JPS63128564A - Power generation process of solid electrolyte fuel battery module - Google Patents
Power generation process of solid electrolyte fuel battery moduleInfo
- Publication number
- JPS63128564A JPS63128564A JP61273643A JP27364386A JPS63128564A JP S63128564 A JPS63128564 A JP S63128564A JP 61273643 A JP61273643 A JP 61273643A JP 27364386 A JP27364386 A JP 27364386A JP S63128564 A JPS63128564 A JP S63128564A
- Authority
- JP
- Japan
- Prior art keywords
- module
- cell
- hydrogen
- cells
- air preheater
- 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
- 238000010248 power generation Methods 0.000 title claims abstract description 7
- 239000000446 fuel Substances 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims description 10
- 239000007784 solid electrolyte Substances 0.000 title claims description 7
- 239000001257 hydrogen Substances 0.000 claims abstract description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 27
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000011261 inert gas Substances 0.000 claims abstract description 11
- 239000007800 oxidant agent Substances 0.000 claims abstract description 11
- 230000005611 electricity Effects 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 10
- 239000001301 oxygen Substances 0.000 abstract description 10
- 229910052760 oxygen Inorganic materials 0.000 abstract description 10
- 230000001590 oxidative effect Effects 0.000 abstract description 3
- 239000002912 waste gas Substances 0.000 abstract 2
- 150000002431 hydrogen Chemical class 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、固体電解質燃料電池モジュールの発電方法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method of generating electricity using a solid electrolyte fuel cell module.
[従来の技術と問題点]
周知の如く、固体電解質燃料電池(以下、5OFCとい
う)は一般にその他の燃料電池(第1世代・・・りん酸
型PAFC,第2世代溶融炭酸塩型MCFC)と比べて
第3世代の燃料電池と考えられており、その技術確立は
約20〜30年後とされている。従って、確立されてい
ない技術が多々ある。[Prior Art and Problems] As is well known, solid oxide fuel cells (hereinafter referred to as 5OFC) are generally different from other fuel cells (first generation...phosphoric acid type PAFC, second generation molten carbonate type MCFC). In comparison, it is considered a third-generation fuel cell, and the technology is expected to be established in about 20 to 30 years. Therefore, there are many technologies that have not yet been established.
本発明は5OFGモジユールの燃料水素、空気及び排出
ガスなどの系統、処理といった未確立の技術について基
本的なアイデアを示すものであり、下記に列挙する技術
的課題が挙げられる。The present invention presents a basic idea regarding unestablished technology such as systems and processing of fuel hydrogen, air, exhaust gas, etc. of the 5OFG module, and the technical problems listed below are posed.
■5OFGモジュール内では酸素と未反応の水素が存在
することから、これがモジュール外部へリークして爆発
雰囲気となることがあり、これを防がなければならない
。(5) Since oxygen and unreacted hydrogen exist within the OFG module, this may leak to the outside of the module and create an explosive atmosphere, which must be prevented.
■モジュール内のガス温度は発電セルの性能面から約9
00〜1000℃に制御される。しかるに、モジュール
内には排出ガスの熱回収を回る為に酸化剤である空気を
昇温させる為の空気予熱器が設けであるが、空気予熱器
出口のガス温度は数100’Cと高いものであることか
ら、より一層の排ガス熱回収が必要である。一つの手段
として、モジュール内部の空気予熱器を大容邑化するこ
とが考えられるが、これではモジュールが大形化し、モ
ジュールのコンパクト化という目的が失われると同時に
、モジュールの大形化により高温に耐える高級材料を多
」に使用せねばならず経済的にも不利になる。■The gas temperature inside the module is approximately 9% due to the performance of the power generation cell.
