JP2005307403A - Polybenzobisoxazole fiber excellent in spinnability - Google Patents

Polybenzobisoxazole fiber excellent in spinnability Download PDF

Info

Publication number
JP2005307403A
JP2005307403A JP2004127957A JP2004127957A JP2005307403A JP 2005307403 A JP2005307403 A JP 2005307403A JP 2004127957 A JP2004127957 A JP 2004127957A JP 2004127957 A JP2004127957 A JP 2004127957A JP 2005307403 A JP2005307403 A JP 2005307403A
Authority
JP
Japan
Prior art keywords
pbo
spinnability
spinning
polymerization
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.)
Withdrawn
Application number
JP2004127957A
Other languages
Japanese (ja)
Inventor
Yasuko Mitooka
靖子 水戸岡
Yukihiro Abe
幸浩 阿部
Fuyuhiko Kubota
冬彦 久保田
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.)
Toyobo Co Ltd
Original Assignee
Toyobo 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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP2004127957A priority Critical patent/JP2005307403A/en
Publication of JP2005307403A publication Critical patent/JP2005307403A/en
Withdrawn legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for obtaining polybenzobisoxasole (PBO) fiber having high physical properties by spinning dope having high degree of polymerization and excellent in spinnability. <P>SOLUTION: The PBO fiber having high physical properties is obtained by hydrolyzing and reducing 2-sulfonic acid-4,6-dinitroresorcinol and polymerizing the resultant high-purity 4,6-diaminoresorcinol to afford a high molecular weight PBO and spinning the PBO. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、高強度・高弾性率繊維に成形することができるポリベンゾビスオキサゾール(以下PBOという。)の紡糸法に関するものである。   The present invention relates to a spinning method of polybenzobisoxazole (hereinafter referred to as PBO) that can be formed into a high-strength and high-modulus fiber.

PBOは下記一般式構造(C)に表されるポリマーであり、下記反応式に示されるように化合物(A)と(B)の縮合反応によって得ることができる。

Figure 2005307403
ここで式中のArは芳香族基であり、Yはカルボキシル基、カルボン酸ハライド基、ハロアルキル基、ニトリル基などの電子不足炭素を有する官能基である。 PBO is a polymer represented by the following general formula structure (C), and can be obtained by a condensation reaction of the compounds (A) and (B) as shown in the following reaction formula.
Figure 2005307403
Here, Ar in the formula is an aromatic group, and Y is a functional group having an electron-deficient carbon such as a carboxyl group, a carboxylic acid halide group, a haloalkyl group, or a nitrile group.

このようにして得られるPBOの用途は繊維やフィルムなどであるが、その強度、弾性率などの諸物性、可紡性はポリマーの重合度に大きく影響を受ける。一般に重縮合反応においてはモノマーの仕込み比が1:1のときに得られるポリマー粘度が最大となり、モノマー仕込み比が1:1からずれるにしたがって急激に低下することが知られている。即ち満足しうる物性や可紡性を得るためには、モノマー仕込み比を厳密に管理し、十分な重合度を持つポリマーを供給することが必要である。   The use of PBO thus obtained is for fibers and films, but its physical properties such as strength and elastic modulus, and spinnability are greatly affected by the degree of polymerization of the polymer. In general, in the polycondensation reaction, it is known that the polymer viscosity obtained becomes maximum when the monomer charge ratio is 1: 1 and rapidly decreases as the monomer charge ratio deviates from 1: 1. That is, in order to obtain satisfactory physical properties and spinnability, it is necessary to strictly control the monomer charge ratio and supply a polymer having a sufficient degree of polymerization.

しかしモノマー中に不純物を多く含有する場合は、モノマー仕込み比の管理が困難となり、特にモノアミンやトリアミン等を含有する場合にはこれらが重合停止や三次元架橋を引き起こすため、微量含有していても重合度や可紡性の低下を引き起こす要因となる。十分な重合度を持ち可紡性に優れたポリマーを得るためには、これらのモノアミンやトリアミン等の不純物を含有しない高純度のモノマーを用いることが必要とされている。   However, if the monomer contains a large amount of impurities, it is difficult to manage the monomer charge ratio. It becomes a factor causing a decrease in the degree of polymerization and spinnability. In order to obtain a polymer having a sufficient degree of polymerization and excellent spinnability, it is necessary to use high-purity monomers that do not contain impurities such as monoamines and triamines.

