JPS61144496A - Metal hydride container - Google Patents
Metal hydride containerInfo
- Publication number
- JPS61144496A JPS61144496A JP59266302A JP26630284A JPS61144496A JP S61144496 A JPS61144496 A JP S61144496A JP 59266302 A JP59266302 A JP 59266302A JP 26630284 A JP26630284 A JP 26630284A JP S61144496 A JPS61144496 A JP S61144496A
- Authority
- JP
- Japan
- Prior art keywords
- metal hydride
- cylindrical
- container
- heat
- heat transfer
- 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
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
-
- 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
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)
Abstract
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水素化および脱水素化反応を利
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) Industrial Application Field The present invention relates to a metal hydride container for storing hydrogen or storing heat by utilizing hydrogenation and dehydrogenation 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、金属水素化物の水
素化および脱水素化反応を促進するには熱媒と金属水素
化物粉体充填層との間の熱伝達を良くすることである。(B) Prior art In order to promote the hydrogenation and dehydrogenation reactions of metal hydrides in this type of metal hydride container, it is necessary to improve the heat transfer between the heating medium and the metal hydride powder packed bed. That's true.
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。Note that a metal hydride becomes a metal by dehydrogenation, and in this specification, this case is also referred to as a metal hydride.
このため、従来は例えば実開昭57−154733号公
報に見られるように、管状圧力容塁の軸心位置には水素
ガスを透過するフィルタ管を配設し、そのフィルタ管と
圧力容器との間に金属水素化物を充填すると共に、そこ
に軸方向に沿って複数枚のフィンを配設する構造を採っ
ていた。For this reason, conventionally, as seen in, for example, Japanese Utility Model Application No. 57-154733, a filter tube that transmits hydrogen gas is disposed at the axial center position of the tubular pressure vessel base, and the filter tube and the pressure vessel are connected. The structure was such that a metal hydride was filled in between and a plurality of fins were arranged along the axial direction.
しかし、上記従来構造によると、内部に充填する金属水
素化物の量を増す場合、管径を大きくすると、フィン枚
数の制限、金属水素化物粉体どの伝達距離の増大等の理
由により、熱媒との熱伝達効率が著しく減少する。従っ
て、上記のような構造で金属水素化物の充填量を増大す
るには、その管状圧力容器の軸方向の長さを長くする方
法しかなく、設置スペース、取り扱い、加工性の点で極
めて不利であった。However, according to the above conventional structure, when increasing the amount of metal hydride to be filled inside, increasing the pipe diameter causes problems such as limiting the number of fins and increasing the transmission distance of the metal hydride powder. heat transfer efficiency is significantly reduced. Therefore, the only way to increase the amount of metal hydride charged in the above structure is to increase the axial length of the tubular pressure vessel, which is extremely disadvantageous in terms of installation space, handling, and processability. there were.
(ハ)発明が解決しようとする問題点
本発明は管状圧力容器の径方向寸法を増すことにより金
属水素化物収納量を増加し、しかも金属水素化物粉体各
部と熱媒体との熱伝達を良好に行ない得る金属水素化物
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 increases the storage capacity of metal hydride by increasing the radial dimension of the tubular pressure vessel, and also improves the heat transfer between each part of the metal hydride powder and the heat medium. The object of the present invention is to provide a metal hydride container that can be used for various purposes.
(ニ)問題点を解消するための手段
このため本発明は、熱媒出入導管を備え、内壁に断熱材
を有する円筒容器の中に同心軸上に複数の金属性円筒パ
イプを配設し、これら各円筒パイプ間に交互に金属水素
化物領域と、熱媒領域とを設け、前記金属水素化物領域
は両端部を閉塞板により閉塞して内部に伝熱フィンを設
けて金属水素を充填すると共に、一方の閉塞板にはフィ
ルタ付水素出入導管を取り付け、前記円筒容器外へ引き
出し、水素の出し入れを行なう一方、前記熱媒領域シこ
はじゃま板を設けて前記熱媒出入導管から熱媒を流すよ
うにしたことを主な特徴としている。(d) Means for solving the problem Therefore, the present invention provides a plurality of metal cylindrical pipes arranged concentrically in a cylindrical container that is equipped with a heat medium inlet and outlet conduit and has a heat insulating material on the inner wall, A metal hydride region and a heat medium region are provided alternately between each of these cylindrical pipes, and both ends of the metal hydride region are closed with closing plates, heat transfer fins are provided inside, and metal hydrogen is filled. A hydrogen inlet/output conduit with a filter is attached to one of the closing plates to draw it out of the cylindrical container to take hydrogen in and out, while a baffle plate is provided in the heating medium area to draw the heat medium out from the heat medium inlet/outlet conduit. The main feature is that it is made to flow.
