JPS59141402A - Metal hydride reactor vessel - Google Patents

Metal hydride reactor vessel

Info

Publication number
JPS59141402A
JPS59141402A JP58015983A JP1598383A JPS59141402A JP S59141402 A JPS59141402 A JP S59141402A JP 58015983 A JP58015983 A JP 58015983A JP 1598383 A JP1598383 A JP 1598383A JP S59141402 A JPS59141402 A JP S59141402A
Authority
JP
Japan
Prior art keywords
hydrogen
metal hydride
porous tube
container
opening
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
JP58015983A
Other languages
Japanese (ja)
Other versions
JPS6313922B2 (en
Inventor
Michiyoshi Nishizaki
西崎 倫義
Minoru Miyamoto
稔 宮本
Yasushi Nakada
泰詩 中田
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP58015983A priority Critical patent/JPS59141402A/en
Publication of JPS59141402A publication Critical patent/JPS59141402A/en
Publication of JPS6313922B2 publication Critical patent/JPS6313922B2/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)
  • Sorption Type Refrigeration Machines (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

PURPOSE:The titled reactor vessel that is provided inside with a porous tube which permeates hydrogen but not metal hydride and contains a fibrous material or metallic coils, thus avoiding its own breakage by the volume expansion of the hydride and maintaining the paths for hydrogen. CONSTITUTION:The tubular pressure vessel 2 is made of copper, stainless steel or aluminum resistant to the volume change of the metal hydride on its absorption and release of hydrogen and to the hydrogen pressure, further has an opening 1 at the top end for passing through hydrogen and a cross-sectional diaphragm 3 near the opening 1. A porous tube 4 which permeates hydrogen but not the metal hydride is air-tightly fixed to the opening of the diaphragm 3 at one opening end 5 and the other end is extended to the bottom the vessel 2 and closed to form the path for hydrogen. In general, the opening end of the tube 4 is equipped with a filter 6 which permeate hydrogen but not the metal hydride. The porous tube 4 is filled with a fibrous material such as glass or carbon fibers 7 so that the tube may not be crushed by the volume expansion of the hydride on hydrogen absorption.

Description

【発明の詳細な説明】 本発明は金属水素化物反応容器に関する。[Detailed description of the invention] FIELD OF THE INVENTION This invention relates to metal hydride reaction vessels.

ある種の金属や合金が発熱的に水素を吸蔵して金属水素
化物を形成し、また、この金属水素化物が可逆的に吸熱
的に水素を放出することが知られており、近年、このよ
うな金属水素化物の特性を利用した水素供給装置、ヒー
トポンプ等、種々の金属水素化物装置が提案されている
It is known that certain metals and alloys exothermically absorb hydrogen to form metal hydrides, and that these metal hydrides reversibly and endothermically release hydrogen. Various metal hydride devices have been proposed, such as hydrogen supply devices and heat pumps, which utilize the characteristics of metal hydrides.

このような金属水素化物装置において、金属水素化物は
密閉した反応容器内に充填されて、水素の吸蔵放出を行
なう。第1図はこのような金属水素化物反応容器の従来
の一例を示し、一端に水素出入口1を有する耐圧容器2
は、その水素出入口に近接して水素を透過しない隔壁3
、を容器横断方向に有し、水素を透過するが金属水素化
物は透過しない多孔質管4がその開口端5において、上
記隔壁の通孔に気密的に支持され、後端は容器底部にま
で容器軸に沿って延びて、水素通路を形成している。こ
の多孔質管の上記開口端は通常、水素を透過するが、金
属水素化物は透過しないフィルター6を介して容器の水
素出入口に連通されている。金属水素化物は、容器内の
多孔質管外の空間に充填される。
In such a metal hydride device, metal hydride is filled in a closed reaction vessel to absorb and release hydrogen. FIG. 1 shows a conventional example of such a metal hydride reaction vessel, which includes a pressure vessel 2 having a hydrogen inlet/outlet 1 at one end.
is a partition wall 3 that does not allow hydrogen to permeate in the vicinity of the hydrogen inlet/outlet.
, which has a porous tube 4 in the transverse direction of the container and which permeates hydrogen but not metal hydrides, is airtightly supported at its open end 5 in the through hole of the partition wall, and its rear end extends to the bottom of the container. It extends along the container axis and forms a hydrogen passageway. The open end of this porous tube is normally connected to the hydrogen inlet/outlet of the container via a filter 6 that permeates hydrogen but not metal hydrides. The metal hydride fills the space outside the porous tube within the container.

