JPS6181292A - Buoyancy generator - Google Patents
Buoyancy generatorInfo
- Publication number
- JPS6181292A JPS6181292A JP20434084A JP20434084A JPS6181292A JP S6181292 A JPS6181292 A JP S6181292A JP 20434084 A JP20434084 A JP 20434084A JP 20434084 A JP20434084 A JP 20434084A JP S6181292 A JPS6181292 A JP S6181292A
- Authority
- JP
- Japan
- Prior art keywords
- buoyancy
- hydrogen
- hydrogen gas
- chamber
- variable volume
- 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.)
- Pending
Links
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- Engine Equipment That Uses Special Cycles (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】
〔産業上の利用分野〕
本発明は水素吸蔵合金を利用する浮力発生装置に関し、
詳細には上記合金収納部と体積可変室の間で水素を可逆
的に往復させることによって体積可変室の体積を変更し
発生浮力の調節を行なえる様に工夫した浮力発生装置に
関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a buoyancy generating device using a hydrogen storage alloy.
Specifically, the present invention relates to a buoyancy generating device devised to change the volume of the variable volume chamber and adjust the generated buoyancy by reversibly reciprocating hydrogen between the alloy storage section and the variable volume chamber.
水素吸蔵合金は、水素の可逆的放出・吸蔵サイクルの応
用分野が拡大するにつれて益々注目を集める様になって
おシ、これを受けて水素吸蔵合金自体についても更に有
力なものが開発されつつある。そして有望な水素吸蔵合
金の実現は、上記可逆的放出・吸蔵サイクルの応用分野
を一層拡大していく方向に資するものであると期待され
ている。Hydrogen storage alloys are attracting more and more attention as the field of application for reversible hydrogen release and storage cycles expands, and in response to this, even more powerful hydrogen storage alloys themselves are being developed. . The realization of a promising hydrogen storage alloy is expected to contribute to further expanding the fields of application of the above-mentioned reversible release/storage cycle.
水素吸蔵合金を加熱したときに放出される水素ガスを圧
力として利用するという考え方は公知である。しかしこ
の様な応用例としては、例えばタービンを回したシ、ピ
ストンを動かしたシするという風に、熱媒の有する熱エ
ネルギーを機械エネルギーに変換し有効な仕事を行なわ
せるととに限られていた様である。The idea of using hydrogen gas released when a hydrogen storage alloy is heated as pressure is well known. However, such applications are limited to converting the thermal energy of a heating medium into mechanical energy to perform useful work, such as turning a turbine or moving a piston. It seems like it was.
水素ガスの比重は空気や水に比べて小さいものであるか
ら、例えば気球内に充填して浮力を発生させるという利
用形態が知られている。しかしこの場合は注入用水素ガ
スを高圧容器内に圧縮充填しておき、浮力を発生させた
いときには高圧容器内の水素ガスを非可逆的に気球内へ
注入するという方式にならざるを得なかった。従って浮
力の軽減を図ろうとすれば気球内の水素ガスを大気中へ
放出するという手段を採用する他なかった。即ち従来の
気球型浮力発生装置では、水素ガスを常に消費の方向へ
使うものであって不経済であると共に、水素ガスの消失
に伴なって浮力発生の機能を失なうという欠点があシ、
又更に周囲の環境によっては水素の放出が危険であった
シ、時には技術的に不可能な場合すらある。Since the specific gravity of hydrogen gas is smaller than that of air or water, it is known to be used, for example, by filling it in a balloon to generate buoyancy. However, in this case, the hydrogen gas for injection had to be compressed and filled into a high-pressure container, and when it was desired to generate buoyancy, the hydrogen gas in the high-pressure container had to be irreversibly injected into the balloon. . Therefore, the only way to reduce buoyancy was to release the hydrogen gas inside the balloon into the atmosphere. In other words, conventional balloon-type buoyancy generating devices always use hydrogen gas for consumption, which is uneconomical, and they also have the drawback of losing their buoyancy generation function as hydrogen gas disappears. ,
Furthermore, depending on the surrounding environment, releasing hydrogen may be dangerous or even technically impossible.
