JPS6159192A - Heat accumulator - Google Patents

Heat accumulator

Info

Publication number
JPS6159192A
JPS6159192A JP59178493A JP17849384A JPS6159192A JP S6159192 A JPS6159192 A JP S6159192A JP 59178493 A JP59178493 A JP 59178493A JP 17849384 A JP17849384 A JP 17849384A JP S6159192 A JPS6159192 A JP S6159192A
Authority
JP
Japan
Prior art keywords
heat
container
hydrogen
pressure
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.)
Pending
Application number
JP59178493A
Other languages
Japanese (ja)
Inventor
Kenji Nasako
名迫 賢二
Ikuro Yonezu
育郎 米津
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
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 JP59178493A priority Critical patent/JPS6159192A/en
Publication of JPS6159192A publication Critical patent/JPS6159192A/en
Pending legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/003—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
    • 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
    • Y02E60/14—Thermal energy storage
    • 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
    • Y02E70/00—Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PURPOSE:To minimize the heat losses and to increase the heat accumulating speed, by housing a metal hydride, heat pipes and a filter in a pressure hydrogen container having a heat insulating material. CONSTITUTION:When heat is to be accumulated, a high-temperature heating medium is admitted from a heating medium inlet conduit 9 into a heat exchange jacket 7. The heat of this heating medium is taken via a heat pipe 5 into a container 1, and is transmitted via heat transmitting fins 6 to a metal hydride 3. As a result, the metal hydride 3 releases hydrogen, and the hydrogen is taken outside via a metal sintered filter 4 in the container, a manifold 11 and a hydrogen inflow/outflow conduit 12 and is stored. On the other hand, when radiation is to be carried out, reversely the hydrogen stored outside is released into the container via the hydrogen inflow/outflow conduit 12, the manifold 11 and the metal sintered filter 4. The heat released when the hydrogen combines with the metal hydride 3 is transmitted from the fins 6 to the heat pipe 5, is recovered by the heating medium flowing through the heat exchange jacket 7 and taken outside via a heating medium outlet conduit 10.

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る蓄熱器に係り、特に熱
効率の良好な蓄熱器に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a heat storage device using a metal hydride, and particularly to a heat storage device with good thermal efficiency.

従来技術 種々の金属や合金は、金属水素化物として液体水素と同
等以上の密度で水素を吸収することが知られており、ク
リーンエネルギーとしての水素を貯蔵するための水素貯
蔵材として期待されている。
Prior Art Various metals and alloys are known to absorb hydrogen in the form of metal hydrides at a density equal to or higher than that of liquid hydrogen, and are expected to be used as hydrogen storage materials for storing hydrogen as clean energy. .

また、このような金属水素化物は、単に水素を貯蔵する
という特徴を有するばかりではなく、水素という化学エ
ネルギーを熱あるいは機械エネルギーに変換するエネル
ギー変換機能も有している。
Moreover, such metal hydrides not only have the characteristic of simply storing hydrogen, but also have an energy conversion function of converting the chemical energy of hydrogen into heat or mechanical energy.

ここで、化学エネルギーと熱エネルギーの相互変換機能
を利用する熱貯蔵に関しては、これまでの顕熱や潜熱の
蓄熱材に対し、単位体積当りの蓄熱量が格段に大きいこ
とから新しい蓄熱材として期待されている。
Regarding heat storage that utilizes the mutual conversion function of chemical energy and thermal energy, it is expected to be a new heat storage material because it can store much more heat per unit volume than conventional heat storage materials that store sensible heat or latent heat. has been done.

このような、金属水素化物をエネルギー変換材料として
利用する技術は現在開発途上にあり、多くの試みがなさ
れている(例えば、ヒートポンプ。
Technology to use metal hydrides as energy conversion materials is currently under development, and many attempts have been made (for example, heat pumps).