(ホ)作用
同心軸上に配設する円筒パイプの数を増すことにより、
金属水素化物充填層の厚みを薄くした状態で多量の金属
水素化物を容器内に収納することができる。従って、軸
方向の長さ寸法を大きくとる必要が無くなり、金属水素
化物容器の設置スペース、取り扱い、加工性が改善され
る。また、上記本発明の構成により、熱媒はじゃま板に
より乱流となり、金属性円筒パイプに効率良く熱を伝え
る。(e) By increasing the number of cylindrical pipes arranged on the working concentric axis,
A large amount of metal hydride can be stored in the container with a reduced thickness of the metal hydride packed layer. Therefore, there is no need to increase the length in the axial direction, and the installation space, handling, and workability of the metal hydride container are improved. Furthermore, with the configuration of the present invention, the heat medium becomes a turbulent flow due to the baffle plate, and efficiently transmits heat to the metallic cylindrical pipe.
更に、この熱は伝熱フィンにより、金属水素化物充填層
内部へ迅速に伝達され効率良く熱交換される。また、金
属水素化物領域と熱媒領域は交互に配置されるため、金
属水素化物充填層には熱媒の熱がその上下方向から伝達
され、大量の金属水素化物粉体と熱媒との熱交換が極め
て迅速に行なわれる。Furthermore, this heat is rapidly transferred to the inside of the metal hydride packed bed by the heat transfer fins, and is efficiently exchanged. In addition, since the metal hydride regions and the heating medium regions are arranged alternately, the heat of the heating medium is transmitted to the metal hydride packed bed from above and below, and the heat between a large amount of metal hydride powder and the heating medium is transferred. Exchange occurs very quickly.
(ハ)実施例 以下1本発明の実施例を図面に基づいて説明する。(c) Examples An embodiment of the present invention will be described below based on the 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
断面図を示し、第2図はそのA−A断面図を示したもの
である。これらの図において、円筒容器1は熱媒が出入
する熱媒出入導管2を備え、その内面には断熱材3が全
体に張設されている1円筒容器1の内側には銅またはア
ルミ製の複数の円筒パイプ4a 、 4b s 4c
、 4d 、 4eが同心軸上に配置されている。これ
らの円筒パイプ間を利用して交互に金属水素化物領域5
.熱媒領域6が設けられる。即ち。FIG. 1 shows a side sectional view of a metal hydride container according to an embodiment of the present invention, and FIG. 2 shows its AA sectional view. In these figures, a cylindrical container 1 is equipped with a heat medium inlet/output conduit 2 through which a heat medium flows in and out, and a heat insulating material 3 is stretched over the entire inner surface of the cylindrical container 1. Multiple cylindrical pipes 4a, 4b s 4c
, 4d, and 4e are arranged on concentric axes. Metal hydride regions 5 are alternately formed between these cylindrical pipes.
.. A heat medium area 6 is provided. That is.
この金属水素化物領域5は円筒パイプ4aと4bの間、
4cと4dの間、 4e内を利用して形成される。円筒
パイプ4aと4bの両端は閉塞板7a、7bにより閉塞
され。This metal hydride region 5 is located between the cylindrical pipes 4a and 4b,
It is formed using the space between 4c and 4d and inside 4e. Both ends of the cylindrical pipes 4a and 4b are closed by closing plates 7a and 7b.
内部に伝熱フィン8が設けられて金属水素化物が充填さ
れると共に、閉塞板7aには水素出入導管9が取り付け
られ、その内側には水素は通すが金属水素化物粉末は通
さないフィルタ10が設けられる。Heat transfer fins 8 are provided inside and filled with metal hydride, and a hydrogen inlet/output conduit 9 is attached to the closing plate 7a, and a filter 10 that allows hydrogen to pass through but not metal hydride powder is installed inside of it. provided.
円筒パイプ4cと4dとの間および円筒パイプ4e内も
同様にして、それぞれの両端部には閉塞板7c、7dお
よび7e 、 7f、その閉塞板7cおよび7e側には
水素出入導管9が取り付けられると共に、フィルタ10
が設けられ、内部には、伝熱フィン8が設けられて金属
水素化物が充填される。また、各金属水素化物領域5に
取り付けられる水素出入導管9は円筒容器1の端壁を貫
通して円筒容器1の外部導出され、1本共通水素出入導
管9にまとめられ、開閉弁11を介して図示せぬ水素貯
蔵タンクへ接続される。Similarly, between the cylindrical pipes 4c and 4d and inside the cylindrical pipe 4e, closing plates 7c, 7d, 7e, and 7f are attached to both ends of each, and a hydrogen inlet/output conduit 9 is attached to the closing plates 7c and 7e side. together with the filter 10
The interior thereof is provided with heat transfer fins 8 and filled with metal hydride. Further, the hydrogen inlet/outlet conduits 9 attached to each metal hydride region 5 penetrate the end wall of the cylindrical container 1 and are led out of the cylindrical container 1 , are combined into one common hydrogen inlet/outlet conduit 9 , and are connected via an on-off valve 11 . It is connected to a hydrogen storage tank (not shown).
