JPH0560423A - Hydrogen adsorbing/discharging device and heat-exchanger - Google Patents

Hydrogen adsorbing/discharging device and heat-exchanger

Info

Publication number
JPH0560423A
JPH0560423A JP3244353A JP24435391A JPH0560423A JP H0560423 A JPH0560423 A JP H0560423A JP 3244353 A JP3244353 A JP 3244353A JP 24435391 A JP24435391 A JP 24435391A JP H0560423 A JPH0560423 A JP H0560423A
Authority
JP
Japan
Prior art keywords
hydrogen
storage alloy
heat
hydrogen storage
wall
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
Application number
JP3244353A
Other languages
Japanese (ja)
Inventor
Seiji Ikeda
清二 池田
Koji Akashi
幸治 明石
Masato Osumi
正人 大隅
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP3244353A priority Critical patent/JPH0560423A/en
Publication of JPH0560423A publication Critical patent/JPH0560423A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Abstract

PURPOSE:To increase the efficiency of heat-exchange by performing fine adjustment of the temperature of a hydrogen storage alloy. CONSTITUTION:A tubular outer wall 4 formed of a material having excellent thermal conductivity and having a hollow part formed at the interior, a particulate-form hydrogen storage alloy 3 with which the hollow part of the outer wall 4 is filled, a heating means 6 contained togetherwith the hydrogen storage alloy 3, and a rod-form hydrogen filter 7 to adsorb and discharge hydrogen are provided. Heat insulating materials 8 arranged to both ends of the hollow part of the outer wall 4 to uniformize the temperature of the hydrogen storage alloy 3 by heating the heating means 6, and a hydrogen absorbing discharging pipe 5 formed to the one end of the outer wall 4 to communicate hydrogen, adsorbed and discharged by the hydrogen storage alloy 3, to the outside through the hydrogen filter 7 are provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、水素吸蔵合金を利用し
て冷熱または温熱を発生する水素吸放出装置およびこの
水素吸放出装置を用いた熱交換器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogen absorbing / releasing device that uses a hydrogen absorbing alloy to generate cold heat or warm heat, and a heat exchanger using this hydrogen absorbing / releasing device.

【0002】[0002]

【従来の技術】近年、太陽熱あるいは各種廃熱を利用し
て水素吸蔵合金による冷暖房装置およびそれに伴う水素
吸蔵合金の反応熱を利用した熱交換器が種々提案されて
いる。その一例として、特開昭60ー69465号公報
には、冷暖房装置の具体的なものとして、次に説明する
ものがある。
2. Description of the Related Art In recent years, various cooling and heating devices using hydrogen storage alloys utilizing solar heat or various waste heats and heat exchangers utilizing the reaction heat of the hydrogen storage alloys have been proposed. As one example thereof, Japanese Patent Application Laid-Open No. 60-69465 discloses a cooling / heating device described below.

【0003】この装置は熱交換器を相互に貫通して、加
熱あるいは放熱を行わせる一連の空気管を配設し、この
一連の管路に設けた数個のダンパを調整して加熱、冷却
を相互にするものである。そして、各熱交換器に設けら
れる水素吸放出装置1は、図5の横断面図および図6の
A−A′断面図に示すように、内部にセラミック等の多
孔質管よりなるフィルタ2を囲んで多孔質金属体および
微粉状の水素吸蔵合金3を充填したステンレス鋼製のフ
ィン付きチューブとしている。なお、4は外壁を示し、
5は水素吸放出管を示し、フィンは図示省略している。
上記した水素吸放出装置1は、外箱の中に18本束ね
て、収容されて熱交換器を形成している。
In this device, a series of air pipes for heating or radiating heat are arranged so as to penetrate through the heat exchanger, and several dampers provided in the series of pipe lines are adjusted to heat and cool. Are mutually exclusive. As shown in the cross-sectional view of FIG. 5 and the AA ′ cross-sectional view of FIG. 6, the hydrogen absorption / desorption device 1 provided in each heat exchanger has a filter 2 made of a porous tube such as ceramic inside. A stainless steel finned tube filled with a porous metal body and a fine powdery hydrogen storage alloy 3 is surrounded. In addition, 4 shows an outer wall,
Reference numeral 5 denotes a hydrogen absorbing / releasing pipe, and fins are not shown.
The above-mentioned hydrogen absorbing / releasing device 1 is formed by bundling 18 hydrogens in an outer box to form a heat exchanger.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記し
た熱交換器は高温空気管路と放熱空気管路とを切替え
て、加熱、冷却が繰り返されるため、構造が複雑となる
上に周辺のダクト等のスペースが大きくなるという問題
がある。
However, in the above heat exchanger, the heating and cooling are repeated by switching between the hot air passage and the heat radiating air passage, so that the structure becomes complicated and the surrounding ducts, etc. There is a problem that the space of becomes large.

