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JPH0610567B2 - Heat pump device - Google Patents
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JPH0610567B2 - Heat pump device - Google Patents

Heat pump device

Info

Publication number
JPH0610567B2
JPH0610567B2 JP28958485A JP28958485A JPH0610567B2 JP H0610567 B2 JPH0610567 B2 JP H0610567B2 JP 28958485 A JP28958485 A JP 28958485A JP 28958485 A JP28958485 A JP 28958485A JP H0610567 B2 JPH0610567 B2 JP H0610567B2
Authority
JP
Japan
Prior art keywords
hydrogen
temperature heat
medium chamber
conduit
rotary shaft
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
Application number
JP28958485A
Other languages
Japanese (ja)
Other versions
JPS62147266A (en
Inventor
純 石浜
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering Co 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP28958485A priority Critical patent/JPH0610567B2/en
Publication of JPS62147266A publication Critical patent/JPS62147266A/en
Publication of JPH0610567B2 publication Critical patent/JPH0610567B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〈産業上の利用分野〉 この発明は、金属水素化物を利用したヒートポンプ装置
に関するものである。
TECHNICAL FIELD The present invention relates to a heat pump device using a metal hydride.

〈従来の技術〉 希土類,チタン,マグネシウム、その他の金属をベース
とした水素貯蔵(吸蔵)合金又はメタルハイドライド
(Metal Hydride)と呼ばれている金属水素化物が、水
素化反応を起して速やかに発熱的に水素を吸蔵し、また
この金属水素化物が可逆的に脱水素化反応を起して吸熱
的に水素を放出することが知られている。
<Prior Art> A metal hydride called a hydrogen storage (occlusion) alloy or metal hydride (Metal Hydride) based on rare earths, titanium, magnesium, and other metals rapidly initiates a hydrogenation reaction. It is known that hydrogen is exothermically occluded and that the metal hydride reversibly causes a dehydrogenation reaction to endothermically release hydrogen.

この化学反応式は次式によって示される。This chemical reaction formula is shown by the following formula.

M+n/2HMH+ΔH M:水素貯(吸)蔵合金 ΔH:反応熱 MH:金属水素化物 しかしながら一旦水素化反応が起り金属水素化物となる
と、完全にもとの合金の状態に戻すことは非常に困難な
ことから次式によって表わされることがある。
M + n / 2H 2 MH n + ΔH M: Hydrogen storage (storage) alloy ΔH: Heat of reaction MH n : Metal hydride However, once the hydrogenation reaction occurs and becomes a metal hydride, it must be completely restored to its original state. May be represented by the following equation because it is very difficult.

MH(m+n)MH+n/2H±ΔH即ち、mは常に
水素貯(吸)蔵合金と結合して金属水素化物を形成して
いる水素原子を表わし、nは実用上、金属水素化物とな
った合金から取出し得る水素を表わしている。
MH (m + n) MH m + n / 2H 2 ± ΔH That is, m always represents a hydrogen atom that is bound to a hydrogen storage (storage) alloy to form a metal hydride, and n is practically a metal hydrogen. It represents the hydrogen that can be extracted from the alloyed alloy.

本明細書においては、上述のM,MH,MH(m+n)
MHを総称して金属水素化物と称し、単に記号Mで表
示する。
In the present specification, the above M, MH n , MH (m + n) ,
MH m is generically referred to as a metal hydride and is simply indicated by the symbol M.

これらの金属水素化物の水素平衡分解圧Pは、第13図
に示すように一般に温度Tの関数であって、高温にて金
属水素化物に高圧水素を発熱的に吸蔵させ、低温の低圧
水素雰囲気下でこの金属水素化物から吸熱的に水素を放
出させることができ、かような性質を利用したケミカル
ヒートポンプ装置が種々提案されている。
The hydrogen equilibrium decomposition pressure P of these metal hydrides is generally a function of temperature T as shown in FIG. Various chemical heat pump devices have been proposed which can release hydrogen endothermically from this metal hydride and utilize such properties.

例えば特開昭57-92690号公報には、密閉した1つのシリ
ンダ内の一端から他端へスクリューによって金属水素化
物を移送し、移送方向に沿って設けた高温熱交換部と低
温熱交換部を順次通過させるようにした装置が提案され
ている。この装置によれば、高温熱交換部を通る際にこ
の部分に外部から供給された高圧の水素を金属水素化物
に発熱的に吸蔵させたのち、水素を吸蔵したこの金属水
素化物を同じシリンダ内の低温熱交換部へスクリューで
移送し、減圧水素雰囲気としたこの低温熱交換部で金属
水素化物から水素を吸熱的に放出させることができ、こ
れによってヒートポンプとして機能する。
For example, in Japanese Patent Laid-Open No. 57-92690, a metal hydride is transferred from one end to the other end in one closed cylinder by a screw, and a high temperature heat exchange section and a low temperature heat exchange section are provided along the transfer direction. An apparatus has been proposed which is designed to sequentially pass. According to this device, when the high-pressure hydrogen supplied from the outside to this portion is exothermically stored in the metal hydride when passing through the high temperature heat exchange section, the hydrogen-absorbed metal hydride is stored in the same cylinder. The hydrogen is transferred from the metal hydride to the low temperature heat exchange section by a screw, and the hydrogen can be released endothermically from the metal hydride in this low temperature heat exchange section, which functions as a heat pump.

〈発明が解決しようとする問題点〉 この種の装置では、各熱交換部は各々所定の圧力を保つ
ため圧力的に遮断する必要がある。しかしながら、上記
の如き従来の装置においては、スクリュー手段によって
固体の金属水素化物を移送させつつ各熱交換部を圧力的
に遮断しなければならないから、圧力遮断のシール性に
問題があるとともに、スクリュー等の機械的トラブルを
生じ易いという欠点がある。
<Problems to be Solved by the Invention> In this type of device, each heat exchange section needs to be shut off by pressure in order to maintain a predetermined pressure. However, in the conventional device as described above, since it is necessary to shut off each heat exchange part while transferring the solid metal hydride by the screw means, there is a problem in the sealing property of the pressure shutoff, and the screw is used. There is a drawback that mechanical troubles such as are likely to occur.

そこでこの発明は、上述のごとき欠点を解消し、各熱交
換部を圧力的に確実に遮断でき、しかも機械的トラブル
も生じにくい、金属水素化物利用のヒートポンプ装置を
提供することを目的としてなされたものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances and has as its object to provide a heat pump device utilizing a metal hydride, which can eliminate the above-mentioned drawbacks, can reliably shut off each heat exchange portion in pressure, and is unlikely to cause mechanical trouble. It is a thing.

〈問題点を解決するための手段〉 すなわちこの発明のヒートポンプ装置は、金属水素化物
を充填した密閉容器の複数個を回転軸に対して放射方向
に配設してなる回転体と、該回転体の回転に伴い各密閉
容器が低温熱媒室および高温熱媒室を交互に順次通過す
るように該回転体の周囲に配設した低温熱媒室および高
温熱媒室と、該回転体の近傍に設けた高圧水素流入口お
よび水素流出口と、各密閉容器と該高圧水素流入口また
は水素流出口と接続する水素導管とからなり、該各水素
導管と高圧水素流入口または水素流出口との前記接続
は、1つの密閉容器が高温熱媒室にあるときこの密閉容
器から延びる水素導管が高圧水素流入口のみと連通し、
この密閉容器が低温熱媒室にあるときこの密閉容器から
延びる水素導管が水素流出口のみと連通するように、各
水素導管が回転体の回転に伴って高圧水素流入口および
水素流出口と順次連通または遮断されるようにしたこと
を特徴とするものである。
<Means for Solving Problems> That is, the heat pump device of the present invention includes a rotating body in which a plurality of closed containers filled with a metal hydride are arranged in a radial direction with respect to a rotating shaft, and the rotating body. With the rotation of each closed container, the low-temperature heat medium chamber and the high-temperature heat medium chamber are arranged around the rotating body so as to alternately pass through the low-temperature heat medium chamber and the high-temperature heat medium chamber, and the vicinity of the rotor. A high-pressure hydrogen inlet and a hydrogen outlet provided in each, and each closed container and a hydrogen conduit connected to the high-pressure hydrogen inlet or the hydrogen outlet, each hydrogen conduit and the high-pressure hydrogen inlet or hydrogen outlet The connection is such that when one closed container is in the high temperature heat transfer medium chamber, the hydrogen conduit extending from this closed container communicates only with the high pressure hydrogen inlet,
When the closed container is in the low temperature heat transfer medium chamber, the hydrogen conduits extending from the closed container communicate with only the hydrogen outlet so that each hydrogen conduit is sequentially connected to the high pressure hydrogen inlet and the hydrogen outlet as the rotor rotates. It is characterized by being connected or disconnected.

上記したごときこの発明の装置によれば、回転体の回転
に伴い密閉容器内の金属水素化物が高温熱媒室から低温
熱媒室へ、あるいは低温熱媒室から高温熱媒室へと回転
移動する際に、高温熱媒室にある金属水素化物は高圧水
素流入口から水素導管を介して密閉容器に加圧供給され
る高圧水素を発熱的に吸蔵し、この金属水素化物が低温
熱媒室にきたときに水素流出口と水素導管を介して連通
してなる低圧水素雰囲気下の密閉容器内で吸熱的に水素
を放出する。
According to the apparatus of the present invention as described above, the metal hydride in the closed container is rotationally moved from the high temperature heat transfer medium chamber to the low temperature heat transfer medium chamber or from the low temperature heat transfer medium chamber to the high temperature heat transfer medium chamber as the rotor rotates. In this case, the metal hydride in the high temperature heat transfer medium chamber exothermically absorbs the high pressure hydrogen that is pressurized and supplied from the high pressure hydrogen inlet port to the closed container via the hydrogen conduit, and this metal hydride is stored in the low temperature heat transfer medium chamber. When it comes to, the hydrogen is released endothermically in a closed container in a low-pressure hydrogen atmosphere which communicates with the hydrogen outlet through a hydrogen conduit.

このとき、高温熱媒室にある密閉容器内にて金属水素化
物が冷却されつつ高圧水素を吸蔵し、低温熱媒室にある
低圧水素雰囲気下の密閉容器内にて金属水素化物が吸熱
的に水素を放出するモードの場合に、低温熱媒室に冷却
負荷を接続すれば冷房装置として機能させることができ
る。また、低温熱媒室にある密閉容器内にて金属水素化
物が加熱されつつ水素を放出し、高温熱媒室にある密閉
容器内にて金属水素化物が発熱的に水素を吸蔵するモー
ドの場合には、高温熱媒に加熱負荷を接続すれば暖房装
置として機能させることができる。
At this time, the metal hydride absorbs high-pressure hydrogen while being cooled in the closed container in the high-temperature heat transfer medium chamber, and the metal hydride absorbs heat in the closed container under the low-pressure hydrogen atmosphere in the low-temperature heat transfer medium chamber. In the mode of releasing hydrogen, if a cooling load is connected to the low temperature heat transfer medium chamber, it can function as a cooling device. Also, in the mode in which the metal hydride releases hydrogen while being heated in the closed container in the low temperature heat transfer medium chamber, and the metal hydride exothermically stores hydrogen in the closed container in the high temperature heat transfer medium chamber. In addition, if a heating load is connected to the high temperature heating medium, it can function as a heating device.

〈実施例〉 以下に図面に示す実施例を参照してこの発明を詳述す
る。
<Examples> The present invention will be described in detail below with reference to the examples shown in the drawings.

第1図はこの発明のヒートポンプ装置の1つの実施例を
模式的に示す説明図であり、円板状の3個の回転体1
a,1b,1cが回転軸2に固着され、この回転軸は軸
受3により支承されて、回転軸2の回転とともに回転体
も回転しうるようになっている。この実施例では3個の
回転体を用いているが、回転体1個でもヒートポンプ装
置として機能させることができる。
FIG. 1 is an explanatory view schematically showing one embodiment of a heat pump device of the present invention, in which three disk-shaped rotating bodies 1 are provided.
The a, 1b, and 1c are fixed to the rotary shaft 2, and the rotary shaft is supported by a bearing 3 so that the rotary body can rotate with the rotation of the rotary shaft 2. Although three rotating bodies are used in this embodiment, even one rotating body can function as a heat pump device.

各回転体1は、第2図の側面図に示したように、放射方
向に配した仕切壁4および環状壁5,5によりその内部
が4個に区画され、各室はそれぞれ1個の密閉容器6を
形成している。各回転体1内に形成される密閉容器6の
数は必ずしも4個とする必要はなく、複数個、好ましく
は3個以上の任意の個数を形成することができる。
As shown in the side view of FIG. 2, each rotary body 1 is divided into four parts by a partition wall 4 and annular walls 5 and 5 arranged in the radial direction, and each chamber is sealed by one. The container 6 is formed. The number of closed containers 6 formed in each rotating body 1 does not necessarily have to be four, and a plurality, preferably three or more, of any number can be formed.

なお、各密閉容器6の仕切壁4を断熱材を用いた断熱壁
とすれば、各密閉容器6間の伝熱の影響を防止すること
ができて好ましい。さらには、各密閉容器の内側および
外側に伝熱フィン等の伝熱面を大きくする手段や、ヒー
トパイプ等の熱伝達手段を設けるといった従来の回転熱
交換器の技術をこの発明にも利用することができる。
If the partition wall 4 of each closed container 6 is a heat insulating wall using a heat insulating material, the influence of heat transfer between the closed containers 6 can be prevented, which is preferable. Furthermore, the technology of the conventional rotary heat exchanger such as a means for enlarging a heat transfer surface such as a heat transfer fin and a heat transfer means such as a heat pipe is provided on the inside and outside of each closed container for this invention. be able to.

各回転体上の密閉容器6内にはいずれも金属水素化物M
が充填されている。また、各密閉容器6の各々からは水
素導管7が引出され、各回転体1a,1b,1cの放射
方向同位置にある密閉容器同士の3本の水素導管は1本
にまとめられて合体水素導管8となり、回転軸の一端へ
延びている。第1図においては合体水素導管として2本
しか図示されていないが、各回転体には4個の密閉容器
6が設けられているから、合計4本の合体水素導管が回
転軸の一端へ延びている。なお、密閉容器6内に充填さ
れた金属水素化物Mは、合体水素導管8を介して連通す
る密閉容器6同士においては同種の金属水素化物Mであ
ることが好ましいが、後述する高温熱媒室14で水素反
応を起し低温熱媒室15で脱水素化反応を起すものであ
れば、同種のものでなくともよい。また金属水素化物M
は、水素化反応と脱水素化反応の繰返しにより細粒化さ
れることがある。そのような場合には、金属水素化物の
細粒が水素導管7に流れ込まないように、密閉容器6内
の水素導管開口部に積層金網等のフィルタ(図示せず)
を取付けてもよい。また、合体水素導管8の回転軸の外
周面に沿って延設することもできるが、図示のように回
転軸2を中空とし、この内部に合体水素導管を通すこと
もできる。
Each of the metal hydrides M is contained in the closed container 6 on each rotating body.
Is filled. Further, a hydrogen conduit 7 is drawn out from each of the hermetically sealed containers 6, and the three hydrogen conduits of the hermetically sealed containers located at the same position in the radial direction of each of the rotating bodies 1a, 1b, 1c are combined into one hydrogen. It becomes the conduit 8 and extends to one end of the rotating shaft. Although only two coalesced hydrogen conduits are shown in FIG. 1, since there are four sealed containers 6 provided in each rotor, a total of four coalesced hydrogen conduits extend to one end of the rotary shaft. ing. The metal hydride M filled in the closed container 6 is preferably the same kind of metal hydride M in the closed containers 6 communicating with each other via the combined hydrogen conduit 8, but a high temperature heat transfer medium chamber described later. As long as the hydrogen reaction occurs in 14 and the dehydrogenation reaction occurs in the low-temperature heat transfer medium chamber 15, the same kind does not have to be used. Also, metal hydride M
May be finely divided by repeating the hydrogenation reaction and the dehydrogenation reaction. In such a case, a filter (not shown) such as a laminated wire mesh is provided at the opening of the hydrogen conduit in the closed container 6 so that the fine particles of the metal hydride do not flow into the hydrogen conduit 7.
May be attached. Further, although it is possible to extend along the outer peripheral surface of the rotating shaft of the combined hydrogen conduit 8, it is also possible to make the rotating shaft 2 hollow as shown in the drawing and pass the combined hydrogen conduit inside.

回転軸2の一端部には、回転軸2の回転に伴って水素導
管7および合体水素導管8を介して各々の密閉容器6と
個別に連通又は遮断する高圧水素流入口9および水素流
出口10が設けられている。
At one end of the rotary shaft 2, a high-pressure hydrogen inlet 9 and a hydrogen outlet 10 that individually communicate with or shut off from the respective closed containers 6 via the hydrogen conduit 7 and the combined hydrogen conduit 8 as the rotary shaft 2 rotates. Is provided.

すなわち、第3図(A)および(B)に示したように、中空回
転軸2の先端は端板20で閉止され、この先端近傍にて
回転軸中空部はフランジ21により取付けられた管板2
2により仕切られ、管板22にて各合体水素導管8が開
口している。端板20と管板22との間の回転軸周壁2
3の周囲には、所定個所に高圧水素流入口9および水素
流出口10が開口する環状部材24を固定するととも
に、端板20と管板22との間の回転軸2中空部には中
実の中心軸25を配設する。この中心軸25と回転軸周
壁23との間に構成される環状空間には、中心軸25か
ら放射方向に配設された4個の仕切部材26によって、
各回転体1の4個の密閉容器6に対応する4個の空洞2
7が形成され、各密閉容器からの合体水素導管8が管板
22の開口部にて各空洞27と連通している。また回転
軸周壁23には各空洞27に連通する開孔28が形成さ
れている。なお、参照番号29は環状部材24を構成し
ている一部材で、各合体水素導管8が空洞27及び開孔
28を介して高圧水素流入口9および水素流出口10の
各出入口と連通する時間及びタイミングを調整するもの
である。かくして、回転軸2の回転に伴ってその周壁2
3は部材29の内周面を摺動回転し、各合体水素導管8
は空洞27及び開孔28を介して高圧水素流入口9との
連通、遮断;および水素流出口10との連通,遮断のサ
イクルを繰返すことになる。
That is, as shown in FIGS. 3 (A) and 3 (B), the tip of the hollow rotating shaft 2 is closed by the end plate 20, and the hollow portion of the rotating shaft is attached by the flange 21 in the vicinity of this end. Two
It is partitioned by 2, and each coalesced hydrogen conduit 8 is opened at the tube sheet 22. Rotating shaft peripheral wall 2 between the end plate 20 and the tube plate 22
An annular member 24 having a high-pressure hydrogen inlet 9 and a hydrogen outlet 10 opened is fixed at a predetermined position around 3, and a solid portion is provided in the hollow portion of the rotary shaft 2 between the end plate 20 and the tube plate 22. The central axis 25 of is arranged. In the annular space formed between the central shaft 25 and the rotary shaft peripheral wall 23, four partition members 26 arranged radially from the central shaft 25
Four cavities 2 corresponding to the four closed containers 6 of each rotating body 1
7 is formed, and the combined hydrogen conduit 8 from each closed container communicates with each cavity 27 at the opening of the tube sheet 22. Further, the rotary shaft peripheral wall 23 is formed with an opening 28 communicating with each cavity 27. Reference numeral 29 is one member forming the annular member 24, and is a time period during which each united hydrogen conduit 8 communicates with each of the high pressure hydrogen inlet 9 and the hydrogen outlet 10 through the cavity 27 and the opening 28. And the timing is adjusted. Thus, as the rotary shaft 2 rotates, its peripheral wall 2
3 slides and rotates on the inner peripheral surface of the member 29, and each united hydrogen conduit 8
Will repeat the cycle of communication with the high-pressure hydrogen inlet 9 through the cavity 27 and the opening 28, shutoff; and communication with the hydrogen outlet 10 and shutoff.

なお、参照番号24aは、回転軸周壁23と環状部材24
との摺動縁部に設けたシール材を表わす。
In addition, reference numeral 24a indicates the rotary shaft peripheral wall 23 and the annular member 24.
The sealing material provided on the sliding edge portion of and.

上記のように一体的に組み立てられた回転体1a,1
b,1cと回転軸2は、第1図に示したように外側ダク
ト12で囲繞され、さらにこの外側ダクトの内部は回転
軸2を挟んで延びる仕切壁13によって2つのダクト部
に区画される。
The rotating bodies 1a, 1 integrally assembled as described above
As shown in FIG. 1, b and 1c and the rotary shaft 2 are surrounded by an outer duct 12, and the inside of the outer duct is divided into two duct parts by a partition wall 13 that extends with the rotary shaft 2 interposed therebetween. .

仕切壁13は回転軸2および回転体1a,1b,1cの
回転に支承がないように、これらに対して僅かな間隙を
隔てて設けられている。この場合、図示したように回転
軸2を中空とし、回転軸内に水素導管7および合体水素
導管8を通すようにすれば、回転軸2と仕切壁13との
間隙を小さくでき各ダクト部の間のシール性を向上さる
ことができる。かくして各ダクト部に高温熱媒あるいは
低温熱媒を流すことによって、回転軸2の一側、例えば
上側に高温熱媒室14が形成され、回転軸2の他側、例
えば下側に低温熱媒室15が形成される。かような構成
によって、外部駆動源(図示せず)による回転軸2の回
転に伴い、各回転体の密閉容器6が高温熱媒室14およ
び低温熱媒室15を交互に順次通過できるようにされて
いる。
The partition wall 13 is provided with a slight gap therebetween so that there is no support for the rotation of the rotary shaft 2 and the rotary bodies 1a, 1b, 1c. In this case, if the rotating shaft 2 is hollow as shown in the drawing and the hydrogen conduit 7 and the combined hydrogen conduit 8 are passed through the rotating shaft, the gap between the rotating shaft 2 and the partition wall 13 can be made small, and the ducts of the respective duct parts can be reduced. The sealing property between them can be improved. Thus, by flowing the high-temperature heat medium or the low-temperature heat medium into each duct, the high-temperature heat medium chamber 14 is formed on one side, for example, the upper side of the rotary shaft 2, and the low-temperature heat medium on the other side, for example, the lower side of the rotary shaft 2. A chamber 15 is formed. With such a configuration, the closed container 6 of each rotating body can alternately pass through the high-temperature heat medium chambers 14 and the low-temperature heat medium chambers 15 alternately in accordance with the rotation of the rotary shaft 2 by the external drive source (not shown). Has been done.

なお、各熱媒室14,15に流す熱媒は、流体であれば
その種類は特に限定されないが、一般的には気体が好ま
しく使用できる。また各熱媒室に実質的に等しい圧力で
流体の熱媒が供給される場合には各熱媒室間のシールを
厳密にする必要はない。
The type of the heat medium flowing in each of the heat medium chambers 14 and 15 is not particularly limited as long as it is a fluid, but in general, gas can be preferably used. Further, when the fluid heat medium is supplied to the heat medium chambers at substantially the same pressure, it is not necessary to strictly seal the heat medium chambers.

高圧水素流入口9へ供給される水素は圧縮機30および
高圧水素タンク31から供給され、一方水素流出口10
から流出する低圧水素は圧縮機30により加圧されて循
環される。なお第1図に示したように、水素流出口10
からの低圧水素の流出は吸引機32により積極的に吸引
して行ない、この水素を低圧水素タンク33に溜めるよ
うにしてもよい。
The hydrogen supplied to the high-pressure hydrogen inlet 9 is supplied from the compressor 30 and the high-pressure hydrogen tank 31, while the hydrogen outlet 10
The low-pressure hydrogen flowing out of the compressor is pressurized by the compressor 30 and circulated. As shown in FIG. 1, the hydrogen outlet 10
The low-pressure hydrogen may be positively sucked by the suction device 32 and the hydrogen may be stored in the low-pressure hydrogen tank 33.

上記したごとき構成のこの発明のヒートポンプ装置の作
動を以下に説明する。第4図は、第1図のように配置さ
れた回転体の1つを取出した説明図であり、第1図と同
じ部材には同じ参照番号を付すことにより説明を省略す
る。第4図は冷房装置に適用される冷凍(降温)モード
を示しており、前述したように、回転軸2の回転に伴い
回転体1の各密閉容器は位置(高温熱媒室14内)→
位置(高温熱媒室14と低温熱媒室15との間)→
位置(低温熱媒室15内)→位置(低温熱媒室15と
高温熱媒室14との間)と図中矢印の方向へ回動する。
The operation of the heat pump device of the present invention having the above-described structure will be described below. FIG. 4 is an explanatory view in which one of the rotating bodies arranged as shown in FIG. 1 is taken out, and the same members as those in FIG. 1 are denoted by the same reference numerals and the description thereof will be omitted. FIG. 4 shows a freezing (cooling) mode applied to the cooling device. As described above, each closed container of the rotating body 1 is positioned (within the high temperature heat transfer medium chamber 14) as the rotating shaft 2 rotates.
Position (between high temperature heat medium chamber 14 and low temperature heat medium chamber 15) →
The position (inside the low temperature heat medium chamber 15) → the position (between the low temperature heat medium chamber 15 and the high temperature heat medium chamber 14) rotates in the direction of the arrow in the figure.

いま、密閉容器6の1つが位置にある場合を考える
と、この位置にある密閉容器から延びる水素導管7およ
び合体水素導管8は、空洞27を介して高圧水素流入口
9と連通している(第3図参照)。したがって高圧水素
ガスは高圧水素流入口9から導入され、空洞27、合体
水素導管8、水素導管7を経て高温熱媒室14内にある
位置の密閉容器6へ供給される。ここで密閉容器6内
の金属水素化物は温度Tに冷却されつつ(発熱しつ
つ)高圧水素ガスを吸蔵する。
Considering now that one of the closed containers 6 is in the position, the hydrogen conduit 7 and the combined hydrogen conduit 8 extending from the closed container in this position communicate with the high-pressure hydrogen inlet 9 via the cavity 27 ( (See FIG. 3). Therefore, the high-pressure hydrogen gas is introduced from the high-pressure hydrogen inlet 9, and is supplied to the closed container 6 located in the high-temperature heat transfer medium chamber 14 through the cavity 27, the combined hydrogen conduit 8 and the hydrogen conduit 7. Wherein the metal hydride in the closed casing 6 while being cooled to a temperature T H (with heating) to absorb high-pressure hydrogen gas.

次いで、この密閉容器が回動して、高温熱媒室14と低
温熱媒室15の間すなわち位置にくると、この密閉容
器から延びる水素導管7と合体水素導管8は、高圧水素
流入口9と水素流出口10のいずれとも連通せずに遮断
された状態を保ち、密閉容器内の金属水素化物の温度は
下降してくる。
Next, when the closed container is rotated and comes to a position between the high temperature heat transfer medium chamber 14 and the low temperature heat transfer medium chamber 15, that is, the hydrogen conduit 7 and the combined hydrogen conduit 8 extending from the closed container are connected to the high pressure hydrogen inlet port 9. And the hydrogen outlet 10 do not communicate with each other and remain in the shut-off state, and the temperature of the metal hydride in the closed container decreases.

さらにこの密閉容器6が回動して低温熱媒室15内すな
わち位置にくると、この密閉容器から延びる水素導管
7と合体水素導管8は空洞27と開孔(第3図)を介し
て水素流出口10と連通し、さらには必要に応じて吸引
機32(第1図)により吸引することによって、この密
閉容器内は低圧水素雰囲気となり、金属水素化物は温度
の熱媒から吸熱しつつ水素を放出する。吸熱された
のちの熱媒に冷却負荷が接続される。一方、放出された
水素は水素流出口10から流出し、圧縮機30(第1
図)へ循環される。
When the closed container 6 further rotates and reaches the low temperature heat transfer medium chamber 15, that is, the position, the hydrogen conduit 7 and the combined hydrogen conduit 8 extending from the closed container are filled with hydrogen via the cavity 27 and the opening (FIG. 3). By communicating with the outflow port 10 and further suctioning by a suction device 32 (FIG. 1) as needed, the inside of this closed container becomes a low-pressure hydrogen atmosphere, and the metal hydride absorbs heat from the heat medium at the temperature T L. While releasing hydrogen. A cooling load is connected to the heat medium that has absorbed heat. On the other hand, the released hydrogen flows out from the hydrogen outlet 10 and flows into the compressor 30 (first
).

この密閉容器6がさらに回動して位置にあるときは、
この密閉容器から延びる水素導管7と合体水素導管8
は、高圧水素流入口9および水素流出口10のいずれと
も連通せずに、遮断された状態を保ち、水素放出後の金
属水素化物は次第に昇温しながら位置へと移動してい
く。
When the closed container 6 is rotated further to the position,
Hydrogen conduit 7 and combined hydrogen conduit 8 extending from this closed container
Does not communicate with either the high-pressure hydrogen inlet 9 or the hydrogen outlet 10 and remains in a blocked state, and the metal hydride after hydrogen release gradually moves to the position while raising the temperature.

上述のようにして各回転体の4個の密閉容器は→→
→→と回転する間に、高温での高圧水素の発熱的
吸蔵→低温での水素を吸熱的放出というサイクルを繰返
し行なうことによって、低温熱媒に冷熱を連続して与え
ることができ、冷凍モードのヒートポンプとして機能す
る。
As described above, the four closed containers of each rotating body are →→
→→ While rotating, the exothermic occlusion of high-pressure hydrogen at high temperature → Endothermic release of hydrogen at low temperature can be repeated to provide cold heat to the low-temperature heat medium continuously. Function as a heat pump.

一方、この装置を昇温モードで運転する場合には、低温
熱媒室15にある密閉容器から水素を除去し、かつ高温
熱媒室14にある密閉容器に高圧水素を供給すれば、金
属水素化物は低温熱媒室15で加熱されつつ(吸熱しつ
つ)水素を放出し、高温熱媒室14で発熱的に水素を吸
蔵する。従って高温熱媒に加熱負荷を接続することによ
って、昇温モードのヒートポンプとして機能させること
ができる。
On the other hand, when this apparatus is operated in the temperature rising mode, if hydrogen is removed from the closed container in the low temperature heat transfer medium chamber 15 and high pressure hydrogen is supplied to the closed container in the high temperature heat transfer medium chamber 14, metallic hydrogen The compound releases hydrogen while being heated (absorbing heat) in the low temperature heat medium chamber 15, and occludes hydrogen in the high temperature heat medium chamber 14 exothermically. Therefore, by connecting a heating load to the high-temperature heat medium, it can function as a heat pump in the temperature rising mode.

ところで、水素化反応をして水素を吸蔵した金属水素化
物は、脱水素化反応をして水素を放出した金属水素化物
よりも、若干重量が重くなるが、この重量差を利用して
回転体1に回転力を付与することも可能である。すなわ
ち第5図に示したように、位置にある回転体1の密閉
容器6内で金属水素化物の水素吸蔵反応が起り、これと
180゜ずれた位置にある密閉容器6内で金属水素化物
の水素放出反応が起るように、高温熱媒室14と低温熱
媒室15の位置および高圧水素流入口9と水素流出口1
0の位置を定めることによって、位置の水素化金属水
素化物重量と位置の脱水素化金属水素化物重量との間
に重量差を生ぜしめ、この重量差によって図中矢印で示
すような回転力を回転体に常時付与することができる。
これによって、回転軸の外部駆動源を無くすことがで
き、あるいは回転軸を回転させるための外部動力を少な
くすることができる。
By the way, a metal hydride that has undergone a hydrogenation reaction and occludes hydrogen is slightly heavier than a metal hydride that has undergone a dehydrogenation reaction to release hydrogen. It is also possible to apply a rotational force to 1. That is, as shown in FIG. 5, the hydrogen storage reaction of the metal hydride occurs in the closed container 6 of the rotating body 1 at the position, and this
The positions of the high-temperature heat transfer medium chamber 14 and the low-temperature heat transfer medium chamber 15 as well as the high-pressure hydrogen inlet 9 and the hydrogen outlet 1 so that the hydrogen-releasing reaction of the metal hydride occurs in the closed container 6 located at a position shifted by 180 °.
By determining the position of 0, a weight difference is generated between the weight of the hydride metal hydride at the position and the weight of the dehydrogenation metal hydride at the position, and this weight difference causes a rotational force as indicated by an arrow in the figure. It can be constantly applied to the rotating body.
As a result, the external drive source of the rotary shaft can be eliminated, or the external power for rotating the rotary shaft can be reduced.

上述したように、回転体の各密閉容器6と高圧水素流入
口9および水素流出口10とは、水素導管7および合体
水素導管8を介して連通、遮断されるが、これらの水素
導管7,8は必ずしも回転軸2と別体のチューブ状とす
る必要はなく、例えば第6図乃至第8図に示したように
中空の回転軸2内を長手方向に延びる十字型の仕切部材
40によって区分し、こ仕切部材40を回転軸周壁23
とによって形成される4本の流路41を水素導管として
利用することもできる。この場合、各流路41は導管4
2によって各密閉容器6と連通させる。この実施例にお
いても、回転軸2の一端部に第8図に示したように、高
圧水素流入口9および水素流出口10を第3図の実施例
と実質的に同様にして配設することができる。なお、第
6図乃至第8図において、第3図と同じ部材にはそれら
と同じ参照番号を付すことにより説明を省略する。
As described above, the closed vessels 6 of the rotating body and the high-pressure hydrogen inlet 9 and the hydrogen outlet 10 are connected and disconnected via the hydrogen conduit 7 and the combined hydrogen conduit 8, but these hydrogen conduits 7, 8 does not necessarily have to be formed in a tubular shape separate from the rotary shaft 2, and is divided by a cross-shaped partition member 40 extending in the longitudinal direction inside the hollow rotary shaft 2 as shown in FIGS. 6 to 8, for example. Then, the partition member 40 is attached to the rotary shaft peripheral wall 23.
The four flow paths 41 formed by and can also be used as hydrogen conduits. In this case, each flow path 41 is connected to the conduit 4
2 to communicate with each closed container 6. Also in this embodiment, as shown in FIG. 8, a high pressure hydrogen inlet 9 and a hydrogen outlet 10 are arranged at one end of the rotary shaft 2 in substantially the same manner as the embodiment of FIG. You can Incidentally, in FIGS. 6 to 8, the same members as those in FIG. 3 are designated by the same reference numerals, and the description thereof will be omitted.

この発明のヒートポンプ装置は、上記した実施例のみに
限定されるものではなく、特許請求の範囲内で種々の変
形が可能である。例えば回転軸2から放射方向に多数の
仕切壁13を延設せしめて、回転軸のまわりに高温熱媒
室と低温熱媒室を対として複数組設けるようにしてもよ
い。また、回転体は必ずしも円板状とする必要はなく、
球状や多角形状としてもよい。さらに、金属水素化物を
充填した複数個の密閉容器は、図示した回転体1a,1
b,1cのように一体構造にする必要はなく、回転軸の
周方向に放射状に散在させて回転軸ともに回転しうるよ
うに配置してあればよい。
The heat pump device of the present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the claims. For example, a large number of partition walls 13 may be extended from the rotary shaft 2 in the radial direction, and a plurality of sets of high-temperature heat medium chambers and low-temperature heat medium chambers may be provided as a pair around the rotary shaft. Also, the rotating body does not necessarily have to be a disc shape,
It may be spherical or polygonal. Further, the plurality of closed containers filled with the metal hydride are the rotors 1a, 1 shown in the figure.
It is not necessary to form an integral structure like b and 1c, but it is sufficient if they are scattered radially in the circumferential direction of the rotary shaft so that they can rotate together with the rotary shaft.

