KR20130074216A - Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same - Google Patents

Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same Download PDF

Info

Publication number
KR20130074216A
KR20130074216A KR1020110142161A KR20110142161A KR20130074216A KR 20130074216 A KR20130074216 A KR 20130074216A KR 1020110142161 A KR1020110142161 A KR 1020110142161A KR 20110142161 A KR20110142161 A KR 20110142161A KR 20130074216 A KR20130074216 A KR 20130074216A
Authority
KR
South Korea
Prior art keywords
stainless steel
fuel cell
cell separator
hydroxide
contact resistance
Prior art date
Application number
KR1020110142161A
Other languages
Korean (ko)
Other versions
KR101356954B1 (en
Inventor
김종희
김광민
조기훈
이윤용
김규영
이상우
Original Assignee
주식회사 포스코
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 주식회사 포스코 filed Critical 주식회사 포스코
Priority to KR1020110142161A priority Critical patent/KR101356954B1/en
Publication of KR20130074216A publication Critical patent/KR20130074216A/en
Application granted granted Critical
Publication of KR101356954B1 publication Critical patent/KR101356954B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • C22C38/50Ferrous alloys, e.g. steel alloys containing chromium with nickel with titanium or zirconium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/001Ferrous alloys, e.g. steel alloys containing N
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/004Very low carbon steels, i.e. having a carbon content of less than 0,01%
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/02Ferrous alloys, e.g. steel alloys containing silicon
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/04Ferrous alloys, e.g. steel alloys containing manganese
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • C22C38/44Ferrous alloys, e.g. steel alloys containing chromium with nickel with molybdenum or tungsten
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • C22C38/46Ferrous alloys, e.g. steel alloys containing chromium with nickel with vanadium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • C22C38/48Ferrous alloys, e.g. steel alloys containing chromium with nickel with niobium or tantalum
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0206Metals or alloys
    • H01M8/0208Alloys
    • H01M8/021Alloys based on iron
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)
  • Chemical Treatment Of Metals (AREA)

Abstract

PURPOSE: A stainless steel for the separator of a polymer electrolyte membrane fuel cell and a manufacturing method thereof are provided to secure the low interfacial contact resistance, thereby obtaining the steel suitable for the separator. CONSTITUTION: A stainless steel for the separator of a polymer electrolyte membrane fuel cell comprises 0 to 0.02 wt% of C, 0 to 0.02 wt% of N, 0 to 0.4 wt% of Si, 0 to 0.2 wt% of Mn, 0 to 0.04 wt% of P, 0 to 0.02 wt% of S, 25 to 34 wt% of Cr, 0 to below 2.5 wt% of Mo, 0 to 1 wt% of Cu, 0 to below 0.2 wt% of Ni, 0 to 0.5 wt% of Ti, 0 to 0.5 wt% of Nb, Fe, and other inevitable impurities. The hydroxide/oxide ratio of a passive film on the surface of the steel is over 1, and the interfacial contact resistance of the film is below 20 mΩcm^2 (150 N/cm^2). The steel further includes one or two elements selected from a group of composites added with one or a mixture of over 0.2 to 1 of V wt% and 0 to 4 wt% of W. A Cr-hydroxide/oxide ratio inside the film is over 2. [Reference numerals] (AA) Intensity; (BB) Hydroxide; (CC) Oxide; (DD) Invention example 4; (EE) Invention example 3; (FF) Invention example 2; (GG) Invention example 1; (HH) Comparative example 2; (II) Comparative example 1; (JJ) Comparative example 3; (KK) Binding energy (eV)

Description

고분자 연료전지 분리판용 스테인리스강 및 그 제조방법{Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same}Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same}

본 발명은 고분자 연료전지(polymer electrolyte membrane fuel cell) 분리판용 스테인리스강 및 그 제조방법에 관한 것으로, 보다 상세하게는 낮은 계면접촉저항을 갖는 고분자 연료전지 분리판용 스테인리스강 및 그 제조방법에 관한 것이다.The present invention relates to a stainless steel for a polymer electrolyte membrane fuel cell separator and a method for manufacturing the same, and more particularly, to a stainless steel for a polymer fuel cell separator having a low interfacial contact resistance and a method for manufacturing the same.

고분자 연료전지는 수소이온교환 특성을 갖는 고분자막을 전해질로 사용하는 연료전지로서, 다른 형태의 연료전지에 비해 80℃ 정도로 작동온도가 낮고 효율이 높다. 또한 전류밀도 및 출력밀도가 크며 구조가 간단하고 빠른 시동과 응답특성을 가지고 있어 자동차용, 가정용 등의 전력원으로서 적용될 수 있다.A polymer fuel cell is a fuel cell that uses a polymer membrane having hydrogen ion exchange characteristics as an electrolyte, and has a low operating temperature and high efficiency at about 80 ° C. compared with other types of fuel cells. Also, it has high current density and power density, simple structure, fast starting and response characteristics, and can be used as a power source for automobiles and households.

이와 같은 고체 고분자 연료전지의 주요 구성요소는 고분자 전해질 막과 전극 그리고 스택을 구성하기 위한 분리판으로 이루어져 있다. 고체 고분자 연료전지에서 분리판은 반응가스인 수소가스와 산소가스가 서로 섞이지 않도록 차단함과 아울러, 막전극집합체(Membrane Electrode Assembly: MEA)를 전기적으로 연결하고, 막전극집합체를 지지하여 연료전지의 형태가 유지되도록 하는 기능을 한다. 따라서, 두 가스가 혼합되지 않을 만큼의 치밀한 구조를 지녀야 하며, 전도체의 역할을 위해 전기전도성이 우수하여야 하고, 지지체의 역할을 위해 충분한 기계적 강도를 가져야 한다.The main components of such a solid polymer fuel cell consist of a polymer electrolyte membrane, an electrode, and a separator to form a stack. In the solid polymer fuel cell, the separator plate is formed so as to block hydrogen gas and oxygen gas as reaction gases from each other, to electrically connect membrane electrode assembly (MEA), to support the membrane electrode assembly, And maintains the shape. Therefore, it should have a dense structure such that the two gases are not mixed, and should have good electrical conductivity for the role of the conductor and sufficient mechanical strength for the role of the support.

