JPS61197899A - Metal hydride container - Google Patents

Metal hydride container

Info

Publication number
JPS61197899A
JPS61197899A JP60033699A JP3369985A JPS61197899A JP S61197899 A JPS61197899 A JP S61197899A JP 60033699 A JP60033699 A JP 60033699A JP 3369985 A JP3369985 A JP 3369985A JP S61197899 A JPS61197899 A JP S61197899A
Authority
JP
Japan
Prior art keywords
heat
container
metal hydride
hydrogen
heat insulation
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.)
Granted
Application number
JP60033699A
Other languages
Japanese (ja)
Other versions
JPH0224762B2 (en
Inventor
Shin Fujitani
伸 藤谷
Kazuhiko Harima
播磨 和彦
Naojiro Honda
本田 直二郎
Takashi Sakai
貴史 酒井
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 JP60033699A priority Critical patent/JPS61197899A/en
Publication of JPS61197899A publication Critical patent/JPS61197899A/en
Publication of JPH0224762B2 publication Critical patent/JPH0224762B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C11/00Use of gas-solvents or gas-sorbents in vessels
    • F17C11/005Use of gas-solvents or gas-sorbents in vessels for hydrogen
    • 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
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PURPOSE:To reduce the sensible heat loss through pressure container by arranging a heatexchanger comprised of a heat medium tube, a heat transmission fin and a hydrogen conduit in a pressure container while covering with heat insulation member the surface of which is coated with excellent heat insulation film. CONSTITUTION:In a metal hydride container, a heatexchange container 3 is contained through a heat insulation material 2 in a pressure container 1. In said container 3, a heat medium tube 6 is penetrated through a tubular container 5 for containing the metal hydride 4 while a hydrogen conduit 7 is fixed. In order to couple said tube 6 and conduit 7 with outer pipings 6' and 7', couplings 11, 12 of excellent heat insulation are employed. Since the heatexchanger 3 enclosed in the pressure container 1 will improve heat insulation in the pressure container 1, the heat insulation material 2 to be placed between the pressure container 1 and the heatexchanger 3 is applied with coating having excellent heat insulation and hard to transmit hydrogen.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は金属水素化物を利用して熱の貯蔵、取り出しを
行なうに好適な金属水素化物容器に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to a metal hydride container suitable for storing and extracting heat using a metal hydride.

(ロ)従来の技術 ある種の金属あるいは合金は水素と可逆的に反応するが
、この際に生じる反応熱を蓄熱等に利用しようという試
みが現在盤んになされ、熱交換機能を備えた金属水素化
物容器の各種提案が行なわれている。
(b) Conventional technology Certain metals or alloys react reversibly with hydrogen, but attempts to use the heat of reaction generated at this time for heat storage, etc., have currently been abandoned, and metals with heat exchange functions have been developed. Various proposals for hydride containers have been made.

しかし、従来のこの種の金属水素化物容器は。However, the conventional metal hydride container of this kind.

例えば、特開昭58−47989号公報の従来例に見ら
れるように、金属水素化物の充填されている耐圧容器と
熱交換器を別々に設け、その間をヒートパイプで接続す
るなど構造が複雑になる上、金属水素化物と耐圧容器が
直に接触するため耐圧容器を通しての熱損失が大きくな
る。また、金属水素化物とヒートパイプ間の熱伝達を良
くするためヒートパイプにその長手方向に垂直なフィン
を取り付けているが、水素ガスの吸収、放出を繰り返す
ことにより金属水素化物が微粉化したとき、そのフィン
と金属水素化物との接触が減少して熱交換機能が低下す
る欠点があった。
For example, as seen in the conventional example of JP-A No. 58-47989, the structure is complicated, such as installing a pressure-resistant container filled with metal hydride and a heat exchanger separately, and connecting them with a heat pipe. Moreover, since the metal hydride and the pressure vessel come into direct contact with each other, heat loss through the pressure vessel increases. In addition, vertical fins are attached to the heat pipe in the longitudinal direction to improve heat transfer between the metal hydride and the heat pipe, but when the metal hydride is pulverized due to repeated absorption and release of hydrogen gas. However, there was a drawback that the contact between the fins and the metal hydride was reduced and the heat exchange function was deteriorated.

