JP2000199183A - Acrylonitrile fiber for producing carbon fiber - Google Patents
Acrylonitrile fiber for producing carbon fiberInfo
- Publication number
- JP2000199183A JP2000199183A JP11000150A JP15099A JP2000199183A JP 2000199183 A JP2000199183 A JP 2000199183A JP 11000150 A JP11000150 A JP 11000150A JP 15099 A JP15099 A JP 15099A JP 2000199183 A JP2000199183 A JP 2000199183A
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- component
- acrylonitrile
- carbon fiber
- oil
- 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
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 89
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 63
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 63
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 title claims abstract description 44
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 229920013822 aminosilicone Polymers 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 claims abstract description 15
- 150000002148 esters Chemical class 0.000 claims abstract description 10
- 125000003118 aryl group Chemical group 0.000 claims abstract description 9
- 229920006015 heat resistant resin Polymers 0.000 claims abstract description 8
- 229960000878 docusate sodium Drugs 0.000 claims abstract description 6
- 239000000839 emulsion Substances 0.000 claims abstract description 6
- APSBXTVYXVQYAB-UHFFFAOYSA-M sodium docusate Chemical compound [Na+].CCCCC(CC)COC(=O)CC(S([O-])(=O)=O)C(=O)OCC(CC)CCCC APSBXTVYXVQYAB-UHFFFAOYSA-M 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 229920002239 polyacrylonitrile Polymers 0.000 claims abstract description 5
- 238000009987 spinning Methods 0.000 claims abstract description 5
- 238000013329 compounding Methods 0.000 claims abstract description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 14
- 239000011261 inert gas Substances 0.000 claims description 7
- 238000007380 fibre production Methods 0.000 claims description 5
- 239000003230 hygroscopic agent Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 abstract description 3
- 239000002131 composite material Substances 0.000 abstract description 2
- 239000004753 textile Substances 0.000 abstract 3
- 230000002745 absorbent Effects 0.000 abstract 1
- 239000002250 absorbent Substances 0.000 abstract 1
- 229920006240 drawn fiber Polymers 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 37
- 238000003763 carbonization Methods 0.000 description 16
- 230000008569 process Effects 0.000 description 9
- 238000004513 sizing Methods 0.000 description 9
- 229910052581 Si3N4 Inorganic materials 0.000 description 8
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 8
- 238000010304 firing Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000011156 evaluation Methods 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000005299 abrasion Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229910052814 silicon oxide Inorganic materials 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 150000003377 silicon compounds Chemical class 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- RPACBEVZENYWOL-XFULWGLBSA-M sodium;(2r)-2-[6-(4-chlorophenoxy)hexyl]oxirane-2-carboxylate Chemical compound [Na+].C=1C=C(Cl)C=CC=1OCCCCCC[C@]1(C(=O)[O-])CO1 RPACBEVZENYWOL-XFULWGLBSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 101100082993 Plasmodium falciparum (isolate 3D7) PF52 gene Proteins 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000003973 alkyl amines Chemical class 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- HBGGXOJOCNVPFY-UHFFFAOYSA-N diisononyl phthalate Chemical compound CC(C)CCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCC(C)C HBGGXOJOCNVPFY-UHFFFAOYSA-N 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
Landscapes
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Artificial Filaments (AREA)
- Inorganic Fibers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、炭素繊維製造に使
用されるアクリロニトリル繊維及びその製造方法に関す
るものである。The present invention relates to acrylonitrile fibers used for producing carbon fibers and a method for producing the same.
【0002】更に詳しくは、炭素繊維製造用アクリロニ
トリル繊維の耐炎化時の集束性と焼成段階での工程通過
性を改良し、かつ、焼成工程中に副生成物として生成す
るSi化合物が少ない特性を有する、優れた炭素繊維製
造用アクリロニトリル繊維に関するものである。More specifically, the acrylonitrile fiber for producing carbon fiber is improved in the convergence during oxidization and the processability in the sintering step, and is characterized in that the amount of Si compound generated as a by-product during the sintering step is small. The present invention relates to an excellent acrylonitrile fiber for producing carbon fiber.
【0003】[0003]
【従来技術】従来、炭素繊維製造用にアクリロニトリル
繊維を使用し、耐炎化処理及び炭素化処理を経て高性能
炭素繊維が得られることは広く知られており、工業的に
実施されている。2. Description of the Related Art Conventionally, it has been widely known that acrylonitrile fibers are used for producing carbon fibers, and high-performance carbon fibers can be obtained through oxidization treatment and carbonization treatment.
【0004】特に近年は、スポーツ・レジャー用品用途
から航空宇宙分野、特に航空機の一次構造材に用途展開
している。さらに、炭素繊維の高い比強度、比弾性の特
性を生かし、省エネルギーによる排出CO2の削減に寄
与すべく各産業界で注目・研究される素材となってい
る。これに伴い、高性能の炭素繊維が要求され、かつ炭
素繊維の性能として、取り扱い性が良好であることが要
求される。[0004] In particular, in recent years, it has been applied to the aerospace field, particularly the primary structural material of aircraft, from sports and leisure goods. Furthermore, utilizing the high specific strength and specific elasticity properties of carbon fiber, it has become a material that has been noticed and studied in various industries to contribute to the reduction of CO 2 emissions by energy saving. Along with this, high performance carbon fibers are required, and the carbon fibers are required to have good handleability.
