JPH04136266A - Surface treatment of carbon yarn and device therefor - Google Patents

Surface treatment of carbon yarn and device therefor

Info

Publication number
JPH04136266A
JPH04136266A JP25635890A JP25635890A JPH04136266A JP H04136266 A JPH04136266 A JP H04136266A JP 25635890 A JP25635890 A JP 25635890A JP 25635890 A JP25635890 A JP 25635890A JP H04136266 A JPH04136266 A JP H04136266A
Authority
JP
Japan
Prior art keywords
electrodes
ozone
carbon
carbon yarn
treatment method
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.)
Pending
Application number
JP25635890A
Other languages
Japanese (ja)
Inventor
Fujio Nakao
中尾 富士夫
Yoichi Kodama
陽一 小玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP25635890A priority Critical patent/JPH04136266A/en
Publication of JPH04136266A publication Critical patent/JPH04136266A/en
Pending legal-status Critical Current

Links

Landscapes

  • Chemical Or Physical Treatment Of Fibers (AREA)

Abstract

PURPOSE:To treat the surface of a carbon yarn in a short time uniformly and safely by passing the carbon yarn through ozone-containing air while heat- treating the carbon yarn between current-carrying electrodes and installing a specific number of electrodes and earthing both ends of the electrodes. CONSTITUTION:Three or more electrodes 2 are installed, both end of the electrodes are earthed, two or more ozone chambers 3 are laid. A carbon yarn 1 heated by current transmission between the electrodes 2 is traveled in the ozone chambers 3 of letting air containing >=10vol.% ozone concentration flow in the same direction as traveling direction of the yarn 1 to carry out the objective oxidation treatment.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は炭素縁維の新規な表面雪化処理法及び装置に関
する本のである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention is a book relating to a novel surface snow treatment method and apparatus for carbon edge fibers.

〔従来技術〕[Prior art]

炭素*aはマトリックス樹脂との接着性やぬル性を改善
するため、大素着維表面の資化処理が施さ几るのが一般
的であり、薬剤醸化処理、気相資化処理、電解酸化処理
iど多くの表面処理方法が提案さ几ている。薬剤實化処
理?′i処理時間が長くかかり工業的には不向きである
。電解酸化処理は連続的:C処理しbすいが、処理した
太素llt雅に付着する置解買の除去のための洗浄が不
可欠であり、I解液の発液処理など多くの問題がある。
In order to improve adhesion and wettability with the matrix resin, carbon*a is generally subjected to assimilation treatment on the surface of the large fibers, such as chemical fermentation treatment, vapor phase assimilation treatment, Many surface treatment methods have been proposed, including electrolytic oxidation treatment. Pharmaceutical processing? 'i It takes a long time to process and is not suitable for industrial use. Electrolytic oxidation treatment is continuous: C treatment is easy, but cleaning is indispensable to remove loose particles that adhere to the treated material, and there are many problems such as liquefaction treatment of I solution. .

その、咀気相酸化処理は、洗浄が不要でありしかも装置
が事羞であるなど多くの利点を有しているが、賃化反応
の’@I fiが維しく、処理斑を生じやすいといった
問題点がある。
The gas-phase oxidation process has many advantages such as no cleaning required and the equipment is safe. There is a problem.

気相酸化処理の1問題点を解決する九めオゾンを含む′
J!f定の温度雰囲気で処理する方法(特開昭61−1
19769号)が提案されているがオゾンが高温では非
常に分解しやすぐ、又外部加熱器で気体を加熱する方法
(=4M昭61−115;3713号)ではオゾンが供
給口から被処理系である炭素g&礁近労に到達するまで
に分解さ几効率が県ぐをる。そこで炭素#i碓が導電性
であることを利用して、炭素献遣を通を加熱することで
より炭素曖准近傍のみを加熱することにより気相酸化処
理全効率よく行う方法(特開昭61−119770号)
が提案さnている。炭素蝋礁を通電加熱処理する方法は
オゾン酸化処理をもつとも効率よ〈実施する方法である
が、人体′/cg電する恐nがあるので安全性7c間組
があった。
Contains ozone, which solves one problem in gas phase oxidation treatment.
J! A method of processing in a constant temperature atmosphere (JP-A-61-1)
No. 19769) has been proposed, but ozone decomposes very quickly at high temperatures, and in the method of heating the gas with an external heater (=4M No. 3713, 1986-115), ozone flows from the supply port into the treated system. The amount of carbon that is decomposed before reaching the carbon g & reef layer is the efficiency of the prefecture. Therefore, by taking advantage of the conductivity of carbon #i and heating only the vicinity of the carbon bond, a method of performing gas phase oxidation treatment with full efficiency (Japanese Patent Laid-Open No. 61-119770)
has been proposed. The method of heating and treating carbon wax with electricity is an efficient method that includes ozone oxidation treatment, but there is a risk of electric shock to the human body, so there is a safety rating of 7c.

〔発明が解決しようとする課題し 本発明ζ、万シン全できるだけ分解させることなく効率
:〈灸素繊錐の酸化文もを行わせ、短時間で均一に酸化
処理せしめると同時に作業性の点から安全に行う方法を
提供することにある。
[The problem to be solved by the present invention is to achieve efficiency without disassembling the entire machine as much as possible: oxidation of the moxibustion fiber cone is carried out uniformly in a short time, and at the same time, workability is improved. The goal is to provide a safe way to do so.

〔課題を解決するための手段〕[Means to solve the problem]

本発明の要旨は、炭素Jl!着を通電用w、qj1闇で
加熱処理しなから該電極間の間でオゾンを含む空気中を
通過走行せしめる#素11!惟り表面処理法に於て電極
を5個以上設置し、その両端の電極を接地することを特
徴とする炭素曽堆の表面処理法)び装置である。
The gist of the invention is that carbon Jl! #Element 11 for energizing w, qj1 heat-treated in the dark and then allowed to run through air containing ozone between the electrodes! This is a method and apparatus for surface treatment of carbon sludge, characterized in that five or more electrodes are installed in the surface treatment method, and the electrodes at both ends are grounded.

通!装置の両端を接地することにより、該電電以外での
感電を防ぐことができる。片方の端のみ投置していると
、もう片方の端以′4D炭素Jil碓に人体が接触する
と、人体に電流が流れる可能性があるので非常にa険で
ある。本発明lこよf′L′f:、本通1を袋、蓋のみ
感i坊止対責全行えば、作業上の安全性を保つことかで
さる。天素q&碓の#造工樫’IC> Zで+d、毛羽
の発生、々どてより笑素鐵錐て直接触nる壕会が多く、
通電処理する上に2いては安全・生全直めることが非常
に1要である。
Pass! By grounding both ends of the device, it is possible to prevent electric shock from sources other than the electric current. If only one end is placed, if the human body comes into contact with the 4D carbon material at the other end, it is extremely dangerous because current may flow through the human body. According to the present invention, work safety can be maintained if all precautions are taken to ensure that only the bag and lid are used. Tensuq &Usui's#Zoukashi'IC> +d in Z, the occurrence of fluff, and there are many trenches that touch directly with iron drills,
In addition to energizing, it is extremely important to ensure safety and complete repairs.

さらに第1図に示すようK、オゾンを吹き込むチャンバ
ーを2個以上設けることによって、安全性の向上とと本
に、処理の効I化を計ることができる。
Furthermore, as shown in FIG. 1, by providing two or more chambers into which K and ozone are blown, it is possible to improve the safety and increase the efficiency of the treatment.

ま±1糖状態にある炭素豐碓にオゾンを含む学究を接触
させると、オゾンD資化5叉応性が1いため1.炭素砿
碓トウの外部のみ豪化され、内部が酸化されないと(ハ
うことが起こる。こ几;d温度が7tE1ハとオゾンが
トウ内部に拡散する速度よりも、炭素暑雉とオゾンとの
反応速度が諾いために生じるものと思ゎ、する。そこで
トウの外部と内部の層化処理レベルを均−二でするため
、炭素磯碓が低温の状ルでオゾンを5つの内部まで拡散
させる必要がある。そこでチャンバー内でのオゾンを含
む空気の流Cがv4の走行方向と同じ方向となる;う;
/l:、チマー・バーのは碓入り口寸近より全オゾン全
音むガスをチャンバー内、C送9込み、ム姫り出0汀乙
a徘ズすることに:り、トウ内、’C,,rシンと均−
Iζぶ教させることができ、斑無く薫化処理することが
できる。
However, when carbon fibers in the monosaccharide state are brought into contact with ozone-containing substances, the ozone D assimilation property is 1, so 1. If only the outside of the carbon tow is oxidized and the inside is not oxidized, this happens. I believe that this occurs because the reaction rate is low.Therefore, in order to equalize the level of stratification on the outside and inside of the tow, ozone is diffused into the inside of the tow using a low-temperature glass tube. Therefore, the flow C of air containing ozone in the chamber is in the same direction as the traveling direction of v4;
/l:, From near the entrance of the chimer bar, all the ozone gas was sent into the chamber. , r syn and uniform
Iζ can be taught, and the aromatic treatment can be carried out without unevenness.

オゾン濃度にば@て制限は鳳込が、α5容積鴫以上好ま
しくは1.0容積4以上の濃度で処理する方が効率よく
酸化される。
Regarding the ozone concentration, it is more efficient to oxidize when the ozone concentration is treated at a concentration of α5 volume or more, preferably 1.0 volume or more.

′を礪ロールは両端を設置するため少なくとも3@以上
は必要であるが、チャンバーの数には制限がなく、1個
のチャンバーの中に!版ロールを3個設けても良く、第
1図のようと2個以上のチャンバーを使用しても良い。
The roll requires at least 3 or more to install both ends, but there is no limit to the number of chambers, and there is no limit to the number of chambers in one chamber! Three plate rolls may be provided, or two or more chambers may be used as shown in FIG.

しかし、設備費及び作業性の点から2個のチャンバーを
使用するのがもつとも効率が良い。
However, in terms of equipment costs and workability, it is more efficient to use two chambers.

通電用電源も基に制限はなく交流、直流どちらでも良く
、また電源の数は各チャンバーて1個づつ設けても良く
、第1図のように1個の電源で各通!用tWクールに電
流が流九るようにしても良−0 〔実施例〕 以下実施例によ、!7本本発明真木的に説明する。
There are no restrictions on the power supply for energizing, either AC or DC may be used, and the number of power supplies may be one for each chamber, as shown in Figure 1, each power supply can be used for each! It is also possible to allow the current to flow through the tW cool. [Example] Below is an example! 7 This invention will be explained in detail by Maki.

(−fiJ定方法) 「寅累jj11錐の表’is性1paBは、耳開昭60
−246864号、60−252718号各公報に示さ
几ているCyclicVO1tammetr7 法疋よ
って測定した。本発明でいうCyclic Volta
zmetry法とは、ポテンシオスタットとファンクシ
ョンゼネレーターとからなる分析装置尤よって炭素繊維
を一方の電極に用いて測定する方法をいう。
(-fiJ determination method) "The table'is characteristic of the 11 cone of the tiger is
It was measured by the CyclicVO1tammeter7 method shown in the publications No.-246864 and No.60-252718. Cyclic Volta in the present invention
The zmetry method refers to a method of measuring using an analyzer consisting of a potentiostat and a function generator, and carbon fiber as one electrode.

本発明では、54りん酸水溶液を甲いてpHIIだ設定
し、窒素をバブリングさせ溶存實素を除去する。参照電
極としてAg/AgC1電極を用い、対極には十分な表
面積を有する白金を板を用い、炭素繊維を作動極として
測定する。電位操作範囲ば、−cL2〜αsv’3とし
、i住換作速度は、2mv/seaとする3 XYL/
:!−ダーにより、電位−電流曲線を描き、5回以上掃
引させ、曲線が安定した段階で、Ag/AgC1を層に
対して、+l14vでの電位全基$にとってI流ff1
1を読み取り、次式に従ってLpa’r算出した。
In the present invention, a 54-phosphoric acid aqueous solution is prepared and set to pH II, and dissolved nitrogen is removed by bubbling nitrogen. An Ag/AgC1 electrode is used as a reference electrode, a platinum plate with a sufficient surface area is used as a counter electrode, and a carbon fiber is used as a working electrode for measurement. The potential operation range is -cL2 to αsv'3, and the relocation speed is 2mv/sea.3XYL/
:! - Draw a potential-current curve using a driver, sweep it 5 times or more, and when the curve becomes stable, the I current ff1 for the total potential group $ at +l14v with respect to the Ag/AgC1 layer.
1 was read and Lpa'r was calculated according to the following formula.

目付、密度は、J工5−R7601に記社さ几ている方
法によって求めた。
The basis weight and density were determined by the method described in J.K. 5-R7601.

「コンポジット性能」け三菱レイヨン%W◆540エボ
ギシンジンを用いてA37M  D790に準じて、増
惟方向と直角方向の曲げ強度(テS±)を測定した。
"Composite Performance" Using Mitsubishi Rayon %W◆540 Evogi Shinjin, the bending strength (TeS±) in the direction perpendicular to the direction of growth was measured according to A37M D790.

