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JPS6224679B2 - - Google Patents
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JPS6224679B2 - - Google Patents

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Publication number
JPS6224679B2
JPS6224679B2 JP55011744A JP1174480A JPS6224679B2 JP S6224679 B2 JPS6224679 B2 JP S6224679B2 JP 55011744 A JP55011744 A JP 55011744A JP 1174480 A JP1174480 A JP 1174480A JP S6224679 B2 JPS6224679 B2 JP S6224679B2
Authority
JP
Japan
Prior art keywords
hydrogen
container
metal
porous
metal hydride
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
Application number
JP55011744A
Other languages
Japanese (ja)
Other versions
JPS56109998A (en
Inventor
Nobuyuki Yanagihara
Koji Gamo
Yoshio Moriwaki
Tsutomu Iwaki
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP1174480A priority Critical patent/JPS56109998A/en
Publication of JPS56109998A publication Critical patent/JPS56109998A/en
Publication of JPS6224679B2 publication Critical patent/JPS6224679B2/ja
Granted 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
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、熱交換器を有する密閉可能な容器内
に水素を吸蔵して金属水素化物となる金属単体ま
たは合金と共に、熱伝導性と通気性のあるスポン
ジ状または繊維状金属多孔体片を内蔵した水素貯
蔵容器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to a metal element or an alloy that stores hydrogen in a sealable container having a heat exchanger to form a metal hydride, and also to improve thermal conductivity and air permeability. This invention relates to a hydrogen storage container containing a sponge-like or fibrous metal porous piece.

従来の技術 従来、水素を貯蔵する方法として、高圧気体水
素や液体水素による方法があるが、高圧気体水素
は重い耐圧容器を必要とし、液体水素は容積を小
さくすることができるが、超低温液体を取り扱う
ために、蒸発によるガス損失や、安全性の面での
十分な注意が必要である。
Conventional technology Conventionally, there are methods for storing hydrogen using high-pressure gaseous hydrogen or liquid hydrogen, but high-pressure gaseous hydrogen requires a heavy pressure-resistant container, and while liquid hydrogen can have a small volume, it is difficult to store ultra-low-temperature liquid. When handling it, sufficient care must be taken to prevent gas loss due to evaporation and safety.

発明が解決しようとする問題点 これらの問題点を解決する方法として、水素の
固形化、すなわち金属水素化物として貯蔵する方
法が提案された。この金属水素化物に対して水素
の吸蔵・放出を繰り返すと、金属水素化物は数μ
〜数10μまで微粉化され、水素貯蔵容器内の微粉
末層に粗密分布が発生しやすくなる。たとえば、
振動、衝撃などにより、とくに容器の底部になる
程、微粉末層が密になる。そしてこの部分の嵩比
重が上昇するため、空間部が著しく減少し、水素
の拡散が遅く、水素の充てん、放出時間が長くか
かるとともに、水素の貯蔵効率も低下するという
欠点を生じる。この欠点を改良するために、多孔
質で通気性のあるアルミナ発泡体、ウレタンフオ
ームなど、無機あるいは有機の粒状充てん物を収
納することが提案されている(特開昭51−16279
号公報)。ところが、これらの充てん物による改
良はそれほど顕著でなく、その原因を調べたとこ
ろ、熱伝導性が非常に悪いため、熱交換器を通し
て熱の移動を行わせる時に非常に効率が悪いこと
にあることがわかつた。
Problems to be Solved by the Invention As a method for solving these problems, a method of solidifying hydrogen, that is, storing it as a metal hydride, has been proposed. When this metal hydride is repeatedly absorbed and released hydrogen, the metal hydride becomes
It is pulverized to ~several 10 microns, and a coarse/dense distribution tends to occur in the fine powder layer inside the hydrogen storage container. for example,
Due to vibrations, shocks, etc., the fine powder layer becomes denser, especially toward the bottom of the container. Since the bulk specific gravity of this portion increases, the space is significantly reduced, hydrogen diffusion is slow, hydrogen filling and discharging time is long, and the hydrogen storage efficiency is also reduced. In order to improve this drawback, it has been proposed to contain inorganic or organic granular fillers such as porous and breathable alumina foam or urethane foam (Japanese Patent Laid-Open No. 51-16279
Publication No.). However, the improvement caused by these fillings was not so remarkable, and when we investigated the cause, we found that the thermal conductivity was very poor, making it extremely inefficient when heat was transferred through the heat exchanger. I understood.