【0005】このような、高性能炭素繊維の製造におい
て、原料繊維であるアクリロニトリル繊維の特性は目的
物である炭素繊維の性能に直接影響し、高性能でかつ取
り扱い性の改善がなされた炭素繊維用アクリロニトリル
の開発が望まれている。In the production of such a high-performance carbon fiber, the characteristics of the acrylonitrile fiber, which is the raw material fiber, directly affect the performance of the target carbon fiber, and the high-performance and improved handleability of the carbon fiber The development of acrylonitrile for use is desired.
【0006】特に原料アクリロニトリル繊維の表面耐擦
過性は、焼成後の炭素繊維の単糸切れによる、所謂毛羽
発生の防止の観点から改善が望まれる。このために、原
料アクリロニトリル繊維に集束剤(繊維油剤)を付与す
る事は知られている。この集束剤としては、当然の事な
がら耐熱性が要求され、シリコン系油剤を集束剤として
使用することは多くの報告で知られている。[0006] In particular, the surface rub resistance of the raw material acrylonitrile fiber is desired to be improved from the viewpoint of preventing the generation of so-called fluff due to breakage of a single fiber of the carbon fiber after firing. For this purpose, it is known to add a sizing agent (fiber oil agent) to raw acrylonitrile fibers. As a matter of course, the sizing agent is required to have heat resistance, and the use of a silicone oil agent as the sizing agent is known in many reports.
【0007】即ち、アクリロニトリル繊維の耐熱集束性
と耐擦過性の為に、繊維束に、アミノシリコン系油剤を
付与し、アクリロニトリル繊維に、これらの性能を付与
することは古くより知られている。(特開昭54−13
4123号、同61−167024号)。これらのシリ
コン系油剤は、耐熱性、集束性、耐擦過性の点において
優れた油剤である。That is, it has long been known that an aminosilicone-based oil agent is applied to a fiber bundle to impart these properties to the acrylonitrile fiber because of heat resistance and abrasion resistance of the acrylonitrile fiber. (Japanese Patent Laid-Open No. 54-13 / 1979)
Nos. 4123 and 61-167024). These silicone oils are excellent in heat resistance, convergence, and abrasion resistance.
【0008】しかしながら、アミノシリコン系油剤の欠
点として、炭素繊維の焼成時にアクリロニトリル繊維に
付着した油剤が揮発・分解し、焼成工程を汚染する問題
や、撥水性が高いため紡糸後の湿潤繊維に対する均一付
着性が悪い等の問題を有する。However, the disadvantages of the aminosilicone-based oil agent are that the oil agent attached to the acrylonitrile fiber during the firing of the carbon fiber is volatilized and decomposed, thereby contaminating the firing process. It has problems such as poor adhesion.
【0009】一般にアクリル系炭素繊維は、原料アクリ
ロニトリル繊維を200〜300℃の雰囲気中で酸化処
理した後、500〜1800℃の不活性雰囲気中で炭素
化処理する事によって得られるが、シリコン系油剤は、
耐炎化炉及び炭素化炉において、粒状の酸化珪素、ウイ
スカー状及び板状の窒化ケイ素の結晶が析出し、繊維通
路を、閉塞し又は狭くするという問題点がある。Generally, acrylic carbon fibers are obtained by oxidizing raw acrylonitrile fibers in an atmosphere at 200 to 300 ° C. and then carbonizing them in an inert atmosphere at 500 to 1800 ° C. Is
In the oxidation furnace and the carbonization furnace, there is a problem that granular silicon oxide, whisker-like and plate-like crystals of silicon nitride precipitate, and the fiber passages are closed or narrowed.
【0010】その結果、被処理繊維が通過する際に、繊
維が炉壁面を擦過する事により、被処理繊維の毛羽発生
の原因となる。また、板状の窒化ケイ素が炉壁面に生成
すると、容易に排除し難く、炭素化炉内温度分布のコン
トロールが困難となり、炭素繊維の品質低下を招く原因
となる。すなわち、炭素繊維の焼成は、求められる性能
に応じ、一定の温度勾配に保持された炭素化炉で処理す
ることが要求され、このため、上記の板状の窒化ケイ素
が炉壁面に生成すると、炭素化炉内温度分布のコントロ
ールの為に炭素化炉の炉心交換頻度を高くし、生産性の
低下を招くという問題を生ずる。ウイスカー状結晶は、
炭素化炉からの除去は容易であるが、脱落した針状のウ
イスカーは、炭素繊維を損傷する原因となり可及的に減
少させることが好ましい。As a result, when the fiber to be treated passes, the fiber rubs against the wall of the furnace, causing fluff of the fiber to be treated. Further, when silicon nitride in the form of a plate is formed on the wall surface of the furnace, it is difficult to remove the silicon nitride easily, it is difficult to control the temperature distribution in the carbonization furnace, and the quality of carbon fibers is reduced. That is, the firing of carbon fiber is required to be performed in a carbonization furnace maintained at a constant temperature gradient according to the required performance, and therefore, when the above-mentioned plate-like silicon nitride is generated on the furnace wall surface, In order to control the temperature distribution in the carbonization furnace, the core replacement frequency of the carbonization furnace is increased, which causes a problem that productivity is reduced. Whisker-like crystals
Although removal from the carbonization furnace is easy, the dropped needle-like whiskers cause damage to the carbon fibers and are preferably reduced as much as possible.