분리판은 일반적으로, 흑연, 카본, Ti 합금, 스테인리스강 및 도전성 플라스틱 중 하나로 형성되며, 바람직하게 스테인리스강으로 형성될 수 있다. 스테인리스강은 열전도성, 낮은 기체투과성 및 대면적화가 가능하고, 양호한 제품 성형성, 박물화가 가능하여 연료전지 스택의 부피저감, 무게감소를 이룰 수 있는 장점을 갖고 있다.The separator is generally formed of one of graphite, carbon, Ti alloy, stainless steel and conductive plastic, and may preferably be formed of stainless steel. Stainless steel has the advantage of being able to achieve thermal conductivity, low gas permeability, and large area, and can form a good product and be made into a thin piece, thereby reducing the volume and weight of the fuel cell stack.

그러나, 스테인리스강 분리판을 사용할 경우, 산성인 전해질 용액에서 부식이 유발되어 전극 및 전해질을 오염시키고, 표면에 부식생성물로 인해 계면 접촉저항이 증가하는 문제점이 있다.However, when a stainless steel separator is used, there is a problem that corrosion occurs in an acidic electrolytic solution to contaminate electrodes and electrolytes, and the interface contact resistance increases due to corrosion products on the surface.

이러한 문제를 해결하기 위해서 금속 바이폴라 소재의 표면에 전도성 코팅을 적용하는 방법 등이 제안되고 있는데, 이 방법의 경우 코팅에 의해 추가로 생성되는 계면들이 화학적 안정성을 저하시켜 부식에 취약할 뿐 아니라 코팅으로 인한 추가적 비용이 발생하는 문제점이 있다. 또한 미국등록특허 제6379476B1호에서는 평균거칠기(Ra)가 0.06 ~ 5 ㎛를 갖도록 하여 계면접촉저항을 감소하는 방법을 제안하고 있다. 또한, 일본공개특허 제2007-026694호에서는 0.01·~ 1.0 ㎛의 마이크로 핏(Micro pit)을 표면 전체에 형성시킴으로써, 표면 특성을 원하는 수준으로 획득하는 방법을 제시하며, 일본공개특허 제2008-091225호에서는 마이크로 핏을 형성시킴은 물론 Cr/Fe 원자비를 4 이상으로 확보하여 접촉저항을 감소하는 방법을 제안하고 있다.In order to solve this problem, a method of applying a conductive coating on the surface of a metal bipolar material has been proposed. In this method, the interfaces generated by the coating are not only susceptible to corrosion due to deterioration of chemical stability. There is a problem that additional costs are caused. In addition, US Patent No. 6379476B1 proposes a method of reducing the interfacial contact resistance by having an average roughness (Ra) of 0.06 ~ 5 ㎛. In addition, Japanese Patent Application Laid-Open No. 2007-026694 discloses a method of obtaining surface characteristics to a desired level by forming a micro pit of 0.01 · ~ 1.0 μm over the entire surface, and Japanese Patent Application Laid-Open No. 2008-091225 The arc proposes a method of reducing contact resistance by forming a micro fit as well as securing a Cr / Fe atomic ratio of 4 or more.

그러나, 상기와 같은 연료전지 분리판의 표면 조도를 조절하여 계면접촉저항을 저감하는 방법은 스테인리스강 표면에 생성되는 비전도성 부동태 피막으로 인해 낮은 계면접촉저항을 안정적으로 확보하기 어려운 문제점이 있다.However, the method of reducing the interfacial contact resistance by adjusting the surface roughness of the fuel cell separator as described above has a problem that it is difficult to stably ensure a low interfacial contact resistance due to the non-conductive passivation film formed on the stainless steel surface.

본 발명은 전술한 종래기술의 문제점을 해결하고 새로운 분리판 소재의 요구에 대응할 수 있도록, 표면 개질 공정을 통해 낮은 계면접촉저항을 확보할 수 있는 연료전지 분리판용 스테인리스강 및 그 제조 방법을 제공하는 것을 목적으로 한다.The present invention provides a stainless steel for fuel cell separator plate and a method for manufacturing the same that can secure a low interfacial contact resistance through a surface modification process to solve the above problems of the prior art and to meet the demand of a new separator material. For the purpose of

본 발명은 중량%로, C: 0~0.02, N: 0~0.02, Si: 0~0.4, Mn: 0~0.2, P: 0~0.04, S: 0~0.02, Cr: 25~34, Mo:0~2.5미만, Cu:0~1, Ni:0~0.2미만, Ti: 0~0.5, Nb: 0~0.5와 Fe 및 기타 불가피한 불순물을 함유하고, 상기 스테인리스강 표면 부동태 피막이 1 이상의 수산화물/산화물 비를 가지며 계면 접촉저항이 20mΩ㎠ (150N/㎠)이하인 고분자 연료전지 분리판용 스테인리스강을 제공한다.In the present invention, by weight%, C: 0 to 0.02, N: 0 to 0.02, Si: 0 to 0.4, Mn: 0 to 0.2, P: 0 to 0.04, S: 0 to 0.02, Cr: 25 to 34, Mo : Less than 0 to 2.5, Cu: 0 to 1, Ni: less than 0 to 0.2, Ti: 0 to 0.5, Nb: 0 to 0.5 and Fe and other unavoidable impurities, and the stainless steel surface passivation coating contains at least one hydroxide / 20mΩ㎠ with interfacial contact resistance Provided are stainless steels for polymer fuel cell separators of less than (150 N / cm 2).

본 발명에서 상기 스테인리스강은 중량 %로, V: 0.2초과~1, W: 0~4를 단일 혹은 혼합 첨가한 조성으로 이루어지는 군에서 선택되는 1종 또는 2종의 원소가 더 포함된다.In the present invention, the stainless steel further includes one or two kinds of elements selected from the group consisting of a composition in which V: over 0.2 and 1 and W: 0 to 4 are added by weight or by weight.

또한, 본 발명에서 상기 스테인리스강의 부동태 피막 내 Cr 수산화물/산화물 비가 2이상이다.Further, in the present invention, the Cr hydroxide / oxide ratio in the passivation film of the stainless steel is two or more.

또한, 본 발명의 또 다른 실시예에서 중량%로, C: 0~0.02, N: 0~0.02, Si: 0~0.4, Mn: 0~0.2, P: 0~0.04, S: 0~0.02, Cr: 25~34, Mo:0~2.5미만, Cu:0~1, Ni:0~0.2미만, Ti: 0~0.5, Nb: 0~0.5와 Fe 및 기타 불가피한 불순물을 함유하고, 상기 스테인리스강을 1 ~ 5 몰 농도 수산화나트륨의 조성으로 유지된 용액에서 침지하여 상기 스테인리스강 표면 부동태 피막이 1 이상의 수산화물/산화물 비를 가져 계면 접촉저항이 20mΩ㎠ (150N/㎠)이하가 되도록 제어하는 고분자 연료전지 분리판용 스테인리스강 제조방법을 제공한다.Further, in another embodiment of the present invention, in weight percent, C: 0 to 0.02, N: 0 to 0.02, Si: 0 to 0.4, Mn: 0 to 0.2, P: 0 to 0.04, S: 0 to 0.02, Cr: 25-34, Mo: 0-2.5, Cu: 0-1, Ni: 0-0.2, Ti: 0-0.5, Nb: 0-0.5 and Fe and other unavoidable impurities Is immersed in a solution maintained at a composition of 1 to 5 molar concentrations of sodium hydroxide so that the stainless steel surface passivation coating has a hydroxide / oxide ratio of at least 1 and the interface contact resistance is 20 m 저항 ㎠. Provided is a method for manufacturing a stainless steel for a polymer fuel cell separator, which is controlled to be (150 N / cm 2) or less.

본 발명에서 상기 스테인리스강은 상기 수산화나트륨 용액에서, 1~5분 침지한다.In the present invention, the stainless steel is immersed for 1 to 5 minutes in the sodium hydroxide solution.

상술한 바와 같이 본 발명에 의하면 본 발명의 합금성분 범위를 가지고 스테인리스강 표면의 부동태 피막을 개질함으로써 낮은 계면접촉저항을 확보할 수 있으며 고분자 연료전지 분리판용으로 적합한 스테인리스강을 얻을 수 있는 효과가 있다.As described above, according to the present invention, it is possible to secure low interfacial contact resistance by modifying the passivation coating on the surface of the stainless steel with the alloy composition range of the present invention, and to obtain a suitable stainless steel for polymer fuel cell separator. .

도 1은 본 발명과 비교예에 의하여 표면 개질 후 부동태 피막을 XPS(X-ray photoelectron spectroscopy) 분석을 실시한 예를 나타낸 그래프.1 is a graph showing an example of XPS (X-ray photoelectron spectroscopy) analysis of a passivation film after surface modification according to the present invention and a comparative example.

이하에서는 본 발명의 발명예를 도시한 도면들을 참조하여 더욱 상세히 설명한다. 여기서 사용되는 전문용어는 단지 특정 실시예를 언급하기 위한 것이며, 본 발명을 한정하는 것을 의도하지 않는다. 여기서 사용되는 단수 형태들은 문구들이 이와 명백히 반대의 의미를 나타내지 않는 한 복수 형태들도 포함한다. 명세서에서 사용되는 "포함하는"의 의미는 특정 특성, 영역, 정수, 단계, 동작, 요소 및/또는 성분을 구체화하며, 다른 특정 특성, 영역, 정수, 단계, 동작, 요소, 성분 및/또는 군의 존재나 부가를 제외시키는 것은 아니다.Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. The terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the invention. As used herein, the singular forms “a,” “an,” and “the” include plural forms as well, unless the phrases clearly indicate the opposite. As used herein, the term "comprising" embodies a particular characteristic, region, integer, step, operation, element, and / or component, and other specific characteristics, region, integer, step, operation, element, component, and / or group. It does not exclude the presence or addition of.

다르게 정의하지는 않았지만, 여기에 사용되는 기술용어 및 과학용어를 포함하는 모든 용어들은 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 일반적으로 이해하는 의미와 동일한 의미를 가진다. 보통 사용되는 사전에 정의된 용어들은 관련기술문헌과 현재 개시된 내용에 부합하는 의미를 가지는 것으로 추가 해석되고, 정의되지 않는 한 이상적이거나 매우 공식적인 의미로 해석되지 않는다.Unless defined otherwise, all terms including technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art. Commonly used predefined terms are further interpreted as having a meaning consistent with the relevant technical literature and the present disclosure, and are not to be construed as ideal or very formal meanings unless defined otherwise.

보통 연료전지 분리판용 스테인리스강에서는 스테인리스강의 표면에 생성되는 비전도성의 부동태 피막으로 인해 계면접촉저항이 증가하는 문제점이 발생할 수 있다. 따라서 낮은 계면접촉저항을 확보하기 위해서는 연료전지 분리판용 스테인리스강이 낮은 접촉저항을 가질 수 있도록 최적의 합금설계와 상기 합금설계에 적합한 부동태 피막 개질 처리를 실시하는 것이 바람직하다.In general, stainless steel for fuel cell separators may have a problem of increasing interfacial contact resistance due to the non-conductive passivation film formed on the surface of the stainless steel. Therefore, in order to secure a low interfacial contact resistance, it is preferable to perform an optimum alloy design and a passivation film reforming treatment suitable for the alloy design so that the stainless steel for fuel cell separator has a low contact resistance.

본 실시예의 스테인리스강은 중량%로, C: 0~0.02, N: 0~0.02, Si: 0~0.4, Mn: 0~0.2, P: 0~0.04, S: 0~0.02, Cr: 25~34, Mo:0~2.5미만, Cu:0~1, Ni:0~0.2미만, Ti: 0~0.5, Nb: 0~0.5의 조성에 V: 0.2초과~1, W: 0~4를 단일 혹은 혼합 첨가하여 합금설계된 스테인리스강을 모재로 한다. 그리고 상기 조성의 스테인리스강을 진공유도로에 의해 주편으로 제조하고, 열간압연을 거처, 소둔, 산세, 냉간압연 및 소둔을 되풀이하여 2㎜의 두께를 갖는 냉연 판재를 제조한다. 본 합금설계에 의하여 제조된 스테인리스강의 조성은 하기 표 1과 같다.Stainless steel of the present Example is weight%, C: 0 to 0.02, N: 0 to 0.02, Si: 0 to 0.4, Mn: 0 to 0.2, P: 0 to 0.04, S: 0 to 0.02, Cr: 25 to 34, Mo: less than 0 to 2.5, Cu: 0 to 1, Ni: less than 0 to 0.2, Ti: 0 to 0.5, Nb: 0 to 0.5 in a composition of V: 0.2 to 1, W: 0 to 4 Alternatively, the base material is made of alloyed stainless steel by mixing and adding. And the stainless steel of the said composition is manufactured by slab by a vacuum induction, and it hot-rolls, repeats annealing, pickling, cold rolling, and annealing, and manufactures the cold rolled sheet material which has a thickness of 2 mm. The composition of the stainless steel produced by the present alloy design is shown in Table 1 below.

Figure pat00001
Figure pat00001

이하에서는 각 성분함량을 한정하는 이유에 관하여 상술하기로 한다. 아울러, 이하에서 설명되는 %는 모두 중량%이다.Hereinafter, the reason for limiting each component content will be described in detail. In addition, all the percentages described below are% by weight.

C와 N은 스테인리스강 중에서 Cr탄질화물을 형성하며, 그 결과 Cr이 결핍된 층의 내식성이 저하되므로 상기 두 원소의 함량은 낮을수록 바람직하다. 본 발명에서는 C:0.02%이하, N:0.02%이하로 그 조성비를 제한한다.C and N form Cr carbonitride in stainless steel, and as a result, the corrosion resistance of the Cr-deficient layer is lowered, so the lower the content of the two elements is preferable. In the present invention, the composition ratio is limited to C: 0.02% or less and N: 0.02% or less.

Si는 탈산에 유효한 원소이나 인성 및 성형성을 억제하므로, 본 발명에서는 Si의 조성비를 0.4% 이내로 제한한다.Since Si suppresses the element, toughness, and moldability which are effective for deoxidation, in the present invention, the composition ratio of Si is limited to within 0.4%.

Mn은 탈산을 증가시키는 원소이나, 개재물인 MnS는 내식성을 감소시킨다. 본 발명에서는 Mn의 조성비를 0.2% 이내로 제한한다.Mn is an element that increases deoxidation, but the inclusion MnS reduces corrosion resistance. In the present invention, the composition ratio of Mn is limited to within 0.2%.

P는 내식성 뿐만 아니라 인성을 감소시키므로, 본 실시예에서는 P의 조성비를 0.04% 이내로 제한한다.Since P not only reduces corrosion resistance but also toughness, in this embodiment, the composition ratio of P is limited to within 0.04%.

S는 MnS를 형성하며, 이러한 MnS는 부식의 기점이 되어 내식성을 감소시킨다. 본 실시예에서는 이를 고려하여 S의 조성비를 0.02% 이내로 제한한다.S forms MnS, which becomes a starting point of corrosion and reduces corrosion resistance. In this embodiment, the composition ratio of S is limited to within 0.02% in consideration of this.

Cr은 연료전지가 작동되는 산성 분위기에서 내식성을 증가시키나, 인성을 감소시키므로, 본 실시예에서는 Cr의 적정 조성비를 25% 내지 34%로 제한한다.Cr increases the corrosion resistance in the acidic atmosphere in which the fuel cell is operated, but reduces the toughness, and therefore, in this embodiment, the appropriate composition ratio of Cr is limited to 25% to 34%.

Mo는 내식성에서는 유리하나 경제성 및 소재의 인성을 열화시킬 수 있으므로, 본 실시예에서는 Mo의 조성비를 0% 내지 2.5% 미만의 범위로 제한한다.Mo is advantageous in corrosion resistance, but may deteriorate the economics and toughness of the material. In this embodiment, the composition ratio of Mo is limited to the range of 0% to less than 2.5%.

Cu는 연료전지가 작동되는 산성 분위기에서 내식성을 증가시키나, 과량 첨가시 Cu의 용출로 인하여 연료전지의 성능이 저하될 수 있다. 본 실시예에서는 이를 고려하여 Cu의 조성비를 0% 내지 1%이내로 제한한다.Cu increases the corrosion resistance in an acidic atmosphere in which the fuel cell operates, but the performance of the fuel cell may be degraded due to the elution of Cu when excessively added. In this embodiment, the composition ratio of Cu is limited within 0% to 1% in consideration of this.

Ni은 과량 첨가시 Ni용출 및 성형성이 저하될 수 있다. 본 실시예에서는 이를 고려하여 Ni의 조성비를 0.2%미만으로 제한한다.When Ni is excessively added, Ni elution and moldability may decrease. In this embodiment, the composition ratio of Ni is limited to less than 0.2% in consideration of this.

Ti와 Nb는 강 중의 C, N을 탄질화물로 형성하는 데 유효한 원소이나 인성을 저하시킨다. 본 실시예에서는 이를 고려하여 각각의 조성비를 0.5%이하로 제한한다.Ti and Nb deteriorate the element and toughness effective for forming C and N in carbon as carbonitrides. In this embodiment, each composition ratio is limited to 0.5% or less in consideration of this.

이 외에도, 1 종 또는 2 종 이상의 V, W 가 첨가될 수 있으며, 이들의 조성비는 다음과 같다.In addition to this, one or two or more kinds of V and W may be added, and their composition ratios are as follows.