本発明は、上記水素の拡散および水素の吸蔵・
放出速度、さらに熱導伝性などの問題を同時に解
決することを目的としたものである。
The present invention provides hydrogen diffusion and hydrogen occlusion and
The aim is to simultaneously solve issues such as release rate and thermal conductivity.

問題点を解決するための手段 上記の問題を解決するため本発明は、熱交換器
を有する密閉可能な容器内に金属水素化物ととも
に、熱伝導性と通気性のあるスポンジ状または繊
維状金属の多孔体片を充てん物全体に占める容積
比が1/4以下であり、かつ容器の上部側における
多孔体片の分散密度が、容器底部側のそれより小
さくなるよう分散させたことを特徴とする水素貯
蔵容器を提供するものである。
Means for Solving the Problems In order to solve the above-mentioned problems, the present invention provides the use of a spongy or fibrous metal material having thermal conductivity and air permeability together with a metal hydride in a sealable container having a heat exchanger. The volume ratio of the porous pieces to the entire filling is 1/4 or less, and the porous pieces are dispersed so that the dispersion density at the top side of the container is smaller than that at the bottom side of the container. The present invention provides a hydrogen storage container.

作 用 このように構成することで、充てん物全体への
熱伝導が良好となり、水素の拡散を容易にして金
属水素化物に対する水素の放出・吸蔵を高めるこ
とができる。
Effect: By configuring as described above, heat conduction to the entire filling material becomes good, hydrogen diffusion becomes easy, and hydrogen release/occlusion in the metal hydride can be enhanced.

実施例 以下、実施例とともに本発明の詳細について説
明する。
Examples Hereinafter, details of the present invention will be explained along with examples.

第1図において、1は水素ガス管で、バルブ2
と圧力計3を介して、金属容器4の先端部の結合
部5と連結されている。金属容器4には熱交換器
用の蛇状管6が取り付けられ、水や温水を導入口
7より供給し、出口8より排出する。金属容器4
内には金属水素化物9の充てん層内に熱伝導性、
通気性のあるスポンジ状もしくは繊維状金属の多
孔体片10が分散させてある。また水素導通管1
には圧力計3が取り付けてあり、水素ガスの供給
時、搬送時の容器4内の圧力がわかるようになつ
ている。
In Figure 1, 1 is a hydrogen gas pipe, and valve 2
is connected to a joint 5 at the tip of the metal container 4 via a pressure gauge 3. A serpentine tube 6 for a heat exchanger is attached to the metal container 4, and water or hot water is supplied through an inlet 7 and discharged through an outlet 8. metal container 4
There is a thermally conductive layer inside the metal hydride 9 filling layer.
Porous pieces 10 of breathable spongy or fibrous metal are dispersed therein. Also, hydrogen conduction pipe 1
A pressure gauge 3 is attached to the container 4 so that the pressure inside the container 4 can be determined when hydrogen gas is supplied and transported.

金属水素化物を構成する金属材料として、市販
のチタンとマンガンをTiMn1.5の組成比となる様
に秤量し、アーク溶解炉で数回加熱溶解して得た
TiMn1.5合金を用いた。つぎに、この合金を細か
く粉砕して長径2〜3cmの無定形粒状にし、水素
化した後試料に供した。使用した合金は6Kgであ
り、その合金の有効水素量は180ml/gであるの
で、全重量6Kg合金中に含まれる有効水素量は
1080である。なお、水素貯蔵用の容器は直径約
70mm、高さ500mmで内容積約2の用筒容器であ
る。
As the metal materials constituting the metal hydride, commercially available titanium and manganese were weighed to have a TiMn composition ratio of 1.5 and heated and melted several times in an arc melting furnace.
TiMn 1.5 alloy was used . Next, this alloy was finely ground into amorphous particles with a major axis of 2 to 3 cm, hydrogenated, and then used as a sample. The weight of the alloy used is 6Kg, and the effective amount of hydrogen in that alloy is 180ml/g, so the effective amount of hydrogen contained in the total weight of the 6Kg alloy is:
It is 1080. Note that the hydrogen storage container has a diameter of approx.
It is a cylindrical container with a length of 70 mm and a height of 500 mm and an internal volume of approximately 2.

また、熱伝導性と通気性のあるスポンジ状金属
多孔体片としては、比較的目が細かく、三次元的
に連続して連なつた空隙部を有するスポンジ状ニ
ツケル多孔体であり、多孔度90〜98%、空孔径20
〜100μ、厚さ1.5〜5.0mm、長径5〜20mm程度の
ものを採用した。
In addition, as a sponge-like porous metal piece that has thermal conductivity and air permeability, it is a sponge-like porous nickel material that has relatively fine mesh and three-dimensionally continuous voids, and has a porosity of 90. ~98%, pore size 20
~100μ, thickness 1.5~5.0mm, and major axis 5~20mm were adopted.

上記の構成の容器をAとし、従来型として金属
多孔体の代わりにアルミナ発泡体を用いたものを
B、金属水素化物のみのものをCとする。
A container having the above structure is designated as A, a conventional container using an alumina foam instead of a porous metal material is designated as B, and a container containing only metal hydride is designated as C.

第2図は水素化物TiMn1.5−Hxの水素成分xと
平衡水素解離圧力との関係を示す。
FIG. 2 shows the relationship between the hydrogen component x of the hydride TiMn 1.5 -H x and the equilibrium hydrogen dissociation pressure.

第3図は、このような特性をもつTiMn1.5−Hx
の上記各容器内における水素放出特性を示すもの
である。水素放出条件は、熱交換器に50℃の温水
を通して水素化物を加熱し、水素放出速度5/
分とした。水素放出特性は、容器内の吸蔵水素を
真空ポンプで吸引除去し、その後、完全状態にま
で水素を吸蔵させ、周囲温度25℃、1atmにおい
て水素を放出させた。
Figure 3 shows TiMn 1.5 −H x with such characteristics.
This figure shows the hydrogen release characteristics in each of the above containers. The hydrogen release conditions were as follows: 50°C hot water was passed through a heat exchanger to heat the hydride, and the hydrogen release rate was 5/5.
It was a minute. Hydrogen release characteristics were determined by sucking and removing the occluded hydrogen in the container using a vacuum pump, then allowing hydrogen to be occluded to a complete state and releasing hydrogen at an ambient temperature of 25°C and 1 atm.

これらの水素放出特性を比較すると、Cは約
700しか水素ガスを放出することができない。
この値は全水素貯蔵量1080に対して約65%の放
出率である。Bは約850の水素ガスを放出する
ことができたが、全水素貯蔵量1080に対して約
80%の放出率である。これに対してAは約1070
の水素ガスの放出量があり、全水素貯蔵量1080
に対して殆んど100%の放出率に相当する。
Comparing these hydrogen release characteristics, C is approximately
Only 700 can release hydrogen gas.
This value is a release rate of approximately 65% of the total hydrogen storage of 1080. B was able to release about 850 hydrogen gas, but the total hydrogen storage was about 1080
The release rate is 80%. On the other hand, A is about 1070
of hydrogen gas, and the total hydrogen storage capacity is 1080
This corresponds to a release rate of almost 100%.

また、従来例の1つとして、上記アルミナ発泡
体の代わりにウレタンフオームの粒状物を入れて
も、Bと同程度の水素放出率しかなかつた。しか
し、本発明の1つである金属の繊維状多孔体片を
入れた場合は、水素の放出率95%を示した。
Furthermore, as one of the conventional examples, even when urethane foam particles were substituted for the alumina foam, the hydrogen release rate was only about the same as B. However, when a metal fibrous porous piece according to the present invention was inserted, the hydrogen release rate was 95%.

このように、本発明によれば水素の放出速度が
従来型と比べて著しく速く、貯蔵水素を有効に利
用できる。これは、金属容器内の金属水素化物の
中に通気性のみでなく、熱伝導性もよい金属多孔
体片を分散させることにより、熱交換器からの熱
放散あるいは熱供給が、この金属多孔体片を通し
て、すばやく全体の金属水素化物に行われ、全金
属水素化物の加熱が円滑に進行するためである。
さらに、通気性の良い金属多孔体であるから、水
素の拡散、移動がより効率良く進行することも、
その理由の1つにあげられる。また金属水素化物
自体の荷重で、容器の底部になる程高密度になら
ないようにするためにも、この金属多孔体の存在
は水素放出特性を確保する上で重要な役割を果た
す。
As described above, according to the present invention, the hydrogen release rate is significantly faster than that of the conventional type, and stored hydrogen can be used effectively. By dispersing porous metal pieces that have good heat conductivity as well as air permeability in the metal hydride in the metal container, heat dissipation or heat supply from the heat exchanger is carried out through the porous metal. This is because the whole metal hydride is heated quickly through the piece, and the heating of the whole metal hydride proceeds smoothly.
Furthermore, since it is a porous metal material with good air permeability, hydrogen diffusion and movement proceed more efficiently.
This is one of the reasons. In addition, the presence of this metal porous body plays an important role in ensuring hydrogen release characteristics, in order to prevent the density from becoming so high that it reaches the bottom of the container due to the load of the metal hydride itself.

これに反して、従来型Cは、微粉化した金属水
素化物の荷重で、底部の方が高密度状態になり、
水素の拡散を阻止し、温水で加熱しているにもか
かわらず、水素ガスの放出量が減少している。水
素の拡散を良くするために、アルミナ発泡体や樹
脂発泡体を金属水素化物中に入れると、水素ガス
の放出量は少し増加するが、これらの熱伝導性が
よくないので、熱交換器からの熱移動が全金属水
素化物にわたつて十分に行われず、全金属水素化
物の加熱が円滑に進行しないので効果は少ない。
On the other hand, in conventional type C, the bottom part becomes denser due to the load of finely divided metal hydride.
Despite preventing hydrogen diffusion and heating with hot water, the amount of hydrogen gas released is reduced. If alumina foam or resin foam is placed in the metal hydride to improve hydrogen diffusion, the amount of hydrogen gas released will increase slightly, but since these have poor thermal conductivity, they will not be able to escape from the heat exchanger. heat transfer is not sufficiently carried out over all metal hydrides, and heating of all metal hydrides does not proceed smoothly, so the effect is small.

実施例ではTiMn1.5合金を用いたが、他の金属
材料を用いることができ、特に少なくともTiと
Mnを含むTiMn系2元もしくは多元系が優れてい
る。
Although a TiMn 1.5 alloy was used in the examples, other metal materials can be used, especially at least Ti and
TiMn-based binary or multi-component systems containing Mn are excellent.

またスポンジ状多孔体、繊維状多孔体を構成す
る金属としては、鉄、銅、亜鉛などもよい。これ
ら多孔体の占める容積は、充てん物全体の容積の
約1/4以下であることが望ましい。1/4以上になる
と水素貯蔵量が減少する。そして、容器上部の水
素の供給側になるにつれて、前記多孔体片の分散
密度を小さくし、金属水素化物の量を多くするの
が好ましい。すなわち、金属容器の底部側には多
孔体片の量を多くして、相対的に、金属水素化物
の量を少なくするのである。この理由は、容器の
底部における金属水素化物の高密度化を防止する
ことと、水素放出時の吸熱反応による温度低下
で、底部の金属水素化物からの水素放出が規制さ
れるので、金属水素化物の量を少なくしておき、
温度が低下する前にすべての水素を放出させてお
くためである。この構成を採用することにより、
水素の放出量を向上させることができる。
Further, as the metal constituting the sponge-like porous body and the fibrous porous body, iron, copper, zinc, etc. may be used. The volume occupied by these porous bodies is preferably about 1/4 or less of the volume of the entire filling. When it becomes 1/4 or more, the amount of hydrogen storage decreases. Then, it is preferable that the dispersion density of the porous body pieces is decreased and the amount of metal hydride is increased toward the hydrogen supply side in the upper part of the container. That is, the amount of porous material pieces is increased on the bottom side of the metal container, and the amount of metal hydride is relatively reduced. The reason for this is to prevent the metal hydride from becoming denser at the bottom of the container, and because the temperature drop due to the endothermic reaction during hydrogen release restricts hydrogen release from the metal hydride at the bottom. Keep the amount of
This is to ensure that all the hydrogen is released before the temperature drops. By adopting this configuration,
The amount of hydrogen released can be improved.

