JPH06276701A - Electric power storing device - Google Patents
Electric power storing deviceInfo
- Publication number
- JPH06276701A JPH06276701A JP5061820A JP6182093A JPH06276701A JP H06276701 A JPH06276701 A JP H06276701A JP 5061820 A JP5061820 A JP 5061820A JP 6182093 A JP6182093 A JP 6182093A JP H06276701 A JPH06276701 A JP H06276701A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- oxygen
- electric power
- electrolysis
- power
- 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
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/186—Regeneration by electrochemical means by electrolytic decomposition of the electrolytic solution or the formed water product
-
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、夜間余剰電力等の電力
を効果的に貯蔵するようにした電力貯蔵装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric power storage device for effectively storing electric power such as surplus electric power at night.
【0002】[0002]
【従来の技術】電力消費が昼と夜で著しく異るために、
夜間に余った電力を貯蔵し昼のピーク負荷時に放電(発
電)する電力貯蔵装置として揚水発電所がある。揚水発
電所では夜間の余剰電力を利用してポンプで下方のダム
から上方のダムへ水を汲みあげ、日中は水車発電機によ
り発電する。揚水発電所は、山間部にダムを築いてつく
られる。このため立地に制限があり、かつ建設期間も長
いため増大する一方の昼と夜の電力消費量格差への対応
が迅速でない。このため、昼間のピーク電力対応は石油
火力発電所等の運転に頼ることになるが、石油火力発電
所は、地球温暖化の原因となる炭酸ガスを排出する。2. Description of the Related Art Since power consumption is significantly different between day and night,
There is a pumped storage power plant as a power storage device that stores excess power at night and discharges (generates power) during peak load during the day. At the pumped storage power plant, surplus electricity at night is used to pump water from the lower dam to the upper dam, and power is generated by the turbine generator during the day. Pumped storage power plants are built by building dams in the mountains. For this reason, there are restrictions on the location and the construction period is long, so it is not quick to respond to the increasing electricity consumption gap between day and night. Therefore, the peak power demand during the daytime depends on the operation of the oil-fired power plant or the like, but the oil-fired power plant emits carbon dioxide which causes global warming.
【0003】[0003]
【発明が解決しようとする課題】本発明は、ダムの建設
などの立地上の制約を受けず、かつ、地球環境保全上問
題となる炭酸ガスを排出することなしに電力を貯蔵する
ことのできる装置を提供することを課題としている。ま
た、本発明は、既設の原子力プラントを有効に活用して
効率の高い電力貯蔵装置を提供することをも課題として
いる。The present invention is capable of storing electric power without being restricted by location such as construction of a dam, and without discharging carbon dioxide gas which is a problem in global environment conservation. An object is to provide a device. Another object of the present invention is to provide a highly efficient power storage device by effectively utilizing an existing nuclear power plant.
【0004】[0004]
【課題を解決するための手段】前記課題を解決するた
め、本発明による電力貯蔵装置では固体酸化物電解質を
有し水蒸気電解セルと燃料電池を兼用する電解兼発電手
段と、該電解兼発電手段によって発生又は消費する水素
及び酸素をそれぞれ貯蔵する手段とを原子力プラントに
隣接し、前記電解兼発電手段は該原子力プラントの熱に
より加熱した水蒸気を該プラントの電力により電解して
水素と酸素を製造し前記水素と酸素をそれぞれ貯蔵する
手段に貯蔵し、該水素及び酸素を用いて再び電力を取り
出し前記原子力プラントへ送電するようにした構成を採
用する。In order to solve the above-mentioned problems, in an electric power storage device according to the present invention, an electrolysis / power generation means having a solid oxide electrolyte and serving both as a steam electrolysis cell and a fuel cell, and the electrolysis / power generation means. And a means for respectively storing hydrogen and oxygen generated or consumed by the nuclear power plant, and the electrolysis / power generation means electrolyzes the steam heated by the heat of the nuclear power plant with the electric power of the plant to produce hydrogen and oxygen. Then, the hydrogen and oxygen are stored in respective storage means, and the hydrogen and oxygen are used to extract electric power again and transmit the electric power to the nuclear power plant.
