JPH0153362B2 - - Google Patents
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- JPH0153362B2 JPH0153362B2 JP15727182A JP15727182A JPH0153362B2 JP H0153362 B2 JPH0153362 B2 JP H0153362B2 JP 15727182 A JP15727182 A JP 15727182A JP 15727182 A JP15727182 A JP 15727182A JP H0153362 B2 JPH0153362 B2 JP H0153362B2
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- fibers
- organic
- substance
- inorganic
- heat treatment
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Description
【発明の詳細な説明】 本発明は炭素繊維の製造方法に関する。[Detailed description of the invention] The present invention relates to a method for manufacturing carbon fiber.
耐熱性や耐薬品性など多くの長所を有する炭素
の性質を活用した炭素繊維をより優れたものとす
るために、近年、形状に対するアプローチが顕著
化している。その最たるものが軽量化や断熱性の
向上などを可能とする中空状の炭素繊維である。 In recent years, approaches to shape have become more prominent in order to improve carbon fibers that take advantage of the many advantages of carbon, such as heat resistance and chemical resistance. The most important example is hollow carbon fiber, which makes it possible to reduce weight and improve heat insulation.
しかし、従来の中空状炭素繊維を製造する方法
にはいくつかの欠点があつた。例えば、ノボラツ
クを主成分とするフエノール系樹脂を溶融紡糸し
た後一部硬化し、次いで未硬化部分を溶媒にて溶
出して中空繊維とし、これを炭化処理する方法
(特公昭51−5090号)、有機高分子体からなる繊維
に無水硫酸あるいはクロルスルホン酸を接触させ
ることによつて、内心部を未処理に残して表面処
理し、これを有機高分子の熱分解温度以上に加熱
して焼成する方法(特開昭49−101618号)、ポリ
アクリルニトリル繊維を酸化性雰囲気中で200〜
300℃に加熱して、得られた耐炎繊維の熱分解時
の発熱量が原糸の30〜60%の範囲のものを、非酸
化性雰囲気中で500℃以上に加熱して炭化する方
法(特開昭50−142819号)など公知の方法におい
ては、確かに中空状の炭素繊維が得られる旨開示
しているが、熱処理前の繊維に対する処理が制御
不十分となつたり、熱処理時の繊維収縮が大きく
なり過ぎたりして、得られた炭素繊維はその中空
部形状などを実質的に制御されないものとなつて
しまう。 However, conventional methods for producing hollow carbon fibers have had several drawbacks. For example, a method in which a phenolic resin whose main component is novolac is melt-spun, then partially cured, and then the uncured portion is eluted with a solvent to form hollow fibers, which are then carbonized (Japanese Patent Publication No. 51-5090). , by contacting the fibers made of organic polymer with sulfuric anhydride or chlorosulfonic acid, the inner core is left untreated and the surface is treated, and then this is heated to a temperature higher than the thermal decomposition temperature of the organic polymer and fired. (Japanese Unexamined Patent Publication No. 49-101618), polyacrylonitrile fibers are heated in an oxidizing atmosphere to
A method of carbonizing the flame-resistant fibers obtained by heating to 300℃ and heating them to 500℃ or higher in a non-oxidizing atmosphere ( Although it is disclosed that hollow carbon fibers can be obtained using known methods such as JP-A No. 50-142819), the treatment of the fibers before heat treatment is insufficiently controlled, and the fibers during heat treatment are If the shrinkage becomes too large, the shape of the hollow portion of the obtained carbon fiber becomes substantially uncontrollable.
本発明は上述した点に鑑みなされたものであ
り、焼成によつての炭素収率の高い有機物Aと、
同じく炭素収率の低い有機物B及び/又は焼成温
度迄の熱処理の過程で気散化してしまうか薬品処
理で除去される無機物とよりなる繊維を、前記有
機物Bや無機物の消失を生じることなく前記有機
物Aの耐炎化処理し、その後、前記有機物Aの焼
成温度迄の熱処理と必要に応じての薬品処理によ
る前記無機物除去をすることを特徴とする炭素繊
維の製造方法を要旨とするものである。 The present invention has been made in view of the above-mentioned points, and includes an organic substance A having a high carbon yield through calcination,
Fibers made of organic matter B, which also has a low carbon yield, and/or inorganic matter that is vaporized in the process of heat treatment up to the calcination temperature or removed by chemical treatment, are processed without causing the disappearance of the organic matter B or the inorganic matter. The gist of the present invention is a method for producing carbon fibers, which comprises subjecting organic substance A to flame-retardant treatment, and then heat-treating the organic substance A to a firing temperature and removing the inorganic substance by chemical treatment as necessary. .
まず、本発明で使用される材料について説明す
ると、有機物Aとしては、ポリ塩化ビニル、ポリ
塩化ビニリデン、塩化ビニル−酢酸ビニル共重合
体、塩素化ポリ塩化ビニル、塩素化ポリエチレン
などの含塩素樹脂やフラン系樹脂やポリアクリル
ニトリルをはじめとする各種合成樹脂は勿論、ポ
リ塩化ビニルの非酸化性雰囲気中乾溜物などのピ
ツチ、セルロース誘導体、リグニン誘導体、アラ
ビアゴム、ポリビニルアルコールなどが列挙で
き、有機物Bとしては、ポリエチレン、ポリプロ
ピレン、ポリブタジエン、ポリイソブチレン、ポ
リスチレン、ナイロン、ポリメタクリル酸メチ
ル、ポリメタクリル酸エチル、ポリ−α−メチル
スチレン、ポリメタメチルスチレン、トリフルオ
ロスチレン、ポリ−α−ドイテロスチレン、ポリ
エステル、天然ゴム、ブチルゴム、ポリテトラフ
ルオロエチレン、ロジン、サリチル酸、アントラ
キノン、ナフタセンなどが例挙できるが、決して
完全な区分を必要とされるものではない。即ち、
クロム、マンガン、鉄、コバルト、ニツケル、亜
鉛、銅などの金属(合金も含む)及びその酸化
物、炭化物など各種化合物の粉末や有機錯塩とい
つたように、適宜エマルジヨンとかデイスパージ
ヨンとかいつた状態で少量割合で使用されながら
炭化促進材として働くものを併用したりすれば炭
素収率を高めることができるからである。従つ
て、有機物A、有機物Bとは、繊維状態にあつ
て、後述する焼成温度迄の熱処理によつて、炭素
収率が高く、低く(零を含む)なるよう、他の材
料とともに混合物化、化合物化されたものも示す
ものである。また、無機物としては、アルミニウ
ム、亜鉛、カドミウム、銅、酸化カドミウム、酸
化バリウム、炭酸カルシウム、炭酸ナトリウム、
塩化ナトリウム、硫化亜鉛などが例挙できるが、
焼成温度迄の熱処理の過程で気散化してしまつた
り薬品処理で除去されるものならば何でもよい。
薬品処理の代表例としては酸、アルカリの水溶液
あるいは水による溶解除去が挙げられる。 First, to explain the materials used in the present invention, organic substances A include chlorine-containing resins such as polyvinyl chloride, polyvinylidene chloride, vinyl chloride-vinyl acetate copolymer, chlorinated polyvinyl chloride, and chlorinated polyethylene. In addition to various synthetic resins such as furan resins and polyacrylonitrile, examples include pitch, such as dry distillation of polyvinyl chloride in a non-oxidizing atmosphere, cellulose derivatives, lignin derivatives, gum arabic, and polyvinyl alcohol. Examples include polyethylene, polypropylene, polybutadiene, polyisobutylene, polystyrene, nylon, polymethyl methacrylate, polyethyl methacrylate, poly-α-methylstyrene, polymetamethylstyrene, trifluorostyrene, poly-α-deuterostyrene, Examples include polyester, natural rubber, butyl rubber, polytetrafluoroethylene, rosin, salicylic acid, anthraquinone, naphthacene, etc., but complete classification is by no means necessary. That is,
Powders and organic complex salts of metals (including alloys) such as chromium, manganese, iron, cobalt, nickel, zinc, and copper, and their oxides and carbides, as well as emulsions and dispersions as appropriate. This is because the carbon yield can be increased by using together with a substance that acts as a carbonization accelerator while being used in a small amount. Therefore, organic matter A and organic matter B are in the form of fibers and are mixed with other materials so that the carbon yield is high or low (including zero) by heat treatment up to the firing temperature described below. It also shows compounds that have been made into compounds. In addition, inorganic substances include aluminum, zinc, cadmium, copper, cadmium oxide, barium oxide, calcium carbonate, sodium carbonate,
Examples include sodium chloride and zinc sulfide.