さらに、例えば第9図に示したように、金属水素化物を
充填した円筒状の密閉容器60の複数個を互いに平行に
なるように環状に並列させてチェーンまたはベルト等の
無端回転送行部材61上に配列し、密閉容器60の下半
部が嵌合する切欠き63を有する複数の回転歯車64
(第1図の実施例の回転軸に相当する)間に該無端回転
送行部材61を架設することによって、回転体62を形
成することができる。そして、高温熱媒室65と低温熱
媒室66とを交互になるように無端回転送行部材61の
送行方向にそれぞれ配設することによって、第1図の実
施例の装置と同様に機能させることができる。
Further, as shown in FIG. 9, for example, a plurality of cylindrical closed containers 60 filled with metal hydride are annularly arranged in parallel so as to be parallel to each other, and the endless transfer member 61 such as a chain or a belt is provided. And a plurality of rotary gears 64 arranged in the
By arranging the endless transfer transfer member 61 between (corresponding to the rotating shaft of the embodiment of FIG. 1), the rotating body 62 can be formed. Then, the high-temperature heat transfer medium chambers 65 and the low-temperature heat transfer medium chambers 66 are alternately arranged in the traveling direction of the endless transfer transfer member 61 so that they function in the same manner as the apparatus of the embodiment of FIG. You can

なお、この実施例においては高圧水素流入口9又は水素
流出口10に接続する水素導管7は、一部可撓性材料を
使用し、第3図の空洞27に接続させることができる。
あるいはまた該空洞が無端回転送行部材61と平行して
移動するように、第10図乃至第12図に示したよう
に、所定間隔で高圧水素流入口9および水素流出口10
が繰返し開口しかつ無端回転送行部材61の送行形状と
略同形の筒状環状部材67を無端回転送行部材61の側
面に配設するとともに、この筒状環状部材67の内部空
間に第3図の空洞27に対応する空洞69を有する複数
のチャンバ68を摺動可能に配設し、各密閉容器60か
らの水素導管7を各チャンバ68と連通させることによ
って、各チャンバ68を無端回転送行部材61上の各密
閉容器60と平行して移動させるようにすることもでき
る。このチャンバ68には空洞69に連通する開口70
が形成されており、無端回転送行部材61の送行に伴っ
て各水素導管7は空洞69と開口70を介して高圧水素
流入口9との連通、遮断;および水素流出口10との連
通、遮断のサイクルを繰返す。
In this embodiment, the hydrogen conduit 7 connected to the high-pressure hydrogen inlet 9 or the hydrogen outlet 10 is made of a partially flexible material and can be connected to the cavity 27 shown in FIG.
Alternatively, as shown in FIGS. 10 to 12, the high pressure hydrogen inlet 9 and the hydrogen outlet 10 are arranged at predetermined intervals so that the cavity moves in parallel with the endless transfer member 61.
A cylindrical annular member 67 that is repeatedly opened and has substantially the same shape as the shape of the endless continuous transfer member 61 is disposed on the side surface of the endless continuous transfer member 61, and the internal space of the cylindrical annular member 67 of FIG. A plurality of chambers 68 having cavities 69 corresponding to the cavities 27 are slidably arranged, and the hydrogen conduit 7 from each closed container 60 is communicated with each chamber 68, whereby each chamber 68 is transferred to the endless transfer member 61. It is also possible to move them in parallel with the respective closed containers 60 above. The chamber 68 has an opening 70 communicating with the cavity 69.
Are formed, and the hydrogen conduits 7 communicate with and shut off from the high-pressure hydrogen inlet 9 through the cavity 69 and the opening 70 as the endless transfer member 61 travels; and the hydrogen outlet 10 communicates and shuts off. Repeat the cycle of.

なお、第10図乃至第12図の参照番号71は、筒状環
状部材67を構成する一部材で、高圧水素流入口9およ
び水素流出口10の各出入口と各水素導管7とが空洞6
9及び開孔70を介して連通する時間及びタイミングを
調整するものである。参照番号72は、隣り合うチャン
バ68の開口70を有する面同士を連結する可撓性材料
からなるシール板であり、筒状環状部材67の部材71
に当接摺動して高圧水素流入口9および水素流出口10
において出入する水素同士が短絡するのを防止する働き
をする。参照番号73は、隣り合うチャンバ68の底面
同士を連結する可撓性の連結部材であり、これによって
複数のチャンバ68を一繋ぎとして筒状環状部材67内
を送行させることができる。また参照番号74は、筒状
環状部材67側面の長手方向に穿設したスリットであ
り、これによって各水素導管7がチャンバ68と連通し
た状態で移動することができる。
Reference numeral 71 in FIGS. 10 to 12 is one member that constitutes the tubular annular member 67, and each inlet / outlet of the high pressure hydrogen inlet 9 and the hydrogen outlet 10 and each hydrogen conduit 7 is a cavity 6.
The time and the timing for communicating with each other through the opening 9 and the opening 70 are adjusted. Reference numeral 72 is a seal plate made of a flexible material that connects surfaces having the openings 70 of the adjacent chambers 68, and is a member 71 of the tubular annular member 67.
Sliding against the high pressure hydrogen inlet 9 and hydrogen outlet 10
It works to prevent short-circuiting between hydrogen flowing in and out. Reference numeral 73 is a flexible connecting member that connects the bottom surfaces of the adjacent chambers 68 to each other, so that the plurality of chambers 68 can be connected together and can be fed through the tubular annular member 67. Further, reference numeral 74 is a slit formed in the longitudinal direction of the side surface of the tubular annular member 67, whereby each hydrogen conduit 7 can move in a state of communicating with the chamber 68.

〈発明の効果〉 以上説明したようにこの発明のヒートポンプ装置によれ
ば、高温熱交換部と低温熱交換部との間の圧力的に遮断
すべき個所に固体の金属水素化物自体を移送させること
なく、金属水素化物を充填した密閉容器を回転軸の回り
に回動させるようにしたため、両熱交換部間に確実な圧
力遮断のシール性をもたらすことができるとともに、金
属水素化物の移送手段としてスクリュー等を用いないか
ら移送手段の機械的トラブルも生じにくいという利点が
ある。
<Effects of the Invention> As described above, according to the heat pump device of the present invention, the solid metal hydride itself is transferred to the location between the high temperature heat exchange section and the low temperature heat exchange section at which pressure is to be shut off. Instead, since the closed container filled with metal hydride is rotated around the rotation axis, it is possible to provide a reliable pressure shut-off sealing property between both heat exchange parts and also as a metal hydride transfer means. Since no screw or the like is used, there is an advantage that mechanical trouble of the transfer means hardly occurs.

【図面の簡単な説明】[Brief description of drawings]

第1図はこの発明のヒートポンプ装置の実施例を示す説
明図;第2図は第1図における回転体の側面図;第3図
(A)および(B)は第1図における高圧水素流入口および水
素流出口の断面図;第4図はこの発明の装置の動作(冷
凍モード)を示す説明図;第5図はこの発明の装置の別
な実施例の動作を示す説明図、第6図はこの発明の装置
のさらに別な実施例を示す説明図;第7図は第6図のA
−A断面図;第8図は第6図のB−B断面図;第9図は
この発明の装置のさらに別な実施例を示す説明図;第1
0図は第9図の装置と組合せる水素出入口の断面図;第
11図は第10図のC−C断面図;第12図は第10図
のD−D断面図;および第13図は一般的な金属水素化
物の水素平衡分解圧特性を示すグラフである。 1,62……回転体、2……回転軸、6,60……密閉
容器、7……水素導管、8……合体水素導管、9……高
圧水素流入口、10……水素流出口、12……外側ダク
ト、13……仕切壁、14,65……高温熱媒室、1
5,66……低温熱媒室、64……回転歯車。
1 is an explanatory view showing an embodiment of a heat pump device of the present invention; FIG. 2 is a side view of a rotating body in FIG. 1; FIG.
(A) and (B) are cross-sectional views of the high-pressure hydrogen inlet and the hydrogen outlet in FIG. 1; FIG. 4 is an explanatory view showing the operation (refrigeration mode) of the apparatus of the present invention; FIG. 6 is an explanatory view showing the operation of another embodiment of the apparatus, FIG. 6 is an explanatory view showing yet another embodiment of the apparatus of the present invention; FIG. 7 is A of FIG.
-A sectional view; FIG. 8 is a BB sectional view of FIG. 6; FIG. 9 is an explanatory view showing still another embodiment of the apparatus of the present invention;
0 is a sectional view of the hydrogen inlet / outlet combined with the apparatus of FIG. 9; FIG. 11 is a sectional view taken along line CC of FIG. 10; FIG. 12 is a sectional view taken along line DD of FIG. 10; and FIG. It is a graph which shows the hydrogen equilibrium decomposition pressure characteristic of a general metal hydride. 1, 62 ... Rotating body, 2 ... Rotating shaft, 6, 60 ... Closed container, 7 ... Hydrogen conduit, 8 ... Combined hydrogen conduit, 9 ... High-pressure hydrogen inlet, 10 ... Hydrogen outlet, 12 ... Outer duct, 13 ... Partition wall, 14, 65 ... High temperature heat transfer chamber, 1
5, 66 ... Low temperature heat medium chamber, 64 ... Rotating gear.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】金属水素化物を充填した密閉容器の複数個
を回転軸に対して放射方向に配設してなる回転体と、該
回転体の回転に伴い各密閉容器が低温熱媒室および高温
熱媒室を交互に順次通過するように該回転体の周囲に配
設した低温熱媒室および高温熱媒室と、該回転体の近傍
に設けた高圧水素流入口および水素流出口と、各密閉容
器と該高圧水素流入口または水素流出口と接続する水素
導管とからなり、該各水素導管と高圧水素流入口または
水素流出口との前記接続は、1つの密閉容器が高温熱媒
室にあるときこの密閉容器から延びる水素導管が高圧水
素流入口のみと連通し、この密閉容器が低温熱媒室にあ
るときこの密閉容器から延びる水素導管が水素流出口の
みと連通するように、各水素導管が回転体の回転に伴っ
て高圧水素流入口および水素流出口と順次連通または遮
断されるようにしたことを特徴とするヒートポンプ装
置。
1. A rotating body comprising a plurality of closed containers filled with a metal hydride in a radial direction with respect to a rotation axis, and each closed container has a low-temperature heat transfer medium chamber as the rotating body rotates. A low-temperature heat medium chamber and a high-temperature heat medium chamber arranged around the rotating body so as to alternately pass through the high-temperature heat medium chamber, and a high-pressure hydrogen inlet and a hydrogen outlet provided near the rotor, Each closed vessel comprises a hydrogen conduit connected to the high-pressure hydrogen inlet or the hydrogen outlet, and the connection between each hydrogen conduit and the high-pressure hydrogen inlet or the hydrogen outlet is such that one closed vessel is a high-temperature heat transfer medium chamber. So that the hydrogen conduit extending from the closed container communicates only with the high-pressure hydrogen inlet when the sealed container is in the low temperature heat transfer medium chamber, and the hydrogen conduit extends from the sealed container communicates only with the hydrogen outlet when the sealed container is in the low temperature heat transfer medium chamber. High-pressure hydrogen inlet as the hydrogen pipe rotates as the rotor rotates Heat pump apparatus which is characterized in that so as to be successively communicated or shut off from the hydrogen outlet and.
【請求項2】前記回転軸を中空とし、各密閉容器からの
水素導管を該回転軸内部を通して該回転軸の一端へ延設
し、該回転軸の一端に設けた高圧水素流入口または水素
流出口と接続したことを特徴とする特許請求の範囲第1
項記載の装置。
2. A high-pressure hydrogen inlet or a hydrogen flow provided at one end of the rotary shaft, wherein the rotary shaft is hollow, and a hydrogen conduit from each closed container is extended through the inside of the rotary shaft to one end of the rotary shaft. Claim 1 characterized in that it is connected to an outlet.
The device according to the item.
JP28958485A 1985-12-23 1985-12-23 Heat pump device Expired - Lifetime JPH0610567B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28958485A JPH0610567B2 (en) 1985-12-23 1985-12-23 Heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28958485A JPH0610567B2 (en) 1985-12-23 1985-12-23 Heat pump device

Publications (2)

Publication Number Publication Date
JPS62147266A JPS62147266A (en) 1987-07-01
JPH0610567B2 true JPH0610567B2 (en) 1994-02-09

Family

ID=17745123

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28958485A Expired - Lifetime JPH0610567B2 (en) 1985-12-23 1985-12-23 Heat pump device

Country Status (1)

Country Link
JP (1) JPH0610567B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7805833B2 (en) * 2022-03-18 2026-01-26 株式会社豊田中央研究所 Rotary Adsorption Device

Also Published As

Publication number Publication date
JPS62147266A (en) 1987-07-01

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