JPH0663674B2 - Energy conversion method and device using hydrogen storage metal - Google Patents

Energy conversion method and device using hydrogen storage metal

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Publication number
JPH0663674B2
JPH0663674B2 JP63228330A JP22833088A JPH0663674B2 JP H0663674 B2 JPH0663674 B2 JP H0663674B2 JP 63228330 A JP63228330 A JP 63228330A JP 22833088 A JP22833088 A JP 22833088A JP H0663674 B2 JPH0663674 B2 JP H0663674B2
Authority
JP
Japan
Prior art keywords
container
hydrogen
reaction
heat
hydrogen storage
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 - Fee Related
Application number
JP63228330A
Other languages
Japanese (ja)
Other versions
JPH0278868A (en
Inventor
正雄 中嶋
Original Assignee
三井建設株式会社
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 三井建設株式会社 filed Critical 三井建設株式会社
Priority to JP63228330A priority Critical patent/JPH0663674B2/en
Publication of JPH0278868A publication Critical patent/JPH0278868A/en
Publication of JPH0663674B2 publication Critical patent/JPH0663674B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

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  • Sorption Type Refrigeration Machines (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、主として水素の貯蔵・輸送システムやエネル
ギーの回収・動力変換システムに利用される水素吸蔵金
属と水素とから金属水素化物を生成する反応及びその逆
反応を利用したエネルギーの変換方法及びエネルギーの
変換装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention produces a metal hydride mainly from a hydrogen storage metal and hydrogen used in a hydrogen storage / transportation system or an energy recovery / power conversion system. The present invention relates to an energy conversion method and an energy conversion device using a reaction and its reverse reaction.

(従来の技術) 水素吸蔵金属と水素とから金属水素化物を生成する際の
発熱を伴う水素の吸蔵反応及びその逆の吸熱を伴う水素
の放出反応を利用した従来のエネルギーの変換方法とし
て、例えば、内部に水素吸蔵金属の粒子を充填した充填
層と、該充填層内に間隔を存して配設した複数の伝熱管
とを設けた容器を用い、該伝熱管内に熱媒体たる冷水又
は温水を流し、該伝熱管を介して該金属粒子を冷却又は
加熱すると共に該充填層に水素ガスを流通させ該金属粒
子に水素の吸蔵反応又は放出反応を行わせ、あるいは該
水素ガスを加圧又は減圧して該金属粒子に吸蔵反応及び
放出反応を起こさせ、これにより生ずる反応熱を利用し
伝熱管を介して熱媒体を加熱又は冷却してエネルギーの
変換を行うもの(特開昭60−101398号公報)、
また、内部にコイル状に伝熱管を配設した容器を用い、
該容器に水素吸蔵金属の粒子を油中に懸濁させた懸濁液
を満たし、該伝熱管に流す熱媒体を介して該懸濁液を冷
却又は加熱すると共に該懸濁液に水素ガスを吹き込んで
水素の吸蔵反応及び放出反応を行わせ、あるいは、上記
のように水素ガスを加圧又は減圧し伝熱管を介して該熱
媒体を加熱又は冷却してエネルギーの変換を行うもの
(特開昭58−217401号公報)が知られている。
(Prior Art) As a conventional energy conversion method utilizing a storage reaction of hydrogen accompanied by heat generation when a metal hydride is produced from a hydrogen storage metal and hydrogen and a hydrogen release reaction accompanied by the opposite heat absorption thereof, for example, , A container provided with a packed bed filled with particles of a hydrogen storage metal inside, and a plurality of heat transfer tubes arranged at intervals in the packed bed, using cold water as a heat medium in the heat transfer tube or Hot water is flown, the metal particles are cooled or heated through the heat transfer tube, and hydrogen gas is circulated in the packed bed to cause hydrogen absorption or desorption reaction in the metal particles, or pressurization of the hydrogen gas. Alternatively, the metal particles are decompressed to cause an occlusion reaction and a desorption reaction, and the reaction heat generated thereby is used to heat or cool a heat medium through a heat transfer tube to convert energy (JP-A-60- No. 101398),
Also, using a container in which a heat transfer tube is arranged in a coil shape,
The container is filled with a suspension of particles of a hydrogen storage metal suspended in oil, and the suspension is cooled or heated through a heat medium flowing through the heat transfer tube, and hydrogen gas is added to the suspension. Injecting hydrogen to cause a hydrogen absorption reaction and a hydrogen desorption reaction, or to convert energy by pressurizing or depressurizing hydrogen gas as described above to heat or cool the heat medium via a heat transfer tube JP-A-58-217401) is known.

