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JP2000087279A - Gas diffusion electrode using bonded body of gas supply layer and porous metal - Google Patents

Gas diffusion electrode using bonded body of gas supply layer and porous metal

Info

Publication number
JP2000087279A
JP2000087279A JP10254116A JP25411698A JP2000087279A JP 2000087279 A JP2000087279 A JP 2000087279A JP 10254116 A JP10254116 A JP 10254116A JP 25411698 A JP25411698 A JP 25411698A JP 2000087279 A JP2000087279 A JP 2000087279A
Authority
JP
Japan
Prior art keywords
porous
gas diffusion
diffusion electrode
ptfe
porous metal
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.)
Granted
Application number
JP10254116A
Other languages
Japanese (ja)
Other versions
JP2987583B1 (en
Inventor
Choichi Furuya
長一 古屋
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.)
Mitsui Chemicals Inc
Toagosei Co Ltd
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Mitsui Chemicals Inc
Toagosei Co Ltd
Kanegafuchi Chemical Industry Co Ltd
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Filing date
Publication date
Application filed by Mitsui Chemicals Inc, Toagosei Co Ltd, Kanegafuchi Chemical Industry Co Ltd filed Critical Mitsui Chemicals Inc
Priority to JP10254116A priority Critical patent/JP2987583B1/en
Application granted granted Critical
Publication of JP2987583B1 publication Critical patent/JP2987583B1/en
Publication of JP2000087279A publication Critical patent/JP2000087279A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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

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  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Inert Electrodes (AREA)

Abstract

(57)【要約】 【課題】 金属多孔体とフィブリル化PTFE多孔体シ
ートを強固に接合したガス供給層と金属多孔体との接合
体、及びこれを用いた長寿命で高性能のガス拡散電極を
提供する。 【解決手段】 金属多孔体とカーボンブラックを0〜5
5%含むフィブリル化PTFE撥水性多孔体シートと
を、温度がPTFEの融点以上、圧力が接触実圧力20
kg/cm2 以上でホットプレスすることによって金属
多孔体と前記撥水性多孔体シートを強固に接合したこと
を特徴とするガス拡散電極用金属多孔体−撥水性多孔体
シート接合体。請求項1の接合体の金属多孔体側から反
応層材料を充填し、反応層材料の最適条件でホットプレ
スすることによって作製したことを特徴とするガス拡散
電極。
PROBLEM TO BE SOLVED: To provide a bonded body of a gas supply layer in which a porous metal body and a fibrillated PTFE porous sheet are firmly bonded to a porous metal body, and a long-life and high-performance gas diffusion electrode using the same. I will provide a. SOLUTION: A metal porous body and carbon black are added in an amount of 0 to 5;
A fibrillated PTFE water-repellent porous sheet containing 5% and a temperature equal to or higher than the melting point of PTFE;
A porous metal-water-repellent porous sheet assembly for a gas diffusion electrode, wherein the porous metal and the water-repellent porous sheet are strongly bonded by hot pressing at a pressure of at least kg / cm 2 . A gas diffusion electrode produced by filling a reaction layer material from the porous metal side of the joined body of claim 1 and hot-pressing the reaction layer material under optimum conditions.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ガス拡散電極特に
食塩電解等に使用されるガス拡散電極用の金属多孔体−
撥水性多孔体シート接合体、及びそれから得られたガス
拡散電極に関し、特に寿命が長いガス拡散電極に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a metal porous body for a gas diffusion electrode, particularly for a gas diffusion electrode used for salt electrolysis and the like.
The present invention relates to a water-repellent porous sheet assembly and a gas diffusion electrode obtained therefrom, and particularly to a gas diffusion electrode having a long life.

【0002】[0002]

【従来の技術】従来、ガス拡散電極においては、反応層
が銀微粒子を担持したカーボンブラックとPTFEのよ
うな樹脂結合材から成り、ガス供給層がPTFEのよう
な樹脂結合材多孔体から成るガス拡散電極があった。し
かしながら、このようなガス拡散電極を酸素極に用いた
場合には、触媒が担持されたカーボンブラックは徐々に
酸化され、担体のカーボンブラックの消滅による触媒微
粒子の脱落、導電性の低下、親水性の増大による三相帯
界面の減少等により、電極性能の低下を来たし、2年以
上の電極寿命が達成できないという問題点があった。食
塩電解槽に使用する場合は5年以上の耐久性が必要であ
るため、このような電極寿命が短い電極ではこの種の電
解槽には使用することができない。そこで、カーボンの
腐食の心配がない銀微粒子とPTFEのみから成る反応
層を持つガス拡散電極が提案され、長寿命が期待されて
いるものとしては、反応層が銀微粒子とPTFE、ガス
供給層がPTFE多孔体から成る非カーボンブラック系
ガス拡散電極があった。
2. Description of the Related Art Conventionally, in a gas diffusion electrode, a reaction layer is formed of carbon black carrying silver fine particles and a resin binder such as PTFE, and a gas supply layer is formed of a resin binder porous body such as PTFE. There was a diffusion electrode. However, when such a gas diffusion electrode is used as an oxygen electrode, the carbon black carrying the catalyst is gradually oxidized, and the fine particles of the catalyst fall off due to disappearance of the carbon black of the carrier, the conductivity is reduced, and the hydrophilicity is reduced. As a result, the electrode performance deteriorates due to the decrease of the interface of the three-phase zone due to the increase of the thickness, and there is a problem that the electrode life of two years or more cannot be achieved. When used in a salt electrolyzer, durability of 5 years or more is required. Therefore, an electrode having such a short electrode life cannot be used in this type of electrolyzer. In view of this, a gas diffusion electrode having a reaction layer consisting of only silver fine particles and PTFE, which does not have to worry about carbon corrosion, has been proposed. As a device expected to have a long life, the reaction layer is composed of silver fine particles, PTFE, and a gas supply layer. There was a non-carbon black-based gas diffusion electrode made of PTFE porous material.

【0003】[0003]

【発明が解決しようとする課題】カーボンブラックに触
媒を担持した従来のガス拡散電極は、強度を上げるため
に結着材のPTFEの融点以上の温度で20kg/cm
2 以上の高圧でプレスしている。しかし、銀微粒子とP
TFEのみから成るガス拡散電極においては、このよう
なプレス条件ではPTFEと銀微粒子は柔らかく、変形
し易いので、電解液及びガス通路となる粒子間の細孔が
閉塞したり、酸素還元触媒の銀表面積が激減する。その
ため銀微粒子を担持するカーボンブラックとPTFEを
使用する場合に比べ、プレス温度は融点以下の250
℃、圧力は10kg/cm2 以下の低圧でプレスしなけ
れば必要な電極性能を得ることが出来ない。このような
作製条件で作られた電極は、機械的強度が小さく、壊れ
やすく、取り扱いに細心の注意が必要であるという問題
があった。特に反応層とガス供給層の剥離が起こり易
く、液漏れ、性能低下の原因となる。このため銀系ガス
拡散電極は、2年以上の耐久性を再現性よく達成するの
が困難であった。
A conventional gas diffusion electrode having a catalyst supported on carbon black requires 20 kg / cm at a temperature not lower than the melting point of PTFE as a binder in order to increase strength.
Pressing at 2 or more high pressure. However, silver fine particles and P
In a gas diffusion electrode consisting only of TFE, PTFE and silver fine particles are soft and easily deformed under such pressing conditions, so that pores between particles serving as an electrolyte and a gas passage are blocked, and silver particles of an oxygen reduction catalyst are used. Surface area is drastically reduced. Therefore, compared with the case of using PTFE and carbon black carrying silver fine particles, the pressing temperature is lower than the melting point of 250 ° C.
The required electrode performance cannot be obtained unless pressed at a low pressure of 10 kg / cm 2 or less at a temperature of 10 ° C. An electrode manufactured under such manufacturing conditions has a problem that mechanical strength is small, it is easily broken, and careful handling is required. In particular, separation of the reaction layer and the gas supply layer easily occurs, which causes liquid leakage and performance degradation. For this reason, it has been difficult for the silver-based gas diffusion electrode to achieve durability of two years or more with good reproducibility.

【0004】本発明は、このような従来の問題点に鑑み
てなされたものであり、少なくとも金属多孔体とフィブ
リル化PTFE多孔体シートとを強固に接合したガス供
給層と金属多孔体との接合体、及びこれを用いた長寿命
で高性能のガス拡散電極を提供することを目的とするも
のである。
The present invention has been made in view of such conventional problems, and has been made in consideration of the above-mentioned problems, and is intended to provide a bonding between a gas supply layer in which at least a porous metal body and a fibrillated PTFE porous sheet are firmly bonded, and a porous metal body. It is an object of the present invention to provide a body and a long-life, high-performance gas diffusion electrode using the same.

【0005】[0005]

【課題を解決するための手段】本発明者は、前記課題を
解決すべく鋭意研究した結果、PTFEの融点以上で加
熱されても細孔が無くならないフィブリル化PTFE撥
水性多孔体シートからなるガス供給層シートを、金属多
孔体にPTFEの融点以上の温度、5kg/cm2 以上
の圧力でホットプレスすることより、金属多孔体とガス
供給層を接触実圧力20kg/cm2 以上で強固に接合
した接合体を作製でき、この接合体に反応層原料を充填
して反応層の最適条件でホットプレスすれば、電極の高
い強度を得、かつ反応層の銀微粒子のシンターは起き
ず、ガス供給層の剥離強度の高い電極が得られることを
見出して、本発明を完成するに到った。なお、前記の撥
水性多孔体シートについては、以下単に「多孔体シー
ト」ということがある。
The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that a gas comprising a fibrillated PTFE water-repellent porous sheet which does not lose its pores even when heated above the melting point of PTFE. By hot-pressing the supply layer sheet to the porous metal body at a temperature higher than the melting point of PTFE and a pressure of 5 kg / cm 2 or higher, the porous metal body and the gas supply layer are firmly joined at a contact actual pressure of 20 kg / cm 2 or higher. If the reaction body is filled with the raw material of the reaction layer and hot-pressed under the optimum conditions of the reaction layer, high strength of the electrode can be obtained, and sintering of silver fine particles in the reaction layer does not occur. The inventors have found that an electrode having a high layer peel strength can be obtained, and have completed the present invention. The water-repellent porous sheet may be simply referred to as a “porous sheet” below.

【0006】すなわち、本発明は、次の構成により前記
の課題を解決することができた。 (1)金属多孔体とカーボンブラックを0〜55%含む
フィブリル化PTFE撥水性多孔体シートとを、温度が
PTFEの融点以上、圧力が接触実圧力20kg/cm
2 以上でホットプレスすることによって前記金属多孔体
と前記撥水性多孔体シートを強固に接合したことを特徴
とするガス拡散電極用金属多孔体−撥水性多孔体シート
接合体。 (2)前記(1)の接合体の金属多孔体側から反応層材
料を充填し、反応層材料の最適条件でホットプレスする
ことによって作製したことを特徴とするガス拡散電極。 (3)前記(1)の接合体の撥水性多孔体シートの一部
が無い欠落部を持つ状態で反応層を構成したことを特徴
とする前記(2)記載のガス拡散電極。 (4)前記欠落部に銀の薄板、銀粉を付着させ、ホット
プレスすることによって液浸透性を少なくし、ガス室側
への導電性を改善したことを特徴とする請求項3記載の
ガス拡散電極。
That is, the present invention has solved the above-mentioned problems by the following constitution. (1) A porous metal body and a fibrillated PTFE water-repellent porous sheet containing 0 to 55% of carbon black are heated at a temperature equal to or higher than the melting point of PTFE and at a pressure of 20 kg / cm.
A bonded metal / water-repellent porous sheet for a gas diffusion electrode, wherein the porous metal and the water-repellent porous sheet are strongly bonded by hot pressing with two or more. (2) A gas diffusion electrode prepared by filling the reaction layer material from the porous metal side of the joined body of (1) and hot-pressing the reaction layer material under optimum conditions. (3) The gas diffusion electrode according to the above (2), wherein the reaction layer is formed in a state in which a part of the water-repellent porous sheet of the joined body of the above (1) has a missing portion without any part. (4) The gas diffusion according to claim 3, wherein a thin silver plate or silver powder is adhered to the missing portion and hot pressing is performed to reduce liquid permeability and improve conductivity to the gas chamber side. electrode.