【0005】[0005]
【作用】本発明では電解兼発電手段に供給された水蒸気
が余剰電力を利用して電気分解されて酸素と水素を発生
し、これらを貯蔵する手段に貯蔵される。発電時には、
酸素、水素の各貯蔵手段から酸素と水素を電解兼発電手
段に供給し、該電解兼発電手段を燃料電池として作用さ
せて酸素と水素を反応させて水蒸気を発生し、その際に
電流を発生させる。In the present invention, the steam supplied to the electrolysis and power generation means is electrolyzed by using the surplus power to generate oxygen and hydrogen, which are stored in the storage means. During power generation,
Oxygen and hydrogen are supplied from the storage means for oxygen and hydrogen to the electrolysis / power generation means, and the electrolysis / power generation means acts as a fuel cell to react oxygen and hydrogen to generate water vapor, at which time an electric current is generated. Let
【0006】なお、この発電時の燃料電池の排熱により
水蒸気を発生させ、蒸気タービンを駆動して電力を得れ
ば、発電効率が高められる。電解兼発電手段による水蒸
気電解時に、供給される水蒸気は電解時に生成した水
素、酸素の熱エネルギで加熱されるが、不足する熱エネ
ルギは、原子力プラントの2次系蒸気等を熱源として補
給する。従って不足する熱エネルギを電力として与える
必要がなく、電解時の電力消費が少なくなる。The power generation efficiency can be improved by generating steam by exhaust heat of the fuel cell at the time of power generation and driving the steam turbine to obtain electric power. During the steam electrolysis by the electrolysis / power generation means, the supplied steam is heated by the thermal energy of hydrogen and oxygen generated during electrolysis, but the insufficient thermal energy is supplemented by the secondary steam of the nuclear power plant as a heat source. Therefore, it is not necessary to supply the insufficient heat energy as electric power, and the electric power consumption during electrolysis is reduced.
【0007】[0007]
【実施例】以下、本発明による電力貯蔵装置を図示した
実施例に基づいて具体的に説明する。まず図1におい
て、1は水蒸気を電気分解して水素と酸素を発生させ、
かつ、水素と酸素を反応させて水蒸気にすることによっ
て発電を行なうリバーシブル形固体酸化物電解セル(以
下リバーシブル形SOE(Solid Oxide Electrolysis)電
解セルと称す)である。このリバーシブル形SOE電解
セルは電解質として安定化ジルコニアのような酸素イオ
ン導電体の板を用い、板の両面に白金等の多孔質性のア
ノード電極、カソード電極を取りつけ、これらの電極に
加圧水型原子力プラントの発生する交流電力がコンバー
タ11を介して接続されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A power storage device according to the present invention will be specifically described below based on the illustrated embodiments. First, in FIG. 1, 1 is the electrolysis of water vapor to generate hydrogen and oxygen,
Further, it is a reversible type solid oxide electrolysis cell (hereinafter referred to as a reversible type SOE (Solid Oxide Electrolysis) electrolysis cell) that generates electric power by reacting hydrogen and oxygen into water vapor. This reversible SOE electrolysis cell uses a plate of oxygen ion conductor such as stabilized zirconia as an electrolyte, and a porous anode electrode and cathode electrode such as platinum are attached to both surfaces of the plate, and pressurized water nuclear power is attached to these electrodes. AC power generated by the plant is connected via a converter 11.
【0008】リバーシブル形SOE電解セル1は水蒸気
の電気分解に当っては水蒸気電解セルとして作用し、一
方、前記したように水素と酸素の反応によって水蒸気を
発生させるときには、酸素イオンが電解質を透過するこ
とによって発電を行なう燃料電池として作用する。The reversible SOE electrolysis cell 1 acts as a steam electrolysis cell in electrolysis of water vapor, while oxygen ions permeate the electrolyte when water vapor is generated by the reaction of hydrogen and oxygen as described above. It acts as a fuel cell that generates electricity.
【0009】3は水タンクで、この水タンク3からの水
は、ポンプ12A、再生熱交換器6A〜6D、熱交換器
7C,7B、補助ヒータ5を経て、リバーシブル形SO
E電解セル1のカソード電極側へ至るように接続され
る。2は水素タンクで、圧縮機13A、再生熱交換器6
A,6Bを経て、前記リバーシブル形SOE電解セルの
カソード電極側に接続される。4は酸素タンクで、圧縮
機13B、再生熱交換器6C,6Dを経て、リバーシブ
ル形SOE電解セル1のアノード電極側へ接続される。Reference numeral 3 denotes a water tank. Water from the water tank 3 passes through a pump 12A, regenerative heat exchangers 6A to 6D, heat exchangers 7C and 7B, and an auxiliary heater 5, and is reversible SO.
The E electrolysis cell 1 is connected to reach the cathode electrode side. 2 is a hydrogen tank, which is a compressor 13A and a regenerative heat exchanger
It is connected to the cathode electrode side of the reversible type SOE electrolysis cell through A and 6B. An oxygen tank 4 is connected to the anode electrode side of the reversible SOE electrolysis cell 1 via the compressor 13B and the regenerative heat exchangers 6C and 6D.
【0010】前記リバーシブル形SOE電解セル1のカ
ソード側の水蒸気と水素のラインは、サーキュレータ1
4と熱交換器7Aを介して、接続される。熱交換器7C
は、加圧水型原子力プラント10の2次系蒸気の熱源が
中間熱交換器8を介して、熱エネルギを輸送できるよう
に接続される。熱交換器7Aおよび7Bの2次側には蒸
気タービン発電機9、コンデンサ16、ポンプ12Bか
らなる水蒸気閉サイクルが構成される。なお、図中15
A,15Bは、それぞれ、圧力調節弁である。The steam and hydrogen lines on the cathode side of the reversible SOE electrolysis cell 1 are connected to the circulator 1.
4 and the heat exchanger 7A. Heat exchanger 7C
Are connected so that the heat source of the secondary steam of the pressurized water nuclear power plant 10 can transfer heat energy via the intermediate heat exchanger 8. A steam closed cycle composed of the steam turbine generator 9, the condenser 16, and the pump 12B is formed on the secondary side of the heat exchangers 7A and 7B. In addition, 15 in the figure
A and 15B are pressure control valves, respectively.
【0011】本実施例において電力貯蔵時の作用につい
て説明する。電力貯蔵は、リバーシブル形SOE電解セ
ル1において水蒸気を電気分解して水素と酸素を製造
し、水素の化学エネルギとして貯蔵することによってお
こなわれる。電気分解に使う水は、水タンク3からポン
プ12Aによって、まず再生熱交換器6B,6Dを通さ
れ、リバーシブル形SOE電解セル1における電解で生
成されて水素タンク2、酸素タンク4へそれぞれ戻る水
素および酸素によって加熱される。さらに熱交換器7C
に至り、ここで加圧水型原子力プラント10の2次系の
蒸気の熱を中間熱交換器8へ伝達された熱エネルギで電
解水が水蒸気へと加熱される。さらに再生熱交換器6
A,6Cを通って、電解セル1で製造された水素、酸素
で加熱され、補助ヒータ5で所定の温度に微調整され、
前記リバーシブル形SOE電解セル1のカソード側へ入
る。In the present embodiment, the operation during power storage will be described. Electric power storage is performed by electrolyzing steam in the reversible SOE electrolysis cell 1 to produce hydrogen and oxygen, and storing the hydrogen and oxygen as chemical energy. The water used for electrolysis is first passed through the regenerative heat exchangers 6B and 6D from the water tank 3 by the pump 12A, is generated by electrolysis in the reversible type SOE electrolysis cell 1, and is returned to the hydrogen tank 2 and the oxygen tank 4, respectively. And heated by oxygen. Further heat exchanger 7C
At this point, the electrolyzed water is heated to steam by the heat energy of the heat of the secondary steam of the pressurized water nuclear power plant 10 transferred to the intermediate heat exchanger 8. Regeneration heat exchanger 6
It is heated by hydrogen and oxygen produced in the electrolysis cell 1 through A and 6C, and finely adjusted to a predetermined temperature by the auxiliary heater 5,
It enters the cathode side of the reversible SOE electrolysis cell 1.
