JPH0760691B2 - Fuel cell power generation system - Google Patents
Fuel cell power generation systemInfo
- Publication number
- JPH0760691B2 JPH0760691B2 JP60072554A JP7255485A JPH0760691B2 JP H0760691 B2 JPH0760691 B2 JP H0760691B2 JP 60072554 A JP60072554 A JP 60072554A JP 7255485 A JP7255485 A JP 7255485A JP H0760691 B2 JPH0760691 B2 JP H0760691B2
- Authority
- JP
- Japan
- Prior art keywords
- steam
- power generation
- fuel cell
- fuel
- generation system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
-
- 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)
Description
【発明の詳細な説明】 〔発明の技術分野〕 本発明は、燃料電池発電システムに関する。Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to a fuel cell power generation system.
従来、燃料の有しているエネルギーを直接電気的エネル
ギーに変換するものとして燃料電池が知られている。第
3図にこの燃料電池を用いた発電ユニットの概略系統お
よび回路構成を示し説明する。Conventionally, a fuel cell is known as a device that directly converts the energy of a fuel into electrical energy. A schematic system and circuit configuration of a power generation unit using this fuel cell is shown in FIG. 3 and explained.
燃料電池1は多数のセル2を直列接続して成り、酸化剤
として酸素(配管3)、燃料剤として水素(配管4)が
供給され、電気化学的反応により直流電力を発生する。The fuel cell 1 is composed of a large number of cells 2 connected in series, oxygen (piping 3) is supplied as an oxidant, and hydrogen (piping 4) is supplied as a fuel, and a direct current power is generated by an electrochemical reaction.
この直流電力は、直流遮断器5を介してインバータ6で
交流電力に変換して電力系統10に供給される。This DC power is converted into AC power by the inverter 6 via the DC circuit breaker 5 and supplied to the power system 10.
また11は気水分離器であって、燃料電池内の反応による
発熱を除去するための冷却水系統7の中にあって、電池
を冷却し自らは加熱された冷却水(熱水または2相流
体)を蒸気と水に分離し(熱水の場合は減圧する)、蒸
気は後述する改質器13へ、水は再び冷却水として燃料電
池1にもどすためのものである。Further, 11 is a steam separator, which is in the cooling water system 7 for removing heat generated by the reaction in the fuel cell, and cools the cell and cools itself by heating (hot water or two-phase). A fluid is separated into steam and water (in the case of hot water, pressure is reduced), steam is returned to the reformer 13 described later, and water is returned to the fuel cell 1 as cooling water again.
改質器13に送られた蒸気は直前で原燃料(一般には天然
ガス)と混合されて器内に入り、内部に充填された触媒
の作用によって燃料電池1の燃料である水素を主体とし
残りの大部分が二酸化炭素であるガスに変成される。Immediately before, the steam sent to the reformer 13 is mixed with the raw fuel (generally natural gas) and enters the reactor, where the main component is hydrogen, which is the fuel of the fuel cell 1, due to the action of the catalyst filled inside. Is transformed into a gas that is mostly carbon dioxide.
上記作用は吸熱反応であるため、図示してはいないが、
改質器13には燃焼室が設けられ、外部から空気及び水素
(電池排燃料あるいは天然ガス)が供給されて反応平衡
状態を維持するための熱が供給される。Since the above action is an endothermic reaction, it is not shown,
The reformer 13 is provided with a combustion chamber, and is supplied with air and hydrogen (battery exhaust fuel or natural gas) from the outside to supply heat for maintaining a reaction equilibrium state.
一方起動時には、燃料電池の発熱が少ないため、上記蒸
気を発生するための電気ヒータ12を気水分離器11に内蔵
している。On the other hand, at the time of start-up, since the heat generation of the fuel cell is small, the electric heater 12 for generating the steam is built in the steam separator 11.
またこの電気ヒータ12は上記と同様燃料電池の発熱が十
分でない、部分負荷時にも使用される。Further, this electric heater 12 is also used during partial load when the heat generation of the fuel cell is insufficient as in the above case.
第4図の曲線21は一般的な燃料電池発電ユニットの不足
蒸気量と負荷の関係を示したもので、無負荷待機時の蒸
気発生量が最も少なく、同図曲線22の如く必要な蒸気量
の大部分を電気ヒータの加熱によって発生させる必要が
あり、負荷の上昇に伴って電池の発熱も増大するため不
足量が減少するが、定格負荷の2/3程度までは自己充足
できない。それ以上では逆に蒸気が余るため余剰蒸気は
冷却して補給水用水タンクにもどされる。The curve 21 in Fig. 4 shows the relationship between the amount of insufficient steam and the load of a general fuel cell power generation unit. The amount of steam generated during standby with no load is the smallest, and the amount of steam required as shown by curve 22 in the same figure. It is necessary to generate most of the above by heating the electric heater, and the heat generation of the battery increases as the load increases, so the shortage amount decreases, but it cannot self-sufficient up to about 2/3 of the rated load. On the contrary, since steam is left over, excess steam is cooled and returned to the makeup water tank.
上記電気ヒータの必要容量は大きく定格出力の20〜30%
にも達し、且つ起動、負荷変化に要する時間を短縮しよ
うとすればするほど大きくなる。しかもこの電気ヒータ
は起動,部分負荷時といった比較的短期間にしか使用さ
れず、その設備費は経済性を阻害する一因ともなってい
る。The required capacity of the above electric heater is large and is 20 to 30% of the rated output.
And the more time it takes to shorten the time required for start-up and load change, the larger it becomes. Moreover, this electric heater is used only for a relatively short period of time, such as when starting up and when it is partially loaded, and its equipment cost is one of the factors that hinders economical efficiency.
一方燃料電池発電システムは小容量でも発電効率が高い
ため中,大容量の発電システムであっても小容量の発電
ユニットを複数台併設した方が起動特性も良く、また技
術上の困難さを回避した発電システムの信頼性を上げる
点でも望ましいが、このように複数台併設した従来のシ
ステムでは構成機器も多くコスト上の難点があると共に
制御機構も複雑となる欠点を有する。On the other hand, the fuel cell power generation system has high power generation efficiency even with a small capacity, so even if it is a medium or large capacity power generation system, it is better to have a plurality of small capacity power generation units together for better starting characteristics and avoid technical difficulties. This is also desirable from the standpoint of increasing the reliability of the power generation system, but the conventional system having a plurality of such power generation systems has the drawbacks of having a large number of constituent devices and cost, and of having a complicated control mechanism.
本発明は複数の燃料電池発電ユニットを併設したマルチ
発電システムまたは熱併給発電システムにおける不経済
性と制御機構の複雑さを解消し、システム全体の信頼性
をも向上させた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 provides a fuel cell power generation system that eliminates the uneconomicality and the complexity of the control mechanism in a multi-power generation system or a co-generation system that has a plurality of fuel cell power generation units, and that also improves the reliability of the entire system. The purpose is to do.
上記の目的を達成するために、本発明は 原燃料を改質して改質燃料を生成する複数の改質器と、
これら改質器それぞれから改質燃料の供給を受ける複数
の燃料電池と、これらの燃料電池で発生する熱を回収し
て蒸気を発生する電池冷却系統とを有し、この電池冷却
系統は発生した蒸気を分離する少なくとも一つの気水分
離器を有し、かつこの少なくとも一つの気水分離器には
電気ヒータが配設されており、この気水分離器で分離さ
れた蒸気は上記複数の改質器に供給されるように構成さ
れている燃料電池発電システムにおいて、 上記気水分離器で分離された蒸気が上記複数の改質器の
一部又は全部に選択的に供給されうるように接続されて
いることを特徴とする。In order to achieve the above object, the present invention comprises a plurality of reformers for reforming raw fuel to produce reformed fuel,
It has a plurality of fuel cells that receive reformed fuel from each of these reformers, and a cell cooling system that recovers the heat generated in these fuel cells to generate steam. There is at least one steam separator for separating steam, and the at least one steam separator is provided with an electric heater, and the steam separated by this steam separator has a plurality of steam generators. In a fuel cell power generation system configured to be supplied to a quality unit, the steam separated by the steam separator is connected so as to be selectively supplied to a part or all of the plurality of reformers. It is characterized by being.
第1図は本発明の一実施例を示す系統および回路構成図
であり、第3図と同一部分には同一符号を付してその説
明を省略し、ここでは異なる部分についてのみ述べる。
すなわち、第1図において15は各発電ユニットの気水分
離器11を連絡する蒸気管であり、その分枝管16および調
節弁あるいは遮断弁17(両者共設置される場合も含む)
を介して必要とする発電ユニットの改質器13に水蒸気を
供給することができるようになっている。電池冷却水系
7にある気水分離器11は1ユニット分のみの電気ヒータ
12を内蔵しており、他の発電ユニットは内蔵していな
い。もちろん電気ヒータ内蔵の気水分離器はどのユニッ
トにあっても良い。第1図は1台目の起動が終了した後
の2台目の起動途中の状態を示しており、弁17の中で黒
く塗ったものは閉じた状態を、また他の弁は開いた状態
を示している。FIG. 1 is a system and circuit configuration diagram showing an embodiment of the present invention. The same parts as those in FIG. 3 are designated by the same reference numerals, and the description thereof will be omitted. Only different parts will be described here.
That is, in FIG. 1, 15 is a steam pipe that connects the steam separator 11 of each power generation unit, and its branch pipe 16 and a control valve or shutoff valve 17 (including the case where both are installed)
The steam can be supplied to the reformer 13 of the power generation unit, which is required via the. The steam separator 11 in the battery cooling water system 7 is an electric heater for only one unit.
12 built in, no other power generation unit. Of course, the steam separator with built-in electric heater may be in any unit. Fig. 1 shows the state in which the second unit is in the process of starting up after the first unit has been started up. The black parts of valve 17 are closed, and the other valves are open. Is shown.
1台目の発電ユニットの起動が終了すると、電池セル2
の発熱で改質用蒸気をまかなうことができ電気ヒータ11
は不要となる。この電気ヒータ不要となる点は、厳密に
は第4図曲線21における75%定格負荷近辺であり、この
負荷も各発電システムによって異なるため以後の説明に
おける起動終了点とは電気ヒータが不要となる負荷まで
とった状態を指す。When the startup of the first power generation unit is completed, the battery cell 2
Electric heater that can cover reforming steam with heat generated by
Is unnecessary. Strictly speaking, the point where the electric heater is not necessary is around the 75% rated load in the curve 21 in FIG. 4, and since this load also differs depending on each power generation system, the electric heater is not necessary in the following explanation. It refers to the state where the load is taken.
この状態では、他ユニットへの蒸気供給は不要なので分
枝管16にある弁17は1台目を除いてすべて閉じている
が、2台目の起動に入ると2台目の弁のみが開いて起動
に必要な蒸気を供給する。但し気水分離器11から分枝管
16への連結管18にある弁19は電池側の発熱が少ない間は
閉じておき、蒸気が発生し始めたら、開ける。In this state, it is not necessary to supply steam to other units, so all valves 17 in the branch pipe 16 are closed except for the first unit, but when starting the second unit, only the second valve opens. Supply the steam required for startup. However, branch pipe from steam separator 11
The valve 19 on the connecting pipe 18 to 16 is closed while the heat generation on the battery side is small, and opened when steam starts to be generated.
この場合1台目の発電ユニットの余剰蒸気も利用できる
ので第4図の曲線23に示すように電気ヒータ12の消費電
力は少なくすることができる。In this case, since the surplus steam of the first power generation unit can be used, the power consumption of the electric heater 12 can be reduced as shown by the curve 23 in FIG.
3台目起動には1台目,2台目の余剰蒸気が使えるのでさ
らに電気ヒータ12の消費電力は少なくて済み、併設台数
によっては起動に電気ヒータの不要なユニットも出る可
能性がある。Since the excess steam of the first and second units can be used for starting the third unit, the power consumption of the electric heater 12 can be further reduced, and depending on the number of units installed, a unit that does not require the electric heater may appear.
一方、2台目の気水分離器11の蒸気発生量が増すにつれ
て弁17を絞りながら電気ヒータ12の負荷を減らして行き
自己補給に切り換える。また電気ヒータの容量に余裕の
出る負荷に達したならば3台目の起動を開始することが
できる。On the other hand, as the amount of steam generated in the second steam-water separator 11 increases, the valve 17 is throttled to reduce the load on the electric heater 12 and switch to self-replenishment. If the capacity of the electric heater reaches a sufficient load, the activation of the third heater can be started.
また本発明の他の実施例について、第2図に示すように
気水分離器11もまとめて全ユニットで1台とすれば、全
ユニット運転中の気水分離を行うだけの容量を確保する
ため内容積は若干大きくなるが、経済的効果も大きく、
システム・制御機構を更に単純にすることもできる。Further, in another embodiment of the present invention, as shown in FIG. 2, if the steam-water separator 11 is also integrated into one unit for all the units, a capacity sufficient to perform steam-water separation during operation of all the units is secured. Therefore, the internal volume is slightly larger, but the economic effect is also large,
The system and control mechanism can be further simplified.
以上説明したように、本発明によれば、マルチ発電シス
テムや熱併給発電システムにおいて大容量のヒータを複
数個使用する必要もなく、1台分の起動および部分負荷
に必要な容量でよく、経済性の大幅な改善と制御機構の
単純化による信頼性向上ができる燃料電池発電システム
を提供することができる。また2台目以降の起動には既
に起動を終了した各ユニットの余剰蒸気を利用すること
ができるので起動損失を小さくする効果もある。As described above, according to the present invention, it is not necessary to use a plurality of large-capacity heaters in a multi-generation system or a combined heat and power generation system, and the capacity required for starting one unit and partial load is sufficient. It is possible to provide a fuel cell power generation system in which reliability is greatly improved and reliability is improved by simplifying a control mechanism. Further, since the surplus steam of each unit which has already been started can be used for starting the second and subsequent units, there is an effect of reducing the starting loss.
第1図は本発明の一実施例を示す系統・回路構成図、第
2図は本発明の他の実施例を示す系統・回路構成図、第
3図は従来の燃料電池発電ユニットの概略系統・回路構
成図、第4図は負荷と発電ユニット不足蒸気量および電
気ヒータによる必要蒸発量の関係を示すグラフである。 1……燃料電池、2……燃料電池セル構成 6……インバータ、7……電池冷却水系統 10……電力系統、11……気水分離器 12……電気ヒータ、13……改質器 15……気水分離器連絡管、16……分枝管 17……調節弁,止め弁 18……気水分離器−分枝管連結管 19……調節弁,止め弁FIG. 1 is a system / circuit configuration diagram showing an embodiment of the present invention, FIG. 2 is a system / circuit configuration diagram showing another embodiment of the present invention, and FIG. 3 is a schematic system of a conventional fuel cell power generation unit. -Circuit configuration diagram, FIG. 4 is a graph showing the relationship between the load, the steam shortage in the power generation unit, and the required evaporation amount by the electric heater. 1 ... Fuel cell, 2 ... Fuel cell configuration 6 ... Inverter, 7 ... Battery cooling water system 10 ... Power system, 11 ... Steam separator 12 ... Electric heater, 13 ... Reformer 15 …… Air / water separator communication pipe, 16 …… Branch pipe 17 …… Control valve, stop valve 18 …… Air / water separator-branch pipe connecting pipe 19 …… Control valve, stop valve
Claims (1)
の改質器と、これら改質器それぞれから改質燃料の供給
を受ける複数の燃料電池と、これらの燃料電池で発生す
る熱を回収して蒸気を発生する電池冷却系統とを有し、
この電池冷却系統は発生した蒸気を分離する少なくとも
一つの気水分離器を有し、かつこの少なくとも一つの気
水分離器には電気ヒータが配設されており、この気水分
離器で分離された蒸気は上記複数の改質器に供給される
ように構成されている燃料電池発電システムにおいて、 上記気水分離器で分離された蒸気が上記複数の改質器の
一部又は全部に選択的に供給されうるように接続されて
いることを特徴とする燃料電池発電システム。1. A plurality of reformers for reforming a raw fuel to produce a reformed fuel, a plurality of fuel cells supplied with reformed fuel from each of the reformers, and a plurality of fuel cells generated by these fuel cells. Has a battery cooling system that recovers the heat that is generated and generates steam,
This battery cooling system has at least one steam separator for separating the generated steam, and an electric heater is provided in this steam separator, and the steam separator separates the steam. In the fuel cell power generation system configured such that the steam is supplied to the plurality of reformers, the steam separated by the steam-water separator is selectively supplied to some or all of the plurality of reformers. A fuel cell power generation system characterized in that the fuel cell power generation system is connected so as to be supplied to the fuel cell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60072554A JPH0760691B2 (en) | 1985-04-08 | 1985-04-08 | Fuel cell power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60072554A JPH0760691B2 (en) | 1985-04-08 | 1985-04-08 | Fuel cell power generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61232569A JPS61232569A (en) | 1986-10-16 |
| JPH0760691B2 true JPH0760691B2 (en) | 1995-06-28 |
Family
ID=13492689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60072554A Expired - Lifetime JPH0760691B2 (en) | 1985-04-08 | 1985-04-08 | Fuel cell power generation system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0760691B2 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3100768B2 (en) * | 1992-06-26 | 2000-10-23 | 関西電力株式会社 | Distributed fuel cell power plant and operation control method thereof |
| JPH0660896A (en) * | 1992-08-04 | 1994-03-04 | Mitsubishi Electric Corp | Fuel cell type power generation device and method for operation thereof |
| JP4081896B2 (en) * | 1998-12-02 | 2008-04-30 | トヨタ自動車株式会社 | Fuel cell system |
| JP4070903B2 (en) * | 1999-04-08 | 2008-04-02 | トヨタ自動車株式会社 | Fuel cell system and fuel cell heating method |
| JP3601399B2 (en) * | 2000-02-14 | 2004-12-15 | 日産自動車株式会社 | Fuel cell system |
| JP4751577B2 (en) * | 2004-03-24 | 2011-08-17 | 東京瓦斯株式会社 | Power generation system |
| JP4855730B2 (en) * | 2005-07-29 | 2012-01-18 | 株式会社東芝 | Hydrogen production system |
| JP5248711B2 (en) * | 2010-07-07 | 2013-07-31 | パナソニック株式会社 | Fuel cell system and operation method thereof |
| JP6812851B2 (en) * | 2017-03-02 | 2021-01-13 | ブラザー工業株式会社 | Fuel cell system and fuel cell |
| DE102021205718A1 (en) | 2021-06-07 | 2022-12-08 | Robert Bosch Gesellschaft mit beschränkter Haftung | Heatable container for storing a fluid |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4098960A (en) * | 1976-12-27 | 1978-07-04 | United Technologies Corporation | Fuel cell fuel control system |
| JPS59149670A (en) * | 1983-02-01 | 1984-08-27 | Toshiba Corp | Fuel battery power generating apparatus |
-
1985
- 1985-04-08 JP JP60072554A patent/JPH0760691B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61232569A (en) | 1986-10-16 |
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