JPH0433721B2 - - Google Patents

Info

Publication number
JPH0433721B2
JPH0433721B2 JP60033698A JP3369885A JPH0433721B2 JP H0433721 B2 JPH0433721 B2 JP H0433721B2 JP 60033698 A JP60033698 A JP 60033698A JP 3369885 A JP3369885 A JP 3369885A JP H0433721 B2 JPH0433721 B2 JP H0433721B2
Authority
JP
Japan
Prior art keywords
heat
metal hydride
container
heat transfer
hydrogen
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
JP60033698A
Other languages
Japanese (ja)
Other versions
JPS61197898A (en
Inventor
Naojiro Honda
Ikuro Yonezu
Kazuhiko Harima
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 JP60033698A priority Critical patent/JPS61197898A/en
Publication of JPS61197898A publication Critical patent/JPS61197898A/en
Publication of JPH0433721B2 publication Critical patent/JPH0433721B2/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)
  • Hydrogen, Water And Hydrids (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (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水素吸収による発熱反
応時における機械的強度を考慮した金属水素化物
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 that takes into consideration mechanical strength during an exothermic reaction due to hydrogen absorption of the metal hydride.

(ロ) 従来の技術 金属水素化物の水素吸収、放出反応を利用して
蓄熱や水素貯蔵等を行なう場合、金属水素化物は
水素加圧下での反応が進められることから耐圧容
器が必要となる。また、金属水素化物の水素化反
応に伴う熱授受を行なうための熱交換器が必要不
可欠となる。尚、金属水素化物は脱水素化して元
の金属に戻るが、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 When storing heat or storing hydrogen by utilizing the hydrogen absorption and release reactions of metal hydrides, a pressure-resistant container is required because the reaction of metal hydrides proceeds under hydrogen pressure. Furthermore, a heat exchanger is essential for transferring heat accompanying the hydrogenation reaction of metal hydrides. Note that metal hydrides are dehydrogenated to return to their original metals, and in this specification, this case is also referred to as metal hydride.

これらの点を考慮して、従来、例えば特開昭58
−47989号公報に見られるように、同心軸上に複
数の円筒体を配設し、中心円筒を水素ガスは通す
が金属水素化物は通さないフイルタ材で構成して
水素出入導管とし、その外側の円筒体に金属水素
化物を充填し、更にその外側の円筒体に熱交換用
熱媒を流すようにしたものが提案されている。
Taking these points into consideration, conventionally, for example,
As seen in Publication No. 47989, a plurality of cylindrical bodies are arranged on a concentric axis, and the central cylinder is made of a filter material that allows hydrogen gas to pass through but not metal hydrides, forming a hydrogen inlet/outlet conduit, and the outside It has been proposed that a cylindrical body is filled with a metal hydride, and a heat medium for heat exchange is allowed to flow through the cylindrical body outside the cylindrical body.

しかし、このような従来の容器構造では、水素
吸収を伴う発熱反応時、熱応力により金属水素化
物充填容器部分に亀裂が入り、容器破壊に至るお
それがあることが判つてきた。
However, in such a conventional container structure, it has been found that during an exothermic reaction accompanied by hydrogen absorption, the metal hydride-filled container portion may crack due to thermal stress, leading to the container being destroyed.

即ち、金属水素化物が充填収納される金属水素
化物充填部と熱交換部との境界面は熱伝等の良い
材質を用いる必要があり、強度面で多少の犠牲が
が強いられる。一方、金属水素化物は、水素放出
時には吸熱反応となり冷却されるのであまり問題
は生じないが、水素吸収による発熱反応時、シヨ
ツクが加わると爆発的に反応を行ない、急激に発
熱する。これにより、金属水素化物充填部と熱交
換部の境界面に大きな熱応力が発生して亀裂が入
り、容器破壊に至るおそれがあることが判つてき
た。
That is, it is necessary to use a material with good heat conductivity for the interface between the metal hydride filling part where the metal hydride is filled and stored and the heat exchange part, which requires some sacrifice in terms of strength. On the other hand, when metal hydrides release hydrogen, they undergo an endothermic reaction and are cooled, so this does not cause much of a problem, but when a shock is applied during an exothermic reaction due to hydrogen absorption, they react explosively and rapidly generate heat. It has been found that this causes large thermal stress to occur at the interface between the metal hydride filling section and the heat exchange section, causing cracks, which may lead to container failure.