【0012】リバーシブル形SOE電解セルで製造され
た水素は再生熱交換器6A,6Bを通るときに電解用水
蒸気、水に熱を伝え、自らは冷えて圧縮機13Aで加圧
されて水素タンク2へ貯蔵される。一方、製造された酸
素は、再生熱交換器6C,6Dを通るときに電解用水蒸
気、水に熱を伝え、自らは冷えて圧縮機13Bで加圧さ
れ酸素タンク4へ貯蔵される。Hydrogen produced in the reversible SOE electrolysis cell transfers heat to electrolysis steam and water as it passes through the regenerative heat exchangers 6A and 6B, cools itself and is pressurized by the compressor 13A, and the hydrogen tank 2 Stored in. On the other hand, the produced oxygen transfers heat to the electrolysis steam and water as it passes through the regenerative heat exchangers 6C and 6D, cools itself and is pressurized by the compressor 13B and stored in the oxygen tank 4.
【0013】次に発電時の作用について説明する。水素
は水素タンク2から、圧力調節弁15Aを経て、再生熱
交換器6B,6Aを通るときに、発電によって製造され
た水蒸気、水で加熱され、リバーシブル形SOE電解セ
ル1のカソード側へ供給される。酸素は酸素タンク4か
ら圧力調節弁15Bを経て再生熱交換器6C,6Dを経
て加熱され、前記リバーシブル形SOE電解セル1のア
ノード側へ供給される。リバーシブル形SOE電解セル
1は燃料電池として作用して、水素と酸素は反応により
水蒸気となり電流が発生する。この電流はコンバータ部
11から逆に原子力プラント10へ送られる。Next, the operation during power generation will be described. Hydrogen is supplied from the hydrogen tank 2 to the cathode side of the reversible SOE electrolysis cell 1 as it is heated by steam and water produced by power generation when passing through the pressure control valve 15A and the regenerative heat exchangers 6B and 6A. It Oxygen is heated from the oxygen tank 4 through the pressure control valve 15B, the regenerative heat exchangers 6C and 6D, and is supplied to the anode side of the reversible SOE electrolysis cell 1. The reversible-type SOE electrolysis cell 1 functions as a fuel cell, and hydrogen and oxygen react with each other to become steam to generate an electric current. This current is sent from the converter unit 11 to the nuclear power plant 10 in reverse.
【0014】電解セル1が燃料電池として作用するとき
に、ほぼ電気出力に等しい排熱が発生する。この熱はサ
ーキュレータ14を駆動してリバーシブル形SOE電解
セル1に多量の水蒸気を再循環し、その循環ラインに設
置される熱交換器7Aと、水タンク3へ戻る水蒸気ライ
ンの熱交換器7Bから、蒸気タービン9およびコンデン
サ16などからなる閉水蒸気サイクル系へ伝熱する。こ
の閉水蒸気サイクル系では、高圧水蒸気を用いて蒸気タ
ービン9を駆動して、前記した燃料電池以外に電力を得
る。When the electrolysis cell 1 acts as a fuel cell, exhaust heat, which is almost equal to the electric output, is generated. This heat drives the circulator 14 to recirculate a large amount of steam in the reversible type SOE electrolysis cell 1, and from the heat exchanger 7A installed in the circulation line and the heat exchanger 7B in the steam line returning to the water tank 3. , To the closed steam cycle system including the steam turbine 9 and the condenser 16. In this closed steam cycle system, high-pressure steam is used to drive the steam turbine 9 to obtain electric power in addition to the fuel cell described above.
【0015】このやり方は、電解時の電力を少なくする
とともに、発電効率が高められるので電力の貯蔵効率を
高める。前記実施例の電力貯蔵装置における電力貯蔵効
率の向上をさらに具体的に示すために、図2のシステム
例と比較する。図2は電解時に利用する熱源も、また発
電時の補助発電手段もない基本的なリバーシブル形SO
E電解セルによる電力貯蔵システムの例であり、必要な
熱はすべて電力で与える方式である。図2における符号
は図1の符号と対応して付してある。According to this method, the electric power at the time of electrolysis is reduced and the power generation efficiency is improved, so that the storage efficiency of the electric power is improved. In order to more specifically show the improvement of the power storage efficiency in the power storage device of the above embodiment, the system is compared with the system example of FIG. Fig. 2 shows a basic reversible SO with neither heat source used during electrolysis nor auxiliary power generation means during power generation.
This is an example of an electric power storage system using an E electrolysis cell, in which all necessary heat is supplied by electric power. The reference numerals in FIG. 2 are given corresponding to the reference numerals in FIG.
【0016】図3と図4にそれぞれ図1と図2のシステ
ムのエネルギフローを示す。図2のシステムでは図4に
みられるように68.6ワットの電力を貯蔵して、再び
とり出せる電力は34.15ワットで、電力貯蔵効率は
49.8%である。これに対し、図1の本発明の実施例
の場合を示す図3では60.03ワットの電力貯蔵に対
し再びとり出せる電力は44.4ワットで電力貯蔵効率
は74%となる。以上、本発明を図示した実施例につい
て具体的に説明したが、本発明がこの実施例に限定され
ないことはいうまでもない。FIGS. 3 and 4 show the energy flow of the system of FIGS. 1 and 2, respectively. In the system shown in FIG. 2, as shown in FIG. 4, 68.6 watts of electric power is stored and can be extracted again at 34.15 watts, and the power storage efficiency is 49.8%. On the other hand, in FIG. 3 showing the case of the embodiment of the present invention in FIG. 1, the electric power that can be extracted again for the electric power storage of 60.03 watts is 44.4 watts, and the electric power storage efficiency is 74%. The present invention has been specifically described above with reference to the illustrated embodiment, but it goes without saying that the present invention is not limited to this embodiment.
【0017】[0017]
【発明の効果】以上具体的に説明したように、本発明に
よる電力貯蔵装置は固体酸化物電解質を有し水蒸気電解
セルと燃料電池を兼用する電解兼発電手段と、該電解兼
発電手段によって発生又は消費する水素及び酸素をそれ
ぞれ貯蔵する手段とを原子力プラントに隣接し、前記電
解兼発電手段は該原子力プラントの熱により加熱した水
蒸気を該プラントの電力により電解して水素と酸素を製
造し前記水素及び酸素をそれぞれ貯蔵する手段に貯蔵
し、該水素と酸素を用いて再び電力を取り出し前記原子
力プラントへ送電するよう構成されているので、原子力
プラントから発生する電力と、熱エネルギを利用するこ
とによって、余剰電力等を利用して水蒸気を水素と酸素
に分解して貯蔵し、必要時にこの水素と酸素を反応させ
て発電効率の高い発電を行なうことができる。As described in detail above, the power storage device according to the present invention has an electrolysis / power generation means which has a solid oxide electrolyte and also serves as a steam electrolysis cell and a fuel cell, and is generated by the electrolysis / power generation means. Or adjacent to the nuclear power plant with a means for respectively storing consumed hydrogen and oxygen, the electrolysis and power generation means to produce hydrogen and oxygen by electrolyzing the steam heated by the heat of the nuclear power plant with the power of the plant, Since hydrogen and oxygen are stored in respective storage means, and the hydrogen and oxygen are used to extract electric power again and transmit the electric power to the nuclear power plant, use of electric power and thermal energy generated from the nuclear power plant. By using the surplus power, etc., steam is decomposed into hydrogen and oxygen and stored, and when necessary, this hydrogen and oxygen are reacted to generate electricity with high power generation efficiency. It can be carried out.
【0018】特に、本発明においては、電力貯蔵装置を
原子力プラントに隣接することによって次の効果が達成
される。In particular, in the present invention, the following effects are achieved by placing the power storage device adjacent to the nuclear power plant.
【0019】(1)原子力プラントの熱を利用して、電
気分解する水蒸気を加熱することにより電力貯蔵効率が
高くなる。(1) By utilizing the heat of the nuclear power plant to heat the steam to be electrolyzed, the power storage efficiency is increased.
【0020】(2)電力を再びとり出すときは、原子力
プラントの送電設備が利用できるので、揚水発電所のよ
うに受送電設備が不要となる。(2) When the electric power is extracted again, the power transmission equipment of the nuclear power plant can be used, so that the power transmission / reception equipment unlike the pumped storage power plant is unnecessary.
【0021】(3)原子力プラントを電力需給に無関係
に常時定格運転することができ、稼働率向上と経済性向
上が計れる。(3) The nuclear power plant can be constantly operated at the rated power regardless of the supply and demand of electric power, and the operating rate and the economical efficiency can be improved.
【図1】本発明の第1実施例に係る電力貯蔵装置の系統
図。FIG. 1 is a system diagram of a power storage device according to a first embodiment of the present invention.
【図2】本発明によらない水素利用電力貯蔵装置の基本
系統図。FIG. 2 is a basic system diagram of a hydrogen-utilizing power storage device according to the present invention.
【図3】図1に示す電力貯蔵装置におけるエネルギフロ
ーを示す線図。FIG. 3 is a diagram showing an energy flow in the power storage device shown in FIG. 1.
【図4】図2に示す電力貯蔵装置におけるエネルギフロ
ーを示す線図。FIG. 4 is a diagram showing an energy flow in the power storage device shown in FIG. 2.
1 リバーシブル形SOE電解セル 2 水素タンク 3 水タンク 4 酸素タンク 5 補助ヒータ 6 再生熱交換器 7 熱交換器 8 中間熱交換器 9 蒸気タービン 10 加圧水型原子力プラント 11 コンバータ 12 ポンプ 13 圧縮機 14 サーキュレータ 15 圧力調節弁 16 コンデンサ 1 Reversible SOE Electrolysis Cell 2 Hydrogen Tank 3 Water Tank 4 Oxygen Tank 5 Auxiliary Heater 6 Regenerative Heat Exchanger 7 Heat Exchanger 8 Intermediate Heat Exchanger 9 Steam Turbine 10 Pressurized Water Nuclear Plant 11 Converter 12 Pump 13 Compressor 14 Circulator 15 Pressure control valve 16 condenser
───────────────────────────────────────────────────── フロントページの続き (72)発明者 釘宮 啓一 神戸市兵庫区和田崎町一丁目1番1号 三 菱重工業株式会社神戸造船所内 (72)発明者 吉野 昌和 神戸市兵庫区和田崎町一丁目1番1号 三 菱重工業株式会社神戸造船所内 (72)発明者 丸山 智義 神戸市兵庫区和田崎町一丁目1番1号 三 菱重工業株式会社神戸造船所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Keiichi Kugimiya 1-1-1, Wadasaki-cho, Hyogo-ku, Kobe Sanbishi Heavy Industries Ltd. Kobe Shipyard (72) Inventor Masakazu Yoshino, Wadazaki-cho, Hyogo-ku, Kobe 1-1-1 Sanryo Heavy Industries Co., Ltd. Kobe Shipyard (72) Inventor Tomoyoshi Maruyama 1-1-1 Wadasaki-cho, Hyogo-ku, Kobe Sanryo Heavy Industry Co., Ltd. Kobe Shipyard
Claims (1)
と燃料電池を兼用する電解兼発電手段と、該電解兼発電
手段によって発生又は消費する水素及び酸素をそれぞれ
貯蔵する手段とを原子力プラントに隣接し、前記電解兼
発電手段は該原子力プラントの熱により加熱した水蒸気
を該プラントの電力により電解して水素と酸素を製造し
前記水素及び酸素をそれぞれ貯蔵する手段に貯蔵し、該
水素と酸素を用いて再び電力を取り出し前記原子力プラ
ントへ送電するよう構成されていることを特徴とする電
力貯蔵装置。1. A nuclear power plant is provided with an electrolysis / power generation means having a solid oxide electrolyte and also used as a steam electrolysis cell and a fuel cell, and means for respectively storing hydrogen and oxygen generated or consumed by the electrolysis / power generation means. Adjacent to each other, the electrolysis / power generation means electrolyzes the steam heated by the heat of the nuclear power plant by the electric power of the plant to produce hydrogen and oxygen, and stores the hydrogen and oxygen in the means for respectively storing the hydrogen and oxygen. An electric power storage device configured to take out electric power again and transmit the electric power to the nuclear power plant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5061820A JPH06276701A (en) | 1993-03-22 | 1993-03-22 | Electric power storing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5061820A JPH06276701A (en) | 1993-03-22 | 1993-03-22 | Electric power storing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06276701A true JPH06276701A (en) | 1994-09-30 |
Family
ID=13182108
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5061820A Pending JPH06276701A (en) | 1993-03-22 | 1993-03-22 | Electric power storing device |
Country Status (1)
Country | Link |
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JP (1) | JPH06276701A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2823592A1 (en) * | 2001-04-13 | 2002-10-18 | Framatome Anp | Nuclear power station auxiliary component emergency power feed uses fuel cell fed with hydrogen and air or oxygen from nuclear plant |
EP1612297A2 (en) * | 2004-07-01 | 2006-01-04 | Westinghouse Electric Company LLC | Hydrogen production process |
