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JPH0352188B2 - - Google Patents
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JPH0352188B2 - - Google Patents

Info

Publication number
JPH0352188B2
JPH0352188B2 JP59016686A JP1668684A JPH0352188B2 JP H0352188 B2 JPH0352188 B2 JP H0352188B2 JP 59016686 A JP59016686 A JP 59016686A JP 1668684 A JP1668684 A JP 1668684A JP H0352188 B2 JPH0352188 B2 JP H0352188B2
Authority
JP
Japan
Prior art keywords
fuel cell
reformer
compressor
compressed air
power generation
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
Application number
JP59016686A
Other languages
Japanese (ja)
Other versions
JPS60160578A (en
Inventor
Hisashi Mitani
Toshiichi Suefuji
Yoshuki Taguma
Kai Nishama
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.)
Mitsubishi Electric Corp
Shimazu Seisakusho KK
Original Assignee
Mitsubishi Electric Corp
Shimazu Seisakusho KK
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 Mitsubishi Electric Corp, Shimazu Seisakusho KK filed Critical Mitsubishi Electric Corp
Priority to JP59016686A priority Critical patent/JPS60160578A/en
Publication of JPS60160578A publication Critical patent/JPS60160578A/en
Publication of JPH0352188B2 publication Critical patent/JPH0352188B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination 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
    • 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

  • 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〕 この発明は燃料電池の空気極出口の余剰空気及
び上記改質器の排ガスによつて駆動され上記燃料
電池と改質器に必要な圧縮空気を供給するターボ
コンプレツサを備えた燃料電池発電システムに関
するものである。
[Detailed Description of the Invention] [Technical Field of the Invention] This invention provides compressed air necessary for the fuel cell and the reformer, which is driven by excess air at the air electrode outlet of the fuel cell and exhaust gas from the reformer. This invention relates to a fuel cell power generation system equipped with a turbo compressor.

〔従来技術〕[Prior art]

燃料電池発電システムは従来の汽力発電に比べ
高効率が期待できること、環境保全性が良い等の
利点があり、実用化を目指し近年盛んに開発が進
められている。燃料電池発電システムは基本的に
は電池本体、改質器、インバータにより構成され
るが、この他のシステムの効率向上に不可欠な構
成機器としてターボコンプレツサがある。
Fuel cell power generation systems have advantages over conventional steam power generation, such as higher efficiency and better environmental protection, and have been actively developed in recent years with the aim of putting them into practical use. A fuel cell power generation system basically consists of a battery, a reformer, and an inverter, but there is also a turbo compressor as an essential component for improving the efficiency of the system.

燃料電池本体は燃料ガスとして天然ガス等の炭
化水素系燃料を改質して得られる水素リツチな改
質ガスを使用し、酸化剤ガスとして空気を使用す
る。電池本体の性能は各反応ガスの圧力の増大に
よつて向上する傾向を示し、このため燃料、空気
各反応ガスの動作圧力は、例えば3〜6Kg/cm2
程度に加圧維持される。このとき、空気の圧縮に
は多大の動力を必要とし、その値は電池の発生エ
ネルギーの約20%にも達する。一方、電池の燃料
ガスを生成するための改質反応は、約800℃の高
温で行われ、改質器からは高い温度の排ガスが排
出される。したがつて空気の圧縮動力源をシステ
ムの排ガスエネルギーに求めることができればシ
ステムの効率向上に大きな効果がある。ターボコ
ンプレツサはこのような目的で導入されるもの
で、システムの排ガスエネルギーをタービンで回
収し、同軸上のコンプレツサで必要な圧縮空気を
供給することによつて、システム内部で動力回収
をし、システム効率の向上を図るものである。
The fuel cell main body uses a hydrogen-rich reformed gas obtained by reforming a hydrocarbon fuel such as natural gas as the fuel gas, and air as the oxidizing gas. The performance of the battery body tends to improve as the pressure of each reaction gas increases, so the operating pressure of each reaction gas, fuel and air, is, for example, 3 to 6 kg/cm 2 g.
The pressure is maintained at a certain level. At this time, compressing the air requires a large amount of power, amounting to about 20% of the energy generated by the battery. On the other hand, the reforming reaction to generate fuel gas for the battery is carried out at a high temperature of approximately 800°C, and high temperature exhaust gas is discharged from the reformer. Therefore, if the exhaust gas energy of the system can be used as the power source for compressing air, it will have a significant effect on improving the efficiency of the system. A turbo compressor is introduced for this purpose; it recovers energy from the system's exhaust gas with a turbine, supplies the necessary compressed air with a coaxial compressor, and recovers power within the system. This aims to improve system efficiency.