The temperature is controlled at 00-1000°C. However, although an air preheater is installed inside the module to raise the temperature of the air, which is an oxidizer, in order to recover heat from exhaust gas, the gas temperature at the outlet of the air preheater is as high as several 100'C. Therefore, even more exhaust gas heat recovery is required. One possible solution is to increase the capacity of the air preheater inside the module, but this would make the module larger and lose the purpose of making the module more compact. This requires the use of a large amount of high-quality materials that can withstand high temperatures, which is economically disadvantageous.
■5OFC出力はセル周囲の燃料水素濃度や雰囲気温度
に依存する。しかるに、これらを別個に制御することは
比較的容易であり、例えば水素濃度調整には不活性ガス
投入、雰囲気温度調整にはヒータによる熱投入、空気、
水素によるモジュールの冷却が考えられるが、これは設
備の大型化を招く。■5OFC output depends on fuel hydrogen concentration and ambient temperature around the cell. However, it is relatively easy to control these separately; for example, to adjust the hydrogen concentration, inert gas is added, and to adjust the ambient temperature, heat is input by a heater, air,
Cooling the module using hydrogen could be considered, but this would lead to an increase in the size of the equipment.
■5OFG出力はセル周囲の酸素濃度にも依存するが、
空気がモジュール内にてセルと垂直に流れる場合には空
気上流側のセルでは酸素濃度が高く大出力が得られ、下
流側のセルでは酸素濃度が低く小出力しか得られないこ
とになって出力アンバランスが生じる。■5OFG output also depends on the oxygen concentration around the cell,
When air flows perpendicular to the cells in the module, the cells on the upstream side have a high oxygen concentration and can produce high output, while the downstream cells have low oxygen concentration and can only produce a small output. An imbalance occurs.
本発明は上記事情に鑑みてなされたもので、モジュール
外部への水素リークの防止、モジュールのコンパクト化
並びに各セルの出力の均一化を図るとともに、セル周囲
の水素濃度、雰囲気温度を同時に制御し得る固体電解質
燃料電池モジュールの発電方法を提供することを目的と
する。The present invention was made in view of the above circumstances, and aims to prevent hydrogen leakage to the outside of the module, make the module more compact, and equalize the output of each cell, and simultaneously control the hydrogen concentration and ambient temperature around the cells. The present invention aims to provide a method for generating electricity using a solid electrolyte fuel cell module.
[問題点を解決するための手段]
本発明は、複数のセル、高温空気予熱器を配設した固体
電解質燃料電池モジュールを発電する方法において、前
記モジュール外部に低温空気予熱器を配設するとともに
、前記モジュール内圧を大気圧と同程度以下に制御し、
かつ不活性ガスを混入した水素をモジュール内へ送給し
、しかも前記セル同志の中間に酸化剤を投入することを
要旨とする。[Means for Solving the Problems] The present invention provides a method for generating electricity using a solid oxide fuel cell module in which a plurality of cells and a high-temperature air preheater are disposed, in which a low-temperature air preheater is disposed outside the module. , controlling the internal pressure of the module to be equal to or lower than atmospheric pressure,
The gist of this method is to feed hydrogen mixed with an inert gas into the module, and to inject an oxidizing agent between the cells.
[作用]
本発明によれば、
■平行通風方式の作用により、モジュール外部への水素
リークを防止できる。[Function] According to the present invention, (1) Hydrogen leakage to the outside of the module can be prevented by the parallel ventilation method.
■モジュール外部に低温空気予熱器を採用し酸化剤であ
る空気との熱交換を図ることにより、モジュールのコン
パクト化を図ることができる。■The module can be made more compact by using a low-temperature air preheater outside the module to exchange heat with air, which is an oxidizing agent.
■水素に不活性ガスを混入する方法を採用することによ
り、セル周囲の水素濃度、雰囲気温度を同時に制御でき
る。■ By using a method of mixing inert gas with hydrogen, the hydrogen concentration and ambient temperature around the cell can be controlled simultaneously.
■セル同志の中間に酸化剤を投入することにより、各セ
ルの主力の均一化を図ることができる。- By introducing an oxidizing agent between the cells, it is possible to equalize the main power of each cell.