ケミカルコンプレッサ、熱貯蔵、熱輸送等)。この中で
蓄熱技術(熱貯蔵)に関しては、金属水素化物の反応熱
を有効に利用することを目的とした容器構造が種々提案
されている(特公昭59−1950号、特開昭56−1
45602号等参照)。しかしながら、これらの容器に
おいては、金属水素化物を構成する耐圧容器の熱損失、
および、金属水素化物に対する迅速な熱伝導および迅速
な水素供給などが太きな課題となっている。
chemical compressors, heat storage, heat transport, etc.). Regarding heat storage technology (heat storage), various container structures have been proposed for the purpose of effectively utilizing the reaction heat of metal hydrides (Japanese Patent Publication No. 59-1950, JP-A No. 56-1
45602 etc.). However, in these containers, heat loss of the pressure container constituting the metal hydride,
In addition, rapid heat conduction and rapid hydrogen supply to metal hydrides are major issues.

すなわち、金属水素化物は水素加圧状態で反応を生起す
るので、金属水素化物を充填する容器を耐圧構造にする
必要があり、容器重量が大きくなる6したがって、蓄熱
もしくは放熱する場合に容器全体を加熱するための熱量
が無視できなくなり。
In other words, since metal hydrides undergo reactions under hydrogen pressure, the container filled with metal hydrides needs to have a pressure-resistant structure, which increases the weight of the container.6 Therefore, when storing or dissipating heat, the entire container must be The amount of heat required for heating can no longer be ignored.

コ その結果、耐圧容器に流入する熱量は蓄熱効率に大きく
影響する。したがって、蓄熱効率の向上を目指すには耐
圧容器による熱損失を極力減少する必要がある。
As a result, the amount of heat flowing into the pressure container has a large effect on heat storage efficiency. Therefore, in order to improve heat storage efficiency, it is necessary to reduce heat loss due to the pressure-resistant container as much as possible.

また、金属水素化物と水素の反応(よ迅速に行なわれる
ので大きな蓄熱速度および放熱速度を期待することがで
きるが、そのためには粉体状の金属水素化物層内での伝
熱速度を極力大きくするとともに、水素の供給および取
り出しを円滑にする必要がある。
In addition, the reaction between metal hydride and hydrogen (which occurs more quickly, so a large heat storage and heat release rate can be expected, but in order to achieve this, it is necessary to increase the heat transfer rate within the powdered metal hydride layer as much as possible). At the same time, it is necessary to smoothly supply and extract hydrogen.

目的 本発明は、上記の点に鑑みなされたもので、熱損失が少
なくかつ蓄熱速度が大きい蓄熱器を提供することを目的
とする。
Purpose The present invention was made in view of the above points, and an object of the present invention is to provide a heat storage device with low heat loss and high heat storage rate.

構成 このため本発明は、内壁に断熱材を付設した円筒状の耐
圧水素容器内部に金属水素化物と共に複数本のヒートパ
イプと□複数本の金属焼結フィルタ円筒体を収納するが
、前記ヒートパイプは前記耐圧水素容器の一端を気密に
貫通して容器内部から外部にわたって配置し、その容器
内部に存在するヒートパイプ部分には所定間隔で扇状伝
熱フィンを固着し、全体として層状円形フィンを形成す
ると共に、容器外部に存在するヒートパイプ部分にはそ
れぞれ熱交換ジャケットを取り付は導管で直列に連続し
て熱媒を連続して流す構造とする一方、前記金属焼結フ
ィルタは各ヒートパイプ毎に固着される扇状伝熱フィン
間に配置すると共に、多岐管に連結して前記耐圧水素容
器の他端から外部の水素出入導管に接続して蓄熱器を構
成するようにしたことを特徴としている。
Structure Therefore, in the present invention, a plurality of heat pipes and a plurality of metal sintered filter cylindrical bodies are housed together with a metal hydride in a cylindrical pressure-resistant hydrogen container with a heat insulating material attached to the inner wall. is arranged to airtightly penetrate one end of the pressure-resistant hydrogen container and extend from the inside of the container to the outside, and fan-shaped heat transfer fins are fixed at predetermined intervals to the heat pipe portion existing inside the container, forming a layered circular fin as a whole. At the same time, a heat exchange jacket is attached to each of the heat pipes existing outside the container, and the structure is such that the heat medium is continuously passed through the conduit in series, while the metal sintered filter is attached to each heat pipe. It is characterized in that it is arranged between the fan-shaped heat transfer fins fixed to the fins, and is connected to a manifold and connected to an external hydrogen inlet/output pipe from the other end of the pressure-resistant hydrogen container to constitute a heat storage device. .

