JPH0278868A - Method and apparatus for energy conversion utilizing hydrogen occluding metal - Google Patents

Method and apparatus for energy conversion utilizing hydrogen occluding metal

Info

Publication number
JPH0278868A
JPH0278868A JP63228330A JP22833088A JPH0278868A JP H0278868 A JPH0278868 A JP H0278868A JP 63228330 A JP63228330 A JP 63228330A JP 22833088 A JP22833088 A JP 22833088A JP H0278868 A JPH0278868 A JP H0278868A
Authority
JP
Japan
Prior art keywords
hydrogen
container
heat
reaction
packed bed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP63228330A
Other languages
Japanese (ja)
Other versions
JPH0663674B2 (en
Inventor
Masao Nakajima
正雄 中嶋
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.)
Mitsui Construction Co Ltd
Original Assignee
Mitsui Construction 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 Mitsui Construction Co Ltd filed Critical Mitsui Construction Co Ltd
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

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • 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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

PURPOSE:To improve heat exchanging efficiency and reacting efficiency by a method wherein hydrogen gas is made to flow through a filling layer, filled with a multitude of small blocks of hydrogen occluding metal, and heat medium is poured from the upper part of said filling layer. CONSTITUTION:A vessel 1 is provided with a filling layer 3, in which a multitude of small blocks S of hydrogen occluding metal is filled between upper and lower perforated plates 2, 2, at the middle part thereof, the connecting port 4a of a hydrogen pipeline 4 at the top thereof, the outflow port 5 of liquid heat medium at the lower part thereof, and a discharging port for pouring the heat medium onto the filling layer 3 or a shower head 6 positioned at the upper part of said filling layer 3. The occluding reaction or releasing reaction of said hydrogen gas of the small blocks S of the hydrogen occluding metal is effected by making the hydrogen gas to flow from the connecting port 4a through the filling layer 3 while the heat medium is poured from the shower head 6 onto the filling layer 3 to effect heat exchange by contacting the heat medium directly with the small blocks S.

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] (Field of Industrial Application) The present invention produces metal hydrides from hydrogen and hydrogen storage metals that are mainly used in hydrogen storage and transportation systems and energy recovery and power conversion systems. The present invention relates to an energy conversion method and an energy conversion device using reactions and their inverse reactions.

(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ぎ込んで
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 that utilizes the exothermic hydrogen storage reaction and the converse endothermic hydrogen release reaction when producing a metal hydride from a hydrogen storage metal and hydrogen, for example, , a container is provided with a packed bed filled with hydrogen-absorbing metal particles and a plurality of heat transfer tubes arranged at intervals within the packed bed, and cold water or a heat medium is placed in the heat transfer tubes. By flowing hot water, the metal particles are cooled or heated through the heat transfer tube, and at the same time, hydrogen gas is caused to flow through the packed bed to cause the metal particles to perform a hydrogen storage or release reaction, or the hydrogen gas is pressurized. Alternatively, the pressure is reduced to cause the metal particles to undergo occlusion and desorption reactions, and the resulting reaction heat is used to heat or cool a heat medium through a heat transfer tube to convert energy (Japanese Unexamined Patent Application Publication No. 1983-1999). 101398),
In addition, using a container with a coiled heat transfer tube inside,
The container is filled with a suspension of hydrogen-absorbing metal particles suspended in oil, and the suspension is cooled or heated via a heat medium flowing through the heat transfer tube, and at the same time hydrogen gas is introduced into the suspension. Hydrogen gas is injected to cause hydrogen absorption and desorption reactions, or hydrogen gas is pressurized or depressurized as described above, and the heat medium is heated or cooled through a heat transfer tube to convert energy (
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か、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。
(Problem 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 exchanger tube, or the metal particles that are in direct contact with the heat exchanger tube are filled with metal particles. Since it is only a part of the particles, there was a problem that the heat exchange efficiency deteriorated.

