JPS62234871A - Fuel cell power generating plant - Google Patents
Fuel cell power generating plantInfo
- Publication number
- JPS62234871A JPS62234871A JP61076581A JP7658186A JPS62234871A JP S62234871 A JPS62234871 A JP S62234871A JP 61076581 A JP61076581 A JP 61076581A JP 7658186 A JP7658186 A JP 7658186A JP S62234871 A JPS62234871 A JP S62234871A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- air
- fuel cell
- supplied
- exhaust gas
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 62
- 239000007789 gas Substances 0.000 claims abstract description 24
- 238000002485 combustion reaction Methods 0.000 claims abstract description 17
- 238000010248 power generation Methods 0.000 claims abstract description 8
- 238000002407 reforming Methods 0.000 claims abstract description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 150000002430 hydrocarbons Chemical class 0.000 claims 1
- 239000001301 oxygen Substances 0.000 abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 abstract description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 12
- 239000011261 inert gas Substances 0.000 abstract description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、燃料電池発電プラントに係り、特にその運転
圧力、運転温度が高圧、高温の燃料電池発電プラントに
関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a fuel cell power generation plant, and particularly to a fuel cell power generation plant whose operating pressure and operating temperature are high pressure and high temperature.
リン酸型燃料電池においては、その電池内に白金又は白
金系合金の貴金属触媒が使用されており、電池的酸性電
解液中の高電位雰囲気において、貴金属粒子が凝集し劣
化を生じることが知られている。また燃料電池はその電
圧−電流特性上、電流が低い領域つまり負荷の低い領域
において電圧が高くなる性質をもっている。従って、負
荷がある値以下に低くなると電池内の触媒が高電位にさ
られることとなり、型部性能の著しい低下をまねくこと
となる。これまで燃料電池の低負荷運転時における電池
電圧の抑性手段として様々な手段が提案されてきた。燃
料電池の特性として、電池の運転圧力、運転温度、空気
極供給空気中の酸素濃度。In phosphoric acid fuel cells, a noble metal catalyst of platinum or platinum-based alloy is used in the cell, and it is known that noble metal particles agglomerate and deteriorate in the high potential atmosphere in the acidic electrolyte of the cell. ing. Further, due to its voltage-current characteristics, a fuel cell has a property that the voltage is high in a region where the current is low, that is, a region where the load is low. Therefore, if the load falls below a certain value, the catalyst within the battery will be exposed to a high potential, resulting in a significant drop in the performance of the mold section. Until now, various means have been proposed as means for suppressing the cell voltage during low-load operation of the fuel cell. Characteristics of fuel cells include cell operating pressure, operating temperature, and oxygen concentration in the air supplied to the air electrode.
燃料極供給燃料中の水素濃度、水素利用率、酸素利用率
等により電池電圧が変化することが知られており、これ
らの特性を利用して電池電圧の抑制をはかることができ
る。この内電池の空気極への供給空気中の酸素濃度を変
化させることにより、低負荷時における電池電圧の抑制
制御を行なうことが、応答性、電池性能への影響などの
面から最も好ましいとされている。It is known that the battery voltage changes depending on the hydrogen concentration, hydrogen utilization rate, oxygen utilization rate, etc. in the fuel supplied to the fuel electrode, and these characteristics can be used to suppress the battery voltage. Of these, controlling the battery voltage during low loads by changing the oxygen concentration in the air supplied to the air electrode of the battery is considered the most preferable from the viewpoint of responsiveness and impact on battery performance. ing.
空気極への供給空気中の酸素濃度を制御して電池電圧の
上昇を抑制する方法として１例えば特公昭６０−１０４
２５号公報に示されるように再循環ブロアを用いて、電
池の空気極出口の低酸素濃度のガスを空気極入口へ循環
させ空気極供給空気中の酸素濃度を下げる方法が知られ
ている。この方法では、空気極入口の空気に比べ圧力の
低い空気極出口のガスを該空気極入口へ戻す為に再循環
ブロアが必要となる。このブロアは電池の運転温度、運
転圧力とほぼ等しい、高温、高圧のガスを取扱うことに
なるため、軸受のシール構造及び耐熱性の面で特殊な構
造を要求され、又ブロア本体の運転制御、保護の面から
系統が複雑化するなどの問題点が有った。As a method for suppressing the rise in battery voltage by controlling the oxygen concentration in the air supplied to the air electrode, for example, Japanese Patent Publication No. 60-104
As shown in Japanese Patent No. 25, a method is known in which a recirculation blower is used to circulate gas having a low oxygen concentration at the air electrode outlet of the battery to the air electrode inlet to lower the oxygen concentration in the air supplied to the air electrode. This method requires a recirculation blower to return the gas at the air electrode outlet, which has a lower pressure than the air at the air electrode inlet, to the air electrode inlet. Since this blower handles high-temperature, high-pressure gas that is approximately equal to the operating temperature and pressure of the battery, it requires a special structure in terms of bearing seal structure and heat resistance, and also requires a special structure in terms of bearing seal structure and heat resistance. There were problems in terms of protection, such as the complexity of the system.
