JPS6261276A - Energy supply device - Google Patents

Energy supply device

Info

Publication number
JPS6261276A
JPS6261276A JP60200495A JP20049585A JPS6261276A JP S6261276 A JPS6261276 A JP S6261276A JP 60200495 A JP60200495 A JP 60200495A JP 20049585 A JP20049585 A JP 20049585A JP S6261276 A JPS6261276 A JP S6261276A
Authority
JP
Japan
Prior art keywords
heat
pair
electrolyte layer
fuel cell
supply device
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
JP60200495A
Other languages
Japanese (ja)
Inventor
Kiyoshi Inoue
潔 井上
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.)
Inoue Japax Research Inc
Original Assignee
Inoue Japax Research Inc
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 Inoue Japax Research Inc filed Critical Inoue Japax Research Inc
Priority to JP60200495A priority Critical patent/JPS6261276A/en
Publication of JPS6261276A publication Critical patent/JPS6261276A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04014Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04029Heat exchange using liquids
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04701Temperature
    • 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
    • Y02E60/50Fuel 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

PURPOSE:To make it possible to efficiently utilize heat energy generated when chemical energy of a fuel is converted into electric energy by combining together a heat accumulator, a fuel cell device and a heat supply device. CONSTITUTION:While a thermal medium 12 such as water inside a heat accumulator heated by heat energy generated when chemical energy is converted into electric energy, not to speak of electromotive force obtained by a fuel cell 3 is taken out as vapor or hot water, the medium 12 inside the heat accumulator 2 is heated by operating a heater device 19 for storing surplus power as heat energy when required power is sufficed by a part of the power generated by the fuel cell 3, or when the power generated by the fuel cell 3 is not required. Further, when the power exceeding the maximum limit which can be generated by the fuel cell 3 is required, a thermal medium such as methane or ammonium enclosed inside a heater 19 is compress-circulated by a compressor 26 to operate a generator 24 for supplementing power.

Description

【発明の詳細な説明】 3、発明のiY−イ■な説明 〔産業−1−の利用分野〕 本発明は工;6ルギ供給装置、特に、燃料電池を利用し
たエネルギ供給装置に関する。
Detailed Description of the Invention 3. Brief Description of the Invention [Field of Application in Industry-1] The present invention relates to an energy supply device, particularly to an energy supply device using a fuel cell.

〔従来の技i、l+〕[Conventional techniques i, l+]

燃料電池は燃料の化学的エネルギを直接電気的エネルギ
に変換する化学反応装置であり、効率が約80%に達す
る可能性がある。また、燃料電池は芹通の−・次電池及
び−次電池と異なり、燃料と酸化剤がO(給され、hば
連続して電力を取り出すことができる連続補給形の電t
+hである。そして、電池の働く温度によって、常温燃
料電池(常温〜300℃) 、il’l+l晶燃訓電池
(燃料0℃[シl )に分けられ、また、使用す?)燃
料にも気体、液体、固体の別がある。
Fuel cells are chemical reaction devices that convert the chemical energy of fuel directly into electrical energy, and can have efficiencies of approximately 80%. In addition, fuel cells differ from Serito's secondary batteries and secondary batteries in that they are a continuously replenishable type of electricity that can be supplied with fuel and oxidizer (O), and can continuously extract electricity for hours.
+h. Depending on the operating temperature of the battery, it can be divided into room temperature fuel cells (room temperature to 300℃) and IL'I+L crystal fuel cells (fuel at 0℃). ) There are also different types of fuel: gas, liquid, and solid.

燃料電池としてム4[、水素 酸素燃料電池、ヒ1ラジ
ン燃料電池、メタノール燃料電池等がイ(−人的なもの
としてあげら引′するが、このうら、水+ 酸素燃料電
池は燃料として水素を使用し、酸化剤として酸素を使用
するものであり、 II2  +  (%) 02 −11p (’1の反
1、トユの自由エネルギに相当する約1Vの起電力が得
られるものである。
As a fuel cell, water+oxygen fuel cells, hydrogen-oxygen fuel cells, hirazine fuel cells, methanol fuel cells, etc. are used as fuel cells. , and oxygen is used as the oxidizing agent, and an electromotive force of about 1 V, which corresponds to the free energy of II2 + (%) 02 -11p ('1 to 1), can be obtained.

燃料電池は化学的エネルギの燃焼反応を電気化学的乙こ
行なわ・υ直接電気的エネルギεご変換する際にJT+
温の熱を発生ずるが、従来の燃料電池ζこ於てはこの熱
エネルギζ;i”i”<利用さ41ず、総て燃料電池の
夕1部へ発敗さ才1てしま・)ものであった。而して、
この熱エネルギもfj仙C,1利用するごとかできれば
極めてジノ率の良いエフ、ルギ+J(給装置となるので
あるが、このような装置は未だ開発され−こいない。
Fuel cells carry out the combustion reaction of chemical energy in an electrochemical manner.
However, in conventional fuel cells, this thermal energy is not utilized, and is completely lost to the fuel cell. It was something. Then,
If this thermal energy could also be utilized, it would become a supply device with extremely high efficiency, but such a device has not yet been developed.

〔発明が解決しよら^すく、問題点〕[Problems that the invention will solve]

本発明は叙」二の観点に立つ−(なさ4′1だものであ
って、その目的とずイ〕とこメ)は、燃料電池に燃料が
供給され、1−記燃料の化学的エネルギが電気的エネル
ギに変換することによってiυられる起電力は勿論のこ
と、十記燃Iiの化学的コ、ネルギが電気的エネルギに
変換する際に発生する熱エネルギもイ1々I+に利用し
く17るエネルギ供給装置を1に供すjllcとにあW
) 6 〔問題点を解決するだめの手段〕 而して、l−記の目的は、蓄ill器に電池室筐体を設
け、その電池室筐体内に燃料電池装置を設けると共に、
十記電池室筺体夕■には)δ慴の熱媒を導入し、その熱
媒のイ1する熱エネルギをり1部に取り出し得る熱供給
装置を設けて成るエネルギ供給装置によって達成される
The present invention is based on the following points (4'1 and 1), and its purpose is not based on the following points: When fuel is supplied to a fuel cell, the chemical energy of the fuel is Not only the electromotive force generated by converting it into electrical energy, but also the thermal energy generated when the chemical energy is converted into electrical energy. Provide energy supply equipment to Jllc and NiaW
) 6 [Means to solve the problem] Therefore, the purpose of item 1 is to provide a battery chamber casing in an illumination device, install a fuel cell device inside the battery chamber casing, and
This is achieved by an energy supply device which introduces a heating medium of δ into the battery compartment housing and is provided with a heat supply device capable of extracting the thermal energy of the heating medium to a portion.

また、本発明装置には負(610′)状況に応じ、熱・
動力変換装置ヌはその逆変換装置の?iilれか一方、
又は双方が設置1られる。
In addition, the device of the present invention has the ability to generate heat and
Is the power conversion device nu its inverse conversion device? iil on the other hand,
Or both can be installed.

〔作  用〕[For production]

一1=記の如き構成であると、燃料電池によって(すら
れた起電力は勿論のこと、化学1ネルギが電気エネルギ
に変換ず乙ド祭に41する熱エネルギも自効に利用でき
るよ・)になる。即I式上記熱エネル丁によって加熱さ
れた蓄熱器内の水等の熱媒を装置及び熱湯とし一ζ取り
出すことができ、更にtit、必要とする電力が燃料電
池が発4I−シた電力の・)らの一部でよいとき、又は
燃料電池から発生1−7た電力が必要でないときには、
残りの電力又番よ発生した電力によって電熱装置をωj
作さセー(蓄熱器内の媒体を加熱し、1゛た、燃料電池
で発4することができる最大限度以上の電力が必要なと
きには、加熱器内に封入された熱媒を発電装置に導き、
発電を行なわせるので、総合的に極めて効率の高いエネ
ルギ供給装置を提供することができる。
11 = With the configuration shown below, the fuel cell can effectively utilize not only the generated electromotive force, but also the thermal energy that is converted from chemical energy into electrical energy. )become. Therefore, the heat medium such as water in the heat storage device heated by the above-mentioned thermal energy unit can be taken out as hot water, and the required electric power can be extracted from the electric power generated by the fuel cell.・), or when the electricity generated from the fuel cell is not required,
The remaining electric power is used to power the electric heating device ωj.
The heating medium in the heat storage device is heated, and when more power than the maximum that can be generated by the fuel cell is required, the heating medium sealed in the heater is guided to the power generation device. ,
Since electricity is generated, it is possible to provide an energy supply device that is extremely efficient overall.

〔実 施 例〕〔Example〕

以下、図面を参照し1)\本発明の、iY−細を具体的
に説明する。
Hereinafter, the iY-thin of the present invention will be specifically explained with reference to the drawings.

図面は、本発明にかかるエネルギ供給装置の一実施例を
示す説明図である。
The drawing is an explanatory diagram showing one embodiment of the energy supply device according to the present invention.

図中、1はエネルギ供給装置、2は蓄熱器、3ば燃料電
池、4は電池室筐体、5及び6は多孔質電極、5.】2
シひ6 a Let端了、’N、l:@解質層、70シ
よ一1記電解質屓7から反I2、生成物を排出する装置
、8は朱?彎)ガスi1(給装置、9 L:i: l′
記燃i“lガスIlj給装置8から多孔質電極5へ供給
される水素の供給量を制御゛4′¥)′「仙イ「、10
 L;に酸化剤ガス供給装置、11は上記酸化剤ガス供
給装置】0から多孔質電極〔jへ供給さl+る酸素の供
給h1を制御する手動弁、12ム1水等の熱媒、13は
圧力εII、I整光、14は蒸気取出「1.15は安全
弁、lEiば」−記蓄4ハ器2内のj用温となった熱媒
12を取り出すための手動弁、17番才上記熱媒12を
11v。
In the figure, 1 is an energy supply device, 2 is a heat storage device, 3 is a fuel cell, 4 is a battery chamber housing, 5 and 6 are porous electrodes, 5. ]2
Shihi 6 a Let end, 'N, l: @ Solute layer, 70 Shiyo 11 Electrolyte layer 7 to anti-I2, device for discharging products, 8 is vermilion? ) Gas i1 (supply device, 9 L:i: l'
Control the amount of hydrogen supplied from the gas Ilj supply device 8 to the porous electrode 5.
L: an oxidant gas supply device; 11 is the above-mentioned oxidant gas supply device; 1 is a manual valve for controlling the supply of oxygen from 0 to the porous electrode [j; 12 is a heating medium such as water; 13 is 14 is the pressure εII, I light adjustment, 14 is the steam extraction "1.15 is the safety valve, 1Ei" - memory 4C is the manual valve for taking out the heating medium 12 which has reached the temperature J in the vessel 2, No. 17 The heating medium 12 is 11v.

り出す熱媒取出l]、18は上記蓄熱R:(2内の熱媒
12の星を富時一定に保つレヘル調整器、+8aは給水
管、18 ))はレヘル咽整器、18cは個節部、19
ば電熱装置、5)0はスイッチング素子、21ば渭熱器
2内に収容された加Pハ器、2211膨張弁、23はガ
スタービン、24は一1記ガスタービン23に接続し7
に発電機、25は冷却器、26はコンプレッサ、27は
il+l−め弁、28 L;lダクト、29は整流器、
30は圧力検出器、31は上記圧力検出器30の出力値
及び予め定められたプログラムに基づいて、l−記スイ
ツチング素了20及び−1ンブレ、す′2(iを制御し
て、電力負荷と熱0萄との比ドに応(−7で十記電PI
!装置19に供給する電力及び発電機24から整流器2
9を介して出力される電力量を制御する制御装置である
18 is the above-mentioned heat storage R: (Rehel regulator that keeps the star of the heat medium 12 in 2 constant when it is rich, +8a is the water supply pipe, 18)) is the Rehel pharyngeal regulator, 18c is the individual Node, 19
5) 0 is a switching element; 21 is a heater housed in the steam heater 2; 2211 is an expansion valve; 23 is a gas turbine; 24 is connected to the gas turbine 23;
25 is a cooler, 26 is a compressor, 27 is an il+l-me valve, 28 is a duct, 29 is a rectifier,
Reference numeral 30 denotes a pressure detector, and 31 indicates a switching operation based on the output value of the pressure detector 30 and a predetermined program. According to the ratio of heat 0 and
! Electric power supplied to the device 19 and from the generator 24 to the rectifier 2
This is a control device that controls the amount of electric power outputted via the power source 9.

而して、蓄熱器2内には電池室筺体4が収容されると共
に、上記電池室筐体4の外周面が常時水等の熱媒12に
よって覆十月・1ように、−1記熱媒120)■がレヘ
ル調整器184こよって一定量に保たれるように制御が
行なわl11イ)。
A battery chamber casing 4 is housed in the heat storage device 2, and the outer circumferential surface of the battery chamber casing 4 is constantly covered with a heat medium 12 such as water. Control is performed so that the medium 120) is maintained at a constant level by the level regulator 184.

」1記電池室筺体4内には電解質層7と、上記電解質闇
7を介して相り11↑11する一対の多孔質電極5及び
6が収容され、1−記一対の多T1.質電極5及び6の
一方の電極5には、燃料ガスを供給する燃Y)ガス供給
装置8から−F動弁9を介U7て水素が供給され、他の
一1jの電極6に(1、酸化ガスを供給」゛5酸化剤ガ
ス供給装置10から手動弁11を介して酸素が供給され
る。
1. Inside the battery chamber housing 4, an electrolyte layer 7 and a pair of porous electrodes 5 and 6 facing each other via the electrolyte layer 7 are accommodated, and 1-a pair of multi-T1. One of the electrodes 5 and 6 is supplied with hydrogen from a fuel gas supply device 8 that supplies fuel gas via a -F valve 9, and the other electrode 6 is supplied with hydrogen (1). , ``Supplying oxidizing gas'' (5) Oxygen is supplied from the oxidizing gas supply device 10 via the manual valve 11 .

而して、−1,記燃料ガス供給装置8から燃料として水
素が供給され、他方の酸化剤ガス供給装置10から酸化
剤として酸素が供給されると、それぞれ供給された水素
及び酸素は多孔質電極5またびGを介して電量!質層7
で11,4(騒)02 ・1120のfi I、i、、
力(行なわれ、1!出了5a、6aには自由コ−不ルギ
に相当すと)起電力が発生する。
-1, When hydrogen is supplied as a fuel from the fuel gas supply device 8 and oxygen is supplied as an oxidant from the other oxidant gas supply device 10, the supplied hydrogen and oxygen are porous. Amount of electricity via electrode 5 and G! quality layer 7
11,4 (sound) 02 ・1120 fi I, i,,
An electromotive force is generated.

燃料型/lb 3 L、を上記112 ト(!A)02
−H20の反応が起り、化学的エネルギが電気的エネル
ギに変換する際に熱を発生するが、この発生した熱は電
池室筺体4の外周壁から蓄熱器2内に供給された熱媒1
2に吸収され、熱エネルギとして貯蔵される。
Fuel type/lb 3 L, above 112 t(!A) 02
-H20 reaction occurs and heat is generated when chemical energy is converted into electrical energy.
2 and stored as thermal energy.

また、上記反応により電解質層7には水が生成するが、
この水は反応物を排出1′ろ装置7aを介し−Cり1部
へ排出される。
In addition, water is generated in the electrolyte layer 7 due to the above reaction, but
This water is discharged to -C 1 part through the reactant discharge 1' filtration device 7a.

而しζ、加熱されノコp;H媒12ば手動弁16を開く
ことによって熱媒取出「117から取り11目′ことが
でき、また、光電(:(圧力調整弁13を開くことに、
L−7て族気取出「114から取り出すことができる。
Then, by opening the manual valve 16, the heating medium 12 can be taken out from 117, and the photovoltaic (:
L-7's family spirit extraction "Can be extracted from 114.

燃ネこi電池3によってijられる電気量は、燃料ガス
供給装置8及び酸化剤ガス供給装置10から多孔質電極
5及び6へ供給される水素及び酸素の量に比例するので
、電気の最大使用量に応してY−UI+弁9及び11を
1渠作して十記多f14質電極5及び6−1供給する水
素及び酸素の量を適宜に設定()でおく。
Since the amount of electricity generated by the fuel-powered I battery 3 is proportional to the amount of hydrogen and oxygen supplied from the fuel gas supply device 8 and the oxidant gas supply device 10 to the porous electrodes 5 and 6, the maximum usage of electricity is One Y-UI+valve 9 and 11 is created according to the amount, and the amount of hydrogen and oxygen to be supplied to the multi-F14 electrodes 5 and 6-1 is set as appropriate ().

制御装置31は圧力検出器30の出力、電力負荷、その
他の情報に基づき、Hlつ予め定められたプログラムに
従って、スイッチング素子20及びコンブl/フサ26
の動作を制御して、電力負荷と熱負荷との比率に応して
電熱装置19に供給する電力量及び発電機24から整流
器29を介して出力される電力量を制御する。
The control device 31 controls the switching element 20 and the combination/fusa 26 according to a predetermined program based on the output of the pressure detector 30, the power load, and other information.
The amount of power supplied to the electric heating device 19 and the amount of power output from the generator 24 via the rectifier 29 are controlled in accordance with the ratio of the power load and the heat load.

即ち、必要とする電力が燃料電池3が発り1した電力の
うちの一部でよいとき、又は燃料電池3によって発生さ
れた電力が必要でないときには、制御装置31はスイッ
チング素子20を動作させ、使用した残りの電力又は発
生した電力の総てが電熱装置19に供給されるように切
換えられ、上記電熱装置19によって熱媒122’l<
 )Jn !:;れされる。
That is, when the required power is only a portion of the power generated by the fuel cell 3, or when the power generated by the fuel cell 3 is not required, the control device 31 operates the switching element 20, The remaining power used or all of the generated power is switched to be supplied to the electric heating device 19, and the heating medium 122'l<
)Jn! :; It will be written down.

また、燃料電池3で発生し得る最大限度以上の電力が必
要なときには、コンプレッサ26をm rib して、
ダクト2B内に封入された液状のメタン又はアン壬二了
等のチ;ハ媒を汀線iA’i環さ廿る。上記メタン又は
アンモニア等の熱媒口加熱器21を通過することによっ
−(加熱され、1rli温高圧と成った(多、膨張弁2
2を通過することによっ゛ζガス化され、」、記ガスは
ガスタービン23を回り1し、冷却器25により冷却さ
れ、ITfびコンプレy g−26により圧縮され加熱
器21に送られる。
Also, when more power than the maximum that can be generated by the fuel cell 3 is required, the compressor 26 is m rib ,
A medium such as liquid methane or aluminum sealed in the duct 2B is passed through the shoreline iA'i. By passing through the heating medium 21 such as methane or ammonia, it is heated to a temperature of 1rli and high pressure.
The gas is gasified by passing through the gas turbine 23, cooled by the cooler 25, compressed by the ITf and compressor 26, and sent to the heater 21.

而して、上記ガスタービン23 +;I発電I幾24に
接続しているので、ガスタービン23の回動に仕って発
電機24が回動U7電力を発/1″する。
Since the gas turbine 23 is connected to the gas turbine 23+;I power generator 24, the generator 24 generates rotational power U7/1'' in accordance with the rotation of the gas turbine 23.

而して、上記発電機24が発生した電力は整jA乙器2
9によって整流された後、一対の多孔質電極5及び6の
導電線を介j〕ζ、燃料電池3から発生した電力にff
l[HL、た形で端子5a、6dから出力される。
Therefore, the electric power generated by the generator 24 is sent to the regulator 2.
After being rectified by 9, the electric power generated from the fuel cell 3 is passed through the conductive wires of the pair of porous electrodes 5 and 6 to the electric power generated from the fuel cell 3.
l[HL, is output from terminals 5a and 6d in the form.

ガスタービン23を回動したガスは冷却器25で冷却さ
れ、低圧にされて再び元の液状の状態に戻され、以下同
様なサイクルが繰り返される。
The gas that has rotated through the gas turbine 23 is cooled by the cooler 25, reduced to a low pressure, and returned to its original liquid state, and the same cycle is repeated thereafter.

〔発明の効果〕〔Effect of the invention〕

本発明は叙−Lの如く構成されるから、本発明によ?)
ときには、燃料電池3によって得られた起電力は勿論の
こと、化学エネルギか電気J−ネルギに変換する際乙こ
イ1゛する熱エネルギに、1、っ゛(加熱された蓄熱器
内の水等の熱媒12を茎気及び熱湯とし−(取り出すこ
とができると共に、必要とする重りが燃料電池3から発
生した電力の・)りの一部でよいとき、又は燃料電池3
によって発生された電力が乙ヒ・要でないときには、残
りの電力又は発1(t、た電力によって電熱装置19を
動作さ−せ゛ζ#熱器2内の媒体12を加熱し7、余剰
電力を熱エネルギと1.て貯蔵し、また、燃料電池3で
発電し得る最大限度以上の電力が必要なときには、加熱
器19内に封入されたメタン又はアンモニア等の熱媒を
コンプレッサ26でYF縮循環さ・Uて発電機24を動
作さ一1′Fli力を補うので、極めて々カ率の高い:
J−ネルギ供給装置が提供できるものである。
Since the present invention is constructed as shown in the following paragraph, is this invention based on the present invention? )
Sometimes, not only the electromotive force obtained by the fuel cell 3, but also the thermal energy that is generated when converting into chemical energy or electrical energy, When the heat medium 12 such as air and boiling water is used as the heat medium 12 (which can be taken out and the required weight is only a part of the electric power generated from the fuel cell 3), or when the fuel cell 3
When the generated electric power is not needed, the remaining electric power or generated electric power is used to operate the electric heating device 19. 1. Thermal energy is stored, and when more power than the maximum power that can be generated by the fuel cell 3 is required, a heat medium such as methane or ammonia sealed in the heater 19 is YF condensed and circulated by the compressor 26. Since the generator 24 is operated to supplement the power, the power generation rate is extremely high:
This is what the J-energy supply device can provide.

そし′ζ、このようなエネルギ供給装置は、家庭や地域
の装置として設置して、電力及び冷暖房の夕(熱湯供給
装置として使用し得るものである。
Such an energy supply device can be installed as a home or community device and used as a power supply and hot water supply device.

なお、本発明の構成は叙−1=の実施例に限定されるも
のでない。叩も、例えば、本実施例に於−(1↑水素と
酸素を利用する燃料電池としたが、」−記燃″F−1電
池に限定されず、ヒ1−ラジン燃料電池、メタノール燃
1′1電池及びその他公知の燃料電池が、必要に応じ触
媒等を(【l加して利用できるものであイ)。
It should be noted that the configuration of the present invention is not limited to the embodiment shown in -1=. For example, in this example, a fuel cell using hydrogen and oxygen was used, but it is not limited to the F-1 battery; '1 Batteries and other known fuel cells can be used in addition to catalysts, etc., if necessary.

また、MI熱器2内に供給する熱媒12を水として説明
したが、水に限定されず他の公知の熱媒を広く利用し7
得るものである。更にまた、燃料ガス供給装置8及び酸
化剤ガス供給装置10から多孔質電極5及び6へ供給さ
れる水素及び酸素の量を丁動弁9及び10によって制御
するよ・)にしたが、制御装置31によって供給量が自
動制御されるようにしてもよい。その他、lj熱器2及
び電池室筺体4の形状、熱・電力の変換装置及びその逆
変換装置の構成等は本発明の[1的の範囲内で自由に設
計変更できるものであって、本発明はこれらの総てを包
摂するものである。
Furthermore, although water has been described as the heating medium 12 supplied into the MI heating device 2, it is not limited to water, and other known heating mediums may be widely used.
It's something you get. Furthermore, the amounts of hydrogen and oxygen supplied from the fuel gas supply device 8 and the oxidant gas supply device 10 to the porous electrodes 5 and 6 are controlled by the hinged valves 9 and 10. 31, the supply amount may be automatically controlled. In addition, the shapes of the lj heater 2 and the battery chamber housing 4, the configuration of the heat/power converter and its inverse converter, etc. can be freely changed in design within the scope of [1] of the present invention. The invention encompasses all of these.

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

図面は、本発明にかかるエネルギ供給装置の一実施例を
示す説明図である。 1      −−−エネルギ供給装置2−−−−−−
   −−−−蓄熱2:;3  −    燃料電池 4−−    −− 電池室筐体 5.6−     多孔質電極 5a、6a  −端子 7 −−−  − 電解質 7a−−−−−−反応生成物を排出する装置8−−−−
−−−−−− 燃料ガス供給装置9、】1.16−−−
− 丁動弁 10−  −  酸化剤ガス供給装置 12−−−−−  −媒体 18−−−一−−−レヘル調整器 19         電熱装置 20−−−−−−−−−   スイッチング素子2+ 
−−−−−−加熱器 22−−−  −−−−  膨張弁 23−−−−−ガスタービン 24−−−−−−−−− −発電)幾 25−−−−−−− −  冷却器 26−−−− −−一−−−コンプレッサ1!8   
       ダク1 29            N tAi ’!A31
         制御装置 特許出願人 株式会社 丼」ジャパックス研究所代理人
(7524)最−1−正大r+++]−″−糸売  ネ
市  1に  テ千昭和に0年11月151 特許庁1毘官 宇 賀 j負 部 殿 1、 串+Qの表示 昭和60年特許願第200495
号2、 発明の名称 エネルギ供給装置 3.1市正をする打 事(Ilとの関係 特許出願人 住所 神奈川県横γ!デ市緑区に律田町字市正5289
番地名称 (048)株j(会?I  井上ジャパック
ス研究所代表打 井 十  潔 4、代理人◎107  Tu 583−0306住 所
 東京都港区赤坂1丁目8番1す6、 補正の対象 8、補正の内容 1)明細書の特許請求の範囲の範囲の欄の記載を別紙の
ように補iLする。 2)明細書第13頁第12行目から間第16行l−1迄
の記載を下記のように補正する。 記 もよい。また、電池室筺体4の構成も実施例のものに限
定されず、例えば、電池室筺体4にその内部を貫通して
外方に1fflじる熱媒流通路を形成することも推奨さ
れる。その他、蓄熱器2及び上記電池室筺体4の形状、
熱、電力の変換装置及びその逆変換装置の構成等は、本
発明の目的の範囲内で自由に設計変更できるものであっ
て、本発明はこれらの総てを包摂するものである。 特;!’F afg求の範囲 1)蓄熱器に電池室筐体を設け、その電池室筐体内には
電解質)響と、その電解質層を介U2て相対向する一対
の多孔質電極と、上記−り1の多孔質電極の一方に燃料
を供給する装置と、他の一方に酸化剤を供給する装置と
、電解質層から民応律成物をIJ)71目゛る装置と、
」二記−タ・jの多孔質電極から電流を耳■り出す導電
線とから成る燃料電池装置を設けると共に、」記電池室
筺体外には適量の熱媒を導入し、その熱媒の有する熱エ
ネルギを夕[部に耳■り出しくびる熱供給装置を設&J
て成るエネルギ供給装置。 a)Wr熱器に電池室筐体を設け、その電池室筐体内に
は電解質層と、その電解質層を介して相対向する一対の
多孔質電極と、上記一対の多孔質電極の電力に燃料を供
給する装置と、他の電力に酸化剤を供給する装置と、電
解質層から反応生成物をJ’ll出する装置と、上記一
対の多孔質電極から電流を取り出す導電線とから成る燃
料電池装置を設けると共に、1.記電池室筐体外には適
量の熱媒を導入し、その熱媒の有する熱エネルギを夕1
部に取り出しiUる熱供給装置と、−[−記一対の導電
線に接続され、−1二記熱媒体を加熱する電熱装置と、
電力負荷と熱負萄との比率に応じて上記電熱装置に供給
する電力を制御する装置とから成るエネルギ供給装置。 装置。 旬ξΩ−舌−ネノ1−±〕八給装置、−−−5)蓄熱器
に電池室筐体を設け、その電池室筐体内には電解質層と
、その電解質層を介して相対向する一対の多孔質電極と
、−に記一対の多孔質電極の一方に燃料を供給する装置
と、他の一方に酸化剤を供給する装置と、電解質層から
反応生成物を排11目”る装置と、」二記一対の多孔質
電極から電流を取り出す導電線とから成る燃料電池装置
を設けると共に、−1゜記電池室筺体夕1にはi81の
熱媒を導入し、その熱媒の有する熱エネルギを夕1部に
取り出し得る熱供給装置と、−1記蓄熱器内に設けられ
1、記#p1器内の熱媒とは別界の熱媒か封入された加
熱器と、上記加熱器によ−、て加す1された熱媒の熱エ
ネルギを電気エネルギ乙こ変換する変換器と、熱負荷と
電力負荷との比率に応じて上記変換器の動作を制御する
制御装置とから成るエネルギ供給装置。 6片−21−耐電坤−室筺体がぞの内…i土貝鴻−り外
力軒坤じる熱媒流5m路を有する特許請求の範囲第5項
記載のエネルギ供給装置。
The drawing is an explanatory diagram showing one embodiment of the energy supply device according to the present invention. 1 ----Energy supply device 2------
--- Heat storage 2: ; 3 -- Fuel cell 4 --- -- Battery chamber housing 5.6 -- Porous electrodes 5a, 6a -- Terminal 7 --- -- Electrolyte 7 a --- Reaction product Discharging device 8
-------- Fuel gas supply device 9, ]1.16---
- Pivot valve 10 - Oxidizing gas supply device 12 - Medium 18 - Level regulator 19 Electric heating device 20 Switching element 2+
------- Heater 22 ---- - Expansion valve 23 - Gas turbine 24 - Power generation) 25 - Cooling Container 26------1----Compressor 1!8
Dak1 29 N tAi'! A31
Control device patent applicant Don Co., Ltd. Japax Research Institute Agent (7524) Sai-1-Shodai r+++]-''-Itouri Neichi 1 Te Chi Showa 0 November 151 Patent Office 1 Hiroki Uga j Negative part 1, Display of skewer + Q 1985 Patent Application No. 200495
No. 2. Name of the invention Energy supply device 3.1 Relationship with the City Council (Relationship with Il) Patent Applicant Address 5289 Ichimasho, Ritsuta-cho, Midori-ku, Yokogamma!de City, Kanagawa Prefecture
Address Name (048) Stock J (Kai? I) Inoue Japax Research Institute Representative Kiyoshi I 4, Agent ◎107 Tu 583-0306 Address 1-8-16 Akasaka, Minato-ku, Tokyo, subject to amendment 8 , Contents of amendment 1) The statement in the scope of claims column of the specification is supplemented as shown in the attached sheet. 2) The description from page 13, line 12 to line 16, line 1-1 of page 13 of the specification is amended as follows. The writing is also good. Further, the structure of the battery chamber housing 4 is not limited to that of the embodiment, and for example, it is recommended to form a heat medium flow path in the battery chamber housing 4 that penetrates the inside thereof and extends outward by 1 ffl. In addition, the shape of the heat storage device 2 and the battery chamber housing 4,
The configuration of the heat and power conversion device and its inverse conversion device can be freely modified within the scope of the purpose of the present invention, and the present invention encompasses all of these. Special;! Scope of requirements for F afg 1) A battery chamber casing is provided in the heat storage device, and within the battery chamber casing there is an electrolyte, a pair of porous electrodes facing each other with the electrolyte layer U2 in between, and the above-mentioned A device for supplying fuel to one of the porous electrodes No. 1, a device for supplying an oxidizing agent to the other porous electrode, and a device for discharging a folk composition from the electrolyte layer.
In addition to providing a fuel cell device consisting of a conductive wire that draws current from a porous electrode in the second section, an appropriate amount of heat medium is introduced outside the battery chamber housing, and the heat medium is A heat supply device is installed that protrudes the heat energy in the evening.
An energy supply device consisting of: a) A battery chamber casing is provided in the Wr heater, and within the battery chamber casing there is an electrolyte layer, a pair of porous electrodes facing each other through the electrolyte layer, and a fuel for the power of the pair of porous electrodes. a device for supplying an oxidizing agent to other electric power, a device for extracting reaction products from an electrolyte layer, and a conductive wire for extracting current from the pair of porous electrodes. In addition to providing the device, 1. An appropriate amount of heat medium is introduced outside the battery compartment housing, and the thermal energy of the heat medium is
an electric heating device connected to the pair of conductive wires and heating the heat medium;
An energy supply device comprising: a device for controlling electric power supplied to the electric heating device according to a ratio between an electric power load and a heat load. Device. ShunξΩ−tongue−neno1−±]8 supply device, ---5) A battery chamber housing is provided in the heat storage device, and within the battery chamber housing there is an electrolyte layer and a pair of electrodes facing each other with the electrolyte layer interposed therebetween. a porous electrode, a device for supplying fuel to one of the pair of porous electrodes, a device for supplying an oxidizing agent to the other one, and a device for removing reaction products from the electrolyte layer. A fuel cell device consisting of a conductive wire for extracting current from a pair of porous electrodes is provided, and a heat medium of i81 is introduced into the battery compartment housing 1, and the heat possessed by the heat medium is a heat supply device capable of extracting energy in the evening, a heater provided in the heat storage device 1 and sealed with a heating medium different from the heat medium in the device 1; It consists of a converter that converts the thermal energy of the heating medium added by the heating medium into electrical energy, and a control device that controls the operation of the converter according to the ratio of the thermal load to the electric power load. Energy supply device. 6. The energy supply device according to claim 5, having a heat medium flow path of 5 m within which the casing is exposed to external force.

Claims (1)

【特許請求の範囲】 1)蓄熱器に電池室筐体を設け、その電池室筐体内には
電解質層と、その電解質層を介して相対向する一対の多
孔質電極と、上記一対の多孔質電極の一方に燃料を供給
する装置と、他の一方に酸化剤を供給する装置と、電解
質層から反応生成物を排出する装置と、上記一対の多孔
質電極から電流を取り出す導電線とから成る燃料電池装
置を設けると共に、上記電池室筐体外には適量の熱媒を
導入し、その熱媒の有する熱エネルギを外部に取り出し
得る熱供給装置を設けて成るエネルギ供給装置。 2)蓄熱器に電池室筐体を設け、その電池室筐体内には
電解質層と、その電解質層を介して相対向する一対の多
孔質電極と、上記一対の多孔質電極の一方に燃料を供給
する装置と、他の一方に酸化剤を供給する装置と、電解
質層から反応生成物を排出する装置と、上記一対の多孔
質電極から電流を取り出す導電線とから成る燃料電池装
置を設けると共に、上記電池室筐体外には適量の熱媒を
導入し、その熱媒の有する熱エネルギを外部に取り出し
得る熱供給装置と、上記一対の導電線に接続され、上記
熱媒体を加熱する電熱装置と、電力負荷と熱負荷との比
率に応じて上記電熱装置に供給する電力を制御する装置
とから成るエネルギ供給装置。 3)蓄熱器に電池室筐体を設け、その電池室筐体内には
電解質層と、その電解質層を介して相対向する一対の多
孔質電極と、上記一対の多孔質電極の一方に燃料を供給
する装置と、他の一方に酸化剤を供給する装置と、電解
質層から反応生成物を排出する装置と、上記一対の多孔
質電極から電流を取り出す導電線とから成る燃料電池装
置を設けると共に、上記電池室筐体外には適量の熱媒を
導入し、その熱媒の有する熱エネルギを外部に取り出し
得る熱供給装置と、上記蓄熱器内に設けられ上記蓄熱器
内の熱媒とは別異の熱媒が封入された加熱器と、上記加
熱器によって加熱された熱媒の熱エネルギを電気エネル
ギに変換する変換器と、熱負荷と電力負荷との比率に応
じて上記変換器の動作を制御する制御装置とから成るエ
ネルギ供給装置。
[Scope of Claims] 1) A battery chamber housing is provided in the heat storage device, and within the battery chamber housing there is an electrolyte layer, a pair of porous electrodes facing each other with the electrolyte layer interposed therebetween, and the above-mentioned pair of porous electrodes. Consisting of a device for supplying fuel to one of the electrodes, a device for supplying an oxidizing agent to the other, a device for discharging reaction products from the electrolyte layer, and a conductive wire for extracting current from the pair of porous electrodes. An energy supply device comprising a fuel cell device and a heat supply device capable of introducing an appropriate amount of heat medium outside the battery chamber housing and extracting thermal energy of the heat medium to the outside. 2) A battery chamber casing is provided in the heat storage device, and within the battery chamber casing there is an electrolyte layer, a pair of porous electrodes facing each other through the electrolyte layer, and fuel is supplied to one of the pair of porous electrodes. A fuel cell device is provided, comprising a device for supplying an oxidizing agent, a device for supplying an oxidizing agent to the other, a device for discharging reaction products from an electrolyte layer, and a conductive wire for extracting current from the pair of porous electrodes. , a heat supply device capable of introducing an appropriate amount of heat medium into the outside of the battery chamber housing and extracting the thermal energy of the heat medium to the outside; and an electric heating device connected to the pair of conductive wires and heating the heat medium. and a device for controlling the electric power supplied to the electric heating device according to the ratio of electric power load to thermal load. 3) A battery chamber casing is provided in the heat storage device, and within the battery chamber casing there is an electrolyte layer, a pair of porous electrodes facing each other through the electrolyte layer, and fuel is supplied to one of the pair of porous electrodes. A fuel cell device is provided, comprising a device for supplying an oxidizing agent, a device for supplying an oxidizing agent to the other, a device for discharging reaction products from an electrolyte layer, and a conductive wire for extracting current from the pair of porous electrodes. , a heat supply device that introduces an appropriate amount of heat medium outside the battery compartment housing and extracts the thermal energy of the heat medium to the outside, and a heat supply device that is provided inside the heat storage device and is separate from the heat medium inside the heat storage device. a heater in which a different heating medium is sealed; a converter that converts the thermal energy of the heating medium heated by the heater into electrical energy; and an operation of the converter according to the ratio of the thermal load to the electric power load. An energy supply device consisting of a control device that controls the
JP60200495A 1985-09-12 1985-09-12 Energy supply device Pending JPS6261276A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60200495A JPS6261276A (en) 1985-09-12 1985-09-12 Energy supply device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60200495A JPS6261276A (en) 1985-09-12 1985-09-12 Energy supply device

Publications (1)

Publication Number Publication Date
JPS6261276A true JPS6261276A (en) 1987-03-17

Family

ID=16425268

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60200495A Pending JPS6261276A (en) 1985-09-12 1985-09-12 Energy supply device

Country Status (1)

Country Link
JP (1) JPS6261276A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997002614A1 (en) * 1995-06-30 1997-01-23 Siemens Aktiengesellschaft High-temperature fuel cell installation and process for its operation
WO1998024138A1 (en) * 1996-11-29 1998-06-04 Siemens Aktiengesellschaft Liquid-cooled fuel cell batteries
KR20020056167A (en) * 2000-12-29 2002-07-10 구자홍 Regenerative rpg
WO2011141554A1 (en) * 2010-05-14 2011-11-17 Bundesrepublik Deutschland, vertreten durch das Bundesministerium für Wirtschaft und Technologie, dieses vertreten durch den Präsidenten der Physikalisch-Technischen Bundesanstalt Explosion-protected fuel cell
CZ308910B6 (en) * 2007-10-04 2021-08-25 Auxilien, A. S. Method of extending the control range of electrical power supplied to the electricity system and energy system with an extended control range

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997002614A1 (en) * 1995-06-30 1997-01-23 Siemens Aktiengesellschaft High-temperature fuel cell installation and process for its operation
WO1998024138A1 (en) * 1996-11-29 1998-06-04 Siemens Aktiengesellschaft Liquid-cooled fuel cell batteries
KR20020056167A (en) * 2000-12-29 2002-07-10 구자홍 Regenerative rpg
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