical axis is the amount of refrigerant evaporation. As shown in Figure 2, as the number of inserted cylinders increases, the amount of evaporation increases up to a certain value. It decreases, but after that it increases. That is, when the number of cylinders is small, the effect of preventing convection is small, and when the number of cylinders increases.
円筒の伝導による侵入熱が増加し蒸発量が増える。The amount of heat that enters through the cylinder increases, and the amount of evaporation increases.
また、円筒の数が増加すれば、各区切られた流路の断面
積が小さくなるため、閉塞の可能性が増加する。Furthermore, as the number of cylinders increases, the cross-sectional area of each divided flow path becomes smaller, increasing the possibility of blockage.
また、この円筒の挿入個数、位置、材質、厚みなどは、
図4に示すように配管内壁および円筒表面より発達する
境界層がその流路全体をしめるように、即ち、流路断面
全体で上昇流となるように決めることが必要である。こ
の様に、本実施例の同軸円筒構成は配管内の対流を抑制
し、冷媒の蒸発量を減少させ、かつ閉塞の可能性を少な
くできる。In addition, the number of inserted cylinders, position, material, thickness, etc.
As shown in FIG. 4, it is necessary to determine so that the boundary layer developed from the inner wall of the pipe and the cylindrical surface closes the entire flow path, that is, the flow is upward across the entire cross section of the flow path. In this way, the coaxial cylindrical structure of this embodiment can suppress convection within the pipe, reduce the amount of evaporation of the refrigerant, and reduce the possibility of blockage.
なお、本発明では、上述した、実施例に限定されるもの
ではなく、種々の変形例が考えられる。Note that the present invention is not limited to the embodiments described above, and various modifications can be made.
すなわち、配管7の流路断面の形状によらず同様の構成
を用いることができる。さらに、自然対流などによる境
界層が十分に発達していない低温部では低温部側だけ挿
入する円筒の数を増やすことで、低温側でも流路断面全
体で上昇流のみを形成させることが出来る。特に、小型
冷凍機などのシールドクーラーにより配管の途中にサー
マルアンカを取る場合には、上述のような構成は特に有
効である。That is, the same configuration can be used regardless of the shape of the flow path cross section of the pipe 7. Furthermore, in low-temperature areas where the boundary layer due to natural convection or the like is not sufficiently developed, by increasing the number of cylinders inserted only on the low-temperature side, it is possible to form only upward flow in the entire channel cross section even on the low-temperature side. In particular, the above-described configuration is particularly effective when a thermal anchor is installed in the middle of piping using a shield cooler such as a small refrigerator.
また、円筒11の代りに四角筒や六角筒等を用いてもよ
い。Further, instead of the cylinder 11, a square cylinder, a hexagonal cylinder, or the like may be used.
以上述べたように1本発明によれば、極低温冷媒の注入
、蒸発気体の回収、電流リードの案内等に供される配管
を通して、対流によって侵入する熱量を大幅に低減でき
、かつ、閉塞の可能性が少ないクライオスタットを提供
できる。As described above, according to the present invention, it is possible to significantly reduce the amount of heat that enters by convection through piping used for injection of cryogenic refrigerant, recovery of evaporated gas, guidance of current leads, etc., and to prevent blockages. We can provide a cryostat that is unlikely.
第を図は本発明の一実施例に関わるフライ第スタットの
概略断面図、第1図は挿入する円筒の数による蒸発量の
変化を示す線図、第1図は円筒内の蒸発ガスの速度分布
の図、第四図は本発明の対流防止部を挿入した場合の配
管内速度分布の概略図である。
1・・・超電導コイル、 2・・・極低温冷媒。
3・・・冷媒容器、 4・・・真空断熱層、5・
・・真空容器、 6・・・熱シールド、71.、
配管、 8・・・サーマルアンカ。
9・・・小型冷凍機、 11・・・円筒。Figure 1 is a schematic cross-sectional view of a fly-stat according to an embodiment of the present invention, Figure 1 is a diagram showing changes in the amount of evaporation depending on the number of inserted cylinders, Figure 1 is the velocity of evaporated gas in the cylinders. The distribution diagram, Figure 4, is a schematic diagram of the velocity distribution in the pipe when the convection prevention part of the present invention is inserted. 1...Superconducting coil, 2...Cryogenic refrigerant. 3... Refrigerant container, 4... Vacuum insulation layer, 5...
...Vacuum container, 6...Heat shield, 71. ,
Piping, 8...Thermal anchor. 9...Small refrigerator, 11...Cylinder.
Claims (4)
を覆うとともに、上記冷媒容器との間に真空断熱層を形
成する真空容器と、一端側が前記冷媒容器に通じるとと
もに他端側が前記真空断熱層と真空容器の壁を貫通して
常温部に位置する配管とを備えてなるクライオスタット
において、前記配管内に低熱伝導材からなる薄肉の筒を
同軸状に配置したことを特徴とするクライオスタット。(1) A refrigerant container that accommodates a cryogenic refrigerant, a vacuum container that covers the refrigerant container and forms a vacuum insulation layer between it and the refrigerant container, one end of which communicates with the refrigerant container and the other end of which is connected to the vacuum A cryostat comprising a heat insulating layer and a pipe that penetrates the wall of a vacuum container and is located in a room temperature region, characterized in that a thin-walled cylinder made of a low thermal conductive material is coaxially disposed within the pipe.
を特徴とする請求項(1)記載のクライオスタット。(2) The cryostat according to claim (1), wherein the tubes in the pipe are a plurality of coaxial tubes having different diameters.
が異なるように配置されたことを特徴とする請求項(1
)記載のクライオスタット。(3) Claim (1) characterized in that the number of tubes is arranged to be different between the low temperature side and the normal temperature side of the pipe.
) Cryostat described.
断面と相似形の断面を持つ仕切り板を同軸状に配置した
ものであることを特徴とする請求項(1)記載のクライ
オスタット。(4) The cryostat according to claim 1, wherein when the cross section of the pipe is not circular, the tube is formed by coaxially disposing partition plates having a cross section similar to the cross section of the pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2095152A JP2575517B2 (en) | 1990-04-12 | 1990-04-12 | Cryostat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2095152A JP2575517B2 (en) | 1990-04-12 | 1990-04-12 | Cryostat |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03293784A true JPH03293784A (en) | 1991-12-25 |
| JP2575517B2 JP2575517B2 (en) | 1997-01-29 |
Family
ID=14129821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2095152A Expired - Fee Related JP2575517B2 (en) | 1990-04-12 | 1990-04-12 | Cryostat |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2575517B2 (en) |
-
1990
- 1990-04-12 JP JP2095152A patent/JP2575517B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2575517B2 (en) | 1997-01-29 |
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