本発明の目的は、このような再循環ブロアを使用するこ
となく、燃料電池の低負荷運転時における電池電圧の上
昇を抑制することにある。An object of the present invention is to suppress the increase in cell voltage during low-load operation of a fuel cell without using such a recirculation blower.
本発明は、燃料改質器の燃焼部からの排出ガスが、窒素
、二酸化炭素を主成分とする高圧の不活性ガスであるこ
とに着目し、燃焼部から排出ガスを電池の空気極への供
給空気に混合することにより、供給空気中の酸素濃度を
下げ、低負荷運転時における電池電圧の上昇抑制を行な
うようにするものである。The present invention focuses on the fact that exhaust gas from the combustion section of a fuel reformer is a high-pressure inert gas containing nitrogen and carbon dioxide as its main components, and directs the exhaust gas from the combustion section to the air electrode of the battery. By mixing it with the supplied air, the oxygen concentration in the supplied air is lowered, thereby suppressing the increase in battery voltage during low load operation.
本発明の一実施例を第１図を参照して説明する。 An embodiment of the present invention will be described with reference to FIG.
外部から該プラントへ供給される天然ガスは。Natural gas is supplied to the plant from outside.
制御弁２６によって所定の流量に制御されて燃料改質器
１の反応部１ａへ供給される０反応部１ａから出力され
たガスは、熱交換器５ａ−４高温ＣＯ変成器３→熱交換
器５ｂ→高温ＣＯ変成器４→熱交換器５ｃ、５ｄを経て
水素を主成分とする燃料ガスに改質された後に、気水分
離器６により脱水され、更に熱交換器５Ｃを経た後に制
御弁２８で流量制御されて燃料電池７の燃料極７ａに供
給される。燃料極７ａにおいて電池出力相当量の水素が
消費された後に余剰の水素を含む燃料ガスは該燃料極７
ａから排出され、補助燃焼′Ｄ１３へ送られて燃料とし
て使用される。The gas output from the reaction section 1a is controlled to a predetermined flow rate by the control valve 26 and is supplied to the reaction section 1a of the fuel reformer 1. 5b → high temperature CO shift converter 4 → heat exchangers 5c and 5d, after which the fuel gas is reformed into hydrogen-based fuel gas, dehydrated by the steam-water separator 6, further passed through the heat exchanger 5C, and then the control valve The flow rate is controlled at 28 and the fuel is supplied to the fuel electrode 7a of the fuel cell 7. After the amount of hydrogen equivalent to the battery output is consumed at the fuel electrode 7a, the fuel gas containing surplus hydrogen is transferred to the fuel electrode 7a.
It is discharged from a and sent to the auxiliary combustion 'D13 to be used as fuel.
一方、空気は圧縮機１１により所定の圧力まで加圧され
た後に制御弁２１で所定の流量に制御され流量計１９を
経て補記燃料電池７の空気ｔ＠ ７ ｂに供給される。On the other hand, air is pressurized to a predetermined pressure by the compressor 11, then controlled to a predetermined flow rate by the control valve 21, and is supplied to the air t@7b of the supplementary fuel cell 7 via the flow meter 19.
空気極７ｂにおいて電池出力相当分の酸素が消費された
後に排出され、前記補助燃焼器１３へ燃焼用空気として
供給される。After oxygen equivalent to the battery output is consumed in the air electrode 7b, it is exhausted and supplied to the auxiliary combustor 13 as combustion air.
