JPH0845512A - Manufacture of electrode for phosphoric acid type fuel cell - Google Patents
Manufacture of electrode for phosphoric acid type fuel cellInfo
- Publication number
- JPH0845512A JPH0845512A JP6195966A JP19596694A JPH0845512A JP H0845512 A JPH0845512 A JP H0845512A JP 6195966 A JP6195966 A JP 6195966A JP 19596694 A JP19596694 A JP 19596694A JP H0845512 A JPH0845512 A JP H0845512A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- electrode
- phosphoric acid
- fuel cell
- surfactant
- 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
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
Landscapes
- Inert Electrodes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、リン酸型燃料電池用電
極の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a phosphoric acid fuel cell electrode.
【0002】[0002]
【従来の技術】リン酸型燃料電池用電極は、カーボンペ
ーパー等の多孔性電極基板上に触媒担持カーボン及びP
TFE(ポリテトラフロオロエチレン)等の撥水性素材
を塗着して電極反応層として構成されている。従来、リ
ン酸型燃料電池用電極は、触媒担持カーボン粉末に界面
活性剤を加えて混合し、この混合液にPTFEディスパ
ージョンを滴下しながら三本ロールや超音波ホモジナイ
ザー等の混合分散装置を使用し混合分散してペースト状
混合物とし、このペースト状混合物を多孔性電極基板上
に塗布した後、乾燥し、洗浄し、再度乾燥した後プレス
成形し、焼成することによって製造されている。2. Description of the Related Art An electrode for a phosphoric acid fuel cell is a catalyst carrying carbon and P on a porous electrode substrate such as carbon paper.
A water-repellent material such as TFE (polytetrafluoroethylene) is applied to form an electrode reaction layer. Conventionally, for phosphoric acid fuel cell electrodes, a surfactant is added to a catalyst-supporting carbon powder and mixed, and a PTFE dispersion is added dropwise to this mixture and a mixing / dispersing device such as a three-roll or ultrasonic homogenizer is used. Then, the mixture is mixed and dispersed to form a paste-like mixture, and the paste-like mixture is applied on a porous electrode substrate, dried, washed, dried again, press-molded, and fired.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、従来の
リン酸型燃料電池用電極の製造方法では、触媒担持カー
ボン粉末及びPTFE粉末の分散が悪く、凝集塊が生成
するため、触媒利用率、ガス拡散性に改良の余地があ
る。又、分散を良くするために添加した界面活性剤が除
去されずに電極中に残留し、電極の濡れを進行させ、そ
の寿命を短くする不具合がある。そこで、本発明は触媒
及びPTFEを良く分散させることにより触媒、電解
質、ガスの三層界面を多く作り、結果として触媒利用率
を高め、かつガス拡散性を良好にし得、更に寿命を長く
し得るリン酸型燃料電池用電極の製造方法を提供するこ
とを目的とする。However, in the conventional method for manufacturing an electrode for a phosphoric acid fuel cell, the catalyst-supporting carbon powder and the PTFE powder are poorly dispersed, and agglomerates are formed. There is room for improvement in sex. Further, there is a problem that the surfactant added for improving the dispersion remains in the electrode without being removed, which promotes the wetting of the electrode and shortens its life. Therefore, in the present invention, the catalyst and the PTFE are well dispersed to form many three-layer interfaces of the catalyst, the electrolyte, and the gas. As a result, the catalyst utilization rate can be increased, the gas diffusivity can be improved, and the life can be further extended. An object of the present invention is to provide a method for manufacturing a phosphoric acid fuel cell electrode.
【0004】[0004]
【課題を解決するための手段】前記課題を解決するた
め、本発明のリン酸型燃料電池用電極の製造方法は、多
孔性電極基板上に触媒担持カーボン粉末をPTFE粉末
で塗着してなるリン酸型燃料電池用電極を製造するに際
し、触媒担持カーボン粉末に所要濃度の界面活性剤水溶
液を加えてボールミルで粉砕して触媒分散液とする一
方、上記界面活性剤水溶液より低濃度の界面活性剤水溶
液にPTFEディスパージョンを滴下しながら撹拌し、
このPTFE分散液に前記触媒分散液及び所要量の水を
加えて撹拌し、この混合液をろ物が均一な厚さとなるよ
うに多孔性シートでろ過し、ろ物を多孔性電極基板に転
写した後、プレス成形し、乾燥し、焼成した後洗浄し、
再度乾燥することを特徴とする。ボールミルとしては遊
星ボールミルを用いることが望ましい。前記カーボン粉
末に担持された触媒は、Pt又はPt合金であることが
好ましい。前記所要濃度の界面活性剤水溶液は、濃度0.
