JPH0232201B2 - - Google Patents
Info
- Publication number
- JPH0232201B2 JPH0232201B2 JP59266305A JP26630584A JPH0232201B2 JP H0232201 B2 JPH0232201 B2 JP H0232201B2 JP 59266305 A JP59266305 A JP 59266305A JP 26630584 A JP26630584 A JP 26630584A JP H0232201 B2 JPH0232201 B2 JP H0232201B2
- Authority
- JP
- Japan
- Prior art keywords
- metal hydride
- metal
- nickel foam
- cylindrical
- insulating material
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C11/00—Use of gas-solvents or gas-sorbents in vessels
- F17C11/005—Use of gas-solvents or gas-sorbents in vessels for hydrogen
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の脱水素化および水素化
反応を利用して水素貯蔵あるいは蓄熱を行なうた
めの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 for storing hydrogen or storing heat by utilizing dehydrogenation and hydrogenation reactions of metal hydrides.
(ロ) 従来の技術
この種の金属水素化物容器において、金属水素
化物の粉体は、脱水素化および水素化反応を繰り
返すうちに次第に微細化され、熱伝導率が更に低
下し、反応が速やかに進行しなくなる。なお、金
属水素化物は脱水素化して金属となるが、本明細
書中ではこの場合も含めて金属水素化物と称す
る。(b) Prior art In this type of metal hydride container, the metal hydride powder becomes finer as it undergoes repeated dehydrogenation and hydrogenation reactions, and its thermal conductivity further decreases, making the reaction more rapid. It stops progressing. Note that a metal hydride becomes a metal by dehydrogenation, and in this specification, this case is also referred to as a metal hydride.
従つて、金属水素化物の脱水素化および水素化
反応を促進し、反応効率を向上するには、熱媒と
金属水素化物との間の熱伝導率を改善することが
必要となる。 Therefore, in order to promote the dehydrogenation and hydrogenation reactions of metal hydrides and improve the reaction efficiency, it is necessary to improve the thermal conductivity between the heat medium and the metal hydride.
従来、この熱伝導率を改善するために、金属水
素化物の粉体充填層中にフインを配設するなどの
方策が取られていたが、これで十分とは言い難か
つた。 Conventionally, measures have been taken to improve this thermal conductivity, such as arranging fins in a powder-packed bed of metal hydride, but this was far from sufficient.
そこで、出願人はこの点を改善すべく研究を重
ねた結果、フインとして発泡金属の使用が効果的
であることを突き止め、先に提案した。これによ
れば、金属水素化物粉体と発泡金属が混じりあつ
た状態となり、金属水素化物粉体と伝熱フインと
しての発泡金属との距離が平均して極めて近くな
り、金属水素化物全体にわたつて熱交換が均一行
なわれるようになり、金属水素化物の利用効率が
改善されるようになつた。 Therefore, as a result of repeated research to improve this point, the applicant found that it was effective to use foam metal as the fin, and proposed it earlier. According to this, the metal hydride powder and the foamed metal are mixed together, and the distance between the metal hydride powder and the foamed metal as heat transfer fins becomes extremely short on average, and the metal hydride powder is spread over the entire metal hydride. As a result, heat exchange has become more uniform, and the efficiency of using metal hydrides has improved.
ところが、発泡金属の製造過程では加熱して発
泡合成樹脂を気化発散させる過程があるため、製
造された発泡金属の表面には厚い酸化膜が形成さ
れ、熱伝導度が低下する。このため、この発泡金
属を利用した金属水素化物容器においても期待す
る程には熱交換効率が改善されない問題点があつ
た。 However, since the manufacturing process of foamed metal includes a process of heating and vaporizing the foamed synthetic resin, a thick oxide film is formed on the surface of the manufactured foamed metal, resulting in a decrease in thermal conductivity. For this reason, even in metal hydride containers using this foamed metal, there was a problem in that the heat exchange efficiency was not improved as much as expected.
(ハ) 発明が解決しようとする問題点
本発明は先に提案した本発明を更に改善して更
に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 An object of the present invention is to further improve the previously proposed present invention and provide a metal hydride container with even better heat exchange efficiency.