前記燃料改質器１の燃焼部１ｂへの燃料は、外部から供
給される天然ガスを制御弁２５で所定の流量に制御して
供給され、空気は前記圧縮４！ｉｌｌから熱交換器５ｅ
を経た後に制御弁２３で流量制御されて前記補助燃焼器
１３へ供給される。燃焼部１ｂからの排出ガスは前記熱
交換器５θを経た後に制御弁２３で流量制御されて前記
補助燃焼器１３へ供給される。補助燃焼器１３八は圧縮
機１１からの加圧空気も制御弁２９を介して供給され、
その排出ガスはタービン１２を回転させて前記圧縮機１
１を駆動する。Fuel to the combustion section 1b of the fuel reformer 1 is supplied by controlling natural gas supplied from the outside to a predetermined flow rate with a control valve 25, and air is supplied by the compression 4! ill to heat exchanger 5e
After that, the flow rate is controlled by a control valve 23 and the fuel is supplied to the auxiliary combustor 13. After passing through the heat exchanger 5θ, the exhaust gas from the combustion section 1b is supplied to the auxiliary combustor 13 with its flow rate controlled by the control valve 23. The auxiliary combustor 138 is also supplied with pressurized air from the compressor 11 via the control valve 29,
The exhaust gas rotates the turbine 12 and the compressor 1
Drive 1.
また、前記燃料改質ｗ１１の燃焼部１ｂからの排出ガス
は前記熱交換器５ｅを経た後に分岐され。Further, the exhaust gas from the combustion section 1b of the fuel reforming w11 is branched after passing through the heat exchanger 5e.
制御弁２２で流量制御された後に流量計２０を経て前記
空気極７ｂへの供給空気に混入される。After its flow rate is controlled by a control valve 22, it passes through a flowmeter 20 and is mixed into the air supplied to the air electrode 7b.
燃料電池７の電池電圧Ｖは電圧計１７により検出され、
電池電流工は電流計１８で検出される。The battery voltage V of the fuel cell 7 is detected by a voltmeter 17,
Battery current is detected by an ammeter 18.
演算器３０は電池電圧Ｖ、電池電流Ｉの検出値を入力し
、電池電流工に基づいて燃料電池７の燃料極７ａへの燃
料供給量および空気極７ｂへの空気供給量を演算して制
御袋Ｗ１１６に制御目標値を設定し、ｔｆｔ池電圧Ｖを
監視してその値が許暮値Ｖｔを越えた場合には供給空気
に前記燃焼部１ｂからの排ガスを混入するように制御表
ｒｉ１６に混入制御信号を与える。制御装置１６は、前
記制御目標値、混入制御信号および流量計１９．２０か
らの計量信号を入力して、制御弁２１，２２．２８の開
閉（開度）を制御する。The calculator 30 inputs the detected values of the battery voltage V and the battery current I, and calculates and controls the amount of fuel supplied to the fuel electrode 7a and the amount of air supplied to the air electrode 7b of the fuel cell 7 based on the battery current value. A control target value is set in the bag W116, and the control table ri16 is configured to monitor the TFT battery voltage V and mix the exhaust gas from the combustion section 1b into the supplied air when the value exceeds the tolerance value Vt. Provides a contamination control signal. The control device 16 inputs the control target value, the mixing control signal, and the measurement signal from the flowmeter 19.20, and controls the opening/closing (opening degree) of the control valves 21, 22, 28.
燃料電池７のクーラ７Ｃを冷却する冷却水は、水蒸気分
離器１４から冷却水ポンプ１５を介してクーラ７Ｃに送
られ、クーラ７Ｃから排出された冷却水は更に熱交換器
５ａ、５ｂおよび制御弁１０を経て水蒸気分離器１４に
戻る閉路を循環する、そして、水蒸気分離ｌｌ１１４で
分離された水蒸気は、制御弁２７を介して前記燃料改質
器１の反応部１ａへの供給ガスに混入される。The cooling water that cools the cooler 7C of the fuel cell 7 is sent from the steam separator 14 to the cooler 7C via the cooling water pump 15, and the cooling water discharged from the cooler 7C is further sent to the heat exchangers 5a, 5b and the control valve. 10 and returns to the steam separator 14, and the steam separated by the steam separator 114 is mixed into the gas supplied to the reaction section 1a of the fuel reformer 1 via the control valve 27. .
