JPH0652119B2 - Mass activation method of metal hydride - Google Patents
Mass activation method of metal hydrideInfo
- Publication number
- JPH0652119B2 JPH0652119B2 JP61196442A JP19644286A JPH0652119B2 JP H0652119 B2 JPH0652119 B2 JP H0652119B2 JP 61196442 A JP61196442 A JP 61196442A JP 19644286 A JP19644286 A JP 19644286A JP H0652119 B2 JPH0652119 B2 JP H0652119B2
- Authority
- JP
- Japan
- Prior art keywords
- metal hydride
- hydrogen
- pressure
- container
- reactor
- 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 - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C11/00—Use of gas-solvents or gas-sorbents in vessels
- F17C11/005—Use of gas-solvents or gas-sorbents in vessels for hydrogen
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、金属水素化物の大量活性化方法に関する。TECHNICAL FIELD OF THE INVENTION The present invention relates to a method for mass activation of metal hydrides.
従来の技術 ある種の金属や合金が発熱的に水素を吸蔵して金属水素
化物を形成し、また、この金属水素化物が可逆的に吸熱
的に水素を放出することが知られている。近年、これら
金属水素化物の特性を利用した種々の装置が提案され、
また、一部では実用化されている。このような装置とし
て、例えば、金属水素化物が水素を大量に吸蔵し得る性
質を利用した水素貯蔵装置や輸送装置、金属水素化物が
水素を選択的に吸蔵する性質を利用した水素精製装置、
金属水素化物が水素を吸蔵放出する際に発熱吸熱するこ
とを利用したヒートポンプや蓄熱装置、金属水素化物が
一定温度で一定の水素平衡圧を有する性質を利用した温
度センサやアクチユエータ等を挙げることができる。2. Description of the Related Art It is known that a certain kind of metal or alloy exothermically absorbs hydrogen to form a metal hydride, and this metal hydride reversibly endothermally releases hydrogen. In recent years, various devices utilizing the characteristics of these metal hydrides have been proposed,
In addition, it has been put to practical use in some cases. As such a device, for example, a hydrogen storage device or a transportation device that uses the property that a metal hydride can store a large amount of hydrogen, a hydrogen purification device that uses the property that a metal hydride selectively stores hydrogen,
Examples include heat pumps and heat storage devices that utilize heat absorption and absorption when metal hydride absorbs and releases hydrogen, temperature sensors and actuators that utilize the property that metal hydride has a constant hydrogen equilibrium pressure at a constant temperature. it can.
上記のような種々の装置においては、その目的に応じた
構造や形態を有する反応器に一定量の金属水素化物を充
填した後、金属水素化物を活性化するか、又は所要の装
置に組み込んだ後、それぞれの反応器について個別的に
活性化する方法が採用されており、従来、多数の反応器
に充填された金属水素化物を同時に大量に活性化する方
法は知られていない。従つて、装置が多数の反応器を含
んで、大型になればなるほど、個々の反応器に充填され
た金属水素化物の活性化に長時間を要し、処理費用が高
価とならざるを得なかつた。In the various devices as described above, after a certain amount of metal hydride is charged into a reactor having a structure or form suitable for the purpose, the metal hydride is activated or incorporated into a required device. After that, a method of individually activating each reactor is adopted, and conventionally, a method of simultaneously activating a large amount of metal hydrides charged in a large number of reactors has not been known. Therefore, the larger the apparatus including a large number of reactors, the longer the activation time of the metal hydride charged in each reactor, and the more expensive the processing cost. It was
発明が解決しようとする問題点 本発明は、容器に充填された金属水素化物の活性化にお
ける上記した問題を解決するためになされたものであつ
て、多数の容器中の金属水素化物を同時に且つ大量に一
括して活性化する方法を提供することを目的とする。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The present invention has been made to solve the above-mentioned problems in activation of a metal hydride filled in a container, in which metal hydrides in a plurality of containers are simultaneously and It is an object to provide a method for activating a large amount in a batch.