【0005】また、高温空気の循環により水素の放出制
御をさせるために熱交換器に用いられる水素吸放出装置
1の水素吸蔵合金3の温度,出熱(水素移動量)の微調
整が困難である等の欠点がある。さらに、水素吸放出装
置1の水素吸蔵合金3に対して一様に加熱することが困
難で温度分布にむらが生じ熱交換が効率的でないという
問題がある。
Further, it is difficult to finely adjust the temperature and heat output (hydrogen transfer amount) of the hydrogen storage alloy 3 of the hydrogen storage / release device 1 used in the heat exchanger for controlling the release of hydrogen by circulating the high temperature air. There are some drawbacks. Further, there is a problem that it is difficult to uniformly heat the hydrogen storage alloy 3 of the hydrogen storage / release device 1 and the temperature distribution becomes uneven so that the heat exchange is not efficient.

【0006】そこで、本発明はコンパクトで、かつ、水
素吸蔵合金への熱の供給が効率的な水素吸放出装置およ
び熱交換器を提供することを目的とする。
Therefore, an object of the present invention is to provide a hydrogen absorbing / releasing device and a heat exchanger that are compact and that can efficiently supply heat to the hydrogen absorbing alloy.

【0007】[0007]

【課題を解決するための手段】本発明は、熱伝導性良好
な材料により形成され内部に中空部分を備えるチューブ
状の外壁と、この外壁の中空部分に充填された微粉状の
水素吸蔵合金と、この水素吸蔵合金と共に前記中空部分
に収納された加熱手段および水素を吸放出するための棒
状の水素フィルタと、前記加熱手段の加熱により前記水
素吸蔵合金を均一温度とするために前記外壁中空部両端
部に配置された断熱材と、前記水素フィルタを介して前
記水素吸蔵合金が吸放出する水素を外部と連通するため
の前記チューブの一端に形成された水素吸放出装置とし
たものである。また、前記水素吸放出装置を複数個積層
し、これら複数個の水素吸放出装置が伝熱促進用フィン
を貫通して形成する熱交換器を設けるようにしたもので
ある。
The present invention provides a tubular outer wall formed of a material having good thermal conductivity and having a hollow portion inside, and a fine powder hydrogen storage alloy filled in the hollow portion of the outer wall. A heating means housed in the hollow portion together with the hydrogen storage alloy, and a rod-shaped hydrogen filter for absorbing and releasing hydrogen, and the outer wall hollow portion for heating the hydrogen storage alloy to a uniform temperature by the heating means. The hydrogen absorbing / releasing device is formed at one end of the tube for communicating the hydrogen absorbed and released by the hydrogen absorbing alloy with the heat insulating material arranged at both ends and the hydrogen filter. In addition, a plurality of the hydrogen absorbing / releasing devices are laminated, and a heat exchanger is provided in which the plurality of hydrogen absorbing / releasing devices are formed by penetrating the heat transfer promoting fins.

【0008】[0008]

【作用】上記構成により、水素吸蔵合金の内部に収納さ
れた加熱手段により加熱するため水素吸蔵合金の温度の
微調節ができる。また、チューブ内部の両端に断熱材を
配置したので水素吸蔵合金の温度が均一となり水素吸蔵
合金への熱の供給が効率的に行える。また、上記水素吸
放出装置を複数個放熱フィンを介して積層することによ
り、熱交換効率が高くコンパクトな熱交換器となる。
With the above structure, the temperature of the hydrogen storage alloy can be finely adjusted because it is heated by the heating means housed inside the hydrogen storage alloy. Further, since the heat insulating materials are arranged at both ends inside the tube, the temperature of the hydrogen storage alloy becomes uniform and the heat can be efficiently supplied to the hydrogen storage alloy. Further, by stacking a plurality of the hydrogen absorbing / releasing devices via the radiation fins, a heat exchanger having high heat exchange efficiency and a compact size can be obtained.

【0009】[0009]

【実施例】以下、本発明の実施例を図面を参照して説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0010】図1は、本発明の一実施例を示す水素吸放
出装置の横断面図、図2は、図1のBーB′断面図であ
る。本実施例の水素吸放出装置1は、円筒状の外壁4
と、この外壁4に充填された微粉状の水素吸蔵合金3
と、外壁4の長手方向に沿って微粉状の水素吸蔵合金3
のほぼ中央部にヒータ6と水素フィルタ7とを配置し、
外壁4の内部の両端に設けた断熱材8と、水素吸放出管
5とで形成されている。
FIG. 1 is a cross-sectional view of a hydrogen absorbing / releasing device showing an embodiment of the present invention, and FIG. 2 is a BB 'sectional view of FIG. The hydrogen absorbing / releasing device 1 of the present embodiment has a cylindrical outer wall 4
And the fine powdery hydrogen storage alloy 3 filled in the outer wall 4
And a fine hydrogen storage alloy 3 along the longitudinal direction of the outer wall 4.
The heater 6 and the hydrogen filter 7 are arranged almost in the center of
It is formed of a heat insulating material 8 provided at both ends inside the outer wall 4 and a hydrogen absorbing / releasing pipe 5.

【0011】微粉状の水素吸蔵合金3は、図3に示す如
くの水素圧力−温度平衡特性を有し、例えば、図示破線
に対応して加熱時の温度150°Cとすると、平衡圧力
は加圧され9atmとなり、また、放熱時の温度35°
Cでは平衡圧力は降下して0.8atmとなるものを用
いている。外壁4は、熱伝導性の良好なアルミなどのチ
ューブ状となっている。ヒータ6は、微粉状の水素吸蔵
合金3の長手方向に収納され、ヒータ6の両端に断熱材
8を取付けて微粉状水素吸蔵合金3を一様に加熱してい
る。水素フィルタ7は、ヒータ6に接して水素吸放出装
置1の長手方向に収納された棒状の多孔質からなる焼結
金属を用いている。水素吸放出管5は、外壁4の一端に
配置され、水素を吸入または放出する。なお、水素フィ
ルタ7は水素吸放出管5から最も遠い、つまり、奥の部
分でも水素吸放出管5と接する近い部分と同様に水素吸
蔵合金3から均一に水素が吸放出できるようになってい
る。
The fine powder hydrogen storage alloy 3 has a hydrogen pressure-temperature equilibrium characteristic as shown in FIG. 3. For example, when the heating temperature is 150 ° C. corresponding to the broken line in the drawing, the equilibrium pressure is applied. The pressure is 9 atm, and the temperature when releasing heat is 35 °
In C, the equilibrium pressure drops to 0.8 atm. The outer wall 4 is in the shape of a tube of aluminum or the like having good heat conductivity. The heater 6 is housed in the longitudinal direction of the fine powdery hydrogen storage alloy 3, and heat insulating materials 8 are attached to both ends of the heater 6 to uniformly heat the fine powdery hydrogen storage alloy 3. The hydrogen filter 7 uses a rod-shaped porous sintered metal that is in contact with the heater 6 and is housed in the hydrogen absorbing / releasing device 1 in the longitudinal direction. The hydrogen absorbing / releasing pipe 5 is arranged at one end of the outer wall 4 and sucks or releases hydrogen. The hydrogen filter 7 is farthest from the hydrogen absorbing / releasing tube 5, that is, even in the inner portion, hydrogen can be uniformly absorbed and released from the hydrogen storage alloy 3 as in the near portion in contact with the hydrogen absorbing / releasing tube 5. ..