以上のような燃料電池発電プラントにおいて、前記制御
装置１６は、燃料極７ａへの燃料供給量および空気極７
ｂへの空気供給量が電池電流■に応じて設定された制御
目標値となるように、制御弁２１．２８の開度を制御す
る。１’！！池電気Ｖが許容値ｖ１以下である場合には
制御弁２２は閉止状態にある。In the fuel cell power generation plant as described above, the control device 16 controls the amount of fuel supplied to the fuel electrode 7a and the amount of fuel supplied to the air electrode 7a.
The opening degrees of the control valves 21 and 28 are controlled so that the amount of air supplied to b becomes the control target value set according to the battery current (2). 1'! ! When the battery electricity V is below the allowable value v1, the control valve 22 is in a closed state.
負荷が低下して電池電流工が小さくなり、それに伴って
型部電圧Ｖが上昇して許容値ＶＬを越えると演算器３０
は前記混入制御信号を発生する。When the load decreases and the battery current becomes smaller, and the mold section voltage V rises and exceeds the allowable value VL, the calculator 30
generates the contamination control signal.
制御装置ｒｆ１６はこの混入制御信号に応動して制御弁
２２を開け、燃料改質器１の燃焼部１ｂから排出される
高圧のガスを空気極７ｂへの供給空気中に混入する。こ
の排出ガスは低酸素の不活性ガスであることから、これ
により空気極７ｂへ供給される酸素量が減少し電池電圧
Ｖの上昇が抑制される。従って、この排出ガスの混入は
、型部電圧■が許容値Ｖｚ以下となるように制御される
。The control device rf16 opens the control valve 22 in response to this mixing control signal, and mixes the high pressure gas discharged from the combustion section 1b of the fuel reformer 1 into the air supplied to the air electrode 7b. Since this exhaust gas is a low-oxygen inert gas, the amount of oxygen supplied to the air electrode 7b is thereby reduced and an increase in the battery voltage V is suppressed. Therefore, the mixing of this exhaust gas is controlled so that the mold section voltage (2) is below the allowable value Vz.
第２図は本発明の他の実施例を示すもので、前述の実施
例において説明した燃焼部１ｂからの排出ガスを空気極
７ｂへの供給空気に混入させるための供給経路、すなわ
ち熱交換器５ｅと制御弁２２の間に冷却装ｖｌｔ３１を
介在させた例である。FIG. 2 shows another embodiment of the present invention, in which a supply path for mixing the exhaust gas from the combustion section 1b explained in the previous embodiment with the air supplied to the air electrode 7b, that is, a heat exchanger is shown. This is an example in which a cooling device vlt31 is interposed between the control valve 5e and the control valve 22.
このようにすれば、供給空気に混入する排出ガスの温度
を所定の温度に低下させることができ、制御弁２２、流
量計２０および燃料電池７の耐熱対策が容易になる。In this way, the temperature of the exhaust gas mixed in the supplied air can be lowered to a predetermined temperature, and heat resistance measures for the control valve 22, flowmeter 20, and fuel cell 7 can be easily taken.
以上のように、本発明によれば、燃料改質器の燃焼部か
ら排出される高圧のガスをそのガス圧を利用して燃料電
池空気極への供給空気に混入するようにしたので、プロ
ア等の補機な使用することなく低負荷運転時の電池電圧
の過」−昇を抑制することができ、従って装置が簡易に
なって発電プラントの信頼性が向上する。As described above, according to the present invention, the high-pressure gas discharged from the combustion section of the fuel reformer is mixed into the air supplied to the fuel cell air electrode using the gas pressure. Excessive rise in battery voltage during low-load operation can be suppressed without the use of auxiliary equipment such as auxiliary equipment, thus simplifying the device and improving the reliability of the power plant.
第１図および第２図は本発明のそれぞれ異なる各実施例
を示す燃料電池発電システムの系統図である。FIGS. 1 and 2 are system diagrams of fuel cell power generation systems showing different embodiments of the present invention.
