JP2001079336A - Gas treating device - Google Patents

Gas treating device

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Publication number
JP2001079336A
JP2001079336A JP26530099A JP26530099A JP2001079336A JP 2001079336 A JP2001079336 A JP 2001079336A JP 26530099 A JP26530099 A JP 26530099A JP 26530099 A JP26530099 A JP 26530099A JP 2001079336 A JP2001079336 A JP 2001079336A
Authority
JP
Japan
Prior art keywords
water
gas
reaction
scattering
stuck
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
JP26530099A
Other languages
Japanese (ja)
Other versions
JP3374801B2 (en
Inventor
Shinobu Kono
忍 河野
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.)
NEC Corp
Original Assignee
NEC Corp
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 NEC Corp filed Critical NEC Corp
Priority to JP26530099A priority Critical patent/JP3374801B2/en
Publication of JP2001079336A publication Critical patent/JP2001079336A/en
Application granted granted Critical
Publication of JP3374801B2 publication Critical patent/JP3374801B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently perform gas treatment of a washing column and also to reduce load and to prevent product deposition at the washing column by generating hydrolyzing reaction by allowing scattering water to contact with the gas to be treated, then capturing reactive organism with a woven textile and removing the captured matter by dissolving to a solution in a water tank. SOLUTION: For example, the gaseous SiF4 to be treated is introduced into an exhaust duct 15 from an exhaust gas inlet 13 and allowed to react at first with the water scattered from a scattering pipe 11. Then the reacted treating gas is brought into contract successively with a wet woven textiles 17 in several stages provided in the exhaust duct 15 to accelerate the reaction by each endothermic reaction (evaporation heat) of the scattering water and the water stuck to the woven textile. Then the H2SiF6 formed by the reaction is stuck to the woven textile 17 at the post stage and the woven textile 17 is introduced into the water tank 14 through plural rollers 16a and 16b to remove the stuck matter by dissolving the stuck matter in water. On the other hand, the water tank 14 is always replenished by the scattering water from the scattering pipe 11 and also surplus water is discharged from a waste water outlet 20.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、ガス処理装置に関
するものである。
The present invention relates to a gas processing apparatus.

【0002】[0002]

【従来の技術】従来例に係るガス処理装置は図3に示す
ように、洗浄塔23内の酸排気入口26より上方に排気
処理用充填物25が設置され、散布管24から排気処理
用充填物25に散水が行われるようになっており、洗浄
塔23の底部に廃水管27が接続されている。また洗浄
塔23の清浄空気出口28から送風ファン22により清
浄空気が排出されるようになっている。
2. Description of the Related Art As shown in FIG. 3, a gas treatment apparatus according to a conventional example is provided with an exhaust treatment filler 25 above an acid exhaust inlet 26 in a washing tower 23, and a discharge pipe 24 is supplied from a scatter pipe 24. Water is sprayed on the object 25, and a waste water pipe 27 is connected to the bottom of the washing tower 23. Further, the clean air is discharged from the clean air outlet 28 of the washing tower 23 by the blower fan 22.

【0003】また洗浄塔23内の廃水の一部は、貯留槽
33に帰還され、また貯留槽33の補給水入口32には
補給管31が接続されている。また貯留槽33には薬品
注入装置30が取付け、貯留槽33から循環ポンプ29
にて排気処理用充填物25に散水が行われる。
A part of the waste water in the washing tower 23 is returned to the storage tank 33, and a supply pipe 31 is connected to a supply water inlet 32 of the storage tank 33. A chemical injection device 30 is attached to the storage tank 33, and a circulating pump 29 is provided from the storage tank 33.
The water is sprayed on the exhaust treatment filling 25.

