JPH0831324B2 - Fuel cell power generation system Fuel system recirculation device - Google Patents
Fuel cell power generation system Fuel system recirculation deviceInfo
- Publication number
- JPH0831324B2 JPH0831324B2 JP60138919A JP13891985A JPH0831324B2 JP H0831324 B2 JPH0831324 B2 JP H0831324B2 JP 60138919 A JP60138919 A JP 60138919A JP 13891985 A JP13891985 A JP 13891985A JP H0831324 B2 JPH0831324 B2 JP H0831324B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel gas
- fuel
- flow rate
- fuel cell
- 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 - Fee Related
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
- H01M8/04—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
- H01M8/04097—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the 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)
- Sustainable Development (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (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(以下FCと記す)発電システムの
燃料系の再循環装置に関する。TECHNICAL FIELD OF THE INVENTION The present invention relates to a fuel system recirculation device for a fuel cell (hereinafter referred to as FC) power generation system.
[発明の技術的背景とその問題点] 従来のFC発電システム燃料系は、FCに水素リッチな燃
料ガスを供給するためのシステムであり、第3図に示す
ように、炭化水素を主成分とする原燃料ガスと水蒸気の
混合ガスを、水素を主成分とするガスに変える改質器1
と、改質器で生成する一酸化炭素に水蒸気を作用させ、
水素と二酸化炭素に変えるシフトコンバータ2、および
燃料ガス流量の調節弁3、により、燃料電池4に所定の
燃料ガスを供給する。また、改質器1での上記の改質反
応が吸熱反応なので、FC4から排出される燃料ガス中の
残留水素を、改質器バーナ5で燃焼させ、上記反応の熱
源としている。[Technical Background of the Invention and Problems Thereof] A conventional FC power generation system fuel system is a system for supplying hydrogen-rich fuel gas to FC, and as shown in FIG. Reformer 1 that changes the mixed gas of raw fuel gas and steam into a gas containing hydrogen as the main component
Then, steam acts on carbon monoxide generated in the reformer,
A predetermined fuel gas is supplied to the fuel cell 4 by the shift converter 2 that converts hydrogen and carbon dioxide and the fuel gas flow rate control valve 3. Further, since the above-mentioned reforming reaction in the reformer 1 is an endothermic reaction, the residual hydrogen in the fuel gas discharged from FC4 is burned in the reformer burner 5 and used as the heat source of the above reaction.
また、FCの構造は第4図に示すように、多数の単位FC
を積層したFCスタック6と、燃料ガスや空気をFCスタッ
クに供給、排気するためのマニホールド7、および、FC
スタックやマニホールド全体を格納する圧力容器8等か
ら構成されている。Moreover, the structure of FC is as shown in FIG.
FC stack 6 in which fuel cells and air are supplied to and exhausted from the FC stack, and FC
It is composed of a pressure vessel 8 and the like that stores the stack and the entire manifold.
この様に、FCスタックは、単位セルを多数直列に積層
したものなので、ごく一部であっても十分な出力の得ら
れない単位セルが存在すると、FCスタック全体の出力
を、この不良セルに合わせざるを得ない。したがって燃
料ガスが片寄って各単位セルに分配された場合、最も少
ない燃料の流れる単位セルの能力に、スタックの出力電
流は制限されてしまい、上記以外の単位セルでは燃料ガ
スは過剰となり、発電に使用されることなく排出されて
しまう。よって、燃料ガスは各単位セルに均等に分配さ
れなければならない。In this way, the FC stack is formed by stacking many unit cells in series, so if there is a unit cell that does not provide sufficient output, even if it is a very small unit, the output of the entire FC stack is transferred to this defective cell. I have no choice but to match. Therefore, when the fuel gas is distributed to each unit cell in a biased manner, the output current of the stack is limited by the capacity of the unit cell through which the least amount of fuel flows, and the fuel gas becomes excessive in the unit cells other than the above, resulting in power generation. It is discharged without being used. Therefore, the fuel gas must be evenly distributed to each unit cell.
