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JPS60205191A - Vessel for metallic hydrogenated substance - Google Patents

Vessel for metallic hydrogenated substance

Info

Publication number
JPS60205191A
JPS60205191A JP59060970A JP6097084A JPS60205191A JP S60205191 A JPS60205191 A JP S60205191A JP 59060970 A JP59060970 A JP 59060970A JP 6097084 A JP6097084 A JP 6097084A JP S60205191 A JPS60205191 A JP S60205191A
Authority
JP
Japan
Prior art keywords
heat
hydrogen
layer
metal hydride
hydrogenated substance
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
Application number
JP59060970A
Other languages
Japanese (ja)
Inventor
Masayuki Kurooka
正之 黒岡
Kenji Nasako
名迫 賢二
Naojiro Honda
本田 直二郎
Takashi Sakai
貴史 酒井
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
Sanyo Denki Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Sanyo Denki 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, Sanyo Denki Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP59060970A priority Critical patent/JPS60205191A/en
Publication of JPS60205191A publication Critical patent/JPS60205191A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/003Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
    • 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
    • Y02E60/14Thermal energy storage
    • 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
    • Y02E70/00Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30Systems combining energy storage with energy generation of non-fossil origin

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To obtain the vessel for metallic hydrogenated substance, compact and provided with good heat transfer efficiency, by a method wherein a pressure vessel, a heat pipe and a heat exchanger are integrated by employig a cylindrical body having three- layered structure while heat medium is flowed through the outermost layer, the intermediate layer is filled with the metallic hydrogenated substance and the heat medium is flowed through the innermost layer. CONSTITUTION:Three layers 4, 5, 6 are formed by cylindrical tubes 1, 2, 3. Upon heat accumulating, the heat medium is flowed through the outermost layer 4 and the innermost layer 6 and whereby the heat is transferred to the metallic hydrogenated substance in the intermediate layer 5. According to the heat transfer, hydrogen releasing reaction is caused in the metallic hydrogenated substance and generated hydrogen is extracted through a hydrogen inlet and outlet conduit 11 to store as hydrogen. On the other hand, upon heat dissipation, the metallic hydrogenated substance absorbs the hydrogen supplied from the filter section 11A of the hydrogen inlet and outlet conduit 11 and heat is generated. The heat is transferred to the heat medium flowing through the outermost layer 4 and the innermost layer 6 to retrieve it by the heat medium. According to this method, the vessel, compact, less in heat loss and excellent in the heat transfer efficiency, may be obtained.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は金属水素化物を用いて蓄熱等を行なうに好適な
金属水素化物容器に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a metal hydride container suitable for storing heat or the like using a metal hydride.

従来技術 種々の金属又は合金が液体水素と同等あるいはそれ以上
の密度で多量の水素を吸収して金属水素化物を生成する
こと、および、この生成した金属水素化物が温度、水素
圧力等を制御することにより水素を放出して元の金属あ
るいは合金に戻ることは既に知られている。これらの性
質を利用して金属水素化物は、蓄熱装置や水素貯蔵装置
への適用が試みられている。この場合、金属水素化物は
水素圧力下での反応が進められることから耐圧容器を必
要とする。また、金属水素化物は熱伝導率が小さいこと
等から、金属水素化物に効率良く熱を吸収させ、また、
金属水素化物から発生する熱を効率良く取り出して利用
することが必要となるにれらの点を考慮して出願人は先
に金属水素化物を充填した耐圧容器と熱交換器とをヒー
トパイプで連結して成る金属水素化物容器を提案した(
特開昭56−23667号公報参照)。
Prior Art Various metals or alloys absorb a large amount of hydrogen at a density equal to or higher than that of liquid hydrogen to generate metal hydrides, and the generated metal hydrides control temperature, hydrogen pressure, etc. It is already known that the metal or alloy returns to its original form by releasing hydrogen. Utilizing these properties, attempts have been made to apply metal hydrides to heat storage devices and hydrogen storage devices. In this case, the metal hydride requires a pressure-resistant container because the reaction proceeds under hydrogen pressure. In addition, since metal hydrides have low thermal conductivity, metal hydrides can absorb heat efficiently, and
Taking into consideration the need to efficiently extract and utilize the heat generated from metal hydrides, the applicant first connected a pressure vessel filled with metal hydride and a heat exchanger with heat pipes. We proposed a metal hydride container consisting of interconnected metal hydride containers (
(See Japanese Patent Application Laid-Open No. 56-23667).

しかし、この金属水素化物利用技術は最近の技術であり
、現在開発途上の技術であるため、上記金属水素化物容
器においても未だ多くの改良すべき点が残されていた。
However, since this metal hydride utilization technology is a recent technology and is currently under development, there are still many points to be improved in the metal hydride container.

即ち、上記金属水素化物容器においては、金属水素化物
を充填した耐圧容器と熱交換器とをヒートパイプで連結
する方式であったため、全体の形状が複雑で容積が大き
くなる上、熱媒と金属水素化物間の熱伝達が悪く、効率
の良い熱交換が行なわれないなどと言った問題点があっ
た。
In other words, in the metal hydride container described above, the pressure-resistant container filled with metal hydride and the heat exchanger are connected by a heat pipe, so the overall shape is complicated and the volume is large, and the heat medium and metal There were problems such as poor heat transfer between hydrides and inefficient heat exchange.

目的 本発明は上記問題点を解消し、金属水素化物と熱媒間の
熱伝達効率の良いあるいは水素を均一に供給できる金属
水素化物容器を提供することを目的とする。
OBJECTS OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and provide a metal hydride container that has good heat transfer efficiency between the metal hydride and the heat medium or can supply hydrogen uniformly.

構成 このため本発明は、従来、耐圧容器、ヒートバイブ、熱
交換器の3つの部分に別れていた容器構造を3層構造の
円筒体を用いることにより一体化し、その最外層には熱
媒を流し、中間層には金属水素化物を充填すると共に、
最内層には熱媒を流すようにしたことを特徴としている
Structure For this reason, the present invention integrates the container structure, which was conventionally separated into three parts: a pressure-resistant container, a heat vibrator, and a heat exchanger, by using a cylindrical body with a three-layer structure, and the outermost layer contains a heat medium. The intermediate layer is filled with metal hydride, and
The feature is that a heating medium is allowed to flow through the innermost layer.

実施例 以、下、本発明の実施例を図面を参照して説明する。尚
、金属水素化物は熱によって脱水素化し金属となるが、
この明細書中ではこの場合も含めて金属水素化物と総称
している。
Embodiments Hereinafter, embodiments of the present invention will be described with reference to the drawings. In addition, metal hydrides are dehydrogenated by heat and become metals,
In this specification, this case is also collectively referred to as metal hydride.

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
成図を示したもので、(a)はその横断面図、(b)は
そのA−A断面図である。図において。
FIG. 1 shows a configuration diagram of a metal hydride container according to an embodiment of the present invention, in which (a) is a cross-sectional view thereof, and (b) is a cross-sectional view taken along the line A-A. In fig.

1.2.3は、同軸上に配置される3つの円筒管である
1.2.3 are three cylindrical tubes arranged coaxially.

この3つの円筒管1,2,3により3つの層4,5.6
が形成される。その最外層4と最内層6には熱媒出入導
管7A、7Bと8A、8Bが取り付けられて熱媒が流さ
れる。
These three cylindrical tubes 1, 2, 3 create three layers 4, 5, 6
is formed. Heat medium inlet/output conduits 7A, 7B and 8A, 8B are attached to the outermost layer 4 and innermost layer 6 to allow the heat medium to flow therethrough.