このような金属水素化物容器において、金属水素化物の
水素吸蔵時には、水素は容器の水素出入口からフィルタ
ーを経て多孔質管の開口端から管内に入り、多孔質管に
より容器内に分配されて、金属水素化物の充填層内に拡
散し、一方、水素放出時には同様に、金属水素化物から
放出された水素は多孔質管に入り、その開口端を経て容
器水素出入口から容器外に導かれる。
In such a metal hydride container, when the metal hydride absorbs hydrogen, hydrogen enters the pipe from the open end of the porous tube through the hydrogen inlet/outlet of the container, passes through the filter, is distributed inside the container by the porous tube, and is absorbed into the metal hydride. During hydrogen release, the hydrogen released from the metal hydride enters the porous tube and is led out of the container from the hydrogen inlet/outlet through the open end of the porous tube.

ここに、多孔質管は水素のみを透過するように40〜8
0%の気孔率を有して、数μの濾過性能を備えると共に
、金属水素化物の水素吸蔵放出時の体積変化を吸収し、
耐圧容器への応力を緩和し得るように、弾性を備えたポ
リエチレン、ポリプロピレン、ポリテトラフルオロエチ
レン等の合成樹脂より製作されていることが多い。
Here, the porous tube has a diameter of 40 to 8 to allow only hydrogen to pass through.
It has a porosity of 0%, has a filtration performance of several microns, and absorbs volume changes when metal hydride absorbs and releases hydrogen.
They are often made of elastic synthetic resins such as polyethylene, polypropylene, and polytetrafluoroethylene so as to relieve stress on the pressure container.

しかし、このような反応容器によれば、金属水素化物は
水素を吸蔵する際にその体積を膨張するので、このとき
に多孔質管はその弾性復元力にかかわらずに圧しつぶさ
れ、水素通路として機能しなくなることがある。このた
め、多孔質管の強度を高めるために気孔率を小さくすれ
ば、水素の流通時の圧損が大きくなる。
However, according to such a reaction vessel, the metal hydride expands in volume when it absorbs hydrogen, and at this time the porous tube is crushed regardless of its elastic restoring force, and is used as a hydrogen passage. It may stop working. For this reason, if the porosity is reduced to increase the strength of the porous tube, the pressure loss during hydrogen flow will increase.

本発明は上記した問題を解決するためになされたもので
あって、多孔質管が金属水素化物の膨張時の応力によく
耐えて、圧しつぶされることがない金属水素化物反応容
器を提供することを目的とする。
The present invention has been made in order to solve the above-mentioned problems, and it is an object of the present invention to provide a metal hydride reaction vessel in which a porous tube can well withstand stress during expansion of metal hydride and will not be crushed. With the goal.

本発明の金属水素化物反応容器は、一端に水素出入口を
宣する容器と、この容器内にその軸方向に延びてml設
され、水素を透過するが、金属水素化物を透過しない多
孔質管と、この多孔質管に充填された繊維材又は金属コ
イルとからなることを特徴とするものである。
The metal hydride reaction container of the present invention includes a container having a hydrogen inlet/outlet at one end, and a porous tube extending in the axial direction of the container and permeating hydrogen but not metal hydride. The porous tube is filled with a fiber material or a metal coil.

以下に柔施例を示す図面に基づいて本発明を説明する。The present invention will be explained below based on the drawings showing flexible embodiments.

尚、図面において、第1図と同じ部材は同じ参照番号を
付しである。
In the drawings, the same members as in FIG. 1 are given the same reference numerals.