本発明は上記の如き事情を考慮してなされたものであっ
て、水素ガスを系外に放出するという経済的表無駄或は
危険を伴なわずに、且つ長期間に亘って浮力の発生成は
調節を行なうことが可能である様な浮力発生装置の提供
を目的とするものである。The present invention has been made in consideration of the above circumstances, and it is possible to generate buoyancy over a long period of time without the economical waste or danger of releasing hydrogen gas outside the system. The object of the invention is to provide a buoyancy generating device which can be adjusted.
本発明の浮力発生装置とは、体積可変室に水素ガス導入
排出用配管を接続すると共に、該配管の端末を水素吸蔵
合金の収納された熱交換装置に接続した点に要旨を有す
るものである。The gist of the buoyancy generating device of the present invention is that a hydrogen gas introduction/exhaust pipe is connected to a variable volume chamber, and the end of the pipe is connected to a heat exchange device containing a hydrogen storage alloy. .
本発明では体積可変室と水素吸蔵合金収納室(熱交換装
置)を水素ガス導入排出用配管で接続しているので、水
素ガスは体積可変室と水素吸蔵合金収納室の間?往復す
ることができる。従って水素吸蔵合金収納室に熱媒を与
えてこれを加熱すれば水素吸蔵合金から水素ガスが解離
され、これが体積可変室に入ってとの部屋の体積を増大
し周囲の液体や気体を排除して浮力を発生する。一方水
素吸蔵合金収納室を冷却すれば、上記配管を介して連通
されている体積可変室内の水素ガスが水素吸蔵合金に吸
収されるので、体積可変室の体積が減少し浮力が減少し
更にはなくなってしまう。In the present invention, the variable volume chamber and the hydrogen storage alloy storage chamber (heat exchange device) are connected by a hydrogen gas introduction/exhaust pipe, so hydrogen gas flows between the variable volume chamber and the hydrogen storage alloy storage chamber. You can go back and forth. Therefore, by supplying a heating medium to the hydrogen storage alloy storage chamber and heating it, hydrogen gas will be dissociated from the hydrogen storage alloy, enter the volume variable chamber, increase the volume of the chamber, and eliminate surrounding liquid and gas. to generate buoyancy. On the other hand, if the hydrogen storage alloy storage chamber is cooled, the hydrogen gas in the variable volume chamber communicated via the piping will be absorbed by the hydrogen storage alloy, so the volume of the variable volume chamber will decrease, the buoyancy will decrease, and It's gone.
第1図は代表的な水素吸蔵合金に関するP−T線図であ
って、横軸の左側へ行くにつれて(高温側へ移行するに
つれて)解離圧が高くなっていくことを示している。代
表的合金としてLaNi1を取上げて説明すると、H2
との間には次式で示す様な平衡関係が存在する。FIG. 1 is a P-T diagram of a typical hydrogen storage alloy, showing that the dissociation pressure increases as one moves to the left side of the horizontal axis (as one moves to the high temperature side). Taking LaNi1 as a representative alloy and explaining it, H2
There exists an equilibrium relationship as shown in the following equation.
LaNi5+3H2#LaNfIIHe −(。LaNi5+3H2#LaNfIIHe -(.
LaNi、1の分子量は432.5であるから、今仮に
1kgのLaNi、を用いて(1)式の右方向へ反応を
進行せしめておき、ここでLaNi、、H6を加熱して
(1)式の平衡全左方向へ移動させたとすると、解な可
能な水素ガス量は、理論的に次の様に計算される。Since the molecular weight of LaNi, 1 is 432.5, let's now use 1 kg of LaNi to advance the reaction in the right direction of equation (1), and then heat LaNi, H6 to form (1). Assuming that the equilibrium of the equation is shifted completely to the left, the amount of hydrogen gas that can be solved can be theoretically calculated as follows.
