JPH0159201B2 - - Google Patents
Info
- Publication number
- JPH0159201B2 JPH0159201B2 JP60206293A JP20629385A JPH0159201B2 JP H0159201 B2 JPH0159201 B2 JP H0159201B2 JP 60206293 A JP60206293 A JP 60206293A JP 20629385 A JP20629385 A JP 20629385A JP H0159201 B2 JPH0159201 B2 JP H0159201B2
- Authority
- JP
- Japan
- Prior art keywords
- metal hydride
- container
- pressure
- hydrogen
- holding container
- 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
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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)
- Hydrogen, Water And Hydrids (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Description
【発明の詳細な説明】
(イ) 産業上の利用分野
本発明は金属水素化物を利用した水素貯蔵装置
や熱利用装置等に使用される金属水素化物容器に
関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a metal hydride container used in hydrogen storage devices, heat utilization devices, etc. that utilize metal hydrides.
(ロ) 従来の技術
ある種の合金(あるいは金属単体)は活性化状
態において、温度、圧力をコントロールすること
により、大量の水素ガスと熱を吸放出することが
知られている。そのときの温度、圧力条件は活性
状態ではそれ程厳しい条件(大きな値)は必要な
い。しかし、不活性状態からそのような活性状態
にもつていくにはかなり厳しい条件が必要とな
る。例えば、FeTiの場合、活性化後の温度は室
温から40℃までの範囲、水素圧力は10atm以下で
反応を行なわせることができる。しかし、その合
金の活性化には温度が400℃以上、水素圧力
40atm以上もの条件が必要となる。(b) Prior Art It is known that certain alloys (or metals) absorb and release large amounts of hydrogen gas and heat in an activated state by controlling temperature and pressure. The temperature and pressure conditions at that time do not need to be so severe (large values) in the active state. However, to go from an inactive state to such an active state requires quite severe conditions. For example, in the case of FeTi, the reaction can be carried out at a temperature in the range from room temperature to 40°C after activation and at a hydrogen pressure of 10 atm or less. However, the activation of the alloy requires temperatures above 400℃ and hydrogen pressure.
Conditions of 40 atm or more are required.
なお、活性化後の金属(合金)は水素の吸収、
放出で金属(合金)と金属水素化物の状態間を行
き来することになるが、これらの状態を全て含め
て以後の記載ではさしつかえない範囲で金属水素
化物と記す。 In addition, the metal (alloy) after activation absorbs hydrogen,
Due to release, the metal (alloy) and metal hydride state will be changed back and forth, but in the following description, all of these states will be referred to as metal hydride to the extent that it does not cause any problem.
従来、これらの金属水素化物を収納して水素の
吸収、放出反応を行なわせる金属水素化物容器に
おいては、活性化した金属水素化物を空気に触れ
させないで容器に出し入れすることが困難なこと
から、活性化も同じ容器内にて行なつていた。こ
のため、容器構造を活性化条件にも耐え得るよう
に設計しなければならず、活性化後の使用には必
要がない大きな肉厚や高価な材質を使わざるを得
なかつた。また、容器内の金属水素化物が不純物
ガス等の原因により劣化し、再生操作のため交換
が必要となつた場合、金属水素化物だけを交換す
ることができず、高価な耐圧容器を伴つて交換し
なければならなかつた。 Conventionally, in metal hydride containers that house these metal hydrides and perform hydrogen absorption and desorption reactions, it is difficult to take the activated metal hydride in and out of the container without exposing it to air. Activation was also performed in the same container. For this reason, the container structure must be designed to withstand the activation conditions, necessitating the use of large wall thicknesses and expensive materials that are unnecessary for use after activation. In addition, if the metal hydride in the container deteriorates due to impurity gas or other causes and needs to be replaced for regeneration operation, it is not possible to replace just the metal hydride, and an expensive pressure-resistant container is required for replacement. I had to.