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 metal particles are suspended comes into contact with the heat transfer tube, but the hydrogen gas blown into the suspension becomes bubbles. There was a problem in that the hydrogen rose up in the suspension, resulting in insufficient contact between the metal particles and hydrogen, resulting in deterioration of reaction efficiency.

本発明は、上記の問題点である熱交換効率とを向上する
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法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 method and an energy conversion device using a hydrogen storage metal that improve the heat exchange efficiency, which is the problem mentioned above, and also improve 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べく、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。
(Means for Solving the Problems) In order to achieve the above object, the present invention is an energy conversion device that utilizes a reaction for producing a metal hydride from a hydrogen storage metal and hydrogen, and the reverse reaction. A packed bed filled with a large number of small pieces of hydrogen-absorbing metal is provided in the container, and a connection port for hydrogen piping is provided in the upper part of the container, and a heat medium outlet is provided in the lower part, and the inside of the container is provided above the packed bed. The present invention is characterized in that a discharge port is provided at which the heating medium is poured 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。
(Function) Hydrogen gas is passed through the connection port of the hydrogen piping to the packed bed, and the cooled heat medium is poured into the packed bed from the discharge port, absorbing reaction heat from the small pieces of hydrogen storage metal that make up the packed bed. to cause a hydrogen occlusion reaction, or to cause high-pressure hydrogen gas to flow through the connection port to the packed bed to cause the small pieces to generate heat due to the hydrogen occlusion reaction, and at the same time pouring a heating medium onto the packed bed; The heating medium is heated as a heat source. On the other hand, for the metal hydride produced by this reaction, a heated heating 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 the small pieces to have an endothermic effect due to a hydrogen release reaction, and a heating medium is poured onto the packed bed to cool the heating medium as 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6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6小塊片の全表面積を伝熱面
績として熱交換を行わせることができ、また水素ガスも
、該6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かできる。
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 flowing hydrogen gas, the heat medium passes through the gaps between the six small pieces and spreads over the surface of the six small pieces. At the same time, hydrogen gas is accompanied by the heating medium or freely flows through the gaps between the small pieces. Therefore, the heating medium can directly contact each small piece of the hydrogen storage metal, and heat exchange can be performed using the entire surface area of the six small pieces as a heat transfer area. The absorption/desorption reaction can be carried out using the total surface area of the reaction area.

(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
連通ずる循環回路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IO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IO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1
0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) Referring to FIG. 1, 1 indicates a container, and the container 1 is filled with a large number of hydrogen-absorbing metal small pieces S in the upper and lower perforated plates 2.2 in the middle thereof. layer 3 is provided, the container 1
A connection port 4a for the hydrogen pipe 4 is provided at the top of the container 1, and an outlet 5 for the liquid heat medium is provided at the bottom of the container 1. A shower head 6 is provided as a discharge port to flow hydrogen gas from the connection port 4a to the packed bed 3 to cause the hydrogen gas to be absorbed or released into the small pieces S of the hydrogen storage metal. At the same time, the heating medium is poured from the shower head 6 onto the packed bed 3, so that the heating medium and the small pieces S are brought into direct contact with each other to perform heat exchange, and further,
A circulation circuit 7 is provided outside the container 1 to communicate the shower head 6 and the outlet 5, and a circulation pump 8 and a heat exchanger IO connected to an external pipe 9 are interposed in the circulation circuit 7. , the heat medium that has fallen onto the packed bed 3 is guided from the lower part of the container to the circulation circuit 7, passed through the heat exchanger IO from the circulation pump 8, and guided to the shower head 6, and the heat exchanger 1
At 0, hot water, cold water, or intermediate water is introduced into the external pipe 9 to exchange heat with the heat medium.

この場合、該熱媒体には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バッ
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 such as an organic solvent or silicon should be used as the heating medium, and the hydrogen storage metal small pieces S should be spherical, about 10 to 50 mm in size, or Raschig ring, etc.
Slotted rings, interlock saddles, terrarets, pole rings, lessing rings, magmahon backings, etc. shall be 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, when the hydrogen storage metal is caused to perform a storage reaction or a desorption reaction, hydrogen gas is passed through the packed bed 3, and cold water is introduced into the external piping 9 to cool the heat medium. is poured into the packed bed 3 and absorbs the reaction heat from the small pieces S to absorb hydrogen, and conversely, hot water is introduced into the external piping 9 to heat the heat medium and transfer the reaction heat to the small pieces S. is supplied 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。
In addition, when recovering heat from the hydrogen storage alloy, the hydrogen gas in the packed bed 3 is pressurized to cause the small pieces S to perform a hydrogen storage reaction to generate heat, and the heat medium is transferred to the packed bed 3. 3 to heat the heat medium and heat the intermediate water introduced into the external piping 9 as a heat source, and conversely reduce the pressure of hydrogen gas to cause the small pieces S to have an endothermic effect due to a release reaction, The intermediate water cooled by cooling the heat medium and introduced into the external pipe 9 is used as a cold heat source.

この場合、水素吸蔵金属の小塊片Sに上記にょうなラシ
ヒリング状やス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 the small pieces S of the hydrogen storage metal are formed into a Raschig ring shape or a slotted ring shape as described above, there will be resistance to the flow of hydrogen gas or the flow of the heat medium into the packed bed 3. In addition, it is possible to form a sufficient gap between the small pieces S and to increase the surface area of the small pieces S, thereby increasing the heat exchange area with the heat medium and the reaction area with 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 water/cold water supply device using the above device will be described based on 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で連通ずると共に、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9a、 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 includes a pair of devices used in the first embodiment, and communicates a first container 1a and a second container 1b through a hydrogen pipe 4 with a gate valve 11, and connects both external pipes 9 to each other. It is composed of a hot heat source pipe 9a and a cold heat source pipe 9b, and intermediate heat source pipes 12a,
12b is connected, and a plurality of switching valves 13 provided thereon are used to appropriately switch between the hot heat source pipe 9a and the intermediate heat source pipe 12a, or between the cold heat source pipe 9b and the intermediate heat source pipe 12b.

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la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tb側に導き、該第2容器1b
に吹き込んで該第2容器lb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
lb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1a、■b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 device is used, for example, in a heating and cooling system that uses late-night electricity, hot water that has been heated using late-night electricity is guided to the heat source piping 9a, and a hydrogen release reaction is caused in the first container la side. , the released hydrogen gas is guided to the second container tb side via the hydrogen pipe 4, and the second container 1b is
to cause a hydrogen storage reaction to occur on the second container lb side, and at the same time, the reaction heat generated by this storage reaction is discarded by exchanging heat with room temperature intermediate water led to the intermediate heat source piping 12b on the second container lb side. When the release reaction and storage reaction are finished and both containers 1a and 1b are in an equilibrium state,
The gate valve 11 of the hydrogen pipe 4 is closed to complete the preparation stage for heating and cooling.

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la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Ya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
lb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lb側の反応熱を中間熱源配
管L2bから冷水として捨てると共に、第1容器la側
の温熱源配管9aから暖房用に温水をiするようする。
When entering the daytime cooling/heating stage, first, the gate valve 11 is opened to supply air from the second container 1b, which is in a high pressure state, to the first container, which is in a low pressure state.
Hydrogen gas is caused to flow into the container 1a, an occlusion reaction is caused on the first container 1a side to heat the heat medium, and a release reaction is caused on the second container 1b side to cool the heat medium, In the summer, the reaction heat from the first container Ya side is discarded as hot water from the intermediate heat source piping 12a, and cold water for cooling is obtained from the cold heat source piping 9b on the second container lb side. The reaction heat on the lb side is discarded as cold water from the intermediate heat source piping L2b, and hot water is supplied for heating from the heat source piping 9a on the first container la side.

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。′ 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。
However, hot water in the 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 late-night power generation. ' FIG. 3 shows a modification of the hot water/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ICと、吸蔵反応専用の第2容器ib及び
第4容器1dとを備え、各容器1a、 lb、 lc、
 ld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ICとを水素配管4,4で連通ずると共に、各
容器1a、lb、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
通ずる搬送配管15を接続し、該各様送配管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ICの熱交換器IOC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+2d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 installed and operated continuously, and a first container 1a dedicated to the release reaction is used.
and a third container IC, and a second container ib and a fourth container 1d dedicated to the occlusion reaction, each container 1a, lb, lc,
Inside the ld, small pieces S of hydrogen storage metal are stacked without using the perforated plate 2.2 to form a packed layer 3, and the first container 1a, the fourth container 1d, and the second container 1b and the third container IC are communicated by hydrogen pipes 4, 4, and a separator 14 is provided on the outlet 5 side of each container 1a, lb, 1c, 1d to separate the heat medium and the small pieces S, The separator 14 includes a first container 1a, a second container 1b, and a third container 1C, respectively.
A conveying pipe 15 is connected between the fourth container 1d and the outflow port 5 side and the upper part thereof, and a conveying device 16 interposed in each direction conveying pipe 15 is used to transfer the flow from one container to the other container. Furthermore, the heat source piping 12a is connected to the heat exchanger 10a of the first container 1a, the heat source piping 9b is connected to the heat exchanger 10b of the second container 1b, and the heat source piping 9b is connected to the heat exchanger 10b of the second container 1b. A cold heat source pipe 9C is connected to the heat exchanger IOC of the IC, and an intermediate heat source pipe +2d is connected to the heat exchanger 10d of the fourth container 1d.

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1
cとは冷暖房工程に用いるようにし、すなイつち、排熱
を用いて昇温した温水を第1容器1a側の熱源配管12
a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ld側の中
間熱源配管12dから捨てるようにし、この内容器1a
、 ldにより$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 for the preparation process, and the second container 1b and the third container 1
c is intended to be used in the cooling and heating process, that is, hot water heated using exhaust heat is supplied to the heat source pipe 12 on the side of the first container 1a.
a, a hydrogen release reaction is caused in the first container 1a, and the released hydrogen gas is passed through the hydrogen pipe 4 to the fourth container 1d.
to cause the fourth container 1d to perform a hydrogen storage reaction, and at the same time, the reaction heat from this storage reaction is discarded from the intermediate heat source piping 12d on the fourth container ld side, and this inner container 1a
, ld performs a release reaction and an occlusion reaction as $ storage steps.

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lb側の温熱源配管9
bから暖房用に温水を得るようにする。
On the other hand, in the heating and cooling process, hydrogen gas is caused to flow from the third container 1c to the second container 1b, so that a release reaction is performed in the third container 1c and an occlusion reaction is performed in the second container 1b,
During the summer, the reaction heat from the second container 1b is transferred to the heat source piping 9b.
At the same time, cold water for cooling is obtained from the cold source pipe 9C on the third container 1c side, and in winter, the reaction heat from the third container 1c side is discarded as cold water from the cold heat source pipe 9c. , heat source piping 9 on the second container lb side
To obtain hot water for heating from b.

そして、上記の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IC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。
Immediately before the above reaction cycle is completed, the small pieces S are exchanged between the first container 1a and the second container 1b, and between the third container IC and the fourth container 1d by each transport device 16. Then, repeat this series of operations to continuously obtain hot 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 release, and the piping can be configured for a heat source, a cold source, a hot source, and an intermediate heat source, without having to change valves. , and the container and piping can each be constructed of thermally suitable materials.

尚、この実施例において前記第4容器Ld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Ic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ユータ室を備える建物等に有
用である。
In this embodiment, the hot water from the intermediate heat source pipe 12d on the fourth container Ld side may be used for heating without being discarded, or the hot water may be used for heating from the cold heat source pipe 9C on the third container Ic side in the winter. If the discarded cold water can be used for air conditioning, it is especially useful for buildings with computer rooms that require air conditioning even in the 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, hydrogen gas is circulated through a packed bed filled with a large number of small pieces of hydrogen-absorbing metal, and a heat medium is poured from above the packed bed to generate heat. It is possible to improve exchange efficiency and reduce costs, and also has the effect of improving reaction efficiency and shortening reaction time, which can be applied to many other uses.