(ハ) 発明が解決しようとする問題点 本発明は上記の点に鑑み、金属水素化物の水素
吸収時の発熱による容器破壊を未然に防止し得る
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 In view of the above-mentioned points, the present invention aims to provide a metal hydride container that can prevent the container from being destroyed due to heat generated when hydrogen is absorbed by the metal hydride. .

(ニ) 問題点を解決するための手段 このため本発明は、従来のように熱媒を流す熱
交換部を外部に配置する代りに内部に配置して金
属水素化物充填部を外部に配置し、その境界面の
内面側を凹凸状に形成すると共に、その肉厚部分
に中空部を設け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, instead of arranging the heat exchange part through which the heat medium flows outside as in the conventional case, it is arranged inside and the metal hydride filling part is arranged outside. , is characterized in that the inner surface of the boundary surface is formed into an uneven shape, and a hollow portion is provided in the thick portion.

(ホ) 作用 金属水素化物の水素吸収による発熱反応時、発
生した熱は境界面を通して熱媒に伝導されるが、
水素化反応が急激に起きた場合、発生する熱のた
め境界面の金属水素化物側が急激に温度が上り熱
膨張するのに対し、熱媒側は熱伝達媒体により熱
が奪われそれ程温度が上らず、境界面に大きな熱
応力が生じる。従来は境界面の内側に金属水素化
物、外側に熱媒を配していたため境界面が発生す
る熱応力に耐え切れず変形していた。しかし、本
発明のように境界面の内側に熱媒、外側に金属水
素化物を配することにより、熱応力は外側に向つ
て発散される上、内側に向う熱応力は境界内面に
形成された凹凸部と、肉厚内部に形成された中空
部により吸収され、容器破壊を未然に防止するこ
とができる。
(e) Effect During the exothermic reaction due to hydrogen absorption of metal hydrides, the generated heat is conducted to the heating medium through the interface, but
When a hydrogenation reaction occurs rapidly, the metal hydride side of the interface rapidly rises in temperature due to the heat generated and thermally expands, whereas the heat transfer medium side loses heat and the temperature rises to a large extent. large thermal stress is generated at the interface. Conventionally, metal hydrides were placed on the inside of the interface and a heating medium was placed on the outside, resulting in the interface being unable to withstand the thermal stress and deforming. However, by arranging the heat medium on the inside of the interface and the metal hydride on the outside as in the present invention, thermal stress is dissipated outward, and inward thermal stress is formed on the inner surface of the boundary. It is absorbed by the uneven parts and the hollow part formed inside the thick wall, and can prevent the container from breaking.

(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断面図を示
したものである。これらの図において、耐圧容器
1は金属水素化物2および伝熱フイン3を収納す
る容器本体部11と蓋部12とから成り、そのフ
ランジ部11a,12aをボルト4、ナツト5で
接合することにより、内部を気密、耐圧的に保持
している。その耐圧容器1の本体側端部11bと
蓋部12のほぼ中央部を気密に貫通して熱媒を流
す伝熱管6が配設されると共に、更に蓋部12に
は水素ガスを供給、排出するバルブ7付き水素導
管8が取り付けられている。
FIG. 1 is a side sectional view of a metal hydride container according to an embodiment of the present invention, and FIG. 2 is a sectional view taken along line A-A thereof. In these figures, a pressure-resistant container 1 consists of a container main body 11 and a lid 12 that house a metal hydride 2 and a heat transfer fin 3, and whose flanges 11a and 12a are joined with bolts 4 and nuts 5. The interior is kept airtight and pressure resistant. A heat transfer tube 6 is installed to airtightly pass through the main body side end 11b of the pressure vessel 1 and the approximate center of the lid 12 to flow a heat medium, and hydrogen gas is further supplied to and discharged from the lid 12. A hydrogen conduit 8 with a valve 7 is attached.

耐圧容器1内部には水素ガスは通すが金属水素
化物粉体は通し得ない断熱材9が一面に張り巡ら
され、その内側に金属水素化物2、伝熱フイン3
は伝熱管6が配置されている。即ち、伝熱フイン
3は伝熱管6の外周面上等間隔に軸方向に沿つて
複数枚固定されると共に、その複数枚の伝熱フイ
ン3によつて仕切られる伝熱管6と断熱材9との
間に金属水素化物2が分配収納されている。ま
た、伝熱管6と本体側端面11bおよび蓋部12
の間は溶接により気密に固着されている。
A heat insulating material 9 that allows hydrogen gas to pass through but not metal hydride powder is placed inside the pressure vessel 1, and inside the heat insulating material 9, a metal hydride 2 and a heat transfer fin 3 are placed.
A heat exchanger tube 6 is arranged. That is, a plurality of heat transfer fins 3 are fixed along the axial direction at equal intervals on the outer peripheral surface of the heat transfer tube 6, and the heat transfer tube 6 and the heat insulating material 9 are partitioned by the plurality of heat transfer fins 3. A metal hydride 2 is distributed and housed between them. In addition, the heat exchanger tube 6, the main body side end surface 11b, and the lid part 12
The space between them is welded to ensure an airtight seal.

伝熱管6の内側は、第2図に示すように軸方向
と垂直な断面が凹凸状に形成されている。また、
その伝熱管6の内面に形成される肉厚凸条部には
軸方向に沿つて複数個の中空部10が形成されて
いる。
As shown in FIG. 2, the inside of the heat transfer tube 6 has an uneven cross section perpendicular to the axial direction. Also,
A plurality of hollow portions 10 are formed along the axial direction in the thick-walled convex portion formed on the inner surface of the heat exchanger tube 6.

以上の構成で、熱交換作用は以下の通り行なわ
れる。即ち、蓄熱時、伝熱管6内部を矢印方向に
流れる熱媒の熱は伝熱管6の凹凸条部により効率
良く伝熱管6に伝わり、更にその表面および伝熱
フイン3の表面から金属水素化物2に効率良く伝
導される。これにより、金属水素化物2は脱水素
化反応を生じ、放出される水素ガスは断熱材9を
通して水素導管8から図示せぬ水素ボンベへ貯蔵
される。
With the above configuration, the heat exchange action is performed as follows. That is, during heat storage, the heat of the heat medium flowing inside the heat transfer tube 6 in the direction of the arrow is efficiently transferred to the heat transfer tube 6 by the uneven stripes of the heat transfer tube 6, and further, the metal hydride 2 is transferred from the surface of the heat transfer tube 6 and the surface of the heat transfer fin 3. is efficiently conducted. As a result, the metal hydride 2 undergoes a dehydrogenation reaction, and the released hydrogen gas is stored in a hydrogen cylinder (not shown) from the hydrogen conduit 8 through the heat insulating material 9.

一方、放熱時には、水素導管8から断熱材9を
通して加圧されて供給される水素ガスにより金属
水素化物2は水素を吸収して発熱するが、このと
き何らかの原因で爆発的に反応し急激に発熱する
場合がある。
On the other hand, during heat dissipation, the metal hydride 2 absorbs hydrogen and generates heat due to hydrogen gas supplied under pressure from the hydrogen conduit 8 through the insulation material 9, but at this time, for some reason, it reacts explosively and rapidly generates heat. There are cases where

従来構造においては、円筒境界面の内側に金属
水素化物、外側に熱媒を配していたため、境界面
の内側が急激に熱膨張するのに対し、外側の熱膨
張が熱媒により抑制されることから熱膨張力の逃
げ場が無くなり、大きな熱応力が発生して境界面
に亀裂が生じるおそれがあつた。
In the conventional structure, the metal hydride was placed inside the cylindrical boundary surface and the heating medium was placed outside, so while the inside of the boundary surface experienced rapid thermal expansion, the thermal expansion on the outside was suppressed by the heating medium. Therefore, there was no place for the thermal expansion force to escape, and there was a risk that large thermal stress would occur and cracks would occur at the interface.

