JP3028578B2 - Battery storage method for lead-acid batteries - Google Patents

Battery storage method for lead-acid batteries

Info

Publication number
JP3028578B2
JP3028578B2 JP02260973A JP26097390A JP3028578B2 JP 3028578 B2 JP3028578 B2 JP 3028578B2 JP 02260973 A JP02260973 A JP 02260973A JP 26097390 A JP26097390 A JP 26097390A JP 3028578 B2 JP3028578 B2 JP 3028578B2
Authority
JP
Japan
Prior art keywords
battery
formation
lead
specific gravity
sulfuric acid
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 - Lifetime
Application number
JP02260973A
Other languages
Japanese (ja)
Other versions
JPH04138666A (en
Inventor
和吉 米津
勝弘 高橋
博 安田
直人 星原
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP02260973A priority Critical patent/JP3028578B2/en
Publication of JPH04138666A publication Critical patent/JPH04138666A/en
Application granted granted Critical
Publication of JP3028578B2 publication Critical patent/JP3028578B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • Y02E60/10Energy storage using batteries

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は鉛蓄電池の電槽化成方法に関するものであ
り、特に正極板活物質に用いるペースト中に鉛丹を混合
した鉛蓄電池の電槽化成方法に関するものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for forming a battery case of a lead-acid battery, and more particularly to a method of forming a battery case for a lead-acid battery in which lead is mixed in a paste used for a positive electrode plate active material. Things.

従来の技術 鉛蓄電池の電槽化成方法には、電槽化成前に比重1.18
0以上の希硫酸を注液し、化成中の電気分解による電解
液の濃縮や極板中より生成する硫酸量を考慮して、その
注液量を定め電槽化成を行い、電槽化成終了後の電解液
比重が任意の比重となるようにする方法がある。また電
槽化成の電気量を合理化するために、1.150以下の低比
重の希硫酸を電槽化成前に注液し、電槽化成終了後に化
成電解液を脱液し、その後1.450以上の高比重の硫酸を
加え、100〜400Aの大電流にて再充電し、短時間の内に
電池内部の電解液を撹拌して、任意の電解液比重に調整
する方法もある。尚、現在は後者の方法が主流として多
く用いられている。
Prior art The battery formation method for lead-acid batteries requires a specific gravity of 1.18 before battery formation.
Inject 0 or more diluted sulfuric acid, consider the concentration of electrolyte by electrolysis during chemical formation and the amount of sulfuric acid generated from the electrode plate, determine the amount of solution to be injected, perform battery forming, and complete battery forming. There is a method in which the specific gravity of the subsequent electrolytic solution becomes an arbitrary specific gravity. Also, in order to rationalize the amount of electricity in the battery case formation, dilute sulfuric acid with a low specific gravity of 1.150 or less is injected before the formation of the battery case, and after the formation of the battery case, the chemical electrolyte is drained. Of sulfuric acid, and recharging with a large current of 100 to 400 A, stirring the electrolyte inside the battery within a short time to adjust the specific gravity of the electrolyte to an arbitrary value. At the present time, the latter method is mainly used.

発明が解決しようとする課題 正極活物質に用いるペーストに鉛丹を混合した鉛蓄電
池においては、その鉛丹の作用により理論的に電槽化成
時の電気量を大幅に削減できる。そしてその効果を最大
限活用するためには、上記の電槽化成前に注液する希硫
酸の比重を低比重とし、電槽化成終了後脱液して高比重
の硫酸を加え、大電流にて撹拌する方法が有効である。
しかし活物質中に鉛丹を混合した正極板は格子と活物質
の結合力が弱いため、大電流で充電する際の電気分解で
のガス発生により活物質が格子から剥離し、電池の寿命
が著しく低下するという大きな課題があった。そのため
正極活物質中に鉛丹を混合した鉛蓄電池においては、電
槽化成前に注液する希硫酸の比重を低比重として、電槽
化成終了後高比重の硫酸を注液して大電流にて撹拌する
という電槽化成方法は、いまだ実用には至っていない。
Problems to be Solved by the Invention In a lead storage battery in which lead paste is mixed into a paste used for a positive electrode active material, the amount of electricity during battery formation can be reduced theoretically by the action of lead lead. In order to maximize the effect, the specific gravity of the diluted sulfuric acid injected before the formation of the above-mentioned battery tank was set to a low specific gravity. The method of stirring with water is effective.
However, since the positive electrode plate in which the lead material is mixed in the active material has a weak binding force between the grid and the active material, the active material peels off from the grid due to gas generation during electrolysis when charged with a large current, and the battery life is shortened. There was a major problem that it was significantly reduced. Therefore, in a lead-acid battery in which lead red is mixed in the positive electrode active material, the specific gravity of dilute sulfuric acid injected before battery formation is set to low specific gravity, and high specific gravity sulfuric acid is injected after battery formation to increase the current. The battery case formation method of stirring with water has not yet been put to practical use.

