JP2003217598A - Electrode material for fuel cell - Google Patents

Electrode material for fuel cell

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Publication number
JP2003217598A
JP2003217598A JP2002010751A JP2002010751A JP2003217598A JP 2003217598 A JP2003217598 A JP 2003217598A JP 2002010751 A JP2002010751 A JP 2002010751A JP 2002010751 A JP2002010751 A JP 2002010751A JP 2003217598 A JP2003217598 A JP 2003217598A
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JP
Japan
Prior art keywords
electrode material
fuel cell
electrode
carbon monoxide
platinum
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
JP2002010751A
Other languages
Japanese (ja)
Other versions
JP4267854B2 (en
Inventor
Yoichi Shimizu
清水陽一
Junichi Tokunaga
徳永純一
Yoshitaka Uchida
内田佳孝
Keigo Tsujimoto
辻本敬吾
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.)
Kyushu Electric Power Co Inc
Original Assignee
Kyushu Electric Power Co Inc
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Filing date
Publication date
Application filed by Kyushu Electric Power Co Inc filed Critical Kyushu Electric Power Co Inc
Priority to JP2002010751A priority Critical patent/JP4267854B2/en
Publication of JP2003217598A publication Critical patent/JP2003217598A/en
Application granted granted Critical
Publication of JP4267854B2 publication Critical patent/JP4267854B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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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  • Fuel Cell (AREA)
  • Inert Electrodes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an electrode material for a fuel cell, which scarcely causes deterioration of cell performance by carbon monoxide. <P>SOLUTION: The electrode material for a fuel cell is composed of a pyrochlore type oxide represented by A<SB>2-</SB>XB<SB>2-</SB>YO<SB>7-</SB>Z, (wherein, A=Pb, B=Ir, 0≤X≤0.2, 0≤Y≤0.2, and 0≤Z≤0.5). <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、燃料電池電極材料
に関し、触媒作用を有するパイロクロア型酸化物であっ
て、A2-X2-Y7-Z(但しA=Pb、B=Irで
あり、0≦X≦0.2、0≦Y≦0.2、0≦Z≦0.
5)の組成からなる燃料電池電極材料に関する。 【0002】 【従来技術】固体高分子形燃料電池の電極触媒として、
一般に白金系触媒が用いられている。白金系触媒の特徴
は、燃料電池の陰極反応H→2H++2e、陽極反応
1/2O+2H++2e→HOにおいて高い触媒活
性、電池性能を示すことである。 【0003】しかしながら、燃料電池の燃料に、改質反
応を用いて炭化水素等から取り出した水素を燃料として
用いる場合、燃料中に含まれる一酸化炭素の影響によ
り、陰極側電極触媒である白金が被毒され、触媒活性が
低下し、電池性能が低下する。 【0004】この一酸化炭素による白金の活性低下を抑
えるために、例えば特開2000−3712号公報に開
示されているように、白金−ルテニウム合金を用いた電
極触媒が提案されている。この触媒は、燃料中に許容濃
度以下の一酸化炭素が含まれていても、一酸化炭素が含
まれない場合と同程度の電池性能を示すことが特徴であ
る。 【0005】 【発明が解決しようとする課題】しかしながら、燃料中
の一酸化炭素を許容濃度以下にするためには、燃料改質
器に一酸化炭素濃度を所定の濃度まで低減させる装置を
設けることが必要となる。さらに許容濃度以上の一酸化
炭素が含まれる燃料が供給されると、電池性能が低下す
るという問題がある。 【0006】そこで、本発明では、上記問題を解決する
ために、一酸化炭素による電池性能低下の少ない燃料電
池電極材料を提供する。 【0007】 【課題を解決するための手段】本発明の燃料電池電極材
料は、A2-X2-Y7-Z(但しA=Pb、B=Ir
であり、0≦X≦0.2、0≦Y≦0.2、0≦Z≦0.
5)で表されるパイロクロア型酸化物であることを特徴
とする。 【0008】 【発明の実施の形態】本発明に用いるパイロクロア型酸
化物の原料として塩化鉛および、塩化イリジウム酸6水
和物を用いた。これらを苛性ソーダ水溶液中に溶解さ
せ、75℃に加温しながら酸素ガスを24時間バブリン
グする共沈法によって沈殿物を得た。 【0009】この沈殿物を120℃で12時間乾燥し、
乳鉢で粉砕し、水洗を行った後さらに120℃で12時
間乾燥し、乳鉢で粉砕した。得られた粉体を空気中で8
00℃または380℃で2時間焼成し、PbIr
6.5のパイロクロア型酸化物を得た。800℃で焼成
した酸化物は粒径約20nm、380℃では粒径約5n
mであった。 【0010】このパイロクロア型酸化物を用いた電極材
料は、図1で示されるように反応層1、ガス拡散層2か
ら成る。反応層材料はブタノール水溶液中に、疎水性カ
ーボンブラックとポリテトラフルオロエチレンと、さき
に合成したパイロクロア型酸化物を、酸化物:疎水性カ
ーボンブラック:PTFE=40:28:32の重量比
で加え1時間混合し、濾過、乾燥することにより得られ
る。 【0011】ガス拡散層材料は、ブタノール水溶液中
で、ポリテトラフルオロエチレンと親水性カーボンブラ
ックを4:6の重量比で加えて混合し、濾過、乾燥する
ことにより得られる。このガス拡散層材料を集電体とし
て用いる銅メッシュ板3とともに380℃、60MPa
でホットプレスしガス拡散層2とした。 【0012】これらの反応層1とガス拡散層2を380
℃、60MPaでホットブレスし、接合することにより
図1で示されるような燃料電池電極材料が得られる。 【0013】比較例 本発明と、従来技術を比較するために、白金を用いた電
極材料を作成した。反応層材料は、ブタノール水溶液中
に、疎水性カーボンブラックと塩化白金酸アンモニウム
溶液を混合した(カーボン:PT=10:1;質量比
率)。さらに、ポリテトラフルオロエチレン(カーボ
ン:PTFE=2:1;質量比率)を加えて1時間混合
し、濾過、乾燥することにより得られる。 【0014】白金を材料とした反応層と、上記と同様な
方法で作製したガス拡散層を370℃、60MPaでホ
ットブレスし、本発明との比較となる電極材料とした。 【0015】上記方法で得られた電極材料を、公知の電
気化学的測定装置に取り付け、電極材料の電極性能を確
認した。この電気化学的測定装置は、2Nの硫酸水溶液
を満たした水槽中に、電極材料を設置し試験電極とし
た。この試験電極には水素又は一酸化炭素を含む水素を
外部から供給することができる。さらに、2N硫酸中に
対極として白金電極を、参照極として水素電極を設置し
た。 【0016】上記の測定装置を用いて、燃料電池電極材
料の電極性能(50℃における水素電極との電位差20
0mV 時の電流密度(mA/cm)を測定した。そ
の結果を表1に示す。 【0017】 【表1】 表1から、50℃において、100ppmの一酸化炭素
を含む水素を燃料とした場合、白金を用いた電極材料よ
りも、380℃で焼成した本発明のパイロクロア型酸化
物を用いた電極材料は、参照極である水素電極との電位
差200mVのときの電流密度が小さいことがわかっ
た。このことから、本発明のパイロクロア型酸化物を用
いた電極材料は、一酸化炭素による電池性能低下が少な
いことがわかった。 【0018】 【発明の効果】以上のように本発明によれば、一酸化炭
素を含む燃料中では従来の白金を材料とした電極材料よ
りも電池性能が向上する。
Description: BACKGROUND OF THE INVENTION [0001] 1. Field of the Invention [0002] The present invention relates to a fuel cell electrode material, which is a pyrochlore type oxide having a catalytic action, and is composed of A 2 -XB 2 -Y 7-. Z (where A = Pb, B = Ir, 0 ≦ X ≦ 0.2, 0 ≦ Y ≦ 0.2, 0 ≦ Z ≦ 0.
It relates to a fuel cell electrode material having the composition of 5). [0002] As an electrode catalyst of a polymer electrolyte fuel cell,
Generally, a platinum-based catalyst is used. The platinum-based catalyst is characterized by exhibiting high catalytic activity and cell performance in the cathode reaction H 2 → 2H + + 2e and the anode reaction 1 / 2O 2 + 2H + + 2e → H 2 O of the fuel cell. [0003] However, when hydrogen extracted from hydrocarbons or the like using a reforming reaction is used as a fuel for a fuel cell, platinum, which is a cathode-side electrode catalyst, is affected by carbon monoxide contained in the fuel. It is poisoned, catalyst activity is reduced, and battery performance is reduced. In order to suppress the decrease in platinum activity due to carbon monoxide, an electrode catalyst using a platinum-ruthenium alloy has been proposed, for example, as disclosed in JP-A-2000-3712. This catalyst is characterized in that even if carbon monoxide is contained in the fuel in an amount equal to or less than the allowable concentration, it exhibits the same cell performance as that in the case where carbon monoxide is not contained. [0005] However, in order to reduce the carbon monoxide concentration in the fuel to an allowable concentration or less, a device for reducing the carbon monoxide concentration to a predetermined concentration is provided in the fuel reformer. Is required. Further, when a fuel containing carbon monoxide at a permissible concentration or more is supplied, there is a problem that the cell performance is reduced. Accordingly, the present invention provides a fuel cell electrode material in which the performance of the fuel cell is hardly degraded by carbon monoxide in order to solve the above problems. [0007] Means for Solving the Problems A fuel cell electrode material of the present invention, A 2-X B 2- Y O 7-Z ( where A = Pb, B = Ir
0 ≦ X ≦ 0.2, 0 ≦ Y ≦ 0.2, 0 ≦ Z ≦ 0.2.
It is a pyrochlore type oxide represented by 5). DETAILED DESCRIPTION OF THE INVENTION As a raw material of a pyrochlore type oxide used in the present invention, lead chloride and iridium chloride hexahydrate were used. These were dissolved in an aqueous solution of caustic soda, and a precipitate was obtained by a coprecipitation method in which oxygen gas was bubbled for 24 hours while heating to 75 ° C. The precipitate is dried at 120 ° C. for 12 hours,
After pulverized in a mortar, washed with water, dried at 120 ° C. for 12 hours, and pulverized in a mortar. The obtained powder is dried in air for 8 hours.
Firing at 00 ° C. or 380 ° C. for 2 hours, Pb 2 Ir 2 O
A pyrochlore type oxide of 6.5 was obtained. The oxide calcined at 800 ° C. has a particle size of about 20 nm, and at 380 ° C., a particle size of about 5 n
m. The electrode material using the pyrochlore type oxide comprises a reaction layer 1 and a gas diffusion layer 2 as shown in FIG. As a reaction layer material, a hydrophobic carbon black, polytetrafluoroethylene, and a pyrochlore-type oxide synthesized earlier were added to a butanol aqueous solution in a weight ratio of oxide: hydrophobic carbon black: PTFE = 40: 28: 32. It is obtained by mixing for 1 hour, filtering and drying. The gas diffusion layer material is obtained by adding and mixing polytetrafluoroethylene and hydrophilic carbon black in a weight ratio of 4: 6 in an aqueous butanol solution, followed by filtration and drying. 380 ° C., 60 MPa together with the copper mesh plate 3 using this gas diffusion layer material as a current collector
And hot pressed to form a gas diffusion layer 2. The reaction layer 1 and the gas diffusion layer 2 are
By hot-breathing and joining at 60 ° C. and 60 ° C., a fuel cell electrode material as shown in FIG. 1 is obtained. Comparative Example In order to compare the present invention with the prior art, an electrode material using platinum was prepared. The reaction layer material was prepared by mixing a hydrophobic carbon black and an ammonium chloroplatinate solution in a butanol aqueous solution (carbon: PT = 10: 1; mass ratio). Furthermore, it is obtained by adding polytetrafluoroethylene (carbon: PTFE = 2: 1; mass ratio), mixing for 1 hour, filtering and drying. A reaction layer made of platinum and a gas diffusion layer produced by the same method as described above were hot-pressed at 370 ° C. and 60 MPa to obtain an electrode material for comparison with the present invention. The electrode material obtained by the above method was attached to a known electrochemical measuring device, and the electrode performance of the electrode material was confirmed. In this electrochemical measurement device, an electrode material was placed in a water tank filled with a 2N aqueous sulfuric acid solution to form a test electrode. Hydrogen or hydrogen containing carbon monoxide can be externally supplied to the test electrode. Further, a platinum electrode was provided as a counter electrode and a hydrogen electrode was provided as a reference electrode in 2N sulfuric acid. Using the above measuring device, the electrode performance of the fuel cell electrode material (potential difference from hydrogen electrode at 50 ° C.
The current density at 0 mV (mA / cm 2 ) was measured. Table 1 shows the results. [Table 1] From Table 1, at 50 ° C., when hydrogen containing 100 ppm of carbon monoxide was used as the fuel, the electrode material using the pyrochlore-type oxide of the present invention fired at 380 ° C., compared to the electrode material using platinum, It was found that the current density was small at a potential difference of 200 mV from the hydrogen electrode serving as the reference electrode. From this, it was found that the electrode material using the pyrochlore type oxide of the present invention did not cause much deterioration in battery performance due to carbon monoxide. As described above, according to the present invention, in a fuel containing carbon monoxide, battery performance is improved as compared with a conventional electrode material using platinum as a material.

【図面の簡単な説明】 【図1】本発明に係わる電極材料の構造を示す側面断面
図である。 【符号の説明】 1…反応層 2…ガス拡散層 3…銅メッシュ板
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a side sectional view showing a structure of an electrode material according to the present invention. [Description of Signs] 1 ... Reaction layer 2 ... Gas diffusion layer 3 ... Copper mesh plate

───────────────────────────────────────────────────── フロントページの続き (72)発明者 内田佳孝 福岡県福岡市南区塩原2丁目1番47号 九 州電力株式会社総合研究所内 (72)発明者 辻本敬吾 福岡県福岡市南区塩原2丁目1番47号 九 州 電力株式会社総合研究所内 Fターム(参考) 5H018 EE02 EE13 HH00 5H026 AA06 BB01 EE13 HH00    ────────────────────────────────────────────────── ─── Continuation of front page    (72) Inventor Yoshitaka Uchida             Fukuoka Prefecture Fukuoka City Minami-ku Shiobara 2-1-1 47             State Electric Power Company Research Institute (72) Inventor Keigo Tsujimoto             Fukuoka Prefecture Fukuoka City Minami-ku Shiobara 2-1-1 47             State Electric Power Co., Inc. F-term (reference) 5H018 EE02 EE13 HH00                 5H026 AA06 BB01 EE13 HH00

Claims (1)

【特許請求の範囲】 【請求項1】 A2-X2-Y7-Z(但しA=Pb、
B=Irであり、0≦X≦0.2、0≦Y≦0.2、0≦
Z≦0.5)で表されるパイロクロア型酸化物であるこ
とを特徴とする燃料電池電極材料。
[Claims 1] A 2-X B 2-Y O 7-Z ( where A = Pb,
B = Ir, 0 ≦ X ≦ 0.2, 0 ≦ Y ≦ 0.2, 0 ≦
An electrode material for a fuel cell, which is a pyrochlore type oxide represented by the following formula: Z ≦ 0.5).
JP2002010751A 2002-01-18 2002-01-18 Fuel cell electrode material Expired - Fee Related JP4267854B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002010751A JP4267854B2 (en) 2002-01-18 2002-01-18 Fuel cell electrode material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002010751A JP4267854B2 (en) 2002-01-18 2002-01-18 Fuel cell electrode material

Publications (2)

Publication Number Publication Date
JP2003217598A true JP2003217598A (en) 2003-07-31
JP4267854B2 JP4267854B2 (en) 2009-05-27

Family

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Country Status (1)

Country Link
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005209607A (en) * 2003-12-24 2005-08-04 Mitsubishi Materials Corp Gas diffusion layer member of solid polymer fuel cell and its manufacturing method
JP2006196329A (en) * 2005-01-14 2006-07-27 Doshisha Air electrode and air secondary battery using this air electrode
WO2006090907A1 (en) * 2005-02-24 2006-08-31 Toyota Jidosha Kabushiki Kaisha Catalyst for fuel cell, membrane electrode assembly, and solid polymer electrolyte fuel cell
JP2007257965A (en) * 2006-03-22 2007-10-04 Toyota Central Res & Dev Lab Inc Polymer electrolyte fuel cell and fuel cell system
WO2010092971A1 (en) * 2009-02-10 2010-08-19 新日本石油株式会社 Process for preparing pyrochlore oxide, and polymer electrolyte membrane fuel cell, fuel cell system, and process for producing electrode catalyst for fuel cell
JP2012049075A (en) * 2010-08-30 2012-03-08 Jx Nippon Oil & Energy Corp Method of preparing pyrochlore type oxide and method of manufacturing electrode catalyst for fuel cell

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005209607A (en) * 2003-12-24 2005-08-04 Mitsubishi Materials Corp Gas diffusion layer member of solid polymer fuel cell and its manufacturing method
JP2006196329A (en) * 2005-01-14 2006-07-27 Doshisha Air electrode and air secondary battery using this air electrode
JP4568124B2 (en) * 2005-01-14 2010-10-27 学校法人同志社 Air electrode and air secondary battery using the air electrode
WO2006090907A1 (en) * 2005-02-24 2006-08-31 Toyota Jidosha Kabushiki Kaisha Catalyst for fuel cell, membrane electrode assembly, and solid polymer electrolyte fuel cell
US8815470B2 (en) 2005-02-24 2014-08-26 Toyota Jidosha Kabushiki Kaisha Fuel cell catalyst, membrane electrode assembly and solid polymer electrolyte fuel cell
JP2007257965A (en) * 2006-03-22 2007-10-04 Toyota Central Res & Dev Lab Inc Polymer electrolyte fuel cell and fuel cell system
WO2010092971A1 (en) * 2009-02-10 2010-08-19 新日本石油株式会社 Process for preparing pyrochlore oxide, and polymer electrolyte membrane fuel cell, fuel cell system, and process for producing electrode catalyst for fuel cell
JP2010184824A (en) * 2009-02-10 2010-08-26 Nippon Oil Corp Method for preparing pyrochlore type oxide, polymer electrolyte fuel cell, fuel cell system and method for producing electrode catalyst for fuel cell
US8329129B2 (en) 2009-02-10 2012-12-11 Jx Nippon Oil & Energy Corporation Method for preparing pyrochlore oxide, polymer electrolyte fuel cell, fuel cell system, and method for producing electro catalyst for fuel cell
JP2012049075A (en) * 2010-08-30 2012-03-08 Jx Nippon Oil & Energy Corp Method of preparing pyrochlore type oxide and method of manufacturing electrode catalyst for fuel cell

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