実施例 以下1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て金属となるが、
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6 第1図は本発明の一実施例に係る蓄熱器の断面図を示し
、また、第2図は第1図のA−A断面図を示したもので
ある。
EXAMPLE An example of the present invention will be described below with reference to the drawings. still,
Metal hydrides are dehydrogenated by heat and become metals,
In this specification, this case is also collectively referred to as metal hydride.6 FIG. 1 shows a cross-sectional view of a heat storage device according to an embodiment of the present invention, and FIG. -A cross-sectional view is shown.

これらの図において、例えばステンレス鋼を用いて構成
される円筒形の耐圧水素容器1の内壁は全面断熱材2で
覆われ、その内部には金属水素化物3と共に、金属焼結
フィルタ4と、容器1の端面を気密に貫通してヒートパ
イプ5が封入されている。
In these figures, the inner wall of a cylindrical pressure-resistant hydrogen container 1 made of stainless steel, for example, is entirely covered with a heat insulating material 2, and inside it there is a metal hydride 3, a metal sintered filter 4, and a container. A heat pipe 5 is hermetically sealed through the end surface of 1.

そのヒートパイプ5は1本実施例の場合、全部で4本あ
り、各ヒートパイプ5の容器1内部に封入される部分に
は、第1図では途中図示省略しているが、第3図に示す
ように所定間隔で複数枚の扇形の伝熱フィン6が固着さ
れている。この伝熱フィン6は軽量化のため、例えばア
ルミ板で構成され。
In the case of one heat pipe 5 in this embodiment, there are four in total, and the part of each heat pipe 5 sealed inside the container 1 is not shown in the middle in FIG. 1, but it is shown in FIG. As shown, a plurality of fan-shaped heat transfer fins 6 are fixed at predetermined intervals. The heat transfer fins 6 are made of, for example, an aluminum plate to reduce weight.

4本束で層状円形フィンが形成されている。また。A layered circular fin is formed by a bundle of four fins. Also.

そのヒートパイプ5の容器1より突出する部分には熱交
換ジャケット7が取り付けられている。これら4個の熱
交換ジャケット7は熱媒を直列に流すことができるよう
に−それぞれの前端部と後端部が導管8で連結されてい
る。更に、その直列に連結さ2Nた熱交換ジャケット7
の最前端部と最後端部には熱媒入口導管9と熱媒出口導
管10が取り付けられている。
A heat exchange jacket 7 is attached to a portion of the heat pipe 5 that protrudes from the container 1. The front and rear ends of these four heat exchange jackets 7 are connected by conduits 8 so that the heat medium can flow in series. Furthermore, the 2N heat exchange jacket 7 connected in series
A heat medium inlet conduit 9 and a heat medium outlet conduit 10 are attached to the frontmost end and the rearmost end.

一方、金属焼結フィルタ4は、例えばステンレス鋼を用
いて形成される細径の円筒フィルタで、水素は通し得る
が金属水素化物3は通さない溝造になっている。この金
属焼結フィルタ4は、多岐管11より分岐して第2図に
示す通り、相隣るヒートパイプ5に固着されている伝熱
フィン6間の間隙に1本実施例の場合、全部で5本配置
されている。
On the other hand, the metal sintered filter 4 is a small-diameter cylindrical filter made of stainless steel, for example, and has a grooved structure that allows hydrogen to pass through but not the metal hydride 3. This metal sintered filter 4 is branched from the manifold 11, and as shown in FIG. Five are arranged.

