JP2002155428A - Method for producing carbonized polyacrylonitrile - Google Patents
Method for producing carbonized polyacrylonitrileInfo
- Publication number
- JP2002155428A JP2002155428A JP2000349244A JP2000349244A JP2002155428A JP 2002155428 A JP2002155428 A JP 2002155428A JP 2000349244 A JP2000349244 A JP 2000349244A JP 2000349244 A JP2000349244 A JP 2000349244A JP 2002155428 A JP2002155428 A JP 2002155428A
- Authority
- JP
- Japan
- Prior art keywords
- polyacrylonitrile
- carbonized
- producing
- resin
- flammable
- 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
Landscapes
- Treatments Of Macromolecular Shaped Articles (AREA)
- Artificial Filaments (AREA)
- Inorganic Fibers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】ポリアクリロニトリルを不炎
化処理する技術は、これまで繊維の形態で不炎化繊維と
して取り組まれている。BACKGROUND OF THE INVENTION The art of flame retarding polyacrylonitrile has been addressed as fiberized fibers in the form of fibers.
【0002】その得られた不炎化繊維はまた、炭素繊維
を製造する中間体として位置付けられ、不炎化繊維を更
に焼成することより高性能な炭素繊維を得る目的で技術
展開がなされて来た。[0002] The obtained non-flammable fiber is also regarded as an intermediate for producing carbon fiber, and its technology has been developed for the purpose of obtaining high-performance carbon fiber by further firing the non-flammable fiber. Was.
【0003】なお、本願明細書において、不炎化処理と
は、当該対象に自己消火性を付与する処理を意味し、通
常、酸化、環化、架橋化等の各種の化学反応が関与す
る。また、このような自己消化性を有する物を不炎化体
という。[0003] In the specification of the present application, the flameproofing treatment means a treatment for imparting self-extinguishing property to the object, and usually involves various chemical reactions such as oxidation, cyclization, and crosslinking. In addition, a substance having such self-digestibility is referred to as an inflammable substance.
【0004】これまで取り組まれてきた炭素化繊維を製
造する技術としては、例えば、特開平5−339813
号公報には、ポリアクリロニトリルのみからなるホモポ
リマーでは、酸化、環化および架橋化反応が遅いために
アクリル酸などのカルボン酸基含有ビニルモノマーを共
重合させて反応を促進させ効率的に不炎化繊維を得る方
法が記載されている。[0004] As a technique for producing carbonized fiber which has been addressed so far, for example, Japanese Unexamined Patent Publication No. 5-339913
According to the publication, a homopolymer consisting of only polyacrylonitrile has a slow oxidation, cyclization and cross-linking reaction, so that a carboxylic acid group-containing vinyl monomer such as acrylic acid is copolymerized to promote the reaction and efficiently produce a flame retardant. A method for obtaining modified fibers is described.
【0005】しかしながら、酸化反応には酸素あるいは
空気を必要としており、依然300℃に近い高温が必要
とされているし、アクリロニトリル以外の共重合成分に
より、繊維としての物性や、後の炭素繊維の物性に悪影
響を及ぼすことが懸念されている。[0005] However, the oxidation reaction requires oxygen or air, and still requires a high temperature close to 300 ° C. The copolymerization component other than acrylonitrile causes the physical properties of the fiber and the carbon fiber It is feared that physical properties are adversely affected.
【0006】更には、酸素や空気の存在下での反応を必
須とするために、後の炭素繊維化での収率を下げる要因
になっている。Further, since the reaction in the presence of oxygen or air is indispensable, this is a factor that lowers the yield in the subsequent carbon fiber formation.
【0007】上記と同様な目的で例えば、Carbon
Vol.29,No.8,pp.1081−1090
(1991)には、ポリアクリロニトリルに塩基性物質
や求核剤を環化助剤として処理せしめ環化を促進する方
法が紹介されている。For the same purpose as described above, for example, Carbon
Vol. 29, No. 8, pp. 1081-1090
(1991) introduces a method of promoting cyclization by treating polyacrylonitrile with a basic substance or a nucleophile as a cyclizing aid.