432.5
従って体積が零である体積可変室を、比重が1であって
0℃の水面近傍(水圧を無視し得る状態)に置き、該可
変室内へ155.4Nノの水素ガスを供給すれば155
.4kgfの浮力が発生することになる。尚L a N
i HのP−T線図(第1図)から見ると、大気圧(
1kg/c♂)に打ち勝ってH2をガス化する為には1
3℃以上の熱媒を与えればよいことになる。どの様な合
金を使用するかについては、使用環境温度を参酌しつつ
第1図のグラフを読んで最適のものを選択すればよい。432.5 Therefore, place a variable volume chamber with a volume of zero near the surface of water with a specific gravity of 1 and a temperature of 0°C (in a state where water pressure can be ignored), and supply 155.4 N of hydrogen gas into the variable chamber. Ba155
.. A buoyant force of 4 kgf will be generated. Sho L a N
i From the P-T diagram of H (Figure 1), atmospheric pressure (
1 kg/c♂) in order to overcome this and gasify H2.
This means that it is sufficient to provide a heating medium of 3°C or higher. As for what kind of alloy to use, the most suitable one can be selected by reading the graph in FIG. 1 while taking into account the operating environment temperature.
尚第1図の合金の表示中、Mmはミツシュメタルを表ワ
ス。In addition, in the display of alloys in Figure 1, Mm represents Mitsushi metal.
尚現在開発されている水素吸蔵合金の水素吸蔵量はMg
系を除いて2重量%止まルであル、合金1kg当たシ約
20gまでの水素が吸蔵されている。The hydrogen storage capacity of currently developed hydrogen storage alloys is Mg.
Up to about 20 g of hydrogen per kg of alloy is stored at 2% by weight, excluding the system.
この量は10モルの水素(20÷2=10 )に相当し
体積的には224Nl!(0℃、1気圧)の水素を解離
し得ることになる。従って合金1kgを使用すれば0℃
、1気圧の下で(水面近くで)224kgfの浮力を得
ることができ、装置の自重が仮に100kgであるとす
れば、124kgfの浮力が発生することになる。但し
水面から10m深くなると圧力が1 kg /c♂上昇
するので、例えば水深600mの海面下であれば60
kg/c♂の圧力が作用することになh、Hzガスが0
℃とすれば上記浮力は、 1
海面直下に比へて約韮となるから、本発明の現実的適用
に自たっては、これらの条件を考慮した上で合金の種類
や使用量を決定することが望まれる。This amount corresponds to 10 moles of hydrogen (20÷2=10), and the volume is 224Nl! (0°C, 1 atm) hydrogen can be dissociated. Therefore, if 1 kg of alloy is used, 0℃
, a buoyancy of 224 kgf can be obtained under 1 atm (near the water surface), and if the weight of the device is 100 kg, a buoyancy of 124 kgf will be generated. However, the pressure increases by 1 kg/c♂ when the depth is 10 m below the water surface, so for example, at a depth of 600 m below the sea surface, the pressure increases by 1 kg/c♂.
The pressure of kg/c♂ will be applied h, and the Hz gas will be 0.
℃, the above buoyancy is approximately 1.0% compared to just below the sea level, so for practical application of the present invention, the type and amount of alloy to be used should be determined by taking these conditions into consideration. is desired.