(発明が解決しようとする課題) 上記前者の発明にあっては、充填層の金属粒子と伝熱管
とを接触させて熱交換を行うが、伝熱管に直接接触する
のは充填されている金属粒子の一部に過ぎず、熱交換効
率が悪化する問題があった。
(Problems to be Solved by the Invention) In the former invention, heat exchange is performed by bringing the metal particles of the packed bed into contact with the heat transfer tube, but the heat transfer tube is in direct contact with the filled metal. There is a problem that the heat exchange efficiency is deteriorated because it is only a part of the particles.

一方、後者の発明にあっては、金属粒子を懸濁させた懸
濁液と伝熱管とが接触するため熱交換効率は多少良くな
るが、懸濁液に吹き込んだ水素ガスは気泡となって懸濁
液中を上昇してしまい、該金属粒子と水素との接触が不
十分となり、反応効率が悪化する問題があった。
On the other hand, in the latter invention, the heat exchange efficiency is somewhat improved because the suspension in which the metal particles are suspended and the heat transfer tube come into contact with each other, but the hydrogen gas blown into the suspension becomes bubbles. There is a problem that the temperature rises in the suspension, the contact between the metal particles and hydrogen becomes insufficient, and the reaction efficiency deteriorates.

本発明は、上記の問題点である熱交換効率とを向上する
と共に、反応効率をも向上する水素吸蔵金属を用いたエ
ネルギー変換方向及びエネルギー変換装置を提供するこ
とをその目的とする。
An object of the present invention is to provide an energy conversion direction and an energy conversion device using a hydrogen storage metal that improves the heat exchange efficiency, which is the above problem, and also improves the reaction efficiency.

(課題を解決するための手段) 本発明は上記目的を達成する変換方法を提案するもの
で、水素吸蔵金属と水素とから金属水素化物を生成する
反応及びその逆の反応を利用したエネルギー変換方法で
あって、容器内に水素吸蔵金属の小塊片を多数充填した
充填層を設け、該充填層に水素ガスを流通させて該水素
ガスを吸蔵又は放出させると共に、該充填層に上方から
熱媒体を降り注ぐようにしたことを特徴とする。
(Means for Solving the Problems) The present invention proposes a conversion method for achieving the above-mentioned object, and an energy conversion method utilizing a reaction for producing a metal hydride from a hydrogen storage metal and hydrogen and an opposite reaction. The container is provided with a packing layer filled with a large number of small pieces of hydrogen storage metal, and the hydrogen gas is occluded or released by circulating hydrogen gas through the packing layer, and the packing layer is heated from above. The feature is that the medium is poured.

更に本発明は、前記変換方法を実施するための変換装置
を提案するもので、水素吸蔵金属と水素とから金属水素
化物を生成する反応及びその逆の反応を利用したエネル
ギー変換装置であって、容器内に水素吸蔵金属の小塊片
を多数充填した充填層を設け、該容器の上部に水素配管
の接続口と下部に熱媒体の流出口とを設けると共に、該
容器の内部に該充填層の上方に位置させて熱媒体を該充
填層に降り注ぐ吐出口を設けたことを特徴とする。
Further, the present invention proposes a conversion device for carrying out the conversion method, which is an energy conversion device utilizing a reaction of producing a metal hydride from a hydrogen storage metal and hydrogen, and a reaction thereof. A filling layer filled with a large number of small pieces of hydrogen storage metal is provided in the container, a connection port of the hydrogen pipe is provided at the upper part of the container, and a heat medium outlet is provided at the lower part, and the filling layer is provided inside the container. And a discharge port for pouring the heat medium onto the packed bed.

(作用) 水素配管の接続口から充填層に水素ガスを流通させると
共に冷却した熱媒体を吐出口から充填層に降り注ぎ、該
充填層を構成する水素吸蔵金属の小塊片から反応熱を吸
収して水素の吸蔵反応を生じさせ、あるいは該接続口か
ら該充填層に高圧の水素ガスを流通させ該小塊片に水素
の吸蔵反応による発熱作用を生じさせると共に熱媒体を
充填層に降り注ぎ、該熱媒体を温熱源用に加熱する。一
方、この反応により生成された金属水素化物に対し、加
熱した熱媒体を充填層に降り注ぎ該金属水素化物の小塊
片に反応熱を供給し水素の放出反応を生じさせ、あるい
は該接続口から水素ガスを吸引し該小塊片に水素の放出
反応による吸熱作用を生じさせると共に熱媒体を充填層
に降り注ぎ、該熱媒体を冷熱源用に冷却する。
(Operation) Hydrogen gas is circulated from the connection port of the hydrogen pipe to the packed bed and the cooled heat medium is poured from the discharge port to the packed bed, and the heat of reaction is absorbed from the small pieces of the hydrogen storage metal constituting the packed bed. To cause a hydrogen occlusion reaction, or a high-pressure hydrogen gas is circulated from the connection port to the packed bed to cause an exothermic action by the hydrogen occlusion reaction in the small pieces and at the same time a heating medium is poured into the packed bed, The heating medium is heated for the heat source. On the other hand, with respect to the metal hydride produced by this reaction, a heated heat medium is poured into the packed bed to supply reaction heat to the small pieces of the metal hydride to cause a hydrogen release reaction, or from the connection port. Hydrogen gas is sucked to cause an endothermic action by the hydrogen releasing reaction in the small pieces, and the heat medium is poured into the packed bed to cool the heat medium for a cold heat source.

このように、水素吸蔵金属の小塊片を多数充填した充填
層に液状の熱媒体を降り注ぐと共に水素ガスを流通させ
ることにより、該熱媒体は該各小塊片の間隙を縫ってそ
れらの表面を洗うように流下し、同時に水素ガスも該熱
媒体に伴われ、あるいは自由にこれらの各小塊片の間隙
を縫って流通する。したがって熱媒体は水素吸蔵金属の
各小塊片に直接接触し、該各小塊片の全表面積を伝熱面
積として熱交換を行わせることができ、また水素ガス
も、該各小塊片の全表面積を反応面積として吸蔵・放出
反応を行うわせることができる。
In this way, by pouring a liquid heat medium into a packed bed filled with a large number of small pieces of hydrogen-absorbing metal and circulating hydrogen gas, the heat medium sew gaps between the small pieces and their surfaces are sewn. At the same time, hydrogen gas is accompanied by the heat medium, or freely sewn through the gaps between these small pieces and flows. Therefore, the heat medium is brought into direct contact with each small piece of the hydrogen storage metal, and heat exchange can be performed by using the entire surface area of each small piece as a heat transfer area. Also, hydrogen gas is also included in each small piece. The total surface area can be used as the reaction area to carry out the occlusion / release reaction.

(実施例) 第1図を参照して、1は容器を示し、該容器1は、その
中間内部に水素吸蔵金属の小塊片Sを上下の孔開きプレ
ート2、2内に多数充填した充填層3を設け、該容器1
の頂部に水素配管4の接続口4aと下部に液状の熱媒体の
流出口5とを設けると共に、該容器1の内部に該充填層
3の上方に位置させて該熱媒体を該充填層3に降り注ぐ
吐出口たるシャワーヘッド6を設けて構成され、該接続
口4aから該充填層3に水素ガスを流通させて水素吸蔵金
属の小塊片Sに該水素ガスの吸蔵反応又は放出反応を行
うなわせると共に、該シャワーヘッド6から該充填層3
に熱媒体を降り注ぐようにして、該熱媒体と該小塊片S
とを直接接触させて熱交換を行うようにし、更に、該容
器1の外部に該シャワーヘッド6と該流出口5とを連通
する循環回路7を設けると共に、該循環回路7に循環ポ
ンプ8と外部配管9を接続した熱交換器10とを介設し、
充填層3に降り注いだ熱媒体を容器の下部から循環回路
7に導き、循環ポンプ8から熱交換器10を通過させてシ
ャワーヘッド6に導くようにし、該熱交換器10において
外部配管9に温水、冷水又は中間水を導入し熱媒体と熱
交換を行わせるようにしている。
(Example) With reference to FIG. 1, reference numeral 1 denotes a container, and the container 1 is filled with a large number of small pieces S of a hydrogen storage metal in the upper and lower perforated plates 2 and 2 in the middle thereof. Layer 3 is provided and the container 1
A connection port 4a of the hydrogen pipe 4 and a liquid heat medium outlet 5 are provided in the lower part of the container, and the heat medium is placed inside the container 1 above the packed layer 3 to dispose the heat medium. It is configured by providing a shower head 6 which is a discharge port that pours into the filling port 3, and causes hydrogen gas to flow from the connection port 4a to the packed layer 3 to cause the hydrogen gas occlusion reaction or desorption reaction on the hydrogen storage metal small lumps S. And the filling layer 3 from the shower head 6
The heating medium and the small pieces S are poured onto the heating medium.
Are directly contacted with each other for heat exchange, and further, a circulation circuit 7 for communicating the shower head 6 and the outlet 5 is provided outside the container 1, and a circulation pump 8 is provided in the circulation circuit 7. With the heat exchanger 10 connected to the external pipe 9,
The heat medium poured into the packed bed 3 is guided from the lower part of the container to the circulation circuit 7, passed from the circulation pump 8 through the heat exchanger 10 to the shower head 6, and in the heat exchanger 10, hot water is supplied to the external pipe 9. , Cold water or intermediate water is introduced to exchange heat with the heat medium.

この場合、該熱媒体には水、有機溶剤やシリコン等の安
定な溶液を用いるものとし、また水素吸蔵金属の小塊片
Sは、10〜50mm程度の球状、あるいはラシヒリン
グ、スロテッドリング、インターロックサドル、テラレ
ット、ポールリング、レッシングリング又はマグマホン
パッキング状等に成形したものを用いるものとする。
In this case, a stable solution of water, an organic solvent, silicon or the like is used as the heat medium, and the small pieces S of the hydrogen storage metal are spherical or have a Raschig ring, a slotted ring, an interstitial ring of about 10 to 50 mm. A molded product such as a rock saddle, terraret, pole ring, lessing ring, or magmaphone packing is used.

以上の構成により、水素吸蔵金属に吸蔵反応又は放出反
応を行わせる場合には、充填層3に水素ガスを流通させ
ると共に、外部配管9に冷水を導入して熱媒体を冷却
し、該熱媒体を該充填層3に降り注いで該小塊片Sから
反応熱を吸収して水素の吸蔵を行わせ、逆に外部配管9
に温水を導入し熱媒体を加熱し、小塊片Sに反応熱を供
給して水素の放出を行わせる。
With the above configuration, in the case of causing the hydrogen storage metal to perform the storage reaction or the release reaction, the hydrogen gas is circulated in the packed bed 3 and cold water is introduced into the external pipe 9 to cool the heat medium. Is poured into the packed bed 3 to absorb the heat of reaction from the small piece S to occlude hydrogen, and conversely the external pipe 9
Hot water is introduced to heat the heating medium to supply heat of reaction to the small piece S to release hydrogen.

また、水素吸蔵合金から熱回収を行う場合には、充填層
3の水素ガスを加圧し小塊片Sに水素の吸蔵反応を行わ
せて発熱作用を生じさせると共に、該熱媒体を該充填層
3に降り注いで該熱媒体を加熱し、外部配管9に導入し
た中間水を温熱源用に加熱するようにし、逆に水素ガス
を減圧して小塊片Sに放出反応による吸熱作用生じさ
せ、熱媒体を冷却して外部配管9に導入した中間水を冷
熱源用に冷却する。
Further, when heat is recovered from the hydrogen storage alloy, the hydrogen gas in the packed bed 3 is pressurized to cause the small lumps S to carry out a hydrogen storage reaction to generate an exothermic effect, and the heating medium is supplied to the packed bed. 3, the heating medium is heated to heat the intermediate water introduced into the external pipe 9 for a heat source, and conversely, the hydrogen gas is depressurized to cause an endothermic action by the release reaction in the small lump S, The heat medium is cooled and the intermediate water introduced into the external pipe 9 is cooled for a cold heat source.