第1図に一般的な燃料電池発電システムの空気
回路系統図を示す。図において、1は燃料電池本
体、2は改質器、3はターボコンプレツサ、3
a,3bはそれぞれターボコンプレツサ3のコン
プレツサ、タービンであり、コンプレツサ3aで
圧縮された空気の一部が流量調節弁5を経て燃料
電池本体1の反応に、残りの空気が流量調節弁6
を経て改質器2の燃料用に使用されたあと、それ
ぞれの排ガスがタービン3bに投入される。4は
タービン3bの不足動力を補う助燃炉であり、タ
ーボコンプレツサ3と組合せて使用される。一般
に空気流量の少ない部分負荷運転条件時は定格負
荷時に比しターボコンプレツサ3の効率が低く、
タービン3bの動力が不足する傾向にある。この
ようなとき、流量調節弁7を開いてコンプレツサ
3aの吐出空気の一部を助燃炉4に導き、その燃
焼ガスをシステムの排ガスに加えることにより、
タービン3bの動力不足をカバーする。又、低負
荷域でコンプレツサ3aのサージングを防止する
必要があるとき、調節弁8を開いて空気の一部を
バイパスさせるが、これによつてタービン3bの
動力が不足する分は助燃炉4に空気を導いて補
う。この他、運転時の負荷調整用にタービンバイ
パス調節弁9、及びタービンノズル(図示せず)
がある。
Figure 1 shows an air circuit diagram of a typical fuel cell power generation system. In the figure, 1 is the fuel cell main body, 2 is the reformer, 3 is the turbo compressor, 3
a and 3b are the compressor and turbine of the turbo compressor 3, respectively; a part of the air compressed by the compressor 3a passes through the flow rate control valve 5 and is reacted in the fuel cell main body 1, and the remaining air is sent to the flow rate control valve 6.
After being used as fuel for the reformer 2, each exhaust gas is input to the turbine 3b. Reference numeral 4 denotes an auxiliary combustion furnace that compensates for the insufficient power of the turbine 3b, and is used in combination with the turbo compressor 3. Generally, under partial load operating conditions with low air flow, the efficiency of the turbo compressor 3 is lower than when under rated load.
The power of the turbine 3b tends to be insufficient. In such a case, by opening the flow control valve 7 and guiding a part of the air discharged from the compressor 3a to the auxiliary combustion furnace 4, and adding the combustion gas to the exhaust gas of the system,
This covers the power shortage of the turbine 3b. Also, when it is necessary to prevent surging of the compressor 3a in a low load range, the control valve 8 is opened to bypass a portion of the air. Guide and supplement air. In addition, a turbine bypass control valve 9 and a turbine nozzle (not shown) are used for load adjustment during operation.
There is.