[実施例] 以下、本発明の一実施例を図を参照して説明する。[Example] An embodiment of the present invention will be described below with reference to the drawings.
図は、5OFCモジユールの説明図である。図中の1は
、複数のセル2・・・及び高温空気予熱器3を配設した
ガス流れ直交型5OFCモジユールである。前記セル2
・・・には、反応不活性ガス(例えば窒素)4を混入し
た水素5が導入される。前記モジュール1の外部には、
低温空気予熱器6が設けられている。また、前記モジュ
ール1の外部には押し込み通風ファン7が設けられ、こ
のファン7から酸化剤空気が低温空気予熱器6及び高温
空気予熱器3を通ってセル2内部へ導かれる。更に、前
記モジュール1の外部には、該モジュール1に入口ダン
パ8を介して連結された誘引通風ファン9、煙突10が
夫々設けられている。The figure is an explanatory diagram of the 5OFC module. 1 in the figure is a gas flow orthogonal type 5OFC module in which a plurality of cells 2 . . . and a high-temperature air preheater 3 are arranged. Said cell 2
... is introduced with hydrogen 5 mixed with a reactive inert gas (for example, nitrogen) 4. Outside the module 1,
A cold air preheater 6 is provided. Further, a forced draft fan 7 is provided outside the module 1, and the oxidizer air is guided from the fan 7 into the cell 2 through the low temperature air preheater 6 and the high temperature air preheater 3. Furthermore, an induced draft fan 9 and a chimney 10 connected to the module 1 via an inlet damper 8 are provided outside the module 1, respectively.
本実施例においては、こうした5OFCモジユールを用
いて、まず反応不活性ガス4を混入した水素5をセル2
の内部に導入する。一方、酸化剤空気は前記ファン7に
より低温空気予熱器6及び高温空気予熱器3へ送られ、
ここで排出ガス11と熱交換を行う。また、モジュール
1の内部へ導かれた水素と空気は、セル2にて発電反応
に利用される。この時、反応不活性ガス4によりセル2
周囲の水素濃度と温度雰囲気が最適に制御され、またセ
ル2間に投入される空気(又は酸素)12によってセル
2の周囲の酸素濃度が制御され、各セル2の出力が十分
かつ均一となる様に制御される。更に、発電反応生成ガ
スいわゆる排出ガス11は空気との熱交換後ファン9へ
導かれ、煙突10から大気へ放出される。このとき、モ
ジュミル1の内圧は、前記入口ダンパ8を動作させてフ
ァン9の吐出圧を変化させることによって、大気圧と同
程度以下に制御される。In this example, using such a 5OFC module, hydrogen 5 mixed with reaction inert gas 4 was first introduced into the cell 2.
to be introduced inside. On the other hand, the oxidant air is sent to the low temperature air preheater 6 and the high temperature air preheater 3 by the fan 7,
Here, heat exchange is performed with the exhaust gas 11. Furthermore, the hydrogen and air introduced into the module 1 are used in the cell 2 for a power generation reaction. At this time, the cell 2 is
The surrounding hydrogen concentration and temperature atmosphere are optimally controlled, and the oxygen concentration around the cells 2 is controlled by the air (or oxygen) 12 injected between the cells 2, so that the output of each cell 2 is sufficient and uniform. controlled in a similar manner. Furthermore, the gas produced by the power generation reaction, so-called exhaust gas 11, is guided to the fan 9 after heat exchange with the air, and is discharged into the atmosphere from the chimney 10. At this time, the internal pressure of the Modumil 1 is controlled to be equal to or lower than atmospheric pressure by operating the inlet damper 8 and changing the discharge pressure of the fan 9.
上記実施例によれば、以下に列挙する効果を有する。According to the above embodiment, the effects listed below are obtained.
■モジュール1の内圧を大気圧と同程度以下に制御する
平行通風方式を採用することにより、モジュール1外へ
の水素のリークを防止できる。(2) By adopting a parallel ventilation system that controls the internal pressure of the module 1 to be equal to or lower than atmospheric pressure, leakage of hydrogen to the outside of the module 1 can be prevented.
■モジュール1の外部に低温空気予熱器6を採用して酸
化剤である空気との熱交換を図るため、モジュール1を
コンパクト化できる。(2) The module 1 can be made more compact because a low-temperature air preheater 6 is installed outside the module 1 to exchange heat with air, which is an oxidizing agent.
■水素5に不活性ガス4を混入するため、セル1の周囲
の水素濃度と雰囲気温度を同時に制御できる。(2) Since the inert gas 4 is mixed into the hydrogen 5, the hydrogen concentration and ambient temperature around the cell 1 can be controlled at the same time.
■セル2同志の中間に酸化剤(空気、酸素)を投入する
ため、セルの出力を均一化できる。■Since the oxidizing agent (air, oxygen) is injected between the two cells, the output of the cells can be made uniform.
[発明の効果]
以上詳述した如く本発明によれば、モジュール外部への
水素リークの防止、モジュールのコンパクト化、各セル
の出力の均一化を図るとともに、セル周囲の水素濃度雰
囲気温度を同時に制御し得る固体電解質燃料電池モジュ
ールの発電方法を提iム、□4゜、4゜[Effects of the Invention] As detailed above, according to the present invention, hydrogen leakage to the outside of the module is prevented, the module is made compact, the output of each cell is made uniform, and the hydrogen concentration atmosphere temperature around the cells is simultaneously adjusted. We propose a controllable power generation method using a solid electrolyte fuel cell module, □4゜, 4゜
図は本発明に係る固体電解質燃料電池モジュールの説明
図である。
1・・・5OFCモジユール、2・・・セル、3・・・
高温空気予熱器、4・・・反応不活性ガス、5・・・水
素、6・・・低温空気予熱器、7・・・押込通風ファン
、8・・・入口ダンパ、9・・・誘引通風ファン、10
・・・煙突、11・・・排出ガス、12・・・空気(又
は酸素)。The figure is an explanatory diagram of a solid electrolyte fuel cell module according to the present invention. 1...5 OFC module, 2... cell, 3...
High temperature air preheater, 4... Reactive inert gas, 5... Hydrogen, 6... Low temperature air preheater, 7... Forced draft fan, 8... Inlet damper, 9... Induced draft fan, 10
...Chimney, 11...Exhaust gas, 12...Air (or oxygen).
Claims (1)
電池モジュールを発電する方法において、前記モジュー
ル外部に低温空気予熱器を配設するとともに、前記モジ
ュール内圧を大気圧と同程度以下に制御する平行通風方
式を採用し、かつ不活性ガスを混入した水素を前記モジ
ュール内へ送給し、しかも前記セル同志間に酸化剤を投
入することを特徴とする固体電解質燃料電池モジュール
の発電方法。In a method for generating electricity using a solid electrolyte fuel cell module equipped with a plurality of cells and a high-temperature air preheater, a low-temperature air preheater is disposed outside the module, and the internal pressure of the module is controlled to be equal to or lower than atmospheric pressure. A power generation method using a solid electrolyte fuel cell module, which adopts a parallel ventilation system, supplies hydrogen mixed with an inert gas into the module, and injects an oxidizing agent between the cells.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61273643A JPS63128564A (en) | 1986-11-17 | 1986-11-17 | Power generation process of solid electrolyte fuel battery module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61273643A JPS63128564A (en) | 1986-11-17 | 1986-11-17 | Power generation process of solid electrolyte fuel battery module |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63128564A true JPS63128564A (en) | 1988-06-01 |
Family
ID=17530546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61273643A Pending JPS63128564A (en) | 1986-11-17 | 1986-11-17 | Power generation process of solid electrolyte fuel battery module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63128564A (en) |
-
1986
- 1986-11-17 JP JP61273643A patent/JPS63128564A/en active Pending
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