第2図は本発明の金属水素化物反応容器の一実施例を示
し、管状の耐圧容器2は、金属水素化物の水素の吸蔵放
出に際しての体積変化や水素圧に耐えると共に、耐水素
脆性を有すれば特に制限されないが、普通、銅やステン
レス鋼、アルミニウム等からなり、前記したように、そ
の前端に水素出入口1を有し、この出入口に近接して容
器を横断する隔壁3を有する。水素を透過するが、金属
水素化物を透過しない多孔質管4が、その一端の開口端
5において上記隔壁の通孔に気密的に固定され、他端は
は容器軸方向に容器底部まで延びて封止され、水素通路
を形成している。金属水素化物の水素の吸蔵放出に伴っ
て、金属水素化物が容器外に飛散するのを防止するため
に、通常、多孔質管の開口端には、水素は透過するが、
金属水素化物は透過しないフィルター6が多孔質管の開
口端に取付けられている。フィルターは、例えば、焼結
金属や樹脂多孔質体等からなり、数μの濾過性能を有す
る。
FIG. 2 shows an embodiment of the metal hydride reaction vessel of the present invention, and the tubular pressure vessel 2 is resistant to volume changes and hydrogen pressure when the metal hydride absorbs and releases hydrogen, and has hydrogen embrittlement resistance. Although not particularly limited, it is usually made of copper, stainless steel, aluminum, etc., and as described above, has a hydrogen inlet/outlet 1 at its front end, and a partition wall 3 extending across the container in proximity to this inlet/outlet. A porous tube 4 that is permeable to hydrogen but not permeable to metal hydrides is hermetically fixed at one open end 5 to the through hole in the partition wall, and the other end extends in the axial direction of the container to the bottom of the container. It is sealed and forms a hydrogen passage. In order to prevent the metal hydride from scattering outside the container as the metal hydride absorbs and releases hydrogen, hydrogen usually passes through the open end of the porous tube.
A filter 6, which is impermeable to metal hydrides, is attached to the open end of the porous tube. The filter is made of, for example, sintered metal or porous resin, and has a filtration performance of several microns.

本発明の金属水素化物反応容器においては、金属水素化
物の水素吸蔵時の体積膨張によっても圧しつぶされない
ように、上記多孔質管内に繊維材7が充填されている。
In the metal hydride reaction vessel of the present invention, the porous tube is filled with fibrous material 7 so as not to be crushed by the volumetric expansion of the metal hydride when it absorbs hydrogen.

繊維材としては、ガラス繊維、炭素繊維、セラミック繊
維、金属繊維等のほか、ポリアミド等の有機繊維も用い
られ、繊維材間の空隙が水素通路をなす。これらの繊維
材ば、多孔質管の軸方向への水素の流通が容易であるよ
うに、好ましくは、糸束やロープ等の暢維東として多孔
質管の軸方向に延びるように装入されるが、しかし、繊
維材の態様はこれらに限定されるものではない。
As the fiber material, in addition to glass fiber, carbon fiber, ceramic fiber, metal fiber, etc., organic fibers such as polyamide are also used, and the voids between the fiber materials form hydrogen passages. These fibrous materials are preferably charged so as to extend in the axial direction of the porous tube in the form of yarn bundles, ropes, etc., so that hydrogen can easily flow in the axial direction of the porous tube. However, the embodiment of the fibrous material is not limited to these.