【0004】以上のように従来例に係るガス処理装置は
図3に示すように、処理ガスを無機ハロゲン化ガスとし
て取扱うものであり、例えばSiF4ガスをガスとして
吸着処理する、或いは空気と混合して排気処理するよう
になっている。
As described above, the conventional gas processing apparatus treats a processing gas as an inorganic halogenated gas, as shown in FIG. 3, and for example, adsorbs SiF 4 gas as a gas or mixes it with air. And then exhaust it.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、図3に
示す従来例に係るガス処理装置では、例えばSiF4
スは、気液接触部分(排気処理用充填物25及び循環ポ
ンプ29による散水)で反応しきれなかったH2Si
6,洗浄塔23の洗浄水によって生成される副生成物
であるNaSiF6,(NH42SiF6などが後段の送
風ファン22に析出して、送風ファン22を停止させる
という問題がある。
However, in the gas processing apparatus according to the conventional example shown in FIG. 3, for example, SiF 4 gas reacts at the gas-liquid contact portion (water spraying by the exhaust treatment packing 25 and the circulation pump 29). H 2 Si that could not be removed
There is a problem in that F 6 , NaSiF 6 , (NH 4 ) 2 SiF 6, etc., which are by-products generated by the washing water in the washing tower 23, are deposited on the blower fan 22 at the subsequent stage, and stop the blower fan 22. .

【0006】本発明の目的は、洗浄塔でのガス処理を効
率的に行い、また洗浄塔への負荷軽減および生成物析出
を防止するガス処理装置を提供することにある。
An object of the present invention is to provide a gas treatment apparatus for efficiently performing gas treatment in a washing tower, reducing the load on the washing tower and preventing product deposition.

【0007】[0007]

【課題を解決するための手段】前記目的を達成するた
め、本発明に係るガス処理装置は、処理対象のガスに散
布管からの散布水を強制的に接触させて加水分解反応を
起こし、その反応生成物を織布で捕獲して水槽の溶液に
溶解させて除去するようにしたものである。
Means for Solving the Problems To achieve the above object, a gas treatment apparatus according to the present invention forcibly contacts spray gas from a spray pipe with a gas to be treated to cause a hydrolysis reaction. The reaction product is captured by a woven cloth, dissolved in a solution in a water tank, and removed.

【0008】[0008]

【発明の実施の形態】以下、本発明の実施の形態を図に
より説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings.

【0009】(実施形態1)図1は、本発明の実施形態
1に係るガス処理装置を示す構成図である。
(Embodiment 1) FIG. 1 is a configuration diagram showing a gas processing apparatus according to Embodiment 1 of the present invention.

【0010】図1に示す本発明の実施形態1に係るガス
処理装置は、処理対象のガスを流動させる排気ダクト1
5を備えており、排気ダクト15の下部に水槽14を取
付けている。
A gas processing apparatus according to a first embodiment of the present invention shown in FIG. 1 has an exhaust duct 1 for flowing a gas to be processed.
5 and a water tank 14 is attached to the lower part of the exhaust duct 15.

【0011】さらに排気ダクト15の天井側にローラ1
6a,16a,16a・・・をガス流に沿って設置し、
かつ水槽14内にローラ16b,16b・・・と方向転
換用ローラ16c,16dを設置している。
Further, a roller 1 is provided on the ceiling side of the exhaust duct 15.
6a, 16a, 16a ... are installed along the gas flow,
Further, rollers 16b, 16b... And direction changing rollers 16c, 16d are provided in the water tank 14.

【0012】そして、ローラ16a,16a,16a、
16b,16b、方向転換用ローラ16c,16dに無
端状の織布17を掛渡し、織布17を水槽14内の洗浄
水S内に浸漬し、方向転換用ローラ16cで方向転換さ
れて水槽14から繰出された織布17を排気ダクト15
内と水槽14内とに交互に移動可能にローラ16a,1
6bで誘導して蛇行させ、織布17を折返して排気ダク
ト15内に複数段に設置している。
And rollers 16a, 16a, 16a,
The endless woven fabric 17 is wrapped around the rollers 16b, 16b and the direction changing rollers 16c, 16d, the woven fabric 17 is immersed in the washing water S in the water tank 14, and the direction is changed by the direction changing roller 16c. The woven fabric 17 fed from the
Roller 16a, 1 so that it can move alternately between the inside and the water tank 14.
The woven cloth 17 is folded back and installed in the exhaust duct 15 in a plurality of stages.