この場合、水素吸蔵金属の小塊片Sに上記にようなラシ
ヒリング状やシロテッドリング状等に成形したものを用
いれば、充填層3に水素ガスが流通し又は熱媒体が流下
するのに抵抗とならない十分な間隙を構成することがで
きると共に、小塊片Sの表面積を大きくして熱媒体との
熱交換面積や水素ガスとの反応面積を大きくすることが
できる。
In this case, if a small piece S of the hydrogen-absorbing metal molded into the Raschig ring shape or the Silotted ring shape as described above is used, the hydrogen gas circulates in the packed bed 3 or the heat medium flows down. It is possible to form a sufficient gap that does not result in the above, and to increase the surface area of the small lump S to increase the heat exchange area with the heat medium and the reaction area with the hydrogen gas.

次ぎに本発明の第2の実施例として、第2図に基づいて
上記装置を用いた温水・冷水供給装置について説明す
る。
Next, as a second embodiment of the present invention, a hot / cold water supply apparatus using the above apparatus will be described with reference to FIG.

この装置は、上記第1の実施例に用いた装置を一対設
け、第1容器1aと第2容器1bとを仕切弁11を介設した水
素配管4で連通すると共に、両外部配管9をそれぞれ温
熱源配管9aと冷熱源配管9bとで構成し、該両熱源配管9
a、9bにそれぞれ中間熱源配管12a、12bを接続し、これに
設けた複数の切替バルブ13により温熱源配管9aと中間熱
源配管12aとを、又は冷熱源配管9bと中間熱源配管12bと
を適宜切替えるようにしている。
This device is provided with a pair of the devices used in the first embodiment, and the first container 1a and the second container 1b are connected by a hydrogen pipe 4 with a sluice valve 11 interposed therebetween, and both external pipes 9 are connected to each other. The heat source pipe 9a and the cold heat source pipe 9b
Intermediate heat source pipes 12a and 12b are connected to a and 9b, respectively, and a plurality of switching valves 13 provided in the heat source pipe 9a and the intermediate heat source pipe 12a, or the cold heat source pipe 9b and the intermediate heat source pipe 12b as appropriate. I am trying to switch.

この装置を用いて例えば深夜電力を利用した冷暖房シス
テムに適用する場合は、深夜電力を用いて昇温した温水
を温熱源配管9aに導き、第1容器1a側に水素の放出反応
を生じさせると共に、この放出した水素ガスを水素配管
4を介して第2容器1b側に導き、該第2容器1bに吹き込
んで該第2容器1b側に水素の吸蔵反応を行わせ、同時に
この吸蔵反応により生ずる反応熱を第2容器1b側の中間
熱源配管12bに導いた常温の中間水と熱交換して捨てる
ようにし、この放出反応と吸蔵反応が終わって両容器1
a、1bが平衡状態になったところで、水素配管4の仕切弁
11を閉じて冷暖房の準備段階を完了する。
When this apparatus is applied to, for example, a cooling and heating system that uses midnight power, hot water heated using midnight power is guided to the heat source pipe 9a to cause a hydrogen release reaction on the first container 1a side. The released hydrogen gas is guided to the second container 1b side through the hydrogen pipe 4 and blown into the second container 1b to cause the hydrogen storage reaction on the second container 1b side. At the same time, the hydrogen storage reaction occurs. The heat of reaction is exchanged with the intermediate water at room temperature introduced into the intermediate heat source pipe 12b on the second container 1b side to be discarded, and the releasing reaction and the occlusion reaction are completed and both containers 1
When a and 1b are in an equilibrium state, the sluice valve of the hydrogen pipe 4
Close 11 to complete the air conditioning preparation stage.