課題を解決するための手段 本発明はこのような正極活物質中に鉛丹を混合した鉛
蓄電池の電槽化成方法として、前記の方法を用いた場合
の大電流での撹拌時に、正極活物質が格子から剥離する
という大きな課題を改善するものである。その具体的な
手段として、電槽化成前に注液する希硫酸の比重を1.15
0以上1.180以下とし、電槽化成終了後に電池を反転脱液
した後、比重1.290以上1.400以下の硫酸を加え、その後
50A以上80A以下の電流にて再充電し、電気分解によるガ
ス発生によって、脱液後の電池内部に残存する低濃度電
解液と脱液後に加えた高濃度硫酸とを撹拌して、任意の
電解液比重とする電槽化成方法である。さらに電槽化成
前に希硫酸を注液した後、5分以上120分以下、好まし
くは30分以上120分以下の期間放置をした後、電槽化成
を開始することを特徴とするものである。
Means for Solving the Problems The present invention is a method for forming a battery of a lead-acid battery in which lead-acid is mixed in such a positive electrode active material, when stirring at a large current when using the above method, the positive electrode active material Is to improve the big problem of peeling off from the lattice. As a specific means, the specific gravity of the diluted sulfuric acid injected before the formation of the battery tank is 1.15.
0 to 1.180 or less, and after inversion of the battery after inversion of the battery tank, sulfuric acid having a specific gravity of 1.290 to 1.400 was added, and then
The battery is recharged at a current of 50A or more and 80A or less, and by gas generation by electrolysis, the low-concentration electrolytic solution remaining inside the battery after dewatering and the high-concentration sulfuric acid added after dewatering are agitated, and any electrolytic This is a battery case formation method with a liquid specific gravity. Further, after injecting dilute sulfuric acid before forming the battery case, after leaving for a period of 5 minutes or more and 120 minutes or less, preferably 30 minutes or more and 120 minutes or less, the battery case formation is started. .

作用 つまり従来の電槽化成での電槽化成前に注液する比重
は1.150以下と非常に低比重であるため、電槽化成終了
後の電解液比重も極端に低くなる。従って電槽化成終了
後脱液を行っても電池内部には極板中などにかなり電解
液が残存するため、任意の電解液比重とするには脱液後
加える硫酸の比重を1.450以上と高くする必要がある。
このため電池内部に残存する低比重電解液と、脱液後加
えた高比重の硫酸とを短時間で再充電によって撹拌しよ
うとする場合、100A以上から400A程度の大電流充電を必
要とする。そしてこのような大電流で充電した場合の電
気分解は非常に活発となり、それに伴うガス発生量も著
しく激しいものとなる。これにより活物質中に鉛丹を混
合した正極板は格子と活物質との結合力が低下している
ため、その激しいガス発生によって格子と活物質が剥離
し、電池の寿命が低下することとなる。
Action In other words, the specific gravity of the liquid injected before the battery formation in the conventional battery case formation is very low at 1.150 or less, so that the specific gravity of the electrolyte after the battery formation is extremely low. Therefore, even if dewatering is performed after the formation of the battery tank, a considerable amount of electrolyte remains inside the battery, such as in the electrode plate, so that the specific gravity of sulfuric acid added after dewatering should be as high as 1.450 or more in order to obtain an arbitrary electrolyte specific gravity. There is a need to.
For this reason, when trying to stir the low specific gravity electrolytic solution remaining inside the battery and the high specific gravity sulfuric acid added after the liquid removal by recharging in a short time, a large current charging of about 100 A or more to about 400 A is required. Electrolysis when charged with such a large current becomes very active, and the amount of gas generated thereby becomes extremely intense. As a result, the binding force between the grid and the active material is reduced in the positive electrode plate in which the lead material is mixed in the active material, and the vigorous gas generation causes the grid and the active material to peel off, shortening the battery life. Become.

これに対して本発明は、種々の試験により電槽化成前
に注液する希硫酸の比重として、電槽化成の電気量を合
理化するのに支障のない範囲を検討し、その結果、従来
用いられていない1.150以上で1.180以下の範囲であれば
問題のないことを発見した。これにより、電槽化成終了
後の電解液比重を高くすることができ、そのため脱液後
加える硫酸の比重も大幅に低くすることが可能となり、
1.290以上1.400以下で対応が可能となった。
On the other hand, the present invention examines a range that does not hinder the rationalization of the amount of electricity of the battery formation as a specific gravity of the diluted sulfuric acid injected before the battery formation by various tests. It was found that there is no problem if the range is 1.150 or more and 1.180 or less. As a result, the specific gravity of the electrolytic solution after the formation of the battery container can be increased, so that the specific gravity of the sulfuric acid added after the dewatering can be significantly reduced.
It became possible to respond from 1.290 to 1.400.

従って撹拌に必要な電気分解によるガス発生も少なく
することができ、そのため再充電時の電流も50A以上で
行えば充分撹拌ができることとなった。これらにより撹
拌の際の再充電時のガス発生による格子と活物質の剥離
を防止することができ、電池の寿命特性を低下させるこ
となく電槽化成電気量の合理化を図ることができるよう
になった。
Therefore, gas generation due to electrolysis required for stirring can be reduced, so that sufficient stirring can be performed if the current at the time of recharging is also 50 A or more. Thus, it is possible to prevent separation of the grid and the active material due to gas generation at the time of recharging at the time of stirring, and it is possible to rationalize the amount of battery formation electricity without lowering the life characteristics of the battery. Was.

またさらに本発明では電槽化成前に希硫酸を注液後、
5分以上120分以下で、好ましくは30分以上120分以下の
放置を行った後電槽化成を開始することにより、希硫酸
中の硫酸分と極板中の活物質とが反応して電解液濃度が
極めて低くなり、電槽化成の初期段階においてα−PbO2
が格子と活物質の界面で生成することとなる。このα−
PbO2は導電性は高いが反応性には乏しいため、格子と活
物質との結合力を高めさらに長期にわたってその高結合
力を維持することができる。これにより、撹拌時のガス
発生による格子と活物質の剥離という課題に対してさら
に改善することが可能となり、電池の寿命特性もより向
上させることができた。
Further, in the present invention, after dilute sulfuric acid is injected before forming the battery case,
After leaving the battery for 5 minutes to 120 minutes, preferably 30 minutes to 120 minutes, and then starting the battery formation, the sulfuric acid in the diluted sulfuric acid reacts with the active material in the electrode plate to cause electrolysis. The liquid concentration becomes extremely low, and α-PbO 2
Are generated at the interface between the lattice and the active material. This α-
Since PbO 2 has high conductivity but poor reactivity, it can increase the bonding force between the lattice and the active material and maintain the high bonding force for a long period of time. As a result, it was possible to further improve the problem of separation of the grid and the active material due to gas generation during stirring, and it was possible to further improve the life characteristics of the battery.

実施例 以下、本発明の実施例について述べる。Examples Hereinafter, examples of the present invention will be described.

まずペースト活物質中に鉛丹を40%混合した正極板を
用いて5HR容量で12V48Ahの電池を作製し、次いでこの電
池を表−1に示す種々の希硫酸を用いて電槽化成前に注
液し、10Aの電流で16Hの充電を施し電槽化成を行った。
その後電池より正極板を取り出し、活物質中のPbO2の定
量分析をした結果を第1図に示す。
First, a 12V48Ah battery with a capacity of 5 HR was prepared using a positive electrode plate containing 40% of lead red in the paste active material, and then this battery was injected with various dilute sulfuric acids shown in Table 1 before battery formation. The mixture was liquefied and charged for 16H with a current of 10A to form a battery case.
Thereafter, the positive electrode plate was taken out of the battery, and the result of quantitative analysis of PbO 2 in the active material is shown in FIG.

第1図より明らかなように、電槽化成前の注液比重が
従来低比重の上限として用いてきた1.150以上であって
も1.180以下であれば、電槽化成後のPbO2生成量はほと
んど差がなく、電槽化成の効率が同じなのが判る。また
その注液する希硫酸の比重が1.180を超え1.190になると
PbO2の生成量が少なくなり、電槽化成の効率が低下して
いるのも判る。次に電槽化成前に注液する希硫酸の比重
を1.180とし、表−2に示す注液後の放置時間別と電槽
化成終了後の撹拌時の電流別による各種条件にて電槽化
成を完了した後、格子と活物質との剥離状態など、寿命
への影響を調べるためサイクル試験を行った。その条件
は放電を9.6Aにて電池の端子電圧が10.5Vまで低下する
まで行い、充電は14.6Aにて放電容量の120%とし、放電
時の容量が5HR容量の50%となった時点を寿命とした。
その結果を表−3に示す。尚、電槽化成時の電流と時間
はいずれも10Aにて16Hとした。
As is evident from FIG. 1, the amount of PbO 2 generated after the formation of the battery is almost constant if the specific gravity of the liquid before the formation of the battery is 1.150 or less, even if the specific gravity of the injected solution is 1.150 or more, which has been conventionally used as the upper limit of the low specific gravity. It can be seen that there is no difference and the efficiency of battery case formation is the same. When the specific gravity of the diluted sulfuric acid to be injected exceeds 1.180 and becomes 1.190
It can also be seen that the production amount of PbO 2 has decreased, and the efficiency of battery formation has decreased. Next, the specific gravity of the diluted sulfuric acid to be injected before the formation of the battery was 1.180, and the battery was formed under various conditions according to the standing time after the injection and the current at the time of stirring after the completion of the formation of the battery as shown in Table-2. After completing the above, a cycle test was performed to examine the influence on the life, such as the state of separation between the lattice and the active material. The conditions are as follows: Discharge at 9.6 A until the terminal voltage of the battery drops to 10.5 V, charge at 120 A of the discharge capacity at 14.6 A, and the time when the capacity at the time of discharge becomes 50% of the 5HR capacity. Life time.
Table 3 shows the results. In addition, the current and the time at the time of battery case formation were both 16 A at 10 A.

表−3の結果より、注液後の放置時間が3分で撹拌電
流が100AのEと80AのFでは明らかにFの方がサイクル
数が多くなっており、試験後の分解した結果においても
Eは格子と活物質との剥離が著しく、撹拌電流の影響が
明確となっている。又撹拌電流が同じ80Aで注液後の放
置時間が3分のFと5分のGとでは、Gの方がサイクル
数が多くなっており、注液後の放置時間を5分以上とす
ることにより寿命が長くなることが判る。次にその放電
時間を30分以上としたHとIではFよりもさらにサイク
ルが伸びており、放置時間は30分以上とした方が好まし
いのが判る。尚注液後の放置時間としては、120分を超
えると放置時間中に活物質が安定した硫酸鉛となり、化
成効率を低下させるので120分までとすることが望まし
い。
From the results in Table-3, it is clear that the number of cycles in E of 100 A and F of 80 A in the stirring time is 3 minutes and the number of cycles in F is clearly larger than that in the decomposition after the test. In E, the separation between the lattice and the active material is remarkable, and the influence of the stirring current is clear. In addition, when the stirring current is the same at 80 A and the leaving time after injection is 3 minutes F and 5 minutes G, G has a larger number of cycles, and the leaving time after injection is 5 minutes or more. This shows that the life is prolonged. Next, it can be seen that the cycle is further extended in H and I where the discharge time is 30 minutes or more than in F, and it is preferable that the leaving time is 30 minutes or more. It is desirable that the standing time after the pouring is up to 120 minutes, since if it exceeds 120 minutes, the active material becomes stable lead sulfate during the standing time and the conversion efficiency is lowered.

発明の効果 以上のように本発明によれば、従来の正極活物質中に
鉛丹を混合した鉛蓄電池において、電槽化成前に注液す
る希硫酸の比重を低比重として、化成終了後に高比重の
硫酸を加え大電流にて撹拌充電するという電槽化成方法
での大きな課題であった、格子と活物質との剥離という
問題を解決し、電池の寿命特性を向上させるとともに電
槽化成の効率化を図るものである。
Effects of the Invention As described above, according to the present invention, in a conventional lead-acid battery in which lead tin is mixed in a positive electrode active material, the specific gravity of dilute sulfuric acid injected before battery formation is set to a low specific gravity, and the specific gravity is increased after the formation. It solves a major problem with the battery case formation method of adding specific sulfuric acid and stirring and charging with a large current, the problem of separation between the grid and the active material, improving the battery life characteristics and improving the battery case formation. It is intended to improve efficiency.

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

第1図は電槽化成前に注液する希硫酸の比重別による、
化成後の正極活物質中のPbO2生成量を示す図である。
Fig. 1 shows the specific gravity of dilute sulfuric acid injected before battery formation.
FIG. 3 is a view showing the amount of PbO 2 generated in a positive electrode active material after chemical formation.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 星原 直人 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 昭52−118223(JP,A) 特開 昭62−93857(JP,A) 特開 昭62−93858(JP,A) 特開 昭63−13263(JP,A) 特公 昭39−9923(JP,B1) (58)調査した分野(Int.Cl.7,DB名) H01M 4/22 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Naoto Hoshihara 1006 Oaza Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-52-118223 (JP, A) 93857 (JP, A) JP-A-62-93858 (JP, A) JP-A-63-13263 (JP, A) JP-B-39-9923 (JP, B1) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 4/22

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】鉛丹を混合したペーストを正極活物質とし
て用いた鉛蓄電池の電槽化成方法において、電槽化成前
に注液する希硫酸の比重を1.150以上1.180以下とし、電
槽化成終了後に電池を反転して脱液した後比重1.290以
上1.400以下の硫酸を加え、その後50A以上80A以下の電
流にて再充電し、電気分解によるガス発生によって、脱
液後に電池内部に残存する低濃度電解液と脱液後に加え
た高濃度硫酸とを撹拌して、任意の電解液比重とする鉛
蓄電池の電槽化成方法。
In a method for forming a battery of a lead-acid battery using a paste containing mixed lead as a positive electrode active material, the specific gravity of dilute sulfuric acid injected before the formation of the battery is set to 1.150 or more and 1.180 or less. After the battery is inverted and drained, sulfuric acid with a specific gravity of 1.290 to 1.400 is added, and then recharged with a current of 50 A to 80 A, and the low concentration remaining inside the battery after the liquid is removed due to gas generation by electrolysis. A method for forming a battery case of a lead-acid battery by stirring an electrolytic solution and high-concentration sulfuric acid added after the liquid removal to obtain an arbitrary specific gravity of the electrolytic solution.
【請求項2】電槽化成前に希硫酸を注液後、5分以上12
0分以下の期間放置を行った後、電槽化成を開始する特
許請求の範囲第1項に記載の鉛蓄電池の電槽化成方法。
2. After the diluted sulfuric acid is injected before the formation of the battery tank, it is required
2. The battery case forming method for a lead-acid storage battery according to claim 1, wherein the battery case formation is started after leaving for a period of 0 minute or less.
JP02260973A 1990-09-28 1990-09-28 Battery storage method for lead-acid batteries Expired - Lifetime JP3028578B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02260973A JP3028578B2 (en) 1990-09-28 1990-09-28 Battery storage method for lead-acid batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02260973A JP3028578B2 (en) 1990-09-28 1990-09-28 Battery storage method for lead-acid batteries

Publications (2)

Publication Number Publication Date
JPH04138666A JPH04138666A (en) 1992-05-13
JP3028578B2 true JP3028578B2 (en) 2000-04-04

Family

ID=17355324

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02260973A Expired - Lifetime JP3028578B2 (en) 1990-09-28 1990-09-28 Battery storage method for lead-acid batteries

Country Status (1)

Country Link
JP (1) JP3028578B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107611498B (en) * 2017-09-13 2020-07-17 淄博火炬能源有限责任公司 Acid circulation rapid formation method for power battery

Also Published As

Publication number Publication date
JPH04138666A (en) 1992-05-13

Similar Documents

Publication Publication Date Title
CN105206830B (en) A kind of deeper cavity lead-acid battery cathode lead plaster and preparation method
CN112510182B (en) Lead paste for lead-acid storage battery and lead-acid storage battery
EP0120128A1 (en) Forming of tetrabasic lead sulfate battery electrodes
JP3028578B2 (en) Battery storage method for lead-acid batteries
JPH10144305A (en) Negative pole plate of lead acid battery
US3733220A (en) Water activated lead-acid battery having dried,discharged electrodes
JP4178442B2 (en) Control valve type lead acid battery manufacturing method
JP2982368B2 (en) Battery storage method for lead-acid batteries
JPS58197662A (en) Pasted positive electrode for lead storage battery
JP2007035496A (en) Chemical formation method of lead-acid storage battery container
JP2006114314A (en) Manufacturing method of lead acid storage battery
JPH0234758Y2 (en)
JPS6136347B2 (en)
JPH0234757Y2 (en)
JPS63187566A (en) Manufacture of lead acid battery
JPS59148282A (en) Manufacturing method for sealed type lead storage battery
JPH0351890Y2 (en)
JPS59138063A (en) Lead storage battery
JPH05325950A (en) Manufacture of lead-acid battery of negative electrode absorbing sealed type
JP3614440B6 (en) High energy battery electrolyte and method for producing the electrolyte
JP3614440B2 (en) High energy battery electrolyte and method for producing the electrolyte
JPH0550813B2 (en)
JPH053709B2 (en)
Skołuda et al. The influence of different factors on the kinetics of potentiostatic forming of pasted positive lead electrodes
JPH04155760A (en) Battery jar formation of lead-acid battery

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080204

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090204

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100204

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100204

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110204

Year of fee payment: 11

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110204

Year of fee payment: 11