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JP6657712B2 - Method for producing carbon fiber and carbon fiber sheet - Google Patents
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JP6657712B2 - Method for producing carbon fiber and carbon fiber sheet - Google Patents

Method for producing carbon fiber and carbon fiber sheet Download PDF

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JP6657712B2
JP6657712B2 JP2015190817A JP2015190817A JP6657712B2 JP 6657712 B2 JP6657712 B2 JP 6657712B2 JP 2015190817 A JP2015190817 A JP 2015190817A JP 2015190817 A JP2015190817 A JP 2015190817A JP 6657712 B2 JP6657712 B2 JP 6657712B2
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carbon fiber
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JP2017066539A (en
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草野瑛司
川真田友紀
矢口忠平
藤野謙一
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Nippon Paper Industries Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Description

本発明は、触媒に有機スルホン酸を用いた炭素繊維及び炭素繊維シートの製造方法に関する。 The present invention relates to a method for producing a carbon fiber and a carbon fiber sheet using an organic sulfonic acid as a catalyst.

炭素繊維は比強度、比弾性率に優れているため、スポーツやレジャー用品から宇宙航空用途まで幅広く利用されつつある。このような構造材として炭素繊維を用いる場合、炭素繊維のトウを製織して得られた織物に熱硬化性樹脂を含浸して得られるプリプレグを成型、硬化させた炭素繊維強化プラスチックとして用いる方法が一般的である。   Since carbon fiber has excellent specific strength and specific elastic modulus, it is being widely used from sports and leisure goods to aerospace applications. When carbon fiber is used as such a structural material, a method is used in which a prepreg obtained by impregnating a thermosetting resin into a woven fabric obtained by weaving a carbon fiber tow is used as a cured carbon fiber reinforced plastic. General.

これまでポリビニルアルコール(PVA)などの水溶性高分子化合物を用いた炭素繊維が種々検討されている。PVAは230℃付近に融点を持ち、炭化に必要な温度条件下では樹脂の一部または全部が溶融し、その形態を保つことが困難である事から、PVAを主体とする炭素繊維は大きく、1)PVAを紡糸し繊維を得る工程、2)200℃程度の条件下で前記繊維を不融化する工程、3)500℃〜2600℃程度の条件下で炭化する工程を経ることによって製造されている。また、更に高弾性率の炭素繊維を製造するために、2200℃〜3200℃での再加熱処理を含む場合もある。   Various carbon fibers using a water-soluble polymer compound such as polyvinyl alcohol (PVA) have been studied. PVA has a melting point around 230 ° C., and part or all of the resin melts under the temperature conditions necessary for carbonization, and it is difficult to maintain its form. 1) a step of spinning PVA to obtain fibers, 2) a step of making the fibers infusible at about 200 ° C., and 3) a step of carbonizing at about 500 ° C. to 2600 ° C. I have. In addition, in order to produce a carbon fiber having a higher elastic modulus, a reheating treatment at 2200 ° C. to 3200 ° C. may be included.

すなわち、従来におけるPVA系炭素繊維の製造においては前記の不融化処理が必須である事を前提として種々検討されており、特許文献1および2では炭素化過程での熱安定性を向上させて、炭化収率を向上させる目的でPVA系樹脂にヨウ素処理等のハロゲン処理を施し不融化処理を行う方法が提案されている。また特許文献3にはハロゲン処理に加えてアルカリ金属塩およびアルカリ土類金属塩から選ばれる少なくとも一種の金属塩を共存させることで、処理時間を短縮できる技術が提案されている。さらに特許文献4にはポリビニルアルコールを溶解した水溶液中に架橋剤を添加する事で、炭化収率を向上する技術が提案されている。   That is, in the production of conventional PVA-based carbon fibers, various studies have been made on the premise that the infusibilization treatment is indispensable. In Patent Documents 1 and 2, the thermal stability in the carbonization process is improved. In order to improve the carbonization yield, a method has been proposed in which a PVA-based resin is subjected to a halogen treatment such as an iodine treatment to perform an infusibilization treatment. Patent Document 3 proposes a technique capable of shortening the processing time by coexisting at least one metal salt selected from an alkali metal salt and an alkaline earth metal salt in addition to the halogen treatment. Further, Patent Document 4 proposes a technique for improving a carbonization yield by adding a crosslinking agent to an aqueous solution in which polyvinyl alcohol is dissolved.

特開2003−128407JP-A-2003-128407 特開2004−339627JP-A-2004-396627 特開2009−249238JP 2009-249238 A 特開2012−067432JP-A-2012-067432

しかしながら、この不融化処理は、炭素繊維の製造工程を煩雑にし、エネルギー消費量が大きい為製造コストを増大させる一因にもなっている。   However, this infusibilization treatment complicates the production process of carbon fibers, and also contributes to an increase in production costs due to a large energy consumption.

そこで、本発明は、炭素繊維の原料となる有機繊維を含有する繊維または繊維シートを加熱処理して炭素繊維または炭素繊維シートを得る製造方法において、不融化工程を省略しても炭素繊維の溶融・融着を抑制できる製造方法を提供することを目的とする。   Therefore, the present invention provides a method for producing a carbon fiber or a carbon fiber sheet by heating a fiber or a fiber sheet containing an organic fiber which is a raw material of the carbon fiber, even if the infusibilization step is omitted. -To provide a manufacturing method capable of suppressing fusion.

本発明は、以下の[1]〜[8]の発明を提供する。
[1] 下記の(a)〜(c)の工程を含むことを特徴とする不融化工程を含まない炭素繊維または炭素繊維シートの製造方法。
(a)炭素繊維または炭素繊維シートの原料となる水溶性高分子化合物と有機スルホン酸を溶解した水溶液を調製する工程
(b)上記水溶液を紡糸し、繊維または繊維シートを得る工程
(c)上記繊維または繊維シートを不活性ガス雰囲気中、500℃〜2600℃の温度にて加熱処理する工程
[2] 更に下記の(d)の工程を含むことを特徴とする[1]に記載の炭素繊維または炭素繊維シートの製造方法。
(d)前記(c)工程で得られた繊維または繊維シートを不活性ガス雰囲気中、2200℃〜3200℃での再加熱処理する工程
[3] 前記水溶性高分子が、ポリビニルアルコール、ポリエチレングリコール、ポリエチレンオキシド、ポリアクリル酸、ポリビニルピロリドンである事を特徴とする[1]〜[2]のいずれかに記載の炭素繊維または炭素繊維シートの製造方法。
[4] 前記有機スルホン酸が、メタンスルホン酸であることを特徴とする[1]〜[3]のいずれか一項に記載の炭素繊維または炭素繊維シートの製造方法。
[5] 前記水溶性高分子化合物に対する有機スルホン酸の比率が0.1wt%〜10.0wt%であることを特徴とする[1]〜[4]のいずれか一項に記載の炭素繊維または炭素繊維シートの製造方法。
[6] 前記繊維または繊維シートが、エレクトロスピニング法により得られることを特徴とする、[1]〜[5]のいずれか一項に記載の炭素繊維または炭素繊維シートの製造方法。
[7] [1]〜[6]のいずれか一項に記載の方法で製造された炭素繊維を用いることを特徴とする織物。
[8] [1]〜[7]のいずれか一項に記載の方法で製造された炭素繊維または炭素繊維シートを用いることを特徴とする複合材料。
[9] [1]〜[7]のいずれか一項に記載の方法で製造された炭素繊維または炭素繊維シートを用いることを特徴とする燃料電池用ガス拡散層。
The present invention provides the following inventions [1] to [8].
[1] A method for producing a carbon fiber or a carbon fiber sheet which does not include the infusibilizing step, which comprises the following steps (a) to (c).
(A) a step of preparing an aqueous solution in which a water-soluble polymer compound and a raw material of a carbon fiber or a carbon fiber sheet are dissolved and an organic sulfonic acid; (b) a step of spinning the aqueous solution to obtain a fiber or a fiber sheet; A step of heat-treating the fiber or the fiber sheet at a temperature of 500 ° C. to 2600 ° C. in an inert gas atmosphere
[2] The method for producing a carbon fiber or carbon fiber sheet according to [1], further comprising the following step (d).
(D) a step of reheating the fiber or fiber sheet obtained in the step (c) at 2200 ° C. to 3200 ° C. in an inert gas atmosphere;
[3] The carbon fiber or carbon fiber according to any one of [1] to [2], wherein the water-soluble polymer is polyvinyl alcohol, polyethylene glycol, polyethylene oxide, polyacrylic acid, or polyvinylpyrrolidone. Sheet manufacturing method.
[4] The method for producing a carbon fiber or a carbon fiber sheet according to any one of [1] to [3], wherein the organic sulfonic acid is methanesulfonic acid.
[5] The carbon fiber according to any one of [1] to [4], wherein a ratio of the organic sulfonic acid to the water-soluble polymer compound is 0.1 wt% to 10.0 wt%. A method for producing a carbon fiber sheet.
[6] The method for producing a carbon fiber or a carbon fiber sheet according to any one of [1] to [5], wherein the fiber or the fiber sheet is obtained by an electrospinning method.
[7] A woven fabric using the carbon fiber produced by the method according to any one of [1] to [6].
[8] A composite material using a carbon fiber or a carbon fiber sheet produced by the method according to any one of [1] to [7].
[9] A gas diffusion layer for a fuel cell, comprising a carbon fiber or a carbon fiber sheet produced by the method according to any one of [1] to [7].

本発明によれば、炭素繊維の原料となる有機繊維を含有する繊維または繊維シートを加熱処理して得られる炭素繊維または炭素繊維シートの製造方法において、不融化工程を省略しても炭素繊維の溶融・融着を抑制できる製造方法を提供することができる。   According to the present invention, in a method for producing a carbon fiber or a carbon fiber sheet obtained by heat-treating a fiber or a fiber sheet containing an organic fiber serving as a raw material of a carbon fiber, even if the infusibilization step is omitted, the carbon fiber It is possible to provide a production method capable of suppressing melting and fusion.

本発明の実施例1の炭素繊維シート表面の電子顕微鏡画像である。It is an electron microscope image of the carbon fiber sheet surface of Example 1 of the present invention. 本発明の比較例1の炭素繊維シート表面の電子顕微鏡画像である。4 is an electron microscope image of the surface of a carbon fiber sheet of Comparative Example 1 of the present invention. 本発明の比較例3の炭素繊維シート表面の電子顕微鏡画像である。It is an electron microscope image of the carbon fiber sheet surface of Comparative Example 3 of the present invention.

本発明の炭素繊維または炭素繊維シートの製造方法は、水溶性高分子化合物と有機スルホン酸を含有する溶液を原料として得られる繊維または繊維シートを、不活性ガス雰囲気中、500℃〜2600℃の温度にて加熱処理することを特徴とする。特に、200℃程度の条件下で繊維または繊維シートを不融化する工程を行わないことが本発明の大きな特徴である。なお、得られた炭素繊維または炭素繊維シートを、2200℃〜3200℃での再加熱処理することも可能である。   The method for producing a carbon fiber or a carbon fiber sheet of the present invention comprises the steps of: producing a fiber or a fiber sheet obtained from a solution containing a water-soluble polymer compound and an organic sulfonic acid in an inert gas atmosphere at 500 ° C. to 2600 ° C. The heat treatment is performed at a temperature. In particular, a major feature of the present invention is that a step of infusifying a fiber or a fiber sheet at about 200 ° C. is not performed. In addition, it is also possible to reheat the obtained carbon fiber or carbon fiber sheet at 2200 ° C. to 3200 ° C.

(水溶性高分子)
本発明における水溶性高分子化合物は、繊維化が可能な材料であれば特に限定されず、例えばポリビニルアルコール、ポリエチレングリコール、ポリエチレンオキシド、ポリアクリル酸、ポリビニルピロリドン、ポリ酢酸ビニル、コラーゲン、澱粉、カルボキシメチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース等が挙げられ、これらを単独で用いても2種以上混合して用いても良く、水溶性を阻害しない範囲で変性されていてもよい。
(Water-soluble polymer)
The water-soluble polymer compound in the present invention is not particularly limited as long as it is a material capable of forming fibers, and examples thereof include polyvinyl alcohol, polyethylene glycol, polyethylene oxide, polyacrylic acid, polyvinyl pyrrolidone, polyvinyl acetate, collagen, starch, and carboxy. Examples thereof include methylcellulose, hydroxyethylcellulose, and hydroxypropylcellulose. These may be used alone or as a mixture of two or more kinds, and may be modified as long as water solubility is not impaired.

これら材料の中でも、水溶液からの紡糸が比較的容易なポリビニルアルコール、ポリエチレングリコール、ポリエチレンオキシド、ポリアクリル酸、ポリビニルピロリドンが好ましく、ポリビニルアルコールがさらに好適である。   Among these materials, polyvinyl alcohol, polyethylene glycol, polyethylene oxide, polyacrylic acid, and polyvinylpyrrolidone, which are relatively easy to spin from an aqueous solution, are preferable, and polyvinyl alcohol is more preferable.

また繊維形成を阻害しない範囲で前記水溶性高分子化合物を溶解した水溶液中に有機・無機材料を混合しても良く、その形態については粒状、繊維状などの固形材料や水溶液中で混和する材料などを適宜使用することが出来る。例えば無機化合物を分散した水溶液を原料として繊維化する事で、加熱処理後の炭素繊維中に無機化合物を担持させ消臭や抗菌などの機能性を付与する事が可能であり、また水溶液中に界面活性剤や導電助剤を添加する事で紡糸工程における繊維形成性を向上させることができる。   Further, an organic / inorganic material may be mixed in an aqueous solution in which the water-soluble polymer compound is dissolved within a range that does not inhibit the fiber formation, and the form may be a granular material, a fibrous solid material or a material that is miscible in the aqueous solution. Etc. can be used as appropriate. For example, by fibrillating an aqueous solution in which an inorganic compound is dispersed as a raw material, it is possible to support the inorganic compound in the carbon fiber after the heat treatment and to impart functionality such as deodorization or antibacterial, and also to the aqueous solution. By adding a surfactant or a conductive auxiliary, the fiber forming property in the spinning step can be improved.

(有機スルホン酸)
本発明において、前記水溶性高分子化合物の水溶液に混合する有機系スルホン酸としては、炭素骨格にスルホ基(1つであっても複数であってもよい)が結合した有機化合物であればいずれであってもよく、脂肪族系、芳香族系の種々のスルホ基を有する化合物が利用可能であるが、取扱いの観点から低分子であることが好ましい。
(Organic sulfonic acid)
In the present invention, the organic sulfonic acid to be mixed with the aqueous solution of the water-soluble polymer compound may be any organic compound having a carbon skeleton to which a sulfo group (which may be one or more) is bonded. May be used, and compounds having various aliphatic or aromatic sulfo groups can be used, but from the viewpoint of handling, it is preferable that the compound has a low molecular weight.

有機スルホン酸の具体例として、例えばR−SO3H(式中、Rは炭素原子数1〜20の直鎖/分岐鎖アルキル基、炭素原子数3〜20のシクロアルキル基、または、炭素原子数6〜20のアリ−ル基を表し、アルキル基、シクロアルキル基、アリ−ル基はそれぞれアルキル基、水酸基、ハロゲン基で置換されていても良い。)で表される化合物が挙げられる。例えば、メタンスルホン酸、エタンスルホン酸、プロパンスルホン酸、1−ヘキサンスルホン酸、ビニルスルホン酸、シクロヘキサンスルホン酸、p−トルエンスルホン酸、p−フェノールスルホン酸、ナフタレンスルホン酸、ベンゼンスルホン酸、カンファ―スルホン酸などが挙げられる。 このうちメタンスルホン酸を選択することが好ましい。また、有機系スルホン酸は1種を単独で用いても良く、2種以上を併用しても良い。   Specific examples of the organic sulfonic acid include, for example, R-SO3H (wherein R is a linear / branched alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, or 6 carbon atoms). And alkyl groups, cycloalkyl groups, and aryl groups, each of which may be substituted with an alkyl group, a hydroxyl group, or a halogen group. For example, methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid, 1-hexanesulfonic acid, vinylsulfonic acid, cyclohexanesulfonic acid, p-toluenesulfonic acid, p-phenolsulfonic acid, naphthalenesulfonic acid, benzenesulfonic acid, camphor Sulfonic acid and the like. Of these, methanesulfonic acid is preferably selected. Further, one type of organic sulfonic acid may be used alone, or two or more types may be used in combination.

本発明において、有機スルホン酸を混合することで、不融化処理が不要となる理由は明らかではないが、水溶性高分子化合物と有機スルホン酸を混合した溶液から紡糸した繊維シートを加熱処理することにより、有機スルホン酸が脱水触媒として作用し、分子内及び分子間における水酸基等の脱水反応を促進し、化合物の耐熱性向上及び脱水反応以外の熱分解反応の抑制に寄与すると考えられる。このため、通常の熱分解に伴う炭化水素系のガスの発生および水溶性高分子化合物中の炭素成分の減少が抑制されることが起因すると推測される。   In the present invention, it is not clear why the infusibilization treatment is not required by mixing the organic sulfonic acid, but the heat treatment of the fiber sheet spun from a solution in which the water-soluble polymer compound and the organic sulfonic acid are mixed is performed. Thus, the organic sulfonic acid acts as a dehydration catalyst, promotes the dehydration reaction of hydroxyl groups and the like in the molecule and between the molecules, and contributes to improvement of the heat resistance of the compound and suppression of a thermal decomposition reaction other than the dehydration reaction. For this reason, it is presumed that the generation of hydrocarbon-based gas and the reduction of the carbon component in the water-soluble polymer compound due to ordinary thermal decomposition are suppressed.

本発明の炭素繊維または炭素繊維シートの製造方法において、前記有機系スルホン酸の添加量は非水溶性高分子化合物100重量部に対して0.1wt%〜10.0wt%であることが好ましく、0.1wt%〜5.0wt%がより好ましい。   In the method for producing a carbon fiber or a carbon fiber sheet of the present invention, the amount of the organic sulfonic acid to be added is preferably 0.1 wt% to 10.0 wt% based on 100 parts by weight of the water-insoluble polymer compound. 0.1 wt% to 5.0 wt% is more preferable.

(繊維および繊維シートの製造:紡糸工程)
本発明における繊維とは1本のフィラメントからなる単糸および複数本の単糸を撚って得られる撚糸を含む。また撚糸の内には短繊維をより合わせて成るスパン糸および、長繊維を撚り合わせて成るフィラメント糸を含む。本発明における繊維を製造する方法は特に限定されず、溶液を原料とする公知の紡糸方法を適宜選択する事ができ、具体的には紡糸金口より溶液を噴出させ熱風にて溶媒を除去する乾式紡糸法および紡糸金口より凝固液中に溶液を導き繊維化する湿式紡糸法を用いる事ができる。得られた繊維にカッティング等の処理を施し任意の長さに切断して用いてもよい。
(Manufacture of fiber and fiber sheet: spinning process)
The fiber in the present invention includes a single yarn composed of one filament and a twisted yarn obtained by twisting a plurality of single yarns. The twisted yarn includes a spun yarn formed by twisting short fibers and a filament yarn formed by twisting long fibers. The method for producing the fiber in the present invention is not particularly limited, and a known spinning method using a solution as a raw material can be appropriately selected. Specifically, the solution is ejected from a spinneret and the solvent is removed with hot air. A dry spinning method and a wet spinning method in which a solution is introduced into a coagulating liquid from a spinneret and formed into fibers can be used. The obtained fiber may be subjected to a treatment such as cutting and cut into an arbitrary length for use.

本発明における繊維シートとは多数の繊維を薄く広い板状に加工したものを言い、織物や編み物、不織布を含む。不織布の製造方法は特に限定されないが、適当な長さに切断された前述の繊維を原料とし乾式法または湿式法などを用いて繊維シートを得る方法や、エレクトロスピニング法などを用いて溶液から直接繊維シートを得る方法が例示できる。さらに不織布を得た後に繊維同士を結合させる目的でレジンボンド、サーマルボンド、スパンレース、ニードルパンチ等による処理を加えてもよい。   The fiber sheet in the present invention refers to a sheet obtained by processing a large number of fibers into a thin and wide plate shape, and includes a woven fabric, a knitted fabric, and a nonwoven fabric. The method for producing the nonwoven fabric is not particularly limited, but a method of obtaining a fiber sheet using a dry method or a wet method using the above-described fibers cut to an appropriate length as a raw material, or directly from a solution using an electrospinning method or the like. A method for obtaining a fiber sheet can be exemplified. Further, after the nonwoven fabric is obtained, a treatment such as resin bond, thermal bond, spunlace, or needle punch may be added for the purpose of bonding the fibers.

特に、サブミクロンオーダーの繊維径を有するエレクトロスピニング法においては、繊維シートを構成する繊維の直径が極端に細いため、熱処理による繊維の断裂や焼失が起こりやすいが、本発明を適用する事で繊維を構成する炭素の残存量を多く保つことができ、結果として熱処理前後で繊維およびシートの形状が保持された炭素繊維シートを製造する事ができる。   In particular, in the electrospinning method having a fiber diameter of a submicron order, the diameter of the fiber constituting the fiber sheet is extremely small, so that the fiber is likely to be broken or burned out by heat treatment. Can be kept large, and as a result, a carbon fiber sheet in which the shape of the fiber and the sheet is maintained before and after the heat treatment can be produced.

エレクトロスピニング法は、周知の手段によって行うことができ、具体的には、紡糸溶液を充填したノズルと基板(コレクターともいう)の間に電圧を印加した状態で、ノズルから紡糸溶液を吐出させて、基板上に繊維を回収する。   The electrospinning method can be performed by a known means. Specifically, in a state where a voltage is applied between a nozzle filled with a spinning solution and a substrate (also called a collector), the spinning solution is discharged from the nozzle. Collect the fibers on the substrate.

ノズルから紡糸溶液を吐出させる基板としては金属板などの電極コレクターをそのまま用いてもよいが、ノズルとコレクターとの間に紙等の非導電性の材料を置いて基板とすることもできる。このような基板としては、特に限定は無く、その形状にも特に限定は無いが、柔軟性を持つシート状であることが好ましい。柔軟性を持つことにより、基板とこの基板上に形成された繊維構造体から成る繊維複合体で、対象を被覆した場合に、この繊維複合体が対象の凹凸に沿って対象に密着することが可能になる。本発明においては、このような基板として、紙、不織布、プラスチックフィルムなどが好適に用いられる。   As the substrate from which the spinning solution is discharged from the nozzle, an electrode collector such as a metal plate may be used as it is, but a non-conductive material such as paper may be placed between the nozzle and the collector to form the substrate. Such a substrate is not particularly limited, and the shape thereof is not particularly limited, but is preferably a flexible sheet. By having flexibility, when a target is covered with a fiber composite comprising a substrate and a fiber structure formed on the substrate, the fiber composite can adhere to the target along irregularities of the target. Will be possible. In the present invention, paper, nonwoven fabric, plastic film, and the like are suitably used as such a substrate.

エレクトロスピニング法を行う条件は、特に限定されず、紡糸溶液の種類や得られるナノファイバーの用途等に応じて適宜調整すればよい。本発明の方法における一般的な条件としては、例えば、印加電圧は5〜30kV、吐出速度は0.01〜1.00mL/分、ノズルと基板の間の垂直距離は100〜200mmとすることができ、ノズルは15〜25Gの径のものを使用することができる。紡糸環境は、特段厳密に制御を行わなくてもよいが、相対湿度10〜50%、温度を10〜25℃とすることが好ましい。   Conditions for performing the electrospinning method are not particularly limited, and may be appropriately adjusted according to the type of the spinning solution, the use of the obtained nanofiber, and the like. As general conditions in the method of the present invention, for example, the applied voltage is 5 to 30 kV, the ejection speed is 0.01 to 1.00 mL / min, and the vertical distance between the nozzle and the substrate is 100 to 200 mm. It is possible to use a nozzle having a diameter of 15 to 25 G. The spinning environment does not need to be strictly controlled, but it is preferable that the relative humidity is 10 to 50% and the temperature is 10 to 25 ° C.

この方法により、直径5nm〜50μmの繊維を得ることができる。また、紡糸条件の設定・調整により、平均長が200〜300nmのナノ繊維を得ることができる。   By this method, fibers having a diameter of 5 nm to 50 μm can be obtained. Further, by setting and adjusting spinning conditions, nanofibers having an average length of 200 to 300 nm can be obtained.

(炭化処理)
本発明においては、水溶性高分子化合物と有機スルホン酸を有機溶剤に溶解した混合液から紡糸した繊維または繊維シートを加熱処理(炭素化)する。炭素化は不活性ガス雰囲気中で行う。不活性ガスとしてはアルゴン、窒素等が例示される。
(Carburizing treatment)
In the present invention, a fiber or a fiber sheet spun from a mixed solution in which a water-soluble polymer compound and an organic sulfonic acid are dissolved in an organic solvent is subjected to heat treatment (carbonization). Carbonization is performed in an inert gas atmosphere. Examples of the inert gas include argon and nitrogen.

本発明において、水溶性高分子化合物と有機系スルホン酸の混合水溶液から紡糸した繊維または繊維シートを不活性ガス雰囲気中、500℃〜2600℃の温度にて加熱処理することが好ましいく、より好ましくは500℃〜1000℃である。この加熱処理条件とすることにより、繊維形態が維持された炭素繊維織物を得ることができる。加熱処理温度が500℃未満であると炭素繊維の炭素含有量が80%以下で炭素化が不十分であり、一方2600℃を超えても炭化状態はもはや殆ど変化しない。また、炭素化処理は連続的に行われても、バッチ状態で行われても良い。   In the present invention, it is preferable, and more preferably, to heat-treat a fiber or a fiber sheet spun from a mixed aqueous solution of a water-soluble polymer compound and an organic sulfonic acid at a temperature of 500 ° C to 2600 ° C in an inert gas atmosphere. Is 500 ° C to 1000 ° C. Under these heat treatment conditions, a carbon fiber woven fabric in which the fiber form is maintained can be obtained. If the heat treatment temperature is less than 500 ° C., the carbon content of the carbon fiber is not more than 80% and the carbonization is insufficient, while if it exceeds 2600 ° C., the carbonized state hardly changes anymore. Further, the carbonization treatment may be performed continuously or in a batch state.

また、水溶性高分子化合物と有機スルホン酸を有機溶剤に溶解した混合液から紡糸した繊維または繊維シートを不活性ガス雰囲気中、500℃〜2600℃の温度にて加熱処理後に、さらに不活性ガス雰囲気中、2200℃〜3200℃で再加熱処理(グラファイト化工程)することが可能である。再加熱処理温度が2200℃未満であるとグラファイト化(結晶化)の進行が殆ど起こらず、一方3200℃を超えても、もはやグラファイト化の程度は殆ど変わらなくなる。   Further, a fiber or a fiber sheet spun from a mixed solution in which a water-soluble polymer compound and an organic sulfonic acid are dissolved in an organic solvent is heated in an inert gas atmosphere at a temperature of 500 ° C. to 2600 ° C. It is possible to perform a reheating treatment (graphitization step) at 2200 ° C. to 3200 ° C. in an atmosphere. If the reheating temperature is lower than 2200 ° C., the progress of graphitization (crystallization) hardly occurs, while if it exceeds 3200 ° C., the degree of graphitization hardly changes.

以下に具体的な炭化方法を記載する。
まず、前記の紡糸行程を経て形成された繊維または繊維シートをその形態を維持した状態で電気炉を用いて窒素又はアルゴン雰囲気下、500℃〜2600℃で加熱処理する。この際、熱処理時間は熱処理温度にもよるが、好ましくは0.5〜1時間である。また、室温から所定熱処理温度までの昇温時間は3〜8℃/分が好ましい。加熱処理工程において管状炉や電気炉等の不活性ガス雰囲気にした高温炉を使用できるが、この場合、不活性ガスの排気管に活性炭素のような吸着材を充填し、スルホン酸から発生する少量の硫黄系のガスの脱硫処理を行うことが好ましい。
The specific carbonization method is described below.
First, the fiber or the fiber sheet formed through the above-described spinning process is heat-treated at 500 ° C. to 2600 ° C. in a nitrogen or argon atmosphere using an electric furnace while maintaining its shape. At this time, the heat treatment time depends on the heat treatment temperature, but is preferably 0.5 to 1 hour. Further, the temperature raising time from room temperature to a predetermined heat treatment temperature is preferably 3 to 8 ° C./min. In the heat treatment step, a high-temperature furnace in an inert gas atmosphere such as a tubular furnace or an electric furnace can be used. In this case, an exhaust pipe of the inert gas is filled with an adsorbent such as activated carbon and generated from sulfonic acid. It is preferable to desulfurize a small amount of sulfur-based gas.

再加熱処理工程(グラファイト化工程)として、好ましくは上記工程で熱処理した繊維または繊維シートを、一旦室温まで戻した後、不活性ガス雰囲気中、2200℃〜3200℃の温度で再加熱処理する。これにより、最初の形態が維持された状態でグラファイト化した炭素繊維または炭素繊維からなるシートを得ることができる。本発明において、再加熱処理の際に、繊維の軸方向に張力を加えてに延伸させることによりグラファイト結晶を効率よく配向させることができるため、炭素繊維の強度が向上する。   In the reheating step (graphitizing step), preferably, the fiber or fiber sheet heat-treated in the above step is once returned to room temperature, and then reheated in an inert gas atmosphere at a temperature of 2200 ° C to 3200 ° C. As a result, it is possible to obtain a carbon fiber or a sheet made of carbon fiber that has been graphitized while maintaining the initial form. In the present invention, the graphite crystal can be efficiently oriented by applying tension in the axial direction of the fiber during the reheating treatment and stretching the fiber, thereby improving the strength of the carbon fiber.

次に本発明を実施例及び比較例より更に詳細に説明するが、本発明はこれらに限定され
るものではない。
Next, the present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited thereto.

<実施例1>
(紡糸工程)
容量200mlのガラス製ビーカーに蒸留水90gを採取し、市販のPVA(クラレ製、PVA117)10gを加え、80℃に加温しながらスターラーを用いて24時間撹拌しPVAが完全に溶解したPVA溶液100gを作製した。該PVA溶液を常温になるまで静置した後、市販のメタンスルホン酸(和光純薬製)0.1gを加え、スターラーを用いて常温で1時間撹拌する事で紡糸用溶液を作製した。
<Example 1>
(Spinning process)
90 g of distilled water is collected in a glass beaker having a capacity of 200 ml, 10 g of commercially available PVA (manufactured by Kuraray, PVA117) is added, and the mixture is stirred for 24 hours with a stirrer while heating to 80 ° C., and the PVA solution in which PVA is completely dissolved is added. 100 g were produced. After allowing the PVA solution to stand at room temperature, 0.1 g of commercially available methanesulfonic acid (manufactured by Wako Pure Chemical Industries, Ltd.) was added, and the mixture was stirred for 1 hour at room temperature using a stirrer to prepare a spinning solution.

該紡糸用溶液を、先端に18Gノンベベルシリンジ針を装着した10mlシリンジを用いて5ml採取し、エレクトロスピニング装置(カトーテック製、NEUナノファイバーエレクトロスピニングユニット)を用いて、ノズル―コレクター距離10cm、印加電圧10kV、溶液送り速度15μl/min、ドラム回転速度10rpm条件にて、2時間紡糸することで、ドラム上に繊維シートを作製した。紡糸時における装置内の温度は25℃、湿度は40%RHであった。   The spinning solution was sampled in an amount of 5 ml using a 10 ml syringe equipped with an 18 G non-bevel syringe needle at the tip, and the nozzle-collector distance was 10 cm using an electrospinning apparatus (manufactured by Kato Tech, NEU nanofiber electrospinning unit). By spinning for 2 hours under the conditions of an applied voltage of 10 kV, a solution feeding speed of 15 μl / min, and a drum rotation speed of 10 rpm, a fiber sheet was produced on the drum. During the spinning, the temperature in the apparatus was 25 ° C., and the humidity was 40% RH.

(炭化工程)
上記紡糸工程で得られた繊維シートをドラムから剥離し縦11cm横9cmにカットした後、該繊維シートの上下を縦11cm横9cm厚さ0.1cmの炭素製プレート2枚を用いて挟み卓上真空ガス置換炉(デンケン・ハイデンタル製、KDF−75)に入れ炉内の圧力を500Pa以下まで減圧した後、窒素ガスを導入し、窒素ガス雰囲気下で800℃まで5℃/minで昇温した。800℃で1時間保持した後、炉内で24時間自然冷却させ、炭素繊維シートを得た。該炭素繊維シートを電子顕微鏡(日立ハイテクノロジーズ製、Minicope TM−1000)で観察したところ、熱処理前の繊維形状を維持していた。電子顕微鏡画像を図1に示す。
(Carburizing process)
The fiber sheet obtained in the above spinning step was peeled from the drum and cut into a length of 11 cm and a width of 9 cm. Then, the upper and lower sides of the fiber sheet were sandwiched between two carbon plates having a length of 11 cm and a width of 9 cm and a thickness of 0.1 cm. After putting into a gas replacement furnace (manufactured by Denken Hydental, KDF-75) and reducing the pressure in the furnace to 500 Pa or less, nitrogen gas was introduced, and the temperature was raised to 800 ° C. at 5 ° C./min in a nitrogen gas atmosphere. . After holding at 800 ° C. for 1 hour, the mixture was naturally cooled in a furnace for 24 hours to obtain a carbon fiber sheet. When the carbon fiber sheet was observed with an electron microscope (Minicope TM-1000, manufactured by Hitachi High-Technologies Corporation), the fiber shape before the heat treatment was maintained. An electron microscope image is shown in FIG.

<比較例1>
メタンスルホン酸を加えない以外は、実施例1と同様の方法にて炭素繊維シートを作製した。炭化工程後の炭素繊維シートは炭化工程前の繊維形状を保持しておらず、繊維の一部が溶融・融着し膜化していた。電子顕微鏡画像を図2に示す。
<Comparative Example 1>
A carbon fiber sheet was produced in the same manner as in Example 1 except that methanesulfonic acid was not added. The carbon fiber sheet after the carbonization step did not retain the fiber shape before the carbonization step, and some of the fibers were melted and fused to form a film. An electron microscope image is shown in FIG.

<比較例2>
メタンスルホン酸に替えて、PVA溶液に硫酸0.5gを加えた以外は実施例1と同様の方法にて紡糸用溶液を作製した。該紡糸用溶液を用いて実施例1と同様の方法で紡糸を試みたが、シリンジから繊維が吐出されず、繊維シートを得る事ができなかった。
<Comparative Example 2>
A spinning solution was prepared in the same manner as in Example 1, except that 0.5 g of sulfuric acid was added to the PVA solution instead of methanesulfonic acid. Spinning was attempted in the same manner as in Example 1 using the spinning solution, but no fibers were discharged from the syringe, and a fiber sheet could not be obtained.

<比較例3>
メタンスルホン酸に替えて、PVA溶液に硫酸0.1gを加えた以外は実施例1と同様の方法にて炭素繊維シートを作製した。炭化工程後の炭素繊維シートは炭化工程前の繊維形状を保持しておらず、繊維の一部が溶融・融着していた。電子顕微鏡画像を図3に示す。
<Comparative Example 3>
A carbon fiber sheet was produced in the same manner as in Example 1, except that 0.1 g of sulfuric acid was added to the PVA solution instead of methanesulfonic acid. The carbon fiber sheet after the carbonization step did not retain the fiber shape before the carbonization step, and some of the fibers were melted and fused. The electron microscope image is shown in FIG.

Claims (8)

下記の(a)〜(c)の工程を含むことを特徴とする不融化工程を含まない炭素繊維または炭素繊維シートの製造方法。
(a)炭素繊維または炭素繊維シートの原料となる水溶性高分子化合物と有機スルホン酸を、水溶性高分子化合物に対する有機スルホン酸を、0.1wt%〜10.0wt%の比率で、溶解した水溶液を調整する工程
(b)上記水溶液液を紡糸し、繊維または繊維シートを得る工程
(c)上記繊維または繊維シートを不活性ガス雰囲気中、500℃〜2600℃の温度にて加熱処理する工程
A method for producing a carbon fiber or a carbon fiber sheet that does not include the infusibilizing step, which comprises the following steps (a) to (c).
(A) A water-soluble polymer compound and an organic sulfonic acid, which are raw materials for a carbon fiber or a carbon fiber sheet , are dissolved in a ratio of 0.1 wt% to 10.0 wt% of an organic sulfonic acid to the water-soluble polymer compound . Adjusting the aqueous solution (b) spinning the aqueous solution to obtain a fiber or a fiber sheet (c) heating the fiber or the fiber sheet at a temperature of 500 ° C. to 2600 ° C. in an inert gas atmosphere
更に下記の(d)の工程を含むことを特徴とする請求項1に記載の炭素繊維または炭素繊維シートの製造方法。
(d)前記(c)工程で得られた繊維または繊維シートを不活性ガス雰囲気中、2200℃〜3200℃での再加熱処理する工程
The method for producing a carbon fiber or a carbon fiber sheet according to claim 1, further comprising the following step (d).
(D) a step of reheating the fiber or fiber sheet obtained in the step (c) at 2200 ° C. to 3200 ° C. in an inert gas atmosphere;
前記水溶性高分子が、ポリビニルアルコール、ポリエチレングリコール、ポリエチレンオキシド、ポリアクリル酸、ポリビニルピロリドンである事を特徴とする請求項1〜2のいずれかに記載の炭素繊維または炭素繊維シートの製造方法。   The method for producing a carbon fiber or a carbon fiber sheet according to any one of claims 1 to 2, wherein the water-soluble polymer is polyvinyl alcohol, polyethylene glycol, polyethylene oxide, polyacrylic acid, or polyvinylpyrrolidone. 前記有機スルホン酸が、メタンスルホン酸であることを特徴とする請求項1〜3のいずれか一項に記載の炭素繊維または炭素繊維シートの製造方法。   The method for producing a carbon fiber or a carbon fiber sheet according to any one of claims 1 to 3, wherein the organic sulfonic acid is methanesulfonic acid. 前記繊維または繊維シートが、エレクトロスピニング法により得られることを特徴とする、請求項1〜のいずれか一項に記載の炭素繊維または炭素繊維シートの製造方法。 The method for producing a carbon fiber or a carbon fiber sheet according to any one of claims 1 to 4 , wherein the fiber or the fiber sheet is obtained by an electrospinning method. 請求項1〜のいずれか一項に記載の方法で製造された炭素繊維を用いることを特徴とする織物。 A woven fabric using carbon fibers produced by the method according to any one of claims 1 to 5 . 請求項1〜のいずれか一項に記載の方法で製造された炭素繊維または炭素繊維シートを用いることを特徴とする複合材料。 A composite material using a carbon fiber or a carbon fiber sheet produced by the method according to any one of claims 1 to 6 . 請求項1〜のいずれか一項に記載の方法で製造された炭素繊維または炭素繊維シートを用いることを特徴とする燃料電池用ガス拡散層。 A gas diffusion layer for a fuel cell, comprising a carbon fiber or a carbon fiber sheet produced by the method according to any one of claims 1 to 6 .
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