昼間の冷暖房段階にはいると、先ず、仕切弁11を開いて
高圧状態にある第2容器1bから低圧状態にある第1容器
1aに水素ガスを流入させ、第1容器1a側では吸蔵反応を
生じさせて熱媒体を加熱するようにし、第2容器1b側で
は放出反応を生じさせて熱媒体を冷却するようにして、
夏期であれば第1容器1a側の反応熱を中間熱源配管12a
から温水として捨てると共に、第2容器1b側の冷熱源配
管9bから冷房用に冷水を得るようにし、冬期であれば第
2容器1b側の反応熱を中間熱源配管12bから冷水として
捨てると共に、第1容器1a側の温熱源配管9aから暖房用
に温水を得るようにする。もっとも、夏期の温水は給湯
用に利用してもよく、また蓄熱槽(図示しない)に蓄え
ておいて上記深夜電力用の温水として利用してもよい。
In the daytime cooling / heating stage, first, the sluice valve 11 is opened to open the second container 1b in the high pressure state to the first container in the low pressure state.
Hydrogen gas is flown into 1a to cause an occlusion reaction on the first container 1a side to heat the heat medium, and to cause a release reaction on the second container 1b side to cool the heat medium,
In summer, the reaction heat from the first container 1a side is transferred to the intermediate heat source pipe 12a.
From the cold heat source pipe 9b on the second container 1b side to obtain cold water for cooling, and in the winter, the reaction heat on the second container 1b side is discarded as cold water from the intermediate heat source pipe 12b. Hot water for heating is obtained from the heat source pipe 9a on the side of the 1st container 1a. However, the hot water in summer may be used for hot water supply, or may be stored in a heat storage tank (not shown) and used as hot water for the midnight power.

第3図は、本発明の第3の実施例として上記温水・冷水
供給装置の変形例を示す。
FIG. 3 shows a modification of the hot / cold water supply device as a third embodiment of the present invention.

この実施例は、前記第1の実施例に用いた装置を4台設
けて連続運転するもので、放出反応専用の第1容器1a及
び第3容器1cと、吸蔵反応専用の第2容器1b及び第4容
器1dとを備え、各容器1a、1b、1c、1dの内部には水素吸蔵
金属の小塊片Sを孔開きプレート2、2を用いることな
く積層して充填層3を構成し、第1容器1aと第4容器1d
とを、又第2容器1bと第3容器1cとを水素配管4,4で
連通すると共に、各容器1a、1b、1c、1dの流出口5側に熱
媒体と小塊片Sとを分離する分離器14を設け、分離器14
にそれぞれ第1容器1aと第2容器1b、及び第3容器1cと
第4容器1dとの間で互いの流出口5側と上部とを連通す
る搬送配管15を接続し、該各搬送配管15に介設した搬送
装置16により互いに一方の容器から他方の容器に小塊片
Sを入替え搬送するようにし、更に、第1容器1aの熱交
換器10aには熱源配管12aを、第2容器1bの熱交換器10b
には温熱源配管9bを、第3容器1cの熱交換器10cには冷
熱源配管9cを、第4容器1dの熱交換器10dには中間熱源
配管12dをそれぞれ接続するようにしている。
In this embodiment, four devices used in the first embodiment are provided for continuous operation, and the first container 1a and the third container 1c dedicated to the release reaction and the second container 1b dedicated to the occlusion reaction and A fourth container 1d is provided, and a small lump piece S of a hydrogen storage metal is stacked inside each container 1a, 1b, 1c, 1d without using the perforated plates 2 and 2 to form a filling layer 3, 1st container 1a and 4th container 1d
And the second container 1b and the third container 1c are connected by hydrogen pipes 4 and 4, and the heat medium and the small pieces S are separated on the outlet 5 side of each container 1a, 1b, 1c, 1d. The separator 14 for
To each of the first container 1a and the second container 1b, and between the third container 1c and the fourth container 1d, respectively, connecting the conveying pipes 15 communicating the outlet 5 side and the upper side, and the conveying pipes 15 The small lumps S are transferred from one container to the other container by the transfer device 16 installed in the container, and the heat exchanger 10a of the first container 1a is provided with the heat source pipe 12a and the second container 1b. Heat exchanger 10b
The heat source pipe 9b is connected to the heat exchanger 10c of the third container 1c, the heat source pipe 9c is connected to the cold heat source pipe 9c, and the heat exchanger 10d of the fourth container 1d is connected to the intermediate heat source pipe 12d.