更には、システムの運転モードを変えるため、
容器に充填している金属水素化物の種類を変えた
い場合にも、高価な耐圧容器を伴つて交換しなけ
ればならないなどといつた問題点があつた。 Furthermore, in order to change the operating mode of the system,
Even when it was desired to change the type of metal hydride filled in the container, there were problems such as having to replace the container with an expensive pressure-resistant container.
(ハ) 発明が解決しようとする問題点
本発明は、上記の問題点を解決し、容器構造を
通常の活性化状態で必要な条件に耐えられるだけ
の安価な構成になし得ると共に、容器の再使用を
可能にして中の金属水素化物を自由に交換できる
金属水素化物容器を提供することを目的とする。(c) Problems to be Solved by the Invention The present invention solves the above-mentioned problems, makes it possible to make the container structure inexpensive enough to withstand the necessary conditions in a normal activated state, and to improve the container structure. It is an object of the present invention to provide a metal hydride container that can be reused and the metal hydride inside can be freely exchanged.
(ニ) 問題点を解決するための手段
このため、本発明は開閉弁を有する水素出入導
管を備えた密閉耐圧容器の内部に、内部の圧力が
外部より高くなると開く逆止弁を有する水素出入
導管と、内部の圧力が外部より低くなると開く逆
止弁を有する水素出入導管とを備えた金属水素化
物保持容器を収納し、この保持容器に金属水素化
物を充填するようにしたことを特徴としている。(d) Means for Solving the Problems For this reason, the present invention provides a hydrogen inlet/outlet conduit having a check valve that opens when the internal pressure becomes higher than the outside pressure inside a sealed pressure vessel equipped with a hydrogen inlet/outlet conduit having an on-off valve. A metal hydride holding container equipped with a conduit and a hydrogen inlet/output pipe having a check valve that opens when the internal pressure is lower than the outside pressure is housed, and the holding container is filled with metal hydride. There is.
(ホ) 作用
逆止弁付の金属水素化物保持容器に金属水素化
物を形成する合金を充填し、予め金属水素化物保
持容器を合金の反応初期の活性化に必要な水素圧
力、温度に耐える活性化用の別途圧力容器で合金
を活性化させる。その圧力容器および金属水素化
物保持容器内の水素圧力を大気圧とほぼ同程度に
した後、金属水素化物保持容器を空気中に取り出
す。このとき、逆止弁の作用により金属水素化物
保持容器中への空気の流入がないため、活性化し
た金属水素化物が空気により酸化されたり、不活
性化されることはない。次いこの容器は、活性化
後の水素吸収、放出反応に必要な水素圧力、温度
に耐えるだけの耐圧容器に収納すればよく、金属
水素化物保持容器内の金属水素化物を比較的緩や
かな条件で水素吸収、放出を行なわせることがで
きる。(e) Action: A metal hydride holding container equipped with a check valve is filled with an alloy that forms metal hydrides, and the metal hydride holding container is preliminarily heated to withstand the hydrogen pressure and temperature necessary for activation of the alloy at the initial stage of the reaction. Activate the alloy in a separate pressure vessel. After the hydrogen pressure in the pressure vessel and the metal hydride holding vessel is brought to approximately the same level as atmospheric pressure, the metal hydride holding vessel is taken out into the air. At this time, since air does not flow into the metal hydride holding container due to the action of the check valve, the activated metal hydride will not be oxidized or inactivated by air. Next, this container can be stored in a pressure-resistant container that can withstand the hydrogen pressure and temperature required for the hydrogen absorption and release reaction after activation, and the metal hydride in the metal hydride holding container can be stored under relatively mild conditions. can absorb and release hydrogen.