燃料電池発電システムは上記のように構成され
るが、このような燃料電池発電システムを起動さ
せるには、通常、反応温度が高く且つ熱時定数の
大きい改質器2の昇温からスタートするが、これ
には燃焼用の空気を必要とする。一方、ターボコ
ンプレツサ3は何等かの入力なしには自力で立ち
上がることができない。したがつて、燃料電池発
電システムを起動するには何等かの外部エネルギ
ーを付与してターボコンプレツサ3を起動させて
やる必要がある。このターボコンプレツサ3は従
来航空機の分野で補助動力ユニツト(APU)や
空調システム(ECS)に一般的に使用される例が
あり、この場合、ターボコンプレツサ3の起動は
例えばジエツトエンジンコンプレツサの圧縮空気
の一部をタービンに導入するとか直結セルモータ
方式で行われていた。但し、燃料電池発電システ
ムにおいては、システム停止状態において、ター
ボコンプレツサ3を起動させるために駆動力を与
えるのに必要な利用できる動力源(圧縮空気)が
周囲に存在しないため、特別にターボコンプレツ
サ3の起動手段を構成する必要がある。そこで、
燃料電池発電システムにおいて、直結セルモータ
方式によりターボコンプレツサ3の起動手段を構
成することが考えられるが、この場合、システム
構成が複雑となり、又ターボコンプレツサ3の動
作効率が低下するという欠点があつた。
The fuel cell power generation system is configured as described above, but in order to start up such a fuel cell power generation system, it is usually started by raising the temperature of the reformer 2, which has a high reaction temperature and a large thermal time constant. , which requires air for combustion. On the other hand, the turbo compressor 3 cannot start up on its own without some kind of input. Therefore, in order to start the fuel cell power generation system, it is necessary to apply some kind of external energy to start the turbo compressor 3. This turbo compressor 3 has conventionally been commonly used in auxiliary power units (APUs) and air conditioning systems (ECS) in the field of aircraft, and in this case, the turbo compressor 3 is activated by, for example, a jet engine compressor. This was done by introducing a portion of the compressed air into the turbine, or by using a direct starter motor system. However, in a fuel cell power generation system, when the system is stopped, there is no usable power source (compressed air) around to provide the driving force to start the turbo compressor 3. It is necessary to configure a means for starting the shank 3. Therefore,
In the fuel cell power generation system, it is conceivable to configure the starting means for the turbo compressor 3 using a direct-coupled cell motor system, but in this case, there are disadvantages that the system configuration becomes complicated and the operating efficiency of the turbo compressor 3 decreases. Ta.

〔発明の概要〕[Summary of the invention]

この発明は上記のような従来のものの欠点に鑑
がみてなされたものであり、ターボコンプレツサ
のコンプレツサ出口側に設置され、システム起動
時に運転されこれに伴う圧縮空気を改質器に供給
して燃焼させ且つ改質器での燃焼後その圧縮空気
の一部を助燃炉に供給して助燃エネルギーを付与
する起動用圧縮空気供給装置を設け、簡単な構成
で効率的にターボコンプレツサを運転することが
できる燃料電池発電システムを提供するものであ
る。
This invention was made in view of the drawbacks of the conventional ones as described above, and is installed on the compressor outlet side of the turbo compressor and is operated when the system is started to supply compressed air to the reformer. The turbo compressor is operated efficiently with a simple configuration by providing a starting compressed air supply device that provides combustion energy by combusting the air and supplying a part of the compressed air to the auxiliary combustion furnace after combustion in the reformer. This provides a fuel cell power generation system that can.

〔発明の実施例〕[Embodiments of the invention]

以下、この発明の一実施例を第2図に基づいて
説明する。図において、1〜9は上述した従来の
構成と同様である。10はターボコンプレツサ3
のコンプレツサ3a出口側に設置され、システム
起動時に運転されこれに伴う圧縮空気を改質器2
に供給して燃焼させ且つ改質器2での燃焼後その
圧縮空気の一部を助燃炉4に供給して助燃エネル
ギーを付与する起動用圧縮空気供給装置、11は
コンプレツサ3a出口側で大気に解放するサージ
防止弁、12は逆止弁である。
Hereinafter, one embodiment of the present invention will be described based on FIG. 2. In the figure, numerals 1 to 9 are similar to the conventional structure described above. 10 is turbo compressor 3
The compressor 3a is installed on the outlet side of the compressor 3a, and is operated when the system is started, and the resulting compressed air is sent to the reformer 2.
A starting compressed air supply device 11 supplies the compressed air to the compressor for combustion, and after combustion in the reformer 2 supplies a part of the compressed air to the auxiliary combustion furnace 4 to provide auxiliary combustion energy. The surge prevention valve to be released, 12, is a check valve.