この供給装置によれば、第1容器1aと第4容器1dとは主
として準備工程に用い、第2容器1bと第3容器1cとは冷
暖房工程に用いるようにし、すなわち、排熱を用いて昇
温した温水を第1容器1a側の熱源配管12aに導き、該第
1容器1aに水素の放出反応を生じさせ、放出した水素ガ
スを水素配管4を介して第4容器1dに導き、該第4容器
1dに水素の吸蔵反応を行わせ、同時に、この吸蔵反応に
よる反応熱を第4容器1d側の中間熱源配管12dから捨て
るようにし、この両容器1a、1dにより準備工程としての
放出反応と吸蔵反応が行われる。
According to this supply device, the first container 1a and the fourth container 1d are mainly used in the preparation process, and the second container 1b and the third container 1c are used in the cooling and heating process, that is, using the exhaust heat to raise the temperature. The heated hot water is introduced into the heat source pipe 12a on the first container 1a side to cause a hydrogen release reaction in the first container 1a, and the released hydrogen gas is introduced into the fourth container 1d through the hydrogen pipe 4 to 4 containers
1d is allowed to perform a hydrogen storage reaction, and at the same time, the heat of reaction due to this storage reaction is discarded from the intermediate heat source pipe 12d on the side of the fourth container 1d, and the release reaction and storage reaction as a preparatory step are performed by both containers 1a and 1d. Is done.

一方、冷暖房工程は、第3容器1cから第2容器1bへ水素
ガスを流入させ、第3容器1cには放出反応が、第2容器
1bには吸蔵反応がそれぞれ行われるようにし、夏期であ
れば第2容器1b側の反応熱を温熱源配管9bから温水とし
て捨てると共に、第3容器1c側の冷熱源配管9cから冷房
用に冷水を得るようにし、冬期であれば逆に第3容器1c
側の反応熱を冷熱源配管9cから冷水として捨てると共
に、第2容器1b側の温熱源配管9bから暖房用に温水を得
るようにする。
On the other hand, in the cooling and heating process, hydrogen gas is caused to flow from the third container 1c into the second container 1b, and the release reaction is generated in the third container 1c.
In the summer, the reaction heat of the second container 1b side is discarded as warm water from the warm heat source pipe 9b, and the cold heat source pipe 9c of the third container 1c side cools the cooling water for cooling. And in the winter season, on the contrary, the third container 1c
The reaction heat on the side is discarded as cold water from the cold heat source pipe 9c, and hot water for heating is obtained from the warm heat source pipe 9b on the second container 1b side.

そして、上記の反応サイクルは徐々に連続して稼動する
ので、該反応サイクルが稼動中、或いは反応サイクルが
完了する直前に各搬送装置16により第1容器1aと第2容
器1b、及び第3容器1cと第4容器1dとの間で互いに小塊
片Sの入替えを行うようにし、この一連の操作を繰り返
して連続的に温水と冷水とを得る。
Since the above reaction cycle is gradually and continuously operated, the first container 1a, the second container 1b, and the third container 1a, 1b, and 3rd container are operated by the respective conveyors 16 during the operation of the reaction cycle or immediately before the completion of the reaction cycle. The small pieces S are exchanged between the 1c and the fourth container 1d, and this series of operations is repeated to continuously obtain hot water and cold water.

このようにすれば、容器は吸蔵用及び放出用に、配管は
熱源用、冷熱源用、温熱源用及び中間熱源用にそれぞれ
専用に構成することができ、繁雑なバルブの切替えをす
ることなく、また容器及び配管はそれぞれ熱的に適した
材質で構成することができる。
In this way, the container can be configured for storage and discharge, and the pipes can be configured for heat source, cold heat source, warm heat source, and intermediate heat source, respectively, without complicated valve switching. Also, the container and the piping can be made of thermally suitable materials.

尚、この実施例において前記第4容器1d側の中間熱源配
管12dからの温水を捨てることなく暖房用に用いるよう
にしてもよいし、また、冬期に第3容器1c側の冷熱源配
管9cから捨てる冷水を冷房用に使えば、特に冬期でも冷
房の必要なコンピュータ室を備える建物等に有用であ
る。
In this embodiment, the warm water from the intermediate heat source pipe 12d on the side of the fourth container 1d may be used for heating without being discarded, or in the winter from the cold heat source pipe 9c on the side of the third container 1c. If the cold water to be discarded is used for cooling, it is particularly useful for a building having a computer room that needs cooling even in winter.