(ニ) 問題点を解決するための手段
このため本発明は、利用する前にニツケル発泡
体に酸洗浄などの表面処理を施すことにより、表
面の厚い酸化膜を除去したのち、伝熱特性の優れ
た銀または銅で表面をメツキし、これを金属水素
化物と共に金属水素化物容器内に充填するように
したことを特徴としている。(d) Means for solving the problem Therefore, in the present invention, the thick oxide film on the surface is removed by subjecting the nickel foam to surface treatment such as acid cleaning before use, and then the heat transfer properties are improved. It is characterized in that the surface is plated with high quality silver or copper, and this is packed together with metal hydride into a metal hydride container.
(ホ) 作用
表面が酸化膜で覆われている発泡金属にそのま
ま銅、銀をメツキしても効果があるが、更に発泡
金属の酸化被膜を表面処理により除去したのち、
良伝熱材の銀または銅をメツキすることにより、
熱伝導度が更に良くなり、金属水素化物と熱媒と
の熱交換効率が改善される。(E) Effect It is effective to plate copper or silver as is on a foam metal whose surface is covered with an oxide film, but after removing the oxide film of the foam metal through surface treatment,
By plating silver or copper, which is a good heat conductive material,
The thermal conductivity is further improved, and the heat exchange efficiency between the metal hydride and the heat medium is improved.
(ヘ) 実施例
以下、本発明の実施例を図面を参照して説明す
る。(f) Examples Examples of the present invention will be described below with reference to the drawings.
第1図aは本発明の一実施例に係る金属水素化
物容器の側断面図、同図bはそのA−A断面図を
示したものである。第1図において、一端にフラ
ンジ部1aを有する円筒状パイプ1のフランジ側
の端部には、中央に熱媒出入導管2aを有する閉
塞円板3が、そのフランジ部においてボルト4、
ナツト5にて前記パイプ1側フランジ部と結合さ
れている。また、円筒状パイプ1の他端には中央
に熱媒出入導管2bを有すると共に、水素出入導
管6を有する閉塞円板7が嵌合固着されている。
これら円筒状パイプ1、閉塞円板3、閉塞円板7
により構成される円筒状耐圧容器20の部には、
熱媒出入導管2aおよび2bと連通する円筒状に
形成された熱媒管2cが設けられ、これらの管2
a,2c,2bで一体的に上記円筒状耐圧容器2
0を貫通する熱媒管30が形成される。 FIG. 1a is a side sectional view of a metal hydride container according to an embodiment of the present invention, and FIG. 1b is a sectional view taken along line A-A. In FIG. 1, at the flange side end of a cylindrical pipe 1 having a flange portion 1a at one end, a closing disk 3 having a heat medium inlet/outlet conduit 2a at the center is provided with bolts 4,
It is connected to the flange portion on the side of the pipe 1 with a nut 5. Further, at the other end of the cylindrical pipe 1, a closing disk 7 having a heat medium inlet/outlet conduit 2b at the center and a hydrogen inlet/outlet conduit 6 is fitted and fixed.
These cylindrical pipe 1, closing disk 3, closing disk 7
The part of the cylindrical pressure-resistant container 20 composed of
A cylindrical heat medium pipe 2c communicating with the heat medium inlet/output pipes 2a and 2b is provided, and these pipes 2
a, 2c, and 2b integrally form the cylindrical pressure vessel 2.
0 is formed.
その円筒状耐圧容器20の内壁には断熱材8が
張り付けられ、その内面には水素は通すが金属水
素化物粉末は通さないフイルタ板9,10を両端
部に有し、その中央部はアルミ等の円筒パイプ1
1で形成されたフイルタ円筒体40が設けられて
いる。 A heat insulating material 8 is pasted on the inner wall of the cylindrical pressure-resistant container 20, and the inner surface has filter plates 9 and 10 at both ends that allow hydrogen to pass through but not metal hydride powder. cylindrical pipe 1
A filter cylinder 40 formed by 1 is provided.