【0013】また排気ダクト15の上流側に散水管11
を設置し、排気ダクト15の下流側に清浄空気出口18
を配置している。織布17は、散布管11から散布した
水の飛散防止と気液接触触媒を兼ねている。
The sprinkler pipe 11 is located upstream of the exhaust duct 15.
And a clean air outlet 18 downstream of the exhaust duct 15.
Has been arranged. The woven fabric 17 also serves as a gas-liquid contact catalyst and for preventing scattering of water sprayed from the spray pipe 11.

【0014】また水槽14には余剰水を排出する廃水管
19が接続され、廃水管19の廃水出口20から余剰水
を廃水するようになっている。
A waste water pipe 19 for discharging surplus water is connected to the water tank 14, and the surplus water is discharged from a waste water outlet 20 of the waste water pipe 19.

【0015】次に、本発明の実施形態1に係るガス処理
装置を使用して処理対象のガスを処理する方法について
説明する。本発明の実施形態1に係るガス処理方法で
は、処理対象のガスとしてSiF4ガスを用いた場合を
例にとって説明する。
Next, a method for processing a gas to be processed using the gas processing apparatus according to the first embodiment of the present invention will be described. In the gas processing method according to the first embodiment of the present invention, a case where SiF 4 gas is used as a processing target gas will be described as an example.

【0016】SiF4ガスは、空気と混合すると空気中
の水分と反応して一部は以下のような反応が起こる。 3SiF4+4H2O→2H2SiF6+Si(OH)4 したがって、排気ガス入口13から排気ダクト15内に
導入されるガスの中には、の反応式で混合物とSiF
4ガスとが混在している。
When the SiF 4 gas is mixed with air, it reacts with the moisture in the air, and the following reaction occurs partially. 3SiF 4 + 4H 2 O → 2H 2 SiF 6 + Si (OH) 4 Therefore, the gas introduced into the exhaust duct 15 from the exhaust gas inlet 13 includes the mixture and the SiF
4 gases are mixed.

【0017】排気ガス入口13から排気ダクト15内に
導入されたSiF4ガスは、まず散布管11から散布さ
れた水と激しく反応してふっ化水素酸(HF)とケイ酸
(SiO2)を生じる。
The SiF 4 gas introduced into the exhaust duct 15 from the exhaust gas inlet 13 violently reacts with water sprayed from the spray pipe 11 to convert hydrofluoric acid (HF) and silicic acid (SiO 2 ). Occurs.

【0018】の反応式で生成した混合物に、このふっ
化水素酸が作用して多量のH2SiF6が生成される。ま
た、以下の反応も同時進行する。 4HF+SiO2→SiF4+2H2O 2HF+SiF4→H2SiF6 さらに散布管11からの散布水領域を通過した処理ガス
は排気ダクト15内に送込まれ、折返して排気ダクト1
5内に複数段に設置された、濡れた織布17に次々に接
触する。
The hydrofluoric acid acts on the mixture formed by the reaction formula to generate a large amount of H 2 SiF 6 . The following reactions also proceed simultaneously. 4HF + SiO 2 → SiF 4 + 2H 2 O 2HF + SiF 4 → H 2 SiF 6 Further, the processing gas that has passed through the spray water area from the spray pipe 11 is sent into the exhaust duct 15, and is turned back to return to the exhaust duct 1.
The wet woven fabric 17 placed in a plurality of stages in the fabric 5 comes into contact with each other one after another.

【0019】処理ガスと散布管11からの散布水との反
応、処理ガスと濡れた織布17との反応は全て発熱反応
であるため、散布水の吸熱反応(蒸発熱)効果及び織布
付着水の吸熱反応(蒸発熱)効果により更に反応は加速
する。
Since the reaction between the processing gas and the spray water from the spray pipe 11 and the reaction between the processing gas and the wet woven fabric 17 are all exothermic reactions, the endothermic reaction (heat of evaporation) of the spray water and the adhesion of the woven cloth. The reaction is further accelerated by the endothermic reaction of water (heat of evaporation).

【0020】これらの反応により生成されたH2SiF6
は、後段の織布17に付着し、織布17はローラ16
a,16bによって水槽14内に導かれ、織布17に付
着したH2SiF6は、水槽17内の水に溶解することに
よって除去される。
The H 2 SiF 6 produced by these reactions
Adheres to the subsequent woven fabric 17, and the woven fabric 17 is
The H 2 SiF 6 guided into the water tank 14 by the a and 16 b and adhered to the woven fabric 17 is removed by dissolving in the water in the water tank 17.

【0021】また水槽14内の水は散布管11からの散
布水により常に補給されるため、余剰水は廃水出口20
から排出される。
Since the water in the water tank 14 is constantly replenished by the spray water from the spray pipe 11, surplus water is supplied to the waste water outlet 20.
Is discharged from

【0022】以上のように本発明の実施形態1は、例え
ばSiF4ガスの排気が行われる洗浄塔の前段(図3参
照)に設置することにより、効率的にSiF4ガスを処
理し得る。また洗浄塔への負荷軽減及び生成物析出を防
止することにより、安定稼動に寄与することができる。
As described above, the first embodiment of the present invention can efficiently treat the SiF 4 gas by being installed, for example, before the washing tower (see FIG. 3) where the exhaust of the SiF 4 gas is performed. In addition, by reducing the load on the washing tower and preventing product precipitation, it is possible to contribute to stable operation.

【0023】(実施形態2)図2は、本発明の実施形態
2に係るガス処理装置を示す構成図である。
(Embodiment 2) FIG. 2 is a configuration diagram showing a gas processing apparatus according to Embodiment 2 of the present invention.

【0024】図2に示す本発明の実施形態2に係るガス
処理装置は、水槽14a,14b,14c,14d内を
多段に分割し、各水槽14a,14b,14c,14d
内にローラ16c,16b1,16b2,16dを設置
し、織布17を水槽14a内の方向転換用ローラ16c
で排気ダクト15内のローラ16a1に方向転換して掛
渡し、ローラ16a1からの織布17を水槽14内のロ
ーラ16b1に掛渡し、ローラ16b1からの織布17を
排気ダクト15内のローラ16a2に掛渡し、ローラ1
6a2からの織布17を水槽14内のローラ16b2に掛
渡し、ローラ16b2からの織布17を排気ダクト15
内のローラ16a3に掛渡し、ローラ16a3からの織布
17を水槽14内のローラ16dに掛渡すことにより無
端状に配置している。
In the gas processing apparatus according to the second embodiment of the present invention shown in FIG. 2, the water tanks 14a, 14b, 14c, 14d are divided into multiple stages, and the water tanks 14a, 14b, 14c, 14d are divided.
Rollers 16c, 16b1, 16b2, 16d are installed in the inside, and the woven fabric 17 is turned in the water tank 14a.
To wrap around the roller 16a1 in the exhaust duct 15, and wrap the woven fabric 17 from the roller 16a1 over the roller 16b1 in the water tank 14, and transfer the woven fabric 17 from the roller 16b1 to the roller 16a2 in the exhaust duct 15. Rolling over, roller 1
The woven fabric 17 from the roller 16b2 is passed over the rollers 16b2 in the water tank 14, and the woven fabric 17 from the rollers 16b2 is
And the woven fabric 17 from the roller 16a3 is wound on the roller 16d in the water tub 14 to be disposed endlessly.

【0025】さらに排気ダクト15内の天井側に設置し
たローラ16a1,16a2,16a3,16a4に隣接し
て散布管11a,11b,11c,11dをそれぞれ設
置し、後段の水槽から前段の散布管に水をポンプ21
a,21bにより送水するようにしたものである。
Further, spraying pipes 11a, 11b, 11c and 11d are installed adjacent to the rollers 16a1, 16a2, 16a3 and 16a4 installed on the ceiling side in the exhaust duct 15, respectively. The pump 21
a, 21b.

【0026】図2に示す本発明の実施形態2に係るガス
処理装置によれば、処理ガスと散布管からの散布水との
反応、処理ガスと濡れた織布との反応を複数回繰返して
行うことができ、反応の遅いガスも効率的に除去処理す
ることができるという利点を有する。
According to the gas processing apparatus according to the second embodiment of the present invention shown in FIG. 2, the reaction between the processing gas and the spray water from the spray pipe and the reaction between the processing gas and the wet woven cloth are repeated a plurality of times. This method has an advantage that gas having a slow reaction can be efficiently removed.

【0027】[0027]

【発明の効果】以上のように本発明によれば、処理ガス
と散布水との反応、処理ガスと濡れた織布との反応を組
合せて行うため、これらの反応は全て発熱反応であり、
散布水の吸熱反応(蒸発熱)効果及び織布付着水の吸熱
反応(蒸発熱)効果により更に反応は加速させて行うこ
とができる。
As described above, according to the present invention, since the reaction between the processing gas and the spray water and the reaction between the processing gas and the wet woven fabric are performed in combination, these reactions are all exothermic,
The reaction can be further accelerated by the endothermic reaction (heat of evaporation) of the spray water and the endothermic reaction (heat of evaporation) of the water adhering to the woven fabric.

【0028】したがって図3に示すような洗浄塔の前段
に設置することにより、効率的にガスを処理することが
でき、洗浄塔への負荷軽減及び生成物析出を防止するこ
とにより、安定稼動に寄与することができる。
Therefore, the gas can be efficiently treated by being installed at the front stage of the washing tower as shown in FIG. 3, and the load on the washing tower can be reduced, and the product can be prevented from being deposited, whereby stable operation can be achieved. Can contribute.

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

【図1】本発明の実施形態1に係るガス処理装置を示す
構成図である。
FIG. 1 is a configuration diagram illustrating a gas processing apparatus according to a first embodiment of the present invention.

【図2】本発明の実施形態2に係るガス処理装置を示す
構成図である。
FIG. 2 is a configuration diagram illustrating a gas processing apparatus according to a second embodiment of the present invention.

【図3】従来例に係るガス処理装置を示す構成図であ
る。
FIG. 3 is a configuration diagram showing a gas processing apparatus according to a conventional example.

【符号の説明】[Explanation of symbols]

11 散水管 14 水槽 15 排気ダクト 17 織布 11 watering pipe 14 water tank 15 exhaust duct 17 woven cloth

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 処理対象のガスに散布管からの散布水を
強制的に接触させて加水分解反応を起こし、その反応生
成物を織布で捕獲して水槽の溶液に溶解させて除去する
ようにしたことを特徴とするガス処理装置。
1. A method in which a spraying water from a spraying tube is forcibly brought into contact with a gas to be treated to cause a hydrolysis reaction, and the reaction product is captured by a woven fabric, dissolved in a solution in a water tank, and removed. A gas processing apparatus characterized in that:
JP26530099A 1999-09-20 1999-09-20 Gas treatment equipment Expired - Fee Related JP3374801B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26530099A JP3374801B2 (en) 1999-09-20 1999-09-20 Gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26530099A JP3374801B2 (en) 1999-09-20 1999-09-20 Gas treatment equipment

Publications (2)

Publication Number Publication Date
JP2001079336A true JP2001079336A (en) 2001-03-27
JP3374801B2 JP3374801B2 (en) 2003-02-10

Family

ID=17415295

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26530099A Expired - Fee Related JP3374801B2 (en) 1999-09-20 1999-09-20 Gas treatment equipment

Country Status (1)

Country Link
JP (1) JP3374801B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005004635A1 (en) 2003-07-10 2005-01-20 Takasago International Corporation Flavor enhancer, food or beverage containing the flavor enhancer, and method of flavor enhancement
CN110141925A (en) * 2019-07-01 2019-08-20 金发科技股份有限公司 A kind of adsorption and sedimentation device, the system and method for the exhaust gas containing particulate matter

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005004635A1 (en) 2003-07-10 2005-01-20 Takasago International Corporation Flavor enhancer, food or beverage containing the flavor enhancer, and method of flavor enhancement
CN110141925A (en) * 2019-07-01 2019-08-20 金发科技股份有限公司 A kind of adsorption and sedimentation device, the system and method for the exhaust gas containing particulate matter

Also Published As

Publication number Publication date
JP3374801B2 (en) 2003-02-10

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