(発明の効果) 以上のように本発明によれば、水素吸蔵金属の小塊片を
多数充填した充填層に水素ガスを流通させると共に、熱
媒体を該充填層の上方から降り注ぐことにより、熱交換
効率を向上してコストの低減を達成することができると
共に、反応効率を向上して反応時間を短縮し多他用途に
適用できる効果を有する。
(Effects of the Invention) As described above, according to the present invention, the hydrogen gas is circulated in the packed bed filled with a large number of small pieces of the hydrogen storage metal, and the heat medium is poured from above the packed bed to generate heat. It has an effect that the exchange efficiency can be improved and the cost can be reduced, and the reaction efficiency can be improved and the reaction time can be shortened to be applied to many other purposes.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明を実施したエネルギー変換装置のシステ
ム図、第2図は本発明の第2の実施例である上記エネル
ギー変換装置を利用した温水・冷水供給装置のシステム
図、第3図は本発明の第2の実施例である上記温水・冷
水供給装置の変形例のシステム図である。 1……容器 3……充填層 4……水素配管 5……流出口 6……シャワーヘッド S……小塊片
FIG. 1 is a system diagram of an energy conversion device embodying the present invention, FIG. 2 is a system diagram of a hot / cold water supply device using the energy conversion device according to a second embodiment of the present invention, and FIG. It is a system diagram of the modification of the said hot / cold water supply apparatus which is the 2nd Example of this invention. 1 ... Container 3 ... Packed bed 4 ... Hydrogen piping 5 ... Outflow port 6 ... Shower head S ... Small piece

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】水素吸蔵金属と水素とから金属水素化物を
生成する反応及びその逆の反応を利用したエネルギー変
換方法であって、容器内に水素吸蔵金属の小塊片を多数
充填した充填層を設け、該充填層に水素ガスを流通させ
て該水素ガスを吸蔵又は放出させると共に、該充填層に
上方から熱媒体を降り注ぐようにしたことを特徴とする
水素吸蔵金属を用いたエネルギー変換方法。
1. A method of energy conversion utilizing a reaction for producing a metal hydride from a hydrogen storage metal and hydrogen and vice versa, which is a packed bed in which a large number of small pieces of hydrogen storage metal are filled in a container. And a hydrogen gas is circulated through the packed bed to occlude or release the hydrogen gas, and a heating medium is poured into the packed bed from above. .
【請求項2】水素吸蔵金属と水素とから金属水素化物を
生成する反応及びその逆の反応を利用したエネルギー変
換装置であって、容器内に水素吸蔵金属の小塊片を多数
充填した充填層を設け、該容器の上部に水素配管の接続
口と下部に熱媒体の流出口とを設けると共に、該容器の
内部に該充填層の上方に位置させて熱媒体を該充填層に
降り注ぐ吐出口を設けたことを特徴とする水素吸蔵金属
を用いたエネルギー変換装置。
2. An energy conversion device utilizing a reaction for producing a metal hydride from a hydrogen storage metal and hydrogen and vice versa, which is a packed bed in which a large number of small pieces of the hydrogen storage metal are filled in a container. A discharge port for pouring the heat medium into the filling layer by arranging a hydrogen pipe connection port in the upper part of the container and a heat medium outlet in the lower part, and being located above the filling layer inside the container. An energy conversion device using a hydrogen storage metal.
JP63228330A 1988-09-14 1988-09-14 Energy conversion method and device using hydrogen storage metal Expired - Fee Related JPH0663674B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63228330A JPH0663674B2 (en) 1988-09-14 1988-09-14 Energy conversion method and device using hydrogen storage metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63228330A JPH0663674B2 (en) 1988-09-14 1988-09-14 Energy conversion method and device using hydrogen storage metal

Publications (2)

Publication Number Publication Date
JPH0278868A JPH0278868A (en) 1990-03-19
JPH0663674B2 true JPH0663674B2 (en) 1994-08-22

Family

ID=16874765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63228330A Expired - Fee Related JPH0663674B2 (en) 1988-09-14 1988-09-14 Energy conversion method and device using hydrogen storage metal

Country Status (1)

Country Link
JP (1) JPH0663674B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3322486B2 (en) * 1994-10-05 2002-09-09 三洋電機株式会社 Hydrogen storage alloy with excellent poisoning resistance and regenerative recovery

Also Published As

Publication number Publication date
JPH0278868A (en) 1990-03-19

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