しかし、FCは、第4図に示すように、マニホールドに
通した配管により燃料ガスを供給する構造なので、燃料
ガス流量が小さい場合に、各単位セル流路での圧力損失
が小さくなるので、マニホールドに流入して来た燃料ガ
スはほとんどそのままの方向に進み、流入燃料配管付近
の単位セルに多くの燃料ガスが流れ、端は少ないという
片寄りを生じていた。特に、燃料ガスは、二酸化炭素と
水素から成っていて、発電に用いると水素のみ減るの
で、FCの使用後燃料ガスの比重は、供給燃料ガスより、
著しく大きい。この結果、燃料ガス流量が少ないとき、
FCの使用後燃料ガスが、FCスタック下部に滞留し、下部
の単位セルに新しい燃料ガスが供給されるのを妨害する
傾向がある。However, as shown in FIG. 4, the FC has a structure in which the fuel gas is supplied through piping that passes through the manifold. Therefore, when the fuel gas flow rate is small, the pressure loss in each unit cell flow path is small, so the manifold The fuel gas flowing into the fuel cell proceeded in almost the same direction, and a large amount of fuel gas flowed into the unit cell near the inflowing fuel pipe, resulting in a deviation that the number of ends was small. In particular, the fuel gas consists of carbon dioxide and hydrogen, and when used for power generation, only hydrogen decreases, so the specific gravity of the fuel gas after use of FC is
Remarkably large. As a result, when the fuel gas flow rate is low,
After the FC is used, the fuel gas tends to stay in the lower part of the FC stack and hinder the supply of new fuel gas to the lower unit cell.
以上の原因により、従来のFC発電プラントでは、低流
量時の燃料ガスの不均一性のため、燃料の利用率を高く
することができず、大部分の燃料ガスを捨てていた。こ
のため、FCの発電コストは、高いものとなっていた。Due to the above reasons, in the conventional FC power plant, the fuel utilization rate cannot be increased due to the non-uniformity of the fuel gas at a low flow rate, and most of the fuel gas is discarded. Therefore, the power generation cost of FC was high.
[発明の目的] 本発明は、上記不都合を除去し、FCスタックを構成す
る単位セルに均等に燃料ガスを供給することのできる燃
料系の再循環装置を提供することを目的とする。[Object of the Invention] An object of the present invention is to eliminate the above-mentioned inconvenience and to provide a fuel system recirculation device capable of uniformly supplying a fuel gas to unit cells constituting an FC stack.
[発明の概要] 低負荷時での燃料ガス流の不均一性を除くため、本発
明は、燃料電池と、前記燃料電池からの排燃料ガスを前
記燃料電池に再供給する燃料ガス再循環系と、前記燃料
電池に供給される燃料ガスの圧力と、前記燃料電池から
排出される排燃料ガスの圧力との差圧を測定する差圧検
出手段と、前記差圧検出手段による測定値と差圧目標値
とをもとに、前記燃料ガス再循環系の流量目標値を演算
する演算手段と、前記燃料ガス再循環系を流れる排燃料
ガスの流量を測定する流量測定手段と、前記演算手段か
らの流量目標値と前記流量測定手段からの流量測定値と
をもとに、前記燃料ガス再循環系の流量調節弁の開度信
号を算出する流量調節手段と、を有することを特徴とす
るものである。この結果、低負荷時、FCの必要な水素が
少量で、外部からの燃料供給量がそれに合わせて少ない
場合にも、FCスタック内には、十分な流量が確保されて
いる。SUMMARY OF THE INVENTION In order to eliminate the non-uniformity of fuel gas flow at low load, the present invention provides a fuel cell and a fuel gas recirculation system for re-supplying exhaust fuel gas from the fuel cell to the fuel cell. A differential pressure detecting means for measuring the differential pressure between the pressure of the fuel gas supplied to the fuel cell and the pressure of the exhausted fuel gas discharged from the fuel cell; and a difference between the measured value by the differential pressure detecting means. Calculating means for calculating a flow rate target value of the fuel gas recirculation system based on a pressure target value, flow rate measuring means for measuring a flow rate of exhaust fuel gas flowing through the fuel gas recirculation system, and the calculating means Flow rate adjusting means for calculating an opening signal of the flow rate adjusting valve of the fuel gas recirculation system based on the flow rate target value from the flow rate measuring means and the flow rate measured value from the flow rate measuring means. It is a thing. As a result, when the load is low and the amount of hydrogen required for FC is small and the amount of fuel supplied from the outside is small accordingly, a sufficient flow rate is secured in the FC stack.