第2図は本発明装置の作動説明図である。体積可変室1
をシリンダ型とし、水素吸蔵合金の収納された熱交換装
置2(以下単に熱交換装置2という)との間には水素ガ
ス導入排出配管(以下単に配管とい5)3が設けられる
。げ)は熱交換装置2に温水を通して水素吸蔵合金を加
熱している状態を示し、熱交換装置2から解離された水
素ガスが体積可変室1に入り、その解離圧が環境圧を超
えるときはピストン4を押上げて体積が膨張する。FIG. 2 is an explanatory diagram of the operation of the device of the present invention. Volume variable chamber 1
is cylinder-shaped, and a hydrogen gas introduction/discharge pipe (hereinafter simply referred to as piping 5) 3 is provided between it and a heat exchanger 2 (hereinafter simply referred to as heat exchanger 2) containing a hydrogen storage alloy. Figure) shows a state in which hot water is passed through the heat exchanger 2 to heat the hydrogen storage alloy, and when hydrogen gas dissociated from the heat exchanger 2 enters the variable volume chamber 1 and its dissociation pressure exceeds the environmental pressure, The volume expands by pushing up the piston 4.
従って浮力が発生する。一方(ロ)は熱交換装置2に冷
却水を通して水素吸蔵合金を冷却している状態を示し体
積可変室1内の水素ガスが配管3を経由して熱交換装置
2に至)、合金に吸蔵される。従ってピストン4は外圧
に服して降下し、体積可変室1の体積が減少して浮力を
失゛なうに至る。体積可変室lはダイヤフラム型やベロ
ーズ型にもできる。Therefore, buoyancy is generated. On the other hand, (b) shows a state in which the hydrogen storage alloy is cooled by passing cooling water through the heat exchange device 2. Hydrogen gas in the variable volume chamber 1 reaches the heat exchange device 2 via the piping 3) and is stored in the alloy. be done. Therefore, the piston 4 descends under the external pressure, the volume of the variable volume chamber 1 decreases, and the piston 4 loses its buoyancy. The variable volume chamber l can also be of a diaphragm type or a bellows type.
第3図は潜水艇や潜水艦における浮力発生装置であって
、潜水艇6が海中へ降下するときは、モータ(或はエン
ジン)5の排熱を系外に放出しておき、浮上したいとき
は図のパルプ8を開いて排熱を熱交換装置2に供給する
。即ち降下時は水素を熱交換装置2内に吸蔵させておく
のでピストン4は降下しておシ浮力は発生しないが、浮
上するときは熱交換装置2内の水素が解離されてピスト
ン4が上昇するので浮力が発生し、浮上を助ける。Figure 3 shows a buoyancy generating device in a submersible or a submarine.When the submersible 6 descends into the sea, the exhaust heat of the motor (or engine) 5 is released outside the system, and when the submersible 6 wants to surface, it The pulp 8 shown in the figure is opened and exhaust heat is supplied to the heat exchange device 2. That is, when descending, hydrogen is stored in the heat exchange device 2, so the piston 4 descends and no buoyancy is generated, but when ascending, the hydrogen in the heat exchange device 2 is dissociated and the piston 4 rises. This creates buoyancy and helps you float.
第4,5図は本発明装置を利用して潜水艇6の制御姿勢
を行なう場合の説明図であシ、まず第4図では潜水艇6
の前後に体積可変室1a、lbを設けている。そして熱
交換装置2との間に夫々独立した配管3a、3bを設け
、各配管3a、3bニハル7’8a、8bを介設してい
る。従ってパルプ8を開放して熱交換装置2に排熱を供
給し、水素ガスを解離させるに当たシ、パルプ8aを開
(バルブ8bを閉)にすると、解離された水素ガスは配
管3aを通して体積可変室1aに入るから、潜水艇6は
頭部側を持上げるととKなる。逆にバルブ8aを閉(バ
ルブ8bを開)にすると、水素ガスは体積可変室1bに
入シ、潜水艇6は尾部側を持上げることになる。又第5
図は正面図で潜水艇6の左右に体積可変室1cyldを
設は夫々に配管3c、3d及びパルプ8c、8dを配設
したものであるから、第4図のものに準じてバルブ操作
を行なえば、潜水艇6の左右への傾動姿勢制御を行なう
ことができる。4 and 5 are explanatory diagrams for controlling the attitude of the submersible 6 using the device of the present invention.