問題点を解決するための手段 本発明による金属水素化物の大量活性化方法は、開口を
有する複数の容器に金属水素化物を充填し、これら容器
を一括して耐圧容器内に置いて、同時に金属水素化物を
活性化することを特徴とする。Means for Solving the Problems In the method for activating large amounts of metal hydride according to the present invention, a plurality of containers having openings are filled with metal hydride, and these containers are collectively placed in a pressure resistant container, and at the same time metal It is characterized by activating a hydride.
以下、第1図に基づいて、本発明の方法を詳細に説明す
る。Hereinafter, the method of the present invention will be described in detail with reference to FIG.
本発明の方法は、水素出入口としての開口1を有する多
数の容器2内にそれぞれ金属水素化物3を充填し、これ
らを一括して耐圧容器4内に収容し、多数の容器内の金
属水素化物を同時に活性化するものである。上記耐圧容
器には、適宜の真空装置(図示せず)に接続されている
真空排気管5、耐圧容器内への水素の充填のための導入
管6及び排気のための排気管7が配設され、更に、耐圧
容器を加熱し、又は冷却するために、耐圧容器の周囲に
熱媒又は冷媒のための加熱冷却管8が配設されている。According to the method of the present invention, a large number of containers 2 each having an opening 1 serving as a hydrogen inlet / outlet are filled with a metal hydride 3 respectively, and these are collectively housed in a pressure-resistant container 4, and the metal hydrides in a large number of containers are filled. Are activated at the same time. The pressure-resistant container is provided with a vacuum exhaust pipe 5 connected to an appropriate vacuum device (not shown), an inlet pipe 6 for filling hydrogen into the pressure-resistant container, and an exhaust pipe 7 for exhaust. Further, in order to heat or cool the pressure resistant container, a heating / cooling pipe 8 for a heat medium or a refrigerant is arranged around the pressure resistant container.
本発明の方法においては、金属水素化物の活性化には、
第1に耐圧容器内を真空とした後、水素を導入し、加圧
する方法、第2の耐圧容器内を加熱しつつ真空とし、こ
の後、水素を導入し、加圧する方法、及び第3に耐圧容
器内に水素を導入し、加圧し、この後、水素を排出する
ことを繰り返す方法等を採用することができる。In the method of the present invention, activation of the metal hydride includes
Firstly, a method of introducing hydrogen into the pressure vessel after applying a vacuum and then pressurizing it, making a vacuum in the second pressure vessel while heating, and then introducing and pressurizing hydrogen, and thirdly A method of introducing hydrogen into the pressure vessel, pressurizing it, and then discharging hydrogen repeatedly can be adopted.
第1の方法によるときは、真空排気管によつて耐圧容器
内を真空とした後、水素を10kg/cm2又は数十kg/cm2程
度まで加圧導入した後、一定時間放置する操作を繰り返
す。第2の方法によるときは、耐圧容器内を真空とした
後、加熱管に高温熱媒を流通させて、金属水素化物を加
熱し、次いで、好ましくは常温まで冷却した後、耐圧容
器内に上記と同様に水素を加圧導入する。第3の方法に
よれば、耐圧容器内を真空にすることなく、容器内に水
素の加圧導入を繰り返して、耐圧容器内を水素で置換
し、金属水素化物を活性化する。In the case of the first method, after the vacuum vessel is evacuated by the vacuum exhaust pipe, hydrogen is introduced under pressure up to about 10 kg / cm 2 or several tens of kg / cm 2, and then left for a certain period of time. repeat. In the case of the second method, after the pressure vessel is evacuated, a high-temperature heating medium is circulated through the heating tube to heat the metal hydride, and then preferably cooled to room temperature, and then the above-mentioned is placed in the pressure vessel. Similarly to the above, hydrogen is introduced under pressure. According to the third method, without introducing a vacuum inside the pressure vessel, hydrogen is repeatedly introduced into the vessel under pressure to replace the inside of the pressure vessel with hydrogen and activate the metal hydride.