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

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 1、 事  件  の  表  示 昭和63年特許願第228330号 及びその装置 3、補正をする者 事件との関係  特許出願人 三井建設 株式会社 4、代  理  人 5、補正命令の日付(自発) 6、補正の対象 明細書の発明の詳細な説明の欄および図面7、補正の内
容 1、明細書の第4頁第12行目の「向上するする」を「
向上する」と訂正する。 2、同書箱4頁16行目と同頁箱17行目との間に次の
文書を加入する。 「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。」3、
同書第4頁第17行目の「本発明は上記目的を達成すべ
く、」を「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、」と訂正する。 4、同書第7頁第20行目の「該熱媒体には」を「該熱
媒体には水、」と訂正する。 5、図面の第2図を添付別紙の通り訂正する。
Fig. 1 is a system diagram of an energy conversion device implementing the present invention, Fig. 2 is a system diagram of a hot water/cold water supply device using the above energy conversion device which is a second embodiment of the invention, and Fig. 3 is a system diagram of an energy conversion device according to the present invention. It is a system diagram of a modification of the above-mentioned hot water/cold water supply device which is a second embodiment of the present invention. 1... Container 3... Filling layer 4... Hydrogen piping 5... Outlet 6... Shower head S... Small piece 1, Incident display 1988 Patent Application No. 228330 and its device 3, Relationship with the case of the person making the amendment Patent applicant Mitsui Construction Co., Ltd. 4 Agent 5 Date of order for amendment (voluntary) 6. Invention of the specification subject to amendment Detailed explanation column, drawing 7, amendment content 1, page 4, line 12 of the specification, “improve” was changed to “improve”.
It will improve,” he corrected. 2. Add the following document between the 16th line on page 4 of the same book box and the 17th line of the same page box. ``The present invention proposes a conversion method that achieves the above object, and is an energy conversion method that utilizes the reaction of producing metal hydride from a hydrogen storage metal and hydrogen, and the reverse reaction. A packed bed filled with a large number of small pieces of storage metal is provided, hydrogen gas is passed through the packed bed to store or release the hydrogen gas, and a heating medium is poured into the packed bed from above. 3.
On page 4, line 17 of the same book, ``The present invention aims to achieve the above object'' is corrected to ``Furthermore, the present invention proposes a conversion device for carrying out the above conversion method.'' 4. In the 20th line of page 7 of the same book, "the heat medium" is corrected to "the heat medium is water." 5. Figure 2 of the drawings is corrected as shown in the attached appendix.

Claims (1)

【特許請求の範囲】 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。 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。
[Scope of Claims] 1. An energy conversion method that utilizes the reaction of producing a metal hydride from a hydrogen-absorbing metal and hydrogen, and its reverse reaction, wherein a large number of small pieces of a hydrogen-absorbing metal are filled in a container. A hydrogen storage metal is used, characterized in that a packed bed is provided, hydrogen gas is passed through the packed bed to store or release the hydrogen gas, and a heating medium is poured into the packed bed from above. Energy conversion method. 2. An energy conversion device that utilizes the reaction of producing a metal hydride from a hydrogen-absorbing metal and hydrogen, and its reverse reaction, in which a packed bed filled with a large number of small pieces of a hydrogen-absorbing metal is provided in a container, A connection port for hydrogen piping is provided in the upper part of the container, and an outlet for the heating medium is provided in the lower part, and a discharge port is provided inside the container, which is located above the packed bed and pours the heating medium onto the packed bed. An energy conversion device using a hydrogen storage metal characterized by the following.
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 true JPH0278868A (en) 1990-03-19
JPH0663674B2 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)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5851690A (en) * 1994-10-05 1998-12-22 Sanyo Electric Co., Ltd. Hydrogen absorbing alloys

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5851690A (en) * 1994-10-05 1998-12-22 Sanyo Electric Co., Ltd. Hydrogen absorbing alloys

Also Published As

Publication number Publication date
JPH0663674B2 (en) 1994-08-22

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