JP2743123B2 - Materials for hydrogen storage - Google Patents

Materials for hydrogen storage

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Publication number
JP2743123B2
JP2743123B2 JP3138545A JP13854591A JP2743123B2 JP 2743123 B2 JP2743123 B2 JP 2743123B2 JP 3138545 A JP3138545 A JP 3138545A JP 13854591 A JP13854591 A JP 13854591A JP 2743123 B2 JP2743123 B2 JP 2743123B2
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JP
Japan
Prior art keywords
hydrogen
hydrogen storage
pressure
amount
materials
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
Application number
JP3138545A
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Japanese (ja)
Other versions
JPH04337045A (en
Inventor
俊樹 兜森
俊男 高橋
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works Ltd
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Application filed by Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP3138545A priority Critical patent/JP2743123B2/en
Publication of JPH04337045A publication Critical patent/JPH04337045A/en
Application granted granted Critical
Publication of JP2743123B2 publication Critical patent/JP2743123B2/en
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Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】この発明は、水素と可逆的に反応
して、水素を吸蔵、放出する水素貯蔵用材料に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogen storage material that stores and releases hydrogen by reversibly reacting with hydrogen.

【0002】[0002]

【従来の技術】周知のように、水素貯蔵材料は、水素と
可逆的に反応して、反応熱の出入りを伴って水素を吸
蔵、放出する性質を有している。この化学反応を利用し
て水素を貯蔵、運搬する技術の実用化が図られており、
さらに反応熱を利用して、熱貯蔵、熱輸送システムなど
を構築する技術の開発、実用化が進められている。
2. Description of the Related Art As is well known, a hydrogen storage material has the property of reversibly reacting with hydrogen to absorb and release hydrogen with the entrance and exit of reaction heat. The technology to store and transport hydrogen using this chemical reaction has been put into practical use.
Furthermore, the technology for constructing heat storage and heat transport systems using reaction heat is being developed and put into practical use.

【0003】各種用途の実用化においては、水素貯蔵材
料の特性を一層向上させる必要があり、例えば、水素貯
蔵量の増加、原料の低廉化、プラトー特性の改善などが
大きな課題として挙げられている。従来、水素貯蔵用材
料としては、La −Ni 、Mg −Ni 、Ti −Fe 、M
m−Ni 、Ti −Cr などが開発、提唱されており、上
記した各種用途への応用、実用化が図られている。
[0003] In practical use of various applications, it is necessary to further improve the characteristics of the hydrogen storage material. For example, increasing the amount of hydrogen storage, lowering the cost of raw materials, and improving the plateau characteristics are cited as major issues. . Conventionally, materials for hydrogen storage include La-Ni, Mg-Ni, Ti-Fe, M
m-Ni, Ti-Cr and the like have been developed and proposed, and are being applied to various applications described above and put to practical use.

【0004】上記した水素貯蔵用材料のうち、Mg −N
i は、他の材料がいずれも200cc/g程度の水素吸
蔵量を示すにすぎないのに対し、400cc/g程度の
優れた水素吸蔵量を示している。しかし、水素吸蔵・放
出反応が遅く、350℃以上の温度でなければ、スムー
ズに水素の吸蔵・放出ができないなどの欠点がある。こ
のため、水素吸蔵・放出反応が速く、しかも、より低い
温度で使用可能な材料の開発が進められており、特公昭
59ー38293号では、Ti-Cr-V合金が提案されて
いる。このTi-Cr-V合金によれば、水素吸蔵・放出反
応が速く、しかも工業的な排熱として存在し得る温度範
囲で利用できるという利点がある。
Among the above hydrogen storage materials, Mg-N
i indicates an excellent hydrogen storage amount of about 400 cc / g, while the other materials only show a hydrogen storage amount of about 200 cc / g. However, the hydrogen storage / release reaction is slow, and if the temperature is not higher than 350 ° C., hydrogen storage / release cannot be performed smoothly. For this reason, the development of a material which has a fast hydrogen storage / release reaction and can be used at a lower temperature is being promoted. Japanese Patent Publication No. 59-38293 proposes a Ti-Cr-V alloy. According to the Ti-Cr-V alloy, there is an advantage that the hydrogen storage / release reaction is fast and that it can be used in a temperature range that can exist as industrial waste heat.