更に、そのフイルタ円筒体40と熱媒管30と
の間に発泡金属体として本実施例では入手し易い
ニツケル発泡体12と共に金属水素化物粉体13
が充填されている。 Further, in this embodiment, a readily available nickel foam 12 and a metal hydride powder 13 are used as a foamed metal body between the filter cylinder 40 and the heat medium pipe 30.
is filled.
このように、円筒状耐圧容器20、熱媒管3
0、フイルタ円筒体40を各部品の組立て構成と
することにより、内部の金属水素化物粉体13の
交換等のメンテナンスを容易にすることができ
る。 In this way, the cylindrical pressure vessel 20, the heat medium pipe 3
0. By constructing the filter cylindrical body 40 by assembling each part, maintenance such as replacement of the metal hydride powder 13 inside can be facilitated.
上記ニツケル発泡体12の形状は第2図の拡大
断面図に示す如くスポンジ状というよりはむしろ
金属を繊維状にして絡み合せたようなヘチマたわ
しのようなものに近い。しかし、この形状だけに
限らないことは言う迄もない。尚、第2図におけ
る12aは金属部分、12bは空間部分を示し、
この空間部分12bに金属水素化物粉体13が充
填される。 As shown in the enlarged cross-sectional view of FIG. 2, the shape of the nickel foam 12 is more like a loofah scrubber made of intertwined metal fibers than a sponge. However, it goes without saying that it is not limited to this shape. In addition, 12a in FIG. 2 indicates a metal part, 12b indicates a space part,
This space portion 12b is filled with metal hydride powder 13.
しかし、このニツケル発泡体12は入手が容易
な代りに熱伝導度が銅、銀等に比較して1桁悪
い。その上、前述したように製造過程でその表面
には厚い酸化膜が形成される。従つて、このまま
用いても、熱交換効率はそれ程改善されない。そ
こで、本実施例ではニツケル発泡体に酸洗浄など
の表面処理を施こし、表面の酸化膜を除去する。
あるいは、ニツケル発泡体の表面に熱伝導性の優
れた銀、銅をメツキする。更にはまた、予め表面
処理を施こし、表面の酸化膜を除去したのち、良
熱伝導性の銀、銅をメツキする。 However, although this nickel foam 12 is easily available, its thermal conductivity is one order of magnitude lower than that of copper, silver, etc. Moreover, as described above, a thick oxide film is formed on the surface during the manufacturing process. Therefore, even if used as is, the heat exchange efficiency will not be improved that much. Therefore, in this embodiment, the nickel foam is subjected to surface treatment such as acid cleaning to remove the oxide film on the surface.
Alternatively, the surface of the nickel foam is plated with silver or copper, which has excellent thermal conductivity. Furthermore, after surface treatment is performed in advance to remove the oxide film on the surface, silver or copper, which has good thermal conductivity, is plated.
第3図はこのときの円筒状耐圧容器20の昇温
特性を示したもので、実線Aは未処理のニツケル
発泡体使用時の昇温特性曲線、破線Bは表面処理
して酸化膜を除去したニツケル発泡体使用時の昇
温特性曲線、一点鎖線Cは未処理表面に銅メツキ
したニツケル発泡体使用時の昇温特性曲線、二点
鎖線Dは表面処理して酸化膜を除いた上更に銅メ
ツキしたニツケル発泡体使用時の昇温度性曲線で
ある。 Figure 3 shows the temperature rise characteristics of the cylindrical pressure vessel 20 at this time, where the solid line A is the temperature rise characteristic curve when untreated nickel foam is used, and the broken line B is the surface treatment to remove the oxide film. The temperature rise characteristic curve when using a nickel foam that has been treated, the one-dot chain line C is the temperature rise characteristic curve when using a nickel foam with copper plating on the untreated surface, and the two-dot chain line D shows the temperature rise characteristic curve when using a nickel foam that has been surface treated to remove the oxide film. This is a temperature rise curve when using copper-plated nickel foam.