【0007】このように構成することにより、反応層の
金属多孔体とガス供給層シートの剥離等が皆無になっ
た。また電極寿命が飛躍的に増加する。そして、従来、
1回のホットプレスで電極を製造していたものをプレス
を2回にすることにより強度と性能を両立させた。
[0007] With this configuration, the metal porous body of the reaction layer and the gas supply layer sheet are not peeled off. In addition, the life of the electrode is dramatically increased. And conventionally,
The electrode was manufactured by one hot press, but the strength and performance were both achieved by performing the press twice.

【0008】[0008]

【発明の実施の形態】金属多孔体としては、銀網、銀メ
ッキニッケル網、銀エクスパンドメタル、銀メッキ発泡
ニッケルが良好に用いられる。銀網の場合は厚さは10
0〜300ミクロン、線径は100から300ミクロ
ン、ピッチは0.5〜3mmが好適に用いられる。次
に、銀網とフィブリル化PTFE多孔体シート(孔径1
ミクロン)を350℃、20kg/cm2 でホットプレ
スを行い、銀網をPTFE多孔体シートに強固に接合さ
せて、銀網とフィブリル化PTFE多孔体シートとの接
合体を得ることができる。ここで、「フィブリル化され
たPTFE多孔体」というのは、PTFE粉末と液状潤
滑剤との混合物をシート状にした未焼成又は焼成状態の
PTFEシートを加熱下で一軸又は二軸延伸することで
作られ、微小な結節と繊維状からなる多孔体である。フ
ィブリル化PTFE多孔体シートにはカーボンブラック
を含有させてもよく、その含有量はフィブリル化PTF
Eを基準にして55重量%までである。カーボンブラッ
クを含有しない場合もあるから、その含有量は0〜55
重量%ということになる。好適な含有量は40〜50重
量%である。
BEST MODE FOR CARRYING OUT THE INVENTION As a porous metal body, a silver net, a silver-plated nickel net, a silver expanded metal, and a silver-plated nickel foam are preferably used. The thickness is 10 for silver mesh
0 to 300 microns, a wire diameter of 100 to 300 microns, and a pitch of 0.5 to 3 mm are preferably used. Next, a silver mesh and a fibrillated PTFE porous sheet (pore size 1
(Micron) at 350 ° C. and 20 kg / cm 2 , and the silver mesh is firmly bonded to the porous PTFE sheet to obtain a bonded body of the silver mesh and the fibrillated PTFE porous sheet. Here, the term “fibrillated PTFE porous body” refers to a uniaxial or biaxial stretching of an unfired or fired PTFE sheet formed from a mixture of PTFE powder and a liquid lubricant under heating. It is a porous body made of fine nodules and fibers. The fibrillated PTFE porous body sheet may contain carbon black, and the content thereof is determined by the amount of the fibrillated PTFE.
Up to 55% by weight based on E. Since carbon black may not be contained in some cases, its content is from 0 to 55
Weight percent. The preferred content is 40 to 50% by weight.

【0009】この接合体の銀網側から、例えば平均粒径
100nmの銀微粒子(三井金属鉱業社製、Ag−30
10)に界面活性剤を加え、PTFEディスパージョン
D−1(ダイキン工業社製)を添加して分散させ、この
分散液にアルコールを加えて自己組織化させ、濾過して
得た泥しょうを反応層材料として充填する。乾燥後、ア
ルコールを用いた抽出装置で界面活性剤を除去する。乾
燥後、例えば260℃、20kg/cm2 の条件でホッ
トプレスを行い、ガス拡散電極を得る。ホットプレスの
最適条件は材料、組成、分散状態で異なる。
From the silver mesh side of the joined body, for example, silver fine particles having an average particle diameter of 100 nm (Ag-30, manufactured by Mitsui Kinzoku Mining Co., Ltd.)
To 10), a surfactant is added, PTFE dispersion D-1 (manufactured by Daikin Industries, Ltd.) is added and dispersed. Alcohol is added to this dispersion, self-assembled, and the slurry obtained by filtration is reacted. Fill as layer material. After drying, the surfactant is removed with an extraction device using alcohol. After drying, hot pressing is performed at, for example, 260 ° C. and 20 kg / cm 2 to obtain a gas diffusion electrode. The optimum conditions for hot pressing differ depending on the material, composition, and dispersion state.

【0010】上記のプレス条件による本発明の技術的特
徴を図面に基づいて詳細に説明する。図1は、金属多孔
体(例えば銀網)2とフィブリル化PTFE多孔体シー
ト3との接合体1の接合状態を示す断面説明図である。
銀網2とPTFEシート3の接合において、フィブリル
化したPTFEは融点以上で10kg/cm2 以下の圧
力では細孔が無くならない。しかし、20kg/cm2
以上の圧力にすると銀網1とPTFEシート3は接触部
aで融着する。もちろん、銀網2同士、PTFEシート
3同士も接合できる。図2は、上記の接合体1の金属多
孔体2側から反応層材料5を充填し、最適条件でホット
プレスして作製したガス拡散電極4を示す断面説明図で
ある。反応層材料5とPTFEシート3の接触部bは、
PTFEの融点以下の温度でプレスすると、50kg/
cm2 でプレスしてもPTFEの細孔は無くならない
し、反応層との接合強度がある程度はある。全体的な強
度は銀網2とPTFE多孔体3の接触部aで持つことに
なる。
The technical features of the present invention under the above press conditions will be described in detail with reference to the drawings. FIG. 1 is an explanatory cross-sectional view showing a bonded state of a bonded body 1 of a porous metal body (for example, a silver mesh) 2 and a fibrillated PTFE porous sheet 3.
In joining the silver mesh 2 and the PTFE sheet 3, the fibrillated PTFE does not lose its pores at a pressure higher than the melting point and lower than 10 kg / cm 2 . However, 20 kg / cm 2
With the above pressure, the silver mesh 1 and the PTFE sheet 3 are fused at the contact portion a. Of course, the silver meshes 2 and the PTFE sheets 3 can also be joined. FIG. 2 is an explanatory cross-sectional view showing a gas diffusion electrode 4 produced by filling the reaction layer material 5 from the metal porous body 2 side of the above-mentioned joined body 1 and hot-pressing it under optimum conditions. The contact part b between the reaction layer material 5 and the PTFE sheet 3 is
When pressed at a temperature below the melting point of PTFE, 50 kg /
Even if pressed at 2 cm 2 , the pores of PTFE do not disappear, and the bonding strength with the reaction layer is to some extent. The overall strength is provided at the contact portion a between the silver mesh 2 and the porous PTFE 3.

【0011】[0011]

【実施例】以下実施例により本発明を具体的に説明す
る。ただし、本発明は、これらの実施例のみに限定され
るものではない。なお、全実施例を通じて、部は全て重
量部を意味する。
The present invention will be described in detail with reference to the following examples. However, the present invention is not limited to only these examples. Throughout the examples, all parts mean parts by weight.

【0012】実施例1 大きさ12cm×12cm、厚さ100ミクロン、線径
100ミクロン、ピッチ2mmの銀エキスパンドメタル
に、フィブリル化PTFE多孔体シート(細孔径1ミク
ロン、厚さ25ミクロン)を重ねて、350℃、20k
g/cm2 、10秒間ホットプレスを行い、急冷して、
銀網の線とPTFE多孔体を強固に接合させた。この開
口部にPTFE多孔体が張られた状態となった。これは
障子の桟に紙が貼られた状態と同様である。銀微粒子
(三井金属鉱業社製、Ag−3010、平均粒径0.1
1ミクロン)5部(重量、以下同様)に界面活性剤トラ
イトンを1部、水9部を加え超音波分散機で分散させ
た。これにPTFEディスパージョンD−1(ダイキン
工業社製)1部を加え、攪拌混合した後にエタノールを
20部加え、攪拌して自己組織化させた。この沈澱物を
0.8ミクロンの濾紙で濾過し、泥しょうを得た。前述
の接合体の銀網側から銀網が隠れる程度に均一に塗り込
み、80℃で3時間乾燥し、界面活性剤をエタノール抽
出装置で除去した。乾燥後、20kg/cm2 で260
℃、60秒間ホットプレスしてガス拡散電極を得た。こ
の電極の酸素還元性能を測定したところ、32%NaO
H、80℃の条件で30A/dm2で0.81V(v
s.RHE)の高い性能が得られた。剥離強度はPTF
E多孔体と銀網を260℃で接合した場合と比べその1
0〜15倍となった。
Example 1 A fibrillated PTFE porous sheet (pore diameter 1 micron, thickness 25 micron) was laminated on a silver expanded metal having a size of 12 cm × 12 cm, a thickness of 100 μm, a wire diameter of 100 μm, and a pitch of 2 mm. , 350 ° C, 20k
g / cm 2 , hot press for 10 seconds, quench,
The silver mesh wire and the PTFE porous body were firmly joined. A state was obtained in which a PTFE porous body was stretched over the opening. This is similar to the state in which paper is stuck to the crosspiece of the shoji. Silver fine particles (Ag-3010, manufactured by Mitsui Kinzoku Mining Co., Ltd., average particle size 0.1
One part of Triton surfactant and 9 parts of water were added to 5 parts (1 micron) (weight, the same applies hereinafter) and dispersed by an ultrasonic dispersing machine. To this, 1 part of PTFE dispersion D-1 (manufactured by Daikin Industries, Ltd.) was added, and the mixture was stirred and mixed. Then, 20 parts of ethanol was added, followed by stirring to form a self-assembly. The precipitate was filtered through 0.8 micron filter paper to obtain a slurry. The above-mentioned conjugate was uniformly applied so that the silver mesh was hidden from the silver mesh side, dried at 80 ° C. for 3 hours, and the surfactant was removed with an ethanol extraction device. After drying, 260 kg at 20 kg / cm 2
Hot pressing was performed at 60 ° C. for 60 seconds to obtain a gas diffusion electrode. When the oxygen reduction performance of this electrode was measured, 32% NaO
H, 0.81 V (v) at 30 A / dm 2 under the conditions of 80 ° C.
s. RHE). Peel strength is PTF
Part 1 compared to the case where the porous E body and the silver mesh are joined at 260 ° C
It became 0 to 15 times.