【0005】[0005]

【発明が解決しようとする課題】しかし、上記したTi-
Cr-V合金では、プラトーの平衡圧が常圧で150℃程
度であり、水素の吸収・放出を行なわせるためには、2
00℃程度の高い熱源を必要とする。したがって、上記
したような排熱利用では有効な材料であるが、水素の貯
蔵、輸送などの用途に使用する場合には、高温の熱源を
用意することは現実的ではなく、実用性に欠ける問題点
がある。
However, the above-mentioned Ti-
In a Cr-V alloy, the equilibrium pressure of the plateau is about 150 ° C. at normal pressure.
Requires a high heat source of about 00 ° C. Therefore, although it is an effective material for utilizing waste heat as described above, it is not practical to prepare a high-temperature heat source when it is used for applications such as storage and transportation of hydrogen, and lacks practicality. There is a point.

【0006】この発明は、上記課題を解決することを基
本的な目的とし、常温で有効に水素を吸収、放出でき、
しかも従来材に比べても優れた水素吸蔵量を示す水素貯
蔵材料を提供することを目的とするものである。
SUMMARY OF THE INVENTION The present invention has as its basic object to solve the above problems, and can effectively absorb and release hydrogen at normal temperature.
Moreover, it is an object of the present invention to provide a hydrogen storage material exhibiting an excellent hydrogen storage capacity as compared with conventional materials.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
本願発明の水素貯蔵材料は、一般式TixCr2-y-zyFe
zで表わされる組成を有することを特徴とするものであ
る。ただし、式中、x、y、zは、0.5≦x≦1.
2、0<y≦1.5、0<z≦0.5、0<y+z<
2.0である。
Means for Solving the Problems] hydrogen storage material of the present invention for solving the above-general formula Ti x Cr 2-yz V y Fe
It has a composition represented by z . However, in the formula, x, y, and z are 0.5 ≦ x ≦ 1.
2, 0 <y ≦ 1.5, 0 <z ≦ 0.5, 0 <y + z <
2.0.

【0009】[0009]

【作用】すなわち、本願発明によれば、Ti 、Cr 、
V、Fe の組成成分の作用により、プラトー平衡圧が常
圧となる温度は常温にまで低下し、常温で水素を有効に
吸収、放出させることができる。また、水素吸蔵量も増
大し、プラト−性も良好になるので水素の貯蔵・輸送効
率が向上する。
According to the present invention, Ti, Cr,
The temperature at which the plateau equilibrium pressure becomes normal pressure is reduced to normal temperature by the action of the composition components of V and Fe, and hydrogen can be effectively absorbed and released at normal temperature. In addition, the hydrogen storage amount is increased and the platability is improved, so that the efficiency of hydrogen storage / transport is improved.

【0010】ここで、Ti の組成比xを限定した理由を
述べると、xが1.2を超えると、合金中の水素の安定
性が著しく高くなり、水素の吸収、放出を行なわせるた
めに100℃以上の高い温度の熱源が必要となり実用的
でなくなる。また、xが0.5未満では、初期活性化条
件として100℃以上の温度で長時間の脱ガス処理を必
要とし、処理自体が困難になるため上記範囲に定めた。
Here, the reason why the composition ratio x of Ti is limited is as follows. When x exceeds 1.2, the stability of hydrogen in the alloy becomes remarkably high. A heat source at a high temperature of 100 ° C. or higher is required, which is not practical. When x is less than 0.5, a long-time degassing treatment at a temperature of 100 ° C. or more is required as an initial activation condition, and the treatment itself becomes difficult.

【0011】また、Vの組成比yを限定した理由を述べ
ると、Vの含有により水素吸蔵量が著しく高くなるもの
の、組成比yが1.5を超えると、Ti が上限を超えた
場合と同様に、合金中の水素の安定性が著しく高くなり
実用的ではないため、その範囲を定めた。
The reason why the composition ratio y of V is limited is as follows. Although the amount of hydrogen occlusion is remarkably increased by the inclusion of V, when the composition ratio y exceeds 1.5, the case where Ti exceeds the upper limit is considered. Similarly, the range was determined because the stability of hydrogen in the alloy was significantly increased and was not practical.