10〜20.0重量%の界面活性剤水溶液であることが好まし
い。0.10重量%未満では粉砕された触媒を分散させるに
は不十分であり、10.0重量%を超えると、ミル中のペー
ストの粘度が上がり、粉砕効率が悪くなる。前記低濃度
の界面活性剤水溶液は、濃度0.01〜0.10重量%の界面活
性剤水溶液であることが好ましい。この範囲の外では分
散液が不安定である。前記所要量の水は、全体の界面活
性剤濃度を0.05〜 5.0重量%にするものであることが好
ましい。0.05重量%未満では分散液が不安定であり、
5.0重量%を超えると、後で除去するのが難しい。又、
前記多孔性シートは、PTFEシートであることが好ま
しい。In order to solve the above problems, the method for producing an electrode for a phosphoric acid fuel cell according to the present invention comprises coating a catalyst-carrying carbon powder with a PTFE powder on a porous electrode substrate. When manufacturing an electrode for a phosphoric acid fuel cell, a surfactant-containing aqueous solution of the required concentration was added to the catalyst-supporting carbon powder and pulverized with a ball mill to form a catalyst dispersion, while a surfactant with a lower concentration than the above-mentioned surfactant-containing aqueous solution was used. Stir while adding PTFE dispersion to the aqueous solution of the agent,
The catalyst dispersion and the required amount of water were added to this PTFE dispersion and stirred, and the mixture was filtered with a porous sheet so that the filtrate had a uniform thickness, and the filter was transferred to a porous electrode substrate. After that, press molding, drying, baking and washing,
It is characterized by being dried again. It is desirable to use a planetary ball mill as the ball mill. The catalyst supported on the carbon powder is preferably Pt or a Pt alloy. The required concentration of the aqueous surfactant solution has a concentration of 0.
It is preferably a 10 to 20.0% by weight aqueous surfactant solution. If it is less than 0.10% by weight, it is insufficient to disperse the crushed catalyst, and if it exceeds 10.0% by weight, the viscosity of the paste in the mill is increased and the pulverization efficiency is deteriorated. The low concentration aqueous surfactant solution is preferably a surfactant aqueous solution having a concentration of 0.01 to 0.10% by weight. The dispersion is unstable outside this range. The required amount of water is preferably such that the total surfactant concentration is 0.05 to 5.0% by weight. If it is less than 0.05% by weight, the dispersion is unstable,
If it exceeds 5.0% by weight, it is difficult to remove it later. or,
The porous sheet is preferably a PTFE sheet.
【0005】[0005]
【作用】本発明のリン酸型燃料電池用電極の製造方法に
おいては、触媒担持カーボン粉末がボールミルで湿式粉
砕されて細かくなり、その細かい粒子表面に界面活性剤
が吸着される。又、PTFEディスパージョンも界面活
性剤水溶液に滴下して希釈することにより、凝集が妨げ
られ、安定した分散液となる。そして、触媒分散液とP
TFE分散液を混合することにより、触媒担持カーボン
粒子とPTFE粒子が均一に分散される。又、ろ過によ
って余分な界面活性剤が取り除かれ、又、残った界面活
性剤の多くは触媒担持カーボン粒子に吸着しているが、
焼成の際に触媒の作用で容易に分解されて除去され、か
つ焼成した後に洗浄することにより、分解物も除去され
る。プレス成形前に洗浄してしまうと、多孔性電極基板
との密着性が悪くなり、ひび、剥がれ等の原因となる。In the method for producing the phosphoric acid fuel cell electrode of the present invention, the catalyst-supporting carbon powder is wet-milled by the ball mill to be fine, and the surface of the fine particles adsorbs the surfactant. Further, the PTFE dispersion is also dropped into the aqueous surfactant solution to be diluted, whereby aggregation is prevented and a stable dispersion liquid is obtained. Then, the catalyst dispersion and P
By mixing the TFE dispersion liquid, the catalyst-supporting carbon particles and the PTFE particles are uniformly dispersed. Further, the excess surfactant is removed by filtration, and most of the remaining surfactant is adsorbed on the catalyst-supporting carbon particles.