【0013】実施例2 銀メッキ発泡ニッケル体(50ppi、2mm厚、空孔
率96%、12×28センチ角)を0.5mmまでロー
ルで薄くした。この発泡体にフィブリル化PTFE多孔
体シート(細孔径1ミクロン、厚さ25ミクロン)を3
50℃、20kg/cm2 、10秒間ホットプレスを行
い急冷して、銀メッキ発泡ニッケルとPTFE多孔体を
強固に接合させた。銀微粒子(三井金属鉱業社製、Ag
−3010、平均粒径0.11ミクロン)5部に界面活
性剤トライトンを1部、水9部を加え超音波分散機で分
散させた。これにPTFEディスパージョンD−1(ダ
イキン工業社製)1部を加え、攪拌混合した後エタノ−
ルを20部加え、攪拌して自己組織化させた。この沈澱
物を0.8ミクロンの濾紙で濾過し、泥しょうを上記接
合体の発泡ニッケル体側から塗り込み、内部にむらなく
充填した。80℃で3時間乾燥し、発泡体側に1mmの
シリコーンラバーを載せ、230℃でプレス圧40kg
/cm2 、60秒間ホットプレスしてガス拡散電極を得
た。この電極の酸素還元性能を測定したところ、30A
/dm2 で0.78V(vsRHE)の高い性能が得ら
れた。
EXAMPLE 2 A silver-plated nickel foam body (50 ppi, 2 mm thick, porosity 96%, 12 × 28 cm square) was thinned to 0.5 mm with a roll. A fibrillated PTFE porous sheet (pore diameter 1 micron, thickness 25 micron) was added to this foam.
Hot pressing was performed at 50 ° C. and 20 kg / cm 2 for 10 seconds, followed by rapid cooling, so that the silver-plated foamed nickel and the PTFE porous body were firmly joined. Silver fine particles (Mitsui Metal Mining Co., Ltd., Ag
(5 parts of −3010, average particle size: 0.11 μm), 1 part of surfactant Triton and 9 parts of water were added and dispersed by an ultrasonic dispersing machine. One part of PTFE dispersion D-1 (manufactured by Daikin Industries, Ltd.) was added thereto, and the mixture was stirred and mixed.
Was added and stirred to form a self-organized mixture. The precipitate was filtered with a 0.8 micron filter paper, and the slurry was applied from the foamed nickel body side of the above-mentioned joined body, and was uniformly filled therein. Dry at 80 ° C. for 3 hours, place 1 mm silicone rubber on the foam side, press pressure at 230 ° C. 40 kg
/ Cm 2 for 60 seconds to obtain a gas diffusion electrode. When the oxygen reduction performance of this electrode was measured, 30 A
A high performance of 0.78 V (vsRHE) was obtained at / dm 2 .

【0014】実施例3 大きさ12cm×12cm、厚さ100ミクロン、線径
100ミクロン、ピッチ2mmの銀エキスパンドメタル
を縦3枚横3枚並べて、それぞれの5mmずつを重あわ
せた。その上から幅33cmのフィブリル化PTFE多
孔体シート(細孔径1ミクロン、厚さ25ミクロン)を
載せ、350℃、20kg/cm2 、10秒間ホットプ
レスを行い急冷して、銀網の線とPTFE多孔体を強固
に接合させた。それぞれの銀網とPTFE多孔体シート
は強固に接合され一枚物になった。
Example 3 Three silver expanded metals each having a size of 12 cm × 12 cm, a thickness of 100 μm, a wire diameter of 100 μm, and a pitch of 2 mm were arranged in three rows and three columns, and 5 mm of each was superposed. A fibrillated PTFE porous sheet (pore diameter 1 micron, thickness 25 micron) having a width of 33 cm is placed on top of this, hot-pressed at 350 ° C., 20 kg / cm 2 for 10 seconds, and quenched to obtain a silver mesh line and PTFE. The porous body was firmly joined. Each silver mesh and the porous PTFE sheet were firmly joined to form a single sheet.

【0015】銀微粒子(三井金属鉱業社製、Ag−30
10、平均粒径0.11ミクロン)5部に界面活性剤ト
ライトンを1部、水9部を加え超音波分散機で分散させ
た。これにPTFEディスパージョンD−1(ダイキン
工業社製)1部を加え、攪拌混合した後にエタノールを
20部加え、攪拌して自己組織化させた。この沈澱物を
0.8ミクロンの濾紙で濾過し、泥しょうを得た。この
泥しょうを前述の接合体の銀網側から銀網が隠れる程度
に均一に塗り込み、80℃で3時間乾燥し、界面活性剤
をエタノール抽出装置で除去した。乾燥後、20kg/
cm2 で260℃、60秒間ホットプレスしてガス拡散
電極を得た。この電極の酸素還元性能を測定したとこ
ろ、30A/dm2 で0.8V(vs.RHE)の高い
性能が得られた。
Silver fine particles (Ag-30, manufactured by Mitsui Kinzoku Mining Co., Ltd.)
(10, average particle size 0.11 micron) 1 part of surfactant Triton and 9 parts of water were added to 5 parts and dispersed by an ultrasonic dispersing machine. To this, 1 part of PTFE dispersion D-1 (manufactured by Daikin Industries, Ltd.) was added, and the mixture was stirred and mixed. Then, 20 parts of ethanol was added, followed by stirring to form a self-assembly. The precipitate was filtered through 0.8 micron filter paper to obtain a slurry. The slurry was uniformly applied to such an extent that the silver mesh was hidden from the silver mesh side of the above-mentioned joined body, dried at 80 ° C. for 3 hours, and the surfactant was removed with an ethanol extraction device. After drying, 20kg /
Hot pressing was performed at 260 ° C. for 60 seconds at cm 2 to obtain a gas diffusion electrode. When the oxygen reduction performance of this electrode was measured, a high performance of 0.8 V (vs. RHE) was obtained at 30 A / dm 2 .

【0016】実施例4 疎水性カーボンブラック(No.6、平均粒径500
Å、試作品、電気化学工業製)2部に界面活性剤の20
%トライトンを20部とPTFEディスパージョンD−
1(ダイキン工業製)2部を分散させる。この分散液に
イソプロピルアルコールを50部加え、自己組織化させ
る。この原料にソルベントナフサを加え、ロールするこ
とにより0.1mmのシートを作り、このシートをエチ
ルアルコールを用いた抽出器で界面活性剤を除去する。
100℃で乾燥後、380℃、50kg/cm2 の圧力
で60秒間ホットプレスする。このシートを150℃で
200%延伸することでカーボンブラックPTFE多孔
体シートを得た。
Example 4 Hydrophobic carbon black (No. 6, average particle size 500)
(Prototype, manufactured by Denki Kagaku Kogyo) 2 parts of surfactant 20
20% Triton and PTFE dispersion D-
1 part (manufactured by Daikin Industries) is dispersed. 50 parts of isopropyl alcohol is added to this dispersion to allow self-organization. Solvent naphtha is added to this raw material and rolled to form a 0.1 mm sheet, and the sheet is used to remove the surfactant by an extractor using ethyl alcohol.
After drying at 100 ° C., hot pressing is performed at 380 ° C. and a pressure of 50 kg / cm 2 for 60 seconds. This sheet was stretched by 200% at 150 ° C. to obtain a carbon black PTFE porous sheet.