第3図は本発明の金属水素化物反応容器の別の実・施例
を示し、上記隔壁に代えてガラスウール、セラミツル繊
維等の繊維材料8が容器水素出入口1に近接して容器2
の横断方向に層状に充填されてフィルター6を構成し、
多孔質管4はその開口@5をこの繊維材料の層内に挿入
されて、この繊維材料を介し、て容器の水素出入口と連
通され、多孔質管自体は容器内に充填された金属水素化
物によって容器内心ζ支持されている。更に、この実施
例においては、多孔質管内には上記繊維材に代えて金属
コイル9が挿入されており、繊維材と同様に多孔質管が
金属水素化物の体積膨張に耐えるようにしている。
FIG. 3 shows another embodiment of the metal hydride reaction vessel of the present invention, in which a fiber material 8 such as glass wool or ceramic fiber is placed close to the hydrogen inlet/outlet 1 of the vessel in place of the partition wall.
are packed in layers in the transverse direction to constitute the filter 6,
The porous tube 4 has its opening @5 inserted into this layer of fibrous material and communicates with the hydrogen inlet/outlet of the container through this fibrous material, and the porous tube itself is connected to the metal hydride filled in the container. The inner center of the container ζ is supported by Furthermore, in this embodiment, a metal coil 9 is inserted in the porous tube instead of the fiber material, so that the porous tube can withstand the volumetric expansion of the metal hydride in the same way as the fiber material.

また、第4図は更に別の実施例を示す。容器2は、第2
図に示した実施例と同様に、その水素出入口1に近接し
て容器を横断する隔壁3を有すると共に、この隔壁にフ
ィルター6が取付けられている。多孔質管4はその両端
が封止され、内11+に繊維材7が充填されていると共
に、一方の封止端が上記フィルターに近接するように、
・容器内の金属水素化物自体により支持されている。こ
の容器の場合には、金属水素化物の水素吸蔵時には、水
素はフィルターを経て、金属水素化物の充填層から水素
の透過抵抗の小さい多孔質管内に入り、多孔質管により
容器軸方向に分配されて後に、再び金属水素化物の充填
層に拡散する。金属水素化物の水素の放出時も、水素は
多孔質管内に入り、再び金属水素化物充填層を経て、フ
ィルターから水素出入口に向かう。
Moreover, FIG. 4 shows yet another embodiment. Container 2 is the second
Similar to the embodiment shown in the figure, it has a partition wall 3 extending across the container in proximity to the hydrogen inlet/outlet port 1, and a filter 6 is attached to this partition wall. Both ends of the porous tube 4 are sealed, and the inside 11+ is filled with a fiber material 7, and one sealed end is placed close to the filter.
- Supported by the metal hydride itself within the container. In the case of this container, when the metal hydride absorbs hydrogen, hydrogen passes through the filter, enters the porous tube with low hydrogen permeation resistance from the packed layer of metal hydride, and is distributed in the axial direction of the container by the porous tube. After that, it diffuses back into the packed layer of metal hydride. When hydrogen is released from the metal hydride, the hydrogen enters the porous tube, passes through the metal hydride packed bed again, and heads from the filter to the hydrogen inlet/outlet.

尚、本発明においては、耐圧容器の両端に水素出入口を
設け、各出入口において上記したように水素の流通を可
能にすることができるのはいうまでもない。
It goes without saying that in the present invention, hydrogen inlets and outlets can be provided at both ends of the pressure vessel to allow hydrogen to flow through each inlet and outlet as described above.

更に、本発明においては、必要に応じて容器内に容器内
壁から半径方向に延びるフィン(図示せず)を適宜数配
設して、金属水素化物と容器壁との熱伝導性を高めるこ
ともできる。
Furthermore, in the present invention, an appropriate number of fins (not shown) extending in the radial direction from the inner wall of the container may be provided in the container as necessary to increase the thermal conductivity between the metal hydride and the container wall. can.

本発明の金属水素化物反応容器によれば、以上のように
、多孔質管内に繊維材又は金属コイルが挿入されている
ので、金属水素化物が水素吸蔵時に体積膨張しても、多
孔質管は圧しつぶされることがなく、しかも、管内には
水素の通路を確保することができる。
According to the metal hydride reaction vessel of the present invention, as described above, since the fiber material or the metal coil is inserted into the porous tube, even if the metal hydride expands in volume when absorbing hydrogen, the porous tube remains unchanged. There is no crushing, and a passage for hydrogen can be secured within the tube.