燃料電池発電システムを起動させる動作を次に
述べる。まず、圧縮空気供給装置10を起動し、
調節弁6を開いて改質器2に空気を導いて改質器
2の燃焼をスタートする。このとき、コンプレツ
サ3aの出口側が締切状態であればサージングを
生じるので、サージ防止弁11を開いてコンプレ
ツサ3a出口側を大気に解放して置く。逆止弁1
2の作用によつて圧縮空気供給装置10からの空
気がコンプレツサ3a側に逆流することはない。
調節弁9が閉じているときは、改質器2に空気を
導くと同時にターボコンプレツサ3の回転がスタ
ートし、改質器2の排ガスの温度上昇とともにタ
ーボコンプレツサ3の回転数が上昇し、コンプレ
ツサ3aの吐出流量が増加する。調節弁9が開い
ているときは、ターボコンプレツサ3は停止した
ままである。改質器2の排ガスの温度がある程度
上昇した時点で、調節弁7を開いて助燃炉4に空
気を導くと同時に助燃炉4に燃料を導入して助燃
炉4の燃焼をスタートする。このとき、圧縮空気
供給装置10からの空気は、改質器2と助燃炉4
に分配される。助燃炉4の排ガスの温度が上昇す
れば、ターボコンプレツサ3の自力運転の条件は
成立する。即ち、調節弁9が閉じているときは、
助燃炉4の排ガスの温度が上昇し、十分なコンプ
レツサ3a吐出流量になつた時点でサージ防止弁
11を閉じれば、コンプレツサ3aの吐出圧力が
圧縮空気供給装置10の吐出圧力を上回り、逆止
弁12が開いてコンプレツサ3aの吐出空気が改
質器2と助燃炉4に供給される。又調節弁9)が
開いているときは、この時点で調節弁9を徐々に
閉じればターボコンプレツサ3は起動し、以後は
同上の手順でコンプレツサ3aの吐出空気を改質
器2と助燃炉4に導くことができる。しかる後、
圧縮空気供給装置10を停止させればターボコン
プレツサ3は自力運転に入ることになる。ターボ
コンプレツサ3が自力運転に入れば、以後のシス
テム立ち上げに必要な空気はターボコンプレツサ
3から供給される。燃料電池本体1へは、このあ
と調節弁5を開いて空気を供給する。このように
して改質器2の排ガスエネルギーを有効に利用し
ながら助燃炉4を使用してターボコンプレツサ3
を立ち上げシステムを起動するようにしている。
ターボコンプレツサ3が自力運転に改質器2の排
ガスエネルギーを利用することは、その分助燃炉
4を小さくできる点でメリツトがある。例えば、
ひとつの試算例として改質器2の燃焼スタートと
同時に助燃炉4を点火し、ターボコンプレツサ3
を自力運転させる場合、電池発生エネルギーの15
%〜20%程度の容量の助燃炉4が必要である。一
方、改質器2の昇温が十分に行われた後に助燃炉
4を点火し、ターボコンプレツサ3を自力運転さ
せる場合、助燃炉4の容量は電池発生エネルギー
の約5%程度でよい。尚、助燃炉4の点火を必要
以上に遅らせば、圧縮空気供給装置10の運転時
間が長くなり、システム起動に要する全消費エネ
ルギーが大きくなるので助燃炉4の点火、ターボ
コンプレツサ3の立ち上げのタイミングは、助燃
炉4の容量とシステム起動時のエネルギー消費量
の双方を勘案して適正値が決められる。以上のよ
うにコンプレツサ3a出口側に起動用圧縮空気供
給装置10を設置するという簡単な構成で、又タ
ーボコンプレツサ3の動作効率を低下させること
なく、システム起動時にターボコンプレツサ3を
起動及び自力運転するようにしている。
The operation of starting up the fuel cell power generation system will be described next. First, start the compressed air supply device 10,
The control valve 6 is opened to introduce air to the reformer 2, and combustion in the reformer 2 is started. At this time, if the outlet side of the compressor 3a is closed, surging will occur, so the surge prevention valve 11 is opened to open the outlet side of the compressor 3a to the atmosphere. Check valve 1
2 prevents the air from the compressed air supply device 10 from flowing back toward the compressor 3a.
When the control valve 9 is closed, the rotation of the turbo compressor 3 starts at the same time that air is introduced into the reformer 2, and as the temperature of the exhaust gas from the reformer 2 rises, the rotation speed of the turbo compressor 3 increases. , the discharge flow rate of the compressor 3a increases. When the control valve 9 is open, the turbo compressor 3 remains stopped. When the temperature of the exhaust gas from the reformer 2 rises to a certain degree, the control valve 7 is opened to introduce air into the auxiliary combustion furnace 4, and at the same time, fuel is introduced into the auxiliary combustion furnace 4 to start combustion in the auxiliary combustion furnace 4. At this time, the air from the compressed air supply device 10 is transferred to the reformer 2 and the auxiliary combustion furnace 4.
distributed to. If the temperature of the exhaust gas from the auxiliary combustion furnace 4 rises, the conditions for self-operation of the turbo compressor 3 are satisfied. That is, when the control valve 9 is closed,
If the surge prevention valve 11 is closed when the temperature of the exhaust gas from the auxiliary combustion furnace 4 rises and reaches a sufficient discharge flow rate from the compressor 3a, the discharge pressure of the compressor 3a will exceed the discharge pressure of the compressed air supply device 10, and the check valve will close. 12 is opened and the air discharged from the compressor 3a is supplied to the reformer 2 and the auxiliary combustion furnace 4. Also, when the control valve 9) is open, if the control valve 9 is gradually closed at this point, the turbo compressor 3 will start up, and from then on, the same procedure as above will be used to transfer the air discharged from the compressor 3a to the reformer 2 and the auxiliary combustion furnace. It can lead to 4. After that,
When the compressed air supply device 10 is stopped, the turbo compressor 3 enters self-operation. Once the turbo compressor 3 enters self-operation, air necessary for subsequent system start-up is supplied from the turbo compressor 3. Thereafter, the control valve 5 is opened to supply air to the fuel cell main body 1. In this way, while effectively utilizing the exhaust gas energy of the reformer 2, the turbo compressor 3 is
and start the system.
The use of the exhaust gas energy of the reformer 2 by the turbo compressor 3 for self-operation has the advantage that the auxiliary combustion furnace 4 can be made smaller accordingly. for example,
As an example of a trial calculation, the auxiliary combustion furnace 4 is ignited at the same time as the reformer 2 starts combustion, and the turbo compressor 3
When operating on its own, 15% of the energy generated by the battery is
% to 20% of the capacity is required. On the other hand, when the auxiliary combustion furnace 4 is ignited after the temperature of the reformer 2 has been sufficiently raised and the turbo compressor 3 is operated on its own, the capacity of the auxiliary combustion furnace 4 may be about 5% of the energy generated by the battery. Note that if the ignition of the auxiliary combustion furnace 4 is delayed more than necessary, the operating time of the compressed air supply device 10 will become longer and the total energy consumption required for starting the system will increase. An appropriate timing is determined by taking into consideration both the capacity of the auxiliary combustion furnace 4 and the amount of energy consumed at the time of system startup. As described above, with a simple configuration in which the starting compressed air supply device 10 is installed on the outlet side of the compressor 3a, the turbo compressor 3 can be started and self-powered at system startup without reducing the operating efficiency of the turbo compressor 3. I try to drive.