Claims (1)
主成分とする燃料を水素を主成分とする燃料へ改質する
反応部及び該反応部へ熱を供給する燃焼部とを有する燃
料改質器と、空気を少なくとも大気圧以上に圧縮する圧
縮機と、前記燃料改質器の反応部より供給される水素を
主成分とする燃料を所定の圧力、温度、流量に制御して
前記燃料電池の燃料極へ供給する燃料供給装置と、前記
圧縮機より供給される空気を所定の圧力、温度、流量に
制御して前記燃料電池の空気却へ供給する空気供給装置
とを備えた燃料電池発電プラントにおいて、前記燃料改
質器の燃焼部からの排出ガスの少なくとも一部を燃料電
池の空気極への供給空気へ合流させる系統及び制御装置
を設けたことを特徴とする燃料電池発電プラント。 ２、特許請求の範囲第１項において、前記燃料改質器の
燃焼部からの排出ガスを空気極への供給空気へ合流させ
る系統は、燃料改質器の燃焼部からの排出ガスを所定の
温度に冷却する冷却装置を備えことを特徴とする燃料電
池発電プラント。[Claims] 1. A fuel cell having a fuel electrode and an air electrode, a reaction section for reforming fuel containing hydrocarbon as a main component into fuel containing hydrogen as a main component, and supplying heat to the reaction section a fuel reformer having a combustion section that compresses air, a compressor that compresses air to at least atmospheric pressure, and a fuel mainly composed of hydrogen supplied from a reaction section of the fuel reformer at a predetermined pressure and temperature. a fuel supply device that controls the flow rate and supplies the air to the fuel electrode of the fuel cell; and a fuel supply device that controls the air supplied from the compressor to a predetermined pressure, temperature, and flow rate and supplies the air to the air outlet of the fuel cell. A fuel cell power generation plant equipped with a supply device, further comprising a system and a control device for merging at least part of the exhaust gas from the combustion section of the fuel reformer into the air supplied to the air electrode of the fuel cell. Features of fuel cell power generation plant. 2. In claim 1, the system for merging the exhaust gas from the combustion section of the fuel reformer with the air supplied to the air electrode is configured to combine the exhaust gas from the combustion section of the fuel reformer into a predetermined A fuel cell power generation plant characterized by being equipped with a cooling device that cools the plant to a certain temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61076581A JPS62234871A (en) | 1986-04-04 | 1986-04-04 | Fuel cell power generating plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61076581A JPS62234871A (en) | 1986-04-04 | 1986-04-04 | Fuel cell power generating plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS62234871A true JPS62234871A (en) | 1987-10-15 |
Family
ID=13609243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61076581A Pending JPS62234871A (en) | 1986-04-04 | 1986-04-04 | Fuel cell power generating plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62234871A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991010266A2 (en) * | 1989-12-29 | 1991-07-11 | International Fuel Cells Corporation | Use and composition of a reactant gas to control fuel cell potential |
| WO1991010267A2 (en) * | 1989-12-29 | 1991-07-11 | International Fuel Cells Corporation | Air ejector system for fuel cell passivation |
| CN113632269A (en) * | 2019-03-27 | 2021-11-09 | 日产自动车株式会社 | Fuel cell system and control method of fuel cell system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61168877A (en) * | 1985-01-23 | 1986-07-30 | Hitachi Ltd | Fuel cell system |
| JPS6280970A (en) * | 1985-10-02 | 1987-04-14 | Ishikawajima Harima Heavy Ind Co Ltd | Power generating method of fuel cell |
| JPS62150662A (en) * | 1985-12-24 | 1987-07-04 | Ishikawajima Harima Heavy Ind Co Ltd | Normal pressure type fuel cell power generation plant |
-
1986
- 1986-04-04 JP JP61076581A patent/JPS62234871A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61168877A (en) * | 1985-01-23 | 1986-07-30 | Hitachi Ltd | Fuel cell system |
| JPS6280970A (en) * | 1985-10-02 | 1987-04-14 | Ishikawajima Harima Heavy Ind Co Ltd | Power generating method of fuel cell |
| JPS62150662A (en) * | 1985-12-24 | 1987-07-04 | Ishikawajima Harima Heavy Ind Co Ltd | Normal pressure type fuel cell power generation plant |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991010266A2 (en) * | 1989-12-29 | 1991-07-11 | International Fuel Cells Corporation | Use and composition of a reactant gas to control fuel cell potential |
| WO1991010267A2 (en) * | 1989-12-29 | 1991-07-11 | International Fuel Cells Corporation | Air ejector system for fuel cell passivation |
| CN113632269A (en) * | 2019-03-27 | 2021-11-09 | 日产自动车株式会社 | Fuel cell system and control method of fuel cell system |
| CN113632269B (en) * | 2019-03-27 | 2024-02-27 | 日产自动车株式会社 | Fuel cell system and control method for fuel cell system |
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