V은 연료전지가 작동되는 산성 분위기에서 내식성을 증가시키나, 과잉 첨가시 이온이 용출되어 전지의 성능이 저하될 수 있다. 본 실시예에서는 이를 고려하여 V의 조성비를 0.2초과~1%로 제한한다.V increases the corrosion resistance in the acidic atmosphere in which the fuel cell operates, but when excessively added, ions are eluted and the performance of the cell may be degraded. In this embodiment, the composition ratio of V is limited to more than 0.2 ~ 1% in consideration of this.

W은 연료전지가 작동되는 산성 분위기에서 내식성을 증가시키고 계면접촉저항을 낮추는 효과가 있으나, 과잉 첨가 시 인성을 저하시킨다. 본 실시예에서는 이를 고려하여 W의 조성비를 4% 이하로 제한한다.W has the effect of increasing the corrosion resistance and lowering the interfacial contact resistance in the acidic atmosphere in which the fuel cell operates, but deteriorates the toughness upon excessive addition. In this embodiment, the composition ratio of W is limited to 4% or less in consideration of this.

또한, 본 발명은 상기의 조성으로 이루어진 스테인리스강을 연주, 열연, 냉연 및 소둔과정을 거쳐 스테인리스강 박판을 제조한다. 그리고 이와 같은 스테인리스강에 대하여 계면접촉저항을 감소시키기 위한 별도의 표면개질처리를 실시한다.In addition, the present invention through the process of playing, hot rolling, cold rolling and annealing the stainless steel made of the above composition to produce a stainless steel sheet. In addition, a separate surface modification treatment is performed on the stainless steel to reduce interfacial contact resistance.

다음은 본 발명의 고분자 연료전지 분리판을 목적으로 하는 낮은 계면접촉저항을 가지는 스테인리스 강재의 제조방법에 대해 설명한다. The following describes a method for manufacturing a stainless steel material having a low interfacial contact resistance for the purpose of the polymer fuel cell separator of the present invention.

먼저 상기 조성의 스테인리스강을 1 ~ 5 몰 농도 수산화나트륨의 조성을 가지는 용액에서 적정한 시간을 유지하는 부동태 피막 개질 처리를 실시한다. 이에 따라 스테인리스강 표면 부동태 피막이 1 이상의 수산화물/산화물 비를 가지며, 특히 3 이상의 Cr 수산화물/산화물 비를 가짐으로써, 스테인리스강의 계면접촉저항이 20 mΩ㎠ 이하를 확보할 수 있다.First, a passivation film reforming treatment of maintaining a suitable time in a solution having a composition of 1 to 5 mol concentration sodium hydroxide of the stainless steel of the composition is carried out. Accordingly, the stainless steel surface passivation film has one or more hydroxide / oxide ratios, and in particular, three or more Cr hydroxide / oxide ratios, so that the interfacial contact resistance of the stainless steel can be 20 mΩcm 2 or less.

이하에서는 고분자 연료전지 분리판을 목적으로 하는 낮은 계면접촉저항을 갖는 스테인리스 강재에 관해 실시예를 통하여 보다 구체적으로 상술한다.Hereinafter, a stainless steel material having a low interfacial contact resistance for the purpose of a polymer fuel cell separator will be described in more detail with reference to Examples.

(실시예)(Example)

스테인리스강은 자연 상태에서 공기 중의 산소와 결합하여 표면에 얇은 보호성 부동태 피막을 생성하기 때문에 안정적으로 낮은 계면접촉저항을 확보하기가 어렵다. 따라서 스테인리스강 표면에 존재하는 부동태 피막을 개질 시킬 필요가 있다. 또한 대기 중에서 형성된 부동태 피막은 Fe 함량이 높기 때문에 연료전지 분리판용으로 사용하기 위해서는 Cr의 비율을 높여 Cr이 농축된 부동태 피막으로 개질 하여야만 한다. 그 이유는 Cr 산화물 및 수산화물은 Fe 산화물 및 수산화물에 비해 안정하며 내식성이 우수하기 때문에 높은 내식성이 요구되는 연료전지 분리판의 표면 생성물로 더 적합하다.Since stainless steel is combined with oxygen in the air in a natural state to form a thin protective passivation film on the surface, it is difficult to secure stable low interfacial contact resistance. Therefore, it is necessary to modify the passivation film existing on the stainless steel surface. In addition, since the passivation film formed in the air has a high Fe content, it must be reformed into a passivation film containing Cr by increasing the ratio of Cr to be used for a fuel cell separator. The reason is that Cr oxides and hydroxides are more stable than Fe oxides and hydroxides, and thus are more suitable as surface products of fuel cell separators requiring high corrosion resistance.

따라서 본 발명에서는 1 ~ 5 몰 농도 수산화나트륨의 조성을 가지는 용액에서 적정한 시간을 유지하여 표면 개질 처리를 하였다.Therefore, in the present invention, the surface modification treatment was performed by maintaining an appropriate time in a solution having a composition of 1 to 5 molar concentration sodium hydroxide.

본 발명에서는 수산화나트륨의 농도를 1 몰 농도 내지 5 몰 농도로 제한하였는데, 1 몰 농도 미만에서는 표면 개질의 효과가 작으며, 반대로 5 몰 농도를 초과하는등 농도가 너무 높을 경우 모재의 심각한 손상 및 안정한 부동태 피막의 발생이 저하될 수 있다.In the present invention, the concentration of sodium hydroxide is limited to 1 to 5 molar concentrations, but the effect of surface modification is less than 1 molar concentration, on the contrary, if the concentration is too high such as exceeding 5 molar concentrations, serious damage to the base material and The generation of a stable passivation film can be reduced.

표 2에서는 표면 개질 조건(침지용액의 농도 및 침지 시간)을 달리하면서 표 1의 실시예 1 강종에 대하여 평가한 결과이다.Table 2 shows the results of the evaluation of the steel sheet of Example 1 of Table 1 while varying the surface modification conditions (the concentration of the immersion solution and the immersion time).

상기 표 2에 나타난 본 발명의 발명예 1 ~ 발명예 4 및 비교예 1 ~ 비교예 3에 따른 계면접촉저항을 살펴본다. 또한 본 비교예와 발명예에 따라 표면 개질을 실시한 후 부동태 피막을 XPS(X-ray photoelectron spectroscopy) 분석을 실시하여 그 결과를 도 1에 나타내었다.The interface contact resistance according to Inventive Examples 1 to 4 and Comparative Examples 1 to 3 of the present invention shown in Table 2 will be described. In addition, after performing surface modification according to the comparative example and the invention example, the passivation film was analyzed by XPS (X-ray photoelectron spectroscopy) and the results are shown in FIG. 1.

표 2에서 보는 바와 같이, 1 몰 농도의 수산화나트륨 용액에서는 침지 시간이 증가하면서 계면접촉저항이 감소됨을 알 수 있다. 비교예 1과 비교예 2에서 보는 것과 같이, 1 몰 농도의 수산화나트륨 용액에서 1분 또는 3분의 침지는 접촉저항 감소 효과가 나타나지 않았으며, 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 비교예 3과 비슷한 값을 나타내었다. 이와 같은 결과는 수산화나트륨의 낮은 농도와 짧은 침지 시간으로는 본 발명에서 요구하는 부동태 피막의 표면 개질이 어렵다는 것을 의미한다.As shown in Table 2, it can be seen that the interface contact resistance decreases as the immersion time increases in the sodium hydroxide solution of 1 mol concentration. As seen in Comparative Example 1 and Comparative Example 2, immersion for 1 minute or 3 minutes in a 1 molar sodium hydroxide solution did not show a decrease in contact resistance, and the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film were not shown. The value similar to the comparative example 3 was shown. This result means that it is difficult to modify the surface of the passivation film required by the present invention with a low concentration of sodium hydroxide and a short immersion time.

Figure pat00002
Figure pat00002

이에 반해 발명예 1에서 보는 바와 같이, 1 몰 농도의 수산화나트륨 용액에서도 5분간의 침지는 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 비교예 3에 비해 증가하였으며 계면접촉저항도 20 mΩ㎠ 이하로 감소함을 알 수 있다. 따라서 낮은 수산화나트륨 농도에서도 침지 시간이 길어지면 부동태 피막이 개질됨을 알 수 있다.On the other hand, as shown in Inventive Example 1, the immersion for 5 minutes even in a 1 molar sodium hydroxide solution increased the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film compared to Comparative Example 3 and the interface contact resistance is also 20 mΩ ㎠ It can be seen that the decrease below. Therefore, it can be seen that even at low sodium hydroxide concentration, if the immersion time is long, the passivation film is modified.

또한, 발명예 2에서 보는 바와 같이, 침지 시간이 1분이라도 수산화나트륨의 농도가 5 몰 농도일 경우 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 크게 증가하였으며 낮은 계면접촉저항을 나타내었다.In addition, as shown in Inventive Example 2, even when the immersion time is 1 minute, when the concentration of sodium hydroxide is 5 mol concentration, the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film was greatly increased and showed low interfacial contact resistance.

발명예 1 ~ 4에서 보는 바와 같이, 적정한 농도의 수산화나트륨과 침지 시간으로 부동태 피막 내 높은 수산화물/산화물 비와 Cr 수산화물/산화물 비와 20 mΩ㎠ 이하의 계면접촉저항을 확보할 수 있음을 알 수 있다.As can be seen from Inventive Examples 1 to 4, it can be seen that, with an appropriate concentration of sodium hydroxide and immersion time, a high hydroxide / oxide ratio, Cr hydroxide / oxide ratio, and interfacial contact resistance of 20 mΩcm 2 or less in the passivation film can be secured. have.

특히 발명예 2에서 보는 바와 같이, 5 몰 농도의 수산화나트륨 용액에서 1분 간 침지한 후 부동태 피막 내 수산화물/산화물 비는 1.2가 됨을 알 수 있으며, Cr 수산화물/산화물 비는 3 이상이 됨을 알 수 있다.In particular, as shown in Inventive Example 2, after immersion for 1 minute in a 5 molar sodium hydroxide solution it can be seen that the hydroxide / oxide ratio in the passivation film is 1.2, the Cr hydroxide / oxide ratio is 3 or more. have.

이와 같이 표 2와 도 1에서 보는 바와 같이, 침지 조건에 따라 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 조절되었으며, 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 증가할수록 계면접촉저항이 감소함을 알 수 있었다. 또한 적정한 침지 조건에서 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비가 각각 1.0, 2.2 이상일 때 20 mΩ㎠ 이하의 계면접촉저항을 확보할 수 있음을 알 수 있다.As shown in Table 2 and FIG. 1, the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film were controlled according to the immersion conditions, and the interface contact resistance increased as the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film were increased. This decrease was found. In addition, it can be seen that the interfacial contact resistance of 20 mΩcm 2 or less can be secured when the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film are 1.0 and 2.2 or more, respectively, under appropriate immersion conditions.

이상의 실험에서 본 발명의 조성 범위를 갖는 스테인리스강의 표면 개질 방법에 있어서, 침지 용액의 조성 그리고 침지 시간이 부동태 피막 내 수산화물/산화물 비와 Cr 수산화물/산화물 비 증가와 계면접촉저항 저감에 중요한 요인으로 작용함을 알 수 있었다.In the above experiments, in the surface modification method of the stainless steel having the composition range of the present invention, the composition of the immersion solution and the immersion time act as important factors for increasing the hydroxide / oxide ratio and Cr hydroxide / oxide ratio in the passivation film and reducing the interfacial contact resistance. I could see.

본 발명의 발명예에 따라, 스테인리스강의 표면을 수산화나트륨 용액에서 침지 처리함으로써 부동태 피막 내에 1.0 이상의 수산화물/산화물 비와 2.2 이상의 Cr 수산화물/산화물 비를 확보 할 수 있으며, 20 mΩ㎠ 이하의 낮은 계면접촉저항을 나타내어 고분자 연료전지 분리판용으로 적합한 스테인리스강을 생산할 수 있다.According to an exemplary embodiment of the present invention, by immersing the surface of stainless steel in a sodium hydroxide solution, it is possible to ensure a hydroxide ratio of 1.0 or more and a Cr hydroxide / oxide ratio of 2.2 or more in the passivation film, and low interfacial contact of 20 mΩcm 2 or less. The resistance allows the production of stainless steel suitable for polymer fuel cell separators.

전술한 발명예에서는 고분자 연료전지 분리판을 예를 들어 설명하였지만, 그 외의 다양한 연료전지 분리판에 적용할 수 있음은 물론이다.In the above-described invention, the polymer fuel cell separator is described as an example, but it can be applied to various other fuel cell separators.

본 발명의 기술 사상은 상기 바람직한 발명예에 따라 구체적으로 기술되었으나, 상기한 발명예는 그 설명을 위한 것이며, 그 제한을 위한 것이 아님을 주지해야 한다. 또한, 본 발명의 기술분야에서 당업자는 본 발명의 기술 사상의 범위 내에서 다양한 발명예가 가능함을 이해할 수 있을 것이다.Although the technical spirit of the present invention has been described in detail according to the above-described preferred invention, it should be noted that the above-described invention is for the purpose of description and not of limitation. In addition, those skilled in the art will understand that various invention examples are possible within the scope of the technical idea of the present invention.

Claims (7)

중량%로, C: 0~0.02, N: 0~0.02, Si: 0~0.4, Mn: 0~0.2, P: 0~0.04, S: 0~0.02, Cr: 25~34, Mo:0~2.5미만, Cu:0~1, Ni:0~0.2미만, Ti: 0~0.5, Nb: 0~0.5와 Fe 및 기타 불가피한 불순물을 함유하고, 상기 스테인리스강 표면 부동태 피막이 1 이상의 수산화물/산화물 비를 가지며 계면 접촉저항이 20mΩ㎠(150N/㎠ ) 이하인 고분자 연료전지 분리판용 스테인리스강.By weight%, C: 0-0.02, N: 0-0.02, Si: 0-0.4, Mn: 0-0.2, P: 0-0.04, S: 0-0.02, Cr: 25-34, Mo: 0- Less than 2.5, Cu: 0 to 1, Ni: less than 0 to 0.2, Ti: 0 to 0.5, Nb: 0 to 0.5 and Fe and other unavoidable impurities, and the stainless steel surface passivation film is characterized by at least one hydroxide / oxide ratio. Interface contact resistance is 20mΩ㎠ (150N / ㎠ Stainless steel for polymer fuel cell separator plates of 제1항에 있어서,
상기 스테인리스강은 중량 %로, V: 0.2초과~1, W: 0~4를 단일 혹은 혼합 첨가한 조성으로 이루어지는 군에서 선택되는 1종 또는 2종의 원소가 더 포함되는 고분자 연료전지 분리판용 스테인리스강.
The method of claim 1,
The stainless steel is a weight%, stainless steel for polymer fuel cell separator further comprising one or two kinds of elements selected from the group consisting of a composition in which V: greater than 0.2 to 1 and W: 0 to 4 are added alone or in combination. River.
제1항에 있어서,
상기 스테인리스강의 부동태 피막내 Cr 수산화물/산화물 비가 2 이상인 고분자 연료전지 분리판용 스테인리스강.
The method of claim 1,
Stainless steel for a polymer fuel cell separator having a Cr hydroxide / oxide ratio of 2 or more in the passivation film of the stainless steel.
중량%로, C: 0~0.02, N: 0~0.02, Si: 0~0.4, Mn: 0~0.2, P: 0~0.04, S: 0~0.02, Cr: 25~34, Mo:0~2.5미만, Cu:0~1, Ni:0~0.2미만, Ti: 0~0.5, Nb: 0~0.5와 Fe 및 기타 불가피한 불순물을 함유하고, 상기 스테인리스강을 1 ~ 5 몰 농도 수산화나트륨의 조성으로 유지된 용액에서 침지하여 상기 스테인리스강 표면 부동태 피막이 1 이상의 수산화물/산화물 비를 가져 계면 접촉저항이 20mΩ㎠(150N/㎠)이하가 되도록 제어하는 고분자 연료전지 분리판용 스테인리스강 제조방법.By weight%, C: 0-0.02, N: 0-0.02, Si: 0-0.4, Mn: 0-0.2, P: 0-0.04, S: 0-0.02, Cr: 25-34, Mo: 0- Less than 2.5, Cu: 0 to 1, Ni: less than 0 to 0.2, Ti: 0 to 0.5, Nb: 0 to 0.5 and Fe and other unavoidable impurities, the stainless steel is composed of 1 to 5 molar concentrations of sodium hydroxide Method of manufacturing a stainless steel for a polymer fuel cell separator plate immersed in a solution maintained by the control to control the surface contact resistance of the stainless steel surface passivation film to have a hydroxide contact ratio of at least 20mΩ ㎠ (150N / ㎠) or less. 제4항에 있어서,
상기 스테인리스강은 중량 %로, V: 0.2초과~1, W: 0~4를 단일 혹은 혼합 첨가한 조성으로 이루어지는 군에서 선택되는 1종 또는 2종의 원소가 더 포함되는 고분자 연료전지 분리판용 스테인리스강 제조방법.
5. The method of claim 4,
The stainless steel is a weight%, stainless steel for polymer fuel cell separator further comprising one or two kinds of elements selected from the group consisting of a composition in which V: greater than 0.2 to 1 and W: 0 to 4 are added alone or in combination. Steel manufacturing method.
제4항에 있어서,
상기 스테인리스강은 상기 수산화나트륨 용액에서, 1~5분 침지하는 고분자 연료전지 분리판용 스테인리스강 제조방법.
5. The method of claim 4,
The stainless steel is a stainless steel manufacturing method for a polymer fuel cell separator plate immersed for 1 to 5 minutes in the sodium hydroxide solution.
제4항에 있어서,
상기 20mΩ㎠이하의 계면접촉저항을 갖도록 제조된 스테인리스강을 연료전지 분리판용으로 박판 성형하는 단계를 더 포함하는 연료전지 분리판용 스테인리스강 제조방법.
5. The method of claim 4,
The method of manufacturing a stainless steel for fuel cell separator further comprises the step of forming a thin plate for the fuel cell separator, the stainless steel manufactured to have an interfacial contact resistance of 20 mΩcm 2 or less.
KR1020110142161A 2011-12-26 2011-12-26 Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same KR101356954B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020110142161A KR101356954B1 (en) 2011-12-26 2011-12-26 Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020110142161A KR101356954B1 (en) 2011-12-26 2011-12-26 Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same

Publications (2)

Publication Number Publication Date
KR20130074216A true KR20130074216A (en) 2013-07-04
KR101356954B1 KR101356954B1 (en) 2014-01-28

Family

ID=48988369

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020110142161A KR101356954B1 (en) 2011-12-26 2011-12-26 Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same

Country Status (1)

Country Link
KR (1) KR101356954B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10991954B2 (en) 2015-12-23 2021-04-27 Posco Stainless steel for polymer fuel cell separation plate having improved hydrophilicity and contact resistance and method for manufacturing same
WO2021221246A1 (en) * 2020-04-28 2021-11-04 주식회사 포스코 Ferritic stainless steel having improved corrosion resistance, and method for manufacturing same
US11398631B2 (en) 2015-12-17 2022-07-26 Posco Stainless steel for separation plate of polymer electrolyte membrane fuel cell having improved hydrophilic property and corrosion resistance, and manufacturing method therefor

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100931457B1 (en) * 2007-12-20 2009-12-11 주식회사 포스코 Surface Modification Method of Stainless Steel for Polymer Fuel Cell Separator
JP4967831B2 (en) 2007-06-08 2012-07-04 Jfeスチール株式会社 Ferritic stainless steel for polymer electrolyte fuel cell separator and polymer electrolyte fuel cell using the same
JP5560533B2 (en) 2008-03-27 2014-07-30 Jfeスチール株式会社 Stainless steel for polymer electrolyte fuel cell separator and polymer electrolyte fuel cell using the same
KR100993412B1 (en) * 2008-12-29 2010-11-09 주식회사 포스코 Stainless steel for polymer electrolyte membrane fuel cell and fabrication method for the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11398631B2 (en) 2015-12-17 2022-07-26 Posco Stainless steel for separation plate of polymer electrolyte membrane fuel cell having improved hydrophilic property and corrosion resistance, and manufacturing method therefor
US10991954B2 (en) 2015-12-23 2021-04-27 Posco Stainless steel for polymer fuel cell separation plate having improved hydrophilicity and contact resistance and method for manufacturing same
WO2021221246A1 (en) * 2020-04-28 2021-11-04 주식회사 포스코 Ferritic stainless steel having improved corrosion resistance, and method for manufacturing same
CN115461486A (en) * 2020-04-28 2022-12-09 株式会社Posco Ferritic stainless steel with improved corrosion resistance and method for manufacturing same
CN115461486B (en) * 2020-04-28 2024-03-19 株式会社Posco Ferritic stainless steel with improved corrosion resistance and method for manufacturing same

Also Published As

Publication number Publication date
KR101356954B1 (en) 2014-01-28

Similar Documents

Publication Publication Date Title
US11085120B2 (en) Stainless steel sheet for fuel cell separators and production method therefor
KR101798406B1 (en) Stainless steel for fuel cell separator and method of manufacturing the same
JP5971446B1 (en) Ferritic stainless steel material, polymer electrolyte fuel cell separator and polymer electrolyte fuel cell using the same
JP2008285731A (en) Stainless steel sheet having excellent surface electrical conductivity, and method for producing the same
WO2016052623A1 (en) Ferritic stainless steel material, separator for solid polymer fuel cells which uses same, and solid polymer fuel cell
JP2019505972A (en) Stainless steel for separator plate of polymer fuel cell with improved hydrophilicity and corrosion resistance and method for producing the same
JP2012067391A (en) Stainless steel sheet for conductive member, excellent in surface electric conductivity
KR102385477B1 (en) Substrate stainless steel sheet for fuel cell separators and production method therefor
KR101356954B1 (en) Stainless steel for polymer electrolyte membrane fuel cell separator and the method of manufacturing the same
KR101312861B1 (en) Stainless steel for bipolar plate of PEMFC with excellent corrosion resistance and contact resistance and method of manufacturing the bipolar plate
JP6898451B2 (en) Stainless steel for polymer fuel cell separation plates with excellent contact resistance and its manufacturing method
KR20080109148A (en) Stainless steel having excellent corrosion resistance and electric conductivity and bipolar plate made of the same
KR101239476B1 (en) stainless steel for bipolar plate of PEMFC and method of manufacturing the same
JP2004269969A (en) Separator for solid polymer type fuel cell and manufacturing method therefor
JP5560533B2 (en) Stainless steel for polymer electrolyte fuel cell separator and polymer electrolyte fuel cell using the same
KR102068479B1 (en) Manufacturing method of ferritic stainless steel for proton exchange membrane fuel cell separator with excellent surface contact resistance
KR101410944B1 (en) Fabrication of stainless steel for PEMFC bipolar plate
CN114730892B (en) Method for manufacturing stainless steel for polymer fuel cell separator
JP7361478B2 (en) Austenitic stainless steel material for fuel cell separator and its manufacturing method, fuel cell separator, and fuel cell
KR100867819B1 (en) Surface layer of metal bipolar plate for fuel cell and method for creating the same
EP4253591A1 (en) Austenitic stainless steel for polymer fuel cell separator with improved contact resistance, and manufacturing method thereof
JP4425702B2 (en) Stainless steel with excellent conductivity and corrosion resistance and polymer electrolyte fuel cell separator formed by the stainless steel
JP2005213539A (en) Ferritic stainless steel for solid polymeric fuel cell separator
JP2015113510A (en) Metal separator material and metal separator

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20170116

Year of fee payment: 4

FPAY Annual fee payment

Payment date: 20180119

Year of fee payment: 5

FPAY Annual fee payment

Payment date: 20190123

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20200122

Year of fee payment: 7