また、多岐管11には、容器1の端面IBから外部に突
出する水素をぷ入放出するための水素出入導管12が接
続されており、この部分の拡大図を第4図に示す。
Further, a hydrogen inlet/outlet conduit 12 for discharging hydrogen protruding outward from the end face IB of the container 1 is connected to the manifold 11, and an enlarged view of this portion is shown in FIG. 4.

かかる構成で、蓄熱時には高温の熱媒が熱媒入口導管9
から熱交換ジャケット7に加えられる。この熱媒の熱は
ヒートパイプ5を介して容器1内に取り込まれ、更に伝
熱フィン6を介して金属水素化物3に伝達される。これ
により、金属水素化物3は水素を放出するが、その水素
は容器1内部に配置される金属焼結フィルタ4から多岐
管11、更に水素出入導管12を経て外部へ取り出され
て貯蔵される。一方、放熱時にはこの逆に外部に貯蔵さ
れていた水素が水素出入導管12から多岐管11、金属
焼結フィルタ4を介して容器1内に放出される。この水
素が金属水素化物3と結合するとき発生する熱は伝熱フ
ィン6からヒートパイプ5に伝達され、熱交換ジャケッ
ト7を流れる熱媒に回収されて熱媒出口導管10より外
部に取り出される。
With such a configuration, during heat storage, a high temperature heat medium flows through the heat medium inlet conduit 9.
from the heat exchange jacket 7. The heat of this heating medium is taken into the container 1 via the heat pipe 5 and further transferred to the metal hydride 3 via the heat transfer fins 6. As a result, the metal hydride 3 releases hydrogen, which is taken out from the metal sintered filter 4 disposed inside the container 1 through the manifold 11 and further through the hydrogen inlet/output conduit 12 and stored. On the other hand, during heat dissipation, on the contrary, hydrogen stored outside is released into the container 1 from the hydrogen inlet/output pipe 12 via the manifold 11 and the metal sintered filter 4. The heat generated when this hydrogen combines with the metal hydride 3 is transferred from the heat transfer fins 6 to the heat pipe 5, recovered by the heat medium flowing through the heat exchange jacket 7, and taken out to the outside through the heat medium outlet conduit 10.

このとき、金属水素化物3は伝熱フィン6間に配置され
るため、伝熱フィン6の伝熱面から極めて短かい距離に
位置させることができ、迅速な熱伝導が可能となる。ま
た、金属水素化物3へ供給する熱あるいは金属水素化物
3で発生した熱は、断熱材2により遮ぎられて耐圧水素
容器1には達しないため、高い蓄熱効率を得ることがで
きる。
At this time, since the metal hydride 3 is placed between the heat transfer fins 6, it can be positioned at an extremely short distance from the heat transfer surface of the heat transfer fins 6, and rapid heat conduction is possible. Further, the heat supplied to the metal hydride 3 or the heat generated in the metal hydride 3 is blocked by the heat insulating material 2 and does not reach the pressure-resistant hydrogen container 1, so that high heat storage efficiency can be obtained.

また、水素の供給、取り出しは、金属焼結フィルタ4、
多岐管11および水素出入導管12を介して行なわれる
ため、金属水素化物3に対する水素の供給、取り出しが
均一になされ、したがって水素流が妨げられることはな
い。
In addition, hydrogen is supplied and taken out using a metal sintered filter 4,
Since this is carried out via the manifold 11 and the hydrogen inlet/output conduit 12, hydrogen is uniformly supplied to and withdrawn from the metal hydride 3, so that the flow of hydrogen is not obstructed.

また、ヒートパイプ5によって金属水素化物3の吸熱、
放熱を行なっているので、伝熱管内管の汚れおよび腐蝕
は全くなく、作動液の蒸気による熱移動を利用するため
長距離熱輸送に優れている。
In addition, the heat pipe 5 absorbs heat from the metal hydride 3,
Since heat is dissipated, there is no dirt or corrosion on the inner tube of the heat transfer tube, and since heat transfer by the steam of the working fluid is used, it is excellent in long-distance heat transport.