Variable volume chambers 1a and lb are provided before and after. Independent pipes 3a and 3b are provided between the heat exchanger 2 and the pipes 3a and 3b, and Nihars 7'8a and 8b are interposed between the pipes 3a and 3b. Therefore, when the pulp 8a is opened (valve 8b is closed) to supply waste heat to the heat exchanger 2 and dissociate hydrogen gas, the dissociated hydrogen gas passes through the pipe 3a. Since it enters the variable volume chamber 1a, the submersible 6 becomes K when the head side is lifted. Conversely, when the valve 8a is closed (valve 8b is opened), hydrogen gas enters the variable volume chamber 1b, and the tail of the submersible 6 is lifted. Also the fifth
The figure is a front view and shows a variable volume chamber 1cyld on the left and right sides of the submersible 6, with pipes 3c and 3d and pulps 8c and 8d installed respectively, so the valves can be operated in accordance with those in Figure 4. For example, the tilting attitude of the submersible 6 to the left and right can be controlled.
第6図は深海艇9による重量物12の運搬操業例を示す
説明図で、(イ)はハンド部10によって重量物12を
把持しようとする状態であるから、浮力が発生しない様
にバルブ8を閉としている。(ロ)は重量物12の積載
が完了して浮上する状態であるからパルプ8を開とし、
体積可変室1に水素ガスを送って体積を大きく浮力を発
生させている。FIG. 6 is an explanatory diagram showing an example of an operation for transporting a heavy object 12 by the deep-sea boat 9. (A) is a state in which the hand section 10 is about to grasp the heavy object 12, so the valve 8 is is closed. In (b), the loading of the heavy object 12 is completed and it is floating, so the pulp 8 is opened.
Hydrogen gas is sent to the variable volume chamber 1 to increase the volume and generate buoyancy.
尚11はパケットを示す。Note that 11 indicates a packet.
第7図は本発明装置を液体の感温センサーとして利用す
る場合の説明図で、げ)がスイッチONの状態、(0)
がスイッチOFFの状態を示す。即ちピ)ではスイッチ
15がONであるから電源13からの電流がヒータ14
に流れている。しかしこの段階では槽16内の水温がま
だ十分暖まっていない為、熱交換装置2内には水素ガス
が吸蔵された状態に1)、従ってベローズ型の体積可変
室1内には十分な量の水素ガスが入っている訳ではなく
、これらの自重に打勝ち得るほどの浮力は発生しておら
ない。やがて槽16内の水温が上昇してくると、熱交換
装置2から水素ガスが解離されはじめ、体積可変室1に
入って体積を膨張させていく。その結果浮力が発生した
体積可変室1は、ガイド17に沿って上昇し、その頭部
でスイッチ15を持上げスイッチOFFとする。こうし
て通電が停止されると槽16内の水温が再び低下をはじ
め、体積可変室1は水素を失なって収縮し、浮力を失な
って降下することによ)0)の状態に戻ると共に再びス
イッチをONとするので、以下(−r)と(ロ)の間を
往復する。従って第1図に示したP−7曲線から適当な
合金を選択すれば、夫々の解離温度についての精密な感
温センサーとなる。FIG. 7 is an explanatory diagram when the device of the present invention is used as a temperature sensor for liquid.
indicates the switch OFF state. In other words, since the switch 15 is ON in P), the current from the power supply 13 flows to the heater 14.
It is flowing to. However, at this stage, the water temperature in the tank 16 has not yet warmed sufficiently, so hydrogen gas is stored in the heat exchanger 2 (1), and therefore a sufficient amount is stored in the bellows-shaped volume variable chamber 1. Since it does not contain hydrogen gas, it does not generate enough buoyancy to overcome its own weight. When the water temperature in the tank 16 eventually rises, hydrogen gas begins to be dissociated from the heat exchange device 2, enters the variable volume chamber 1, and expands in volume. As a result, the variable volume chamber 1, which has generated buoyancy, rises along the guide 17, and lifts the switch 15 at its head to turn the switch OFF. When the electricity supply is stopped in this way, the water temperature in the tank 16 starts to drop again, and the variable volume chamber 1 loses hydrogen and contracts, loses its buoyancy and descends, returning to the state of 0) and again. Since the switch is turned on, it goes back and forth between (-r) and (b). Therefore, if an appropriate alloy is selected from the P-7 curve shown in FIG. 1, a precise temperature sensor for each dissociation temperature will be obtained.