【0017】大きさ12×24cm、厚さ100ミクロ
ン、線径100ミクロン、ピッチ2mmの銀エキスパン
ドメタルの上から前記カーボンブラックPTFE多孔体
シート(細孔径0.9ミクロン、厚さ56ミクロン)を
載せ、350℃、40kg/cm2 、10秒間ホットプ
レスを行い急冷して、銀網の線とカーボンブラックPT
FE多孔体シートを強固に接合させた。それぞれの銀網
とカーボンブラックPTFE多孔体シートは強固に接合
され一枚物になった。銀微粒子(田中貴金属製試作品、
比表面積8.7m2 /g)5部にトライトンを1部、水
9部を加え超音波分散機で分散させる。これにPTFE
ディスパージョンD−1(ダイキン工業製)1部を加
え、攪拌混合した後にエタノールを20部加え、攪拌す
ることで自己組織化させる。この沈殿物を孔径0.2ミ
クロンの濾紙で濾過し、泥漿を得る。前記の接合体の銀
網側から銀網が隠れる程度に均一に塗り込み、80℃で
3時間乾燥し、界面活性剤をエタノール抽出装置で除去
する。乾燥後、20kg/cm2 で260℃、60秒間
ホットプレスすることにより電極を得た。この電極の酸
素還元性能を測定したところ、32%NaOH、80℃
において、30A/dm2 で0.81V(vs.RH
E)の高い性能が得られた。
The porous carbon black PTFE sheet (pore diameter 0.9 micron, thickness 56 micron) is placed on a silver expanded metal having a size of 12 × 24 cm, a thickness of 100 μm, a wire diameter of 100 μm, and a pitch of 2 mm. , 350 ° C., 40 kg / cm 2 , hot-press for 10 seconds, quenched, silver wire and carbon black PT
The porous FE sheet was firmly joined. Each silver mesh and the carbon black PTFE porous sheet were firmly joined to form a single sheet. Silver fine particles (Tanaka precious metal prototype,
5 parts of specific surface area (8.7 m 2 / g), 1 part of Triton and 9 parts of water are added and dispersed by an ultrasonic dispersing machine. This is PTFE
One part of Dispersion D-1 (manufactured by Daikin Industries, Ltd.) is added, and the mixture is stirred and mixed. Then, 20 parts of ethanol is added, and the mixture is stirred to be self-organized. The precipitate is filtered through a filter paper having a pore size of 0.2 micron to obtain a slurry. The mixture is uniformly applied to the extent that the silver mesh is hidden from the silver mesh side, dried at 80 ° C. for 3 hours, and the surfactant is removed with an ethanol extraction device. After drying, an electrode was obtained by hot pressing at 260 ° C. for 60 seconds at 20 kg / cm 2 . When the oxygen reduction performance of this electrode was measured, 32% NaOH, 80 ° C.
At 30 A / dm 2 , 0.81 V (vs. RH
High performance E) was obtained.

【0018】[0018]

【発明の効果】本発明によれば、金属多孔体とPTFE
多孔体の接合は、PTFEの融点以上で10kg/cm
2 以上の高温、高圧でホットプレスするので、金属多孔
体とPTFE多孔体の接着強度は融点以下の場合と比べ
著しく増加した。小さな銀網、小さなPTFE多孔体シ
ートを重ねあわせることで大きな一枚物が作製できる。
また、反応層のプレス条件は、触媒金属微粒子のシンタ
ーがそれほど進行しないが、金属多孔体と接合し、性能
が極大となる最適条件でホットプレスできる。その結
果、ガス拡散電極からガス供給層が剥離せず長寿命で、
高性能なガス拡散電極が得られた。ガス供給層が金属多
孔体に強固に接合しているので、ガス拡散電極の機械的
強度が向上し、取扱いが容易になった。
According to the present invention, porous metal and PTFE
Bonding of porous body is 10 kg / cm above the melting point of PTFE
Since hot pressing was performed at a high temperature and a high pressure of 2 or more, the adhesive strength between the metal porous body and the PTFE porous body was significantly increased as compared with the case where the melting point was equal to or lower than the melting point. A large sheet can be produced by stacking a small silver mesh and a small porous PTFE sheet.
As for the pressing conditions of the reaction layer, the sintering of the catalytic metal fine particles does not proceed so much, but hot pressing can be performed under the optimum conditions for bonding with the porous metal and maximizing the performance. As a result, the gas supply layer does not peel off from the gas diffusion electrode and has a long life,
A high performance gas diffusion electrode was obtained. Since the gas supply layer is firmly joined to the porous metal body, the mechanical strength of the gas diffusion electrode is improved, and handling is easy.

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

【図1】本発明の金属多孔体とフィブリル化PTFE多
孔体シートの接合体の一実施例を示す断面説明図であ
る。
FIG. 1 is an explanatory cross-sectional view showing one embodiment of a bonded body of a porous metal body and a fibrillated PTFE porous sheet according to the present invention.

【図2】本発明のガス拡散電極の一実施例を示す断面説
明図である。
FIG. 2 is an explanatory sectional view showing one embodiment of the gas diffusion electrode of the present invention.

【符号の説明】[Explanation of symbols]

1 接合体 2 金属多孔体(銀網) 3 フィブリル化PTFE多孔体シート 4 ガス拡散電極 5 反応層材料 a 接触部 b 接触部 DESCRIPTION OF SYMBOLS 1 Joined body 2 Metal porous body (silver net) 3 Fibrillated PTFE porous sheet 4 Gas diffusion electrode 5 Reaction layer material a Contact part b Contact part

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成11年8月2日(1999.8.2)[Submission date] August 2, 1999 (1999.8.2)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】発明の名称[Correction target item name] Name of invention

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【発明の名称】 ガス供給層と金属多孔体との接合体
いたガス拡散電極
[Title of the Invention] A joined body of a gas supply layer and a porous metal body
Gas diffusion electrodes had use

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】特許請求の範囲[Correction target item name] Claims

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【特許請求の範囲】[Claims]

【請求項前記撥水性多孔体シートの一部が無い欠
落部を持つ状態で反応層を構成したことを特徴とする請
求項記載のガス拡散電極。
Wherein said water-repellent porous body according to claim 1 gas diffusion electrode, wherein the configuring the reaction layer with a partially with no missing portion of the sheet.

【請求項】 前記欠落部に銀の薄板、銀粉を付着さ
せ、ホットプレスすることによって液浸透性を少なく
し、ガス室側への導電性を改善したことを特徴とする請
求項記載のガス拡散電極。
3. A silver sheet to the missing part, by adhering silver powder, to reduce the liquid permeability by hot pressing, according to claim 2, characterized in that to improve the conductivity of the gas chamber side Gas diffusion electrode.

【手続補正3】[Procedure amendment 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0001[Correction target item name] 0001

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0001】[0001]

【発明の属する技術分野】本発明は、ガス拡散電極特に
食塩電解等に使用される金属多孔体−撥水性多孔体シー
ト接合体から得られたガス拡散電極に関し、特に寿命が
長いガス拡散電極に関する。
BACKGROUND OF THE INVENTION The present invention is Rukin genus porous body is used in particular gas diffusion electrode brine electrolysis, etc. - relates repellent porous body sheet assembly or we obtained gas diffusion electrode, in particular a long life gas diffusion Electrodes.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0002[Correction target item name] 0002

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0002】[0002]

【従来の技術】従来、ガス拡散電極においては、反応層
が銀微粒子を担持したカーボンブラックとポリ四フッ化
エチレン(以下「PTFE」という)のような樹脂結合
材から成り、ガス供給層がPTFEのような樹脂結合材
多孔体から成るガス拡散電極があった。しかしながら、
このようなガス拡散電極を酸素極に用いた場合には、触
媒が担持されたカーボンブラックは徐々に酸化され、担
体のカーボンブラックの消滅による触媒微粒子の脱落、
導電性の低下、親水性の増大による三相帯界面の減少等
により、電極性能の低下を来たし、2年以上の電極寿命
が達成できないという問題点があった。食塩電解槽に使
用する場合は5年以上の耐久性が必要であるため、この
ような電極寿命が短い電極ではこの種の電解槽には使用
することができない。そこで、カーボンの腐食の心配が
ない銀微粒子とPTFEのみから成る反応層を持つガス
拡散電極が提案され、長寿命が期待されているものとし
ては、反応層が銀微粒子とPTFE、ガス供給層がPT
FE多孔体から成る非カーボンブラック系ガス拡散電極
があった。
2. Description of the Related Art Conventionally, in a gas diffusion electrode, a reaction layer has a carbon black carrying silver fine particles and a polytetrafluoride.
There has been a gas diffusion electrode made of a resin binder such as ethylene (hereinafter referred to as "PTFE") and a gas supply layer made of a porous resin binder such as PTFE. However,
When such a gas diffusion electrode is used as an oxygen electrode, the carbon black carrying the catalyst is gradually oxidized, and the fine particles of the catalyst fall off due to disappearance of the carbon black on the carrier,
Electrode performance is reduced due to a decrease in conductivity and a decrease in a three-phase band interface due to an increase in hydrophilicity, and there has been a problem that an electrode life of two years or more cannot be achieved. When used in a salt electrolyzer, durability of 5 years or more is required. Therefore, an electrode having such a short electrode life cannot be used in this type of electrolyzer. In view of this, a gas diffusion electrode having a reaction layer consisting of only silver fine particles and PTFE, which does not have to worry about carbon corrosion, has been proposed. As a device expected to have a long life, the reaction layer is composed of silver fine particles, PTFE, and a gas supply layer. PT
There was a non-carbon black gas diffusion electrode made of a porous FE.

【手続補正5】[Procedure amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0004[Correction target item name] 0004

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0004】本発明は、このような従来の問題点に鑑み
てなされたものであり、少なくとも金属多孔体とフィブ
リル化PTFE多孔体シートとを強固に接合したガス供
給層と金属多孔体との接合体を用いた長寿命で高性能の
ガス拡散電極を提供することを目的とするものである。
The present invention has been made in view of such conventional problems, and has been made in consideration of the above-mentioned problems, and is intended to provide a bonding between a gas supply layer in which at least a porous metal body and a fibrillated PTFE porous sheet are firmly bonded, and a porous metal body. It is an object of the present invention to provide a long-life, high-performance gas diffusion electrode using a body .