以上のようにして、それぞれの反応器内の金属水素化物
を活性化した後、耐圧容器からこれらを取り出せば、金
属水素化物が活性化された状態で充填されている金属水
素化物反応器を得ることができる。しかし、例えば、反
応器が溶接によつて装置に組み込まれる場合のように、
火気や高温に曝されるときは、水素への引火のおそれが
あるので、耐圧容器内において前述したように個々の容
器内の金属水素化物の活性化を完了した後、耐圧容器を
真空として、金属水素化物を脱水素した後、容器内にア
ルゴンやヘリウム等の不活性気体を導入し、反応器内を
これら不活性気体にて置換して、耐圧容器から取り出す
のが好ましい。After activating the metal hydrides in the respective reactors as described above, if these are taken out from the pressure vessel, a metal hydride reactor filled with the metal hydrides in an activated state is obtained. be able to. But, for example, when the reactor is integrated into the device by welding,
When exposed to fire or high temperature, there is a risk of ignition of hydrogen, so after completing the activation of the metal hydride in each container as described above in the pressure vessel, vacuum the pressure vessel, After dehydrogenating the metal hydride, it is preferable to introduce an inert gas such as argon or helium into the container, replace the inside of the reactor with the inert gas, and take out from the pressure resistant container.
更に、本発明によれば、容器内の金属水素化物に所定量
の水素を吸蔵させた金属水素化物反応器を容易に得るこ
とができる。即ち、容器内の金属水素化物を前述した方
法によつて活性化した後、目的とする水素吸蔵量に相当
する金属水素化物水素平衡圧が大気圧に等しいように、
金属水素化物の温度を設定し、保持する。第2図に金属
水素化物における水素吸蔵量(H/M)と水素平衡圧
(P)との関係を示すが、例えば、A点にて示す量にて
金属水素化物に水素を吸蔵させる場合は、金属水素化物
の温度をA点が大気圧であるように保持すればよい。具
体例で説明すれば、金属水素化物がLaNi5であるとき
は、耐圧容器を約10℃に保持し、水素を大気圧以上の
圧力にて耐圧容器内に加圧導入して、金属水素化物に水
素を吸蔵させた後、水素を耐圧容器から大気圧まで自然
排出させれば、LaNi5はほぼA点に相当する水素を吸蔵
する。Further, according to the present invention, it is possible to easily obtain a metal hydride reactor in which a predetermined amount of hydrogen is stored in the metal hydride in the container. That is, after activating the metal hydride in the container by the method described above, so that the metal hydride hydrogen equilibrium pressure corresponding to the desired hydrogen storage amount is equal to atmospheric pressure,
Set and hold the temperature of the metal hydride. FIG. 2 shows the relationship between the hydrogen storage amount (H / M) in the metal hydride and the hydrogen equilibrium pressure (P). For example, in the case where the metal hydride stores hydrogen in the amount shown at point A, The temperature of the metal hydride may be maintained so that the point A is atmospheric pressure. Explaining in a specific example, when the metal hydride is LaNi 5 , the pressure proof container is maintained at about 10 ° C., and hydrogen is introduced under pressure at a pressure of atmospheric pressure or higher into the pressure proof container to form a metal hydride. If hydrogen is naturally discharged from the pressure-resistant container up to atmospheric pressure after occluding hydrogen in, the LaNi 5 occludes hydrogen corresponding to approximately point A.
以上のようにして、活性化された金属水素化物を内蔵す
る反応器は、耐圧容器から取り出した後、反応器の開口
をかしめ、又はろう付けし、所定の金属水素化物装置に
組み込まれる。As described above, the reactor containing the activated metal hydride is taken out of the pressure vessel, and then the opening of the reactor is caulked or brazed to be incorporated in a predetermined metal hydride device.
発明の効果 以上のように、本発明の方法によれば、多数の容器内に
それぞれ充填された金属水素化物を一挙に大量に活性化
することができ、従来のように、容器ごとにその金属水
素化物を活性化する方法に比べて、活性化の時間及び労
力を顕著に節減することができる。特に、本発明の方法
によれば、金属水素化物を活性化した後、所定量の水素
を吸蔵させた金属水素化物を内蔵した反応器を得ること
ができ、これらはその後、何らの処理や工程も必要とせ
ずに、直ちに所定の金属水素化物装置に組み込むことが
できる。EFFECTS OF THE INVENTION As described above, according to the method of the present invention, it is possible to activate a large amount of metal hydrides respectively filled in a large number of containers at once, and, as in the conventional case, the metal hydrides can be activated for each container. Compared with the method of activating a hydride, the activation time and labor can be significantly reduced. In particular, according to the method of the present invention, after activating the metal hydride, it is possible to obtain a reactor containing a metal hydride in which a predetermined amount of hydrogen has been occluded. Can be immediately incorporated into a given metal hydride device.