(ヘ) 実施例
以下、本発明の実施例を図面を参照して説明す
る。(f) Examples Examples 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る金属水素化物
容器の構成図で、同図aはその断面図、同図bは
そのA−A矢視断面図である。これらの図におい
て、本実施例の金属水素化物容器は、耐圧容器本
体1に金属水素化物2を充填した金属水素化物保
持容器3を収納した上、水素出入導管4の付いた
容器蓋体5を耐圧容器本体1上部にフランジ接合
により取り付けて内部を密封して成る。水素出入
導管4には容器内部に水素ガスを出し入れするた
めの開閉弁6が設けられる。 FIG. 1 is a block diagram of a metal hydride container according to an embodiment of the present invention, in which FIG. 1A is a sectional view thereof, and FIG. In these figures, the metal hydride container of this embodiment houses a metal hydride holding container 3 filled with a metal hydride 2 in a pressure-resistant container body 1, and also has a container lid 5 with a hydrogen inlet/output conduit 4. It is attached to the upper part of the pressure vessel main body 1 by flange connection and the inside is sealed. The hydrogen inlet/outlet conduit 4 is provided with an on-off valve 6 for letting hydrogen gas in and out of the container.
金属水素化物保持容器3は各々に逆止弁7,8
を有する2本の水素出入導管9,10が取り付け
られた容器で構成され、内部に金属水素化物2が
充填される。その逆止弁7は金属水素化物保持容
器3内の水素圧力が外部より高くなつたときに開
き、逆止弁8は金属水素化物保持容器内の水素圧
力が外部より低くなつたときに開くように設定さ
れる。逆止弁7,8としては例えばばね式のもの
が使用できる。この場合、逆止弁を開くには一定
圧力以上の差圧が必要となるが、この差圧は
0.5atm程度にすると良い。 The metal hydride holding container 3 is provided with check valves 7 and 8, respectively.
It consists of a container to which two hydrogen inlet and outlet conduits 9 and 10 are attached, and the metal hydride 2 is filled inside. The check valve 7 opens when the hydrogen pressure inside the metal hydride holding container 3 becomes higher than the outside, and the check valve 8 opens when the hydrogen pressure inside the metal hydride holding container becomes lower than the outside. is set to For example, spring type check valves can be used as the check valves 7 and 8. In this case, a pressure difference greater than a certain pressure is required to open the check valve, but this pressure difference is
It is best to set it to around 0.5 atm.
この金属水素化物保持容器3に活性化前の合金
例えばFeTi合金を充填した上、その合金の活性
化条件に耐え得る別途容器(図示省略)に収容し
て活性化処理を行なう。即ち、耐圧容器本体1に
金属水素化物保持容器3を入れ、容器内を温度
400℃以上、水素圧力40atm以上に保つ。すると、
金属水素化物保持容器3内も、逆止弁7,8を介
して水素ガスの出し入れが行なわれる結果、耐圧
容器内とほぼ同じ条件になる。これにより、金属
水素化物保持容器3内に充填された金属水素化
物、この場合FeTi合金の活性化が行なわれる。 This metal hydride holding container 3 is filled with an alloy before activation, such as an FeTi alloy, and then placed in a separate container (not shown) that can withstand the activation conditions of the alloy, and then subjected to activation treatment. That is, the metal hydride holding container 3 is placed in the pressure-resistant container body 1, and the temperature inside the container is maintained.
Keep above 400℃ and hydrogen pressure above 40atm. Then,
Hydrogen gas is taken in and out of the metal hydride holding container 3 through the check valves 7 and 8, so that the conditions are almost the same as in the pressure container. As a result, the metal hydride filled in the metal hydride holding container 3, in this case the FeTi alloy, is activated.
金属水素化物2の活性化が完了した金属水素化
物保持容器3を内部水素圧力をほぼ大気圧に調節
したのち、耐圧容器本体1から取り出す。このと
き、金属水素化物保持容器3の水素出入導管9,
10に設けられる逆止弁7,8を開くには一定圧
力以上の差圧が必要となる。従つて、空気圧およ
び金属水素化物保持容器3内の水素圧力に若干の
圧力変動があつても、金属水素化物保持容器3内
を閉鎖し続けることができる。これにより、金属
水素化物保持容器3を空気中に取り出しても、金
属水素化物2は外部の空気と接触することなく、
安定して活性状態を保つことができる。 The metal hydride holding container 3 in which the metal hydride 2 has been activated is taken out from the pressure container body 1 after adjusting the internal hydrogen pressure to approximately atmospheric pressure. At this time, the hydrogen inlet/output pipe 9 of the metal hydride holding container 3,
In order to open the check valves 7 and 8 provided in the valve 10, a pressure difference greater than a certain pressure is required. Therefore, even if there are slight pressure fluctuations in the air pressure and the hydrogen pressure inside the metal hydride holding container 3, the inside of the metal hydride holding container 3 can be kept closed. As a result, even if the metal hydride holding container 3 is taken out into the air, the metal hydride 2 will not come into contact with the outside air.
It can remain stable and active.
この金属水素化物保持容器3を耐圧容器本体1
内に収納し、開閉弁6を有する水素出入導管4を
具備した蓋体5をフランジ接合により取り付け、
内部を密閉する。次いで、水素出入導管4より水
素ガスを導入、排気し、金属水素化物2の水素吸
収、放出反応を行なわせる。このとき、金属水素
化物2は既に活性化処理が終つているため、活性
化前と比べてはるかに緩やかな条件で水素吸収、
放出反応を行なわせることができる。 This metal hydride holding container 3 is connected to the pressure container main body 1.
A lid body 5 equipped with a hydrogen inlet/outlet conduit 4 having an on-off valve 6 is attached by flange joining,
Seal the inside. Next, hydrogen gas is introduced and exhausted from the hydrogen inlet/output pipe 4 to cause the metal hydride 2 to undergo hydrogen absorption and release reactions. At this time, since the metal hydride 2 has already undergone the activation process, it absorbs hydrogen under much gentler conditions than before activation.
A release reaction can take place.
この結果、耐圧容器本体1および蓋体5は、こ
の活性化状態下での温度、圧力条件に耐え得る材
質、構造のもので良くなり、材質としては、
SUS316、SUS304のステンレスあるいは銅、ア
ルミ等幅広い材料の選択が可能となり、また、容
器肉厚も大幅に低減することができる。更に、耐
圧容器本体1と蓋体5の接合部にはバイトン、テ
フロン、シリコン等の材質を用いてパツキングす
るなど、比較的簡単な密閉構造を採用することが
可能となる。 As a result, the pressure-resistant container main body 1 and the lid 5 can be made of materials and structures that can withstand the temperature and pressure conditions under this activation state.
A wide range of materials can be selected, including stainless steel (SUS316 and SUS304), copper, and aluminum, and the container wall thickness can also be significantly reduced. Furthermore, it is possible to employ a relatively simple hermetic structure, such as packing the joint between the pressure-resistant container body 1 and the lid 5 using a material such as Viton, Teflon, or silicone.
またこのとき、金属水素化物保持容器3も差圧
0.5atm程度に耐えればよいので、耐圧構造にす
る必要はなく、極く簡単な密閉容器構造とすれば
よい。 At this time, the metal hydride holding container 3 also has a differential pressure.
Since it only needs to withstand about 0.5 atm, it is not necessary to have a pressure-resistant structure, and an extremely simple closed container structure is sufficient.
従つて、容器の製作、使用上の法規の点でも、
10Kg/cm2以下の圧力で使用できることから、高圧
ガス取締法の適用範囲外となり、設置場所等に制
限されることなく、誰でも容易かつ安全に取り扱
うことができるようになる。 Therefore, in terms of regulations regarding the manufacture and use of containers,
Since it can be used at a pressure of 10 kg/cm 2 or less, it is outside the scope of the High Pressure Gas Control Law, and anyone can easily and safely handle it without being restricted by installation location.
尚、本発明の金属水素化物容器の構造は上記実
施例に示した構造のみに限らず、特許請求の範囲
の記述を逸脱しない範囲で種々の変更が可能であ
る。 Incidentally, the structure of the metal hydride container of the present invention is not limited to the structure shown in the above embodiments, and various changes can be made without departing from the scope of the claims.