【手続補正6】[Procedure amendment 6]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0006[Correction target item name] 0006

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0006】すなわち、本発明は、次の構成により前記
の課題を解決することができた。 (1)金属多孔体とカーボンブラックを0〜55%含む
フィブリル化ポリ四フッ化エチレン撥水性多孔体シート
とを、温度がポリ四フッ化エチレンの融点以上、圧力が
接触実圧力20kg/cm2 以上でホットプレスするこ
とによって前記金属多孔体と前記撥水性多孔体シートを
強固に接合した接合体の金属多孔体側から反応層材料を
充填し、反応層材料のポリ四フッ化エチレンの融点以下
の条件でホットプレスすることによって作製したことを
特徴とするガス拡散電極。前記撥水性多孔体シートの一部が無い欠落部を持
つ状態で反応層を構成したことを特徴とする前記(
記載のガス拡散電極。 ()前記欠落部に銀の薄板、銀粉を付着させ、ホット
プレスすることによって液浸透性を少なくし、ガス室側
への導電性を改善したことを特徴とする前記()記載
のガス拡散電極。
That is, the present invention has solved the above-mentioned problems by the following constitution. (1) A porous metal body and a fibrillated polytetrafluoroethylene water-repellent porous sheet containing 0 to 55% of carbon black are heated at a temperature equal to or higher than the melting point of polytetrafluoroethylene and at a contact pressure of 20 kg / cm 2. The reaction layer material is applied from the metal porous body side of the joined body in which the porous metal body and the water repellent porous sheet are firmly joined by hot pressing as described above.
Filled, below the melting point of polytetrafluoroethylene of the reaction layer material
That it was made by hot pressing under the conditions
Characterized gas diffusion electrode. (2) above, wherein in that constitutes the reaction layer in a state with a missing portion part is not the repellent porous sheet (1)
The gas diffusion electrode as described in the above. ( 3 ) The gas according to ( 2 ), wherein a thin silver plate or silver powder is adhered to the missing portion and hot pressing is performed to reduce liquid permeability and improve conductivity to the gas chamber side. Diffusion electrode.

───────────────────────────────────────────────────── フロントページの続き (71)出願人 000000941 鐘淵化学工業株式会社 大阪府大阪市北区中之島3丁目2番4号 (72)発明者 古屋 長一 山梨県甲府市中村町2−14 Fターム(参考) 4K011 AA10 AA11 AA68 BA03 BA04 BA06 CA04 DA02 5H018 AA01 AS01 BB01 BB03 BB05 BB06 BB08 BB09 BB11 BB12 CC06 DD01 DD03 DD08 EE02 EE05 EE16 EE19  ──────────────────────────────────────────────────続 き Continued on the front page (71) Applicant 000000941 Kanebuchi Chemical Industry Co., Ltd. 3-4-2 Nakanoshima, Kita-ku, Osaka-shi, Osaka (72) Inventor Choichi Furiya 2-14F, Nakamuracho, Kofu-shi, Yamanashi Prefecture Terms (reference) 4K011 AA10 AA11 AA68 BA03 BA04 BA06 CA04 DA02 5H018 AA01 AS01 BB01 BB03 BB05 BB06 BB08 BB09 BB11 BB12 CC06 DD01 DD03 DD08 EE02 EE05 EE16 EE19

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 金属多孔体とカーボンブラックを0〜5
5%含むフィブリル化PTFE撥水性多孔体シートと
を、温度がPTFEの融点以上、圧力が接触実圧力20
kg/cm2 以上でホットプレスすることによって前記
金属多孔体と前記撥水性多孔体シートを強固に接合した
ことを特徴とするガス拡散電極用金属多孔体−撥水性多
孔体シート接合体。
1. The method of claim 1, wherein the porous metal and carbon black are mixed in an amount of 0 to 5
A fibrillated PTFE water-repellent porous sheet containing 5% and a temperature equal to or higher than the melting point of PTFE;
A porous metal-water-repellent porous sheet assembly for a gas diffusion electrode, wherein the porous metal body and the water-repellent porous sheet are strongly bonded by hot pressing at a pressure of at least kg / cm 2 .
【請求項2】 請求項1の接合体の金属多孔体側から反
応層材料を充填し、反応層材料の最適条件でホットプレ
スすることによって作製したことを特徴とするガス拡散
電極。
2. A gas diffusion electrode prepared by filling a reaction layer material from the metal porous body side of the joined body of claim 1 and hot-pressing the reaction layer material under optimum conditions.
【請求項3】 請求項1の接合体の撥水性多孔体シート
の一部が無い欠落部を持つ状態で反応層を構成したこと
を特徴とする請求項2記載のガス拡散電極。
3. The gas diffusion electrode according to claim 2, wherein the reaction layer is formed in a state in which a part of the water-repellent porous sheet of the joined body of the bonded body has a missing portion.
【請求項4】 前記欠落部に銀の薄板、銀粉を付着さ
せ、ホットプレスすることによって液浸透性を少なく
し、ガス室側への導電性を改善したことを特徴とする請
求項3記載のガス拡散電極。
4. The method according to claim 3, wherein a thin silver plate or silver powder is adhered to said missing portion and hot pressing is performed to reduce liquid permeability and improve conductivity to the gas chamber side. Gas diffusion electrode.
JP10254116A 1998-09-08 1998-09-08 Gas diffusion electrode using bonded body of gas supply layer and porous metal Expired - Lifetime JP2987583B1 (en)

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JP2000087279A true JP2000087279A (en) 2000-03-28

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007119817A (en) * 2005-10-26 2007-05-17 Permelec Electrode Ltd Oxygen reducing gas diffusion cathode for salt electrolysis and salt electrolysis method
KR100728127B1 (en) 2005-11-30 2007-06-13 삼성에스디아이 주식회사 Membrane-electrode assembly for fuel cell
US20220023946A1 (en) * 2020-07-27 2022-01-27 c/o OHMIUM INTERNATIONAL, INC., Porous electrolyzer gas diffusion layer and method of making thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007119817A (en) * 2005-10-26 2007-05-17 Permelec Electrode Ltd Oxygen reducing gas diffusion cathode for salt electrolysis and salt electrolysis method
KR100728127B1 (en) 2005-11-30 2007-06-13 삼성에스디아이 주식회사 Membrane-electrode assembly for fuel cell
US20220023946A1 (en) * 2020-07-27 2022-01-27 c/o OHMIUM INTERNATIONAL, INC., Porous electrolyzer gas diffusion layer and method of making thereof
US12440894B2 (en) * 2020-07-27 2025-10-14 Ohmium International, Inc. Porous electrolyzer gas diffusion layer and method of making thereof

Also Published As

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