実施例1 弾性率24 t/m”の#毫9,412にトウ50本を
120 s/hrの速度で、1個のチャン/<−の長さ
が50国である炉を2炉走行ぜしb1各チャンバー間の
間で通!処理するのに際して、第1図のように1面端を
投首して各チャン/く−に27Aの電流を流した。オゾ
ンがt4容墳鴫濃度の空気を、CF走走行万石1同じ7
向に流れるように1N堝’ / h r 流した。
Example 1 50 tows of #9,412 rods with a modulus of elasticity of 24 t/m were run at a speed of 120 s/hr through two furnaces each having a length of 50 mm. During processing, a current of 27 A was passed through each chamber by tilting the end of one side as shown in Figure 1. Air, CF running Mangoku 1 same 7
It was flowed in a 1N basin/hr so that it flowed in the opposite direction.

その結果、処理前の炭素Wl碓の1つaは11(tIA
/cN2)であったが、本処理に:すLph d(12
3+’ pA//cn?)まで上昇した。
As a result, one a of carbon Wl before treatment is 11 (tIA
/cN2), but in this process: Lph d(12
3+'pA//cn? ) rose to

処理、″@Dコンポジット/4:能″PS二江s<q/
舅2であつ之が、I処理/こ;glo:<・J/箇2ま
で同上した。
Processing, ``@D Composite/4: Noh'' PS Futae s<q/
Atsuyuki in father-in-law 2 did the same as above until I treatment/ko;glo:<・J/section 2.

また本装置処理前、処理後の炭素繊維に人体が接触して
本安全であることを確かめた。
Furthermore, human bodies came into contact with the carbon fibers before and after treatment with this device, and it was confirmed that the device was completely safe.

実施例2 炭素繊維の処理速度、処理電流を変えて、実施例1と同
様な処理を行い得ら几た寅饗朦碓の表面特性(ipa)
及びコンポジット性3(Fs±)を測定したところ第1
表に示すよりなis梁が得らnた。
Example 2 Surface characteristics (IPA) of tora buns obtained by performing the same treatment as in Example 1 by changing the processing speed and processing current of carbon fibers
When the composite property 3 (Fs±) was measured, the first result was
IS beams shown in the table were obtained.

第1表 4、固有の、1mな説問 第1図と本発明を実施子るので好適な装置の略解図を示
す。
Table 1 shows a schematic illustration of a suitable apparatus for implementing the present invention with a unique, 1m explanatory diagram.

1・・・・・炭素繊維 2・・・・・通電、■熱用の1.極ロール5・・・・・
オゾンチャンバ 4・−・・・オゾンを含むガスD吹込入口5・・・・・
排気口 6・・・・・1竃用tfi 7・・・・・接地用端子 精秤出願人 三菱レイヨン株式会ケ
1...Carbon fiber 2...Electricity, ■ Heat use 1. Extreme roll 5...
Ozone chamber 4 --- Gas D inlet containing ozone 5 ---
Exhaust port 6...TFI for 1 stove 7...Grounding terminal precision scale Applicant: Mitsubishi Rayon Co., Ltd.

Claims (1)

【特許請求の範囲】 1、炭素繊維を通電用電極間で加熱処理しながら該電極
間の間でオゾンを含む空気中を通過走行せしめる炭素繊
維の表面処理法に於て、電極を3個以上設置し、その両
端の電極を接地することを特徴とする炭素繊維の表面処
理法。 2、オゾンを吹き込むチャンバーを2個以上設けること
を特徴とする請求項1記載の処理法。 3、チャンバー内でのオゾンを含む空気の流れが繊維の
走行方向と同じ方向となるように、チャンバーの繊維入
り口付近よりオゾンを含む空気をチャンバー内に送り込
み、繊維の出口付近より排気することを特徴とする請求
項1記載の処理法。 4、オゾン濃度が1.0容積%以上である空気を使用す
ることを特徴とする請求項1記載の処理法。 5、請求項1記載の処理法を実施するための装置。
[Scope of Claims] 1. In a surface treatment method for carbon fiber in which the carbon fiber is heat-treated between current-carrying electrodes and passed through air containing ozone between the electrodes, three or more electrodes are used. A carbon fiber surface treatment method characterized by installing the carbon fiber and grounding the electrodes at both ends. 2. The treatment method according to claim 1, further comprising providing two or more chambers into which ozone is blown. 3. In order to ensure that the flow of air containing ozone in the chamber is in the same direction as the running direction of the fibers, air containing ozone is sent into the chamber from near the fiber entrance of the chamber and exhausted from near the fiber exit. The treatment method according to claim 1, characterized in that: 4. The treatment method according to claim 1, characterized in that air having an ozone concentration of 1.0% by volume or more is used. 5. An apparatus for carrying out the treatment method according to claim 1.
JP25635890A 1990-09-26 1990-09-26 Surface treatment of carbon yarn and device therefor Pending JPH04136266A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25635890A JPH04136266A (en) 1990-09-26 1990-09-26 Surface treatment of carbon yarn and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25635890A JPH04136266A (en) 1990-09-26 1990-09-26 Surface treatment of carbon yarn and device therefor