しかし、本実施例の場合は、上述したように、
境界面である伝熱管6の内側に熱媒、外側に金属
水素化物2を配しているので、熱膨張時に発生す
る熱応力は外側に向けて発散される。しかもその
伝熱管6の内側は断面凹凸状に形成すると共に、
その肉厚部には中空部10を設けている。これに
より、内側に向う熱応力はその凹凸部と、中空部
10により吸収される。この結果、金属水素化物
2に急激な水素化反応が生じても伝熱管6はこれ
に充分耐えることができ、極めて安全性の高い金
属水素化物容器が得られることとなる。このと
き、伝熱管6の内側に形成した凹凸部は、熱媒と
の熱交換効率を向上する上でも役立つている。
However, in the case of this embodiment, as mentioned above,
Since the heat medium is placed inside the heat transfer tube 6, which is the boundary surface, and the metal hydride 2 is placed outside, the thermal stress generated during thermal expansion is dissipated outward. Moreover, the inside of the heat exchanger tube 6 is formed with an uneven cross section, and
A hollow portion 10 is provided in the thick portion. As a result, inward thermal stress is absorbed by the uneven portion and the hollow portion 10. As a result, even if a rapid hydrogenation reaction occurs in the metal hydride 2, the heat exchanger tube 6 can sufficiently withstand it, and an extremely safe metal hydride container can be obtained. At this time, the uneven portions formed on the inside of the heat transfer tube 6 are also useful for improving the efficiency of heat exchange with the heat medium.

尚、上記実施例では、伝熱管6内面の肉厚凸条
部に形成する中空部10を、軸方向に連続する例
で説明したが、第3図の側断面図に示す如く、偏
平球状に形成しても良い。あるいはまた、球状に
形成する等、その形状は適宜設計し得ることは言
う迄もない。
In the above embodiment, the hollow part 10 formed in the thick convex strip on the inner surface of the heat exchanger tube 6 was explained as being continuous in the axial direction, but as shown in the side sectional view of FIG. It may be formed. Alternatively, it goes without saying that the shape can be designed as appropriate, such as forming it into a spherical shape.

また、上記実施例では、金属水素化物2外周を
直接フイルタ性断熱材9で被覆するようにした
が、断熱材9は通常のものを使用し、水素導管8
の内部に水素ガスは通すが金属水素化物は通し得
ないフイルタ材を介在させ、この水素導管8を前
記断熱材を貫通させて金属水素化物層に延長せし
めるようにしてもよい。
Further, in the above embodiment, the outer periphery of the metal hydride 2 was directly covered with the filter-like heat insulating material 9, but a normal heat insulating material 9 was used, and the hydrogen conduit 8
A filter material that allows hydrogen gas to pass through but not metal hydride may be interposed therein, and this hydrogen conduit 8 may be extended to the metal hydride layer by passing through the heat insulating material.

(ト) 発明の効果 以上のように本発明によれば、伝熱管を中心部
に配置し、その周囲に金属水素化物を配置し、更
にその外周に断熱材を介在させて耐圧容器内に収
納し、その耐圧容器を気密に貫通する伝熱管の内
面を軸方向に沿つて複数個の肉厚凸条を形成する
と共に、その伝熱管内面に形成した肉厚凸条部に
は軸方向に沿つて複数個の中空部を配設するよう
にしたので、金属水素化物の水素化反応時に急激
な発熱が生じても、やつかいな熱応力は分散吸収
されて、伝熱管の破壊は未然に防止され、極めて
安全性の高い金属水素化物容器が得られ、ヒート
ポンプ装置等の金属水素化物利用熱機器の開発に
利用することができるようになる。
(G) Effects of the Invention As described above, according to the present invention, a heat transfer tube is arranged in the center, a metal hydride is arranged around it, and a heat insulating material is interposed around the outer periphery of the heat exchanger tube, and the tube is housed in a pressure-resistant container. A plurality of thick protrusions are formed along the axial direction on the inner surface of the heat transfer tube that airtightly penetrates the pressure-resistant container, and a plurality of thick protrusions formed on the inner surface of the heat transfer tube are provided with a plurality of thick protrusions along the axial direction. Since multiple hollow sections are provided in the tube, even if rapid heat generation occurs during the hydrogenation reaction of metal hydride, the severe thermal stress is dispersed and absorbed, preventing damage to the heat transfer tube. , an extremely safe metal hydride container can be obtained, which can be used for the development of thermal equipment using metal hydrides such as heat pump devices.

【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
容器の側断面図、第2図はそのA−A断面図、第
3図は本発明の他の実施例に係る金属水素化物容
器の側断面図である。 1……耐圧容器、2……金属水素化物、3……
伝熱フイン、4……ボルト、5……ナツト、6…
…伝熱管、7……バルブ、8……水素導管、9…
…断熱材、10……中空部、11……容器本体
部、12……蓋部、11a,12a……フランジ
部、11b……本体側端面。
FIG. 1 is a side sectional view of a metal hydride container according to one embodiment of the present invention, FIG. 2 is a sectional view taken along line A-A, and FIG. FIG. 1...Pressure container, 2...Metal hydride, 3...
Heat transfer fin, 4... Bolt, 5... Nut, 6...
...Heat transfer tube, 7...Valve, 8...Hydrogen conduit, 9...
...Insulating material, 10...Hollow part, 11...Container body part, 12...Lid part, 11a, 12a...Flange part, 11b...Body side end surface.

Claims (1)

【特許請求の範囲】[Claims] 1 外部から水素ガスの供給、排出を行なうため
の水素導管を備えた円筒状耐圧容器内に断熱材を
介在させて金属水素化物を収納し、その軸心部を
気密に貫通して内部に熱媒を流す伝熱管を設け、
この伝熱管の内面に軸方向に沿つて複数個の肉厚
凸条を形成すると共に、その伝熱管内面に形成し
た肉厚凸条部に軸方向に沿つて中空部を設けて成
ることを特徴とする金属水素化物容器。
1 A metal hydride is stored in a cylindrical pressure-resistant container equipped with a hydrogen conduit for supplying and discharging hydrogen gas from the outside with a heat insulating material interposed, and the axial center of the container is hermetically penetrated to supply heat inside. A heat transfer tube is installed to flow the medium,
A plurality of thick protrusions are formed along the axial direction on the inner surface of the heat exchanger tube, and a hollow portion is provided along the axial direction in the thick protrusion formed on the inner surface of the heat exchanger tube. metal hydride container.
JP60033698A 1985-02-23 1985-02-23 Metal hydride container Granted JPS61197898A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60033698A JPS61197898A (en) 1985-02-23 1985-02-23 Metal hydride container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60033698A JPS61197898A (en) 1985-02-23 1985-02-23 Metal hydride container

Publications (2)

Publication Number Publication Date
JPS61197898A JPS61197898A (en) 1986-09-02
JPH0433721B2 true JPH0433721B2 (en) 1992-06-03

Family

ID=12393634

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60033698A Granted JPS61197898A (en) 1985-02-23 1985-02-23 Metal hydride container

Country Status (1)

Country Link
JP (1) JPS61197898A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108240552B (en) * 2016-12-27 2020-01-10 有研工程技术研究院有限公司 Quick-response hydrogen storage tank and manufacturing method thereof
KR102696346B1 (en) * 2021-03-30 2024-08-19 피엔피에너지텍 주식회사 Additive Modular Hydrogen Storage Device Using Hydrogen Storage Alloy

Also Published As

Publication number Publication date
JPS61197898A (en) 1986-09-02

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