【0008】例えば、J.Mats.Sci.Lett
s.7,pp.628(1988)には、過マンガン酸
カリウム水溶液でポリアクリロニトリル繊維を処理し環
化を促進することが報告されている。For example, in J. Mats. Sci. Lett
s. 7, pp. 628 (1988) reports that a polyacrylonitrile fiber is treated with an aqueous solution of potassium permanganate to promote cyclization.
【0009】しかしながら、実用に到る効果的な方法が
見出されていないのが実状である。However, in reality, no effective method for practical use has been found.
【0010】[0010]
【発明が解決しようとする課題】本願発明の目的は、効
率的にアクリロニトリル樹脂の炭素化体を製造する方法
を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for efficiently producing a carbonized acrylonitrile resin.
【0011】[0011]
【課題を解決するための手段】我々は、ポリアクリロニ
トリルの不炎化、炭素化の一連の検討の中で、上記のよ
うな課題に対して鋭意検討した結果、まず、ポリアクリ
ロニトリルのホモポリマーをヨウ素ガスと接触させ、低
い温度条件下においてすみやかに不炎化できる方法を見
出した。更に該不炎化体を焼成することにより従来の炭
素化体製造方法には無い特徴として炭化収率が高いこと
を見出し、本願発明に到った。Means for Solving the Problems In a series of studies on the nonflammability and carbonization of polyacrylonitrile, we conducted intensive studies on the above-mentioned problems, and as a result, we first obtained a homopolymer of polyacrylonitrile. The present inventors have found a method capable of promptly making a flame non-flammable under low temperature conditions by contacting with iodine gas. Further, by calcining the nonflammable body, it has been found that a carbonization yield is high as a feature not found in the conventional carbonized body production method, and the present invention has been achieved.
【0012】すなわち本願発明は、下記の通り、ポリア
クリロニトリル樹脂をヨウ素ガスと接触させることを特
徴とするポリアクリロニトリル系炭素化体の製造方法で
ある。That is, the present invention is a method for producing a polyacrylonitrile-based carbonized material, which comprises contacting a polyacrylonitrile resin with iodine gas as described below.
【0013】1. ポリアクリロニトリル樹脂をヨウ素
ガスと接触せしめ不炎化体とした後、300〜3000
℃の不活性ガスの雰囲気内で焼成することを特徴とする
ポリアクリロニトリル系炭素化体の製造方法。1. The polyacrylonitrile resin is brought into contact with iodine gas to form a non-flammable body, and then 300 to 3000
A method for producing a polyacrylonitrile-based carbonized material, characterized by firing in an atmosphere of an inert gas at a temperature of ° C.
【0014】2. ポリアクリロニトリル樹脂中のアク
リロニトリルモノマー成分が80〜100モル%である
ことを特徴とする上記1記載のポリアクリロニトリル系
炭素化体の製造方法。2. 2. The method for producing a polyacrylonitrile-based carbonized product according to the above item 1, wherein the acrylonitrile monomer component in the polyacrylonitrile resin is 80 to 100 mol%.
【0015】3. ポリアクリロニトリル樹脂の形態が
繊維状であることを特徴とする上記1または2記載のポ
リアクリロニトリル系炭素化体の製造方法。3. 3. The method for producing a polyacrylonitrile-based carbonized product according to the above item 1 or 2, wherein the form of the polyacrylonitrile resin is fibrous.
【0016】4. ポリアクリロニトリル樹脂の形態が
フィルム状であることを特徴とする上記1または2記載
のポリアクリロニトリル系炭素化体の製造方法。4. 3. The method for producing a polyacrylonitrile-based carbonized product according to the above item 1 or 2, wherein the polyacrylonitrile resin is in the form of a film.
【0017】[0017]
【発明の実施の形態】以下に本願発明を詳述する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail.
【0018】本願発明においては、まず、ポリアクリロ
ニトリル樹脂をヨウ素ガス中に存在せしめて不炎化処理
することによって、炭素化体の前駆体である不炎化体を
低温で効率よく製造することができる。In the present invention, first, a polyacrylonitrile resin is made to exist in iodine gas and subjected to a nonflammable treatment to efficiently produce a nonflammable body which is a precursor of a carbonized substance at a low temperature. it can.