一方、熱媒領域6は断熱材3の内1i3aと円筒パイプ
4aの間、円筒パイプ4bと40の間、円筒パイプ4d
と4eの間を利用して形成される。即ち、それらの間隙
には乱流が生じるようにじゃま板12が配設され、また
、それらの両端部は共通流路が形成されてそれぞれ熱媒
出入導管2に連通される。On the other hand, the heat medium area 6 is located between the heat insulating material 3 1i3a and the cylindrical pipe 4a, between the cylindrical pipes 4b and 40, and between the cylindrical pipe 4d.
and 4e. That is, the baffle plate 12 is disposed in the gap between them so that turbulent flow occurs, and a common flow path is formed at both ends thereof, which communicate with the heat medium inlet/outlet conduit 2, respectively.
ここで、使用する円筒パイプ4a〜4eおよび閉塞板7
8〜7fは水素加圧に耐え、しかも熱伝導率に優れた材
質として1例えばアルミニウム、銅等を用いるのがよい
。また、伝熱フィン8は金属水素化物の充填層の熱伝導
率の向上させるためのもので、円筒パイプと同材質、例
えばアルミニウム等を用いるのがよい、更に、この伝熱
フィンと円筒パイプとは一体成形が可能で、この伝熱フ
ィン8を介して内管と外管1例えば円筒パイプ4aと4
bを一体成形したものも用いることができ、これにより
より伝熱抵抗の小さい熱交換能力の優れた金属水素化物
領域を形成させることが可能となる。また、じゃま板1
2は波状の表面をもつ円筒パイプ等が使用でき、熱媒体
の流れを乱流にし、熱交換能力を大きく向上させる働き
をする。Here, the cylindrical pipes 4a to 4e and the closing plate 7 to be used are
8 to 7f are preferably made of a material that can withstand hydrogen pressurization and has excellent thermal conductivity, such as aluminum or copper. The heat transfer fins 8 are used to improve the thermal conductivity of the packed bed of metal hydrides, and are preferably made of the same material as the cylindrical pipe, such as aluminum. can be integrally molded, and the inner tube and the outer tube 1, for example, the cylindrical pipes 4a and 4, are connected via the heat transfer fins 8.
It is also possible to use one in which b is integrally molded, thereby making it possible to form a metal hydride region with lower heat transfer resistance and excellent heat exchange ability. Also, baffle board 1
As for 2, a cylindrical pipe or the like with a corrugated surface can be used, which makes the flow of the heat medium turbulent and greatly improves the heat exchange ability.
従って、上記構成によれば、金属水素化物容器は、円筒
パイプ4a〜4eを介して金属水素化物と熱媒体とが交
互に接触する構造であるため、伝熱面積は大きく、その
熱交換速度も大きくなる。更に、熱伝導率の小さい金属
水素化物粉体充填層の厚みは、伝熱フィン8により熱伝
導の点から見て更に小さくされ、熱伝達速度が高められ
る。熱媒体との熱交換も円滑に行なわれる。Therefore, according to the above configuration, since the metal hydride container has a structure in which the metal hydride and the heat medium are alternately contacted through the cylindrical pipes 4a to 4e, the heat transfer area is large and the heat exchange rate is also low. growing. Furthermore, the thickness of the metal hydride powder packed layer, which has a low thermal conductivity, is further reduced by the heat transfer fins 8 in terms of heat conduction, and the heat transfer rate is increased. Heat exchange with the heat medium is also performed smoothly.
また、充填する金属水素化物の量がより大きい場合にも
円筒パイプの本数、径、伝熱フィンの枚数を適宜増加す
ることにより、金属水素化物粉末充填層の厚みを容易に
小さくすることができ、優れた熱交換能力が発揮される
。Furthermore, even when the amount of metal hydride to be filled is larger, the thickness of the metal hydride powder packed layer can be easily reduced by appropriately increasing the number and diameter of the cylindrical pipes and the number of heat transfer fins. , exhibits excellent heat exchange ability.