During calcination, it is easily decomposed and removed by the action of the catalyst, and decomposed products are also removed by washing after calcination. If it is washed before press molding, the adhesion to the porous electrode substrate deteriorates, causing cracks and peeling.
【0006】[0006]
【実施例】以下、本発明の実施例について従来例と共に
説明する。先ず、触媒としてPt合金(Pt:Ni:C
o=2:1:1(モル))粉末を担持した触媒担持カー
ボン粉末(カーボン1g相当)に5重量%界面活性剤水
溶液5gを加え、遊星ボールミルを用いて30分間湿式粉
砕して触媒分散液を精製した。次いで、0.05重量%界面
活性剤水溶液 350gをビーカーに入れ、これにPTFE
ディスパージョンを滴下しながらスターラを用いて10分
間撹拌し、このPTFE分散液に前記触媒分散液と全体
の界面活性剤濃度を 0.05 重量%にするに足る水とを加
えて30分間撹拌した。次に、上記混合液をろ物が均一な
厚さ(例えば 150μm)となるように多孔性のPTFE
シートでろ過し、ろ物をカーボンペーパー等の多孔性電
極基板に転写した後、プレス成形した。然る後、60℃の
温度で1時間乾燥し、 350℃の温度で30分かけて焼成し
た後、洗浄し、再度60℃の温度で乾燥して電極を得た。EXAMPLES Examples of the present invention will be described below together with conventional examples. First, as a catalyst, a Pt alloy (Pt: Ni: C)
o = 2: 1: 1 (mol)) catalyst-supporting carbon powder (corresponding to 1 g of carbon) to which 5 g of a 5% by weight aqueous solution of a surfactant is added, and wet-milled for 30 minutes using a planetary ball mill to prepare a catalyst dispersion liquid. Was purified. Then, 350 g of 0.05% by weight aqueous surfactant solution was placed in a beaker, and PTFE was added thereto.
The dispersion was added dropwise and stirred for 10 minutes using a stirrer. To this PTFE dispersion, the catalyst dispersion and water sufficient to make the total surfactant concentration 0.05% by weight were added and stirred for 30 minutes. Next, the above-mentioned mixed solution is added to the porous PTFE so that the filtrate has a uniform thickness (for example, 150 μm).
After filtering with a sheet and transferring the filter to a porous electrode substrate such as carbon paper, press molding was performed. Then, it was dried at a temperature of 60 ° C. for 1 hour, baked at a temperature of 350 ° C. for 30 minutes, washed, and dried again at a temperature of 60 ° C. to obtain an electrode.
【0007】[0007]
【従来例】先ず、実施例と同様の触媒担持カーボン粉末
(カーボン2g相当)に20重量%界面活性剤水溶液17g
を加えて混合した後、これにPTFEディスパージョン
を滴下しながら三本ロールミルを用いて混合分散してペ
ースト状混合物とした。次いで、上記ペースト状混合物
をカーボンペーパー等の多孔性電極基板上に均一な厚さ
となるように塗布し、これを60℃の温度で一時間乾燥し
た後、洗浄し、再度60℃の温度で乾燥した後プレス成形
し、 350℃の温度で30分かけて焼成して電極を得た。Conventional Example First, the same catalyst-supporting carbon powder (corresponding to 2 g of carbon) as in the example was used, and 17 g of 20% by weight aqueous surfactant solution
Was added and mixed, and then the PTFE dispersion was added dropwise thereto and mixed and dispersed using a three-roll mill to obtain a paste-like mixture. Next, the above paste-like mixture is applied on a porous electrode substrate such as carbon paper so as to have a uniform thickness, dried at 60 ° C for 1 hour, washed, and dried again at 60 ° C. After that, it was press-molded and baked at a temperature of 350 ° C. for 30 minutes to obtain an electrode.
【0008】実施例、従来例で得た電極をリン酸型燃料
電池用電極として用いた場合の発電特性を表1に示す。Table 1 shows the power generation characteristics when the electrodes obtained in Examples and Conventional Examples were used as electrodes for phosphoric acid fuel cells.
【0009】[0009]
【表1】 [Table 1]
【0010】表1から明らかなように、実施例のリン酸
型燃料電池用電極は、従来例のそれよりも高い触媒利用
率及びガス拡散性を達成できた。又、電極寿命について
も、電位の低下が少ないことやO2 −gainの上昇速
度が小さいことから、より長寿命化していることが判
る。As is clear from Table 1, the phosphoric acid fuel cell electrodes of the examples were able to achieve higher catalyst utilization and gas diffusivity than those of the conventional examples. Regarding the electrode life, it can be seen that the life is extended because the decrease in the potential is small and the rate of increase of O 2 -gain is small.
【0011】なお、上記実施例においては、ボールミル
として遊星ボールミルを用いる場合について述べたが、
これに限らずアトライター、バイブレーション等のボー
ルミルを用いても良い。In the above embodiment, the planetary ball mill is used as the ball mill.
Not limited to this, a ball mill such as an attritor or a vibration may be used.
【0012】[0012]
【発明の効果】以上説明したように、本発明のリン酸型
燃料電池用電極の製造方法によれば、触媒担持カーボン
粉末が細かくなり、その細かい粒子表面に表面活性剤が
吸着され、又、PTFE分散液も界面活性剤の存在で凝
集が妨げられ、個別に調製した触媒分散液とPTFE分
散液を混合することにより、触媒担持カーボン粒子とP
TFE粒子が均一に分散されるので、従来に比べて高い
触媒利用率とガス拡散性を得ることができる。又、ろ過
によって余分な界面活性剤が取り除かれ、又、残った界
面活性剤が焼成時に触媒の作用で分解、除去され、かつ
焼成後の洗浄により除去されるので、従来のように電極
の濡れが進行しにくくなってその長寿命化を図ることが
できる。As described above, according to the method for producing a phosphoric acid fuel cell electrode of the present invention, the catalyst-carrying carbon powder becomes fine, and the surface active agent is adsorbed on the surface of the fine particles. Aggregation of the PTFE dispersion is also hindered by the presence of the surfactant, and the catalyst-supported carbon particles and P are mixed by mixing the individually prepared catalyst dispersion with the PTFE dispersion.
Since the TFE particles are uniformly dispersed, it is possible to obtain a higher catalyst utilization rate and a higher gas diffusivity than ever before. In addition, the excess surfactant is removed by filtration, and the remaining surfactant is decomposed and removed by the action of the catalyst during firing, and is removed by washing after firing. Is less likely to progress, and its life can be extended.
Claims (6)
末をPTFE粉末で塗着してなるリン酸型燃料電池用電
極を製造するに際し、触媒担持カーボン粉末に所要濃度
の界面活性剤水溶液を加えてボールミルで粉砕して触媒
分散液とする一方、上記界面活性剤水溶液より低濃度の
界面活性剤水溶液にPTFEディスパージョンを滴下し
ながら攪拌し、このPTFE分散液に前記触媒分散液及
び所要量の水を加えて撹拌し、この混合液をろ物が均一
な厚さとなるように多孔性シートでろ過し、ろ物を多孔
性電極基板に転写した後、プレス成形し、乾燥し、焼成
した後洗浄し、再度乾燥することを特徴とするリン酸型
燃料電池用電極の製造方法。1. When manufacturing a phosphoric acid fuel cell electrode in which a catalyst-carrying carbon powder is coated on a porous electrode substrate with PTFE powder, a surfactant-containing aqueous solution of a required concentration is added to the catalyst-carrying carbon powder. While crushing with a ball mill to obtain a catalyst dispersion, while stirring the PTFE dispersion while dripping the PTFE dispersion into the surfactant aqueous solution having a lower concentration than the above surfactant aqueous solution, the catalyst dispersion and the required amount of the PTFE dispersion are added. After adding water and stirring, the mixture was filtered with a porous sheet so that the filter cake had a uniform thickness, the filter cake was transferred to a porous electrode substrate, and then press-molded, dried and baked. A method for producing an electrode for a phosphoric acid fuel cell, which comprises washing and drying again.
た事を特徴とする請求項1に記載のリン酸型燃料電池用
電極の製造方法。2. The method for producing a phosphoric acid fuel cell electrode according to claim 1, wherein a planetary ball mill is used as the ball mill.
Pt又はPt合金であることを特徴とする請求項1又は
2に記載のリン酸型燃料電池用電極の製造方法。3. The catalyst supported on the carbon powder,
It is Pt or Pt alloy, The manufacturing method of the electrode for phosphoric acid fuel cells of Claim 1 or 2 characterized by the above-mentioned.
0.10〜20.0重量%の界面活性剤水溶液であることを特徴
とする請求項1、2又は3記載のリン酸型燃料電池用電
極の製造方法。4. The concentration of the aqueous surfactant solution having the required concentration
The method for producing an electrode for a phosphoric acid fuel cell according to claim 1, 2 or 3, which is a 0.10 to 20.0% by weight aqueous surfactant solution.
01〜0.10重量%の界面活性剤水溶液であることを特徴と
する請求項1、2、3又は4記載のリン酸型燃料電池用
電極の製造方法。5. The low-concentration aqueous surfactant solution has a concentration of 0.
The method for producing an electrode for a phosphoric acid fuel cell according to claim 1, 2, 3 or 4, which is an aqueous solution of a surfactant of 01 to 0.10% by weight.
度を0.05〜 5.0重量%にするものであることを特徴とす
る請求項1、2、3、4又は5記載のリン酸型燃料電池
用電極の製造方法。6. The phosphoric acid type product according to claim 1, wherein the required amount of water makes the total surfactant concentration 0.05 to 5.0% by weight. Manufacturing method of fuel cell electrode.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6195966A JPH0845512A (en) | 1994-07-28 | 1994-07-28 | Manufacture of electrode for phosphoric acid type fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6195966A JPH0845512A (en) | 1994-07-28 | 1994-07-28 | Manufacture of electrode for phosphoric acid type fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0845512A true JPH0845512A (en) | 1996-02-16 |
Family
ID=16349958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6195966A Pending JPH0845512A (en) | 1994-07-28 | 1994-07-28 | Manufacture of electrode for phosphoric acid type fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0845512A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003100305A (en) * | 2001-09-19 | 2003-04-04 | Matsushita Electric Ind Co Ltd | Method of manufacturing electrode for fuel cell |
WO2007106963A1 (en) * | 2006-03-17 | 2007-09-27 | Coppe/Ufrj - Coordenação Dos Programas De Pós Graduação De Engenharia Da Universidade Federal Do Rio De Janeiro | Process for obtaining aqueous suspensions for electrodes of solid oxide fuel cells and other electrocatalytic devices |
JP2011072872A (en) * | 2009-09-29 | 2011-04-14 | Equos Research Co Ltd | Treatment method of catalyst carrying carbon and electrode for fuel cell |
JP2011076806A (en) * | 2009-09-30 | 2011-04-14 | Sekisui Chem Co Ltd | Paste for electrode, electrode, membrane-electrode assembly, and fuel cell |
JP2011078890A (en) * | 2009-10-06 | 2011-04-21 | Equos Research Co Ltd | Method for manufacturing catalyst |
-
1994
- 1994-07-28 JP JP6195966A patent/JPH0845512A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003100305A (en) * | 2001-09-19 | 2003-04-04 | Matsushita Electric Ind Co Ltd | Method of manufacturing electrode for fuel cell |
WO2007106963A1 (en) * | 2006-03-17 | 2007-09-27 | Coppe/Ufrj - Coordenação Dos Programas De Pós Graduação De Engenharia Da Universidade Federal Do Rio De Janeiro | Process for obtaining aqueous suspensions for electrodes of solid oxide fuel cells and other electrocatalytic devices |
JP2011072872A (en) * | 2009-09-29 | 2011-04-14 | Equos Research Co Ltd | Treatment method of catalyst carrying carbon and electrode for fuel cell |
JP2011076806A (en) * | 2009-09-30 | 2011-04-14 | Sekisui Chem Co Ltd | Paste for electrode, electrode, membrane-electrode assembly, and fuel cell |
JP2011078890A (en) * | 2009-10-06 | 2011-04-21 | Equos Research Co Ltd | Method for manufacturing catalyst |
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