このように本発明は金属水素化物の貯蔵容器と
して重要な、熱伝導性と水素ガスの通気性の両方
の性能を改善したものである。この本発明と、先
に本発明者らが提案したスポンジ状金属多孔体内
に金属水素化物を保持させた特開昭55−126199号
公報記載の容器と比較しても本発明は金属水素化
物の有効伝熱面積が増大し、熱伝導性が一層向上
すると共に、構成が簡単で実用的な貯蔵容器を提
供できるものである。
As described above, the present invention improves both the thermal conductivity and hydrogen gas permeability, which are important for a metal hydride storage container. Comparing this invention with the container described in JP-A-55-126199 in which a metal hydride is held in a sponge-like porous metal body previously proposed by the present inventors, the present invention is a The effective heat transfer area is increased, the thermal conductivity is further improved, and it is possible to provide a storage container that is simple in structure and practical.

発明の効果 以上の様に、本発明によれば水素の拡散を容易
にし、水素の放出・吸蔵能力を向上させ、しかも
その速度を速くすることができる。
Effects of the Invention As described above, according to the present invention, it is possible to facilitate hydrogen diffusion, improve the hydrogen release/storage ability, and increase the speed.

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

第1図は本発明の実施例の水素貯蔵容器の縦断
面図、第2図はTiMn1.5−Hxの水素成分xと平衡
水素解離圧力との関係を示す図、第3図は水素貯
蔵容器の水素放出特性の比較を示す。 1……水素ガス管、4……容器、6……熱交換
用管、9……金属水素化物、10……多孔体片。
FIG. 1 is a longitudinal cross-sectional view of a hydrogen storage container according to an embodiment of the present invention, FIG. 2 is a diagram showing the relationship between the hydrogen component x of TiMn 1.5 -H x and the equilibrium hydrogen dissociation pressure, and FIG. A comparison of hydrogen release characteristics of storage vessels is shown. DESCRIPTION OF SYMBOLS 1... Hydrogen gas pipe, 4... Container, 6... Heat exchange tube, 9... Metal hydride, 10... Porous body piece.

Claims (1)

【特許請求の範囲】[Claims] 1 熱交換器を有する密閉可能な容器内に、水素
を吸蔵して金属水素化物となる金属単体または合
金の粒子を充てんするとともに、前記充てん層内
に熱伝導性と通気性のあるスポンジ状もしくは繊
維状金属の多孔体片を、充てん物全体に占める容
積比が1/4以下であり、かつ容器の上部側におけ
る多孔体片の分散密度が容器底部側のそれより小
さくなるよう分散させたことを特徴とする水素貯
蔵容器。
1 A sealable container having a heat exchanger is filled with particles of a single metal or alloy that absorbs hydrogen and becomes a metal hydride, and the filling layer is filled with a sponge-like or alloy material having thermal conductivity and air permeability. The porous pieces of fibrous metal are dispersed so that the volume ratio of the entire filling is 1/4 or less, and the dispersion density of the porous pieces on the top side of the container is smaller than that on the bottom side of the container. A hydrogen storage container featuring:
JP1174480A 1980-02-01 1980-02-01 Hydrogen storing container Granted JPS56109998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1174480A JPS56109998A (en) 1980-02-01 1980-02-01 Hydrogen storing container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1174480A JPS56109998A (en) 1980-02-01 1980-02-01 Hydrogen storing container

Publications (2)

Publication Number Publication Date
JPS56109998A JPS56109998A (en) 1981-08-31
JPS6224679B2 true JPS6224679B2 (en) 1987-05-29

Family

ID=11786523

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1174480A Granted JPS56109998A (en) 1980-02-01 1980-02-01 Hydrogen storing container

Country Status (1)

Country Link
JP (1) JPS56109998A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61144499A (en) * 1984-12-19 1986-07-02 Sanyo Electric Co Ltd Metal hydride container
DE10022803B4 (en) * 2000-05-10 2006-07-06 GfE Gesellschaft für Elektrometallurgie mbH Tank for the reversible storage of hydrogen

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2841333A1 (en) * 1978-09-21 1980-03-27 Mannesmann Ag HEAT EXCHANGER

Also Published As

Publication number Publication date
JPS56109998A (en) 1981-08-31

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