Any material may be used as long as it is vaporized during the heat treatment up to the firing temperature or removed by chemical treatment.
Typical examples of chemical treatment include dissolution and removal using an aqueous acid or alkali solution or water.
無機物は有機物Bと基本的使用目的を同じくす
る。しかし、好適に使用される範囲は相違点を有
する。無機物は一般に成形性が劣り、例えば細線
状にするには相当の延性があることが望まれた
り、あるいは、ウイスカーのように大きさの制限
を受けたりする。相対的に、有機物Bはコスト、
成形性の点では無機物に優るが、熱的安定性では
劣る。従つて、中空状の炭素繊維を得るには断面
が星形などの多角形あるいは円形といつた繊維化
の容易な有機物Bを使用する方が概して有利であ
り、分散多孔状の炭素繊維を得るなら、粒子化、
粉体化は容易であるから、無機物を使用する方が
概して有利である。 Inorganic substances have the same basic purpose of use as organic substance B. However, there are differences in the ranges that are preferably used. Inorganic materials generally have poor moldability; for example, considerable ductility is required to form them into thin wires, or they are subject to size restrictions, such as whiskers. Comparatively, organic matter B costs
It is superior to inorganic materials in terms of moldability, but inferior in thermal stability. Therefore, in order to obtain hollow carbon fibers, it is generally more advantageous to use organic material B that is easy to fiberize and whose cross section is polygonal, such as a star, or circular, and to obtain dispersed porous carbon fibers. Then, particleization,
It is generally advantageous to use inorganic materials since they are easier to powder.
また、無機物と有機物Bとの併用は種々の利点
を生む。例えば、フイルター用材などとして好ま
しい中空かつ分散多孔状の炭素繊維は前述組み合
わせて容易に得られるし、例えば、有機物Bの表
面を金属めつきなどしたものを使用すると両者の
長所を発揮することができる。 Moreover, the combination of inorganic substance and organic substance B produces various advantages. For example, hollow and dispersed porous carbon fibers, which are preferred as filter materials, can be easily obtained by combining the above-mentioned materials, and the advantages of both can be obtained by using, for example, organic material B whose surface is plated with metal. .
次に、上述有機物A、有機物B、無機物のそれ
ぞれ1種もしくは2種以上、それに必要に応じて
使用される可塑剤、溶剤、安定剤などよりなり、
必要に応じて適宜集束、撚糸などされた繊維の炭
素繊維化処理について説明する。 Next, it consists of one or more types of each of the above-mentioned organic substance A, organic substance B, and inorganic substance, as well as a plasticizer, a solvent, a stabilizer, etc., which are used as necessary.
The carbon fiber treatment of the fibers, which are bundled, twisted, etc. as necessary, will be explained.
炭素繊維化処理は有機物Aを中心に考えた場
合、耐炎化と炭素化とに大別される。耐炎化処理
は有機物Aの炭素の割合を高め、形状維持や製品
強度に効果をもたらすもので、必要に応じて適宜
張力をかけながら酸化雰囲気中で、例えば200〜
300℃程度といつた低温熱処理する方法や薬品処
理する方法などがあるが、工業的に見た場合、比
較的大きなものの生産や大量生産が可能で、か
つ、品質安定性に優れる点で熱処理が好適であ
る。熱処理における問題は熱処理中に有機物Bや
無機物が解重合や昇華などして消失してしまわな
いよう留意することぐらいであろう。尤も、薬品
処理などする場合でも有機物Bや無機物の消失に
対する留意は必要である。有機物Aが十分に耐炎
化される前に有機物Bや無機物が消失して、残つ
た有機物Aの繊維の炭素化をすれば、従来技術と
同様、大きな繊維収縮による中空部あるいは孔部
の制御不能を生じることになる。従つて、熱処理
する場合、使用される有機物Bとしては、ナイロ
ンやポリテトラフルオロエチレンなどのように分
解温度の高いものが好ましい一例として挙げられ
る。また、分解温度の高いものは一般に軟化点や
融点も高く、例えば、有機物Aとして塩化ビニル
を使用して中空状炭素繊維を得んとする場合のよ
うに、熱処理時の形状繊維の主役として働かせる
こともでき得る。尚、耐炎化された塩化ビニルな
どが自身で形状維持できることは言うまでもな
い。 When considering the organic substance A as the main component, carbon fiber treatment can be roughly divided into flame resistance and carbonization. Flame-retardant treatment increases the proportion of carbon in organic substance A, which has the effect of maintaining shape and improving product strength.
There are methods such as low-temperature heat treatment, such as around 300℃, and chemical treatment, but from an industrial perspective, heat treatment is preferred because it allows production of relatively large items and mass production, and has excellent quality stability. suitable. The only problem in heat treatment is to be careful not to cause organic matter B and inorganic matter to disappear due to depolymerization, sublimation, etc. during heat treatment. Of course, even in the case of chemical treatment, it is necessary to pay attention to the disappearance of organic matter B and inorganic matter. If organic matter B and inorganic matter disappear before organic matter A becomes sufficiently flame resistant and the remaining organic matter A fibers are carbonized, the hollow or pore portions will become uncontrollable due to large fiber shrinkage, as in the conventional technology. will occur. Therefore, in the case of heat treatment, preferable examples of the organic substance B used include those having a high decomposition temperature, such as nylon and polytetrafluoroethylene. In addition, materials with a high decomposition temperature generally have high softening and melting points, and for example, when vinyl chloride is used as organic substance A to obtain hollow carbon fibers, they act as the main character of the shaped fiber during heat treatment. It may also be possible. It goes without saying that flame-resistant vinyl chloride can maintain its shape by itself.
炭素化処理は有機物Aを十分に炭素化、また場
合によつては黒鉛化するまで熱処理することであ
り、本発明ではこれを焼成温度迄の熱処理と表わ
したが、窒素雰囲気などの還元雰囲気や真空雰囲
気など一般に非酸化雰囲気と呼ばれる中で500℃
程度〜3000℃程度迄加熱して行う。温度が高いと
黒鉛化する。この過程で有機物Bはそのほとんど
もしくは全部が消失し、また、無機物も消失す
る。消失しない無機物が予め及び/又は更に薬品
処理で適宜除去されることは前述のとおりであ
る。 Carbonization treatment is heat treatment of organic matter A until it is sufficiently carbonized and, in some cases, graphitized. In the present invention, this is referred to as heat treatment up to the firing temperature, but it may also be treated in a reducing atmosphere such as a nitrogen atmosphere, or in a reducing atmosphere such as a nitrogen atmosphere. 500℃ in what is generally called a non-oxidizing atmosphere such as a vacuum atmosphere
This is done by heating to about 3000℃. It graphitizes at high temperatures. In this process, most or all of the organic matter B disappears, and the inorganic matter also disappears. As described above, inorganic substances that do not disappear are appropriately removed in advance and/or further by chemical treatment.
無機物の全てを積極的に除去しない場合もあ
る。薬品処理をしない、あるいは薬品処理をして
も無機物の一部が残るようにするのである。中空
状炭素繊維を得る場合について例をとると、有機
物Bを細線状にし、その表面を金属めつきなどし
て覆い、更にその外周に有機物Aが存在する繊維
を熱処理し、有機物Bだけを除去すると中空壁部
に金属を有する炭素繊維が得られる。導電性の向
上や金属的弾性の必要がある場合など、わざわざ
金属を除去する必要はない。 In some cases, not all inorganic substances are actively removed. Either no chemical treatment is applied, or even after chemical treatment some inorganic matter remains. For example, when obtaining hollow carbon fibers, organic material B is made into a thin wire, the surface is covered with metal plating, etc., and the fiber with organic material A present on its outer periphery is further heat-treated to remove only organic material B. Then, a carbon fiber having metal in the hollow wall portion is obtained. There is no need to remove metal when there is a need for improved conductivity or metallic elasticity.