更に、ヒートパイプ5に付設した熱交換ジャケット7は
各々直列に連結されているので、伝熱面での熱媒流量を
大きくすることができ、熱媒のよどみがなく効率の良い
熱交換ができる。
Furthermore, since the heat exchange jackets 7 attached to the heat pipes 5 are connected in series, the flow rate of the heat medium on the heat transfer surface can be increased, and efficient heat exchange can be performed without stagnation of the heat medium. .

効果 以上説明したように、本発明によれば、耐圧水素容器の
内壁に断熱材を付設したので耐圧水素容器への熱量の流
入を防止でき、熱損失を改善できる。金属水素化物層内
に所定間隔で扇形伝熱フィンを配設するようにしたので
、伝熱速度を極めて大きくできる。水素出入導管を多岐
管を介して金属焼結フィルタに接続したので、金属水素
化物への水素供給、取り出しを円滑にできる。伝熱管と
してヒートパイプを用いたので長距離熱輸送が有利にな
るなどの効果が得られる。
Effects As explained above, according to the present invention, since a heat insulating material is attached to the inner wall of the pressure-resistant hydrogen container, it is possible to prevent the amount of heat from flowing into the pressure-resistant hydrogen container, thereby improving heat loss. Since the fan-shaped heat transfer fins are arranged at predetermined intervals within the metal hydride layer, the heat transfer rate can be extremely increased. Since the hydrogen inlet/output pipe is connected to the metal sintered filter via the manifold, hydrogen can be smoothly supplied to and taken out of the metal hydride. Since a heat pipe is used as the heat transfer tube, effects such as long-distance heat transport can be obtained.

【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を示した断面図、第2図第1
図のA−A断面図、第3図はヒートパイプと扇形フィン
の取付状態を示した斜視図、第4図は多岐管部を詳紹に
示した拡大図である。 1 ・・耐圧水素容器、2・・・断熱材、3・・・金属
水素化物、4・・・金属焼結フィルタ、5・・・ ヒー
トパイプ、6・・・伝熱フィン、7・・・熱交換ジャケ
ット、8・・・導管、9・・・熱媒入口導管、10・・
・熱媒出口導管、11・・・多岐管、12・・・水素出
入導管。
Fig. 1 is a sectional view showing one embodiment of the present invention, Fig. 2 is a sectional view showing an embodiment of the present invention;
3 is a perspective view showing how the heat pipe and fan-shaped fins are attached, and FIG. 4 is an enlarged view showing the manifold section in detail. 1...Pressure-resistant hydrogen container, 2...Insulating material, 3...Metal hydride, 4...Metal sintered filter, 5...Heat pipe, 6...Heat transfer fin, 7... Heat exchange jacket, 8... Conduit, 9... Heat medium inlet conduit, 10...
・Heat medium outlet conduit, 11...manifold pipe, 12...hydrogen in/out conduit.

Claims (1)

【特許請求の範囲】[Claims]  内壁が断熱材で覆われた円筒状の耐圧水素容器と、こ
の耐圧水素容器内に収納される金属水素化物と、その耐
圧水素容器の一端を気密に貫通して容器内部から外部に
わたって配設される複数本のヒートパイプと、これらヒ
ートパイプの容器内部に配置される部分に所定間隔で固
定され、全体として層状円形フィンを形成する軽量かつ
良熱伝導度の材質からなる複数枚の扇形伝熱フィンと、
前記ヒートパイプの容器外部に配置される部分にそれぞ
れ取り付けられ、熱媒流路導管で直列に接続された複数
個の熱交換ジャケットと、前記耐圧水素容器内部の各ヒ
ートパイプ毎に設けられる伝熱フィン間に配設される複
数本の金属焼結フィルタ円筒体と、これら金属焼結フィ
ルタ円筒体を連結する多岐管と、この多岐管に接続され
、前記耐圧水素容器の他端を気密に貫通し、外部に突出
して設けられる水素出入導管とを備えていることを特徴
とする蓄熱器。
A cylindrical pressure-resistant hydrogen container whose inner wall is covered with a heat insulating material, a metal hydride stored in the pressure-resistant hydrogen container, and a container that airtightly penetrates one end of the pressure-resistant hydrogen container and extends from the inside of the container to the outside. A fan-shaped heat transfer system consisting of a plurality of heat pipes and a plurality of fan-shaped heat transfer sheets made of a lightweight and highly thermally conductive material that are fixed at predetermined intervals to the parts of these heat pipes that are placed inside the container, and that form a layered circular fin as a whole. fin and
a plurality of heat exchange jackets each attached to a portion of the heat pipe disposed outside the container and connected in series through a heat medium flow conduit; and a heat transfer provided for each heat pipe inside the pressure-resistant hydrogen container. A plurality of metal sintered filter cylinders disposed between the fins, a manifold pipe connecting these metal sintered filter cylinders, and a manifold connected to the manifold and airtightly passing through the other end of the pressure-resistant hydrogen container. and a hydrogen inlet/output conduit protruding from the outside.
JP59178493A 1984-08-29 1984-08-29 Heat accumulator Pending JPS6159192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59178493A JPS6159192A (en) 1984-08-29 1984-08-29 Heat accumulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59178493A JPS6159192A (en) 1984-08-29 1984-08-29 Heat accumulator