【0012】上記構成の水素吸放出装置1では、ヒータ
6により加熱すれば微粉状水素吸蔵合金3が平衡状態か
ら図3に示した水素圧力−温度特性に従って、水素を水
素フィルタ7を介して水素吸放出管5より放出して吸熱
反応となり、また、逆に水素吸放出管5より水素フィル
タ7を介して微粉状の水素吸蔵合金3が水素を吸収する
とき発熱反応となる。この場合、ヒータ6の加熱手段
で、均一に加熱し、かつ、ヒータ6の両端部を断熱材8
を設けているためヒータ6の両端部が中央部に比べ放熱
により低温となることがなく微粉状の水素吸蔵合金3の
温度分布にむらがなく熱交換が効率的にできる。
In the hydrogen absorbing / releasing device 1 having the above-mentioned structure, when heated by the heater 6, the fine powder hydrogen absorbing alloy 3 is brought from the equilibrium state to hydrogen through the hydrogen filter 7 according to the hydrogen pressure-temperature characteristic shown in FIG. When the fine powdery hydrogen storage alloy 3 absorbs hydrogen from the hydrogen absorption / desorption tube 5 via the hydrogen filter 7, it becomes an exothermic reaction. In this case, the heating means of the heater 6 uniformly heats and both ends of the heater 6 are covered with the heat insulating material 8.
Since the heater 6 is provided, both ends of the heater 6 do not have a lower temperature than the central part due to heat radiation, and the temperature distribution of the fine powdery hydrogen storage alloy 3 is uniform and heat exchange can be efficiently performed.

【0013】一方、微粉状の水素吸蔵合金3が水素を吸
収するときの反応熱は、外壁4および水素フィルタ7を
伝って均一に分散して放熱することができる。また、従
来例で説明した高温空気の循環により水素の放出制御す
る場合に比べ、本実施例では、ヒータ6の加熱手段によ
り制御しているため水素移動量の微調整が容易にでき
る。このように本実施例によれば、微粉状の水素吸蔵合
金3の水素の放出または吸収を円滑に効率的に実施する
ことができる。
On the other hand, the reaction heat when the fine powdery hydrogen storage alloy 3 absorbs hydrogen can be dissipated and evenly dissipated through the outer wall 4 and the hydrogen filter 7. Further, as compared with the case where the release of hydrogen is controlled by circulating the high temperature air described in the conventional example, in this embodiment, since the control is performed by the heating means of the heater 6, the fine adjustment of the hydrogen transfer amount can be easily performed. As described above, according to this embodiment, it is possible to smoothly and efficiently release or absorb hydrogen in the fine powdery hydrogen storage alloy 3.

【0014】図4は、図1および図2の水素吸放出装置
1を実装した熱交換器の斜視図である。
FIG. 4 is a perspective view of a heat exchanger in which the hydrogen absorbing / releasing device 1 of FIGS. 1 and 2 is mounted.

【0015】本実施例の熱交換器9は、水素吸放出装置
1の長手方向を水平にして縦方向および横方向に適宜間
隔で複数の微粉状水素吸蔵合金3を積層して配置し、こ
れらの水素吸放出装置1は、適宜間隔で設けた複数のフ
ィン10を貫通して形成している。さらに、フィン10
の上部には、上板11aとフィン10の下部には、下板
11bとが取り付けられ、それぞれの水素吸放出装置1
の一端は、水素吸放出管5に接続され、この水素吸放出
管5は他の熱交換器9と水素の吸放出するための連通管
12に接続している。なお、上記フィン10は各水素吸
放出装置1の伝熱促進用でアルミ等の熱伝導度の高い材
料とし、上板11aと下板11bは、熱交換のときの通
風路を形成するために設けている。
In the heat exchanger 9 of this embodiment, a plurality of fine hydrogen storage alloys 3 are laminated and arranged with the longitudinal direction of the hydrogen absorption / desorption device 1 horizontal and the longitudinal and lateral directions at appropriate intervals. The hydrogen absorbing / releasing device 1 is formed by penetrating a plurality of fins 10 provided at appropriate intervals. Furthermore, the fin 10
An upper plate 11a is attached to the upper part of the fins, and a lower plate 11b is attached to the lower parts of the fins 10.
One end of is connected to a hydrogen absorbing / releasing pipe 5, and this hydrogen absorbing / releasing pipe 5 is connected to another heat exchanger 9 and a communication pipe 12 for absorbing / releasing hydrogen. The fins 10 are made of a material having high thermal conductivity such as aluminum for promoting heat transfer of each hydrogen absorbing / releasing device 1, and the upper plate 11a and the lower plate 11b form a ventilation passage for heat exchange. It is provided.

【0016】次に、上記構成の熱交換器9を利用した冷
却システムの1例を示すと次のようになる。
Next, an example of the cooling system using the heat exchanger 9 having the above-mentioned structure is as follows.

【0017】この冷却システムでは、一方に2個の熱交
換器9を連通管12で接続して配設して1組とし、他方
に、上記同様の構成の熱交換器9を2個1組として設け
る。上記一方の熱交換器9には、異なった組成の2種類
の微粉状の水素吸蔵合金3をそれぞれ封入した水素吸放
出装置1を実装する。そして、ヒータ6の加熱手段によ
り2個1組の一方を熱交換器9の水素吸放出装置1を均
一に加熱して水素放出させて吸熱反応させているとき、
連通する熱交換器9の水素吸放出装置1は、水素を吸蔵
して放熱するがフィン10等の空冷により効率的に均一
に発散される。逆に、このとき2個1組の他方の熱交換
器9の水素吸放出装置1では、水素を吸蔵し上記同様に
空冷放熱がされ、これに連通する熱交換器9の水素吸放
出装置1では、ヒータ6の加熱手段により水素を放出し
て吸熱反応をする。上記した2個1組からなる熱交換器
9の動作を交互に繰返し、連続的に冷却を行うことによ
り、熱交換効率の高い冷却装置とすることができる。
In this cooling system, two heat exchangers 9 are connected to each other by a communication pipe 12 and arranged to form one set, and on the other side, two heat exchangers 9 having the same structure as the above are set one by one. It is provided as. On one of the heat exchangers 9 is mounted a hydrogen absorbing / releasing device 1 in which two kinds of fine powdery hydrogen absorbing alloys 3 having different compositions are respectively enclosed. When the heating means of the heater 6 uniformly heats the hydrogen absorbing / releasing device 1 of the heat exchanger 9 to heat one of the pair of two to cause hydrogen to be released and endothermic reaction,
The hydrogen absorbing / releasing device 1 of the heat exchanger 9 in communication occludes and radiates hydrogen, but is efficiently and uniformly radiated by air cooling of the fins 10 and the like. On the contrary, at this time, in the hydrogen absorbing / releasing device 1 of the other heat exchanger 9 of the pair of two, the hydrogen absorbing / releasing device 1 of the heat exchanger 9 which occludes hydrogen and radiates heat by air cooling in the same manner as described above. Then, the heating means of the heater 6 releases hydrogen to cause an endothermic reaction. By repeating the operation of the heat exchanger 9 consisting of two pieces as described above alternately and continuously performing cooling, a cooling device having high heat exchange efficiency can be obtained.

【0018】[0018]

【発明の効果】以上説明したように本発明によれば、水
素吸放出装置の加熱手段により水素吸蔵合金の温度、出
熱(水素移動量)の微調節ができる。さらに、水素吸放
出装置の水素吸蔵合金を一様に加熱して温度分布のむら
がないから熱の供給が効率的にできる。その上、この水
素吸放出装置を複数個用いた本発明による熱交換器は、
構成が簡単でコンパクトで熱交換効率が高いという効果
が得られる。
As described above, according to the present invention, the temperature of the hydrogen storage alloy and the heat output (hydrogen transfer amount) can be finely adjusted by the heating means of the hydrogen storage / release device. Furthermore, since the hydrogen storage alloy of the hydrogen storage / release device is uniformly heated and there is no uneven temperature distribution, heat can be efficiently supplied. Furthermore, the heat exchanger according to the present invention using a plurality of the hydrogen absorbing / releasing devices,
The effect is that the structure is simple and compact, and the heat exchange efficiency is high.

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

【図1】本発明の一実施例を示す水素吸放出装置の横断
面図。
FIG. 1 is a cross-sectional view of a hydrogen absorbing / releasing device showing an embodiment of the present invention.

【図2】図1のBーB′断面図。FIG. 2 is a sectional view taken along line BB ′ of FIG.

【図3】水素吸蔵合金の水素圧力−温度平衡特性を示す
説明図
FIG. 3 is an explanatory diagram showing hydrogen pressure-temperature equilibrium characteristics of a hydrogen storage alloy.

【図4】本発明の水素吸蔵合金を用いた熱交換器の1例
を示す斜視図。
FIG. 4 is a perspective view showing an example of a heat exchanger using the hydrogen storage alloy of the present invention.

【図5】従来の水素吸放出装置を示す横断面図。FIG. 5 is a cross-sectional view showing a conventional hydrogen absorbing / releasing device.

【図6】図5のA−A′断面図。6 is a sectional view taken along the line AA ′ in FIG.

【符号の説明】[Explanation of symbols]

1 水素吸放出装置 3 水素吸蔵合金 4 外壁 5 水素吸放出管 6 ヒータ 7 水素フィルタ 8 断熱材 10 フィン 11a 上板 11b 下板 12 連通管 DESCRIPTION OF SYMBOLS 1 Hydrogen absorbing / releasing device 3 Hydrogen absorbing alloy 4 Outer wall 5 Hydrogen absorbing / releasing pipe 6 Heater 7 Hydrogen filter 8 Heat insulating material 10 Fins 11a Upper plate 11b Lower plate 12 Communication pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱伝導性良好な材料により形成され内部
に中空部分を備えるチューブ状の外壁と、 この外壁の中空部分に充填された微粉状の水素吸蔵合金
と、 この水素吸蔵合金と共に前記中空部分に収納された加熱
手段および水素を吸放出するための棒状の水素フィルタ
と、 前記加熱手段の加熱により前記水素吸蔵合金を均一温度
とするために前記外壁中空部両端部に配置された断熱材
と、 前記水素フィルタを介して前記水素吸蔵合金が吸放出す
る水素を外部と連通するための前記チューブの一端に形
成された水素吸放出管とを備えることを特徴とする水素
吸放出装置。
1. A tubular outer wall formed of a material having good thermal conductivity and having a hollow portion inside, a fine powder hydrogen storage alloy filled in the hollow portion of the outer wall, and the hollow body together with the hydrogen storage alloy. A heating means housed in a portion and a rod-shaped hydrogen filter for absorbing and releasing hydrogen, and a heat insulating material arranged at both ends of the hollow portion of the outer wall so as to make the hydrogen storage alloy have a uniform temperature by heating by the heating means. And a hydrogen absorption / desorption tube formed at one end of the tube for communicating hydrogen absorbed / desorbed by the hydrogen storage alloy with the outside through the hydrogen filter.
【請求項2】前記請求項1記載の水素吸放出装置を複数
個積層し、これら複数個の水素吸放出装置が伝熱促進用
フィンを貫通して形成していることを特徴とする熱交換
器。
2. A heat exchange characterized in that a plurality of hydrogen absorbing / releasing devices according to claim 1 are laminated, and the plurality of hydrogen absorbing / releasing devices are formed by penetrating heat transfer promoting fins. vessel.
JP3244353A 1991-08-31 1991-08-31 Hydrogen adsorbing/discharging device and heat-exchanger Pending JPH0560423A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3244353A JPH0560423A (en) 1991-08-31 1991-08-31 Hydrogen adsorbing/discharging device and heat-exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3244353A JPH0560423A (en) 1991-08-31 1991-08-31 Hydrogen adsorbing/discharging device and heat-exchanger

Publications (1)

Publication Number Publication Date
JPH0560423A true JPH0560423A (en) 1993-03-09

Family

ID=17117442

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3244353A Pending JPH0560423A (en) 1991-08-31 1991-08-31 Hydrogen adsorbing/discharging device and heat-exchanger

Country Status (1)

Country Link
JP (1) JPH0560423A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5797269A (en) * 1996-02-23 1998-08-25 Sanyo Electric Co., Ltd. Hydrogen storage containers
KR20020071572A (en) * 2001-03-07 2002-09-13 차승식 The Header stucture of an air conditioner and heating used of metal Hydride
WO2016009916A1 (en) * 2014-07-15 2016-01-21 株式会社豊田自動織機 Chemical heat storage apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5797269A (en) * 1996-02-23 1998-08-25 Sanyo Electric Co., Ltd. Hydrogen storage containers
US5987895A (en) * 1996-02-23 1999-11-23 Sanyo Electric Co., Ltd. Hydrogen storage containers
KR20020071572A (en) * 2001-03-07 2002-09-13 차승식 The Header stucture of an air conditioner and heating used of metal Hydride
WO2016009916A1 (en) * 2014-07-15 2016-01-21 株式会社豊田自動織機 Chemical heat storage apparatus

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