実施例 1
太さ3ミルの6.6ナイロン繊維をポリアクリロ
ニトリルの30%ジメチルホルムアミドの溶液に浸
漬し、0.3mmφのダイスを通して直ちに乾燥し、
6.6ナイロンの外周を実質的均一にポリアクリロ
ニトリルで覆つた繊維を得、これを空気雰囲気中
で200℃10時間の耐炎化処理をし、次いで、窒素
雰囲気中で500℃迄20℃/時間の昇温とその後の
1300℃迄100℃/時間の昇温並びに1300℃繊維の
1時間熱処理をし中空状炭素繊維を得た。Example 1 A 6.6 nylon fiber with a thickness of 3 mils was immersed in a solution of polyacrylonitrile and 30% dimethylformamide, passed through a 0.3 mmφ die, and immediately dried.
6.6 A fiber made of nylon whose outer periphery was substantially uniformly covered with polyacrylonitrile was obtained, and this was subjected to flameproofing treatment at 200°C for 10 hours in an air atmosphere, and then heated to 500°C at a rate of 20°C/hour in a nitrogen atmosphere. Warm and then
Hollow carbon fibers were obtained by increasing the temperature to 1300°C at a rate of 100°C/hour and heat treating the fibers at 1300°C for 1 hour.
実施例 2
太さ6ミルのポリテトラフルオルエチレン繊維
の外周に塩化ビニリデン−アクリルニトリル共重
合体が配するよう、クロスヘツド使用の押出機で
電線被覆の要領で押出し、太さ10ミルの繊維を
得、これを酸素雰囲気中で230℃3時間の耐炎化
処理(この場合、塩化ビニリデン−アクリロニト
リル共重合体は脱塩酸反応をする)し、次いで、
真空雰囲気中で700℃迄20℃/時間の昇温とその
後の1500℃迄100℃/時間の昇温並びに1500℃繊
維の1.5時間熱処理をし、中空炭素繊維を得た。Example 2 Polytetrafluoroethylene fibers with a thickness of 6 mils were extruded using an extruder using a crosshead in the same manner as for covering electric wires so that vinylidene chloride-acrylonitrile copolymer was distributed around the outer periphery of polytetrafluoroethylene fibers with a thickness of 10 mils. This was subjected to flameproofing treatment at 230°C for 3 hours in an oxygen atmosphere (in this case, the vinylidene chloride-acrylonitrile copolymer undergoes a dehydrochloric acid reaction), and then
In a vacuum atmosphere, the temperature was raised to 700°C at a rate of 20°C/hour, then the temperature was raised to 1500°C at a rate of 100°C/hour, and the fibers were heat-treated at 1500°C for 1.5 hours to obtain hollow carbon fibers.
実施例 3
ラム式押出機のシリンダー内に、ポリ塩化ビニ
ル70重量%と酸化亜鉛粉末25重量%と可塑剤(ジ
オクチルフタレート)5重量%との混合物を入
れ、120℃にして0.1mmφの細線状に押出した。こ
れを空気雰囲気中で230℃5時間の耐炎化処理し、
次いで、窒素雰囲気中で1100℃迄30℃/時間の昇
温並びに1100℃維持の30分間熱処理をし、分散多
孔状の炭素繊維を得た。Example 3 A mixture of 70% by weight of polyvinyl chloride, 25% by weight of zinc oxide powder, and 5% by weight of a plasticizer (dioctyl phthalate) was placed in the cylinder of a ram extruder, and heated to 120°C to form a thin wire of 0.1 mmφ. It was pushed out. This was flame-resistant treated at 230℃ for 5 hours in an air atmosphere.
Next, heat treatment was performed in a nitrogen atmosphere at a rate of 30°C/hour to 1100°C and maintained at 1100°C for 30 minutes to obtain dispersed porous carbon fibers.