Publications (1)

Publication Number Publication Date
JPH04136266A true JPH04136266A (en) 1992-05-11

Family

ID=17291575

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25635890A Pending JPH04136266A (en) 1990-09-26 1990-09-26 Surface treatment of carbon yarn and device therefor

Country Status (1)

Country Link
JP (1) JPH04136266A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335624A (en) * 2005-06-06 2006-12-14 Denso Corp Method and apparatus for manufacturing carbon nanotube fiber
KR101236199B1 (en) * 2011-03-31 2013-02-22 최대규 Apparatus for maunfacturing carbon fiber
KR101296718B1 (en) * 2011-07-20 2013-08-20 최대규 A manufacture apparatus for carbon fiber

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335624A (en) * 2005-06-06 2006-12-14 Denso Corp Method and apparatus for manufacturing carbon nanotube fiber
KR101236199B1 (en) * 2011-03-31 2013-02-22 최대규 Apparatus for maunfacturing carbon fiber
KR101296718B1 (en) * 2011-07-20 2013-08-20 최대규 A manufacture apparatus for carbon fiber

Similar Documents

Publication Publication Date Title
DE69328139D1 (en) Process for pickling and passivating stainless steel without using nitric acid
JPH06182195A (en) Method for glow discharge plasma treatment under atmospheric pressure
PT76472A (en) NEW DERIVATIVES OF CYCLOALKA &lt;C&gt; PYRROL CARBONE ACES PROCESS FOR THE MANUFACTURE OF THE AGENTS CONTAINING THEM AND THEIR USE, AND NEW CYCLOALKA &lt;C&gt; PYRROL CARBON ACIDS AS INTERMEDIATES AND METHOD FOR THE PRODUCTION THEREOF
ATE113324T1 (en) METAL OXIDIZING ARRANGEMENT AND PROCESS.
JPH04136266A (en) Surface treatment of carbon yarn and device therefor
ES8104136A1 (en) Process and apparatus for regenerating sulfuric acid.
DE69907767D1 (en) Process for the thermal processing of workpieces by means of a thermal transfer liquid and condensation furnace for carrying out the process
US20040052680A1 (en) Treatment of environmental unit atmosphere and/or interior with generation of radicals
WO2023191194A1 (en) Apparatus for preparing ammonium sulfate by using combustion exhaust gas
JPS6259504A (en) Ozonizer by corona discharge
DE69602867D1 (en) Device and method for producing wire electrodes for EDM cutting
US482879A (en) Method of and apparatus for tempering wire
ATE201282T1 (en) METHOD AND DEVICE FOR CONTROLLING THE ELECTRICAL CURRENT DENSITY OVER A WORKPIECE DURING HEAT TREATMENT IN PLASMA
JP4071874B2 (en) Carbon fiber processing method
JPH03164405A (en) Ozonizer
US20220296751A1 (en) Plasma treatment
JPS61119770A (en) Surface treatment of carbon fiber
SU906945A1 (en) Method for purifying effluents
BR0208747B1 (en) hydrogen peroxide removal process and apparatus.
JPH06163480A (en) Surface treating method and surface treater
JP3509405B2 (en) Improvement of furnace atmosphere in continuous heat treatment furnace for steel strip
Yonetani et al. Residual Stresses Produced in Steel Specimens of Various Composition by Induction Hardening
SU804572A1 (en) Method and device for carbon material purification
JPH05271750A (en) Heat treatment method of steel material
Kinoshita et al. Removal of SO 2 using a wet-type nonthermal plasma reactor