JP3072034B2 - Fuel cell separator - Google Patents
Fuel cell separatorInfo
- Publication number
- JP3072034B2 JP3072034B2 JP7218867A JP21886795A JP3072034B2 JP 3072034 B2 JP3072034 B2 JP 3072034B2 JP 7218867 A JP7218867 A JP 7218867A JP 21886795 A JP21886795 A JP 21886795A JP 3072034 B2 JP3072034 B2 JP 3072034B2
- Authority
- JP
- Japan
- Prior art keywords
- plate
- cathode
- center plate
- anode
- center
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
- H01M8/0254—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form corrugated or undulated
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、溶融炭酸塩型燃料
電池に用いられるセパレータの構成に関する。The present invention relates to a structure of a separator used in a molten carbonate fuel cell.
【0002】[0002]
【従来の技術】溶融炭酸塩型燃料電池は、高効率で環境
への影響が少ないなど、従来の発電装置にない特徴を有
しており、水力、火力、原子力に続く発電システムとし
て注目を集め、現在鋭意研究が進められている。2. Description of the Related Art Molten carbonate fuel cells have features not found in conventional power generators, such as high efficiency and low environmental impact, and have attracted attention as power generation systems following hydro, thermal and nuclear power. Currently, intensive research is underway.
【0003】溶融炭酸塩型燃料電池は単セルでは低電圧
(0.8V程度)であるため、実用上はセパレータ(バ
イポーラプレート)を介して多段数に積層した電池を用
いる。この積層電池をスタックと呼ぶ。図3は積層電池
の構成を示す。1は単セルを示す。単セル1は中心に電
解質板2を設け、一方の面にカソード3(空気極)、他
方の面にアノード4(燃料極)を配置し、セパレータ5
によりカソード3には酸素を含むカソードガス6を供給
し、アノード4には水素を含むアノードガス7を供給す
るように構成される。これをセパレータ5を中心にして
考えると、一方の面にカソード3が設けられ、他方の面
にアノード4が設けられ、カソード3にはカソードガス
6を、アノード4にはアノードガス7をそれぞれ分離し
て供給する。[0003] Since a molten carbonate fuel cell has a low voltage (about 0.8 V) in a single cell, a battery stacked in multiple stages via a separator (bipolar plate) is practically used. This stacked battery is called a stack. FIG. 3 shows a configuration of the laminated battery. 1 indicates a single cell. The unit cell 1 is provided with an electrolyte plate 2 at the center, a cathode 3 (air electrode) on one surface, an anode 4 (fuel electrode) on the other surface, and a separator 5.
Thus, a cathode gas 6 containing oxygen is supplied to the cathode 3 and an anode gas 7 containing hydrogen is supplied to the anode 4. Considering this with the separator 5 as the center, the cathode 3 is provided on one surface, the anode 4 is provided on the other surface, the cathode gas 6 is separated from the cathode 3, and the anode gas 7 is separated from the anode 4. Supply.
【0004】スタックは電解質板2を介してセパレータ
5を多段に積層することにより構成されるので、セパレ
ータ5は溶融炭酸塩型燃料電池の製作費のうち大きなウ
エイトを占める。セパレータ5を多量に製作する場合薄
板構造のプレス成形方法が低コスト化に最も有望であ
る。図3に模式的に示したセパレータ5は機械加工で削
り出して製作するイメージであるが、プレスで成形する
場合、1枚の板(これをセンタープレートと呼ぶことに
するが)をプレスで波形に成形してカソードガス6とア
ノードガス7の通路を設ける。[0004] Since the stack is formed by stacking the separators 5 in multiple stages with the electrolyte plate 2 interposed therebetween, the separators 5 occupy a large part of the production cost of the molten carbonate fuel cell. When a large number of separators 5 are manufactured, a press forming method having a thin plate structure is most promising for cost reduction. The separator 5 schematically shown in FIG. 3 is an image produced by shaving out by machining, but when it is formed by pressing, a single plate (this is called a center plate) is corrugated by pressing. And a passage for the cathode gas 6 and the anode gas 7 is provided.
【0005】[0005]
【発明が解決しようとする課題】燃料電池用セパレータ
5ではカソード3、アノード4の両電極及び電解質板2
を保持する役割がある。電極3、4や電解質板2は金属
に比較して非常に脆いため、セパレータ5が変形してい
ると組立時に電極3、4や電解質板2に割れを発生させ
る恐れがある。セパレータ5の主要部材であるセンター
プレートにプレス加工をする場合、単位面積当たりの荷
重はかなりの大きさとなるため全体的に変形の発生する
可能性が大きい。このため現状では多くの場合セパレー
タ5をプレス加工した後熱処理を行い、変形を除去して
おり、これによるコストアップや作業時間の増加が問題
となっている。In the fuel cell separator 5, both the cathode 3 and the anode 4 and the electrolyte plate 2 are provided.
There is a role to hold. Since the electrodes 3 and 4 and the electrolyte plate 2 are very brittle as compared with metal, if the separator 5 is deformed, the electrodes 3 and 4 and the electrolyte plate 2 may be cracked during assembly. In the case where the center plate, which is a main member of the separator 5, is pressed, the load per unit area is considerably large, so that there is a large possibility that deformation will occur as a whole. For this reason, under the present circumstances, in many cases, heat treatment is performed after pressing the separator 5 to remove the deformation, and thus, there is a problem that the cost is increased and the working time is increased.
【0006】本発明は上述の問題に鑑みてなされたもの
で、プレスにより成形するセパレータの変形を抑制する
ことを目的とする。The present invention has been made in view of the above problems, and has as its object to suppress deformation of a separator formed by pressing.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するた
め、請求項1の発明では、アノードガスとカソードガス
を分離するセンタープレートと、このセンタープレート
とほぼ同一の外形寸法で中央に電極用の開口を有しセン
タープレートを挟んで所定の間隔で平行に設けられ外周
端でセンタープレートに密着した2枚のマスクプレート
と、このマスクプレートの内面に接してこれと平行に前
記電極用の開口を覆うように設けられたパンチプレート
と、を備え、前記マスクプレートの所定の間隔を有する
外周端の周囲にわたり前記センタープレートを波形にす
る。In order to achieve the above object, according to the first aspect of the present invention, a center plate for separating an anode gas and a cathode gas, and a center electrode having substantially the same external dimensions as the center plate and having a central electrode. Two mask plates having openings and provided in parallel at a predetermined interval with the center plate interposed therebetween and closely attached to the center plate at the outer peripheral end, and the openings for the electrodes in contact with and in parallel with the inner surface of the mask plate. And a punch plate provided so as to cover the center plate, and the center plate is corrugated around an outer peripheral end of the mask plate having a predetermined interval.
【0008】センタープレートの外周に沿って波形の形
状を設けることにより周囲の剛性が増加し、変形を防止
することができる。By providing a corrugated shape along the outer periphery of the center plate, the rigidity of the periphery is increased and deformation can be prevented.
【0009】請求項2の発明では、前記波形の上下の間
隔は前記マスクプレートの前記所定の間隔に嵌合する寸
法である。これによりセンタープレートは周囲でマスク
プレートにより保持されるため変形を抑制することがで
きる。According to the second aspect of the present invention, the vertical interval between the waveforms is a dimension that fits into the predetermined interval of the mask plate. This allows the center plate to be held around by the mask plate, thereby suppressing deformation.
【0010】[0010]
【発明の実施の形態】以下、本発明の実施の形態につい
て図面を参照して説明する。図1はセパレータの実施の
形態を示す平面図で、一部カソードガスの流れる面を示
す。本図において図3と同一機能を有するものは同一符
号で表す。図2は図1のA−A断面、B−B断面、及び
C−C断面を示す。セパレータ5はほぼ正方形で、中央
の開口部は電池領域10でカソード3またはアノード4
が設けられる。図1はカソード3の面を示しこの下面が
アノード4であるとして説明するが、この逆でもよい。
電池領域10の下側にはカソードガス6を供給するカソ
ードガス開口11とアノードガス7を供給するアノード
ガス開口12が設けられ、上側にはカソード3を通過し
て電池反応を行って排出されたカソード排ガス8を収集
するカソード排ガス開口13と、アノード4を通過して
電池反応を行って排出されたアノード排ガス9を収集す
るカソード排ガス開口14が設けられている。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a plan view showing an embodiment of a separator, partially showing a surface through which a cathode gas flows. In this drawing, components having the same functions as those in FIG. 3 are denoted by the same reference numerals. FIG. 2 shows an AA section, a BB section, and a CC section of FIG. The separator 5 has a substantially square shape, and a central opening is formed in the battery area 10 by the cathode 3 or the anode 4.
Is provided. FIG. 1 shows the surface of the cathode 3 and it is assumed that the lower surface is the anode 4, but the reverse is also possible.
A cathode gas opening 11 for supplying the cathode gas 6 and an anode gas opening 12 for supplying the anode gas 7 are provided on the lower side of the battery region 10, and the upper side is passed through the cathode 3 to perform a battery reaction and discharged. A cathode exhaust gas opening 13 for collecting the cathode exhaust gas 8 and a cathode exhaust gas opening 14 for collecting the anode exhaust gas 9 that has passed through the anode 4 to perform a battery reaction and have been discharged are provided.
【0011】カソードガス流路15は4段となってお
り、各段ごとに多少ずらすことによりガスの流れを流れ
方向と直角方向に拡散させるようにしている。周囲には
溝16が設けられ内部のガスが外に漏れないよう、また
外から空気が入らないようにしている。The cathode gas passage 15 has four stages, and the gas flow is diffused in a direction perpendicular to the flow direction by slightly shifting each stage. Grooves 16 are provided around the periphery to prevent gas inside from leaking out and to prevent air from entering from outside.
【0012】図2のA−A断面において、センタープレ
ート20は波形にプレスされており、この周囲、上下に
平行に2枚のマスクプレート21が設けられている。上
下のマスクプレート21の内面に接してパンチプレート
22が平行に設けられ、このパンチプレート22間にセ
ンタープレート20の波形が配置され、パンチプレート
22を支持している。パンチプレート22の上面の電池
領域10にはカソード3が設けられ、下面の電池領域1
0にはアノード4が設けられている。パンチプレート2
2は電極3、4を支持するとともに多数の開口を通して
カソードガス6、アノードガス7を電極3、4に伝達す
る働きをする。センタープレート20の波形のカソード
3側にはカソードガス6が流れ、アノード4側にはアノ
ードガス7が流れる。なお、溝16を構成する波形の位
置にはガスは流れない。B−B断面はA−A断面とほぼ
同じ構造である。In the AA cross section of FIG. 2, the center plate 20 is pressed into a corrugated shape, and two mask plates 21 are provided in parallel around the center plate 20 in the vertical direction. Punch plates 22 are provided in parallel in contact with the inner surfaces of the upper and lower mask plates 21, and the waveform of the center plate 20 is arranged between the punch plates 22 to support the punch plates 22. The cathode 3 is provided in the battery region 10 on the upper surface of the punch plate 22, and the battery region 1 on the lower surface.
At 0, an anode 4 is provided. Punch plate 2
2 functions to support the electrodes 3 and 4 and to transmit the cathode gas 6 and the anode gas 7 to the electrodes 3 and 4 through a number of openings. The cathode gas 6 flows on the cathode 3 side of the waveform of the center plate 20, and the anode gas 7 flows on the anode 4 side. The gas does not flow at the position of the waveform forming the groove 16. The cross section BB has substantially the same structure as the cross section AA.
【0013】C−C断面はセパレータ5の外周に沿って
全周にわたり上下のマスクプレート21間にセンタープ
レート20を波形23にして設けたものである。このよ
うにセンタープレート20の全周に波形23を設けるこ
とによりセンタープレート20の剛性が増し、全体的な
変形を抑制する。この波形23はA−A断面、B−B断
面ではでは左端に示されている。なお、この波形23は
上下のマスクプレート21間と嵌合することによりセパ
レータ5の全体的な変形を抑制することができる。な
お、波形の形状は正弦(サイン)波状としたが矩形波状
としてもよい。The C-C cross section is such that the center plate 20 is provided in a waveform 23 between the upper and lower mask plates 21 over the entire circumference along the outer circumference of the separator 5. By providing the waveform 23 over the entire circumference of the center plate 20 in this manner, the rigidity of the center plate 20 increases, and overall deformation is suppressed. This waveform 23 is shown at the left end in the AA section and the BB section. Note that the waveform 23 can suppress the overall deformation of the separator 5 by fitting between the upper and lower mask plates 21. Although the shape of the waveform is sinusoidal (sine), it may be rectangular.
【0014】[0014]
【発明の効果】以上の説明より明らかなように、本発明
はセパレータのセンタープレートの外周全周にわたりマ
スクプレート間に波形を設け、プレスによって生じる全
体的な変形を防止することができる。これにより熱処理
による変形除去作業が不要になりセパレータの製作費用
の削減や製作期間の短縮を実現できる。As is apparent from the above description, according to the present invention, a corrugation is provided between the mask plates over the entire circumference of the center plate of the separator, so that the entire deformation caused by the press can be prevented. This eliminates the need for the deformation removal operation by heat treatment, thereby reducing the production cost and the production period of the separator.
【図1】実施の形態のセパレータ平面図である。FIG. 1 is a plan view of a separator according to an embodiment.
【図2】図1のA−A断面、B−B断面、C−C断面を
示す。FIG. 2 shows an AA section, a BB section, and a CC section of FIG.
【図3】燃料電池の模式図である。FIG. 3 is a schematic diagram of a fuel cell.
1 単セル 2 電解質板 3 カソード 4 アノード 5 セパレータ 6 カソードガス 7 アノードガス 8 カソード排ガス 9 アノード排ガス 10 電池領域 11 カソードガス開口 12 アノードガス開口 13 カソード排ガス開口 14 アノード排ガス開口 15 カソードガス流路 16 溝 20 センタープレート 21 マスクプレート 22 パンチプレート 23 波形 DESCRIPTION OF SYMBOLS 1 Single cell 2 Electrolyte plate 3 Cathode 4 Anode 5 Separator 6 Cathode gas 7 Anode gas 8 Cathode exhaust gas 9 Anode exhaust gas 10 Battery area 11 Cathode gas opening 12 Anode gas opening 13 Cathode exhaust gas opening 14 Anode exhaust gas opening 15 Cathode gas flow path 16 groove Reference Signs List 20 center plate 21 mask plate 22 punch plate 23 waveform
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭63−241870(JP,A) 特開 平7−85880(JP,A) 特開 平9−63598(JP,A) 特開 平9−63599(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 8/00 - 8/24 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-63-241870 (JP, A) JP-A-7-85880 (JP, A) JP-A-9-63598 (JP, A) JP-A-9-98 63599 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 8/00-8/24
Claims (2)
センタープレートと、このセンタープレートとほぼ同一
の外形寸法で中央に電極用の開口を有しセンタープレー
トを挟んで所定の間隔で平行に設けられ外周端でセンタ
ープレートに密着した2枚のマスクプレートと、このマ
スクプレートの内面に接してこれと平行に前記電極用の
開口を覆うように設けられたパンチプレートと、を備
え、 前記マスクプレートの所定の間隔を有する外周端の周囲
にわたり前記センタープレートを波形にしたことを特徴
とする燃料電池用セパレータ。1. A center plate for separating anode gas and cathode gas, and an opening for an electrode at the center having substantially the same outer dimensions as the center plate, and provided in parallel at a predetermined interval with the center plate interposed therebetween. Two mask plates that are in close contact with the center plate at the ends, and a punch plate that is in contact with the inner surface of the mask plate and that is provided so as to cover the opening for the electrode in parallel with the inner surface of the mask plate; Wherein the center plate is corrugated over the periphery of an outer peripheral end having an interval of.
ートの前記所定の間隔に嵌合する寸法であることを特徴
とする請求項1記載の燃料電池用セパレータ。2. The fuel cell separator according to claim 1, wherein the upper and lower intervals of the waveform have dimensions that fit into the predetermined interval of the mask plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7218867A JP3072034B2 (en) | 1995-08-28 | 1995-08-28 | Fuel cell separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7218867A JP3072034B2 (en) | 1995-08-28 | 1995-08-28 | Fuel cell separator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0963601A JPH0963601A (en) | 1997-03-07 |
JP3072034B2 true JP3072034B2 (en) | 2000-07-31 |
Family
ID=16726558
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7218867A Expired - Fee Related JP3072034B2 (en) | 1995-08-28 | 1995-08-28 | Fuel cell separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3072034B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101753713B1 (en) | 2015-10-28 | 2017-07-04 | 김창식 | String working Device for Raket |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6544681B2 (en) | 2000-12-26 | 2003-04-08 | Ballard Power Systems, Inc. | Corrugated flow field plate assembly for a fuel cell |
DE10233982B4 (en) * | 2002-07-25 | 2007-08-16 | Forschungszentrum Jülich GmbH | Bipolar plate for a fuel cell and fuel cell stack |
-
1995
- 1995-08-28 JP JP7218867A patent/JP3072034B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101753713B1 (en) | 2015-10-28 | 2017-07-04 | 김창식 | String working Device for Raket |
Also Published As
Publication number | Publication date |
---|---|
JPH0963601A (en) | 1997-03-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6833210B2 (en) | Fuel cell | |
US7695845B2 (en) | Fuel cell | |
CA2705651C (en) | Fuel cell | |
JPH07109770B2 (en) | Fuel cell and fuel cell stack | |
US7531265B2 (en) | Fuel cell | |
JP2011258323A (en) | Fuel cell stack | |
JP5334469B2 (en) | Fuel cell stack | |
JP5226431B2 (en) | Fuel cell stack | |
US7569301B2 (en) | Fuel cell | |
US8153288B2 (en) | Fuel cell and fuel cell stack | |
US20050136306A1 (en) | Fuel cell | |
CN209804806U (en) | Proton exchange membrane fuel cell bipolar plate | |
JP2000260439A (en) | Stainless steel separator, spacer, polymer membrane for polymer electrolyte fuel cell and polymer electrolyte fuel cell | |
EP2860806B1 (en) | Stack structure of fuel cell | |
JPH06251790A (en) | Fuel cell | |
JP3072034B2 (en) | Fuel cell separator | |
JP2000323149A (en) | Separator for fuel cell and manufacturing device thereof | |
JP3257757B2 (en) | Fuel cell separator | |
JP2002075408A (en) | Separator for fuel cell | |
JP3072033B2 (en) | Manufacturing method of fuel cell separator | |
JP2708500B2 (en) | Stacked fuel cell | |
JP3072032B2 (en) | Fuel cell separator | |
JPS63181271A (en) | Fused carbonate fuel cell | |
KR101451838B1 (en) | Molten carbonate fuel cell and method for manufacturing of shielded slot plate thereof | |
JPH07161365A (en) | Fuel cell separator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313115 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080526 Year of fee payment: 8 |
|
S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080526 Year of fee payment: 8 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080526 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090526 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090526 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090526 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100526 Year of fee payment: 10 |
|
LAPS | Cancellation because of no payment of annual fees |