【0011】本発明者等の検討によると、油剤組成を適
正化することによって炭素繊維の製造工程において、通
過する温度ゾーンによって、集束剤に要求される特性が
異なり、炭素繊維製造の全焼成工程において、集束剤と
してアミノシリコン系油剤の特性が要求される温度領域
は少なく、此より低温領域では他の集束剤の特性を活用
する事によってアミノシリコン系油剤の絶対付与量を減
少させ、もって焼成炉内における酸化珪素、ウイスカー
状及び板状の窒化ケイ素結晶の析出を減少させ、繊維通
路の狭さくを遅延しうることを見出し本発明に到った。According to the study of the present inventors, in the carbon fiber production process, the characteristics required for the sizing agent differ depending on the temperature zone through which the carbon fiber is produced by optimizing the oil agent composition. In the temperature range where the properties of aminosilicone oils are required as sizing agents are small, and in the lower temperature range, the absolute application amount of aminosilicone oils is reduced by utilizing the properties of other sizing agents and firing The present invention has been found that the precipitation of silicon oxide, whisker-like and plate-like silicon nitride crystals in the furnace can be reduced, and the narrowing of the fiber passage can be delayed.
【0012】[0012]
【発明が解決しようとする課題】本発明は、アミノシリ
コン系油剤付与における利点を生かし、集束性と耐擦過
性付与効果を損なうことなく、高品位の炭素繊維を得る
ことにある。SUMMARY OF THE INVENTION An object of the present invention is to obtain a high-quality carbon fiber without deteriorating the effect of imparting convergence and abrasion resistance by taking advantage of the application of an aminosilicone-based oil agent.
【0013】また、アミノシリコン系油剤集束剤付与に
依って引き起こされる、焼成工程における上記の問題点
を解決し、工程の安定性を確保するに有る。Another object of the present invention is to solve the above-mentioned problems in the firing step caused by the application of the aminosilicone oil agent sizing agent, and to ensure the stability of the step.
【0014】本発明は、炭素繊維の製造過程において、
原料アクリロニトリル繊維に付与されたアミノシリコン
系油剤に起因して、不活性ガス雰囲気中での炭素化処理
工程における、ケイ素化合物の生成を減少させ、長期の
安定連続運転を可能にすると共に、毛羽の発生を抑え高
品質の炭素繊維を得ることを目的とする。The present invention relates to a process for producing carbon fiber,
Due to the aminosilicone-based oil agent added to the raw material acrylonitrile fiber, it reduces the production of silicon compounds in the carbonization treatment step in an inert gas atmosphere, enables long-term stable continuous operation, and reduces fluff. An object is to obtain high-quality carbon fibers by suppressing generation thereof.
【0015】[0015]
【課題を解決するための手段】前記した問題点を解決す
るための本発明は次の構成からなる。 (請求項1) 下記A成分、B成分及びC成分を含む繊
維油剤を全繊維重量に対し0.05〜1重量%付着した
ことを特徴とする炭素繊維製造用アクリロニトリル繊
維。 A成分:アミノシリコン系オイル B成分:空気中での熱処理条件が250℃×2時間で残
渣80%以上、且つ500℃×5分で残渣が10%以下
の耐熱樹脂 C成分:吸湿剤The present invention for solving the above-mentioned problems has the following construction. (1) An acrylonitrile fiber for producing carbon fiber, wherein a fiber oil containing the following A component, B component and C component is adhered in an amount of 0.05 to 1% by weight based on the total fiber weight. A component: aminosilicone oil B component: heat-resistant resin whose heat treatment condition in air is 250 ° C. × 2 hours and residue is 80% or more and 500 ° C. × 5 minutes and residue is 10% or less C component: hygroscopic agent
【0016】(請求項2)繊維油剤成分の、A成分とB
成分との配合比が下記式(1)で示される範囲であるこ
とを特徴とする請求項1記載の炭素繊維製造用アクリロ
ニトリル繊維。 B/A =1〜10 (1)(Claim 2) Component A and component B of the fiber oil component
The acrylonitrile fiber for producing carbon fiber according to claim 1, wherein the compounding ratio with the component is in a range represented by the following formula (1). B / A = 1 to 10 (1)
【0017】(請求項3)B成分が、空気中250℃で
加熱処理した後、加熱残存量が80%以上でしかも繊維
表面に液状の皮膜形成能を有する芳香族複合エステル系
誘導体であることを特徴とする請求項1及び請求項2記
載の炭素繊維製造用アクリロニトリル繊維。(Claim 3) The component B is an aromatic complex ester derivative having a residual heat content of 80% or more after heating at 250 ° C. in air and having a liquid film-forming ability on the fiber surface. The acrylonitrile fiber for producing carbon fiber according to claim 1 or 2, characterized in that:
【0018】(請求項4)C成分が、ジオクチルスルフ
ォサクシネートである請求項3記載の炭素繊維製造用ア
クリロニトリル繊維。(Claim 4) The acrylonitrile fiber for producing carbon fiber according to claim 3, wherein the component C is dioctyl sulfosuccinate.