[発明の効果] 上記の燃料系の再循環装置により、各単位セルにはほ
ぼ均等な燃料流を確保できるので、全ての単位セルの燃
料利用率がほぼ同じになり、したがって低負荷時、即ち
燃料ガスの低流量時においても、高い燃料利用率が可能
となる。この結果、FC発電システムの経済性が著しく向
上する。[Effects of the Invention] Since the fuel recirculation device described above can ensure a substantially uniform fuel flow in each unit cell, the fuel utilization rate of all unit cells becomes substantially the same, and therefore, at the time of low load, that is, A high fuel utilization rate is possible even when the flow rate of the fuel gas is low. As a result, the economic efficiency of the FC power generation system is significantly improved.
また、燃料ガスの再循環量の増加に伴い、FCスタック
内の水素分圧が低下するので、この現象を利用して電圧
制御を行うこともできる。しかも、低負荷時ほど、FCス
タック内の流量確保のため再循環量を大きく取る必要が
あるが、これは同時に、低負荷時の電圧を硬化させる。
低負荷時には、触媒保護のため、電池電圧を下げる必要
があるので、燃料ガスの再循環量による調節は極めて有
効である。In addition, since the hydrogen partial pressure in the FC stack decreases as the recirculation amount of the fuel gas increases, this phenomenon can also be used for voltage control. In addition, the lower the load, the larger the amount of recirculation required to secure the flow rate in the FC stack, but this also cures the voltage at the low load.
When the load is low, it is necessary to lower the cell voltage in order to protect the catalyst. Therefore, adjustment by the recirculation amount of fuel gas is extremely effective.
[発明の実施例] 以下、本発明によって構成されるFC発電プラント燃料
系の再循環装置の一実施例を第1図に従い詳細に説明す
る。この実施例では、FC4の排燃料ガスラインから供給
ラインへ至る燃料ガスの再循環ライン9を設け、このラ
インに排燃料ガスを流すブロワ10と、その流量を調節す
る弁11を用いて、FC4内での燃料ガスの圧損を差圧計12
で測定し、この圧損が目標値になるように、調節計13で
再循環量を流量計14で検知しつつ、制御する。[Embodiment of the Invention] An embodiment of an FC power plant fuel system recirculation apparatus according to the present invention will be described in detail below with reference to FIG. In this embodiment, a fuel gas recirculation line 9 from the exhaust fuel gas line of FC4 to the supply line is provided, and a blower 10 for flowing the exhaust fuel gas to this line and a valve 11 for adjusting the flow rate thereof are used for FC4 Pressure loss of fuel gas inside the differential pressure gauge 12
The control unit 13 controls the flow rate meter 14 to detect the recirculation amount so that the pressure loss reaches a target value.
また、調節計13のアルゴリズムは、第2図に示すよう
に、差圧目標値とその測定値の差からPI演算により燃料
ガスの再循環流量目標値を求め、この目標値と、再循環
流量の測定値との差から再循環流量弁の開度を、PI演算
により求め、燃料ガス再循環系の流量を調節する流量調
節手段である弁11に出力する。As shown in FIG. 2, the algorithm of the controller 13 obtains the fuel gas recirculation flow rate target value by PI calculation from the difference between the differential pressure target value and its measured value, and determines this target value and the recirculation flow rate. The opening of the recirculation flow valve is obtained from the difference between the measured value and the measured value by the PI calculation, and is output to the valve 11 which is a flow rate adjusting means for adjusting the flow rate of the fuel gas recirculation system.
この実施例によって、FCスタック内で常に所定以上の
圧損を発生させることができ、スタック内の各単位セル
の燃料流を均一にすることができる。According to this embodiment, it is possible to constantly generate a pressure loss of a predetermined value or more in the FC stack, and to make the fuel flow of each unit cell in the stack uniform.
第1図は、本発明にかかる燃料ガス再循環システムの一
実施例を示す構成図、第2図は、調節計の演算アルゴリ
ズムのブロック図、第3図は、従来のFC発電プラント燃
料系の構成図、第4図は、FCスタックの構造図である。 1……改質器、2……シフトコンバータ 3……弁、4……燃料電池 5……改質器バーナ、6……燃料電池スタック 7……マニホールド、8……圧力容器 9……燃料ガス再循環ライン 10……ブロワー、11……弁 12……差圧計、13……調節計 14……流量計、15……燃料ガス流量計 16……演算装置FIG. 1 is a block diagram showing an embodiment of a fuel gas recirculation system according to the present invention, FIG. 2 is a block diagram of a calculation algorithm of a controller, and FIG. 3 is a conventional FC power plant fuel system. FIG. 4 is a structural diagram of the FC stack. 1 ... Reformer, 2 ... Shift converter 3 ... Valve, 4 ... Fuel cell 5 ... Reformer burner, 6 ... Fuel cell stack 7 ... Manifold, 8 ... Pressure vessel 9 ... Fuel Gas recirculation line 10 …… Blower, 11 …… Valve 12 …… Differential pressure gauge, 13 …… Controller 14 …… Flowmeter, 15 …… Fuel gas flowmeter 16 …… Computer
Claims (1)
する燃料ガス再循環系と、 前記燃料電池に供給される燃料ガスの圧力と、前記燃料
電池から排出される排燃料ガスの圧力との差圧を測定す
る差圧検出手段と、 前記差圧検出手段による測定値と差圧目標値とをもと
に、前記燃料ガス再循環系の流量目標値を演算する演算
手段と、 前記燃料ガス再循環系を流れる排燃料ガスの流量を測定
する流量測定手段と、 前記演算手段からの流量目標値と前記流量測定手段から
の流量測定値とをもとに、前記燃料ガス再循環系の流量
調節弁の開度信号を算出する流量調節手段と、 を有することを特徴とする燃料電池発電システム燃料系
の再循環装置。1. A fuel cell, a fuel gas recirculation system for re-supplying exhaust fuel gas from the fuel cell to the fuel cell, a pressure of the fuel gas supplied to the fuel cell, and an exhaust from the fuel cell. The differential pressure detection means for measuring the differential pressure with the pressure of the exhausted fuel gas, and the flow rate target value of the fuel gas recirculation system based on the measured value and the differential pressure target value by the differential pressure detection means. Based on the flow rate target value from the calculation means and the flow rate measurement value from the flow rate measurement means, the flow rate measurement means for measuring the flow rate of the exhaust fuel gas flowing through the fuel gas recirculation system, A flow rate adjusting means for calculating an opening signal of a flow rate adjusting valve of the fuel gas recirculation system, and a recirculation device for a fuel system of the fuel cell power generation system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60138919A JPH0831324B2 (en) | 1985-06-27 | 1985-06-27 | Fuel cell power generation system Fuel system recirculation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60138919A JPH0831324B2 (en) | 1985-06-27 | 1985-06-27 | Fuel cell power generation system Fuel system recirculation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS622461A JPS622461A (en) | 1987-01-08 |
| JPH0831324B2 true JPH0831324B2 (en) | 1996-03-27 |
Family
ID=15233203
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60138919A Expired - Fee Related JPH0831324B2 (en) | 1985-06-27 | 1985-06-27 | Fuel cell power generation system Fuel system recirculation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0831324B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101240981B1 (en) * | 2010-11-19 | 2013-03-11 | 현대자동차주식회사 | Method for estimating hydrogen recirculation flow rate of fuel cell system |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4672120B2 (en) * | 2000-08-24 | 2011-04-20 | 三菱重工業株式会社 | Fuel cell device and method of operating fuel cell device. |
| CN1291516C (en) * | 2001-08-16 | 2006-12-20 | 亚太燃料电池科技股份有限公司 | Anode gas circulation system for fuel cells |
| WO2008034454A1 (en) * | 2006-09-20 | 2008-03-27 | Daimler Ag | Recirculation arrangement for an anode-side gas supply in a fuel cell apparatus and fuel cell apparatus for mobile use |
| JP7415971B2 (en) * | 2021-02-08 | 2024-01-17 | トヨタ自動車株式会社 | fuel cell system |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58133784A (en) * | 1982-02-01 | 1983-08-09 | Hitachi Ltd | Fuel cell power plant control system |
| JPS607068A (en) * | 1983-06-24 | 1985-01-14 | Toshiba Corp | Fuel cell power generation system |
-
1985
- 1985-06-27 JP JP60138919A patent/JPH0831324B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101240981B1 (en) * | 2010-11-19 | 2013-03-11 | 현대자동차주식회사 | Method for estimating hydrogen recirculation flow rate of fuel cell system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS622461A (en) | 1987-01-08 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |