JPH07161371A - Method and apparatus for controlling temperature of fuel cell - Google Patents
Method and apparatus for controlling temperature of fuel cellInfo
- Publication number
- JPH07161371A JPH07161371A JP5309562A JP30956293A JPH07161371A JP H07161371 A JPH07161371 A JP H07161371A JP 5309562 A JP5309562 A JP 5309562A JP 30956293 A JP30956293 A JP 30956293A JP H07161371 A JPH07161371 A JP H07161371A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- fuel cell
- cathode
- gas
- 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.)
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Classifications
-
- 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
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- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、燃料電池の温度制御方
法及び装置に係わり、更に詳しくは、溶融炭酸塩型燃料
電池の温度制御方法及び装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a temperature control method and apparatus for a fuel cell, and more particularly to a temperature control method and apparatus for a molten carbonate fuel cell.
【0002】[0002]
【従来の技術】溶融炭酸塩型燃料電池は、高効率、かつ
環境への影響が少ないなど、従来の発電装置にはない特
徴を有しており、水力・火力・原子力に続く発電システ
ムとして注目を集め、現在世界各国で鋭意研究開発が行
われている。特に天然ガスを燃料とする溶融炭酸塩型燃
料電池を用いた発電設備では、図3に示すように天然ガ
ス1と水蒸気2とを混合してなる燃料ガス3を水素を含
むアノードガス4に改質する改質器10と、アノードガ
ス4と酸素を含むカソードガス5とから発電する燃料電
池20とを一般的に備えており、改質器10で作られた
アノードガス4は燃料電池20に供給され、燃料電池内
でその大部分(例えば80%)を消費してアノード排ガ
ス6となり、その水分を分離した後、燃焼用ガス7とし
て改質器10の燃焼器に供給される。改質器では燃焼用
ガス7中の可燃成分(水素、一酸化炭素、メタン等)を
燃焼器で燃焼して高温の燃焼ガスを生成し、この高温の
燃焼ガスにより改質管10aを加熱し改質管内を流れる
燃料ガス3を改質する。改質器を出た燃焼排ガス8は空
気11が合流してカソードガス5となり、このカソード
ガス5は、燃料電池20内で一部が反応して高温のカソ
ード排ガス9となり、その一部がリサイクルされ、残り
は動力回収装置30のタービン31で動力を回収し、ボ
イラ35で熱を回収して、系外に排出される。2. Description of the Related Art Molten carbonate fuel cells have characteristics that conventional power generators do not have, such as high efficiency and little impact on the environment, and they are attracting attention as a power generation system following hydropower, thermal power, and nuclear power. Is currently being researched and developed all over the world. In particular, in a power generation facility using a molten carbonate fuel cell using natural gas as a fuel, a fuel gas 3 obtained by mixing natural gas 1 and water vapor 2 is converted to an anode gas 4 containing hydrogen as shown in FIG. A reformer 10 that produces a reforming gas and a fuel cell 20 that generates electric power from an anode gas 4 and a cathode gas 5 containing oxygen are generally provided. The anode gas 4 produced by the reformer 10 is supplied to the fuel cell 20. It is supplied and consumes most (for example, 80%) of it in the fuel cell to become the anode exhaust gas 6, and after separating its water content, it is supplied to the combustor of the reformer 10 as the combustion gas 7. In the reformer, combustible components (hydrogen, carbon monoxide, methane, etc.) in the combustion gas 7 are burned in the combustor to generate high temperature combustion gas, and the high temperature combustion gas heats the reforming pipe 10a. The fuel gas 3 flowing in the reforming pipe is reformed. The flue gas 8 exiting the reformer joins with the air 11 to become the cathode gas 5, and a part of this cathode gas 5 reacts in the fuel cell 20 to become the hot cathode exhaust gas 9 and a part thereof is recycled. The remaining power is recovered by the turbine 31 of the power recovery device 30, the heat is recovered by the boiler 35, and the heat is discharged to the outside of the system.
【0003】[0003]
【発明が解決しようとする課題】上述した発電設備にお
いて、燃料電池の入口ガス温度が低すぎると燃料電池
を構成する電解液が部分的に凝固し燃料電池を本質的に
損傷させるおそれがある、また、燃料電池の発熱をカ
ソードガスで除去(冷却)するようになっているため、
カソードガスの流量が少な過ぎると出口付近の電解液が
高温になって蒸発し、電池寿命を極端に短くする問題点
があった。このため、カソードガスの入口ガス温度Ti
を所定の範囲(例えば550〜600℃)に維持すると
共に、カソード排ガスの出口温度Toと入口温度との差
ΔTを所定の範囲(例えば100〜150℃以下)に抑
える必要があった。In the above-described power generation equipment, if the inlet gas temperature of the fuel cell is too low, the electrolyte constituting the fuel cell may be partially solidified and the fuel cell may be essentially damaged. Also, since the heat generated by the fuel cell is removed (cooled) by the cathode gas,
If the flow rate of the cathode gas is too low, the electrolyte near the outlet becomes hot and evaporates, resulting in a problem of extremely shortening the battery life. Therefore, the inlet gas temperature Ti of the cathode gas
Must be maintained within a predetermined range (for example, 550 to 600 ° C.), and the difference ΔT between the outlet temperature To of the cathode exhaust gas and the inlet temperature must be suppressed within a predetermined range (for example, 100 to 150 ° C. or less).
【0004】かかる要望を満たすため、従来の発電設備
では、カソード循環ブロア16により比較的多量のカソ
ード排ガス(To=700℃前後)をカソード入口側に
再循環させ、低温(Ta=150〜200℃)の空気と
混合し、このガス温度(図3における入口ガス温度T
i)を検出してこの温度が所定の温度範囲になるように
カソード循環ブロア16による流量を制御していた。In order to meet such a demand, in the conventional power generation equipment, a relatively large amount of cathode exhaust gas (To = about 700 ° C.) is recirculated to the cathode inlet side by the cathode circulation blower 16, and low temperature (Ta = 150 to 200 ° C.). ) Air and mixed with this gas temperature (inlet gas temperature T in FIG. 3).
i) is detected and the flow rate by the cathode circulation blower 16 is controlled so that this temperature falls within a predetermined temperature range.
【0005】しかし、図2に例示するように燃料電池の
性能は長期運転により徐々に劣化するため、同一の電流
を取り出してもその出力電圧は徐々に低下し、同一出力
(=電圧×電流)を維持しようとすると、電流を増大さ
せる必要がある。そのため、劣化に伴う内部抵抗の増大
等により燃料電池20における発熱量は徐々に増大し、
カソード排ガスの温度Toが徐々に高くなる問題点があ
った。特に、上述した燃料電池の温度制御手段では、カ
ソード排ガスの温度Toが高くなると、空気と混合後の
カソードガスの温度Tiを所定の範囲に維持するため、
カソード循環ブロア16のガス流量を低下させるように
制御されるため、カソードガス3の全流量が低下してカ
ソード排ガス7の温度Toが更に高くなり、出口付近の
電解液が早期に高温になってしまい、電池寿命を短縮さ
せてしまう問題点があった。However, as illustrated in FIG. 2, the performance of the fuel cell gradually deteriorates due to long-term operation. Therefore, even if the same current is taken out, the output voltage thereof gradually decreases, and the same output (= voltage × current) is obtained. In order to maintain, the current needs to be increased. Therefore, the amount of heat generated in the fuel cell 20 gradually increases due to an increase in internal resistance due to deterioration,
There is a problem that the temperature To of the cathode exhaust gas gradually increases. In particular, in the temperature control means of the fuel cell described above, when the temperature To of the cathode exhaust gas becomes high, the temperature Ti of the cathode gas after being mixed with air is maintained within a predetermined range.
Since the gas flow rate of the cathode circulation blower 16 is controlled to be decreased, the total flow rate of the cathode gas 3 is decreased, the temperature To of the cathode exhaust gas 7 is further increased, and the temperature of the electrolyte solution near the outlet is quickly increased. Therefore, there is a problem that the battery life is shortened.
【0006】本発明はかかる問題点を解決するために創
案されたものである。すなわち、本発明の目的は、燃料
電池の性能が長期運転により徐々に劣化する場合でも、
カソードガスの入口ガス温度Tiを所定の範囲に維持で
きると共に、カソードガスの出口温度Toと入口温度T
iとの差ΔTを所定の範囲に抑えることができる、燃料
電池の温度制御方法及び装置を提供することにある。The present invention was devised to solve such problems. That is, the object of the present invention is to improve the performance of a fuel cell even if it gradually deteriorates due to long-term operation.
The inlet gas temperature Ti of the cathode gas can be maintained within a predetermined range, and the outlet temperature To and the inlet temperature T of the cathode gas can be maintained.
An object of the present invention is to provide a temperature control method and apparatus for a fuel cell, which can suppress the difference ΔT from i within a predetermined range.
【0007】[0007]
【課題を解決するための手段】本発明によれば、水素を
含むアノードガスと酸素を含むカソードガスとから発電
する燃料電池の温度制御方法であって、カソードガスに
低温の空気を供給する空気供給ラインと、燃料電池を通
過したカソード排ガスの一部を燃料電池の上流側のカソ
ードガスに混入させる再循環ラインと、を備え、燃料電
池の入口におけるカソードガスの温度が所定の範囲にな
るように再循環ラインの流量を制御し、かつ、燃料電池
の出口におけるカソード排ガスの温度が所定の範囲にな
るように空気供給ラインの流量を制御する、ことを特徴
とする燃料電池の温度制御方法が提供される。According to the present invention, there is provided a fuel cell temperature control method for generating power from an anode gas containing hydrogen and a cathode gas containing oxygen, wherein air for supplying low temperature air to the cathode gas is used. A supply line and a recirculation line for mixing a part of the cathode exhaust gas that has passed through the fuel cell with the cathode gas on the upstream side of the fuel cell are provided so that the temperature of the cathode gas at the inlet of the fuel cell falls within a predetermined range. To control the flow rate of the recirculation line, and to control the flow rate of the air supply line so that the temperature of the cathode exhaust gas at the outlet of the fuel cell is within a predetermined range. Provided.
【0008】また、本発明によれば、水素を含むアノー
ドガスと酸素を含むカソードガスとから発電する燃料電
池の温度制御装置であって、空気流量調節弁を有しカソ
ードガスに低温の空気を供給する空気供給ラインと、カ
ソード循環ブロアを有し燃料電池を通過したカソード排
ガスの一部を燃料電池の上流側のカソードガスに混入さ
せる再循環ラインと、燃料電池の入口におけるカソード
ガスの温度を計測するカソードガス温度検出器と、燃料
電池の出口におけるカソード排ガスの温度を計測するカ
ソード排ガス温度検出器と、カソードガス温度検出器に
よる計測値が所定の範囲になるように再循環ラインの流
量を制御しかつカソード排ガス温度検出器による計測値
が所定の範囲になるように空気供給ラインの流量を制御
する制御装置と、を備えたことを特徴とする燃料電池の
温度制御装置が提供される。Further, according to the present invention, there is provided a temperature control device for a fuel cell for generating electric power from an anode gas containing hydrogen and a cathode gas containing oxygen, which has an air flow rate control valve to supply low temperature air to the cathode gas. The air supply line for supplying, the recirculation line for mixing a part of the cathode exhaust gas passing through the fuel cell with the cathode gas on the upstream side of the fuel cell, which has a cathode circulation blower, and the temperature of the cathode gas at the inlet of the fuel cell Adjust the flow rate of the recirculation line so that the cathode gas temperature detector to measure, the cathode exhaust gas temperature detector to measure the temperature of the cathode exhaust gas at the outlet of the fuel cell, and the measured value by the cathode gas temperature detector are within the specified range. A control device for controlling and controlling the flow rate of the air supply line so that the measurement value by the cathode exhaust gas temperature detector falls within a predetermined range, Temperature control apparatus for a fuel cell characterized by comprising is provided.