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

第1図は従来の金属水素化物反応容器を示す軸方向断面
図、第2図乃至第4図は本発明の金属水素化物反応容器
を示す軸方向断面図である。 1・・・水素出入口、2・・・耐圧容器、3・・・隔壁
、4・・・多孔質管、5・・・多孔質管開口端、6・・
・フィルター、7・・・繊維材、8・・・繊維材料、9
・・・金属コイル。 特許出願人 積水化学工業株式会社 代表者 藤 沼 基 利 第2図 第:3図 第4図 6
FIG. 1 is an axial sectional view showing a conventional metal hydride reaction vessel, and FIGS. 2 to 4 are axial sectional views showing the metal hydride reaction vessel of the present invention. DESCRIPTION OF SYMBOLS 1... Hydrogen inlet/outlet, 2... Pressure-resistant container, 3... Partition wall, 4... Porous pipe, 5... Porous pipe opening end, 6...
・Filter, 7... Fiber material, 8... Fiber material, 9
...Metal coil. Patent applicant Sekisui Chemical Co., Ltd. Representative Mototoshi Fujinuma Figure 2: Figure 3 Figure 4 Figure 6

Claims (1)

【特許請求の範囲】[Claims] (11一端に水素出入口を有する容器と、この容器内に
その軸方向に延びて配設され、水素を透過するが、金属
水素化物を透過しない多孔質管と、この多孔質哨に充填
された繊維材又は金属コイルとからなることを特徴とす
る金属水素化物反応容器。
(11) A container having a hydrogen inlet/outlet at one end, a porous tube disposed extending in the axial direction of the container and permeable to hydrogen but not permeable to metal hydride, and filled in the porous tube. A metal hydride reaction vessel characterized by being made of a fibrous material or a metal coil.
JP58015983A 1983-02-01 1983-02-01 Metal hydride reactor vessel Granted JPS59141402A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58015983A JPS59141402A (en) 1983-02-01 1983-02-01 Metal hydride reactor vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58015983A JPS59141402A (en) 1983-02-01 1983-02-01 Metal hydride reactor vessel

Publications (2)

Publication Number Publication Date
JPS59141402A true JPS59141402A (en) 1984-08-14
JPS6313922B2 JPS6313922B2 (en) 1988-03-28

Family

ID=11903904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58015983A Granted JPS59141402A (en) 1983-02-01 1983-02-01 Metal hydride reactor vessel

Country Status (1)

Country Link
JP (1) JPS59141402A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5678405A (en) * 1979-11-30 1981-06-27 Sanyo Electric Co Ltd Hydrogenation or metal of alloy

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5678405A (en) * 1979-11-30 1981-06-27 Sanyo Electric Co Ltd Hydrogenation or metal of alloy

Also Published As

Publication number Publication date
JPS6313922B2 (en) 1988-03-28

Similar Documents

Publication Publication Date Title
JP5661636B2 (en) Pressure vessel for storing pressurized gaseous media
GB1581639A (en) Storage of gas
JP2623245B2 (en) Active metal bead
JP2008303956A (en) Hydrogen storage tank
US3142354A (en) Sound absorption device and method of manufacture
JP2004209418A (en) Hollow fiber membrane module
JPS627407A (en) Double-ported hollow fiber permeating device
JPS59141402A (en) Metal hydride reactor vessel
CN101084159B (en) Recombination device
JP2008196575A (en) Hydrogen storage tank
JP4890938B2 (en) Gas separation tube housing structure
JPS59146901A (en) Metallic hydride reaction vessel and its manufacture
JPS5925956B2 (en) metal hydride container
JPS58194703A (en) Reactor for metal hydride
JPS59141403A (en) Metal hydride reactor vessel
JPS6350281B2 (en)
JPS5899103A (en) Reactor for metallic hydride
JP2000191301A (en) Metal hydride reactor
JPS5899104A (en) Reactor for metallic hydride
JPS58145601A (en) Reaction vessel for metal hydride
CN101248320B (en) Thermochemical reactor for cooling and/or heating device
JPS62251600A (en) Hydrogen flow material for metal hydride reaction container
JP2002139199A (en) Metal hydride reactor
JP7800388B2 (en) pressure vessel
JP2002154801A (en) Vent material for hydrogen storage container