尚、上記実施例の圧縮空気供給装置10は、タ
ーボコンプレツサ3を初起動させるだけの容量が
あればよく、例えば電動その他の駆動によるコン
プレツサ又はブロワが使用される。
The compressed air supply device 10 of the above embodiment only needs to have enough capacity to initially start up the turbo compressor 3, and for example, a compressor or blower driven by electric or other means is used.

又、圧縮空気供給装置10の位置は、コンプレ
ツサ3a出口側逆止弁12の下流側で、調節弁
5,6,7,8のそれぞれの弁に至までの間の回
路上であれば何処に設置してもよく、上記実施例
と同様の効果を奏する。
The compressed air supply device 10 can be located anywhere on the circuit downstream of the compressor 3a outlet side check valve 12 and up to each of the control valves 5, 6, 7, and 8. It may be installed, and the same effect as the above embodiment is produced.

〔発明の効果〕〔Effect of the invention〕

この発明は以上説明した通り、ターボコンプレ
ツサのコンプレツサ出口側に設置され、システム
起動時に運転されこれに伴う圧縮空気を改質器に
供給して燃焼させ且つ改質器での燃焼後その圧縮
空気の一部を助燃炉に供給して助燃エネルギーを
付与する起動用圧縮空気供給装置を設けたことに
より、簡単な構成で効率的にターボコンプレツサ
を運転することができる燃料電池発電システムを
得ることができる。
As explained above, this invention is installed on the compressor outlet side of a turbo compressor, is operated when the system is started, supplies the accompanying compressed air to the reformer for combustion, and after combustion in the reformer, the compressed air To obtain a fuel cell power generation system capable of efficiently operating a turbo compressor with a simple configuration by providing a starting compressed air supply device that supplies a part of fuel to an auxiliary combustion furnace to provide auxiliary combustion energy. I can do it.