【0009】[0009]
【作用】上記本発明の方法及び装置によれば、燃料電池
の出口におけるカソード排ガスの温度Toが所定の範囲
になるように空気供給ラインの流量が制御されるので、
図2に例示したように燃料電池の性能が長期運転により
徐々に劣化し、同一出力(=電圧×電流)を維持するた
め電流を増大させて燃料電池における発熱量が増大して
カソード排ガスの温度Toが高くなると、この温度が所
定の範囲になるように空気供給ラインの流量すなわちカ
ソードガスに流入する低温空気量が増大する。これによ
り、燃料電池の入口におけるカソードガスの温度Tiが
低下すると共にカソードガスの全量が増大するため、カ
ソード排ガスの温度Toも低下する。According to the above method and apparatus of the present invention, the flow rate of the air supply line is controlled so that the temperature To of the cathode exhaust gas at the outlet of the fuel cell falls within a predetermined range.
As illustrated in FIG. 2, the performance of the fuel cell gradually deteriorates due to long-term operation, and in order to maintain the same output (= voltage × current), the current is increased and the calorific value of the fuel cell is increased to increase the temperature of the cathode exhaust gas. When To increases, the flow rate of the air supply line, that is, the amount of low temperature air flowing into the cathode gas increases so that this temperature falls within a predetermined range. As a result, the temperature Ti of the cathode gas at the inlet of the fuel cell decreases and the total amount of the cathode gas increases, so the temperature To of the cathode exhaust gas also decreases.
【0010】一方、燃料電池の入口におけるカソードガ
スの温度Tiが所定の範囲になるように再循環ラインの
流量が制御されるので、燃料電池における発熱量が増大
してカソード排ガスの温度が高くなると、上述の制御で
燃料電池の入口におけるカソードガスの温度Tiが低下
するので、再循環ラインからカソードガスに流入するカ
ソード排ガスが増加し、これにより、カソードガスの全
量が増大するため、カソード排ガスの温度Toは更に低
下する。On the other hand, since the flow rate of the recirculation line is controlled so that the temperature Ti of the cathode gas at the inlet of the fuel cell is within a predetermined range, the amount of heat generated in the fuel cell increases and the temperature of the cathode exhaust gas rises. Since the temperature Ti of the cathode gas at the inlet of the fuel cell is lowered by the above-mentioned control, the cathode exhaust gas flowing into the cathode gas from the recirculation line is increased, which increases the total amount of the cathode gas. The temperature To further decreases.
【0011】従って、空気供給ラインの制御と再循環ラ
インの制御が相乗的にカソード排ガスの温度上昇を抑え
るように作用するため、燃料電池の性能が長期運転によ
り徐々に劣化する場合でも、効果的にカソードガスの入
口ガス温度Tiを所定の範囲に維持し、かつカソードガ
スの出口温度と入口温度との差ΔTを所定の範囲に抑え
ることができる。Therefore, since the control of the air supply line and the control of the recirculation line act synergistically to suppress the temperature rise of the cathode exhaust gas, it is effective even when the performance of the fuel cell gradually deteriorates due to long-term operation. In addition, the inlet gas temperature Ti of the cathode gas can be maintained within a predetermined range, and the difference ΔT between the outlet temperature and the inlet temperature of the cathode gas can be suppressed within a predetermined range.
【0012】[0012]
【実施例】以下に本発明の好ましい実施例を図面を参照
して説明する。なお、各図において共通する部分には同
一の符号を付して使用する。図1は、本発明による燃料
電池の温度制御装置の全体構成図である。この図におい
て、燃料電池20は、水素を含むアノードガス4と酸素
を含むカソードガス5とから発電する図3と同様の溶融
炭酸塩型燃料電池である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the present invention will be described below with reference to the drawings. In addition, in each figure, the same parts are denoted by the same reference numerals. FIG. 1 is an overall configuration diagram of a temperature control device for a fuel cell according to the present invention. In this figure, a fuel cell 20 is a molten carbonate fuel cell similar to that in FIG. 3, which generates electric power from an anode gas 4 containing hydrogen and a cathode gas 5 containing oxygen.