本発明は上記の如く構成されているので、合金室の温度
を制御することによって水素の解離を調節し、解離され
た水素ガスによる体積膨張の度合いに応じた浮力を得る
ことができる。従って水素ガスを系外に放出するという
無駄や危険を伴わずに、長期に亘って且つ多数回に亘っ
て浮力発生・浮力消失を繰返すことができる様になった
。又単に熱媒の利用のみで浮力の発生を調節できるので
機構的にも簡単であって作動上のトラブルも少なく、極
めて安全・安定・安価な浮力発生装置が提供されること
となった。Since the present invention is configured as described above, by controlling the temperature of the alloy chamber, it is possible to adjust the dissociation of hydrogen and obtain buoyancy depending on the degree of volumetric expansion due to the dissociated hydrogen gas. Therefore, it has become possible to repeat generation and loss of buoyancy over a long period of time and many times without the waste and danger of releasing hydrogen gas out of the system. In addition, since the generation of buoyancy can be adjusted simply by using a heating medium, it is mechanically simple and there are few operational troubles, and an extremely safe, stable, and inexpensive buoyancy generating device has been provided.
第1図は各種水素吸蔵合金のP−T線図、第2図は本発
明装置の原理説明図、第3〜7図は本発明装置の応用例
を示す説明図である。
1・・・体積可変室 2・・・熱交換装置3・・・
配管 4・・・ピストン6・・・潜水艇
8・・・バルブ9・・・深海艇 14・
・・ヒータ第2図
第3図
第4図
第5図FIG. 1 is a P-T diagram of various hydrogen storage alloys, FIG. 2 is an explanatory diagram of the principle of the device of the present invention, and FIGS. 3 to 7 are explanatory diagrams showing application examples of the device of the present invention. 1... Volume variable chamber 2... Heat exchange device 3...
Piping 4...Piston 6...Submersible
8...Valve 9...Deep sea boat 14.
...Heater Fig. 2 Fig. 3 Fig. 4 Fig. 5
Claims (1)
、該水素ガス導入排出用配管の端末を水素吸蔵合金の収
納された熱交換装置に接続してなることを特徴とする浮
力発生装置。A buoyancy generating device characterized in that a hydrogen gas introduction/exhaust pipe is connected to a variable volume chamber, and an end of the hydrogen gas introduction/exhaust pipe is connected to a heat exchange device containing a hydrogen storage alloy.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20434084A JPS6181292A (en) | 1984-09-28 | 1984-09-28 | Buoyancy generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20434084A JPS6181292A (en) | 1984-09-28 | 1984-09-28 | Buoyancy generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6181292A true JPS6181292A (en) | 1986-04-24 |
Family
ID=16488878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20434084A Pending JPS6181292A (en) | 1984-09-28 | 1984-09-28 | Buoyancy generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6181292A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012030637A (en) * | 2010-07-29 | 2012-02-16 | M Hikari Energy Kaihatsu Kenkyusho:Kk | Method of sinking and surfacing heavy load underwater |
| JP2021115965A (en) * | 2020-01-27 | 2021-08-10 | 株式会社Ihi | Buoyancy generating device |
-
1984
- 1984-09-28 JP JP20434084A patent/JPS6181292A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012030637A (en) * | 2010-07-29 | 2012-02-16 | M Hikari Energy Kaihatsu Kenkyusho:Kk | Method of sinking and surfacing heavy load underwater |
| JP2021115965A (en) * | 2020-01-27 | 2021-08-10 | 株式会社Ihi | Buoyancy generating device |
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