更に、本発明の方法によれば、金属水素化物を充填され
た容器は、耐圧容器内で活性化されるので、この活性化
に際しては、容器自体はその内外に圧力差がないので、
金属水素化物の活性化に特に高圧水素を必要とする場合
であつても、容器の壁厚が薄くてよい利点もある。Furthermore, according to the method of the present invention, the container filled with the metal hydride is activated in the pressure-resistant container, and therefore there is no pressure difference between the inside and the outside of the container during this activation.
Even when high-pressure hydrogen is particularly required for activation of the metal hydride, there is an advantage that the wall thickness of the container may be thin.
実施例 以下に本発明の実施例を挙げる。Examples Examples of the present invention will be given below.
実施例1 (水素貯蔵装置の製作における実施) 第3図に示すように、一端を封止した外径19.05mm、長
さ300mmの銅製容器9の内部に外径10mmのセラミツ
クス製多孔質管10を水素流通材として配設し、金属水
素化物としてLaNi4.8Al0.2を160g充填した。このよ
うな容器21本を耐圧容器内に置き、80℃に加熱しな
がら、30分間真空処理した後、水素を10kg/cm2圧ま
で導入し、20℃に冷却し、この後、10時間放置し
た。この後、80℃の温度で30分間真空処理した後、
20℃の温度で水素を10kg/cm2導入し、次いで、30
分間放置する操作を5回繰り返した。Example 1 (Implementation in manufacturing hydrogen storage device) As shown in FIG. 3, a ceramic porous tube 10 having an outer diameter of 10 mm was placed inside a copper container 9 having an outer diameter of 19.05 mm and a length of 300 mm with one end sealed. was arranged as a hydrogen circulation material, a LaNi 4. 8 Al 0. 2 was 160g filled as a metal hydride. Twenty-one such containers are placed in a pressure resistant container, vacuum treated for 30 minutes while heating to 80 ° C, hydrogen is introduced to a pressure of 10 kg / cm 2 and cooled to 20 ° C, and then left for 10 hours. did. Then, after vacuum treatment at a temperature of 80 ° C. for 30 minutes,
Hydrogen was introduced at a temperature of 20 ° C. at 10 kg / cm 2 , and then 30
The operation of leaving for a minute was repeated 5 times.
このようにして、活性化金属水素化物に水素を吸蔵させ
た状態で反応器を耐圧容器から取り出し、反応器21本
を一挙に得ることができた。第4図に示すように、9本
のこれら反応器11をジヨイント12にて水素分岐ヘツ
ダー13に取り付け、反応器を外殻14にて気密的に被
覆して、外殻内を熱媒流路15とする水素貯蔵精製装置
を構成した。In this way, 21 reactors could be obtained all at once by taking out the reactor from the pressure vessel with hydrogen stored in the activated metal hydride. As shown in FIG. 4, nine reactors 11 are attached to the hydrogen branch header 13 with a joint 12 and the reactor is hermetically covered with an outer shell 14 so that the inside of the outer shell has a heat medium flow path. A hydrogen storage and refining apparatus having a capacity of 15 was constructed.
この装置によれば、反応器内の金属水素化物を冷却しな
がら、これに水素を吸蔵させることによつて水素を貯蔵
させることができ、他方、金属水素化物を加熱すれば、
水素を放出させることができる。According to this apparatus, while cooling the metal hydride in the reactor, hydrogen can be stored by storing hydrogen in the reactor, while heating the metal hydride,
Hydrogen can be released.