【0013】本発明の温度制御装置は、空気流量調節弁
32を有しカソードガス5に低温の空気を供給する空気
供給ライン34と、カソード循環ブロア36を有し燃料
電池20を通過したカソード排ガス9の一部を燃料電池
20の上流側のカソードガスに混入させる再循環ライン
38と、燃料電池20の入口におけるカソードガス5の
温度Tiを計測するカソードガス温度検出器40と、燃
料電池の出口におけるカソード排ガス9の温度Toを計
測するカソード排ガス温度検出器42と、制御装置44
とを備えている。The temperature control device of the present invention has an air flow control valve 32, an air supply line 34 for supplying low-temperature air to the cathode gas 5, and a cathode circulation blower 36. The cathode exhaust gas passes through the fuel cell 20. A recirculation line 38 for mixing a part of 9 into the cathode gas on the upstream side of the fuel cell 20, a cathode gas temperature detector 40 for measuring the temperature Ti of the cathode gas 5 at the inlet of the fuel cell 20, and an outlet for the fuel cell. A cathode exhaust gas temperature detector 42 for measuring the temperature To of the cathode exhaust gas 9 at
It has and.
【0014】制御装置44は、カソードガス温度検出器
40による計測値が所定の範囲になるように再循環ライ
ン38の流量を制御し、かつカソード排ガス温度検出器
42による計測値が所定の範囲になるように空気供給ラ
イン34の流量を制御する。すなわち、制御装置44に
より燃料電池20の入口におけるカソードガス5の温度
Tiが所定の範囲になるようにカソード循環ブロア36
により再循環ライン38の流量が制御され、かつ、燃料
電池20の出口におけるカソード排ガス9の温度Toが
所定の範囲になるように空気流量調節弁32により空気
供給ライン34の流量が制御される。The controller 44 controls the flow rate of the recirculation line 38 so that the value measured by the cathode gas temperature detector 40 falls within a predetermined range, and the value measured by the cathode exhaust gas temperature detector 42 falls within a predetermined range. The flow rate of the air supply line 34 is controlled so that That is, the cathode circulation blower 36 is controlled by the controller 44 so that the temperature Ti of the cathode gas 5 at the inlet of the fuel cell 20 falls within a predetermined range.
Thus, the flow rate of the recirculation line 38 is controlled, and the flow rate of the air supply line 34 is controlled by the air flow rate control valve 32 so that the temperature To of the cathode exhaust gas 9 at the outlet of the fuel cell 20 falls within a predetermined range.
【0015】以下、本発明の温度制御装置による作動内
容を説明する。燃料電池の出口におけるカソード排ガス
9の温度Toが所定の範囲(例えば650〜700℃)
になるように空気供給ラインの流量を制御することによ
り、図2に例示したように燃料電池の性能が長期運転に
より徐々に劣化し、同一出力(=電圧×電流)を維持す
るため電流を増大させて燃料電池における発熱量が増大
してカソード排ガス9の温度Toが高くなる(例えば7
00℃以上)と、この温度が所定の範囲になるように空
気供給ライン34の流量すなわちカソードガスに流入す
る低温(例えばTa=150〜200℃)の空気量が増
大する。これにより、燃料電池の入口におけるカソード
ガス5の温度Tiが低下すると共にカソードガスの全量
が増大するため、カソード排ガスの温度Toは低下し、
所定の範囲(例えば650〜700℃)になる。The operation of the temperature control device of the present invention will be described below. The temperature To of the cathode exhaust gas 9 at the outlet of the fuel cell is within a predetermined range (for example, 650 to 700 ° C.)