【0019】本願発明に用いられるポリアクリロニトリ
ル樹脂は、公知の方法で調製される、アクリロニトリル
モノマー成分が80〜100モル%からなるポリマーを
用いることができる。As the polyacrylonitrile resin used in the present invention, a polymer prepared by a known method and containing 80 to 100 mol% of an acrylonitrile monomer component can be used.
【0020】また、従来技術の酸化促進効果を持たせる
ためにアクリロニトリルモノマー以外に他のモノマーを
20〜0モル%を共重合せしめて得られる共重合ポリア
クリロニトリルも用いることができる。In addition to the acrylonitrile monomer, a copolymerized polyacrylonitrile obtained by copolymerizing 20 to 0 mol% of another monomer other than the acrylonitrile monomer can be used in order to have the oxidation promoting effect of the prior art.
【0021】好ましくはアクリロニトリル100モル%
から重合せしめて調製されるポリアクリロニトリル樹脂
である。Preferably, acrylonitrile 100 mol%
Is a polyacrylonitrile resin prepared by polymerization from
【0022】本願発明においては、上記ポリアクリロニ
トリル樹脂をヨウ素ガスと接触処理する。In the present invention, the above-mentioned polyacrylonitrile resin is subjected to contact treatment with iodine gas.
【0023】本願発明に用いられるヨウ素ガスは、公知
の方法で調製されるガスを用いることができるが、純度
の高いヨウ素を用いることが望ましい。As the iodine gas used in the present invention, a gas prepared by a known method can be used, but it is preferable to use iodine having high purity.
【0024】純度が低いと目的の不炎化体が得られなく
なったり、不炎化体の力学物性が低下するため、好まし
くない。好ましくは99重量%以上、より好ましくは9
9.5重量%以上、更に好ましくは99.9重量%以上
の純度のヨウ素を使用する。If the purity is low, the desired non-flammable product cannot be obtained, or the mechanical properties of the non-flammable product deteriorate, which is not preferable. Preferably at least 99% by weight, more preferably 9% by weight.
Iodine having a purity of 9.5% by weight or more, more preferably 99.9% by weight or more, is used.
【0025】固体ヨウ素は、加熱することによりガス化
せしめポリアクリロニトリル樹脂が存在する系内へ導入
することが望ましい。It is desirable that the solid iodine be gasified by heating and introduced into the system in which the polyacrylonitrile resin is present.
【0026】以下、ポリアクリロニトリル樹脂をヨウ素
ガスにて処理する条件を詳述する。Hereinafter, conditions for treating the polyacrylonitrile resin with iodine gas will be described in detail.
【0027】不炎化処理の温度条件としては、0〜50
0℃の温度条件が好ましい。温度がこの範囲を外れる
と、目的の不炎化体が得られなくなったり、不炎化体の
力学物性が低下するため好ましくない。より好ましくは
100〜450℃の範囲である。更に好ましくは200
〜400℃の範囲である。The temperature conditions of the non-flammable treatment are from 0 to 50.
A temperature condition of 0 ° C. is preferred. If the temperature is out of this range, the desired non-flammable body cannot be obtained, or the mechanical properties of the non-flammable body deteriorate, which is not preferable. It is more preferably in the range of 100 to 450 ° C. More preferably 200
~ 400 ° C.
【0028】ヨウ素ガスは、不活性ガス、酸素、空気な
どとの混合ガスの状態で用いても何ら問題はないが、そ
の際にはヨウ素ガス濃度を気体全体のモル量に対して、
1〜100モル%の間に保つことが好ましい。濃度がこ
の範囲を外れると、目的の不炎化体が得られなくなった
り、不炎化体の力学物性が低下するため好ましくない。There is no problem if the iodine gas is used in a mixed gas state with an inert gas, oxygen, air or the like.
It is preferred to keep it between 1 and 100 mol%. If the concentration is outside this range, the desired non-flammable product cannot be obtained, or the mechanical properties of the non-flammable product deteriorate, which is not preferable.
【0029】また、その際の圧力条件としては、用いる
混合ガスの種類にもよるが、実質的には、全圧として1
Pa〜100MPaの範囲である。接触時間は特に制限
はないが、好ましくは1秒から10時間である。The pressure condition at that time depends on the kind of the mixed gas used, but is substantially 1% as the total pressure.
The range is from Pa to 100 MPa. The contact time is not particularly limited, but is preferably 1 second to 10 hours.
【0030】なお、上記温度は、ポリアクリロニトリル
樹脂とガスとの双方の温度を意味するが、両者が同一で
ある必要はなく、また、たとえば一方の温度が両者の接
触前に好ましい温度範囲を逸脱していても、両者の接触
の結果、好ましい温度範囲に入れば十分である。むし
ろ、たとえば一方の温度が両者の接触前に好ましい温度
範囲を逸脱していても両者の接触の結果、不炎化体が得
られれば、好ましい温度範囲に入ったものと推察するこ
とができる。故に、加熱されたヨウ素ガスを加熱されて
いないポリアクリロニトリルと接触させることによっ
て、優れた不炎化体を得ることも可能である。The above-mentioned temperature means the temperature of both the polyacrylonitrile resin and the gas, but it is not necessary that they are the same, and for example, one of the temperatures may deviate from the preferable temperature range before contacting the two. Even if it does, it is sufficient that the temperature falls within a preferable temperature range as a result of the contact between the two. Rather, for example, even if one of the temperatures deviates from the preferable temperature range before the contact between the two, if the non-flammable body is obtained as a result of the contact between the two, it can be inferred that the temperature has entered the preferable temperature range. Therefore, by bringing the heated iodine gas into contact with the non-heated polyacrylonitrile, it is also possible to obtain an excellent non-flammable body.
【0031】本願発明では、上記のようにして得られた
ポリアクリロニトリル不炎化体を300〜3000℃の
不活性ガスが充填された雰囲気内で焼成することによ
り、炭素化体を得る。In the present invention, the carbonized product is obtained by firing the non-flammable polyacrylonitrile obtained as described above in an atmosphere filled with an inert gas at 300 to 3000 ° C.
【0032】焼成温度は、300〜3000℃が好まし
い。より好ましくは400〜2900℃、更に好ましく
は500〜2800℃の範囲である。また昇温の方法
は、段階的に上げても、連続的に上げても何ら問題が無
い。なお、より均一な炭素化体を得るには連続的に上げ
た方が好ましい場合が多い。The firing temperature is preferably from 300 to 3000.degree. The temperature is more preferably in the range of 400 to 2900 ° C, and still more preferably in the range of 500 to 2800 ° C. In addition, there is no problem in raising the temperature either stepwise or continuously. In order to obtain a more uniform carbonized product, it is often preferable to continuously increase the carbonized product.
【0033】目的とする炭素化体の形態が繊維の場合に
は、昇温の際に引張応力を作用させて収縮あるいは伸張
の具合を制御することは、何ら問題無く行うことができ
る。When the desired form of the carbonized product is a fiber, it is possible to control the degree of contraction or expansion by applying a tensile stress at the time of raising the temperature without any problem.
【0034】焼成に用いる不活性ガスとしては、アルゴ
ン,窒素などを用いることが好ましい。As the inert gas used for firing, it is preferable to use argon, nitrogen, or the like.
【0035】本願発明の炭素化体の製造における形態に
は制限はないが、本願発明は、形態が繊維状あるいはフ
ィルム状のポリアクリロニトリル系炭素化体を得るため
の製造方法として有用である。The form in the production of the carbonized product of the present invention is not limited, but the present invention is useful as a production method for obtaining a polyacrylonitrile-based carbonized product in a fibrous or film form.
【0036】すなわち、ポリアクリロニトリル樹脂を一
度可溶性の有機溶媒に溶解せしめたのち、繊維状、フィ
ルム状あるいは他の形態に成形せしめ、これをヨウ素ガ
ス処理することで、目的の繊維状あるいはフィルム状の
炭素化体を得ることができる。That is, after the polyacrylonitrile resin is once dissolved in a soluble organic solvent, it is molded into a fibrous, film or other form, and this is treated with iodine gas to obtain the desired fibrous or film form. A carbonized product can be obtained.