また、中間層5は閉鎖板9,10により閉鎖されて金属
水素化物が充填されると共に、その金属水素化物への水
素の供給1回収を行なうために、閉鎖板9には先端部に
水素は通すが金属水素化物は通さない金属焼結フィルタ
ー部11Aを有する水素出入導管11が取り付けられる
。尚、このフィルター部11Aは中間層5内を軸方向に
沿って長く延長して設けてもよい。
Further, the intermediate layer 5 is closed by closing plates 9 and 10 and filled with metal hydride, and in order to supply and recover hydrogen to the metal hydride, the closing plate 9 has hydrogen at its tip. A hydrogen inlet/outlet conduit 11 is attached which has a metal sintered filter section 11A that passes metal hydrides but not metal hydrides. Incidentally, the filter portion 11A may be provided to extend within the intermediate layer 5 along the axial direction.

上記構成で、蓄熱時には金属水素化物層の温度分布を考
慮して熱媒を最外層4.最内層6に最適流量比で流すこ
とにより、中間層5の金属水素化物には平均して熱が伝
達される。これにより金属水素化物が水素解離反応を起
こし、発生する水素は水素出入導管11より取り出され
、化学エネルギー(水素)として貯蔵される。一方、放
熱時には、水素出入導管11のフィルター部11Aから
供給される水素を金属水素化物が吸収して熱を発生する
。この熱は最外層4.および、最内層6へ伝達されてそ
こを流れる熱媒により回収される。
With the above configuration, during heat storage, the heat medium is transferred to the outermost layer 4.0, taking into consideration the temperature distribution of the metal hydride layer. By flowing the innermost layer 6 at an optimum flow rate, heat is transferred to the metal hydride in the intermediate layer 5 on average. This causes a hydrogen dissociation reaction in the metal hydride, and the generated hydrogen is taken out from the hydrogen in/out conduit 11 and stored as chemical energy (hydrogen). On the other hand, during heat dissipation, the metal hydride absorbs hydrogen supplied from the filter section 11A of the hydrogen in/out conduit 11 and generates heat. This heat is transferred to the outermost layer 4. The heat is then transmitted to the innermost layer 6 and recovered by the heat medium flowing therethrough.

このように、金属水素化物容器を3層内部体構造とし、
その最外層4と最内層6には熱媒を流すようにする一方
、中間層5には金属水素化物を充填して水素反応を起こ
させるように構成することにより、極めてコンパクトに
して、外界への熱損失が少なく極めて熱伝達効率の良い
金属水素化物容器が得られる。
In this way, the metal hydride container has a three-layer internal structure,
A heating medium is allowed to flow through the outermost layer 4 and the innermost layer 6, while the intermediate layer 5 is filled with metal hydride to cause a hydrogen reaction, making it extremely compact and allowing it to be released to the outside world. A metal hydride container with extremely high heat transfer efficiency and low heat loss can be obtained.

第2図は本発明の他の実施例を示したもので、第1図(
b)に対応する縦断面図である。図中、第1図と同一符
号は同−又は相当部分を示す。図の構成で第1図と異な
る点は、軸方向に沿って円筒管2と円筒管3間にフィン
12を設けた点である。このように、金属水素化物容器
の円筒管3にフィン12を軸方向に複数枚取り付け、中
間層5を複数ブロックに分割することにより、熱伝達効
率は更に良くなる。その上、フィン12により金属水素
化物の均一な充填およびスエリングによる圧力集中を分
散させることが可能となる。
Figure 2 shows another embodiment of the present invention, and Figure 1 (
It is a longitudinal cross-sectional view corresponding to b). In the figure, the same reference numerals as in FIG. 1 indicate the same or corresponding parts. The configuration shown in the figure differs from FIG. 1 in that fins 12 are provided between the cylindrical tubes 2 and 3 along the axial direction. In this way, heat transfer efficiency is further improved by attaching a plurality of fins 12 in the axial direction to the cylindrical tube 3 of the metal hydride container and dividing the intermediate layer 5 into a plurality of blocks. Moreover, the fins 12 enable uniform filling of the metal hydride and dispersion of pressure concentrations due to swelling.

金属水素化物容器をこのように構成することにより、第
1図の実施例同様極めてコンパクトにして金属水素化物
容器内の水素化・脱水素化が均一。
By configuring the metal hydride container in this way, it can be made extremely compact as in the embodiment shown in FIG. 1, and hydrogenation and dehydrogenation within the metal hydride container can be uniform.

且つ迅速に行なわれ、充填された金属水素化物を有効に
利用できる。
Moreover, it is carried out rapidly and the filled metal hydride can be effectively utilized.

第3図および第4図は本発明の更に別の実施例を示した
もので、第3図は第1図(b)に対応する縦断面図、第
4図は第3図の内部部分斜視図を示したものである。図
中、第1図および第2図と同一符号は同−又は相当部分
を示す。
3 and 4 show still another embodiment of the present invention, FIG. 3 is a longitudinal sectional view corresponding to FIG. 1(b), and FIG. 4 is a perspective view of an internal part of FIG. 3. The figure is shown below. In the figure, the same reference numerals as in FIGS. 1 and 2 indicate the same or corresponding parts.

第3図に示すように、金属水素化物容器の円筒管2の内
側に、フィルター円筒管3に接触しない範囲で軸方向に
沿ったフィン13を設け、中間層5を複数ブロックに分
割する。このとき、そのフィン13を中間層5でしっか
り固定するため、第4図に示すように、通路孔14を有
する円筒管15に予めフィン13を形成したものを円筒
管2内に圧入嵌合し、その円筒管15の両端を閉鎖板9
.10(第1図参照)に固定して金属水素化物容器を構
成する。
As shown in FIG. 3, fins 13 are provided inside the cylindrical tube 2 of the metal hydride container along the axial direction within a range that does not contact the filter cylindrical tube 3, and the intermediate layer 5 is divided into a plurality of blocks. At this time, in order to securely fix the fins 13 with the intermediate layer 5, as shown in FIG. , both ends of the cylindrical tube 15 are closed by plates 9
.. 10 (see FIG. 1) to form a metal hydride container.

金属水素化物容器をこのように構成すれば、更に、熱媒
と金属水素化物との熱伝達効率が改善される上、水素化
反応時における金属水素化物の体積変化によるスエリン
グの影響を分散させることができ、その結果、スエリン
グで生じる応力変化による容器の破損を防止することが
できるようになる。
By configuring the metal hydride container in this way, the heat transfer efficiency between the heating medium and the metal hydride is further improved, and the effects of swelling due to volume changes of the metal hydride during the hydrogenation reaction can be dispersed. As a result, damage to the container due to stress changes caused by swelling can be prevented.

効果 以上のように本発明によれば、容器を3層構造とし、最
外層は熱媒路とし、中間層は金属水素化物を充填し、最
内層は熱媒路としたので、極めてコンパクトになり、外
部への熱損失を少なくして熱伝達効率の良い金属水素化
物容器が得られるようになる。
Effects As described above, according to the present invention, the container has a three-layer structure, the outermost layer is a heating medium path, the middle layer is filled with metal hydride, and the innermost layer is a heating medium path, so it is extremely compact. , a metal hydride container with high heat transfer efficiency can be obtained by reducing heat loss to the outside.

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

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、(a)はその横断面図、(b)はそのA−A断
面図、第2図は本発明の他の実施例における第1図(b
)に対応する縦断面図、第3図は本発明の更に別の実施
例における第1図(b)に対応する縦断面図、第4図は
第3図のフィン部分の部分斜視図である。 1.2.3・・・円筒管、4・・ 最外層、5・・・中
間層、6・・・最内層、 7A、7B、8A、8B・・
・熱媒出入導層、9、lO・・・閉鎖板、11・・・水
素出入導管、1]、A・・フィルター部、12.13・
・・ フィン、14・・・通路孔。 15・・・円筒管。 第1図 (a) (b) 第2図 第3図 第4図 1?
FIG. 1 is a block diagram of a metal hydride container according to an embodiment of the present invention, (a) is a cross-sectional view thereof, (b) is a cross-sectional view taken along line A-A, and FIG. 2 is a diagram showing another embodiment of the present invention. FIG. 1 (b) in Example
), FIG. 3 is a vertical cross-sectional view corresponding to FIG. 1(b) in yet another embodiment of the present invention, and FIG. 4 is a partial perspective view of the fin portion of FIG. 3. . 1.2.3...Cylindrical tube, 4...Outermost layer, 5...Middle layer, 6...Innermost layer, 7A, 7B, 8A, 8B...
・Heat medium inlet/outlet guide layer, 9, lO... Closing plate, 11... Hydrogen inlet/outlet conduit, 1], A... Filter part, 12.13.
... Fin, 14... Passage hole. 15...Cylindrical tube. Figure 1 (a) (b) Figure 2 Figure 3 Figure 4 Figure 1?

Claims (1)

【特許請求の範囲】[Claims] (1) 同軸上に3つの円筒管を配置して3層目筒体を
形成し、その3層目筒体の最外層と最内層には熱媒出入
導管を設ける一方、前記3層目筒体の中間層には水素出
入導管を設けると共に、該中間層の内部に金属水素化物
を充填して成ることを特徴とする金属水素化物容器。 (2、特許請求の範囲第1項記載において、前記中間層
は円筒軸方向に設けた複数枚のフィンによって複数ブロ
ックに分割し、各ブロック毎に水素出入導管を設けて成
ることを特徴とする金属水素化物容器。
(1) Three cylindrical tubes are arranged coaxially to form a third layer cylinder, and a heat medium inlet/output conduit is provided in the outermost layer and innermost layer of the third layer tube, while the third layer tube A metal hydride container characterized in that a hydrogen inlet/output conduit is provided in an intermediate layer of the body, and a metal hydride is filled inside the intermediate layer. (2. Claim 1, characterized in that the intermediate layer is divided into a plurality of blocks by a plurality of fins provided in the direction of the cylinder axis, and a hydrogen inlet/output conduit is provided for each block. Metal hydride container.
JP59060970A 1984-03-30 1984-03-30 Vessel for metallic hydrogenated substance Pending JPS60205191A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59060970A JPS60205191A (en) 1984-03-30 1984-03-30 Vessel for metallic hydrogenated substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59060970A JPS60205191A (en) 1984-03-30 1984-03-30 Vessel for metallic hydrogenated substance

Publications (1)

Publication Number Publication Date
JPS60205191A true JPS60205191A (en) 1985-10-16

Family

ID=13157780

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59060970A Pending JPS60205191A (en) 1984-03-30 1984-03-30 Vessel for metallic hydrogenated substance

Country Status (1)

Country Link
JP (1) JPS60205191A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62119393A (en) * 1985-11-19 1987-05-30 Sanyo Electric Co Ltd Heat exchanger for metal hydride
WO2024202907A1 (en) * 2023-03-31 2024-10-03 愛知製鋼株式会社 Chemical heat storage apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5712294A (en) * 1980-06-23 1982-01-22 Kobe Steel Ltd Heat exchanger utilizing hydrogen occluding material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5712294A (en) * 1980-06-23 1982-01-22 Kobe Steel Ltd Heat exchanger utilizing hydrogen occluding material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62119393A (en) * 1985-11-19 1987-05-30 Sanyo Electric Co Ltd Heat exchanger for metal hydride
WO2024202907A1 (en) * 2023-03-31 2024-10-03 愛知製鋼株式会社 Chemical heat storage apparatus

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