WO2006105385A1 (en) * | 2005-03-31 | 2006-10-05 | Smith William F | Modular regenerative fuel cell system |
KR100715222B1 (en) * | 2005-10-31 | 2007-05-08 | 한국전력공사 | Energy storage system of nuclear power plant |
US8034219B2 (en) | 2005-12-21 | 2011-10-11 | General Electric Company | System and method for the production of hydrogen |
WO2022254969A1 (en) * | 2021-05-31 | 2022-12-08 | 株式会社日立製作所 | Nuclear power plant, and hydrogen production method for nuclear power plant |
WO2023013674A1 (en) * | 2021-08-04 | 2023-02-09 | 住友重機械工業株式会社 | Power-conditioning system, power-conditioning method, and power-conditioning program |
CN116505042A (en) * | 2023-06-30 | 2023-07-28 | 中石油深圳新能源研究院有限公司 | Hydrogen production device and fuel cell coupled hydrogen production power generation system |
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JPS63148840A (en) * | 1986-12-12 | 1988-06-21 | 三菱重工業株式会社 | Facility for converting, storing and utilizing electric energy |
JPH03208259A (en) * | 1990-01-10 | 1991-09-11 | Mitsubishi Heavy Ind Ltd | Solid electrolyte fuel cell system |
JPH0541236A (en) * | 1991-08-07 | 1993-02-19 | Mitsubishi Heavy Ind Ltd | Electric power storage |
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JPS63148840A (en) * | 1986-12-12 | 1988-06-21 | 三菱重工業株式会社 | Facility for converting, storing and utilizing electric energy |
JPH03208259A (en) * | 1990-01-10 | 1991-09-11 | Mitsubishi Heavy Ind Ltd | Solid electrolyte fuel cell system |
JPH0541236A (en) * | 1991-08-07 | 1993-02-19 | Mitsubishi Heavy Ind Ltd | Electric power storage |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002084670A1 (en) * | 2001-04-13 | 2002-10-24 | Framatome Anp | Device for emergency power supply to auxiliary components of a nuclear power plant and use method |
FR2823592A1 (en) * | 2001-04-13 | 2002-10-18 | Framatome Anp | Nuclear power station auxiliary component emergency power feed uses fuel cell fed with hydrogen and air or oxygen from nuclear plant |
EP1612297A2 (en) * | 2004-07-01 | 2006-01-04 | Westinghouse Electric Company LLC | Hydrogen production process |
JP2006021992A (en) * | 2004-07-01 | 2006-01-26 | Westinghouse Electric Co Llc | Separate hydrogen production process |
EP1612297A3 (en) * | 2004-07-01 | 2006-12-13 | Westinghouse Electric Company LLC | Hydrogen production process |
US8003268B2 (en) | 2005-03-31 | 2011-08-23 | Smith William F | Modular regenerative fuel cell system |
WO2006105385A1 (en) * | 2005-03-31 | 2006-10-05 | Smith William F | Modular regenerative fuel cell system |
KR100715222B1 (en) * | 2005-10-31 | 2007-05-08 | 한국전력공사 | Energy storage system of nuclear power plant |
US8034219B2 (en) | 2005-12-21 | 2011-10-11 | General Electric Company | System and method for the production of hydrogen |
WO2022254969A1 (en) * | 2021-05-31 | 2022-12-08 | 株式会社日立製作所 | Nuclear power plant, and hydrogen production method for nuclear power plant |
WO2023013674A1 (en) * | 2021-08-04 | 2023-02-09 | 住友重機械工業株式会社 | Power-conditioning system, power-conditioning method, and power-conditioning program |
CN116505042A (en) * | 2023-06-30 | 2023-07-28 | 中石油深圳新能源研究院有限公司 | Hydrogen production device and fuel cell coupled hydrogen production power generation system |
CN116505042B (en) * | 2023-06-30 | 2024-01-26 | 中石油深圳新能源研究院有限公司 | Hydrogen production device and fuel cell coupled hydrogen production power generation system |
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