Publications (1)

Publication Number Publication Date
JPS6159192A true JPS6159192A (en) 1986-03-26

Family

ID=16049413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59178493A Pending JPS6159192A (en) 1984-08-29 1984-08-29 Heat accumulator

Country Status (1)

Country Link
JP (1) JPS6159192A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5746269A (en) * 1996-02-08 1998-05-05 Advanced Mobile Telecommunication Technology Inc. Regenerative heat exchanger
JP2014137153A (en) * 2013-01-15 2014-07-28 Furukawa Electric Co Ltd:The Heat storage device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS591951A (en) * 1982-06-25 1984-01-07 Hidehiko Yoshida Heating apparatus
JPS5984087A (en) * 1982-11-05 1984-05-15 Agency Of Ind Science & Technol Hydrogenated metal heat accumulating device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS591951A (en) * 1982-06-25 1984-01-07 Hidehiko Yoshida Heating apparatus
JPS5984087A (en) * 1982-11-05 1984-05-15 Agency Of Ind Science & Technol Hydrogenated metal heat accumulating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5746269A (en) * 1996-02-08 1998-05-05 Advanced Mobile Telecommunication Technology Inc. Regenerative heat exchanger
JP2014137153A (en) * 2013-01-15 2014-07-28 Furukawa Electric Co Ltd:The Heat storage device

Similar Documents

Publication Publication Date Title
US5029638A (en) High heat flux compact heat exchanger having a permeable heat transfer element
CN110634580A (en) A heat pipe type deep-sea application nuclear reactor system
JPH0436081B2 (en)
JPH0527563B2 (en)
JPH0224763B2 (en)
JPS6334487A (en) Hydrogenated metal heat exchanger
RU2204773C2 (en) Tube-in-tube heat exchanger
JP2000111193A (en) Hydrogen occlusion alloy heat exchanger
JPS5848480Y2 (en) Hydrogen storage device using metal hydride
JPS62119393A (en) Heat exchanger for metal hydride
JPH0253362B2 (en)
JPS61246594A (en) Regenerator utilizing metallic hydride
CN223772393U (en) A uniform temperature storage and temperature control device
CN116591853B (en) A decay heat Stirling converter for space use
JPS61202091A (en) Utilizing device for metallic hydrogen compound
JPS60205191A (en) Vessel for metallic hydrogenated substance
JPH0412377Y2 (en)
JPH073250Y2 (en) Hydrogen storage / desorption heat exchanger
CN120650630A (en) Integrated hydrogen storage device of metal hydride reactor and working method thereof
CN120299760A (en) A reactor system for deep sea
JP2957515B2 (en) Hydrogen storage alloy container
JPS58182087A (en) Heat accumulating device by metal hydride
JPS647319B2 (en)
JPS5919906Y2 (en) Heat exchange device using hydrogen storage metal
JPH0579723A (en) Htdrogen storage alloy heat exchanger