実施例 4
実施例1において、ナイロン繊維として、予め
無電解めつき及びその上からの電気めつきによつ
てニツケル皮膜を形成しておいたものを使用した
以外すべて実施例1と同様にした。Example 4 Everything was the same as in Example 1, except that the nylon fibers had a nickel film formed in advance by electroless plating and electroplating thereon.
実施例 5
実施例3において、耐炎化処理した繊維の焼成
温度迄の熱処理として、窒素雰囲気中で700℃迄
20℃/時間の昇温並びに700℃維持の1時間熱処
理とした以外すべて実施例3と同様にし、更に、
10%塩酸水溶液中で超音波洗浄の要領で10時間処
理した。Example 5 In Example 3, the flame-retardant fibers were heat-treated up to 700°C in a nitrogen atmosphere to the firing temperature.
The procedure was the same as in Example 3 except that the temperature was increased at 20°C/hour and the heat treatment was maintained at 700°C for 1 hour, and further,
It was treated in a 10% aqueous hydrochloric acid solution for 10 hours in an ultrasonic cleaning manner.
本発明は、一例として示した各実施例を含む上
述のように、炭化させるべき物質と炭化させるべ
きではない物質とを併用し、炭化させるべき物質
を十分に炭化させるべき状態にした後、炭化させ
るべきではない物質の除去と炭化させるべき物質
の炭化をするという考え方に基づくものであり、
除去される物質の形状に応じて所望の炭素繊維
を、しかも、仮り1μmとは1mmといつたように
繊維の太さに依らず寸法精度のよい繊維を得るこ
とができ、補強用材とか気体や液体のフイルター
用材あるいは断熱用材など従来の利用分野におけ
る機能品質を向上するのみならず、電気分野など
その利用分野の拡大をも可能化するものである。 As described above, including each embodiment shown as an example, the present invention uses a substance that should be carbonized and a substance that should not be carbonized together, brings the substance that should be carbonized to a state where it should be sufficiently carbonized, and then carbonizes the substance. It is based on the idea of removing substances that should not be carbonized and carbonizing substances that should be carbonized.
It is possible to obtain the desired carbon fiber according to the shape of the substance to be removed, and also to obtain fibers with good dimensional accuracy regardless of the thickness of the fiber, for example, 1 μm is 1 mm. This not only improves the functional quality of conventional applications such as liquid filter materials and insulation materials, but also enables the expansion of applications such as electrical fields.
Claims (1)
同じく炭素収率の低い有機物(B)及び/又は焼成温
度迄の熱処理の過程で気散化してしまうか薬品処
理で除去される無機物とよりなる繊維を、前記有
機物(B)や無機物の消失を生じることなく前記有機
物(A)の耐炎化処理し、その後、前記有機物(A)の焼
成温度迄の熱処理と必要に応じての薬品処理によ
る前記無機物除去をすることを特徴とする炭素繊
維の製造方法。1 An organic substance (A) with a high carbon yield through calcination,
Similarly, fibers made of organic matter (B) with a low carbon yield and/or inorganic matter that is vaporized during the heat treatment process up to the calcination temperature or removed by chemical treatment are used to reduce the disappearance of the organic matter (B) and inorganic matter. Production of carbon fibers, characterized in that the organic substance (A) is flame-resistant treated without generation, and then the inorganic substance is removed by heat treatment up to the firing temperature of the organic substance (A) and, if necessary, chemical treatment. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15727182A JPS5947425A (en) | 1982-09-09 | 1982-09-09 | Manufacture of carbon fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15727182A JPS5947425A (en) | 1982-09-09 | 1982-09-09 | Manufacture of carbon fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5947425A JPS5947425A (en) | 1984-03-17 |
| JPH0153362B2 true JPH0153362B2 (en) | 1989-11-14 |
Family
ID=15646002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15727182A Granted JPS5947425A (en) | 1982-09-09 | 1982-09-09 | Manufacture of carbon fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5947425A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7073748B2 (en) * | 2017-02-08 | 2022-05-24 | 東レ株式会社 | Manufacturing method of carbon membrane for fluid separation |
-
1982
- 1982-09-09 JP JP15727182A patent/JPS5947425A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5947425A (en) | 1984-03-17 |
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