この図からも明らかなように、ニツケル発泡体
を表面処理乃至は表面メツキすることによりニツ
ケル発泡体の熱伝導性が数%程良くなり、円筒状
耐圧容器20に充填される金属水素化物粉体13
と熱媒管30を流れる熱媒との熱交換率が改善さ
れる。 As is clear from this figure, by surface-treating or plating the nickel foam, the thermal conductivity of the nickel foam improves by several percent, and the metal hydride powder to be filled into the cylindrical pressure-resistant container 20 13
The heat exchange coefficient between the heat medium and the heat medium flowing through the heat medium pipe 30 is improved.
尚、フイルタ円筒体40と熱媒管30間に充填
するニツケル発泡体12は上記実施例に示した如
く小片に分割したものでも良いし、また、第4図
に示す如く一体的に形成したものであつても良
い。図中、12cは熱媒管2cを嵌合する通し穴
である。 The nickel foam 12 filled between the filter cylinder 40 and the heat medium pipe 30 may be divided into small pieces as shown in the above embodiment, or may be formed integrally as shown in FIG. It's okay to be. In the figure, 12c is a through hole into which the heat medium pipe 2c is fitted.
また、容器構造は、第5図aの側断面図および
同図bのB−B断面図に示すように、円筒パイプ
11も含めて全体フイルタで構成したフイルタ円
筒体40を用いると良い。また、熱媒管2cの外
側には軸方向に沿つてフイン2dを形成すること
が好ましい。 As shown in the side cross-sectional view of FIG. 5a and the BB cross-sectional view of FIG. Moreover, it is preferable to form fins 2d along the axial direction on the outside of the heat medium pipe 2c.
このように、全体がフイルタ構成のフイルタ円
筒体40を用いることにより、フイルタの有効面
積が拡大し、金属水素化物粉体13との水素交換
が均一に行なわれるようになる。また、熱媒管2
cの外部にフイン2dを形成することにより、ニ
ツケル発泡体と熱媒間との熱伝達が有効に行なわ
れるようになる。 In this manner, by using the filter cylinder 40 whose entire structure is a filter, the effective area of the filter is expanded, and hydrogen exchange with the metal hydride powder 13 is uniformly performed. In addition, heat medium pipe 2
By forming the fins 2d on the outside of the fins 2d, heat transfer between the nickel foam and the heating medium can be carried out effectively.
(ト) 発明の効果
以上のように本発明によれば、金属水素化物容
器内にはニツケル発泡体の表面酸化膜を除去した
のち銀または銅をメツキした表面処理発泡金属体
と共に、金属水素化物粉体を充填するようにした
ので、熱媒と金属水素化物粉体との熱交換効率が
改善される。また、その金属水素化物容器は耐圧
容器内面全体を断熱材で覆うようにしたので、顕
熱損失を減少させることができる。また、金属水
素化物はフイルタ円筒体内に収納するようにした
ので、金属水素化物と水素との反応が均一に行な
われるようになる。(G) Effects of the Invention As described above, according to the present invention, the metal hydride container contains a surface-treated foamed metal body that has been plated with silver or copper after removing the surface oxide film of the nickel foam, as well as a metal hydride. Since the powder is filled, the heat exchange efficiency between the heating medium and the metal hydride powder is improved. Furthermore, since the entire inner surface of the pressure-resistant container is covered with a heat insulating material, sensible heat loss can be reduced. Further, since the metal hydride is housed within the filter cylinder, the reaction between the metal hydride and hydrogen can be uniformly carried out.
第1図は本発明の一実施例に係る金属水素化物
容器の構成図で、同図aはその側面図、同図bは
そのA−A断面図、第2図はその容器内部に収納
するニツケル発泡体の断面図、第3図は各種条件
のニツケル発泡体を使用したときの耐圧容器の各
昇温特性曲線図、第4図は耐圧容器内に収納する
ニツケル発泡体の他の例を示す外形図、第5図は
本発明の他の実施例に係る金属水素化物容器の構
成図で、同図aはその側断面図、同図bはそのB
−B断面図である。
1……円筒状パイプ、1a……フランジ部、2
a,2b……熱媒出入導管、2c,30……熱媒
管、2d……フイン、3,7……閉塞円板、4…
…ボルト、5……ナツト、6……水素出入導管、
8……断熱材、9,10……フイルタ板、11…
…円筒パイプ、12……ニツケル発泡体、13…
…金属水素化物粉体、20……円筒状耐圧容器、
40……フイルタ円筒体。
Fig. 1 is a configuration diagram of a metal hydride container according to an embodiment of the present invention, in which Fig. 1a is a side view thereof, Fig. 1b is a sectional view taken along line A-A, and Fig. 2 is a diagram showing a container for storing metal hydride inside the container. A cross-sectional view of a nickel foam, Figure 3 shows each temperature rise characteristic curve of a pressure container when using a nickel foam under various conditions, and Figure 4 shows another example of a nickel foam housed in a pressure container. 5 is a configuration diagram of a metal hydride container according to another embodiment of the present invention, and FIG. 5A is a side sectional view thereof, and FIG.
-B sectional view. 1... Cylindrical pipe, 1a... Flange part, 2
a, 2b... Heat medium inlet/output conduit, 2c, 30... Heat medium pipe, 2d... Fin, 3, 7... Closing disk, 4...
...Bolt, 5...Nut, 6...Hydrogen inlet/output pipe,
8...Insulating material, 9,10...Filter plate, 11...
...Cylindrical pipe, 12...Nickel foam, 13...
...Metal hydride powder, 20...Cylindrical pressure-resistant container,
40... Filter cylindrical body.
Claims (1)
端部には水素出入導管が取り付けられて円筒状に
形成された耐圧容器と、この耐圧容器の円筒軸心
部に前記閉塞円板を貫通して配設された円筒状の
熱媒管と、前記耐圧容器の内壁に張り付けられた
断熱材と、この断熱材の内側に設けられた水素は
通すが金属水素化物粉体は通さない全体がフイル
タからなるフイルタ円筒体とを備え、このフイル
タ円筒体と前記熱媒管との間に、ニツケル発泡体
の表面酸化膜を除去したのち銀または銅をメツキ
した表面処理発泡金属体と共に金属水素化物粉体
を収納して成ることを特徴とする金属水素化物容
器。1 A pressure-resistant container formed in a cylindrical shape with a closed disk at both ends and a hydrogen inlet/output conduit attached to one end of the closed disk, and the closed disk at the cylindrical axis of this pressure-resistant container. A cylindrical heat transfer pipe installed through the pressure vessel, a heat insulating material attached to the inner wall of the pressure vessel, and a heat insulating material provided inside the heat insulating material that allows hydrogen to pass through but not metal hydride powder. A filter cylinder whose entire body is made of a filter is provided between the filter cylinder and the heating medium tube together with a surface-treated foam metal body which is plated with silver or copper after removing the surface oxide film of the nickel foam. A metal hydride container characterized by containing hydride powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26630584A JPS61144499A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26630584A JPS61144499A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61144499A JPS61144499A (en) | 1986-07-02 |
| JPH0232201B2 true JPH0232201B2 (en) | 1990-07-19 |
Family
ID=17429083
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26630584A Granted JPS61144499A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61144499A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4888777B2 (en) * | 2007-06-07 | 2012-02-29 | 国立大学法人東北大学 | Method for producing hydrogen storage material |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5684301A (en) * | 1979-12-14 | 1981-07-09 | Kawasaki Heavy Ind Ltd | Holding apparatus for hydrogen storing metal |
| JPS56109998A (en) * | 1980-02-01 | 1981-08-31 | Matsushita Electric Ind Co Ltd | Hydrogen storing container |
| JPS57154733U (en) * | 1981-03-23 | 1982-09-29 | ||
| JPS5935001A (en) * | 1982-08-23 | 1984-02-25 | Mitsubishi Steel Mfg Co Ltd | Preparation of hydrogen storing material |
-
1984
- 1984-12-19 JP JP26630584A patent/JPS61144499A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61144499A (en) | 1986-07-02 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |