JPH0224762B2 - - Google Patents

Info

Publication number
JPH0224762B2
JPH0224762B2 JP60033699A JP3369985A JPH0224762B2 JP H0224762 B2 JPH0224762 B2 JP H0224762B2 JP 60033699 A JP60033699 A JP 60033699A JP 3369985 A JP3369985 A JP 3369985A JP H0224762 B2 JPH0224762 B2 JP H0224762B2
Authority
JP
Japan
Prior art keywords
heat
hydrogen
metal hydride
pipe
container
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
JP60033699A
Other languages
Japanese (ja)
Other versions
JPS61197899A (en
Inventor
Shin Fujitani
Kazuhiko Harima
Naojiro Pponda
Takashi Sakai
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)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Hydrogen, Water And Hydrids (AREA)

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) Field of Industrial Application 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盛んになされ、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) Prior art Certain metals or alloys react reversibly with hydrogen, and attempts are currently being made to utilize the heat of reaction generated at this time for heat storage, etc. Various proposals for chemical containers have been made.

しかし、従来のこの種の金属水素化物容器は、
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インを取り付
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
イ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つた。
However, conventional metal hydride containers of this type
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つ
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. It was hot.

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つている
ため、その分だけ伝熱抵抗が増し顕熱損失が生じ
る上、伝熱速度が低下する欠点もあつた。
In addition, in both cases, heat exchange is performed between the metal hydride and the heating medium via the heat pipe, which increases heat transfer resistance, causes sensible heat loss, and reduces the heat transfer rate. There were also some 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 the sensible heat loss caused by the pressure vessel, improves the heat transfer state between the metal hydride and the heating medium, and produces a metal hydride with high heat exchange efficiency. The purpose is to provide a container.

(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、その軸方向に沿つて伝熱フインを
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透過させるフイルター
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
イングした断熱材で覆つて耐圧容器内に設置し、
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。
(d) Means for Solving the Problems Therefore, the present invention provides a method in which heat transfer fins are arranged along the axial direction inside a cylindrical container through which a heat medium tube passes through in an airtight manner, and a metal hydride is housed inside the cylindrical container. Furthermore, a hydrogen conduit with a filter that allows hydrogen to permeate is attached to the end of the cylindrical container 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 in a container,
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) Effect During heat regeneration, 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 and is transferred to the outside. It is taken out. In addition, the coating on the surface of the insulation material prevents hydrogen from entering the insulation material surrounding the heat exchanger, which prevents hydrogen from transferring heat from the surface of the heat exchanger body to the pressure vessel, significantly reducing heat loss. do.

(ヘ) 実施例 以下、図面に示す実施例について、更に詳細に
説明する。
(f) Examples The examples shown in the drawings 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、第2図は正面断面図、第3図は側面断面図で
ある。
Each figure shows a configuration diagram of a metal hydride container according to an embodiment of the present invention, in which FIG. 1 is a side view, 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、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
The cylindrical container 5 has a heat transfer pipe 6 inserted therethrough and a hydrogen conduit 7 attached to the cylindrical container 5 for storing the metal hydride 4. In order to seal the metal hydride 4 inside the cylindrical container 5, Seal members 8 and 9 are inserted between 5 and hydrogen conduit 7 and between cylindrical container 5 and 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製の円筒体より成
り、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
ないフイルター7aが形成されている。
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 circumferential surface, and the hydrogen conduit 7 is fixed in advance to its inner circumferential 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 through which hydrogen can pass 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つて心持ち広がるテーパー
状に形成されている。このシール部材9を取り付
ける熱媒管6の部分も、シール部材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
向つて広がるテーパー状に形成されている。従つ
て、円筒容器5の端面中央部に予め形成されてい
るネジ穴に熱媒管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、
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。
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. 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 member 9. Therefore, if the heat medium pipe 6 is passed through a screw hole previously formed in the center of the end face of the cylindrical container 5, the seal member 9 is passed through the heat medium pipe 6, and the seal member 9 is screwed into the screw hole. The heat medium pipe 6 and the seal member 9 are airtightly fixed by their tapered joint,
Airtightness is maintained between the cylindrical container 5 and the seal member 9 by screwing them 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が気密に取り付けられた
円筒容器5の内部には金属水素化物4が収納され
るが、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の軸方向に沿つ
て熱媒管6から円筒容器5に放射状に複数枚の伝
熱フイン10が配設されている。
In this way, the metal hydride 4 is stored inside the cylindrical container 5 to which the hydrogen conduit 7 and the heat medium tube 6 are airtightly attached via the seal members 8 and 9. In order to improve heat conduction between the heat medium pipe 6 and the heat medium pipe 6, a plurality of heat transfer fins 10 are arranged radially from the heat medium pipe 6 to the cylindrical container 5 along the axial direction of the heat medium pipe 6.

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、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。
On the other hand, on the pressure vessel 1 side, joints 11 and 12 are provided to connect the heat medium pipe 6 and hydrogen conduit 7 disposed inside the vessel to external pipes 6' and 7'. This joint 11 has thread grooves carved on both the inner and outer circumferences, while the joint 12 has thread grooves formed only on the outer circumference, and the tips of the external pipes 6' and 7' are formed on the inner circumference in the axial direction of the inner circumference. It is inserted and fixed halfway.

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1a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′,7′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、前以つて行
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。
In order to connect the heat medium pipe 6, the hydrogen pipe 7, and the external pipes 6' and 7' using these joints, the pressure vessel 1
First, the joint 11 is screwed and fixed into each screw hole formed at a predetermined position on the end surface 1a and the cover plate 1b. Next, the joint 12 to which the external pipes 6' and 7' are fixed is screwed into the inside of the joint 11. This results in
Airtightness is maintained between the pressure vessel 1 and the joint 11 and between the joints 11 and 12 by screwing them together. 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. Additionally, the areas between each joint 12 and the external pipes 6' and 7' are sealed by the previously performed fixing process, and the areas between the heat medium pipe 6, hydrogen pipe 7, and the joint 12 are sealed with the heat medium pipe 6 described above. An airtight structure is formed in the same manner as in the case of joining the members 9.

ここで、継手を11,12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
ツ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 reason why the joint has a double structure of 11 and 12 is to improve the heat insulation between the heat medium pipe 6, the hydrogen pipe 7 and the pressure vessel 1.The joint 11 is made of metal, and the joint 12 is made of metal. It is preferable that the joints 11 and 12 be made of a material with excellent heat insulation properties such as Teflon or fired ceramics, but the joints 11 and 12 may be made of the opposite material.

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、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1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イングされている。更に
全体は耐圧容器1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 this way, the heat exchange container 3 is almost completely thermally isolated from the outside air and sealed inside the pressure container 1.
In order to improve the heat insulation inside the pressure vessel 1, the heat insulating material 2 interposed between the pressure vessel 1 and the heat exchange vessel 3 has a surface coated with a film that is difficult to permeate hydrogen and has excellent heat insulation properties. There is. Further, the entire interior is sealed by flange joining of the main body of the pressure vessel 1 and the lid plate 1b, thereby forming 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
よび伝熱フイン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。また、発生した水素ガスはフイルター7
a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
フイルター7aを介して供給される水素ガスは、
金属水素化物4と給合して熱を発生する。この発
生した熱は断熱材2によつて耐圧容器1への伝熱
が阻止され、全て伝熱フイン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熱され、
効率良く外部配管6′へ取り出され利用される。
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, from the heat medium to the pressure vessel 1
The heat conduction to the metal hydride 4 is prevented by the heat insulating joint 12 and conducted to the heat exchange container 3 without heat loss, and the heat is efficiently supplied 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. Also, the generated hydrogen gas is filtered through filter 7.
The hydrogen is taken out from the hydrogen conduit 7 to the external pipe 7' via a, 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 through the filter 7a is
It combines with 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 the heat is transferred to the heat transfer fins 10 and the heat medium pipe 6.
Heat is transferred from the surface to the heating medium flowing inside it,
It is efficiently taken out to the external piping 6' and utilized.