【0012】さらに、Fe の組成比zを限定した理由
は、zが0.5を超えると、水素吸蔵量が低下し、前記
したTi-Cr-V合金と同程度またはこれ以下の吸蔵能力
を有するにすぎず、十分な吸蔵量が確保できないためで
ある。なお、上記zと水素吸蔵量との関係を実証するた
めに、xを1、yを1.2に固定し、zをパラメータと
した場合の水素吸蔵量を図1に示した。図1から明らか
なように、zが0.5を超えると、Fe を含有しない場
合よりも水素吸蔵量が低下しており、過量のFe の含有
が吸蔵能力を阻害していることを示している。
Further, the reason why the composition ratio z of Fe is limited is that, when z exceeds 0.5, the hydrogen storage capacity is reduced, and the storage capacity is equal to or less than that of the above-mentioned Ti-Cr-V alloy. This is because it does not have a sufficient storage amount. In order to verify the relationship between z and the hydrogen storage amount, FIG. 1 shows the hydrogen storage amount when x is fixed to 1 and y is fixed to 1.2, and z is used as a parameter. As is apparent from FIG. 1, when z exceeds 0.5, the hydrogen storage amount is lower than that in the case where Fe is not contained, indicating that the excessive amount of Fe inhibits the storage capacity. I have.

【0013】[0013]

【実施例】以下に、この発明の実施例(発明材)を、本
発明の範囲外の比較材と比較しつつ、説明する。Ti 、
Cr 、V、Fe の各成分原料を、それぞれ秤量して、表
1に示す組成となるように配合した。この配合物を、ア
ーク式真空溶解装置のるつぼ内に収納し、高純度Ar ガ
ス雰囲気下でアーク溶解し、装置内で室温まで冷却して
凝固させた。得られた合金は、大気中で、100〜20
0メッシュに粉砕して測定試料とし、各試料5gを、高
圧法金属水素化物製造装置内のステンレス鋼製反応容器
内に封入した。
EXAMPLES Examples of the present invention (materials of the invention) will be described below in comparison with comparative materials outside the scope of the present invention. Ti,
The raw materials for each of Cr, V, and Fe were weighed and blended to have the composition shown in Table 1. This mixture was placed in a crucible of an arc vacuum melting apparatus, melted in an arc under a high purity Ar gas atmosphere, cooled to room temperature in the apparatus, and solidified. The obtained alloy is 100 to 20 in air.
The sample was pulverized to 0 mesh to obtain measurement samples, and 5 g of each sample was sealed in a stainless steel reaction vessel in a high-pressure metal hydride manufacturing apparatus.

【0014】なお、上記試料を用いて水素吸蔵・放出特
性を測定する前の処理として、活性化処理を行った。す
なわち、前記反応容器内を減圧(約10-2mmHg)排気
しながら、50℃にて約1時間加熱して脱ガスした後、
同温度で、40Kgf /cm2 圧の高純度水素を導入し、次
いで、20℃まで冷却した。このような処理によって試
料はただちに水素を吸蔵し始め、30分後には、水素の
吸蔵が完了した。さらに、容器を50℃に加熱しながら
排気して、前記試料から水素を放出させた。これらの処
理を複数回繰返して活性化処理を終了した。
Note that an activation process was performed as a process before measuring the hydrogen storage / release characteristics using the sample. That is, after degassing by heating at 50 ° C. for about 1 hour while evacuating the reaction vessel under reduced pressure (about 10 −2 mmHg),
At the same temperature, high-purity hydrogen at a pressure of 40 kgf / cm 2 was introduced, and then cooled to 20 ° C. By such treatment, the sample immediately began to absorb hydrogen, and after 30 minutes, the absorption of hydrogen was completed. Further, the vessel was evacuated while being heated to 50 ° C. to release hydrogen from the sample. These processes were repeated plural times to complete the activation process.

【0015】次に、各試料の水素吸蔵・放出特性を測定
した。すなわち、容器温度を20℃に降下させ保持した
後、容器内に高純度水素を所定量導入した。試料に水素
が吸収され容器内の圧力が安定した後、容器内の水素圧
力及び定容積法を用いて試料に吸収された水素量を求め
た。再び、所定量の水素を容器に導入し、圧力の安定
後、水素圧力及び水素吸収量を求めた。以上の操作を、
容器内の圧力が50Kgf /cm2 となるまで繰返し、水素
圧力−吸収量−等温曲線を求めた。各試料の水素圧力−
吸収量−等温曲線を測定し、50Kgf /cm2 の水素圧力
における水素吸蔵量を表1に示す。
Next, the hydrogen storage / release characteristics of each sample were measured. That is, after the vessel temperature was lowered to 20 ° C. and maintained, a predetermined amount of high-purity hydrogen was introduced into the vessel. After hydrogen was absorbed by the sample and the pressure in the container was stabilized, the amount of hydrogen absorbed in the sample was determined using the hydrogen pressure in the container and the constant volume method. Again, a predetermined amount of hydrogen was introduced into the container, and after the pressure was stabilized, the hydrogen pressure and the amount of absorbed hydrogen were determined. The above operation,
The process was repeated until the pressure in the vessel became 50 kgf / cm 2, and a hydrogen pressure-absorption amount-isothermal curve was obtained. Hydrogen pressure of each sample-
The absorption amount-isothermal curve was measured, and the hydrogen storage amount at a hydrogen pressure of 50 kgf / cm 2 is shown in Table 1.