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

第1図は一般的な燃料電池発電システムを示す
系統図、第2図はこの発明の一実施例による燃料
電池発電システムを示す系統図である。 図において、1は燃料電池本体、2は改質器、
3はターボコンプレツサ、4は助燃炉、10は圧
縮空気供給装置である 尚、図中同一符号は同一又は相当部分を示す。
FIG. 1 is a system diagram showing a general fuel cell power generation system, and FIG. 2 is a system diagram showing a fuel cell power generation system according to an embodiment of the present invention. In the figure, 1 is the fuel cell main body, 2 is a reformer,
3 is a turbo compressor, 4 is an auxiliary combustion furnace, and 10 is a compressed air supply device. In the drawings, the same reference numerals indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】 1 燃料電池と、炭化水素系燃料を改質して上記
燃料電池に水素ガスを供給する改質器と、この改
質器の排ガス又は上記燃料電池の空気極出口の余
剰空気及び上記改質器の排ガスの両に方よつて駆
動され上記燃料電池と改質器に必要な圧縮空気を
供給するコンプレツサとタービンを有するターボ
コンプレツサと、上記コンプレツサ出口空気の一
部を上記タービン入口回路にバイパスする回路上
に設置され上記タービンの不足動力を補う助燃炉
を備えた燃料電池発電システムにおいて、上記タ
ーボコンプレツサのコンプレツサ出口側に設置さ
れ、システム起動時に運転されたこれに伴う圧縮
空気を上記改質器に供給して燃焼させ且つ上記改
質器での燃焼後その圧縮空気の一部を上記助燃炉
に供給して助燃エネルギーを付与する起動用圧縮
空気供給装置を備えたことを特徴とする燃料電池
発電システム。 2 圧縮空気供給装置はコンプレツサであること
を特徴とする特許請求の範囲第1項記載の燃料電
池発電システム。 3 圧縮空気供給装置はブロワであることを特徴
とする特許請求の範囲第1項記載の燃料電池発電
システム。
[Scope of Claims] 1. A fuel cell, a reformer that reforms hydrocarbon fuel and supplies hydrogen gas to the fuel cell, and exhaust gas from the reformer or surplus at the air electrode outlet of the fuel cell. a turbo compressor having a compressor and a turbine driven by both air and the exhaust gas of the reformer to supply the compressed air necessary for the fuel cell and the reformer; In a fuel cell power generation system equipped with an auxiliary combustion furnace that is installed on a circuit that bypasses the turbine inlet circuit and supplements the insufficient power of the turbine, the furnace is installed on the compressor outlet side of the turbo compressor and is operated at the time of system startup. A starting compressed air supply device is provided for supplying compressed air to the reformer for combustion, and for supplying a part of the compressed air after combustion in the reformer to the auxiliary combustion furnace to provide auxiliary combustion energy. A fuel cell power generation system characterized by: 2. The fuel cell power generation system according to claim 1, wherein the compressed air supply device is a compressor. 3. The fuel cell power generation system according to claim 1, wherein the compressed air supply device is a blower.
JP59016686A 1984-01-30 1984-01-30 Fuel cell power generation system Granted JPS60160578A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59016686A JPS60160578A (en) 1984-01-30 1984-01-30 Fuel cell power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59016686A JPS60160578A (en) 1984-01-30 1984-01-30 Fuel cell power generation system

Publications (2)

Publication Number Publication Date
JPS60160578A JPS60160578A (en) 1985-08-22
JPH0352188B2 true JPH0352188B2 (en) 1991-08-09

Family

ID=11923195

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59016686A Granted JPS60160578A (en) 1984-01-30 1984-01-30 Fuel cell power generation system

Country Status (1)

Country Link
JP (1) JPS60160578A (en)

Also Published As

Publication number Publication date
JPS60160578A (en) 1985-08-22

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