(ト)発明の詳細
な説明したように本発明によれば、金属水素化物と熱媒
体とが1円筒パイプを介して交互に接触するため、金属
水素化物と熱媒体との間の熱交換速度が大きく1円滑な
熱伝達が可能になり、熱交換効率の良い金属水素化物容
器が得られる。また、円筒パイプの本数、径、フィンの
枚数を適宜選択することにより、金属水素化物の充填量
が大きくなっても金属水素化物充填層の厚みを小さくす
ることができ、軸方向寸法を大きくすることなく、設置
スペースが少なく、製造、取り扱いが容易な優れた金属
水素化物容器が得られる。(G) Detailed Description of the Invention According to the present invention, as described above, the metal hydride and the heating medium alternately contact each other through one cylindrical pipe, so that the rate of heat exchange between the metal hydride and the heating medium is 1, smooth heat transfer is possible, and a metal hydride container with high heat exchange efficiency can be obtained. In addition, by appropriately selecting the number, diameter, and number of fins of the cylindrical pipes, the thickness of the metal hydride packed layer can be reduced even when the amount of metal hydride packed is large, and the axial dimension can be increased. Therefore, an excellent metal hydride container that requires less installation space and is easy to manufacture and handle can be obtained.
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
断面図、第2図はそのA−A断面図である。
l・・・円筒容器、2・・・熱媒出入導管、3・・・断
熱材、 4a〜4e・・・円筒パイプ、5・・・金属水
素化物領域、6・・・熱媒領域、7a〜7f・・・閉塞
板、8・・・伝熱フィン、9・・・水素出入導管、10
・・・フィルタ、11・・・開閉弁、12・・・ じゃ
ま板。FIG. 1 is a side cross-sectional view of a metal hydride container according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along line A-A. l... Cylindrical container, 2... Heat medium inlet/output conduit, 3... Heat insulating material, 4a to 4e... Cylindrical pipe, 5... Metal hydride region, 6... Heat medium region, 7a ~7f... Closure plate, 8... Heat transfer fin, 9... Hydrogen in/out conduit, 10
...Filter, 11...Opening/closing valve, 12...Baffle plate.
Claims (3)
容器の中に同心軸上に複数の金属性円筒パイプを配設し
、これら各円筒パイプ間に交互に金属水素化物領域と、
熱媒領域とを設け、前記金属水素化物領域は両端部を閉
塞板により閉塞し、内部に伝熱フィンを設けて金属水素
化物を収納すると共に、一方の閉塞板にはフィルタ付水
素出入導管を取り付け、前記円筒容器外へ引き出し、水
素の出し入れを行なう一方、前記熱媒領域にはじやま板
を設けて前記熱媒出入導管から熱媒を流すように構成し
たことを特徴とする金属水素化物容器。(1) A plurality of metal cylindrical pipes are arranged concentrically in a cylindrical container equipped with a heat medium inlet/output conduit and has a heat insulating material on the inner wall, and metal hydride regions are alternately arranged between each of these cylindrical pipes,
The metal hydride region has both ends closed by closing plates, heat transfer fins are provided inside to accommodate the metal hydride, and one of the closing plates is provided with a hydrogen inlet/output pipe with a filter. A metal hydride container, characterized in that the metal hydride container is configured to be attached and pulled out of the cylindrical container to take in and take out hydrogen, and at the same time, a baffle plate is provided in the heating medium area so that the heating medium flows through the heating medium inlet/output conduit. .
イプは銅またはアルミニウム製であることを特徴とする
金属水素化物容器。(2) The metal hydride container according to claim 1, wherein the cylindrical pipe is made of copper or aluminum.
物領域に設けた伝熱フィンにより固定される内管と外管
とが一体成形物であることを特徴とする金属水素化物容
器。(3) A metal hydride container according to claim 1, wherein the inner tube and the outer tube fixed by heat transfer fins provided in the metal hydride region are integrally molded.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59266302A JPS61144496A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59266302A JPS61144496A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61144496A true JPS61144496A (en) | 1986-07-02 |
Family
ID=17429046
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59266302A Pending JPS61144496A (en) | 1984-12-19 | 1984-12-19 | Metal hydride container |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61144496A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5082048A (en) * | 1988-07-26 | 1992-01-21 | Kabushiki Kaisha Toyoda Jidoshokki Seisakusho | Hydrogen engine system with metal hydride container |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5427396U (en) * | 1977-07-28 | 1979-02-22 | ||
JPS5925956A (en) * | 1982-08-03 | 1984-02-10 | Furukawa Electric Co Ltd:The | Alloy with high magnetic permeability |
-
1984
- 1984-12-19 JP JP59266302A patent/JPS61144496A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5427396U (en) * | 1977-07-28 | 1979-02-22 | ||
JPS5925956A (en) * | 1982-08-03 | 1984-02-10 | Furukawa Electric Co Ltd:The | Alloy with high magnetic permeability |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5082048A (en) * | 1988-07-26 | 1992-01-21 | Kabushiki Kaisha Toyoda Jidoshokki Seisakusho | Hydrogen engine system with metal hydride container |
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JPS6238638B2 (en) | ||
JPS58164994A (en) | Vessel for metal hydride | |
JPS62297696A (en) | Heat exchanger for refrigerant | |
JPS6249100A (en) | Metal hydride container | |
JPH0236521B2 (en) | KINZOKUSUISOKABUTSUYOKI |