実施例2 (感温駆動装置の製作における実施) 金属水素化物としてTiCoを充填した開口16を有する容
器17の20本を耐圧容器内に置き、実施例1と同じ方
法で最初の活性化を行なつた後、20℃の温度で水素を
圧力2kg/cm2にて加圧導入して、金属水素化物に水素を
吸蔵させた。次いで、水素を大気圧まで耐圧容器から排
気させた後、反応器を耐圧容器から取り出し、開口16
をかしめ、ろう付けした。Example 2 (Implementation in Fabrication of Temperature Sensitive Drive) Twenty containers 17 having openings 16 filled with TiCo as a metal hydride were placed in a pressure resistant container, and the first activation was performed in the same manner as in Example 1. After that, hydrogen was introduced under pressure at a pressure of 2 kg / cm 2 at a temperature of 20 ° C. to occlude hydrogen in the metal hydride. Next, after evacuating hydrogen from the pressure resistant container to atmospheric pressure, the reactor was taken out of the pressure resistant container and the opening 16
Crimped and brazed.
このようにして得た反応器を温度を検出するための感温
筒として用いて、第5図に示すように伸縮方向の先端に
電気接点18の一方を有するベローズ19に細管20で
連通した。この感温駆動装置によれば、感温筒の感知す
る温度に応じてベローズが伸縮するので、例えば、この
伸縮を利用して、電気接点18の開閉を行なうことがで
きる。The reactor thus obtained was used as a temperature sensing tube for detecting the temperature, and was connected to a bellows 19 having one of the electrical contacts 18 at the end in the expansion / contraction direction by a thin tube 20 as shown in FIG. According to this temperature-sensitive drive device, the bellows expands and contracts according to the temperature sensed by the temperature-sensitive cylinder, so that the expansion and contraction can be utilized to open and close the electrical contact 18, for example.
第1図は本発明の方法を説明するための耐圧容器及び金
属水素化物を充填した多数の容器を示す断面図、第2図
は一般に金属水素化物における水素吸蔵量と水素平衡圧
との関係を示すグラフ、第3図は反応器の一例を示す断
面図、第4図は水素貯蔵装置の一例を示す断面図、第5
図は感温駆動装置の一例を示す断面図である。 1……容器開口、2……容器、3……金属水素化物、4
……耐圧容器、5……真空排気管、6……水素導入管、
7……水素排出管、8……加熱冷却管。FIG. 1 is a cross-sectional view showing a pressure resistant container and a number of containers filled with metal hydride for explaining the method of the present invention, and FIG. 2 generally shows the relationship between hydrogen storage amount and hydrogen equilibrium pressure in metal hydride. The graph which shows, FIG. 3 is sectional drawing which shows an example of a reactor, FIG. 4 is sectional drawing which shows an example of a hydrogen storage device, 5th.
The figure is a cross-sectional view showing an example of the temperature-sensitive drive device. 1 ... container opening, 2 ... container, 3 ... metal hydride, 4
...... Pressure resistant container, 5 ...... vacuum exhaust pipe, 6 ...... hydrogen inlet pipe,
7 ... Hydrogen discharge pipe, 8 ... Heating / cooling pipe.
Claims (1)
充填し、これら容器を耐圧容器内に置いて、同時に金属
水素化物を活性化することを特徴とする金属水素化物の
大量活性化方法。1. A method for mass-activating metal hydride, which comprises filling a plurality of containers having openings with metal hydride, placing the containers in a pressure resistant container, and simultaneously activating the metal hydride. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61196442A JPH0652119B2 (en) | 1986-08-20 | 1986-08-20 | Mass activation method of metal hydride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61196442A JPH0652119B2 (en) | 1986-08-20 | 1986-08-20 | Mass activation method of metal hydride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6353400A JPS6353400A (en) | 1988-03-07 |
| JPH0652119B2 true JPH0652119B2 (en) | 1994-07-06 |
Family
ID=16357891
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61196442A Expired - Lifetime JPH0652119B2 (en) | 1986-08-20 | 1986-08-20 | Mass activation method of metal hydride |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0652119B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000017408A (en) * | 1998-07-03 | 2000-01-18 | Japan Metals & Chem Co Ltd | Apparatus for activating hydrogen storage alloy and method therefor |
| JP4916367B2 (en) * | 2007-04-09 | 2012-04-11 | 株式会社日本製鋼所 | Device for activating hydrogen storage alloy container |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS582201A (en) * | 1981-06-29 | 1983-01-07 | Sekisui Chem Co Ltd | Manufacture of metallic hydride reactor |
-
1986
- 1986-08-20 JP JP61196442A patent/JPH0652119B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6353400A (en) | 1988-03-07 |
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