JPH06247708A - Purifying method of hydrosilicofluoric acid - Google Patents
Purifying method of hydrosilicofluoric acidInfo
- Publication number
- JPH06247708A JPH06247708A JP5499893A JP5499893A JPH06247708A JP H06247708 A JPH06247708 A JP H06247708A JP 5499893 A JP5499893 A JP 5499893A JP 5499893 A JP5499893 A JP 5499893A JP H06247708 A JPH06247708 A JP H06247708A
- Authority
- JP
- Japan
- Prior art keywords
- compounds
- hydrosilicofluoric acid
- impurities
- acid
- liter
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/08—Compounds containing halogen
- C01B33/107—Halogenated silanes
- C01B33/10778—Purification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
(57)【要約】
【構成】ケイフッ化水素酸(フッ化水素 7.8 モル/リ
ットル、四フッ化ケイ素 3.9モル/リットル)100 kg
に酸化剤である過マンガン酸カリウムを攪拌しながら液
色が淡紫色になるまで投入し、その液をフッ素樹脂製の
蒸留装置に導入して加熱蒸留を行い、その水溶液中に含
有される硫黄化合物、燐化合物、硼素化合物及び砒素化
合物を酸化除去する。
【効果】従来の蒸留法だけでは精製が困難であった不純
物を、超微量濃度まで除去できる。(57) [Summary] [Structure] 100 kg of hydrosilicofluoric acid (hydrogen fluoride 7.8 mol / liter, silicon tetrafluoride 3.9 mol / liter)
While stirring potassium permanganate, which is an oxidizer, is added until the liquid color becomes pale purple, the liquid is introduced into a distillation apparatus made of fluororesin and heated and distilled, and the sulfur contained in the aqueous solution is added. Compounds, phosphorus compounds, boron compounds and arsenic compounds are oxidized and removed. [Effect] It is possible to remove impurities, which have been difficult to purify only by the conventional distillation method, to an ultratrace amount.
Description
【0001】[0001]
【産業上の利用分野】本発明は、ケイフッ化水素酸の精
製方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying hydrosilicofluoric acid.
【0002】[0002]
【従来の技術】従来、ケイフッ化水素酸中において、基
板に二酸化ケイ素を堆積する技術が知られている(例え
ば、特開昭57−196744号、同61−12034
号、同61−28104号、同62−20876号、特
開平1−36770号)。2. Description of the Related Art Conventionally, a technique of depositing silicon dioxide on a substrate in hydrosilicofluoric acid is known (for example, JP-A-57-196744 and 61-12034).
No. 61-28104, No. 62-20876, and JP-A No. 1-367770).
【0003】この技術は、光ディスク、液晶ガラス基板
の二酸化ケイ素コーティングや半導体素子の絶縁膜の成
膜に利用されている。そして、上記のような分野で使用
される薬品は、きわめて高い純度の薬液が要求される。
特に、半導体素子製造プロセスでは、硫黄化合物、燐化
合物、硼素化合物及び砒素化合物等の不純物の混入をき
わめて嫌うため、高純度のケイフッ化水素酸の供給への
希望が増大している。また、市販されているケイフッ化
水素酸は通常の半導体用薬品(例えば、フッ化水素酸、
過酸化水素水等)に比べ多量の不純物を含んでおり、上
記の利用分野で使用するには不純物の含有量の点で問題
がある。This technique is used for coating silicon dioxide on optical disks and liquid crystal glass substrates and for forming insulating films on semiconductor elements. The chemicals used in the above fields are required to have extremely high purity.
In particular, in the semiconductor device manufacturing process, since impurities such as sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds are extremely disliked, there is an increasing demand for supplying high-purity hydrosilicofluoric acid. Further, commercially available hydrosilicofluoric acid is an ordinary semiconductor chemical (for example, hydrofluoric acid,
It contains a large amount of impurities as compared with hydrogen peroxide water, etc., and there is a problem in terms of the content of impurities for use in the above application fields.
【0004】そのような状況の中で、工業的にケイフッ
化水素酸を精製する方法の確立が望まれ、高純度のケイ
フッ化水素酸供給の必要性が高まっている。Under such circumstances, it is desired to industrially establish a method for purifying hydrosilicofluoric acid, and the necessity of supplying high-purity hydrosilicofluoric acid is increasing.