例えば、第2図に示すように、耐圧容器の蓋体
5から金属水素化物保持容器3を気密に貫通して
金属水素化物保持容器3内部に熱媒管路11を設
けるようにしても良く、このようにした場合に
は、金属水素化物2の加熱冷却を行なつて水素吸
収、放出反応を効率良く促進させることができる
ようになる。 For example, as shown in FIG. 2, a heat medium pipe 11 may be provided inside the metal hydride holding container 3 by airtightly penetrating the metal hydride holding container 3 from the lid 5 of the pressure container. In this case, the metal hydride 2 can be heated and cooled to efficiently promote hydrogen absorption and release reactions.
また、第3図に示すように、金属水素化物2の
内部上面に水素は通すが金属水素化物は通さない
円板状のフイルタ12を配設することにより、金
属水素化物2の金属水素化物保持容器3外への飛
散を防止することができる。 In addition, as shown in FIG. 3, by disposing a disk-shaped filter 12 on the inner upper surface of the metal hydride 2 that allows hydrogen to pass through but not the metal hydride, the metal hydride of the metal hydride 2 can be retained. Scattering outside the container 3 can be prevented.
また、このフイルタは、第4図に示すように、
円筒状に形成し、この円筒状フイルタ13,14
をそれぞれ水素出入導管9,10に接続して金属
水素化物保持容器3の内部金属水素化物2内に深
く配設するようにしても良い。そのようにした場
合には、金属水素化物2の飛散防止と共に、金属
水素化物2と水素ガスとの接触をよりし易くして
水素吸収、放出反応を効率良く行なわせることが
できるようになる。 In addition, this filter, as shown in Figure 4,
The cylindrical filters 13 and 14 are formed into a cylindrical shape.
may be connected to the hydrogen inlet/output conduits 9 and 10, respectively, and disposed deeply within the internal metal hydride 2 of the metal hydride holding container 3. In this case, it is possible to prevent the metal hydride 2 from scattering, and to make it easier for the metal hydride 2 to come into contact with hydrogen gas, so that the hydrogen absorption and release reactions can be carried out efficiently.
(ト) 発明の効果
以上説明したように本発明によれば、以下の効
果が得られる。(g) Effects of the invention As explained above, according to the present invention, the following effects can be obtained.
(1) 金属水素化物の活性化を別途耐圧容器で行な
えるため、耐圧容器は活性化後の水素吸収、放
出反応に必要な緩やかな温度、圧力条件に耐え
得れば良くなる結果、幅広い容器材料の選択
と、容器肉厚の低減化が可能となり、耐圧容器
を安価に製作できるようになる。(1) Activation of metal hydrides can be performed in a separate pressure-resistant container, so the pressure-resistant container only needs to withstand the gentle temperature and pressure conditions required for hydrogen absorption and release reactions after activation.As a result, a wide range of containers can be used. It becomes possible to select materials and reduce the container wall thickness, making it possible to manufacture pressure-resistant containers at low cost.
(2) これまで、水素吸収、放出に優れ安価に入手
できるにも拘わらず、活性化が困難なため使用
されていなかつた、FeTi等の合金の使用が容
易となるなど、使用する金属の選択範囲が広が
る。(2) Selection of the metal to be used, such as the ease of using alloys such as FeTi, which had not been used until now because they were difficult to activate despite being excellent in hydrogen absorption and release and available at low cost. The range expands.
(3) 金属水素化物容器内の金属水素化物が万一劣
化等により再生処理あるいは交換が必要となつ
た場合も耐圧容器の交換を伴わずに、金属水素
化物保持容器だけを取り出して交換することが
できる。また、このように金属水素化物保持容
器を空気中に取り出しても金属水素化物は一切
空気と接触するおそれがない。従つて、金属水
素化物だけを経済的かつ安全に交換することが
でき、メンテナンスが極めて簡単になる。(3) In the unlikely event that the metal hydride in the metal hydride container needs to be recycled or replaced due to deterioration, etc., only the metal hydride holding container should be removed and replaced without replacing the pressure container. Can be done. Further, even if the metal hydride holding container is taken out into the air in this way, there is no risk that the metal hydride will come into contact with the air. Therefore, only the metal hydride can be replaced economically and safely, making maintenance extremely simple.
(4) 金属水素化物容器を使用した熱利用システム
等において、その運転モードを変えるため金属
水素化物の種類を変える必要が生じた場合も、
耐圧容器を伴う交換を必要としないため、経済
的にして交換作業も極めて容易となる。(4) When it becomes necessary to change the type of metal hydride in order to change the operation mode of a heat utilization system using a metal hydride container,
Since there is no need to replace a pressure-resistant container, the replacement work is economical and extremely easy.
第1図〜第4図は本発明の各実施例を示す金属
水素化物容器の構成図を示し、各図を通じてaは
縦断面図、bは横断面図である。
1……耐圧容器本体、2……金属水素化物、3
……金属水素化物保持容器、4,9,10……水
素出入導管、5……蓋体、6……開閉弁、7,8
……逆止弁、11……熱媒管路、12……フイル
タ、13,14……円筒状フイルタ。
1 to 4 show configuration diagrams of metal hydride containers showing respective embodiments of the present invention, and in each figure, a is a vertical sectional view, and b is a horizontal sectional view. 1...Pressure vessel main body, 2...Metal hydride, 3
...Metal hydride holding container, 4,9,10...Hydrogen inlet/output conduit, 5...Lid, 6...Opening/closing valve, 7,8
... Check valve, 11 ... Heat medium pipe, 12 ... Filter, 13, 14 ... Cylindrical filter.
Claims (1)
密閉構造に形成された耐圧容器と、この耐圧容器
内部に収納され、内部の圧力が外部より高くなる
と開く逆止弁を有する水素出入導管と、内部の圧
力が外部より低くなると開く逆止弁を有する水素
出入導管とを備え、内部に金属水素化物を収納し
て密閉構造に形成された金属水素化物保持容器と
からなることを特徴とする金属水素化物容器。 2 特許請求の範囲第1項記載において、前記耐
圧容器から金属水素化物保持容器を気密に貫通し
てその保持容器内部に熱媒管路を配設したことを
特徴とする金属水素化物容器。 3 特許請求の範囲第1項記載において、前記金
属水素化物保持容器内部に水素は通すが金属水素
化物は通し得ないフイルタを配設したことを特徴
とする金属水素化物容器。[Scope of Claims] 1. A pressure-resistant container having a closed structure inside and equipped with a hydrogen inlet/output conduit having an on-off valve, and a check valve that is housed inside the pressure-resistant container and opens when the internal pressure becomes higher than the outside pressure. a hydrogen inlet/outlet conduit with a check valve that opens when the internal pressure is lower than the outside pressure, and a metal hydride holding container that stores a metal hydride inside and has a sealed structure. A metal hydride container characterized by: 2. A metal hydride container according to claim 1, characterized in that a heat medium pipe is provided inside the metal hydride holding container by airtightly penetrating the metal hydride holding container from the pressure-resistant container. 3. The metal hydride container according to claim 1, characterized in that a filter is disposed inside the metal hydride holding container to allow hydrogen to pass through but not to allow metal hydride to pass through.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60206293A JPS6267399A (en) | 1985-09-20 | 1985-09-20 | Vessel for metal hydride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60206293A JPS6267399A (en) | 1985-09-20 | 1985-09-20 | Vessel for metal hydride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6267399A JPS6267399A (en) | 1987-03-27 |
| JPH0159201B2 true JPH0159201B2 (en) | 1989-12-15 |
Family
ID=16520902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60206293A Granted JPS6267399A (en) | 1985-09-20 | 1985-09-20 | Vessel for metal hydride |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6267399A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008133834A (en) * | 2005-03-01 | 2008-06-12 | Taiheiyo Cement Corp | Hydrogen storage device and hydrogen storage method |
-
1985
- 1985-09-20 JP JP60206293A patent/JPS6267399A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6267399A (en) | 1987-03-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |