JPH09115537A - Fuel cell power-generation system - Google Patents

Fuel cell power-generation system

Info

Publication number
JPH09115537A
JPH09115537A JP7270039A JP27003995A JPH09115537A JP H09115537 A JPH09115537 A JP H09115537A JP 7270039 A JP7270039 A JP 7270039A JP 27003995 A JP27003995 A JP 27003995A JP H09115537 A JPH09115537 A JP H09115537A
Authority
JP
Japan
Prior art keywords
hydrogen
fuel cell
oxygen
fuel
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
JP7270039A
Other languages
Japanese (ja)
Inventor
Yutaka Kuwata
豊 鍬田
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.)
Nippon Telegraph and Telephone Corp
Original Assignee
Nippon Telegraph and Telephone Corp
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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP7270039A priority Critical patent/JPH09115537A/en
Publication of JPH09115537A publication Critical patent/JPH09115537A/en
Pending 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
    • Y02E60/50Fuel cells

Landscapes

  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a fuel cell power-generation system without the output reduction of a fuel cell in the case of an electric output fluctuation and fuel switching. SOLUTION: This system consists of a reformer 2 which reforms the fossil fuel to produce hydrogen, a fuel cell 3 which generates electricity using hydrogen from the reformer 2 and oxygen in the air as a fuel, and an electric power conversion device 9 which converts the generated power of the fuel cell 3. In this system, a hydrogen supply device 100 which supplies hydrogen together with the hydrogen from the reformer 2 to the fuel cell 3 or an oxygen supply device 200 which supplies oxygen together with the oxygen 7 in the air to the fuel cell 3 is provided, and the hydrogen in the hydrogen supply device 100 or the oxygen in the oxygen supply device 200 is supplied to the fuel cell 3 according to the output power fluctuation of the power conversion device 9.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、化石燃料を水素に
改質する改質器と、水素と酸素を燃料として発電を行う
燃料電池と、燃料電池の発電電力を変換する電気出力系
とからなる燃料電池発電システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention comprises a reformer for reforming fossil fuel into hydrogen, a fuel cell for generating electric power using hydrogen and oxygen as fuel, and an electric output system for converting electric power generated by the fuel cell. Fuel cell power generation system.

【0002】[0002]

【従来の技術】従来の燃料電池発電システムでは、図4
に示すように都市ガス等の燃料を常用燃料1として用い
ている。燃料電池3は燃料極4、電解質5と空気極6か
ら構成されており、燃料極4に水素を、空気極6に空気
中の酸素7を供給することで電池反応により直流電力8
を得る。得られた直流電力8を電力変換装置9に供給し
て電気出力として利用する。燃料極4に供給する水素を
作るには、常用燃料1である都市ガスを改質器2で改質
して水素を多量に含む改質ガスに変化させる。この改質
ガスを燃料電池3の燃料極4に供給し、空気中の酸素7
を空気極6に供給することで燃料電池3は発電を行う。
燃料電池3の発電電力を増加(または減少)するために
は、都市ガス等の常用燃料1、空気中の酸素7の量を増
加(または減少)させることで発電電力8を変化させ
る。
2. Description of the Related Art A conventional fuel cell power generation system is shown in FIG.
As shown in, a fuel such as city gas is used as the regular fuel 1. The fuel cell 3 is composed of a fuel electrode 4, an electrolyte 5, and an air electrode 6. By supplying hydrogen to the fuel electrode 4 and oxygen 7 in the air to the air electrode 6, a DC power 8 is generated by a cell reaction.
Get. The obtained DC power 8 is supplied to the power converter 9 and used as an electric output. In order to produce hydrogen to be supplied to the fuel electrode 4, the city gas, which is the regular fuel 1, is reformed by the reformer 2 to be a reformed gas containing a large amount of hydrogen. This reformed gas is supplied to the fuel electrode 4 of the fuel cell 3 so that oxygen in the air 7
Is supplied to the air electrode 6, the fuel cell 3 generates electricity.
In order to increase (or decrease) the generated power of the fuel cell 3, the generated power 8 is changed by increasing (or decreasing) the amounts of the common fuel 1 such as city gas and the oxygen 7 in the air.

【0003】図4の従来の燃料電池発電システムでは、
常用燃料1として都市ガスを用いているが、都市ガスの
供給が途絶えた時には発電を行えないので、通信用電源
システムのように高信頼が要求されるシステムに燃料電
池発電システムを適用するためには、図5のように、プ
ロパンのような予備燃料1’を備蓄しておいて都市ガス
が途絶えた時には、燃料切替装置10を用いてプロパン
等の予備燃料1’に切り替えて発電を継続する燃料電池
発電システムが提案されている。図5のシステムでは、
予備燃料1’であるプロパンを改質器2に供給して水素
を作るが、この場合には都市ガスの場合と改質条件が異
なるので、予め決められた改質温度、燃料供給量および
水蒸気供給量に制御することが必要となる。このように
して常用燃料1の都市ガスの供給が途絶えた時にも予備
燃料1’に切り替えて改質器で水素を発生させることで
燃料電池の発電を継続することができる。
In the conventional fuel cell power generation system shown in FIG. 4,
Although city gas is used as the regular fuel 1, it cannot generate power when the supply of city gas is interrupted. Therefore, in order to apply the fuel cell power generation system to a system that requires high reliability such as a communication power supply system. As shown in FIG. 5, when the reserve gas 1'such as propane is stored and the city gas runs out, the fuel switching device 10 is used to switch to the reserve fuel 1'such as propane to continue power generation. Fuel cell power generation systems have been proposed. In the system of FIG. 5,
Propane, which is the reserve fuel 1 ', is supplied to the reformer 2 to produce hydrogen. In this case, since the reforming conditions are different from the case of city gas, a predetermined reforming temperature, fuel supply amount and steam It is necessary to control the supply amount. In this way, even when the supply of the city gas of the regular fuel 1 is interrupted, it is possible to continue the power generation of the fuel cell by switching to the reserve fuel 1 ′ and generating hydrogen in the reformer.

【0004】[0004]

【発明が解決しようとする課題】上述した従来の燃料電
池発電システムでは、燃料電池から急激に電気出力を取
り出す時には電気出力に見合った水素を改質器で作るに
は時間遅れが生じるため、水素の供給不足により燃料電
池出力が一時的に低下し、燃料電池の劣化が生じるとい
う問題があった。従って、電気出力変動の大きな負荷に
燃料電池から電力供給を行うことはできなかった。
In the above-described conventional fuel cell power generation system, when the electric output is rapidly taken out from the fuel cell, there is a time delay in producing hydrogen corresponding to the electric output in the reformer. There was a problem that the output of the fuel cell was temporarily reduced due to the insufficient supply of hydrogen and the fuel cell was deteriorated. Therefore, it was not possible to supply electric power from the fuel cell to a load with a large fluctuation in electric output.

【0005】また、常用燃料である都市ガスから予備燃
料であるプロパンへ燃料切替を行った場合、同じ改質器
を用いるとしても改質条件がことなるため、改質器から
安定に水素が取り出せる定常状態に達するまでには時間
遅れが生じる。従って、燃料切替時には燃料となる水素
の供給不足が生じ、燃料電池出力が一次的に低下する現
象が生じる。燃料電池出力が低下した状態で一定の電気
出力を取り出し続けると燃料電池の急激な劣化が生じ、
燃料電池がシステムダウンするという問題があった。こ
のため通信用電源のような高信頼性が要求される電源と
して燃料電池発電システムを適用するには、燃料切替時
にシステムダウンが起こる恐れがある。
Further, when the fuel is switched from city gas, which is a regular fuel, to propane, which is a preliminary fuel, reforming conditions are different even if the same reformer is used, so that hydrogen can be stably taken out from the reformer. There is a time delay until the steady state is reached. Therefore, when the fuel is switched, a shortage of hydrogen as a fuel occurs, and the output of the fuel cell temporarily decreases. Sudden deterioration of the fuel cell occurs if a constant electric output is continuously taken out with the fuel cell output decreasing,
There was a problem that the fuel cell system went down. Therefore, in order to apply the fuel cell power generation system as a power supply that requires high reliability, such as a power supply for communication, there is a possibility that the system will go down during fuel switching.

【0006】上記従来技術の電気出力変動時における水
素供給量と燃料電池出力電圧の時間変化を図6に示す。
電気出力変動時にΔt1時間の間、水素供給量の不足と
それに伴う燃料電池出力電圧が低下を生じることが容易
に理解できる。また、上記従来技術の燃料切替時におけ
る水素供給量と燃料電池出力の時間変化を図7に示す。
燃料切替時にΔt2時間の間水素供給量の不足とそれに
伴う燃料電池の電圧低下が生じることが容易に理解でき
る。
FIG. 6 shows the changes over time in the hydrogen supply amount and the fuel cell output voltage when the electric output changes in the prior art.
It can be easily understood that the hydrogen supply amount is insufficient and the fuel cell output voltage is reduced during the Δt1 hour when the electric output changes. Further, FIG. 7 shows a time change of the hydrogen supply amount and the fuel cell output at the time of fuel switching of the above-mentioned conventional technique.
It can be easily understood that when the fuel is switched, the hydrogen supply amount is insufficient for Δt2 hours and the fuel cell voltage is reduced accordingly.

【0007】本発明は上記の事情に鑑みてなされたもの
で、電気出力変動時や燃料切替時における燃料電池出力
低下のない燃料電池発電システムを提供することを目的
とする。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a fuel cell power generation system in which the fuel cell output does not decrease when the electric output changes or when the fuel is switched.

【0008】[0008]

【課題を解決するための手段】前記課題の解決は、本発
明が次に列挙する新規な特徴的構成をとることにより達
成される。すなわち、本発明の第1の特徴は、化石燃料
を改質して水素を作り出す改質器と、前記改質器からの
水素と空気中の酸素を燃料として発電を行う燃料電池、
および前記燃料電池の発電電力を変換する電気出力系と
からなる燃料電池発電システムにおいて、前記改質器か
らの水素と合わせて燃料電池に水素を供給する水素供給
装置または空気中の酸素と合わせて燃料電池に酸素を供
給する酸素供給装置を備え、前記電気出力系の電力変動
に応じて前記水素供給装置の水素または前記酸素供給装
置の酸素を供給することである。
The solution to the above problems can be achieved by the present invention having the following novel characteristic configurations. That is, the first feature of the present invention is a reformer that reforms fossil fuel to produce hydrogen, and a fuel cell that generates electricity using hydrogen from the reformer and oxygen in the air as fuel.
And a fuel cell power generation system including an electric output system for converting generated power of the fuel cell, in combination with hydrogen from the reformer and hydrogen supply device for supplying hydrogen to the fuel cell or oxygen in the air An oxygen supply device for supplying oxygen to the fuel cell is provided, and hydrogen of the hydrogen supply device or oxygen of the oxygen supply device is supplied in accordance with power fluctuation of the electric output system.

【0009】本発明の第2の特徴は、化石燃料を改質し
て水素を作り出す改質器と、前記改質器からの水素と空
気中の酸素を燃料として発電を行う燃料電池、および前
記燃料電池の発電電力を変換する電気出力系とからなる
燃料電池発電システムにおいて、常用燃料と予備燃料を
切り替えて前記改質器に供給する燃料切替装置と、前記
改質器からの水素と合わせて燃料電池に水素を供給する
水素供給装置または空気中の酸素と合わせて燃料電池に
酸素を供給する酸素供給装置を備え、前記燃料切替装置
により燃料切替を行うときに前記水素供給装置の水素ま
たは前記酸素供給装置の酸素を供給することである。
A second feature of the present invention is a reformer for reforming fossil fuel to produce hydrogen, a fuel cell for generating electricity using hydrogen from the reformer and oxygen in the air as fuel, and In a fuel cell power generation system including an electric output system that converts generated power of a fuel cell, a fuel switching device that switches between a regular fuel and a backup fuel to supply the reformer and hydrogen from the reformer are combined. A hydrogen supply device for supplying hydrogen to the fuel cell or an oxygen supply device for supplying oxygen to the fuel cell together with oxygen in the air is provided, and when the fuel is switched by the fuel switching device, the hydrogen of the hydrogen supply device or the To supply oxygen from the oxygen supply device.

【0010】本発明第3の特徴は、前記第1の特徴また
は前記第2の特徴における燃料電池発電システムが、水
の電気分解によって発生する水素または酸素を貯蔵する
高圧タンクを備え、前記水素及び前記酸素を改質器から
の水素または前記空気中の酸素と合わせて燃料電池に供
給することである。
A third feature of the present invention is that the fuel cell power generation system according to the first feature or the second feature includes a high-pressure tank for storing hydrogen or oxygen generated by electrolysis of water. The oxygen is supplied to the fuel cell together with hydrogen from the reformer or oxygen in the air.

【0011】本発明の第4の特徴は、前記第3の特徴に
おける燃料電池発電システムが、燃料電池の排熱により
発電する熱電素子を備え、前記熱電素子の発電電力によ
り水の電気分解を行うことである。
A fourth feature of the present invention is that the fuel cell power generation system according to the third feature includes a thermoelectric element for generating power by exhaust heat of the fuel cell, and electrolyzes water by the power generated by the thermoelectric element. That is.

【0012】本発明は上記のような構成をとっているの
で、燃料切替時には水素供給装置または酸素供給装置に
蓄えられている水素または酸素を改質器からの水素や空
気中の酸素と合わせて供給することで、燃料電池の劣化
を防止して高信頼な燃料電池発電システムを実現でき
る。
Since the present invention has the above-mentioned structure, when the fuel is switched, the hydrogen or oxygen stored in the hydrogen supply device or the oxygen supply device is combined with the hydrogen from the reformer or the oxygen in the air. By supplying, it is possible to prevent deterioration of the fuel cell and realize a highly reliable fuel cell power generation system.

【0013】また、水の電気分解によって発生させた水
素や酸素を高圧タンクに貯蔵しておくことで、燃料電池
の電気出力変動が大きい時に高圧タンク内の水素や酸素
を供給することで燃料電池の劣化を防止することができ
る。さらに、水の電気分解に必要な電力を燃料電池の排
熱を利用した熱電素子から得ることにより高効率な燃料
電池発電システムを実現できる。
By storing hydrogen and oxygen generated by electrolysis of water in a high-pressure tank, hydrogen and oxygen in the high-pressure tank can be supplied when the electric output of the fuel cell fluctuates greatly. Can be prevented from deteriorating. Furthermore, a highly efficient fuel cell power generation system can be realized by obtaining the electric power required for the electrolysis of water from the thermoelectric element using the exhaust heat of the fuel cell.

【0014】[0014]

【発明の実施の形態】以下図面を参照して本発明の実施
の形態例を詳細に説明する。なお、本発明の精神を逸脱
しない範囲で種々の変更あるいは改良を行いうることは
言うまでもない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. Needless to say, various changes and improvements can be made without departing from the spirit of the present invention.

【0015】図1は本発明の第1の実施形態例の燃料電
池発電システムを示す構成説明図である。図中、1は常
用燃料、2は改質器、3は燃料電池、4は燃料極、5は
電解質、6は空気極、7は酸素、8は直流電力、9は電
力変換装置、100は水素供給装置、110は水素タン
ク、120は弁、200は酸素供給装置、210は酸素
タンク、220は弁である。
FIG. 1 is a structural explanatory view showing a fuel cell power generation system according to a first embodiment of the present invention. In the figure, 1 is a regular fuel, 2 is a reformer, 3 is a fuel cell, 4 is a fuel electrode, 5 is an electrolyte, 6 is an air electrode, 7 is oxygen, 8 is direct current power, 9 is a power converter, and 100 is A hydrogen supply device, 110 is a hydrogen tank, 120 is a valve, 200 is an oxygen supply device, 210 is an oxygen tank, and 220 is a valve.

【0016】即ち、化石燃料の常用燃料1を改質器2で
改質して水素を作り出し、この改質器2からの水素を燃
料電池3の燃料極4に供給すると共に水素供給装置10
0からの水素を燃料電池3の燃料極4に供給する。また
空気中の酸素7を燃料電池3の空気極6に供給すると共
に酸素供給装置200からの酸素を燃料電池3の空気極
6に供給する。燃料電池3は改質器2及び水素供給装置
100からの水素と空気中の酸素7及び酸素供給装置2
00からの酸素を燃料として電解質5の電池反応により
直流電力8の発電を行う。前記燃料電池3からの直流電
力8を電力変換装置9に供給して電気出力として利用す
る。この電気出力系の電力変動に応じて前記水素供給装
置100の弁120を制御して水素タンク110から水
素を供給するか、または前記酸素供給装置200の弁2
20を制御して酸素タンク210から酸素を供給する。
That is, the fossil fuel common fuel 1 is reformed by the reformer 2 to produce hydrogen, and the hydrogen from the reformer 2 is supplied to the fuel electrode 4 of the fuel cell 3 and the hydrogen supply device 10 is supplied.
Hydrogen from 0 is supplied to the fuel electrode 4 of the fuel cell 3. Further, oxygen 7 in the air is supplied to the air electrode 6 of the fuel cell 3, and oxygen from the oxygen supply device 200 is supplied to the air electrode 6 of the fuel cell 3. The fuel cell 3 includes hydrogen from the reformer 2 and the hydrogen supply device 100 and oxygen 7 in the air and the oxygen supply device 2.
Direct current power 8 is generated by a cell reaction of the electrolyte 5 using oxygen from 00 as fuel. The DC power 8 from the fuel cell 3 is supplied to the power converter 9 and used as an electric output. The valve 120 of the hydrogen supply device 100 is controlled to supply hydrogen from the hydrogen tank 110, or the valve 2 of the oxygen supply device 200 is controlled according to the power fluctuation of the electric output system.
20 is controlled to supply oxygen from the oxygen tank 210.

【0017】尚、前記水素供給装置100か前記酸素供
給装置200のいずれか一方のみを備える燃料電池発電
システムを構成してもよい。図2は、本発明の第2の実
施形態例を示す燃料電池発電システムの構成を示す。図
2は、図5の燃料切替を考慮した燃料電池発電システム
の燃料電池3の燃料極4に水素を多量に含んだ改質ガス
を供給するラインと並列に水素を供給する水素供給装置
100を設けたことを特徴とするものである。また、空
気中の酸素7を燃料電池3の空気極6に供給するライン
と並列に酸素を供給する酸素供給装置200を設けたこ
とを特徴とする。なお、図2に示した記号のうち図5と
同一のものは同一の部分を示し、説明を省略する。
A fuel cell power generation system may be configured to include only one of the hydrogen supply device 100 and the oxygen supply device 200. FIG. 2 shows the configuration of a fuel cell power generation system showing a second embodiment of the present invention. FIG. 2 shows a hydrogen supply device 100 that supplies hydrogen in parallel with a line that supplies a reformed gas containing a large amount of hydrogen to a fuel electrode 4 of a fuel cell power generation system of the fuel cell power generation system in FIG. It is characterized by being provided. Further, an oxygen supply device 200 for supplying oxygen is provided in parallel with a line for supplying oxygen 7 in the air to the air electrode 6 of the fuel cell 3. Note that, of the symbols shown in FIG. 2, the same symbols as those in FIG.

【0018】水素供給装置100において、水素を蓄え
る水素タンク110には、圧力の高い水素を蓄えてお
き、燃料電池3の必要水素量が不足する燃料切替時等に
は、弁120を調節して改質ガスと合わせて水素を燃料
電池3の燃料極4に供給する。弁120を調節するタイ
ミングとしては、常用燃料1と予備燃料1’を切り替え
る燃料切替装置10の切替信号を用いて予め燃料が切り
替わる前に水素タンク110から水素を供給することで
水素の不足がなくなる。燃料極4に多くの水素を供給し
ても電池反応に用いられなかった余剰水素は燃料極4の
出口から流出する。余剰水素を有効に活用するために
は、改質反応に必要な熱量を確保するための改質器2の
燃料ガスとして用いてもよい。
In the hydrogen supply device 100, hydrogen having a high pressure is stored in the hydrogen tank 110 for storing hydrogen, and the valve 120 is adjusted when the fuel is switched when the required amount of hydrogen in the fuel cell 3 is insufficient. Hydrogen is supplied to the fuel electrode 4 of the fuel cell 3 together with the reformed gas. The timing for adjusting the valve 120 is to supply hydrogen from the hydrogen tank 110 before the fuel is switched in advance by using the switching signal of the fuel switching device 10 that switches between the regular fuel 1 and the auxiliary fuel 1 ′, so that there is no shortage of hydrogen. . Even if a large amount of hydrogen is supplied to the fuel electrode 4, surplus hydrogen that has not been used in the cell reaction flows out from the outlet of the fuel electrode 4. In order to effectively utilize the surplus hydrogen, it may be used as the fuel gas of the reformer 2 for securing the heat quantity necessary for the reforming reaction.

【0019】一方、燃料電池3の電池反応には水素の他
に酸素も必要となるが、空気極6の酸素が不足すると燃
料電池3の出力特性が低下して劣化する。急激な電気出
力変化に耐えるためには燃料電池3の燃料極4及び空気
極6への素早い水素と酸素の供給が必要となる。このた
め、燃料極4への水素の供給に加えて空気極6へも空気
中の酸素7の他に酸素供給装置200の酸素タンク21
0から酸素を弁220を調節して供給することで燃料電
池3から急激に電気出力を取り出しても燃料電池3の出
力特性低下の少ない燃料電池発電システムを提供でき
る。
On the other hand, oxygen is required for the cell reaction of the fuel cell 3 in addition to hydrogen, but if oxygen in the air electrode 6 is insufficient, the output characteristics of the fuel cell 3 will deteriorate and deteriorate. In order to withstand a sudden change in electric output, it is necessary to quickly supply hydrogen and oxygen to the fuel electrode 4 and the air electrode 6 of the fuel cell 3. Therefore, in addition to supplying hydrogen to the fuel electrode 4, not only oxygen 7 in the air but also the oxygen tank 21 of the oxygen supply device 200 is supplied to the air electrode 6.
By supplying oxygen from 0 by adjusting the valve 220, it is possible to provide a fuel cell power generation system in which the output characteristic of the fuel cell 3 is not significantly deteriorated even when the electric output is rapidly taken out from the fuel cell 3.

【0020】常用燃料1から予備燃料1′に燃料が切り
替わって安定するまでの時間は、比較的短い時間である
ため、燃料切替時に不足する水素及び酸素の量はタンク
に蓄えておき、不足した時に切り替えることで対処でき
る。一方、燃料電池3の出力電力変動に対して燃料電池
3を応答させようとすると、水素タンク110と酸素タ
ンク210の取り替えが頻繁に繰り返されるため常に水
素と酸素を作りだす必要がある。
Since the time required for the fuel to switch from the regular fuel 1 to the backup fuel 1'and stabilize is relatively short, the amount of hydrogen and oxygen that is insufficient at the time of fuel switching is stored in the tank and is insufficient. You can deal with it by switching from time to time. On the other hand, when attempting to make the fuel cell 3 respond to fluctuations in the output power of the fuel cell 3, the replacement of the hydrogen tank 110 and the oxygen tank 210 is frequently repeated, so that it is necessary to constantly produce hydrogen and oxygen.

【0021】図3は本発明の第3の実施形態例であり、
図2の水素タンク110と酸素タンク210に常に水素
と酸素を蓄えておくための構成である。高圧タンク30
0内に水を蓄えておき正極310と負極320の電極に
よる水の電気分解により水素と酸素を作り出す方法を用
いるものである。高圧タンク300の水素貯蔵部330
と酸素貯蔵部340を電気は流れるが気体の移動ができ
ないように隔壁350で仕切っている。水の電気分解に
より得られた水素ガスと酸素ガスは高圧タンク300内
の水素貯蔵部330と酸素貯蔵部340に蓄えられてい
るため弁360、370を調節することにより、燃料電
池3の急激な変動に対しても十分な水素と酸素を燃料電
池3へ供給できる。電気分解によって消費される水は外
部から補給する必要があるが、このための補給水380
としては、一般の水道水を用いてもよいが、電池反応に
より燃料電池3から排出される水蒸気を凝縮して用いて
もよい。この際、水道水等には不純物が多く含まれてい
るので、一般には不純物を取り除くためにイオン交換樹
脂等により濾過して供給する。
FIG. 3 shows a third embodiment of the present invention.
This is a configuration for always storing hydrogen and oxygen in the hydrogen tank 110 and the oxygen tank 210 of FIG. High pressure tank 30
In this method, water is stored in 0 and hydrogen and oxygen are produced by electrolysis of water by the electrodes of the positive electrode 310 and the negative electrode 320. Hydrogen storage unit 330 of high-pressure tank 300
The oxygen storage unit 340 is partitioned by a partition wall 350 so that electricity can flow but gas cannot move. Since hydrogen gas and oxygen gas obtained by electrolysis of water are stored in the hydrogen storage unit 330 and the oxygen storage unit 340 in the high-pressure tank 300, the valves 360 and 370 are adjusted to rapidly change the fuel cell 3. Sufficient hydrogen and oxygen can be supplied to the fuel cell 3 even with fluctuations. The water consumed by electrolysis needs to be replenished from the outside, but make-up water 380 for this is supplied.
For this, general tap water may be used, but water vapor discharged from the fuel cell 3 by the cell reaction may be condensed and used. At this time, since tap water contains a large amount of impurities, it is generally supplied after being filtered with an ion exchange resin or the like to remove the impurities.

【0022】高圧タンク300の電極310,320へ
電力を供給する方法としては、燃料電池3の電気出力を
利用する方法もあるが、図3には燃料電池3から得られ
る排熱を熱電素子400の発電に利用して水の電気分解
を行う方法を示している。改質器2は化石燃料を水素に
改質するために高温に維持されるので、この改質器2の
高い温度と室温の温度差によって熱電素子400を用
い、得られる電力を利用して水の電気分解に利用する。
電力変換回路500は水の電気分解によって発生する水
素や酸素の量に応じて熱電素子400から供給する電力
を調整する。このように電力変換回路500により熱電
素子400からの供給電力を調整することで高圧タンク
300内の圧力を一定に制御できるというメリットがあ
る。このように構成することで、高圧タンク300内に
水素と酸素を高い圧力で貯蔵できるので、弁360,3
70を調整することで必要なときに必要なだけの水素と
酸素を供給することができる。ここでは電気出力変動時
や燃料切替時にのみ高い濃度の水素や酸素を利用する例
について説明したが、常時これらの水素や酸素を燃料電
池3の発電に利用することで高効率な燃料電池発電を行
えることは言うまでもない。本実施形態例では改質器2
の高温と室温の差を利用した熱電素子400による発電
電力を水の電気分解に利用する例について説明したが、
改質器2以外の箇所であっても水の電気分解に必要な電
力が得られる箇所に熱電素子を取り付けてもよい。ま
た、熱電素子以外のものを用いて水の電気分解を行うこ
とで水素または酸素を発生させてもよいことは言うまで
もない。
As a method of supplying electric power to the electrodes 310 and 320 of the high-pressure tank 300, there is a method of utilizing the electric output of the fuel cell 3. In FIG. 3, the exhaust heat obtained from the fuel cell 3 is used as the thermoelectric element 400. It shows a method of electrolyzing water by using it for power generation. Since the reformer 2 is maintained at a high temperature for reforming the fossil fuel into hydrogen, the thermoelectric element 400 is used according to the temperature difference between the high temperature of the reformer 2 and the room temperature, and the obtained electric power is used to generate water. Used for electrolysis of.
The power conversion circuit 500 adjusts the power supplied from the thermoelectric element 400 according to the amount of hydrogen or oxygen generated by electrolysis of water. Thus, there is an advantage that the pressure in the high-pressure tank 300 can be controlled to be constant by adjusting the power supplied from the thermoelectric element 400 by the power conversion circuit 500. With this configuration, hydrogen and oxygen can be stored in the high-pressure tank 300 at a high pressure, so that the valves 360, 3
By adjusting 70, the required amount of hydrogen and oxygen can be supplied when needed. Here, an example in which high concentration hydrogen or oxygen is used only when the electric output fluctuates or when the fuel is switched has been described. However, by constantly using these hydrogen and oxygen for the power generation of the fuel cell 3, highly efficient fuel cell power generation can be achieved. It goes without saying that you can do it. In the present embodiment example, the reformer 2
The example in which the electric power generated by the thermoelectric element 400 that utilizes the difference between the high temperature and the room temperature of is used for the electrolysis of water was described
A thermoelectric element may be attached to a place other than the reformer 2 where electric power required for electrolyzing water is obtained. It goes without saying that hydrogen or oxygen may be generated by electrolyzing water using something other than a thermoelectric element.

【0023】[0023]

【発明の効果】以上述べたように本発明によれば、都市
ガスからプロパンへの燃料切替時や燃料電池の電気出力
変動時に高い圧力で貯蔵している水素や酸素を速やかに
供給することにより、燃料電池の燃料極および空気極へ
十分な燃料を供給できるため燃料電池の劣化を防止でき
る高信頼な燃料電池発電システムを実現でき、通信用電
源としても適用が可能となる。水素と酸素の発生には燃
料電池の排熱を用いることで高効率な燃料電池発電シス
テムを実現できる。
As described above, according to the present invention, hydrogen and oxygen stored at a high pressure are rapidly supplied at the time of fuel switching from city gas to propane or when the electric output of the fuel cell fluctuates. Since a sufficient amount of fuel can be supplied to the fuel electrode and the air electrode of the fuel cell, it is possible to realize a highly reliable fuel cell power generation system that can prevent deterioration of the fuel cell and can also be applied as a communication power source. A highly efficient fuel cell power generation system can be realized by using the exhaust heat of the fuel cell to generate hydrogen and oxygen.

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

【図1】本発明の第1の実施形態例を示す構成説明図で
ある。
FIG. 1 is a configuration explanatory view showing a first embodiment of the present invention.

【図2】本発明の第2の実施形態例を示す構成説明図で
ある。
FIG. 2 is a configuration explanatory view showing a second embodiment example of the present invention.

【図3】本発明の第3の実施形態例を示す構成説明図で
ある。
FIG. 3 is a configuration explanatory view showing a third embodiment example of the present invention.

【図4】従来の燃料電池発電システムの一例を示す構成
説明図である。
FIG. 4 is a structural explanatory view showing an example of a conventional fuel cell power generation system.

【図5】従来の燃料電池発電システムの他の例を示す構
成説明図である。
FIG. 5 is a configuration explanatory view showing another example of a conventional fuel cell power generation system.

【図6】従来の燃料電池発電システムにおける燃料電池
電気出力変動時の各部波形の一例を示す波形図である。
FIG. 6 is a waveform diagram showing an example of waveforms at various portions when a fuel cell electric output varies in a conventional fuel cell power generation system.

【図7】従来の燃料電池発電システムにおける燃料切替
時の各部波形の一例を示す波形図である。
FIG. 7 is a waveform diagram showing an example of waveforms of various parts when switching fuels in a conventional fuel cell power generation system.

【符号の説明】[Explanation of symbols]

1…常用燃料、1′…予備燃料、2…改質器、3…燃料
電池、4…燃料極、5…電解質、6…空気極、7…酸
素、8…直流電力、9…電力変換装置、10…燃料切替
装置、100…水素供給装置、110…水素タンク、1
20…弁、200…酸素供給装置、210…酸素タン
ク、220…弁、300…高圧タンク、310…正極、
320…負極、330…水素貯蔵部、340…酸素貯蔵
部、350…隔壁、360,370…弁、380…補給
水、400…熱電素子、500…電力変換回路。
DESCRIPTION OF SYMBOLS 1 ... Regular fuel, 1 '... Reserve fuel, 2 ... Reformer, 3 ... Fuel cell, 4 ... Fuel electrode, 5 ... Electrolyte, 6 ... Air electrode, 7 ... Oxygen, 8 ... DC power, 9 ... Power converter 10 ... Fuel switching device, 100 ... Hydrogen supply device, 110 ... Hydrogen tank, 1
20 ... Valve, 200 ... Oxygen supply device, 210 ... Oxygen tank, 220 ... Valve, 300 ... High pressure tank, 310 ... Positive electrode,
320 ... Negative electrode, 330 ... Hydrogen storage section, 340 ... Oxygen storage section, 350 ... Partition wall, 360, 370 ... Valve, 380 ... Make-up water, 400 ... Thermoelectric element, 500 ... Power conversion circuit.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 化石燃料を改質して水素を作り出す改質
器と、前記改質器からの水素と空気中の酸素を燃料とし
て発電を行う燃料電池、および前記燃料電池の発電電力
を変換する電気出力系とからなる燃料電池発電システム
において、 前記改質器からの水素と合わせて燃料電池に水素を供給
する水素供給装置または空気中の酸素と合わせて燃料電
池に酸素を供給する酸素供給装置を備え、前記電気出力
系の電力変動に応じて前記水素供給装置の水素または前
記酸素供給装置の酸素を供給することを特徴とする燃料
電池発電システム。
1. A reformer that reforms fossil fuel to produce hydrogen, a fuel cell that generates electricity using hydrogen from the reformer and oxygen in the air as fuel, and power generated by the fuel cell is converted. And a hydrogen supply device for supplying hydrogen to the fuel cell together with hydrogen from the reformer or an oxygen supply for supplying oxygen to the fuel cell together with oxygen in the air. A fuel cell power generation system, comprising a device, and supplying hydrogen of the hydrogen supply device or oxygen of the oxygen supply device according to power fluctuations of the electric output system.
【請求項2】 化石燃料を改質して水素を作り出す改質
器と、前記改質器からの水素と空気中の酸素を燃料とし
て発電を行う燃料電池、および前記燃料電池の発電電力
を変換する電気出力系とからなる燃料電池発電システム
において、 常用燃料と予備燃料を切り替えて前記改質器に供給する
燃料切替装置と、前記改質器からの水素と合わせて燃料
電池に水素を供給する水素供給装置または空気中の酸素
と合わせて燃料電池に酸素を供給する酸素供給装置を備
え、前記燃料切替装置により燃料切替を行うときに前記
水素供給装置の水素または前記酸素供給装置の酸素を供
給することを特徴とする燃料電池発電システム。
2. A reformer for reforming fossil fuel to produce hydrogen, a fuel cell for generating electricity using hydrogen from the reformer and oxygen in the air as fuel, and converting generated power of the fuel cell. In a fuel cell power generation system including an electric output system for supplying electricity, hydrogen is supplied to a fuel cell together with a fuel switching device that switches between a regular fuel and a backup fuel to supply to the reformer, and hydrogen from the reformer. A hydrogen supply device or an oxygen supply device that supplies oxygen to the fuel cell together with oxygen in the air, and supplies hydrogen of the hydrogen supply device or oxygen of the oxygen supply device when performing fuel switching by the fuel switching device. A fuel cell power generation system characterized by:
【請求項3】 水素を供給する水素供給装置及び酸素を
供給する酸素供給装置として高圧タンクを用い、前記高
圧タンク内の水の電気分解によって前記水素または前記
酸素を得ることを特徴とする請求項1または2記載の燃
料電池発電システム。
3. A high-pressure tank is used as a hydrogen supply device for supplying hydrogen and an oxygen supply device for supplying oxygen, and the hydrogen or the oxygen is obtained by electrolysis of water in the high-pressure tank. The fuel cell power generation system according to 1 or 2.
【請求項4】 燃料電池の排熱により発電する熱電素子
を備え、前記熱電素子の発電電力により水の電気分解を
行うことを特徴とする請求項3記載の燃料電池発電シス
テム。
4. The fuel cell power generation system according to claim 3, further comprising a thermoelectric element that generates electric power by exhaust heat of the fuel cell, and electrolysis of water is performed by electric power generated by the thermoelectric element.
JP7270039A 1995-10-18 1995-10-18 Fuel cell power-generation system Pending JPH09115537A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7270039A JPH09115537A (en) 1995-10-18 1995-10-18 Fuel cell power-generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7270039A JPH09115537A (en) 1995-10-18 1995-10-18 Fuel cell power-generation system

Publications (1)

Publication Number Publication Date
JPH09115537A true JPH09115537A (en) 1997-05-02

Family

ID=17480688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7270039A Pending JPH09115537A (en) 1995-10-18 1995-10-18 Fuel cell power-generation system

Country Status (1)

Country Link
JP (1) JPH09115537A (en)

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JP2006008418A (en) * 2004-06-22 2006-01-12 Idemitsu Kosan Co Ltd Apparatus for producing hydrogen and fuel cell system
JP2006282452A (en) * 2005-03-31 2006-10-19 Toyota Central Res & Dev Lab Inc Hydrogen fuel feeding system
JP2009289419A (en) * 2008-05-27 2009-12-10 Casio Comput Co Ltd Power generator and electronic device
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JP2013200990A (en) * 2012-03-23 2013-10-03 Seiko Instruments Inc Fuel cell device
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003100312A (en) * 2001-09-27 2003-04-04 Chugoku Electric Power Co Inc:The Reversible cogeneration system
JP2006008418A (en) * 2004-06-22 2006-01-12 Idemitsu Kosan Co Ltd Apparatus for producing hydrogen and fuel cell system
JP2006282452A (en) * 2005-03-31 2006-10-19 Toyota Central Res & Dev Lab Inc Hydrogen fuel feeding system
JP2009289419A (en) * 2008-05-27 2009-12-10 Casio Comput Co Ltd Power generator and electronic device
WO2013084623A1 (en) * 2011-12-05 2013-06-13 コニカミノルタ株式会社 Fuel cell system
JPWO2013084623A1 (en) * 2011-12-05 2015-04-27 コニカミノルタ株式会社 Fuel cell system
JP2013200990A (en) * 2012-03-23 2013-10-03 Seiko Instruments Inc Fuel cell device
WO2013146396A1 (en) * 2012-03-28 2013-10-03 コニカミノルタ株式会社 Secondary battery fuel cell system
JP2014032871A (en) * 2012-08-03 2014-02-20 Tokyo Gas Co Ltd Fuel supply method and system for fuel cell
CN112687914A (en) * 2019-10-18 2021-04-20 丰田自动车株式会社 Energy management system
CN112687914B (en) * 2019-10-18 2023-11-24 丰田自动车株式会社 energy management system

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