The flow rate of the air supply line is controlled so that the fuel cell performance gradually deteriorates due to long-term operation as illustrated in FIG. 2, and the current is increased to maintain the same output (= voltage × current). As a result, the amount of heat generated in the fuel cell increases and the temperature To of the cathode exhaust gas 9 rises (for example, 7
When the temperature is 00 ° C. or higher, the flow rate of the air supply line 34, that is, the low-temperature (for example, Ta = 150 to 200 ° C.) air amount flowing into the cathode gas increases so that this temperature falls within a predetermined range. As a result, the temperature Ti of the cathode gas 5 at the inlet of the fuel cell decreases and the total amount of the cathode gas increases, so the temperature To of the cathode exhaust gas decreases.
It becomes a predetermined range (for example, 650 to 700 ° C.).
【0016】一方、燃料電池の入口におけるカソードガ
スの温度Tiが所定の範囲(例えば550〜600℃)
になるように再循環ライン38の流量を制御することに
より、燃料電池20における発熱量が増大してカソード
排ガスの温度Toが高くなると、上述の制御で燃料電池
の入口におけるカソードガスの温度Tiが低下するの
で、再循環ライン38からカソードガス5に流入するカ
ソード排ガスが増加し、これにより、カソードガスの全
量が増大するため、カソード排ガスの温度Toは更に低
下する。On the other hand, the temperature Ti of the cathode gas at the inlet of the fuel cell is in a predetermined range (for example, 550 to 600 ° C.).
By controlling the flow rate of the recirculation line 38 so that the amount of heat generation in the fuel cell 20 increases and the temperature To of the cathode exhaust gas rises, the temperature Ti of the cathode gas at the inlet of the fuel cell is increased by the above control. Since the temperature of the cathode exhaust gas decreases, the amount of cathode exhaust gas flowing into the cathode gas 5 from the recirculation line 38 increases, which increases the total amount of cathode gas, and thus the temperature To of the cathode exhaust gas further decreases.
【0017】従って、空気供給ライン34の制御と再循
環ライン38の制御が相乗的にカソード排ガスの温度上
昇を抑えるように作用するため、燃料電池の性能が長期
運転により徐々に劣化する場合でも、効果的にカソード
ガスの入口ガス温度Tiを所定の範囲に維持し、かつカ
ソードガスの出口温度と入口温度との差ΔTを所定の範
囲に抑えることができる。Therefore, since the control of the air supply line 34 and the control of the recirculation line 38 synergistically act to suppress the temperature rise of the cathode exhaust gas, even when the performance of the fuel cell gradually deteriorates due to long-term operation, It is possible to effectively maintain the inlet gas temperature Ti of the cathode gas within a predetermined range and suppress the difference ΔT between the outlet temperature and the inlet temperature of the cathode gas within a predetermined range.
【0018】なお、本発明は上述した実施例に限定され
るものではなく、本発明の要旨を逸脱しない範囲で自由
に変更できることは勿論である。The present invention is not limited to the above-described embodiments, and it goes without saying that the present invention can be freely modified without departing from the gist of the present invention.
【0019】[0019]
【発明の効果】上述したように本発明の方法及び装置
は、空気供給ラインの制御と再循環ラインの制御が相乗
的にカソード排ガスの温度上昇を抑えるように作用する
ため、燃料電池の性能が長期運転により徐々に劣化する
場合でも、効果的にカソードガスの入口ガス温度Tiを
所定の範囲に維持し、かつカソードガスの出口温度と入
口温度との差ΔTを所定の範囲に抑えることができる、
優れた効果を有する。As described above, in the method and apparatus of the present invention, the control of the air supply line and the control of the recirculation line act synergistically to suppress the temperature rise of the cathode exhaust gas, so that the performance of the fuel cell is improved. Even when the temperature gradually deteriorates due to long-term operation, it is possible to effectively maintain the cathode gas inlet gas temperature Ti within a predetermined range and suppress the difference ΔT between the cathode gas outlet temperature and the inlet temperature within a predetermined range. ,
Has excellent effect.
【図1】本発明による燃料電池の温度制御装置の全体構
成図である。FIG. 1 is an overall configuration diagram of a temperature control device for a fuel cell according to the present invention.
【図2】劣化前後の燃料電池の性能特性である。FIG. 2 is a performance characteristic of a fuel cell before and after deterioration.
【図3】従来の燃料電池発電装置の全体構成図である。FIG. 3 is an overall configuration diagram of a conventional fuel cell power generator.
1 天然ガス 2 水蒸気 3 燃料ガス 4 アノードガス 5 カソードガス 6 アノード排ガス 7 燃焼用ガス 8 燃焼排ガス 9 カソード排ガス 10 改質器 10a 改質管 11 空気 20 燃料電池 30 動力回収装置 31 タービン 32 空気流量調節弁 34 空気供給ライン 35 ボイラ 36 カソード循環ブロア 38 再循環ライン 40 カソードガス温度検出器 42 カソード排ガス温度検出器 44 制御装置 A アノード側 C カソード側 Re 改質室 Co 燃焼室 1 Natural Gas 2 Water Vapor 3 Fuel Gas 4 Anode Gas 5 Cathode Gas 6 Anode Exhaust Gas 7 Combustion Gas 8 Combustion Exhaust Gas 9 Cathode Exhaust Gas 10 Reformer 10a Reformer Tube 11 Air 20 Fuel Cell 30 Power Recovery Device 31 Turbine 32 Air Flow Control Valve 34 Air supply line 35 Boiler 36 Cathode circulation blower 38 Recirculation line 40 Cathode gas temperature detector 42 Cathode exhaust gas temperature detector 44 Control device A Anode side C Cathode side Re Reforming chamber Co Combustion chamber
Claims (2)
ソードガスとから発電する燃料電池の温度制御方法であ
って、 カソードガスに低温の空気を供給する空気供給ライン
と、 燃料電池を通過したカソード排ガスの一部を燃料電池の
上流側のカソードガスに混入させる再循環ラインと、を
備え、 燃料電池の入口におけるカソードガスの温度が所定の範
囲になるように再循環ラインの流量を制御し、かつ、燃
料電池の出口におけるカソード排ガスの温度が所定の範
囲になるように空気供給ラインの流量を制御する、こと
を特徴とする燃料電池の温度制御方法。1. A method for controlling a temperature of a fuel cell for generating power from an anode gas containing hydrogen and a cathode gas containing oxygen, comprising: an air supply line for supplying low temperature air to the cathode gas; and a cathode passing through the fuel cell. A recirculation line for mixing a part of the exhaust gas into the cathode gas on the upstream side of the fuel cell, and controlling the flow rate of the recirculation line so that the temperature of the cathode gas at the inlet of the fuel cell falls within a predetermined range, Moreover, the temperature control method of the fuel cell, wherein the flow rate of the air supply line is controlled so that the temperature of the cathode exhaust gas at the outlet of the fuel cell falls within a predetermined range.
ソードガスとから発電する燃料電池の温度制御装置であ
って、 空気流量調節弁を有しカソードガスに低温の空気を供給
する空気供給ラインと、カソード循環ブロアを有し燃料
電池を通過したカソード排ガスの一部を燃料電池の上流
側のカソードガスに混入させる再循環ラインと、燃料電
池の入口におけるカソードガスの温度を計測するカソー
ドガス温度検出器と、燃料電池の出口におけるカソード
排ガスの温度を計測するカソード排ガス温度検出器と、
カソードガス温度検出器による計測値が所定の範囲にな
るように再循環ラインの流量を制御しかつカソード排ガ
ス温度検出器による計測値が所定の範囲になるように空
気供給ラインの流量を制御する制御装置と、を備えたこ
とを特徴とする燃料電池の温度制御装置。2. A temperature control device for a fuel cell, which generates electric power from an anode gas containing hydrogen and a cathode gas containing oxygen, comprising an air supply line having an air flow rate control valve and supplying low temperature air to the cathode gas. , A recirculation line that has a cathode circulation blower and mixes a part of the cathode exhaust gas that has passed through the fuel cell with the cathode gas on the upstream side of the fuel cell, and the cathode gas temperature detection that measures the temperature of the cathode gas at the inlet of the fuel cell And a cathode exhaust gas temperature detector that measures the temperature of the cathode exhaust gas at the outlet of the fuel cell,
Control to control the flow rate of the recirculation line so that the value measured by the cathode gas temperature detector falls within a predetermined range and to control the flow rate of the air supply line so that the value measured by the cathode exhaust gas temperature detector falls within a predetermined range. A device for controlling a temperature of a fuel cell.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30956293A JP3208970B2 (en) | 1993-12-10 | 1993-12-10 | Fuel cell temperature control method and apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30956293A JP3208970B2 (en) | 1993-12-10 | 1993-12-10 | Fuel cell temperature control method and apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07161371A true JPH07161371A (en) | 1995-06-23 |
JP3208970B2 JP3208970B2 (en) | 2001-09-17 |
Family
ID=17994519
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JP30956293A Expired - Fee Related JP3208970B2 (en) | 1993-12-10 | 1993-12-10 | Fuel cell temperature control method and apparatus |
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Cited By (7)
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---|---|---|---|---|
JP2004071279A (en) * | 2002-08-05 | 2004-03-04 | Central Res Inst Of Electric Power Ind | Fused carbonate fuel cell power generation system, and power generation method in system |
US7056611B2 (en) * | 2002-07-16 | 2006-06-06 | Siemens Power Generation, Inc. | System for controlling the operating temperature of a fuel cell |
JP2007194005A (en) * | 2006-01-18 | 2007-08-02 | Hitachi Ltd | Solid oxide fuel cell power generation system and its operation control method |
WO2009040621A2 (en) | 2007-09-27 | 2009-04-02 | Nissan Motor Co., Ltd. | Fuel cell system and method of controlling fuel cell system |
WO2011012942A1 (en) * | 2009-07-30 | 2011-02-03 | Nissan Motor Co., Ltd. | Fuel cell system and control method thereof |
US20120183876A1 (en) * | 2009-09-28 | 2012-07-19 | Ono Takashi | Fuel cell device |
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1993
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
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US7056611B2 (en) * | 2002-07-16 | 2006-06-06 | Siemens Power Generation, Inc. | System for controlling the operating temperature of a fuel cell |
JP2004071279A (en) * | 2002-08-05 | 2004-03-04 | Central Res Inst Of Electric Power Ind | Fused carbonate fuel cell power generation system, and power generation method in system |
JP4629950B2 (en) * | 2002-08-05 | 2011-02-09 | 財団法人電力中央研究所 | Molten carbonate fuel cell power generation system and power generation method in the power generation system |
JP2007194005A (en) * | 2006-01-18 | 2007-08-02 | Hitachi Ltd | Solid oxide fuel cell power generation system and its operation control method |
WO2009040621A2 (en) | 2007-09-27 | 2009-04-02 | Nissan Motor Co., Ltd. | Fuel cell system and method of controlling fuel cell system |
US8394546B2 (en) | 2007-12-27 | 2013-03-12 | Nissan Motor Co., Ltd. | Fuel cell system and control method thereof |
WO2011012942A1 (en) * | 2009-07-30 | 2011-02-03 | Nissan Motor Co., Ltd. | Fuel cell system and control method thereof |
US9406949B2 (en) | 2009-07-30 | 2016-08-02 | Nissan Motor Co., Ltd. | Fuel cell system and control method thereof |
US9929415B2 (en) | 2009-07-30 | 2018-03-27 | Nissan Motor Co., Ltd. | Fuel cell system and control method thereof |
US20120183876A1 (en) * | 2009-09-28 | 2012-07-19 | Ono Takashi | Fuel cell device |
EP2485310A1 (en) * | 2009-09-28 | 2012-08-08 | Kyocera Corporation | Fuel cell device |
EP2485310A4 (en) * | 2009-09-28 | 2014-04-16 | Kyocera Corp | Fuel cell device |
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