一方、このような欠点を除くため、前記公報には、容器
外側にヒートパイプを配置し、その内側に金属水素化物
を充填して水素の吸収、放出を行なわせ、更に、前記ヒ
ートパイプの外側に熱交換器を取り付けて熱の貯蔵、取
り出しを行なう容器構成例についての提案がなされてい
るが、金属水素化物容器をこのように構成した場合には
耐圧容器本体による顕熱損失が大きくなる欠点があった
On the other hand, in order to eliminate such drawbacks, the above-mentioned publication discloses that a heat pipe is placed outside the container, a metal hydride is filled inside the container to absorb and release hydrogen, and the outside of the heat pipe is A proposal has been made for a container configuration in which a heat exchanger is attached to the container to store and extract heat, but if the metal hydride container is configured in this way, the disadvantage is that sensible heat loss due to the pressure container body becomes large. was there.

また、いずれの場合もヒートパイプを介して金属水素化
物と熱媒との間の熱交換を行なっているため、その分だ
け伝熱抵抗が増し畑熱損失が生じる上、伝熱速度が低下
する欠点もあった。
In addition, in both cases, heat exchange is performed between the metal hydride and the heat medium via a heat pipe, which increases heat transfer resistance, causes heat loss, and reduces heat transfer rate. There were also drawbacks.

(ハ)発明が解決しようとする問題点 本発明は耐圧容器による顕熱損失を減少させると共に、
金属水素化物と熱媒との間の伝熱状態を改善して熱交換
効率の良い金属水素化物容器を提供することを目的とす
る。
(c) Problems to be solved by the invention The present invention reduces sensible heat loss due to pressure-resistant containers, and
The purpose of the present invention is to provide a metal hydride container with high heat exchange efficiency by improving the heat transfer state between the metal hydride and the heat medium.

(ニ)問題点を解決するための手段 このため本発明は、熱媒管が気密に貫通する円筒容器内
部に、その軸方向に沿って伝熱フィンを配設すると共に
、金属水素化物を収納し、更にその円筒容器端部には水
素を通過させるフィルター付き水素導管を取り付けて熱
交換器を構成し、この熱交換器を断熱性の優れた被膜で
表面をコーティングした断熱材で覆って耐圧容器内に設
置し。
(d) Means for Solving the Problems Therefore, the present invention provides heat transfer fins along the axial direction inside a cylindrical container through which a heat medium pipe passes through in an airtight manner, and also houses a metal hydride. Furthermore, a hydrogen conduit with a filter is attached to the end of the cylindrical container to allow hydrogen to pass through to form a heat exchanger, and this heat exchanger is covered with a heat insulating material whose surface is coated with a film with excellent heat insulation properties to make it resistant to pressure. Place it inside the container.

その耐圧容器両端部より断熱性の優れた材質の接続継手
を介して熱媒管と水素導管を外部へ連通させるようにし
たことを特徴としている。
It is characterized in that the heat medium pipe and the hydrogen conduit are communicated with the outside from both ends of the pressure-resistant container via connection joints made of a material with excellent heat insulation properties.

(ホ)作用 熱の再生時に金属水素化物より熱媒管に伝えられた反応
熱は、熱媒管が耐圧容器と断熱されているため、耐圧容
器に伝導することなく熱媒に効率良く伝わり外部に取り
出される。また、熱交換器を包む断熱材中への水素の混
入が断熱材表面の被膜により抑制されるため、熱交換器
本体表面より耐圧容器への水素による伝熱が防止され、
熱損失が著しく減少する。
(e) During the regeneration of the heat of action, the heat of reaction transferred from the metal hydride to the heat medium tube is efficiently transferred to the heat medium without being conducted to the pressure vessel because the heat medium tube is insulated from the pressure vessel. It is taken out. In addition, since the infiltration of hydrogen into the heat insulating material surrounding the heat exchanger is suppressed by the coating on the surface of the heat insulating material, heat transfer due to hydrogen from the surface of the heat exchanger body to the pressure vessel is prevented.
Heat loss is significantly reduced.

(へ)実施例 以下1図面に示す実施例について、更に詳細に説明する
(F) EXAMPLE An example shown in one drawing will be described in more detail below.

各図は本発明の一実施例に係る金属水素化物容器の構成
図を示したもので、第1図はその側面図。
Each figure shows a configuration diagram of a metal hydride container according to an embodiment of the present invention, and FIG. 1 is a side view thereof.

