JPS6047516B2 - metal hydride equipment - Google Patents
metal hydride equipmentInfo
- Publication number
- JPS6047516B2 JPS6047516B2 JP55168666A JP16866680A JPS6047516B2 JP S6047516 B2 JPS6047516 B2 JP S6047516B2 JP 55168666 A JP55168666 A JP 55168666A JP 16866680 A JP16866680 A JP 16866680A JP S6047516 B2 JPS6047516 B2 JP S6047516B2
- Authority
- JP
- Japan
- Prior art keywords
- metal hydride
- cylinder
- hydrogen
- heat exchange
- heat
- 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
Links
Classifications
-
- 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
- Y02E60/14—Thermal energy storage
-
- 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
-
- 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
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Hydrogen, Water And Hydrids (AREA)
Description
【発明の詳細な説明】
本発明は金属水素化物装置に関し、例えばヒートポンプ
装置や水素の圧縮機として利用てきる金属水素化物装置
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a metal hydride device, and relates to a metal hydride device that can be used, for example, as a heat pump device or a hydrogen compressor.
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−−、−J4八ワ」3
主ル仏/に、サ鉱八初r]■■nは一般に温度Tの函数
であつて、第1図に示すように温度が高い程、平衡分解
圧も大きい。It is known that certain metals and alloys exothermically absorb hydrogen to form metal hydrides, and that these metal hydrides reversibly and endothermically release hydrogen. ”3
In general, sako eight first r]■■n is a function of temperature T, and as shown in FIG. 1, the higher the temperature, the higher the equilibrium decomposition pressure.
近年、金属水素化物のこのような特性を利用してヒート
ポンプ等、種々の金属水素化物装置が提案されているが
、多くは、平衡分解圧特性の異なる金属水素化物をそれ
ぞれ熱交換器をなす密閉容器に充填し、一方の熱交換器
内の金属水素化物から吸熱的に水素を放出させると共に
、この水素を他方の熱交換器に導き、他方の金属水素化
物に吸蔵させる動作を各熱交換器について交互に繰返さ
せて、各熱交換器から金属水素化物の発熱又は吸熱をバ
ッチ式に出力として取出している。In recent years, various metal hydride devices such as heat pumps have been proposed by taking advantage of these characteristics of metal hydrides, but in most cases, metal hydrides with different equilibrium decomposition pressure characteristics are connected to each other in a hermetically sealed heat exchanger. Each heat exchanger fills a container, causes hydrogen to be released endothermically from the metal hydride in one heat exchanger, and leads this hydrogen to the other heat exchanger, where it is absorbed into the metal hydride in the other heat exchanger. The exothermic or endothermic heat generated by the metal hydride is output from each heat exchanger in a batch manner by repeating the process alternately.
従つて、このような装置においては、各熱交換器を交互
に加熱又は冷却するために複雑な熱媒回路とそのための
制御機構を要すると共に、熱媒回路の切換え時における
熱損失も無視できない。このために、金属水素化物を密
閉された通路内を連続的に移送し、この移送の過程て所
定の位置に配された熱交換部を通過させることにより、
熱J媒回路の切換えを不要として、連続的に動作させる
方法も提案されているが、二つの熱交換部が金属水素化
物の通路を介して接続されている場合、熱交換部間の水
素圧の差によつて水素が一部熱交換部間を流通し、従つ
て、各熱交換部において所i定の圧力レベルで金属水素
化物の水素の吸蔵、放出反応を行なわせることが困難な
こともある。Therefore, in such a device, a complicated heating medium circuit and a control mechanism therefor are required to alternately heat or cool each heat exchanger, and heat loss when switching the heating medium circuit cannot be ignored. For this purpose, the metal hydride is continuously transferred in a closed passage, and during this transfer it passes through a heat exchanger placed at a predetermined position.
A method of continuous operation without the need to switch the heat exchanger circuit has also been proposed, but when two heat exchange parts are connected via a metal hydride passage, the hydrogen pressure between the heat exchange parts Part of the hydrogen flows between the heat exchange sections due to the difference in pressure, and therefore it is difficult to cause the metal hydride to absorb and desorb hydrogen at a predetermined pressure level in each heat exchange section. There is also.
本発明は上記の問題を解決するためになされたものてあ
つて、金属水素化物を連続して移送し、少なくとも二つ
の異なる温度の熱交換部を通過させる過程で熱媒と熱交
換させ、従つて、複雑な熱媒回路やそのための制御機構
を要せすして、本質的に連続して動作する金属水素化物
装置において、熱交換部間を圧力的に遮断し、所定の圧
力に保つことがてきる金属水素化物装置を提供すること
を目的とする。本発明の金属水素化物装置は、密閉され
た第一のシリンダと、このシリンダ内で水素雰囲気下に
回転して金属水素化物を移送するスクリューと、この金
属水素化物が移送される過程で上記シリンダ壁又はスク
リュー壁を介して金属水素化物と熱交換する第一の熱交
換部と、この熱交換部に連通する水素管と、密閉された
第二のシリンダと、このシリンダ内で水素雰囲気下に回
転して上記金属水素化物を移送するスクリューと、この
金属水素化物が移送される過程で上記シリンダ壁又はス
クリュー壁を介して金属水素化物と熱交換する第二の熱
交換部と、この熱交換部に連通する水素管と、第一のシ
リンダの排出端から金属水素化物を受取り、密閉された
空間を輸送し、第二のシリンダの供給端に供給する金属
水素化物輸送部材とを有することを特徴とするものであ
る。The present invention has been made to solve the above problems, and the present invention has been made to continuously transfer a metal hydride and exchange heat with a heating medium in the process of passing through at least two heat exchange sections having different temperatures. Therefore, in metal hydride equipment that essentially operates continuously, requiring a complicated heat medium circuit and its control mechanism, it is difficult to maintain a predetermined pressure by pressure-blocking the heat exchange parts. The purpose of the present invention is to provide a metal hydride device that can perform the following steps. The metal hydride device of the present invention includes a first sealed cylinder, a screw that rotates in a hydrogen atmosphere within the cylinder to transfer the metal hydride, and a screw that rotates in the cylinder in a hydrogen atmosphere to transfer the metal hydride. A first heat exchange section that exchanges heat with the metal hydride through a wall or screw wall, a hydrogen pipe communicating with this heat exchange section, a sealed second cylinder, and a hydrogen atmosphere in the cylinder. a screw that rotates to transfer the metal hydride; a second heat exchange section that exchanges heat with the metal hydride through the cylinder wall or the screw wall during the process of transferring the metal hydride; and a metal hydride transport member that receives the metal hydride from the discharge end of the first cylinder, transports it through a sealed space, and supplies it to the supply end of the second cylinder. This is a characteristic feature.
以下に実施例を示す図面に基づいて本発明を説明する。The present invention will be described below based on drawings showing examples.
第2図に示すように、密閉された第一のシリンダ1内で
水素雰囲気下にスクリュー3が回転駆動され、金属水素
化物を移送する。この金属水素化物は供給口4からシリ
ンダ内に供給され、シリンダ末端の排出端5から金属水
素化物輸送部材6に供給される。第一のシリンダ1壁内
又はスクリュー3内には所定位置に熱媒流通路7が設け
られ、例えば高温熱媒が循環流通されて、シリンダ内を
移送される金属水素化物と熱交換する。この高温熱媒を
加熱源として金属水素化物を加熱して水素を放出させ、
又はこの高温熱源を吸熱源として金属水素化物を冷却し
つつ水素を吸蔵させるために、この熱交換部8にはシリ
ンダ内に連通する水素管9が設けられている。図面では
スクリューは主要な数個のねじ山を除いて記載が省略さ
れているが、これらねじ山はシリンダ内壁に接触しつつ
、又は近接しつつ回転し、かくして金属水素化物をねじ
溝に沿つてらせん状に移送する。図示した実施例におい
ては、金属水素化物輸送部材6は、第一のシリンダの排
出端に連通する球状、円筒状等の密閉容器10内にスク
リューの横断方向に回転軸11が支持され、この回転軸
から放射状に延びると共に、その周縁が容器の内壁と接
触しつつ、又は微細な隙間を有するように中子12が取
付けられて、回転軸と共に回転するように構成されてい
る。As shown in FIG. 2, a screw 3 is rotated in a hydrogen atmosphere in a sealed first cylinder 1 to transfer metal hydride. This metal hydride is supplied into the cylinder from the supply port 4, and is supplied to the metal hydride transport member 6 from the discharge end 5 at the end of the cylinder. A heat medium flow passage 7 is provided at a predetermined position within the wall of the first cylinder 1 or within the screw 3, and, for example, a high temperature heat medium is circulated and exchanged heat with the metal hydride transferred within the cylinder. Using this high-temperature heating medium as a heating source, the metal hydride is heated to release hydrogen,
Alternatively, in order to store hydrogen while cooling the metal hydride using this high-temperature heat source as a heat absorbing source, the heat exchange section 8 is provided with a hydrogen pipe 9 that communicates with the inside of the cylinder. In the drawing, the screw is omitted except for a few main threads, but these threads rotate while contacting or close to the inner wall of the cylinder, thus transporting the metal hydride along the thread groove. Transfer in a spiral. In the illustrated embodiment, the metal hydride transport member 6 has a rotating shaft 11 supported in a transverse direction of the screw in a closed container 10, such as a spherical or cylindrical shape, which communicates with the discharge end of the first cylinder. The core 12 extends radially from the shaft and is attached so that its peripheral edge is in contact with the inner wall of the container or has a minute gap, and is configured to rotate together with the rotation shaft.
従つて、第一のシリンダの排出端から排出される金属水
素化物は密閉容器6内において中子にすくい上げられ、
中子の回転によつて第二のシリンダ2の供給端13に供
給される。ここにおいて、容器内壁に臨む二つの中子に
よつて形成される空間14は圧力的に実質的に遮断され
ているため、第一と第二のシリンダも圧力的に遮断され
、このようにして第一と第二のシリンダ内が所定の圧力
レベルに維持される。第二のシリンダ2においても、金
属水素化物輸送部材が供給端13に供給した金属水素化
物はスクリュー15によつてシリンダ内を移送され、所
定位置の熱交換部16で熱媒流通路17に循環供給され
る熱媒と熱交換し、排出端18から排出される。Therefore, the metal hydride discharged from the discharge end of the first cylinder is scooped up into the core in the closed container 6,
The rotation of the core feeds the feed end 13 of the second cylinder 2. Here, since the space 14 formed by the two cores facing the inner wall of the container is substantially blocked in terms of pressure, the first and second cylinders are also blocked in terms of pressure, and in this way, A predetermined pressure level is maintained within the first and second cylinders. Also in the second cylinder 2, the metal hydride supplied to the supply end 13 by the metal hydride transport member is transferred inside the cylinder by the screw 15, and circulated to the heat medium flow path 17 at the heat exchange section 16 at a predetermined position. It exchanges heat with the supplied heat medium and is discharged from the discharge end 18.
上記熱交換部では、例えば低温熱媒により金属水素化物
が冷却され、従つて、熱交換部にはシリンダ内に連通す
る水素管19が設けられる。動作の一例を説明すると、
供給口から第一のシリンダ内に供給された金属水素化物
はスクリューによつて第一のシリンダ内を移送される間
に先ず”熱交換部8にて高温熱媒によつて加熱され、こ
の温度における高い平衡分解圧で水素を放出し、この水
素は水素導出管によつてシリンダ内から取出される。次
に、水素を放出した金属水素化物は輸送部材によつて第
一のシリンダと圧力的に遮断されて第二のシリンダの供
給端に供給される。この金属水素化物は、第一のシリン
ダにおけると同様に移送され、熱交換部16にて低温熱
媒によつて冷却されると共に、この熱交換部に低圧の水
素をシリンダ内に導入することにより、金属水素化物”
はこの水素を吸蔵する。従つて、この装置によれば低温
熱媒の温度における低い平衡分解圧の水素から高温熱媒
の温度における高い平衡分解圧の水素を得ることができ
、いわば水素圧縮機として機能する。金属水素化物は第
二のシリンダの排出端18から第一のシリンダの供給端
4へ密閉空間内を適宜手段により循環させることができ
、従つて、この場合には第一のシリンダの水素管9から
連続して高圧の水素を得ることができる。In the heat exchange section, the metal hydride is cooled by, for example, a low-temperature heating medium, and therefore, the heat exchange section is provided with a hydrogen pipe 19 that communicates with the inside of the cylinder. To explain an example of the operation,
The metal hydride supplied into the first cylinder from the supply port is first heated by a high-temperature heating medium in the heat exchange section 8 while being transferred through the first cylinder by the screw, and is heated to this temperature. Hydrogen is released at a high equilibrium decomposition pressure at The metal hydride is fed to the feed end of the second cylinder.This metal hydride is transferred in the same manner as in the first cylinder, cooled by a low temperature heat medium in the heat exchange section 16, and By introducing low-pressure hydrogen into the cylinder into this heat exchange section, metal hydride"
absorbs this hydrogen. Therefore, according to this device, hydrogen having a high equilibrium decomposition pressure at the temperature of the high-temperature heat medium can be obtained from hydrogen having a low equilibrium decomposition pressure at the temperature of the low-temperature heat medium, and functions as a so-called hydrogen compressor. The metal hydride can be circulated in a closed space by suitable means from the discharge end 18 of the second cylinder to the supply end 4 of the first cylinder, so that in this case the hydrogen pipe 9 of the first cylinder High-pressure hydrogen can be obtained continuously from
また、本発明の装置はヒートポンプとして機能させるこ
とができる。Furthermore, the device of the present invention can function as a heat pump.
第3図に冷房装置の概略図を示し、水素管9及び19は
圧縮機20を介して接続され、温度TLの低温熱交換部
16からは水素が除去されると共に、温度THの高温熱
交換部8に水素が加圧供給される。従つて、金属水素化
物は第一のシリンダ内を移送される過程で先ず高温熱交
換部にて温度THに冷却されつつ、水素を吸蔵し、金属
水素化物輸送部材6によつて圧力的に遮断されて第二の
シリンダの供給端に移送され、第二のシリンダの低温熱
交換部にて減圧水素雰囲気下におけれるので、温度TL
の熱媒から吸熱しつつ水素を放出する。温度Tしの熱媒
が冷却負荷に接続される(第1図)。水素を放出した金
属水素化物を第一のシリンダの供給端に循環することに
よつて、低温熱媒には連続して冷熱が与えられる。逆に
、低温熱交換部から水素を除去し、高温熱交換部に水素
を加圧供給すれは、金属水素化物は低温熱交換部にて加
熱されつつ水素を放出し、高温熱交換部にて発熱的に水
素を吸蔵するから、高温熱媒を加熱負荷に接続すること
により暖房装置として機能する。FIG. 3 shows a schematic diagram of the cooling system. Hydrogen pipes 9 and 19 are connected via a compressor 20, hydrogen is removed from the low temperature heat exchange section 16 at a temperature TL, and hydrogen is removed from the high temperature heat exchange section 16 at a temperature TH. Hydrogen is supplied to section 8 under pressure. Therefore, in the process of being transferred within the first cylinder, the metal hydride is first cooled to the temperature TH in the high-temperature heat exchange section, absorbs hydrogen, and is pressured shut off by the metal hydride transport member 6. is transferred to the supply end of the second cylinder and placed in a reduced pressure hydrogen atmosphere in the low temperature heat exchange section of the second cylinder, so that the temperature TL
It releases hydrogen while absorbing heat from the heat medium. A heating medium at a temperature T is connected to a cooling load (FIG. 1). By circulating the metal hydride that has released hydrogen to the feed end of the first cylinder, cold heat is continuously provided to the low temperature heating medium. Conversely, if hydrogen is removed from the low-temperature heat exchange section and hydrogen is supplied under pressure to the high-temperature heat exchange section, the metal hydride releases hydrogen while being heated in the low-temperature heat exchange section, and then is heated in the high-temperature heat exchange section. Since it absorbs hydrogen exothermically, it functions as a heating device by connecting a high-temperature heat medium to a heating load.
第4図は本発明の別の実施例を示し、第一と第二のシリ
ンダ1及び2は一体に形成されていると共に、第一と第
二のスクリュー3及び15も両シリンダに共通して一体
に形成され、第一のシリンダの排出端5から第二のシリ
ンダの供給端13に向つてスクリュー軸が漸次大きくさ
れ、これによつて熱交換部の間でシリンダ内壁とスクリ
ューのねじ溝との間の空隙を小さくし、金属水素化物を
圧縮しつつ移送することにより、第一と第二のシリンダ
間を圧力的に遮断している。FIG. 4 shows another embodiment of the present invention, in which the first and second cylinders 1 and 2 are integrally formed, and the first and second screws 3 and 15 are also common to both cylinders. The screw shaft is gradually enlarged from the discharge end 5 of the first cylinder to the supply end 13 of the second cylinder, so that the inner wall of the cylinder and the thread groove of the screw are connected between the heat exchange part. By reducing the gap between the first and second cylinders and transferring the metal hydride while compressing it, the first and second cylinders are pressure-blocked.
同時にスクリューのピッチを漸次小さくしてもよい。ま
た、所望ならば、第4図に示したように、各熱交換部を
挾んでスクリューの軸方向の両側において、金属水素化
物の移送方向にスクリュー軸を漸次大きくし、熱交換部
をシリンダ内において圧力的に遮断することもできる。At the same time, the pitch of the screw may be gradually reduced. If desired, as shown in Fig. 4, the screw shafts can be gradually enlarged in the direction of metal hydride transfer on both sides of the screw in the axial direction, sandwiching each heat exchange part, so that the heat exchange part can be moved into the cylinder. It is also possible to shut it off pressure-wise.
以上のように本発明の装置によれば、金属水素化物をシ
リンダ内を連続して移送しつつ、少なくとも二つの熱交
換部で熱交換させる際に、熱交換部は相互に圧力的に遮
断されているので、各熱交換部においては所定の圧力レ
ベルて金属水素化物の水素の吸蔵、放出を行なわせるこ
とができ、装置を小型化し得て、しかも効率が高い。As described above, according to the apparatus of the present invention, when the metal hydride is continuously transferred inside the cylinder and is subjected to heat exchange in at least two heat exchange sections, the heat exchange sections are pressure-blocked from each other. Therefore, in each heat exchange section, hydrogen can be stored and released from the metal hydride at a predetermined pressure level, and the device can be made smaller and more efficient.
第1図は金属水素化物の平衡分解圧特性を示し、第2図
は本発明の金属水素化物装置の一実施例を示す断面図、
第3図は本発明の装置をヒートポンプ装置として機能さ
せる場合の回路図、第4図は別の実施例を示す断面図て
ある。
1,2・・・・・シリンダ、3,15・・・・・・スク
リュー、4,13・・・・・・供給端、5,18・・・
・・・排出端、6・・・・・・金属水素化物輸送部材、
7,17・・・・・・熱媒流通路、8,16・・・・・
・熱交換部、9,19・・・・・・水B素管、10・・
・・・密閉容器、11・・・・・・回転軸、12・・・
・中子、14・・・・・密閉空間、20・・・・・圧縮
機。FIG. 1 shows the equilibrium decomposition pressure characteristics of a metal hydride, and FIG. 2 is a sectional view showing an embodiment of the metal hydride device of the present invention.
FIG. 3 is a circuit diagram when the device of the present invention functions as a heat pump device, and FIG. 4 is a sectional view showing another embodiment. 1, 2... Cylinder, 3, 15... Screw, 4, 13... Supply end, 5, 18...
...Discharge end, 6...Metal hydride transport member,
7, 17... Heat medium flow path, 8, 16...
・Heat exchange section, 9, 19... Hydrogen B tube, 10...
... Airtight container, 11 ... Rotating shaft, 12 ...
- Core, 14... closed space, 20... compressor.
Claims (1)
素雰囲気下に回転して金属水素化物を移送するスクリュ
ーと、この金属水素化物が移送される過程で上記シリン
ダ壁又はスクリュー壁を介して金属水素化物と熱交換す
る第一の熱交換部と、この熱交換部に連通する水素管と
、密閉された第二のシリンダと、このシリンダ内で水素
雰囲気下に回転して上記金属水素化物を移送するスクリ
ューと、この金属水素化物が移送される過程で上記シリ
ンダ壁又はスクリュー壁を介して金属水素化物と熱交換
する第二の熱交換部と、この熱交換部に連通する水素管
と、第一のシリンダの排出端から金属水素化物を受取り
、密閉された空間を輸送し、第二のシリンダの供給端に
供給する金属水素化物輸送部材とを有することを特徴と
する金属水素化物装置。1 A sealed first cylinder, a screw that rotates in a hydrogen atmosphere within this cylinder to transfer a metal hydride, and a metal hydride that is transferred through the cylinder wall or the screw wall in the process of transferring the metal hydride. A first heat exchange section that exchanges heat with the hydride, a hydrogen pipe communicating with this heat exchange section, a sealed second cylinder, and a cylinder that rotates in a hydrogen atmosphere in this cylinder to exchange the metal hydride. A screw for transferring, a second heat exchange section that exchanges heat with the metal hydride through the cylinder wall or the screw wall during the process of transferring the metal hydride, and a hydrogen pipe communicating with the heat exchange section; 1. A metal hydride transporting member that receives metal hydride from a discharge end of a first cylinder, transports the metal hydride through a closed space, and supplies the metal hydride to a supply end of a second cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55168666A JPS6047516B2 (en) | 1980-11-29 | 1980-11-29 | metal hydride equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55168666A JPS6047516B2 (en) | 1980-11-29 | 1980-11-29 | metal hydride equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5792691A JPS5792691A (en) | 1982-06-09 |
| JPS6047516B2 true JPS6047516B2 (en) | 1985-10-22 |
Family
ID=15872241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55168666A Expired JPS6047516B2 (en) | 1980-11-29 | 1980-11-29 | metal hydride equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6047516B2 (en) |
-
1980
- 1980-11-29 JP JP55168666A patent/JPS6047516B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5792691A (en) | 1982-06-09 |
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