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、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、断熱性の優れた被膜材でコーテイングした
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、量に止まり、
水素ガスを介しての熱損失も未然に防止され効率
の良い熱交換が期待できる。また、熱媒流路と耐
圧容器1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1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。
In this way, in this embodiment, the cylindrical container 5
A hydrogen conduit 7, with seal members 8 and 9 interposed therein,
Since the heat medium pipe 6 is provided, the inside of the cylindrical container 5 is kept airtight, and leakage of hydrogen gas from the cylindrical container 5 is prevented. Furthermore, since the surface of the heat insulating material 2 is coated with a coating material that is difficult for hydrogen to permeate and has excellent heat insulating properties, even if hydrogen gas leaks from the cylindrical container 5, the amount will be limited to a very small area around it. ,
Heat loss through hydrogen gas is also prevented, and 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.

なお、水素が透過し難く断熱性の優れた被膜材
としては、セロハン、ポリプロピレン(サランコ
ート処理する)等の高分子材料が有望である。何
故ならば、その水素透過性は、通常構造材として
よく使用されるテフロンの1/100〜1/1000程度で
あり、また、その断熱性は、水素透過性の少ない
金属(Al等)に比べ1000倍程度にも上がるから
である。(例えば、高分子材料便覧、高分子学
会編、昭和48年、コロナ社発行、第1297〜1299
頁、化学工業便覧、化学工学協会編、1968年、
丸善発行、第58〜59頁参照) (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。
Note that polymer materials such as cellophane and polypropylene (treated with Saran coating) are promising as coating materials that are difficult for hydrogen to permeate and have excellent heat insulation properties. This is because its hydrogen permeability is about 1/100 to 1/1000 of Teflon, which is commonly used as a structural material, and its insulation properties are lower than metals with low hydrogen permeability (such as Al). This is because it increases by about 1000 times. (For example, Polymer Materials Handbook, edited by the Society of Polymer Science and Technology, 1971, published by Corona Publishing, Nos. 1297-1299)
p., Chemical Industry Handbook, edited by the Society of Chemical Engineers, 1968,
Published by Maruzen, pp. 58-59) (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 due to hydrogen gas is suppressed. Since heat transfer from the exchange container body to the pressure container is also suppressed, sensible heat loss due to the pressure container can be significantly reduced, and a metal hydride container with excellent heat exchange efficiency can be obtained.

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

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―A断面図、
第3図はその側面断面図である。 1…耐圧容器、1a…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…フイルター、8,9…シー
ル部材、10…伝熱フイン、11,12…継手、
13…オーリング。
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 AA,
FIG. 3 is a side sectional view thereof. 1...Pressure container, 1a...End face, 1b...Lid plate, 2...
Heat insulating material, 3... Heat exchange container, 4... Metal hydride, 5
...Cylindrical container, 6...Heat medium pipe, 6', 7'...External piping,
7... Hydrogen conduit, 7a... Filter, 8, 9... Seal member, 10... Heat transfer fin, 11, 12... Joint,
13...O ring.

Claims (1)

【特許請求の範囲】[Claims] 1 熱媒管が気密に貫通する円筒容器内部に、そ
の軸方向に沿つて伝熱フイ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
は水素を透過させるフイルター付き水素導管を取
り付けて熱交換器を構成し、この熱交換器を水素
が透過し難く断熱性の優れた被膜材で表面をコー
テイングした断熱材で覆つ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。
1 A heat transfer fin is arranged along the axial direction inside a cylindrical container through which a heat medium pipe passes airtightly,
A heat exchanger is constructed by storing a metal hydride and attaching a hydrogen conduit with a filter to the end of the cylindrical container to allow hydrogen to pass through.This heat exchanger is coated with a coating material that is difficult for hydrogen to pass through and has excellent heat insulation properties. The heat transfer pipe and the hydrogen pipe are installed in a pressure-resistant container whose surface is covered with a heat-insulating material coated with heat-insulating material, and the heat transfer pipe and hydrogen pipe are led out from both ends of the pressure-resistant container through connection joints made of a material with excellent heat insulation properties. Characteristic metal hydride containers.
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 JPS61197899A (en) 1986-09-02
JPH0224762B2 true 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
JPS61197899A (en) 1986-09-02

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