【0019】(請求項5) アクリルニトリル重合体溶
液を紡糸、浴中延伸して得た繊維に、下記A成分、B成
分及びC成分を含む繊維油剤のエマルジョン液を付与し
次いで、乾燥し、さらにスチーム中で延伸する事を特徴
とする炭素繊維製造用アクリロニトリル繊維の製造方
法。 A成分:アミノシリコン系オイル B成分:空気中での熱処理条件が250℃×2時間で残
存率80%以上、且つ500℃×5分で残存率が10%
以下の耐熱樹脂 C成分:吸湿剤(Claim 5) An emulsion liquid of a fiber oil containing the following components A, B and C is applied to a fiber obtained by spinning an acrylonitrile polymer solution and stretching in a bath, followed by drying. A method for producing acrylonitrile fiber for producing carbon fiber, further comprising drawing in steam. A component: Aminosilicone-based oil B component: Residual rate is 80% or more at 250 ° C. × 2 hours under heat treatment in air, and 10% at 500 ° C. × 5 minutes
The following heat-resistant resin C component: hygroscopic agent
【0020】(請求項6)B成分は、不活性ガス雰囲気
中500℃で加熱処理した後、加熱残存率10%以下で
ある芳香族複合エステルであることを特徴とする請求項
5記載の炭素繊維製造用アクリロニトリル繊維の製造方
法。(6) The carbon according to (5), wherein the component B is an aromatic complex ester having a heating residual rate of 10% or less after heat treatment at 500 ° C. in an inert gas atmosphere. A method for producing acrylonitrile fiber for producing fiber.
【0021】(請求項7)B成分は、不活性ガス雰囲気
中500℃で加熱処理した後、加熱残存率が5%以下で
ある芳香族複合エステルであることを特徴とする請求項
5記載の炭素繊維製造用アクリロニトリル繊維の製造方
法。(7) The component (B) is an aromatic complex ester having a residual heat rate of 5% or less after heat treatment at 500 ° C. in an inert gas atmosphere. A method for producing acrylonitrile fiber for producing carbon fiber.
【0022】(請求項8)A,B,C成分からなる繊維
油剤の付着量が繊維に対し0.1〜1重量%であること
を特徴とする請求項5乃至請求項7記載の炭素繊維製造
用アクリロニトリル繊維の製造方法。(8) The carbon fiber according to any one of the above (5) to (7), wherein the amount of the fiber oil comprising the components A, B and C is 0.1 to 1% by weight based on the fiber. A method for producing acrylonitrile fiber for production.
【0023】[0023]
【発明の実施の形態】以下本発明について詳細に説明す
る。本発明において、アクリロニトリル繊維とは、アク
リロニトリルのホモポリマー又はコモノマーを少量含む
コポリマーからの繊維であり、コモノマーとしては、通
常知られているアクリル酸、メタクリル酸、イタコン
酸、及びこれらの塩類などを0.1〜9.0%共重合し
たコポリマーが好ましく用いられる。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. In the present invention, the acrylonitrile fiber is a fiber from a homopolymer of acrylonitrile or a copolymer containing a small amount of a comonomer. Examples of the comonomer include acrylic acid, methacrylic acid, itaconic acid, and salts thereof. A copolymer obtained by copolymerizing 0.1 to 9.0% is preferably used.
【0024】本発明に於いて、A成分のアミノシリコン
系油剤は、炭素繊維製造用アクリロニトリル繊維の集束
剤(油剤)として広く知られているものが使用できる。
特に、下記構造式(化1)に示されるものが、耐炎化の
時点での集束効果より好ましいIn the present invention, as the aminosilicone oil agent of the component A, those widely known as sizing agents (oil agents) for acrylonitrile fibers for producing carbon fibers can be used.
In particular, those represented by the following structural formula (Formula 1) are more preferable than the focusing effect at the time of flame resistance.
【0025】[0025]
【化1】 Embedded image
【0026】[B成分]B成分は、250℃×1時間で
残存率80%以上で、しかも500℃×1分で残存率1
0重量%以下となる耐熱樹脂である。特に250℃〜3
00℃において、繊維表面に皮膜を形成する樹脂であ
る。このような条件を満足する樹脂としては、具体的に
は、例えば高分子量の複合エステルである。特に芳香族
複合エステルが好適である。具体的には下記の構造式
(化2)を持つ芳香族エステルを主成分とする化合物で
ある。このものは特再平9−809474号公報で知ら
れている。[Component B] The component B has a residual ratio of 80% or more at 250 ° C. × 1 hour, and a residual ratio of 1 at 500 ° C. × 1 minute.
It is a heat-resistant resin of 0% by weight or less. Especially 250 ° C ~ 3
A resin that forms a film on the fiber surface at 00 ° C. Specifically, the resin satisfying such conditions is, for example, a high molecular weight composite ester. Particularly, an aromatic complex ester is preferable. Specifically, it is a compound mainly composed of an aromatic ester having the following structural formula (Formula 2). This is known from Japanese Patent Publication No. 9-809474.
【0027】[0027]
【化2】 Embedded image
【0028】本発明において、加熱残存率は次のように
して測定される。樹脂約1gを秤量し、熱風循環式乾燥
機或いは電気炉を用いて所定温度で熱処理した後、秤量
し残存率を求める。但し、所定温度までの昇温速度は2
0℃/分である。本発明に使用したB成分の上記方法に
よる加熱残存量を下表1に示す。In the present invention, the residual heating ratio is measured as follows. About 1 g of the resin is weighed and heat-treated at a predetermined temperature using a hot air circulation dryer or an electric furnace, and then weighed to obtain a residual ratio. However, the heating rate up to the predetermined temperature is 2
0 ° C./min. The heating residual amount of the component B used in the present invention by the above method is shown in Table 1 below.
【0029】[0029]
【表1】 [Table 1]
【0030】B成分の混合割合はA成分に対し1〜10
と成ることが好ましく、さらに好ましくは、1〜5であ
る。The mixing ratio of the component B is 1 to 10 with respect to the component A.
And more preferably 1 to 5.
【0031】[C成分]A成分であるアミノシリコン系
油剤は、撥水性であるため、アクリロニトリル繊維をス
チーム延伸する場合、繊維の水分率が不均一になり、延
伸処理が不均一になるなどの不都合がある。このため、
吸湿性成分を加えることが好ましい。[Component C] The aminosilicone-based oil agent which is the component A is water-repellent. Therefore, when acrylonitrile fiber is subjected to steam drawing, the moisture content of the fiber becomes non-uniform, and the drawing process becomes non-uniform. There are inconveniences. For this reason,
It is preferred to add a hygroscopic component.
【0032】吸湿成分としては、ジオクチルスルフォサ
クシネートNa塩、POEアルキルエーテルやアルキル
アミンオキサイド等が挙げられる。特には、吸湿能力に
優れる点からジオクチルスルフォサクシネートNa塩が
好ましい。Examples of the moisture absorbing component include dioctyl sulfosuccinate Na salt, POE alkyl ether, alkylamine oxide and the like. In particular, dioctyl sulfosuccinate Na salt is preferred from the viewpoint of excellent moisture absorbing ability.
【0033】吸湿性成分の配合比は、A成分に対し0.
1〜2.0の比率が好ましく、さらに好ましくは0.1
〜0.5の比率である。The mixing ratio of the moisture-absorbing component is 0.1% with respect to the component A.
A ratio of 1 to 2.0 is preferred, more preferably 0.1
0.50.5.
【0034】本発明ではA/B/C成分の配合比率を適
正化することで、CF生産性を低下させることなく、品
質の良いCFが製造できるプリカーサーの製造に至っ
た。In the present invention, by optimizing the mixing ratio of the A / B / C components, a precursor that can produce high-quality CF without lowering the CF productivity has been produced.
【0035】油剤の繊維に対する付与の割合は、0.1
〜1%が好ましく、さらに好ましくは0.15〜0.5
%である。油剤付着量が0.1%より少ない場合は、耐
炎化工程での集束性が劣り、該当工程以降での工程通過
性が著しく損なわれ、1%超の付着量であると炭素化工
程での窒化珪素発生量が著しく増加し、炭素繊維の品位
を著しく損ねる。The ratio of the oil agent to the fiber is 0.1%.
To 1%, more preferably 0.15 to 0.5
%. If the amount of the oil agent is less than 0.1%, the convergence in the flame-proofing step is inferior, and the passability of the step after the corresponding step is significantly impaired. The amount of silicon nitride generated significantly increases, and the quality of the carbon fiber is significantly impaired.
【0036】[製造方法]これらの油剤のアクリロニト
リル繊維に対する付与の手段は、湿式紡糸又は紡糸原液
を一旦気体中に吐出後凝固浴中に導入し、浴中延伸した
後、該ゲル状のアクリロニトリル繊維に本発明油剤を付
与せしめる。この後、乾燥、延伸処理し、炭素繊維前駆
体繊維を得る。通常の油剤付与方法は、混合油剤のエマ
ルジョンに該ゲル状繊維を浸漬せしめることで付与され
る。 本発明の場合、アミノシリコーン油剤(A成分)
の特性から浴温度40℃以下、また、B成分の溶液安定
性は10℃以上が好ましいことから、この油剤の付与温
度は、10〜40℃の範囲内である。10℃より低いと
溶液の層分離やマイグレーションが起こり易く、繊維に
対して不均一な付着を引き起こす。一方40℃を超える
と、エマルジョンのミセルが破壊され、溶液中にスカム
が発生しやすくなる。この様にして得られた前駆体繊維
の物性は、下記に示す通りの良好な炭素繊維を得る為に
必要な物性を満足するものである。[Production Method] The means for applying these oils to acrylonitrile fiber is as follows: wet spinning or spinning stock solution is once discharged into a gas, then introduced into a coagulation bath, stretched in the bath, and then subjected to the gel-like acrylonitrile fiber. Of the present invention. Thereafter, drying and drawing are performed to obtain carbon fiber precursor fibers. The usual oil agent application method is applied by immersing the gel fiber in an emulsion of a mixed oil agent. In the case of the present invention, an amino silicone oil agent (component A)
Since the bath temperature is preferably 40 ° C. or less and the solution stability of the component B is preferably 10 ° C. or more from the characteristics of the above, the temperature at which the oil agent is applied is in the range of 10 to 40 ° C. When the temperature is lower than 10 ° C., layer separation and migration of the solution are apt to occur, causing non-uniform adhesion to the fiber. On the other hand, when the temperature exceeds 40 ° C., the micelles of the emulsion are broken, and scum tends to be generated in the solution. The physical properties of the precursor fiber obtained in this way satisfy the physical properties necessary for obtaining good carbon fibers as shown below.
【0037】繊 度:0.3〜1.5d 強 度: 7 g/d以上 伸 度: 11 %以上 X線配向度: 90%以上Fineness: 0.3 to 1.5 d Strength: 7 g / d or more Elongation: 11% or more X-ray orientation degree: 90% or more
【0038】本発明のアクリロニトリル系繊維を用いて
の炭素繊維の製造は、通常採用されている方法が採用で
きる。即ち、空気中200〜300℃で耐炎化した後、
不活性ガス中300〜2000℃で炭素化し、表面処理
を施した後、サイジング剤を付与し、該炭素繊維を得
る。得られた炭素繊維は、良好な物性さらに良好な取り
扱い性を示し、本発明の目的を満足しうる製造が可能と
なる。For the production of carbon fiber using the acrylonitrile fiber of the present invention, a commonly employed method can be employed. That is, after flame resistance at 200 to 300 ° C. in air,
After carbonization at 300 to 2000 ° C. in an inert gas and surface treatment, a sizing agent is applied to obtain carbon fibers. The obtained carbon fibers exhibit good physical properties and good handling properties, and can be manufactured to satisfy the object of the present invention.
【0039】[0039]
【実施例】以下、本発明を実施例より具体的に説明す
る。尚、実施例中の付着油脂量、耐炎化糸の集束性、炭
素繊維の毛羽量、炭素化工程での窒化珪素発生量は次の
方法に準じた。The present invention will be described below more specifically with reference to examples. In the examples, the amount of oils and fats adhered, the bundling property of the oxidized yarn, the amount of fluff of carbon fibers, and the amount of silicon nitride generated in the carbonization step were according to the following methods.
【0040】(1)付着油脂量 エタノールとベンゼンの混合液により炭素繊維製造用ア
クリロニトリル繊維より油剤を抽出した後、油剤の含ま
れる溶液を乾燥し、得られた固形分を秤量することによ
って得られる。(1) Amount of attached fats and oils After extracting an oil agent from acrylonitrile fiber for producing carbon fiber with a mixed solution of ethanol and benzene, the solution containing the oil agent is dried, and the obtained solid is weighed. .
【0041】(2)耐炎化糸の集束性 空気中250℃で炭素繊維製造用アクリロニトリル繊維
束(単繊維12,000本)を耐炎化せしめた後、該繊
維束を3mmに切断し約100ccのアセトンに入れ、
1分間超音波をあてて、分散せしめた後、接着している
モノフィラメント数を顕微鏡を用いて測定する。集束性
の評価は下表2に基づいて行う。(2) Bundleability of Flame-Retardant Yarn After acrylonitrile fiber bundles (12,000 single fibers) for carbon fiber production were made to be flame-resistant at 250 ° C. in the air, the fiber bundle was cut into 3 mm and about 100 cc. Put in acetone,
After applying ultrasonic waves for 1 minute to disperse, the number of adhered monofilaments is measured using a microscope. The convergence is evaluated based on Table 2 below.
【0042】[0042]
【表2】 [Table 2]
【0043】(3)炭素繊維の毛羽量 サイズ処理された炭素繊維ストランドをウレタンスポン
ジ(寸法32mm×64mm×10mm、重さ約0.2
5g)2枚の間に挟み、125gのおもりをウレタンス
ポンジ全面にかかるようにのせ、炭素繊維ストランドを
15m/minの速度で2分間通過させたときのスポン
ジに付着した毛羽の重量を毛羽量とした。(3) Fuzz amount of carbon fiber A sized carbon fiber strand is coated with a urethane sponge (dimensions 32 mm x 64 mm x 10 mm, weight about 0.2
5g) sandwiched between the two pieces, put a weight of 125g over the entire surface of the urethane sponge, and let the weight of the fuzz adhering to the sponge when the carbon fiber strand pass at a speed of 15m / min for 2 minutes be the fluff quantity. did.
【0044】(4)炭素化工程でのSi化合物発生量 耐炎化工程、炭素化工程でそれぞれできるSi化合物を
収集し、アクリロニトリル繊維1トン当たりに発生する
Si化合物重量を測定し、発生量とした。(4) Amount of Si Compound Generated in Carbonization Step The Si compounds generated in each of the flame-proofing step and the carbonization step were collected, and the weight of the Si compound generated per ton of acrylonitrile fiber was measured to determine the amount generated. .
【0045】[0045]
【実施例1】アクリロニトリル重合体を湿式紡糸した
後、水洗、浴中延伸をした後の水膨潤状態の繊維束をA
成分(アミノシリコーン 竹本油脂株式会社製 BS−
379)を7g/l、C成分(ジオクチルスルフォサク
シネート)を3g/l、B成分(芳香族複合エステル
松本油脂株式会社 BFー42)を10g/l含むエマ
ルジョン溶液に浸漬した後、乾燥・緻密化し、スチーム
延伸して水分率38%の繊維を得た。この繊維を250
℃で耐炎化した後、窒素中1400℃で炭素化し、炭素
繊維を得た。得られた炭素繊維の評価を表3に示す。Example 1 After the acrylonitrile polymer was wet-spun, washed with water and stretched in a bath, the water-swelled fiber bundle was treated as A.
Ingredient (amino silicone Takemoto Yushi Co., Ltd. BS-
379), 7 g / l, C component (dioctyl sulfosuccinate) 3 g / l, B component (aromatic complex ester)
After immersion in an emulsion solution containing 10 g / l of Matsumoto Yushi Co., Ltd., 10 g / l, it was dried, densified, and steam-stretched to obtain a fiber having a water content of 38%. 250 of this fiber
After oxidization at 1400C, carbonization was performed in nitrogen at 1400C to obtain carbon fibers. Table 3 shows the evaluation of the obtained carbon fibers.
【0046】[0046]
【実施例2】前記実施例1の油剤付着量を0.70にし
たことを除いて前記実施例1で実施したのと同様にして
炭素繊維を得た。得られた炭素繊維の評価を表3に示
す。Example 2 A carbon fiber was obtained in the same manner as in Example 1 except that the amount of oil applied was changed to 0.70. Table 3 shows the evaluation of the obtained carbon fibers.
【0047】[0047]
【実施例3】前記実施例1の油剤組成A成分を7g/
l、C成分を7g/l、B成分を6g/lにしたことを
除いて前記実施例1で実施したのと同様にして炭素繊維
を得た。得られた炭素繊維の評価を表3に示す。EXAMPLE 3 The oil component A of Example 1 was used in an amount of 7 g /
Carbon fibers were obtained in the same manner as in Example 1 except that the components 1 and C were 7 g / l and the component B was 6 g / l. Table 3 shows the evaluation of the obtained carbon fibers.
【0048】[0048]
【比較例】前記実施例1の油剤組成及び油剤付着量を表
1のようにしたことを除いて前記実施例1で実施したの
と同様にして炭素繊維を得た。得られた炭素繊維の評価
を表3、表4に示す。Comparative Example A carbon fiber was obtained in the same manner as in Example 1 except that the composition of the oil and the amount of the oil applied were as shown in Table 1. Tables 3 and 4 show the evaluation of the obtained carbon fibers.
【0049】[0049]
【表3】 [Table 3]
【0050】[0050]
【表4】 [Table 4]
【0051】[0051]
【発明の効果】本発明によると、アミノシリコン系油剤
の繊維に対する付着量を減少させることが出来、その結
果、CF工程における酸化珪素及び、窒化ケイ素の発生
量を低く押さえることができ、高強度でかつ取り扱い性
に優れた炭素繊維を得ることができる。本発明による
と、炭素繊維製造工程の内、耐炎化工程においては、A
成分のアミノシリコン油剤とB成分の耐熱樹脂との相互
作用によって繊維束は集束され、工程を通じ円滑に通過
し、より高温の不活性ガス中での炭素化工程において
は、B成分の耐熱樹脂は速やかに分解し、アミノシリコ
ン系油剤のみの集束作用によって、工程中の繊維は集束
される。According to the present invention, it is possible to reduce the amount of the aminosilicone-based oil agent adhering to the fibers. As a result, it is possible to reduce the amount of silicon oxide and silicon nitride generated in the CF process, and to obtain high strength. And a carbon fiber excellent in handleability can be obtained. According to the present invention, in the flameproofing step of the carbon fiber manufacturing process, A
The fiber bundle is bundled by the interaction between the amino silicone oil agent of the component and the heat-resistant resin of the component B, smoothly passes through the process, and in the carbonization process in a higher temperature inert gas, the heat-resistant resin of the component B is The fibers in the process are rapidly decomposed and are bunched by the bunching action of only the aminosilicone-based oil agent.
【0052】その結果、アクリロニトリル繊維に付与さ
れているアミノシリコン系油剤は単独付与の場合より付
与量が少なくても炭素化工程の集束効果を得ることが出
来、結果的にシリコン化合物の発生量が少なくなり、炭
素化工程の長期間連続運転が可能となる。As a result, even if the amount of the aminosilicone oil agent applied to the acrylonitrile fiber is smaller than that in the case where the acrylonitrile fiber is applied alone, the focusing effect of the carbonization step can be obtained, and as a result, the amount of the silicon compound generated can be reduced Thus, the carbonization process can be continuously operated for a long period of time.
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4L033 AA05 AB01 AC05 BA28 BA29 CA59 4L035 BB03 BB60 BB61 BB66 BB69 BB80 BB85 FF01 MB03 MB04 MB06 4L037 CS03 PA53 PA55 PA67 PA69 PA70 PC05 PF29 PF32 PF45 PF52 PS02 UA20 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4L033 AA05 AB01 AC05 BA28 BA29 CA59 4L035 BB03 BB60 BB61 BB66 BB69 BB80 BB85 FF01 MB03 MB04 MB06 4L037 CS03 PA53 PA55 PA67 PA69 PA70 PC05 PF29 PF32 PF45 PF52 PS02 UA
Claims (8)
油剤を全繊維重量に対し0.05〜1重量%付着したこ
とを特徴とする炭素繊維製造用アクリロニトリル繊維。 A成分:アミノシリコン系オイル B成分:空気中での熱処理条件が250℃×2時間で残
渣80%以上、且つ500℃×5分で残渣が10%以下
の耐熱樹脂 C成分:吸湿剤An acrylonitrile fiber for producing carbon fiber, wherein a fiber oil containing the following components A, B and C is adhered in an amount of 0.05 to 1% by weight based on the total fiber weight. A component: aminosilicone oil B component: heat-resistant resin whose heat treatment condition in air is 250 ° C. × 2 hours and residue is 80% or more and 500 ° C. × 5 minutes and residue is 10% or less C component: hygroscopic agent
比が下記式(1)で示される範囲であることを特徴とす
る請求項1記載の炭素繊維製造用アクリロニトリル繊
維。 B/A =1〜10 (1)2. The acrylonitrile fiber for producing carbon fiber according to claim 1, wherein the compounding ratio of the component A and the component B of the fiber oil component is in a range represented by the following formula (1). B / A = 1 to 10 (1)
後、加熱残存量が80%以上でしかも繊維表面に液状の
皮膜形成能を有する芳香族複合エステル系誘導体である
ことを特徴とする請求項1及び請求項2記載の炭素繊維
製造用アクリロニトリル繊維。3. The component B is an aromatic complex ester derivative having a residual heat amount of 80% or more after heating at 250 ° C. in air and having a liquid film-forming ability on the fiber surface. The acrylonitrile fiber for producing carbon fiber according to claim 1 or claim 2.
トである請求項3記載の炭素繊維製造用アクリロニトリ
ル繊維。4. The acrylonitrile fiber for producing carbon fiber according to claim 3, wherein the component C is dioctyl sulfosuccinate.
中延伸して得た繊維に、下記A成分、B成分及びC成分
を含む繊維油剤のエマルジョン液を付与し次いで、乾燥
し、さらにスチーム中で延伸する事を特徴とする炭素繊
維製造用アクリロニトリル繊維の製造方法。 A成分:アミノシリコン系オイル B成分:空気中での熱処理条件が250℃×2時間で残
存率80%以上、且つ500℃×5分で残存率が10%
以下の耐熱樹脂 C成分:吸湿剤5. A fiber obtained by spinning an acrylonitrile polymer solution and drawing in a bath is provided with an emulsion of a fiber oil containing the following components A, B and C, dried, and then dried. And a method for producing acrylonitrile fiber for producing carbon fiber. A component: Aminosilicone-based oil B component: Residual rate is 80% or more at 250 ° C. × 2 hours under heat treatment in air, and 10% at 500 ° C. × 5 minutes
The following heat-resistant resin C component: hygroscopic agent
加熱処理した後、加熱残存率10%以下である芳香族複
合エステルであることを特徴とする請求項5記載の炭素
繊維製造用アクリロニトリル繊維の製造方法。6. The carbon fiber production method according to claim 5, wherein the component B is an aromatic complex ester having a heating residual ratio of 10% or less after heat treatment at 500 ° C. in an inert gas atmosphere. A method for producing acrylonitrile fiber.
加熱処理した後、加熱残存率が5%以下である芳香族複
合エステルであることを特徴とする請求項5記載の炭素
繊維製造用アクリロニトリル繊維の製造方法。7. The carbon fiber production according to claim 5, wherein the component B is an aromatic complex ester having a residual heat rate of 5% or less after heat treatment at 500 ° C. in an inert gas atmosphere. Of producing acrylonitrile fiber for use.
が繊維に対し0.1〜1重量%であることを特徴とする
請求項5乃至請求項7記載の炭素繊維製造用アクリロニ
トリル繊維の製造方法。8. The acrylonitrile for carbon fiber production according to claim 5, wherein the amount of the fiber oil agent comprising the components A, B and C is 0.1 to 1% by weight based on the fiber. Fiber manufacturing method.
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JP2002266239A (en) * | 2001-03-12 | 2002-09-18 | Mitsubishi Rayon Co Ltd | Carbon fiber precursor acrylic fiber and method for producing the same and oil agent composition |
JP2002317335A (en) * | 2001-04-20 | 2002-10-31 | Mitsubishi Rayon Co Ltd | Carbon fiber and method for producing the same |
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