第2図は正面断面図、第3図は側面断面図である。FIG. 2 is a front sectional view, and FIG. 3 is a side sectional view.

これらの図に示すように1本実施例の金属水素化物容器
は、耐圧容器1内部に断熱材2を介して熱交換容器3を
収容して成る。その熱交換容器3は、金属水素化物4を
収納する円筒容器5に熱媒管6が貫通配置されると共に
、水素導管7が取り付けられて成り、円筒容器5内部に
は金属水素化物4を密封するため、円筒容器5と水素導
管7の間および円筒容器5と熱媒管6の間には、シール
部材8および9が介挿される。
As shown in these figures, the metal hydride container of this embodiment includes a heat exchange container 3 housed inside a pressure-resistant container 1 with a heat insulating material 2 interposed therebetween. The heat exchange container 3 is made up of a cylindrical container 5 that houses a metal hydride 4, through which a heat medium pipe 6 is disposed, and a hydrogen conduit 7 attached.The metal hydride 4 is sealed inside the cylindrical container 5. For this purpose, seal members 8 and 9 are inserted between the cylindrical container 5 and the hydrogen conduit 7 and between the cylindrical container 5 and the heat medium pipe 6.

即ち、このシール部材8は、外周面にネジ溝が刻設され
た例えばステンレス類の円筒体より成り。
That is, the sealing member 8 is made of a cylindrical body made of stainless steel, for example, and has a threaded groove carved on its outer peripheral surface.

その内周面には予め水素導管7が固着される。この水素
導管7付きシール部材8を円筒容器5の端面に予め形成
されたネジ穴にネジ込む。これにより、水素導管7を円
筒容器5に気密に取り付けることができる。なお、水素
導管7の先端部には水素は通し得るが金属水素化物粉体
は通し得ないフィルター7aが形成されている。
A hydrogen conduit 7 is fixed in advance to its inner peripheral surface. This sealing member 8 with the hydrogen conduit 7 is screwed into a screw hole previously formed in the end face of the cylindrical container 5. Thereby, the hydrogen conduit 7 can be attached to the cylindrical container 5 in an airtight manner. Note that a filter 7a is formed at the tip of the hydrogen conduit 7, which allows hydrogen to pass through but not metal hydride powder.

一方、シール部材9は、シール部材8と同様その外周面
にはネジ溝が刻設されると共に、その内周面は軸方向先
端に向って心持ち広がるテーパー状に形成されている。
On the other hand, the seal member 9, like the seal member 8, is provided with a threaded groove on its outer circumferential surface, and its inner circumferential surface is formed in a tapered shape that gradually widens toward the axial tip.

このシール部材9を取り付ける熱媒管6の部分も、シー
ル扉材9の内周面のテーパー形状に対応して心持ち円筒
容器5内部に向って広がるテーパー状に形成されている
。従って。
The portion of the heat transfer pipe 6 to which the seal member 9 is attached is also formed in a tapered shape that widens toward the inside of the cylindrical container 5, corresponding to the tapered shape of the inner circumferential surface of the seal door member 9. Therefore.

円筒容器5の端面吊央部に□予め形成されているネジ穴
に熱−管6を通し、その熱媒管6にシール部材9を通し
て上記ネジ穴にシール部材9をネジ込んで行けば、熱媒
管6とシール部材9の間はそのテーパー形状の接合によ
り気密に固着され1円筒容器5とシール部材9の間は螺
合により気密が保たれる。
Pass the heat pipe 6 through a screw hole pre-formed in the center of the end surface of the cylindrical container 5, pass the seal member 9 through the heat medium pipe 6, and screw the seal member 9 into the screw hole to remove the heat. The medium pipe 6 and the sealing member 9 are airtightly fixed by their tapered joints, and the cylindrical container 5 and the sealing member 9 are kept airtight by screwing together.

このように、シール部材8および9を介して水素導管7
および熱媒管6が気菌に取り付けられた円筒容器5の内
部には金属水素化物4が収納されるが。
In this way, the hydrogen conduit 7
A metal hydride 4 is housed inside a cylindrical container 5 to which a heat medium pipe 6 is attached.

この金属水素化物4と熱媒管6との間の熱伝導を改善す
るために、熱媒′管6の軸方向に沿って熱媒管6から円
筒容i5に放射状に複数枚の伝熱フィン10が配設され
ている。
In order to improve heat conduction between the metal hydride 4 and the heat medium tube 6, a plurality of heat transfer fins are provided radially from the heat medium tube 6 to the cylindrical volume i5 along the axial direction of the heat medium tube 6. 10 are arranged.

一方、耐圧容器1側にはその内部に配設される熱媒管6
および水素導管7を外部配管6′および7′と接続する
ため、継手11.12が設けられる。この継手11は内
外周両面にネジ溝が刻設される一方。
On the other hand, on the side of the pressure vessel 1, there is a heat medium pipe 6 disposed inside the vessel.
Couplings 11.12 are provided for connecting the hydrogen conduit 7 and the external pipes 6' and 7'. This joint 11 has thread grooves carved on both the inner and outer circumferential surfaces.

継手12は外周面のみネジ溝が形成され、内周面には外
部配管6’ 、7’の先端部分が内周面軸方向途中まで
挿入固定されている。
The joint 12 has a threaded groove formed only on its outer circumferential surface, and the tip portions of the external pipes 6', 7' are inserted and fixed halfway in the axial direction of the inner circumferential surface.

これらの継手を用いて熱媒管6.水素導管7と外部配管
6’ 、7’ とを接続するには、耐圧容器1の端面1
aおよび蓋板1bの所定の位置に形成された各ネジ穴に
夫々先ず継手11をネジ込み固定する。次いで、外部配
管6’ 、?’ を固着した継手12を継手11の内側
にネジ込む。これにより、耐圧容器1と継手11の間お
よび継手11と継手12の間は螺合により気密が保たれ
る。このとき気密を更により完全なものにしたいと思え
ば、継手11のフランジ部と耐圧容器1との間、および
、継手11.12のフランジ間に弾性材でできたオーリ
ング13を介在させれば良い。また、各継手12と外部
配管6’ 、7’の間は、前以って行なわれる固着加工
により、更に、熱媒管6.水素導管7と継手12の間は
前述した熱媒管6とシール部材9間の接合の場合と同じ
要領で気密保持構造が形成される。
Using these joints, heat transfer pipe 6. To connect the hydrogen conduit 7 and the external piping 6', 7', the end face 1 of the pressure vessel 1 is
First, the joint 11 is screwed into each screw hole formed at a predetermined position in the cover plate 1b and the cover plate 1b. Next, external piping 6', ? ' Screw the fitting 12 with the screws fixed into the inside of the fitting 11. Thereby, airtightness is maintained between the pressure vessel 1 and the joint 11 and between the joints 11 and 12 due to the screw engagement. At this time, if you want to make the airtightness even more perfect, you can interpose an O-ring 13 made of an elastic material between the flange of the joint 11 and the pressure vessel 1, and between the flanges of the joints 11 and 12. Good. Furthermore, the heat medium pipes 6. and 6.0 are bonded between each joint 12 and the external pipes 6' and 7' by a fixing process performed in advance. An airtight structure is formed between the hydrogen conduit 7 and the joint 12 in the same manner as in the case of joining the heat medium pipe 6 and the seal member 9 described above.

ここで、継手を1142の2重構造にしているのは熱媒
管6.水素導管7と耐圧容器1間の断熱性を良くするた
めで、継手11を金属製に、また、継手12をテフロン
あるいは焼成したセラミックス製の断熱性の優れた材質
で形成することが好ましいが、継手11と12の材質を
その反対に用いて構成しても良い。
Here, the joint has a double structure of 1142 heat medium pipes 6. This is to improve the heat insulation between the hydrogen conduit 7 and the pressure vessel 1, and it is preferable that the joint 11 be made of metal and the joint 12 made of a material with excellent heat insulation such as Teflon or fired ceramics. The materials of the joints 11 and 12 may be reversed.

このようにして熱的にほぼ完全に外気と遮断され、耐圧
容器1内部に密封される熱交換容器3は。
In this way, the heat exchange vessel 3 is almost completely thermally isolated from the outside air and sealed inside the pressure vessel 1.

耐圧容器1内部における断熱性を向上するため、耐圧容
器lと熱交換容器3間に介在させる断熱材2は、表面が
水素を透過し難く、しかも断熱性に優れた被膜でコーテ
ィングされている。更に全体は耐圧容器lの本体部と蓋
板1bのフランジ接合により内部が密封されて金属水素
化物が構成される。
In order to improve the heat insulation inside the pressure vessel 1, the surface of the heat insulating material 2 interposed between the pressure vessel 1 and the heat exchange vessel 3 is coated with a film that is hardly permeable to hydrogen and has excellent heat insulation properties. Furthermore, the interior of the whole is sealed by flange joining of the main body of the pressure vessel 1 and the lid plate 1b to form a metal hydride.

以上の構成で、蓄熱時、外部配管6′から熱媒管6を流
れる熱媒からの熱は、熱媒管6の表面および伝熱フィン
10を介して金属水素化物4に均一に伝達される。この
とき、熱媒から耐圧容器1への熱伝導は、断熱性の継手
12により阻止されて熱交換容器3へ熱損失無く伝導さ
れ、金属水素化物4へ効率良く給熱される。この熱媒か
らの給熱により金属水素化物4は脱水素化して元の金属
に戻る。
With the above configuration, during heat storage, heat from the heat medium flowing through the heat medium pipe 6 from the external pipe 6' is uniformly transferred to the metal hydride 4 via the surface of the heat medium pipe 6 and the heat transfer fins 10. . At this time, heat conduction from the heat medium to the pressure vessel 1 is blocked by the heat insulating joint 12 and is conducted to the heat exchange vessel 3 without heat loss, thereby efficiently supplying heat to the metal hydride 4. The metal hydride 4 is dehydrogenated by the heat supplied from this heating medium and returns to the original metal.

また1発生した水素ガスはフィルター78を介して水素
導管7から外部配管7′へと取り出され、図示せぬ水素
ボンベへ貯えられる。一方、放熱時、外部配管7′から
水素導管7を通りフィルター7aを介して供給される水
素ガスは、金属水素化物4と給金して熱を発生する。こ
の発生した熱は断熱材2によって耐圧容器1への伝熱が
阻止され、全て伝熱フィン10および熱媒管6の表面か
らその内部を流れる熱媒へと伝達され、効率良く外部配
管6′へ取り出され利用される。
Further, the generated hydrogen gas is taken out from the hydrogen conduit 7 to the external pipe 7' via the filter 78 and stored in a hydrogen cylinder (not shown). On the other hand, during heat dissipation, hydrogen gas supplied from the external pipe 7' through the hydrogen conduit 7 and the filter 7a interacts with the metal hydride 4 to generate heat. This generated heat is prevented from being transferred to the pressure vessel 1 by the heat insulating material 2, and all of it is transferred from the surface of the heat transfer fins 10 and the heat medium pipe 6 to the heat medium flowing inside the heat transfer fin 10 and the heat medium pipe 6, and is efficiently transferred to the external pipe 6'. It is taken out and used.

このように、本実施例においては、円筒容器5にはシー
ル部材8,9を介在させて水素導管7.熱媒管6を配設
したので1円筒容器5内部が気密に保たれ、円筒容器5
からの水素ガスの洩れが防止される。また、断熱材2の
表面を水素が透過し難く。
As described above, in this embodiment, the seal members 8 and 9 are interposed in the cylindrical container 5, and the hydrogen conduit 7. Since the heat medium pipe 6 is provided, the inside of the cylindrical container 5 is kept airtight, and the cylindrical container 5
This prevents hydrogen gas from leaking from the Further, hydrogen is difficult to permeate through the surface of the heat insulating material 2.

断熱性の優れた被膜でコーティングしたので、たとえ円
筒容器5から水素ガスが洩れたとしてもその周囲の極く
僅かな範囲、fflに止まり、水素ガスを介しての熱損
失も未然に防止さ扛効率の良い熱交換が期待できる。ま
た、熱媒流路と耐圧容器lとの間および水素流路と耐圧
容器1との間には継手11.12を介在させたため、耐
圧容器1内部の気密が保たれると共に、熱媒管6あるい
は水素導管7から耐圧容器lへの熱損失も著しく減少し
、極めて熱効率の良い金属水素化物容器が得られる。
Since it is coated with a film with excellent heat insulation properties, even if hydrogen gas leaks from the cylindrical container 5, it will be confined to a very small area around it, and heat loss through the hydrogen gas will be prevented. Efficient heat exchange can be expected. In addition, since the joints 11 and 12 are interposed between the heat medium flow path and the pressure vessel 1 and between the hydrogen flow path and the pressure vessel 1, the airtightness inside the pressure vessel 1 is maintained, and the heat medium pipe 6 or the heat loss from the hydrogen conduit 7 to the pressure vessel 1 is also significantly reduced, resulting in a metal hydride vessel with extremely high thermal efficiency.

(ト)発明の効果 以上のように本発明によれば、熱媒流路および水素流路
から耐圧容器への伝熱が抑制され、同時に水素ガスによ
る熱交換容器本体より耐圧容器への伝熱も抑制されるた
め、耐圧容器による顕熱損失を著しく減少させることが
でき、熱交換効率の優れた金属水素化物容器が得られる
(G) Effects of the Invention As described above, according to the present invention, heat transfer from the heat medium flow path and the hydrogen flow path to the pressure vessel is suppressed, and at the same time, heat transfer from the heat exchange vessel body to the pressure vessel due to hydrogen gas is suppressed. Since this also suppresses sensible heat loss due to the pressure container, a metal hydride container with excellent heat exchange efficiency can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例に係る金属水素化物容器の側
面図、第2図はその正面A−^断面図、第3図はその側
面断面図である6 1・・・耐圧容器、 la・・・端面、1b・・・蓋板
。 2・・・断熱材、3・・・熱交換容器、4・・・金属水
素化物、5・・・円筒容器、6・・・熱媒管。 6’ 、7’  ・・・外部配管、7・・・水素導管、
 7a・・・ フィルター、8,9・・・シール部材、
10・・・伝熱フィン。 11.12・・・継手、13・・・オーリング。 S2図
FIG. 1 is a side view of a metal hydride container according to an embodiment of the present invention, FIG. 2 is a front sectional view taken along line A-^, and FIG. 3 is a side sectional view thereof. 6 1... Pressure-resistant container; la... end surface, 1b... lid plate. 2... Heat insulating material, 3... Heat exchange container, 4... Metal hydride, 5... Cylindrical container, 6... Heat medium tube. 6', 7'...External piping, 7...Hydrogen conduit,
7a... Filter, 8, 9... Seal member,
10...Heat transfer fin. 11.12...Joint, 13...O-ring. S2 figure

Claims (1)

【特許請求の範囲】[Claims] 熱媒管が気密に貫通する円筒容器内部に、その軸方向に
沿って伝熱フィンを配設すると共に、金属水素化物を収
納し、更にその円筒容器端部には水素を通過させるフィ
ルター付き水素導管を取り付けて熱交換器を構成し、こ
の熱交換器を断熱性の優れた被膜で表面をコーディング
した断熱材で覆って耐圧容器内に設置し、その耐圧容器
両端部より断熱性に優れた材質の接続継手を介して熱媒
管と水素導管を外部へ導出させて成ることを特徴とする
金属水素化物容器。
Heat transfer fins are arranged along the axial direction inside a cylindrical container through which a heat medium pipe passes airtight, and a metal hydride is housed inside the cylindrical container, and a hydrogen filter is installed at the end of the cylindrical container to allow hydrogen to pass through. A heat exchanger is constructed by attaching a conduit, and this heat exchanger is covered with a heat insulating material whose surface is coated with a film with excellent heat insulation properties, and is installed inside a pressure vessel. A metal hydride container characterized in that a heat medium pipe and a hydrogen pipe are led out to the outside through a connecting joint made of a material.
JP60033699A 1985-02-23 1985-02-23 Metal hydride container Granted JPS61197899A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60033699A JPS61197899A (en) 1985-02-23 1985-02-23 Metal hydride container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60033699A JPS61197899A (en) 1985-02-23 1985-02-23 Metal hydride container

Publications (2)

Publication Number Publication Date
JPS61197899A true JPS61197899A (en) 1986-09-02
JPH0224762B2 JPH0224762B2 (en) 1990-05-30

Family

ID=12393661

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60033699A Granted JPS61197899A (en) 1985-02-23 1985-02-23 Metal hydride container

Country Status (1)

Country Link
JP (1) JPS61197899A (en)

Also Published As

Publication number Publication date
JPH0224762B2 (en) 1990-05-30

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