PBOのモノマーとして4,6−ジアミノレゾルシンが使用されており、種々の合成法が報告されている。例えばレゾルシンをアセチル化してニトロ化後加水分解して還元する方法(Ber.Dtch.Chem.,16,552,1883)、1,3−ビス(アルキルカーボネート)ベンゼンをニトロ化後加水分解して還元する方法(特開平2−136号公報)などがある。しかしこれらの方法においてはニトロ化においてトリニトロ体が生成し、還元工程でトリアミノ体となって三次元架橋を引き起こし、可紡性が低下するという問題点がある。また別の方法としてアニリンをジアゾ化してレゾルシンとジアゾカップリングした後に水素化分解を行うという方法が特開平7−242604号公報、特開平9−124575号公報で提案されているが、この方法においては水素化分解で発生したアニリンが製品中に混入し、十分な重合度が得られず可紡性が低下する恐れがある。一方で、2−スルホン酸−4,6−ジニトロレゾルシンを加水分解することで、異性体やトリニトロ体を含まない4,6−ジニトロレゾルシンが得られ、これを還元して高純度の4,6−ジアミノレゾルシンを得るという方法が特開2000−319231号公報で提案されている。この高純度4,6−ジアミノレゾルシンを用いて重合すると、重合阻害や三次元架橋が起こらず高分子量のPBOが得られる(特開2001−139685号公報)。   4,6-Diaminoresorcin has been used as a monomer for PBO, and various synthetic methods have been reported. For example, a method in which resorcin is acetylated, nitrated, hydrolyzed and reduced (Ber. Dtch. Chem., 16, 552, 1883), 1,3-bis (alkyl carbonate) benzene is nitrated, hydrolyzed and reduced There is a method (Japanese Patent Laid-Open No. 2-136). However, in these methods, there is a problem that a trinitro body is formed in nitration and becomes a triamino body in the reduction step to cause three-dimensional crosslinking, resulting in a decrease in spinnability. As another method, Japanese Patent Application Laid-Open No. 7-242604 and Japanese Patent Application Laid-Open No. 9-124575 propose methods in which aniline is diazotized and diazo-coupled with resorcin and then hydrocracked. In the case of aniline, aniline generated by hydrogenolysis is mixed in the product, and there is a possibility that a sufficient degree of polymerization cannot be obtained and the spinnability is lowered. On the other hand, hydrolysis of 2-sulfonic acid-4,6-dinitroresorcin yields 4,6-dinitroresorcin, which does not contain isomers or trinitro, and is reduced to high purity 4,6. A method for obtaining diaminoresorcin has been proposed in JP 2000-319231 A. When polymerized using this high purity 4,6-diaminoresorcin, high molecular weight PBO is obtained without polymerization inhibition or three-dimensional crosslinking (Japanese Patent Laid-Open No. 2001-139985).

本発明は高純度の4,6−ジアミノレゾルシンを用いて重合した高重合度のドープを用いることで、可紡性に優れた高物性のPBO繊維を得る方法を提供することである。   An object of the present invention is to provide a method for obtaining PBO fibers having high physical properties excellent in spinnability by using a dope having a high polymerization degree obtained by polymerization using high-purity 4,6-diaminoresorcin.

本発明は、2−スルホン酸−4,6−ジニトロレゾルシンを加水分解し、還元して得られた高純度の4,6−ジアミノレゾルシンを用いて重合することにより得た高分子量のPBOを用いることで、可紡性に優れた高物性PBO繊維を得ることである。   The present invention uses a high molecular weight PBO obtained by polymerizing with a high-purity 4,6-diaminoresorcin obtained by hydrolyzing 2-sulfonic acid-4,6-dinitroresorcin and reducing it. Thus, it is to obtain PBO fibers having high physical properties excellent in spinnability.

本発明における2−スルホン−4,6−ジニトロレゾルシンより合成された4,6−ジアミノレゾルシンは重合阻害物となり得るモノアミノ体やトリニトロ体を含まず、それゆえに該化合物を用いて重合したポリベンゾビスオキサゾールは十分な分子量を有し可紡性に優れ、紡糸により優れた特性を発揮する。即ち本発明によればポリベンゾビスオキサゾール繊維を工業的に有利に製造することができる。   The 4,6-diaminoresorcinol synthesized from 2-sulfone-4,6-dinitroresorcin in the present invention does not contain a monoamino or trinitro compound that can be a polymerization inhibitor, and is therefore a polybenzobispolymerized using the compound. Oxazole has a sufficient molecular weight, excellent spinnability, and exhibits excellent properties by spinning. That is, according to the present invention, polybenzobisoxazole fibers can be produced industrially advantageously.

本発明で使用するPBOは、2−スルホン酸−4,6−ジニトロレゾルシンを加水分解し、還元して得られた高純度4,6−ジアミノレゾルシンを用いて重合される。このモノマーは、製造工程においてモノニトロ体やトリニトロ体を含まないため、重合時の阻害物となりうるモノアミノ体やトリアミノ体を生じる恐れがない。   PBO used in the present invention is polymerized using high-purity 4,6-diaminoresorcin obtained by hydrolyzing 2-sulfonic acid-4,6-dinitroresorcin and reducing it. Since this monomer does not contain a mononitro compound or a trinitro compound in the production process, there is no possibility of producing a monoamino compound or a triamino compound that can be an inhibitor during polymerization.

この高純度4,6−ジアミノレゾルシンを用いた重合は公知の方法で行うことができる。例えばポリリン酸に窒素気流下、五酸化リンを加え、該4,6−ジアミノレゾルシン二塩酸塩、4,6−ジアミノレゾルシンとほぼ当モル量の芳香族ジカルボン酸を添加して加熱攪拌を行うことにより得られる。芳香族ジカルボン酸としては例えばテレフタル酸、イソフタル酸、4,4’−ビス(安息香酸)、4,4’−オキシビス(安息香酸)、2,6−ナフタレンジカルボン酸などが使用できる。
以下に実例を用いて本発明を具体的に説明するが、本発明はもとより下記の実施例によって制限を受けるものではなく、前後機の主旨に適合し得る範囲で適当に変更を加えて実施することも勿論可能であり、それらはいずれも本発明の技術範囲に含まれる。
The polymerization using this high purity 4,6-diaminoresorcin can be carried out by a known method. For example, phosphorus pentoxide is added to polyphosphoric acid under a nitrogen stream, and the 4,6-diaminoresorcin dihydrochloride, 4,6-diaminoresorcin and an approximately equimolar amount of aromatic dicarboxylic acid are added and heated and stirred. Is obtained. As the aromatic dicarboxylic acid, for example, terephthalic acid, isophthalic acid, 4,4′-bis (benzoic acid), 4,4′-oxybis (benzoic acid), 2,6-naphthalenedicarboxylic acid and the like can be used.
Hereinafter, the present invention will be described in detail with reference to examples. However, the present invention is not limited by the following examples, and is appropriately modified within a range that can be adapted to the gist of the front and rear machines. Of course, it is also possible and they are all included in the technical scope of the present invention.

(極限粘度)
メタンスルホン酸を溶媒として、0.5g/lの濃度に調製したポリマー溶液の粘度をオストワルド粘度計を用いて25℃恒温槽中で測定し、算出した。
こうして重合したPBOドープはフィラメント径が11.5μm、1.5デニールになるような条件で紡糸された。紡糸温度175℃で孔径180μm、孔数166のノズルからフィラメントを適当な位置で収束させてマルチフィラメントにするように配置された第1洗浄浴中に押し出した。紡糸ノズルと第1洗浄浴の間のエアギャップには、より均一な温度でフィラメントが引き伸ばされるようにクエンチチャンバーを設置した。エアギャップ長は30cmとした。60℃の空気中にフィラメントを紡出した。テークアップ速度を200m/分とし、紡糸延伸倍率を30とした。PBO繊維中の残留リン濃度が6000ppm以下になるまで水洗した。さらに、1%NaOH水溶液で10秒間中和した後30秒間水洗後、200℃で3分間乾燥して、糸を糸管に巻き取った。
以下に実例を用いて本発明を具体的に説明するが、本発明はもとより下記の実施例によって制限を受けるものではなく、前後機の主旨に適合し得る範囲で適当に変更を加えて実施することも勿論可能であり、それらはいずれも本発明の技術範囲に含まれる。
(Intrinsic viscosity)
The viscosity of a polymer solution prepared to a concentration of 0.5 g / l using methanesulfonic acid as a solvent was measured and calculated using a Ostwald viscometer in a thermostatic chamber at 25 ° C.
The polymerized PBO dope was spun under conditions such that the filament diameter was 11.5 μm and 1.5 denier. The filament was extruded from a nozzle having a spinning temperature of 175 ° C. with a pore diameter of 180 μm and a pore number of 166 into a multifilament by converging the filament at an appropriate position. A quench chamber was installed in the air gap between the spinning nozzle and the first cleaning bath so that the filaments were stretched at a more uniform temperature. The air gap length was 30 cm. Filaments were spun in air at 60 ° C. The take-up speed was 200 m / min, and the spinning draw ratio was 30. The PBO fiber was washed with water until the residual phosphorus concentration was 6000 ppm or less. Further, the mixture was neutralized with 1% NaOH aqueous solution for 10 seconds, washed with water for 30 seconds, dried at 200 ° C. for 3 minutes, and the yarn was wound around a yarn tube.
Hereinafter, the present invention will be described in detail with reference to examples. However, the present invention is not limited by the following examples, and is appropriately modified within a range that can be adapted to the gist of the front and rear machines. Of course, it is also possible and they are all included in the technical scope of the present invention.

(実施例1)
116%のポリリン酸16.37kgに窒素気流下、五酸化リン5.33kgを加えた後、4,6−ジアミノレゾルシン3.56kg及びテレフタル酸2.69kgを加え、反応器内、60℃で10分撹拌混合した。さらに130℃まで昇温させ2時間撹拌混合し脱塩酸を行い、160℃まで昇温させ3.5時間撹拌しオリゴマー化した。その後、210℃に加熱した二軸押し出し機を用いて重合し、PBOポリマードープを得た。ポリマードープの色は黄色であり、固有粘度は28.4dl/gであった。こうして重合したPBOドープはフィラメント径が11.5μm、1.5デニールになるような条件で紡糸された。紡糸温度175℃で孔径180μm、孔数166のノズルからフィラメントを適当な位置で収束させてマルチフィラメントにするように配置された第1洗浄浴中に押し出した。紡糸ノズルと第1洗浄浴の間のエアギャップには、より均一な温度でフィラメントが引き伸ばされるようにクエンチチャンバーを設置した。エアギャップ長は30cmとした。60℃の空気中にフィラメントを紡出した。テークアップ速度を200m/分とし、紡糸延伸倍率を30とした。PBO繊維中の残留リン濃度が6000ppm以下になるまで水洗した。さらに、1%NaOH水溶液で10秒間中和した後30秒間水洗後、200℃で3分間乾燥して、糸を糸管に巻き取った。得られた糸の強度は39.2cN/dTex、弾性率は1152cN/dTexであった。紡糸に際して、120分(24km)間で単糸切れは全く発生しなかった。
(Example 1)
After adding 5.33 kg of phosphorus pentoxide to 16.37 kg of 116% polyphosphoric acid under a nitrogen stream, 3.56 kg of 4,6-diaminoresorcin and 2.69 kg of terephthalic acid were added. Stir and mix for minutes. The temperature was further raised to 130 ° C., and the mixture was stirred and mixed for 2 hours to remove hydrochloric acid. Then, it superposed | polymerized using the biaxial extruder heated at 210 degreeC, and obtained PBO polymer dope. The color of the polymer dope was yellow and the intrinsic viscosity was 28.4 dl / g. The polymerized PBO dope was spun under conditions such that the filament diameter was 11.5 μm and 1.5 denier. The filament was extruded from a nozzle having a spinning temperature of 175 ° C. with a pore diameter of 180 μm and a pore number of 166 into a multifilament by converging the filament at an appropriate position. A quench chamber was installed in the air gap between the spinning nozzle and the first cleaning bath so that the filaments were stretched at a more uniform temperature. The air gap length was 30 cm. Filaments were spun in air at 60 ° C. The take-up speed was 200 m / min, and the spinning draw ratio was 30. The PBO fiber was washed with water until the residual phosphorus concentration was 6000 ppm or less. Further, the mixture was neutralized with 1% NaOH aqueous solution for 10 seconds, washed with water for 30 seconds, dried at 200 ° C. for 3 minutes, and the yarn was wound around a yarn tube. The obtained yarn had a strength of 39.2 cN / dTex and an elastic modulus of 1152 cN / dTex. During spinning, no single yarn breakage occurred in 120 minutes (24 km).

(比較例1)
116%のポリリン酸16.19kgに窒素気流下、五酸化リン5.27kgを加えた後、1,3−ビス(アルキルカーボネート)ベンゼンを出発原料に合成された4,6−ジアミノレゾルシン3.52kg及びテレフタル酸2.66kgを加え、反応器内、60℃で10分撹拌混合した。さらに130℃まで昇温させ2時間撹拌混合し脱塩酸を行い、160℃まで昇温させ3.5時間撹拌しオリゴマー化した。その後、210℃に加熱した二軸押し出し機を用いて重合し、PBOポリマードープを得た。ポリマードープの色は黄色であり、固有粘度は29.3dl/gであった。実施例1記載の方法で紡糸を行った。得られた糸の強度は37.4cN/dTex、弾性率は1143cN/dTexであった。紡糸に際して、120分(24km)間で単糸切れ発生回数は2回であった。
(Comparative Example 1)
After adding 5.27 kg of phosphorus pentoxide under nitrogen flow to 16.19 kg of 116% polyphosphoric acid, 3.52 kg of 4,6-diaminoresorcinol synthesized using 1,3-bis (alkyl carbonate) benzene as a starting material And 2.66 kg of terephthalic acid were added, and the mixture was stirred and mixed in the reactor at 60 ° C. for 10 minutes. The temperature was further raised to 130 ° C., and the mixture was stirred and mixed for 2 hours to remove hydrochloric acid. Then, it superposed | polymerized using the biaxial extruder heated at 210 degreeC, and obtained PBO polymer dope. The color of the polymer dope was yellow and the intrinsic viscosity was 29.3 dl / g. Spinning was carried out by the method described in Example 1. The strength of the obtained yarn was 37.4 cN / dTex, and the elastic modulus was 1143 cN / dTex. During spinning, the number of occurrences of single yarn breakage was 2 times within 120 minutes (24 km).

本発明によると、良好な可紡性により強度・弾性率を充分に発揮することができるポリベンザゾール繊維を提供できるため、産業用資材として実用性を高め、利用分野を拡大する効果が絶大である。即ち、織物、編物、組み紐、ロープ、コードなどに加工される用途、すなわち、ケーブル、電線や光ファイバー等のテンションメンバー、ロープ等の緊張材、耐弾材等の耐衝撃用部材、手袋等の耐切創用部材、ベルト、タイヤ、靴底、ロープ、ホース等のゴム補強材等広範にわたる用途に使用可能である。   According to the present invention, it is possible to provide a polybenzazole fiber that can sufficiently exhibit strength and elastic modulus due to good spinnability. Therefore, the effect of enhancing practicality as an industrial material and expanding the field of use is tremendous. is there. In other words, applications that are processed into woven fabrics, knitted fabrics, braids, ropes, cords, etc., that is, tension members such as cables, electric wires and optical fibers, tension materials such as ropes, impact-resistant members such as bullet-proof materials, and cut-off resistance such as gloves It can be used for a wide range of applications, such as rubber reinforcements such as creative members, belts, tires, shoe soles, ropes, hoses and the like.

Claims (1)

2−スルホン酸−4,6−ジニトロレゾルシンを加水分解後、還元して得られた4,6−ジアミノレゾルシンと芳香族ジカルボン酸を反応させて得たポリベンゾビスオキサゾールを用いることを特徴とする、可紡性に優れたポリベンゾビスオキサゾール繊維。   It is characterized by using polybenzobisoxazole obtained by reacting 4,6-diaminoresorcinol obtained by hydrolysis of 2-sulfonic acid-4,6-dinitroresorcin and then reducing it, and aromatic dicarboxylic acid. Polybenzobisoxazole fiber with excellent spinnability.
JP2004127957A 2004-04-23 2004-04-23 Polybenzobisoxazole fiber excellent in spinnability Withdrawn JP2005307403A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004127957A JP2005307403A (en) 2004-04-23 2004-04-23 Polybenzobisoxazole fiber excellent in spinnability

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004127957A JP2005307403A (en) 2004-04-23 2004-04-23 Polybenzobisoxazole fiber excellent in spinnability

Publications (1)

Publication Number Publication Date
JP2005307403A true JP2005307403A (en) 2005-11-04

Family

ID=35436490

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004127957A Withdrawn JP2005307403A (en) 2004-04-23 2004-04-23 Polybenzobisoxazole fiber excellent in spinnability

Country Status (1)

Country Link
JP (1) JP2005307403A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109487355A (en) * 2018-12-10 2019-03-19 浙江鼎龙科技有限公司 A kind of preparation method of polyparaphenylene's benzo dioxazole fiber

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109487355A (en) * 2018-12-10 2019-03-19 浙江鼎龙科技有限公司 A kind of preparation method of polyparaphenylene's benzo dioxazole fiber
CN109487355B (en) * 2018-12-10 2021-05-11 浙江鼎龙科技股份有限公司 Preparation method of poly (p-phenylene-benzobisoxazole) fibers

Similar Documents

Publication Publication Date Title
JP3717405B2 (en) Polyketone solution
KR101921393B1 (en) Polyamide multifilament fiber and tire cord including said fiber
JP3883510B2 (en) Polyketone fiber and method for producing the same
JP6164379B2 (en) Polyamide resin fiber, method for producing polyamide resin fiber, polyamide resin composition, woven fabric and knitted fabric
WO2003055934A1 (en) Polyketone and process for producing the same
TWI288189B (en) Polyketone fiber and method for production thereof
TW201000700A (en) Polyethylene naphthalate fiber and process for producing the polyethylene naphthalate fiber
TWI453311B (en) Polyethylene naphthalate fiber and its manufacturing method
JP4342056B2 (en) Polyketone fiber and production method thereof
KR102104658B1 (en) HIGH PERFORMANCE POLYAMIDE, SPINNING DOPE COMPOSITION and MOLD COMPRISING THEREOF
JP5536904B2 (en) Aromatic diamine and method for producing the same, aramid fiber and method for producing the same
JP4118721B2 (en) Method for producing polyketone fiber
KR102401622B1 (en) Semi-aromatic polyamide fibers and method for producing the same
JP2005307403A (en) Polybenzobisoxazole fiber excellent in spinnability
JP5503055B2 (en) Para-type wholly aromatic copolyamide drawn fiber and method for producing the same
JP2004091969A (en) Method for producing polyketone cord
JPH11241281A (en) Tire cord and tire
JP2011047088A (en) Para-oriented wholly aromatic copolyamide fiber and method for producing the same
JP2005232598A (en) Process for producing dense meta-type aromatic polyamide fiber
KR100494063B1 (en) Polyvinyl alcohol fiber for the reinforcement of tire and method for the production of the same
JP4563925B2 (en) Method for producing aromatic copolyamide fiber
JP4242408B2 (en) Manufacturing method of polyamide fiber
JP2006001285A (en) Fiber-reinforced composite material
JP4439745B2 (en) Method for producing polyketone fiber
JP6588259B2 (en) Polyamide fiber for transmission belt, and cord, woven fabric, and transmission belt using the same

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070410

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090807

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090820

A761 Written withdrawal of application

Free format text: JAPANESE INTERMEDIATE CODE: A761

Effective date: 20091016