【0016】上記のように、水素を各試料に50Kgf /
cm2の圧力まで吸蔵させた後、反応容器を前記20℃に
保持したままで、容器から所定量の水素を排出した。容
器内の水素圧力が安定した後、容器内の圧力及び定容積
法を用いて試料から放出された水素量を求めた。再び反
応容器から所定量の水素を排出した。以上の操作を、容
器内の圧力が0.2Kgf /cm2 となるまで繰返し、水素
放出過程における水素圧力−吸収量−等温曲線を求め
た。上記水素放出時の水素圧力−吸収量−等温曲線上の
プラトー中心部における曲線の傾きよりプラトー性を評
価した。具体的には、Δ(LnP)/Δ(H/M)をプ
ラトー性評価値として、表1に示した。なお、Pは水素
圧力、H/Mは試料に吸収されている水素量(水素と金
属の原子比)を示す。なお、比較材No.1およびN
o.2では、プラト−平衡圧が常圧となるのは発明材よ
りも高い温度であり、したがって、他の材料では20℃
で水素を吸蔵させたのに対し、比較材No.1およびN
o.2は水素の吸蔵を100℃で行った(活性化処理を
含む)。
As described above, hydrogen was applied to each sample at 50 kgf /
After occlusion to a pressure of cm 2, a predetermined amount of hydrogen was discharged from the vessel while the reaction vessel was kept at the aforementioned 20 ° C. After the hydrogen pressure in the container was stabilized, the amount of hydrogen released from the sample was determined using the pressure in the container and the constant volume method. A predetermined amount of hydrogen was discharged again from the reaction vessel. The above operation was repeated until the pressure in the vessel became 0.2 kgf / cm 2, and a hydrogen pressure-absorption amount-isothermal curve in a hydrogen releasing process was obtained. The plateau property was evaluated from the slope of the curve at the center of the plateau on the hydrogen pressure-absorption amount-isothermal curve at the time of hydrogen release. Specifically, Table 1 shows Δ (LnP) / Δ (H / M) as a plateau evaluation value. Note that P indicates the hydrogen pressure, and H / M indicates the amount of hydrogen (atomic ratio between hydrogen and metal) absorbed by the sample. In addition, comparative material No. 1 and N
o. In the case of No. 2, the plate-equilibrium pressure becomes normal pressure at a higher temperature than that of the inventive material, and therefore, for other materials, 20 ° C.
In comparison material no. 1 and N
o. No. 2 absorbed hydrogen at 100 ° C. (including activation treatment).

【0017】[0017]

【表1】 [Table 1]

【0018】表1から明らかなように、本発明材は、い
ずれも(No.4〜7)、水素吸蔵量が、比較材No.
1〜3よりも大幅に増加している。また、発明材のプラ
ト−性はいずれも良好であったが、比較材ではNo.3
を除いてプラト−性は劣っていた。なお、比較材No.
3は、Fe の含有によってプラト−性は良好であるもの
の過剰なFe の含有によって水素吸蔵量は大幅に低下し
ている。以上のように、発明材は、水素吸蔵量、プラト
−性のいずれの点においても優れた特性を有している。
しかも、常温(20℃)で常圧のプラト−平衡圧を示し
ており、常温における水素の吸収、放出を効率よく行う
ことができた。これに対し、比較材No.1およびN
o.2は、前述したように、プラト−平衡圧が常圧とな
る温度は常温を超えており、常温で水素を有効に吸収、
排出することは困難であった。
As is clear from Table 1, all of the materials of the present invention (Nos. 4 to 7) showed a hydrogen storage capacity of Comparative material No.
It is much larger than 1-3. In addition, the platen properties of the inventive materials were all good, but the comparative materials were no. 3
Except for, the platiness was inferior. In addition, comparative material No.
In No. 3, although the platability was good due to the inclusion of Fe, the hydrogen storage amount was greatly reduced due to the excessive Fe content. As described above, the inventive material has excellent characteristics in both the hydrogen storage capacity and the plateau property.
In addition, it exhibited a plateau-equilibrium pressure of normal pressure at normal temperature (20 ° C.), and was able to efficiently absorb and release hydrogen at normal temperature. On the other hand, the comparative material No. 1 and N
o. 2, as described above, the temperature at which the plate-equilibrium pressure becomes normal pressure exceeds normal temperature, and hydrogen is effectively absorbed at normal temperature.
It was difficult to discharge.

【0019】[0019]

【発明の効果】以上説明したように、本発明によれば、
一般式TixCr2-y-zy Fezで表わされる組成(ただ
し、式中、x、y、zは、0.5≦x≦1.2、0<y
≦1.5、0<z≦0.5、0<y+z<2.0)で水
素貯蔵用材料を構成したので、常温で水素の吸収、放出
を有効に行うことができるとともに、水素吸蔵量を増大
させることができ、また、プラト−性が改善される効果
がある。したがって、水素の貯蔵、運搬などの用途に有
効に利用できる効果がある。
As described above, according to the present invention,
Formula Ti x Cr composition represented by 2-yz V y Fe z (where in the formula, x, y, z are, 0.5 ≦ x ≦ 1.2,0 <y
≦ 1.5, 0 <z ≦ 0.5, 0 <y + z <2.0), so that hydrogen can be effectively absorbed and released at room temperature, and the hydrogen storage amount Can be increased, and there is an effect that the plateability is improved. Therefore, there is an effect that it can be effectively used for applications such as storage and transportation of hydrogen.

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

【図1】 水素吸収量に対するFe 含有量の影響を示す
グラフである。
FIG. 1 is a graph showing the effect of the Fe content on the amount of hydrogen absorbed.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一般式TixCr2-y-zy Fezで表わされ
る組成を有することを特徴とする水素貯蔵用材料ただ
し、式中、x、y、zは、0.5≦x≦1.2、0<y
≦1.5、0<z≦0.5、0<y+z<2.0
1. A general formula hydrogen storage material and having a composition represented by Ti x Cr 2-yz V y Fe z In the formula, x, y, z are, 0.5 ≦ x ≦ 1.2, 0 <y
≦ 1.5, 0 <z ≦ 0.5, 0 <y + z <2.0
JP3138545A 1991-05-15 1991-05-15 Materials for hydrogen storage Expired - Fee Related JP2743123B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3138545A JP2743123B2 (en) 1991-05-15 1991-05-15 Materials for hydrogen storage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3138545A JP2743123B2 (en) 1991-05-15 1991-05-15 Materials for hydrogen storage

Publications (2)

Publication Number Publication Date
JPH04337045A JPH04337045A (en) 1992-11-25
JP2743123B2 true JP2743123B2 (en) 1998-04-22

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Country Status (1)

Country Link
JP (1) JP2743123B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3626298B2 (en) * 1996-10-03 2005-03-02 トヨタ自動車株式会社 Hydrogen storage alloy and manufacturing method
JPH11310844A (en) 1998-04-30 1999-11-09 Toyota Motor Corp Hydrogen storage alloy and hydrogen storage alloy electrode
JP3528599B2 (en) * 1998-05-21 2004-05-17 トヨタ自動車株式会社 Hydrogen storage alloy
US7108757B2 (en) * 2003-08-08 2006-09-19 Ovonic Hydrogen Systems Llc Hydrogen storage alloys providing for the reversible storage of hydrogen at low temperatures
KR100846235B1 (en) * 2007-01-10 2008-07-15 한국지질자원연구원 Ti-cr-v-fe hydrogen storage alloy

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5938293B2 (en) * 1982-06-09 1984-09-14 工業技術院長 Titanium-chromium-vanadium hydrogen storage alloy
JPS62151540A (en) * 1985-12-25 1987-07-06 Japan Steel Works Ltd:The Titanium-chromium-iron metallic alloy for hydrogen storage

Also Published As

Publication number Publication date
JPH04337045A (en) 1992-11-25

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