【0037】用いる有機溶媒としては、ポリアクリロニ
トリルが可溶であれば特に制限はないが、以下に挙げる
有機溶媒、すなわち、ハロゲン化炭化水素、非プロトン
性極性溶媒を好ましく用いることができる。1,1,
2,2−テトラクロロエタン、クロロホルム、ジメチル
クロライド、テトラヒドロフラン、N−メチルピロリド
ン、ジメチルアセトアミド、ジメチルホルムアミド、ジ
メチルスルホキシドがより好ましく、N−メチルピロリ
ドン、ジメチルアセトアミド、ジメチルホルムアミドが
さらに好ましい。The organic solvent to be used is not particularly limited as long as polyacrylonitrile is soluble, but the following organic solvents, that is, halogenated hydrocarbons and aprotic polar solvents can be preferably used. 1,1,
2,2-tetrachloroethane, chloroform, dimethyl chloride, tetrahydrofuran, N-methylpyrrolidone, dimethylacetamide, dimethylformamide and dimethylsulfoxide are more preferred, and N-methylpyrrolidone, dimethylacetamide and dimethylformamide are even more preferred.
【0038】[0038]
【発明の効果】本願発明によれば、まず、ポリアクリロ
ニトリル樹脂をヨウ素ガスと接触させることによって、
低温においても効率的に不炎化体を得ることができる。According to the present invention, first, a polyacrylonitrile resin is brought into contact with iodine gas,
Even at a low temperature, an inflammable body can be obtained efficiently.
【0039】これは、ヨウ素ガスが、ポリアクリロニト
リル樹脂を速やかに酸化、環化および架橋化反応を進行
せしめているからと考えられる。This is presumably because the iodine gas rapidly oxidized, cyclized and crosslinked the polyacrylonitrile resin.
【0040】更に、得られたポリアクリロニトリル不炎
化体を経て焼成して得られた炭素化体は、従来の方法に
比べて炭化収率が高く、強度的に優れた炭素繊維が安定
して得られ、プリプレグ、複合材料へ展開することによ
って従来より機械的強度に優れた製品を安価に得ること
ができる。Further, the carbonized product obtained by firing through the obtained non-flammable polyacrylonitrile has a higher carbonization yield than the conventional method, and a carbon fiber excellent in strength can be stably obtained. Thus, by developing it into a prepreg or a composite material, a product having excellent mechanical strength can be obtained at a low cost.
【0041】[0041]
【実施例】以下に本願発明の実施例を詳述する。ただ
し、本願発明はこれらに限定されるものではない。Embodiments of the present invention will be described below in detail. However, the present invention is not limited to these.
【0042】<燃焼試験>ガスバーナーの炎を2センチ
大の大きさに調整し、そこへ切り取った不炎化体試験サ
ンプルをピンセットで挟んで、炎に近づける。<Combustion Test> The flame of the gas burner was adjusted to a size of 2 cm, and the cut nonflammable body test sample was pinched with tweezers to approach the flame.
【0043】炎が試験サンプルに燃え移ったことを確認
した後、炎からサンプルを遠ざけ、その後の様子を観察
し、自然に炎が消え、自己消火性を示した場合は「○」
とし、遠ざけてもそのまま炎が燃えつづける場合を
「×」とした。After confirming that the flame had burned to the test sample, the sample was moved away from the flame, and the appearance afterward was observed.
The case where the flame continued to burn as it was kept away was marked as "x".
【0044】ポリアクリロニトリル樹脂は、アルドリッ
チ社製のものを使用した。As the polyacrylonitrile resin, a resin manufactured by Aldrich was used.
【0045】ヨウ素は、関東化学製のもの(純度99.
8重量%)を、昇華精製等で精製して使用した。Iodine was manufactured by Kanto Chemical (purity 99.
8% by weight) was used after purification by sublimation purification or the like.
【0046】<炭化収率>不炎化処理に至る前の乾燥処
理したポリアクリロニトリル樹脂の重量に対する焼成後
に得られた炭素化体の重量を「炭化収率」として100
分率で示した。<Carburization Yield> The weight of the carbonized product obtained after the calcination with respect to the weight of the dried polyacrylonitrile resin before the flameproofing treatment is defined as a “carbonization yield” of 100.
Shown in fractions.
【0047】[参考例1]ポリアクリロニトリル粉末3
4Kgを、N−メチルピロリドン166Kgに溶解さ
せ、17重量%の溶液を調製した。得られた溶液を湿式
紡糸し、単糸0.11テックス,繊維束333テックス
のポリアクリロニトリル繊維を得た。Reference Example 1 Polyacrylonitrile Powder 3
4 kg was dissolved in 166 kg of N-methylpyrrolidone to prepare a 17% by weight solution. The resulting solution was wet-spun to obtain polyacrylonitrile fiber having a single yarn of 0.11 tex and a fiber bundle of 333 tex.
【0048】[参考例2]ポリアクリロニトリル粉末3
4gを、N−メチルピロリドン166gに溶解させ、1
7重量%の溶液を調製した。得られた溶液をフィルムキ
ャスト法により製膜し、乾燥させることにより、厚さ5
0μmのポリアクリロニトリルフィルムを得た。Reference Example 2 Polyacrylonitrile Powder 3
4 g was dissolved in 166 g of N-methylpyrrolidone, and 1
A 7% by weight solution was prepared. The resulting solution is formed into a film by a film casting method and dried to obtain a film having a thickness of 5 mm.
A 0 μm polyacrylonitrile film was obtained.
【0049】[実施例1,2]参考例1,2で得られた
ポリアクリロニトリル繊維およびフィルムをそれぞれ耐
圧ガラス瓶(容量420mL)の中に入れ、固体ヨウ素
1.066gを入れた後、窒素置換をして密閉した。そ
の耐圧瓶ごと200℃の熱風乾燥機の中に入れ,2時間
後、取りだし放冷した。[Examples 1 and 2] The polyacrylonitrile fibers and the films obtained in Reference Examples 1 and 2 were each placed in a pressure-resistant glass bottle (capacity: 420 mL), and 1.066 g of solid iodine was added. And sealed. The pressure bottle was put into a hot air drier at 200 ° C., taken out after 2 hours, and allowed to cool.
【0050】取り出したサンプルを、燃焼試験を行った
結果、いずれの繊維、フィルムも自己消火性を示した不
炎化体であった。The samples taken out were subjected to a combustion test. As a result, all of the fibers and films were non-flammable, exhibiting self-extinguishing properties.
【0051】上記で得られた不炎化体あについて、窒素
ガス流量100mL/分で充填された焼成炉(シリコニ
ット製電気炉「1800SpUSH」)内で700℃,
次いで1300℃の条件で段階的に焼成し、それぞれの
焼成後に得られた炭素化体の結果を表1にまとめた。The non-flammable body obtained above was heated at 700 ° C. in a firing furnace (siliconit electric furnace “1800 SpUSH”) filled with a nitrogen gas flow rate of 100 mL / min.
Next, firing was carried out stepwise at 1300 ° C., and the results of the carbonized bodies obtained after each firing were summarized in Table 1.
【0052】[実施例3,4]200℃,2時間の条件
に代えて、250℃,1時間とした以外は実施例1,2
と同様な処置を行った。それぞれの焼成後に得られた炭
素化体の結果を表1にまとめた。[Examples 3 and 4] Examples 1 and 2 except that the conditions of 200 ° C. and 2 hours were changed to 250 ° C. and 1 hour.
The same treatment was performed. Table 1 summarizes the results of the carbonized products obtained after each firing.
【0053】[比較例1,2]参考例1,2で得られた
ポリアクリロニトリル繊維およびフィルムを、それぞれ
そのまま(すなわち固体ヨウ素を入れ、窒素置換をする
という操作をせずに)200℃の熱風乾燥機の中に入れ
た以外は実施例1,2と同様な処置を行った。それぞれ
の焼成後に得られた炭素化体の結果を表1にまとめた。[Comparative Examples 1 and 2] The polyacrylonitrile fibers and films obtained in Reference Examples 1 and 2 were each heated as they were (ie, without the operation of adding solid iodine and replacing with nitrogen) at 200 ° C. The same treatment as in Examples 1 and 2 was carried out except that it was placed in a dryer. Table 1 summarizes the results of the carbonized products obtained after each firing.
【0054】[比較例3,4]参考例1,2で得られた
ポリアクリロニトリル繊維およびフィルムをそれぞれ耐
圧ガラス瓶(容量420mL)の中に入れ、固体ヨウ素
を入れずに窒素置換をして密閉した以外は実施例1,2
と同様な処置を行った。それぞれの焼成後に得られた炭
素化体の結果を表1にまとめた。[Comparative Examples 3 and 4] The polyacrylonitrile fiber and the film obtained in Reference Examples 1 and 2 were respectively placed in pressure-resistant glass bottles (capacity: 420 mL), replaced with nitrogen without containing solid iodine, and sealed. Other than Examples 1 and 2
The same treatment was performed. Table 1 summarizes the results of the carbonized products obtained after each firing.
【0055】[比較例5,6]参考例1,2で得られた
ポリアクリロニトリル繊維およびフィルムを、それぞれ
そのまま(すなわち固体ヨウ素を入れ、窒素置換をする
という操作をせずに)250℃の熱風乾燥機の中に入れ
た以外は実施例1,2と同様な処置を行った。それぞれ
の焼成後に得られた炭素化体の結果を表1にまとめた。[Comparative Examples 5 and 6] The polyacrylonitrile fibers and films obtained in Reference Examples 1 and 2 were each heated as they were (ie, without the operation of adding solid iodine and purging with nitrogen) at 250 ° C. The same treatment as in Examples 1 and 2 was carried out except that it was placed in a dryer. Table 1 summarizes the results of the carbonized products obtained after each firing.
【0056】なお、表の炭化収率の欄中、「−」は、燃
焼試験により、耐炎化が不十分であるために、後に炭化
処理を行っても、断糸、破断などが起こるため炭化収率
の測定が不可能であったことを意味する。In the column of carbonization yield in the table, "-" indicates that the flame resistance was insufficient in the combustion test, and even if carbonization was performed later, thread breakage and breakage would occur. It means that the yield could not be measured.
【0057】[0057]
【表1】 [Table 1]
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F073 AA12 BA18 BB01 DA02 GA01 HA04 4L035 BB03 BB06 BB11 FF01 MB00 4L037 CS03 PA53 PC10 PC11 PS03 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4F073 AA12 BA18 BB01 DA02 GA01 HA04 4L035 BB03 BB06 BB11 FF01 MB00 4L037 CS03 PA53 PC10 PC11 PS03
Claims (4)
と接触せしめ不炎化体とした後、300〜3000℃の
不活性ガスの雰囲気内で焼成することを特徴とするポリ
アクリロニトリル系炭素化体の製造方法。1. A method for producing a polyacrylonitrile-based carbonized material, comprising: bringing a polyacrylonitrile resin into contact with iodine gas to form a non-flammable body; and firing the resultant in an inert gas atmosphere at 300 to 3000 ° C. .
ニトリルモノマー成分が80〜100モル%であること
を特徴とする請求項1記載のポリアクリロニトリル系炭
素化体の製造方法。2. The method for producing a polyacrylonitrile-based carbonized product according to claim 1, wherein the acrylonitrile monomer component in the polyacrylonitrile resin is 80 to 100 mol%.
状であることを特徴とする請求項1または2記載のポリ
アクリロニトリル系炭素化体の製造方法。3. The method for producing a polyacrylonitrile-based carbonized product according to claim 1, wherein the form of the polyacrylonitrile resin is fibrous.
ルム状であることを特徴とする請求項1または2記載の
ポリアクリロニトリル系炭素化体の製造方法。4. The method for producing a polyacrylonitrile-based carbonized product according to claim 1, wherein the polyacrylonitrile resin is in the form of a film.
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JP2013256749A (en) * | 2009-03-31 | 2013-12-26 | Donghua Univ | Method for producing carbon fiber, precursor fiber thereof, and pre-oxidized fiber |
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