【0005】このケイフッ化水素酸は100〜140℃
程度に加熱することによって四フッ化ケイ素、フッ化水
素及び水に分解しガス化するため、従来、蒸留すること
によって不純物をある程度除去できることが知られてい
る(特公昭43−17412号公報参照)。This hydrosilicofluoric acid has a temperature of 100 to 140 ° C.
Since it is decomposed into silicon tetrafluoride, hydrogen fluoride and water by heating to a certain degree and gasified, it is conventionally known that impurities can be removed to some extent by distillation (see Japanese Patent Publication No. 43-17412). .
【0006】[0006]
【発明が解決しようとする課題】しかしながら、ケイフ
ッ化水素酸を精製する場合、高沸点の金属不純物に関し
ては前記の方法でppbレベルといわれる半導体用薬品
のグレードまで精製できるが、硫黄化合物、燐化合物、
硼素化合物及び砒素化合物等の不純物に関しては、それ
らの不純物自体が各種の沸点をもつ化合物が存在するの
に加え、ケイフッ化水素酸中ではフッ素と反応し、かな
りの種類の沸点をもつフッ素化合物を生成する可能性が
あるために、蒸留だけでこれらの不純物をppbレベル
まで精製することは、蒸留塔の段数を多くすること等の
装置的な工夫だけでは、非常に困難であるという問題が
ある。However, in the case of refining hydrosilicofluoric acid, high-boiling metal impurities can be purified to the ppb level, which is a chemical grade for semiconductors, by the above-mentioned method. ,
Regarding impurities such as boron compounds and arsenic compounds, in addition to the compounds having various boiling points, the impurities themselves react with fluorine in hydrosilicofluoric acid to form fluorine compounds having considerable boiling points. There is a problem that it is very difficult to purify these impurities to the ppb level only by distillation because they are likely to be generated only by devising the device such as increasing the number of stages of the distillation column. .
【0007】[0007]
【課題を解決するための手段】本発明者らは鋭意研究の
結果、上記問題点を解決するため、ケイフッ化水素酸に
過マンガン酸カリウム等の酸化剤を添加し、加熱蒸留す
ることによって硫黄化合物、燐化合物、硼素化合物及び
砒素化合物等の不純物が超微量まで除去できることを見
い出し、本発明を完成するに至った。As a result of earnest studies, the present inventors have found that, in order to solve the above problems, sulfur is obtained by adding an oxidizing agent such as potassium permanganate to hydrosilicofluoric acid and subjecting it to heat distillation. It has been found that impurities such as compounds, phosphorus compounds, boron compounds and arsenic compounds can be removed in an extremely small amount, and the present invention has been completed.
【0008】すなわち、本発明は、ケイフッ化水素酸を
精製するに当って、フッ化水素に対して0.3 〜1.3 倍モ
ル数の四フッ化ケイ素を含有し、その両者が20〜65重量
パーセントである水溶液に、過マンガン酸カリウム等の
酸化剤を添加し、加熱蒸留して、その水溶液に含有され
る硫黄化合物、燐化合物、硼素化合物及び砒素化合物を
酸化除去するようにしたものである。That is, according to the present invention, in purifying hydrosilicofluoric acid, 0.3 to 1.3 times the molar number of silicon tetrafluoride is contained with respect to hydrogen fluoride, both of which are 20 to 65 weight percent. An oxidizing agent such as potassium permanganate is added to a certain aqueous solution and heated and distilled to oxidize and remove sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds contained in the aqueous solution.
【0009】本発明の趣旨は、ケイフッ化水素酸を精製
するに当って、フッ化水素と四フッ化ケイ素を含有する
水溶液に酸化剤を添加し、加熱蒸留することによって、
前記した蒸留法だけでは精製が困難であった不純物を、
超微量濃度まで除去することにある。The object of the present invention is to purify hydrosilicofluoric acid by adding an oxidizing agent to an aqueous solution containing hydrogen fluoride and silicon tetrafluoride, and heating and distilling the solution.
Impurities that were difficult to purify by the above-mentioned distillation method alone,
It is to remove to a very small amount.
【0010】本発明で使用し得る酸化剤は過マンガン酸
カリウムだけでなく、ケイフッ化水素酸中の硫黄化合
物、燐化合物、硼素化合物及び砒素化合物等の不純物に
対して酸化作用を示すものであればよい。例えば、重ク
ロム酸カリウム、過硫酸カリウム、過酸化水素、フッ素
ガス、塩素ガス及びオゾン等も使用可能である。また、
その添加方法は蒸留する前にケイフッ化水素酸の液中に
添加しても、また、蒸留時に蒸留缶あるいは蒸留塔に投
入してもよい。The oxidizing agent which can be used in the present invention is not limited to potassium permanganate, but may be one which has an oxidizing action on impurities such as sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds in hydrosilicofluoric acid. Good. For example, potassium dichromate, potassium persulfate, hydrogen peroxide, fluorine gas, chlorine gas, ozone and the like can be used. Also,
The addition method may be such that it is added to the liquid of hydrosilicofluoric acid before distillation, or it may be added to a distillation can or a distillation column at the time of distillation.
【0011】[0011]
【作用】前記した蒸留法だけでは精製が困難であった不
純物を本発明により精製することができるのは、次のこ
とによると推測される。 1 硫黄化合物、燐化合物、硼素化合物及び砒素化合物
等の不純物が酸化剤によって酸化され、その結果生成し
た化合物の沸点がケイフッ化水素酸の沸点に対して著し
く高い方へシフトするか、逆に低い方へシフトすること
によって、蒸留による分離を容易にする。 2 ケイフッ化水素酸中の硫黄化合物、燐化合物、硼素
化合物及び砒素化合物等の不純物が酸化剤によって酸化
分解され、その結果生成した化合物の沸点がケイフッ化
水素酸の沸点に対して著しく高い方へシフトするか、逆
に低い方へシフトすることによって、蒸留による分離を
容易にする。It is presumed that the impurities which were difficult to purify by the above-mentioned distillation method can be purified by the present invention as follows. 1 Impurities such as sulfur compounds, phosphorus compounds, boron compounds, and arsenic compounds are oxidized by an oxidant, and the boiling point of the resulting compound shifts to a remarkably higher side than the boiling point of hydrosilicofluoric acid, or conversely low. The shift to the side facilitates separation by distillation. 2 Impurities such as sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds in hydrosilicofluoric acid are oxidatively decomposed by an oxidant, and the boiling point of the resulting compound is significantly higher than that of hydrosilicofluoric acid. Shifting or vice versa facilitates separation by distillation.
【0012】しかし、この酸化剤と加熱蒸留による精製
法の効果は、実用上充分満足し得るものであって、多数
の実験によって確認されたものである。しかも、本発明
による精製法は、粗製ケイフッ化水素酸がフッ化水素に
対して0.3 〜1.3 倍モル数の四フッ化ケイ素を含有し、
その両者が20〜65重量パーセントである水溶液のように
広範囲な濃度領域で効果が発揮される。However, the effect of this oxidizing method and the refining method by heat distillation is practically sufficiently satisfactory, and has been confirmed by many experiments. Moreover, the purification method according to the present invention is such that the crude hydrosilicofluoric acid contains 0.3 to 1.3 times the molar number of silicon tetrafluoride with respect to hydrogen fluoride,
The effect is exhibited in a wide concentration range such as an aqueous solution in which both are 20 to 65% by weight.
【0013】[0013]
【実施例】以下、実施例をもって、本発明の効果を説明
するが、本発明の方法はこの実施例のみに限定されるも
のではない。EXAMPLES The effects of the present invention will be described below with reference to examples, but the method of the present invention is not limited to these examples.
【0014】実施例1 表1に示す不純物を含む原料ケイフッ化水素酸(フッ化
水素 7.8 モル/リットル、四フッ化ケイ素 3.9 モル
/リットル)100 kgに過マンガン酸カリウムを攪拌しな
がら液色が淡紫色を示すまで投入した。その液をフッ素
樹脂製の蒸留装置に導入し、加熱蒸留を行ってケイフッ
化水素酸を精製し、精製ケイフッ化水素酸80kgを得た。
そして、精製したケイフッ化水素酸中の不純物含有量を
ICP-MS法及びICP-AES 法で調べて表1に示す結果を得
た。Example 1 100 kg of a raw material hydrosilicofluoric acid (hydrogen fluoride 7.8 mol / liter, silicon tetrafluoride 3.9 mol / liter) containing impurities shown in Table 1 was mixed with potassium permanganate to obtain a liquid color. It was charged until it showed a light purple color. The liquid was introduced into a distillation apparatus made of fluororesin, and heated and distilled to purify hydrosilicofluoric acid to obtain 80 kg of purified hydrofluorosilicic acid.
Then, the content of impurities in the purified hydrofluorosilicic acid
The results shown in Table 1 were obtained by the ICP-MS method and the ICP-AES method.
【0015】[0015]
【表1】 [Table 1]
【0016】実施例2 表2に示す不純物を含む原料ケイフッ化水素酸(フッ化
水素 3.3 モル/リットル、四フッ化ケイ素 3.9 モル
/リットル)200 kgに過マンガン酸カリウムを攪拌しな
がら液色が淡紫色を示すまで投入した。その液をフッ素
樹脂製の蒸留装置に導入し、加熱蒸留を行ってケイフッ
化水素酸を精製し、精製ケイフッ化水素酸170 kgを得
た。そして、精製したケイフッ化水素酸中の不純物含有
量をICP-MS法及びICP-AES 法で調べて表2に示す結果を
得た。Example 2 200 kg of a raw material hydrosilicofluoric acid (hydrogen fluoride: 3.3 mol / liter, silicon tetrafluoride: 3.9 mol / liter) containing impurities shown in Table 2 was mixed with potassium permanganate to obtain a liquid color. It was charged until it showed a light purple color. The solution was introduced into a distillation apparatus made of fluororesin, and subjected to heat distillation to purify hydrosilicofluoric acid to obtain 170 kg of purified hydrofluorosilicic acid. Then, the content of impurities in the purified hydrofluorosilicic acid was examined by the ICP-MS method and the ICP-AES method, and the results shown in Table 2 were obtained.
【0017】[0017]
【表2】 [Table 2]
【0018】実施例3 表3に示す不純物を含む原料ケイフッ化水素酸(フッ化
水素 3.3 モル/リットル、四フッ化ケイ素 4.0 モル
/リットル)150 kgをフッ素樹脂製の蒸留装置に導入
し、蒸留塔にフッ素ガスを100 ミリリットル/分で投入
しながら15kg/時間の蒸発量で蒸留を行ってケイフッ化
水素酸を精製し、精製ケイフッ化水素酸120 kgを得た。
そして、精製したケイフッ化水素酸中の不純物含有量を
ICP-MS法及びイオンクロマトグラフ法で調べて表3に示
す結果を得た。Example 3 150 kg of raw material hydrosilicofluoric acid (hydrogen fluoride: 3.3 mol / liter, silicon tetrafluoride: 4.0 mol / liter) containing impurities shown in Table 3 was introduced into a distillation apparatus made of a fluororesin and distilled. The fluorohydrofluoric acid was purified by performing distillation at an evaporation rate of 15 kg / hour while introducing 100 ml / min of fluorine gas into the column to obtain 120 kg of purified hydrofluoric acid.
Then, the content of impurities in the purified hydrofluorosilicic acid
The results shown in Table 3 were obtained by an ICP-MS method and an ion chromatography method.
【0019】[0019]
【表3】 [Table 3]
【0020】表4に示す不純物を含む原料ケイフッ化水
素酸(フッ化水素 7.8 モル/リットル、四フッ化ケイ
素 3.9 モル/リットル)100 kgに重クロム酸カリウム
200gを攪拌しながら投入した。その液をフッ素樹脂製の
蒸留装置に導入し、加熱蒸留を行ってケイフッ化水素酸
を精製し、精製ケイフッ化水素酸70kgを得た。そして、
精製したケイフッ化水素酸中の不純物含有量をICP-MS法
及びイオンクロマトグラフ法で調べて表4に示す結果を
得た。Raw material hydrosilicofluoric acid (hydrogen fluoride 7.8 mol / liter, silicon tetrafluoride 3.9 mol / liter) containing impurities shown in Table 4 was added to 100 kg of potassium dichromate.
200 g was added while stirring. The liquid was introduced into a distillation apparatus made of fluororesin, and heated and distilled to refine hydrosilicofluoric acid to obtain 70 kg of purified hydrosilicofluoric acid. And
The content of impurities in the purified hydrosilicofluoric acid was examined by the ICP-MS method and the ion chromatography method, and the results shown in Table 4 were obtained.
【0021】[0021]
【表4】 [Table 4]
【0022】対比実験 表5に示す不純物を含む原料ケイフッ化水素酸(フッ化
水素 7.8 モル/リットル、四フッ化ケイ素 3.9 モル
/リットル)100 kgをフッ素樹脂製の蒸留装置に導入
し、加熱蒸留を行ってケイフッ化水素酸を精製し、精製
ケイフッ化水素酸65kgを得た。そして、精製したケイフ
ッ化水素酸中の不純物含有量をICP-MS法及びイオンクロ
マトグラフ法で調べて表5に示す結果を得た。Comparative Experiment 100 kg of a raw material hydrosilicofluoric acid (hydrogen fluoride: 7.8 mol / liter, silicon tetrafluoride: 3.9 mol / liter) containing impurities shown in Table 5 was introduced into a distillation apparatus made of a fluororesin, and heated and distilled. Was performed to purify hydrosilicofluoric acid to obtain 65 kg of purified hydrosilicofluoric acid. Then, the content of impurities in the purified hydrofluorosilicic acid was examined by the ICP-MS method and the ion chromatography method, and the results shown in Table 5 were obtained.
【0023】[0023]
【表5】 [Table 5]
【0024】[0024]
【発明の効果】以上からも明らかなように、本発明にお
けるケイフッ化水素酸の精製方法は、ケイフッ化水素酸
中の硫黄化合物、燐化合物、硼素化合物及び砒素化合物
等の不純物の除去に関して、きわめて有効なものであ
る。As is apparent from the above, the method for purifying hydrosilicofluoric acid according to the present invention is extremely effective in removing impurities such as sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds in hydrosilicofluoric acid. It is valid.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡田 友克 大阪府大阪市中央区高麗橋2丁目6番10号 森田化学工業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tomokatsu Okada 2-6-10 Koraibashi, Chuo-ku, Osaka City, Osaka Prefecture Morita Chemical Industry Co., Ltd.
Claims (1)
四フッ化ケイ素を含有し、その両者が20〜65重量パーセ
ントである水溶液に、過マンガン酸カリウム等の酸化剤
を添加し、加熱蒸留して、その水溶液に含有される硫黄
化合物、燐化合物、硼素化合物及び砒素化合物を酸化除
去することを特徴とするケイフッ化水素酸の精製方法。1. An aqueous solution containing 0.3 to 1.3 times the number of moles of silicon tetrafluoride with respect to hydrogen fluoride, both of which is 20 to 65 weight percent, is added with an oxidizing agent such as potassium permanganate. A method for purifying hydrosilicofluoric acid, which comprises heating and distilling to oxidize and remove sulfur compounds, phosphorus compounds, boron compounds and arsenic compounds contained in the aqueous solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05499893A JP3436381B2 (en) | 1993-02-19 | 1993-02-19 | Purification method of hydrofluorosilicic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05499893A JP3436381B2 (en) | 1993-02-19 | 1993-02-19 | Purification method of hydrofluorosilicic acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06247708A true JPH06247708A (en) | 1994-09-06 |
| JP3436381B2 JP3436381B2 (en) | 2003-08-11 |
Family
ID=12986334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP05499893A Expired - Lifetime JP3436381B2 (en) | 1993-02-19 | 1993-02-19 | Purification method of hydrofluorosilicic acid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3436381B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11639302B2 (en) | 2016-11-10 | 2023-05-02 | Mexichem Fluor S.A. De C.V. | Process for reducing the concentration of arsenic in an aqueous solution comprising a fluoroacid |
-
1993
- 1993-02-19 JP JP05499893A patent/JP3436381B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11639302B2 (en) | 2016-11-10 | 2023-05-02 | Mexichem Fluor S.A. De C.V. | Process for reducing the concentration of arsenic in an aqueous solution comprising a fluoroacid |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3436381B2 (en) | 2003-08-11 |
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