JPS6325085B2 - - Google Patents

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Publication number
JPS6325085B2
JPS6325085B2 JP56214089A JP21408981A JPS6325085B2 JP S6325085 B2 JPS6325085 B2 JP S6325085B2 JP 56214089 A JP56214089 A JP 56214089A JP 21408981 A JP21408981 A JP 21408981A JP S6325085 B2 JPS6325085 B2 JP S6325085B2
Authority
JP
Japan
Prior art keywords
fibers
fiber
oxidized
acrylonitrile
weight
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.)
Expired
Application number
JP56214089A
Other languages
Japanese (ja)
Other versions
JPS58130110A (en
Inventor
Hiroyasu Ogawa
Kazuo Izumi
Kenji Shimazaki
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.)
Teijin Ltd
Original Assignee
Toho 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 Toho Rayon Co Ltd filed Critical Toho Rayon Co Ltd
Priority to JP56214089A priority Critical patent/JPS58130110A/en
Priority to US06/452,489 priority patent/US4460650A/en
Priority to FR8221667A priority patent/FR2522697B1/en
Priority to DE3248040A priority patent/DE3248040C2/en
Priority to GB08236749A priority patent/GB2116592B/en
Publication of JPS58130110A publication Critical patent/JPS58130110A/en
Publication of JPS6325085B2 publication Critical patent/JPS6325085B2/ja
Granted legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Inorganic Fibers (AREA)
  • Separation Of Gases By Adsorption (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は繊維状活性炭の製造法、さらに詳しく
は、水溶性塩基性アルミニウム複合塩を付着させ
たアクリロニトリル系繊維を酸化処理後、賦活す
ることからなる高収率で高性能の繊維状活性炭を
製造する方法に関する。 繊維状活性炭(ACF)は、セルロース系繊維、
フエノール樹脂繊維またはアクリロニトリル系繊
維などを原料としてこれを炭化、次いで賦活する
ことにより製造され、トウ、織物またはフエルト
状等の形態で吸着材、フイルター等として例えば
溶剤回収装置において使用され、その需要は近年
増大しつつある。 特に、アクリロニトリル系繊維を原料とする
ACFは含有する窒素原子による特異な吸着性能
と優れた機械的強度により種々な用途が期待され
ている。 一般に、アクリロニトリル系繊維を原料とする
ACFは次のようにして製造される。 すなわち、第1段階の酸化工程においてアクリ
ロニトリル系繊維を酸素等の酸化性雰囲気中200
〜300℃で処理して酸化を行ない、次いで第2段
階の賦活工程において酸化繊維を水蒸気、炭酸ガ
ス等の雰囲気中700〜1000℃で賦活処理する。 通常、フエルト、織物、ヤーン等の形態にする
には第1段階終了後の酸化繊維束を加工するか、
あるいは第2段階終了後のACFを加工するかの
いずれかの方法がとられる。 ACFを加工する場合、特に充分な強度とクリ
ンプ性が要求されるが、このようなACFの加工
性は第1段階の酸化繊維の性能に依存する。従つ
ていずれの段階で加工する場合でも、酸化繊維が
加工に必要な高い強度と優れたクリンプ性を具備
ていなければならない。 しかしながら、従来よりこの酸化繊維はクリン
プがかかり難く、このため糸とする際に糸切れが
多発し、作業の効率を著しく悪くする傾向があつ
た。また、フエルト等にする場合は落綿が多く収
率の低下、作業性の悪化を招き、フエルトの強度
を低下させる等の問題があつた。このような酸化
繊維の加工性を高めるために従来法では第1段階
の酸化工程は、アクリロニトリル系繊維束の急激
な発熱を抑えて繊維の開繊性を良好に保つととも
に繊維強度の低下を防止する目的で低温で相当長
時間の加熱処理を行なうことを余儀なくされてい
るが、加工性の点でなお問題がある。 また、このような長時間の加熱処理を要する酸
化工程にACF製造の全所要時間の約8割が費や
されており、コスト高の要因となつている。 本発明者等は、このような問題について検討の
結果、水溶性の塩基性アルミニウム複合塩をアク
リロニトリル系繊維束に付着させることにより、
上記の如き問題のない酸化繊維が高能率で得ら
れ、ひいては高収率かつ高性能のACFが得られ
ることを見出し、本発明に至つたものである。 すなわち、本発明は下記一般式で示される水溶
性の塩基性アルミニウム複合塩を繊維重量に対し
アルミニウムとして0.01〜5重量%付着させたア
クリロニトリル系繊維を酸化性雰囲気中で酸化処
理した後、賦活ガス中700℃で処理することを特
徴とするACFの製造法である。 Al2(OH)xCly(PO4)z 式中x,y,z:整数または小数 5.6≦x+y+3z≦6 0.4≦x/x+y+z≦0.9 本発明によればACFの酸化工程における所要
時間を従来法の約1/2以下に短縮することができ、
それでいて良好な吸着性能および機械的性能を有
するACFを高収率で製造することができる。 本発明について更に詳述する。 本発明において、アクリロニトリル系繊維とは
アクリロニトリルを少なくとも85重量%以上好ま
しくは90〜98重量%含有するポリアクリレニトリ
ルよりなる繊維またはアクリロニトリルと共重合
可能な不飽和化合物との2種以上の共重合体より
なる繊維あるいはこれらの共重合体を混合してで
きた重合体よりなる繊維をいう。 該繊維に付着させる水溶性の塩基性アルミニウ
ム複合塩は例えば特開昭49―130387号、特開昭50
―153799号公報で知られた方法に準じて製造され
る、前記一般式で示されるごときものである。こ
れに代えて水酸化アルミニウム、硫酸アルミニウ
ム、燐酸アルミニウムなどを用いた場合には全く
効果がなく、逆に繊維のクリンプ付与が困難とな
る。 本発明に使用される複合塩は水酸基を含有しか
つ水溶性の複合塩であるため、繊維に斑なく付与
しうるだけでなく、アクリロニトリル系繊維を酸
化する過程で生ずる発熱を程よく吸収して、過度
の蓄熱や温度上昇を防ぐことができるため、均質
な酸化繊維をつくりうるうえ繊維へのクリンプ付
与を容易となすのに有効である。 本発明に用いられる複合塩をアクリロニトリル
系繊維束に付着させるには、複合塩の水溶液をつ
くり、この液に繊維束を浸漬するか、もしくは該
水溶液スプレーするなどの通常使われる付着方法
が用いられる。 アクリロニトリル系繊維束に対するこれらの複
合塩の付着量は後掲第2表、第3表から明らかな
如く繊維重量に対しアルミニウムとして0.01〜5
重量%の範囲であることが必要である。この範囲
未満では本発明の効果が発揮されず、この範囲を
越えると酸化処理時に繊維強度の低下および賦活
収率の低下を招来する。 以上の如き水溶性の塩基性アルミニウムを付着
させたアクリロニトリル系繊維は酸素等の酸化性
雰囲気中で酸化処理される。この場合処理温度は
原料繊維のコモノマー量によつて異なり、適宜最
適条件が選択されるが、本発明の水溶性塩基性ア
ルミニウム複合塩を付着させた繊維は従来のアク
リロニトル系繊維に比較し、より高温短時間で酸
化処理することができる。本発明の大きな利点
は、従来のアクリロニトリル系繊維に水溶性の塩
基性アルミニウム複合塩を付着させることにより
次のような効果が発現することにある。 すなわち(1)従来方法より酸化処理温度を高くし
ても繊維束の燃焼を惹起せず、したがつて酸化時
間を大巾に短縮することができる。(2)従来方法と
同一酸化処理温度においても従来方法より酸化速
度が速く処理時間が短縮される。(3)従来方法より
高い強度と優れたクリンプ性を有する酸化繊維が
得られる。(4)従来方法より賦活時間が短縮され賦
活収率が向上する。(5)従来方法より高い強度と加
工性を有するACFが得られる。 以上のように、本発明方法によれば特に酸化工
程の生産性および品質の向上が顕著である。 例えば、アクリロニトリル92重量%、アクリル
酸メチル8重量%からなる共重合繊維にAl2
(OH)3Cl1.7(PO40.3の組成からなる水溶性の塩基
性アルミニウム複合塩をアルミニウムとして0.05
重量%付着せしめて2段階で酸化処理した場合に
ついて従来法のアルミニウムを含まないものと比
較して示すと第1表の通りである。
The present invention relates to a method for producing fibrous activated carbon, and more specifically, to producing high-yield, high-performance fibrous activated carbon by oxidizing and activating acrylonitrile fibers to which a water-soluble basic aluminum composite salt is attached. Regarding how to. Fibrous activated carbon (ACF) is a cellulosic fiber,
It is produced by carbonizing and then activating phenolic resin fibers or acrylonitrile fibers as raw materials, and is used in the form of tow, woven fabric, or felt as an adsorbent or filter in, for example, solvent recovery equipment. It has been increasing in recent years. In particular, those made from acrylonitrile fibers
ACF is expected to have a variety of uses due to its unique adsorption performance due to the nitrogen atoms it contains and its excellent mechanical strength. Generally made from acrylonitrile fibers
ACF is manufactured as follows. That is, in the first oxidation process, acrylonitrile fibers are heated in an oxidizing atmosphere such as oxygen at 200%
Oxidation is carried out by treatment at ~300°C, and then, in the second activation step, the oxidized fibers are activated at 700~1000°C in an atmosphere of water vapor, carbon dioxide, or the like. Normally, in order to form felt, woven fabric, yarn, etc., the oxidized fiber bundle after the first stage is processed or
Alternatively, either method is used to process the ACF after the second stage is completed. When processing ACF, particularly sufficient strength and crimpability are required, and the processability of such ACF depends on the performance of the oxidized fiber in the first stage. Therefore, at any stage of processing, the oxidized fiber must have high strength and excellent crimpability necessary for processing. However, conventionally, this oxidized fiber has been difficult to crimp, and as a result, yarn breakage has occurred frequently when it is made into yarn, which has tended to significantly reduce work efficiency. Furthermore, when it is made into felt, there are problems such as a large amount of falling cotton, resulting in a decrease in yield, deterioration in workability, and a decrease in the strength of the felt. In order to improve the processability of such oxidized fibers, in the conventional method, the first oxidation step suppresses the rapid heat generation of the acrylonitrile fiber bundle, maintains good fiber opening properties, and prevents a decrease in fiber strength. For this purpose, it is necessary to carry out heat treatment at a low temperature for a considerable period of time, but there are still problems in terms of processability. Furthermore, approximately 80% of the total time required for manufacturing ACF is spent on the oxidation step, which requires such a long heat treatment, which is a factor in high costs. As a result of studying these problems, the present inventors discovered that by attaching a water-soluble basic aluminum composite salt to an acrylonitrile fiber bundle,
The inventors have discovered that oxidized fibers free from the above-mentioned problems can be obtained with high efficiency, and that ACF with high yield and high performance can be obtained, leading to the present invention. That is, in the present invention, acrylonitrile fibers to which a water-soluble basic aluminum composite salt represented by the general formula below is attached in an amount of 0.01 to 5% by weight as aluminum based on the weight of the fibers are oxidized in an oxidizing atmosphere, and then treated with an activating gas. This is an ACF production method characterized by processing at medium temperature of 700℃. Al 2 ( OH) It can be shortened to about 1/2 or less,
Yet ACF with good adsorption performance and mechanical performance can be produced in high yield. The present invention will be explained in further detail. In the present invention, acrylonitrile fibers are fibers made of polyacrylenitrile containing at least 85% by weight or more preferably 90 to 98% by weight of acrylonitrile, or fibers made of polyacrylonitrile containing two or more types of unsaturated compounds copolymerizable with acrylonitrile. It refers to fibers made from a combination of fibers or fibers made from a polymer made by mixing these copolymers. Water-soluble basic aluminum composite salts to be attached to the fibers are disclosed in, for example, JP-A-49-130387 and JP-A-50.
- It is produced according to the method known in Publication No. 153799 and is represented by the above general formula. When aluminum hydroxide, aluminum sulfate, aluminum phosphate, etc. are used instead, there is no effect at all, and on the contrary, it becomes difficult to crimp the fibers. Since the complex salt used in the present invention is a water-soluble complex salt that contains a hydroxyl group, it can not only be applied uniformly to the fibers, but also moderately absorb heat generated during the process of oxidizing acrylonitrile fibers. Since it is possible to prevent excessive heat accumulation and temperature rise, it is effective in making homogeneous oxidized fibers and making it easier to crimp the fibers. In order to attach the composite salt used in the present invention to the acrylonitrile fiber bundle, a commonly used attachment method is used, such as preparing an aqueous solution of the composite salt and immersing the fiber bundle in this solution, or spraying the aqueous solution. . As is clear from Tables 2 and 3 below, the amount of these composite salts deposited on acrylonitrile fiber bundles is 0.01 to 5% as aluminum based on the fiber weight.
It is necessary that the amount is within the range of % by weight. If it is less than this range, the effect of the present invention will not be exhibited, and if it exceeds this range, a decrease in fiber strength and activation yield will occur during oxidation treatment. The acrylonitrile fiber to which water-soluble basic aluminum is attached is oxidized in an oxidizing atmosphere such as oxygen. In this case, the treatment temperature varies depending on the amount of comonomer in the raw fiber, and the optimum conditions are selected as appropriate. However, the fiber to which the water-soluble basic aluminum composite salt of the present invention is attached has a higher temperature than the conventional acrylonitrile fiber. Oxidation treatment can be performed at high temperature and in a short time. A major advantage of the present invention is that the following effects are produced by attaching a water-soluble basic aluminum composite salt to conventional acrylonitrile fibers. That is, (1) even if the oxidation treatment temperature is higher than that of the conventional method, the fiber bundle does not burn, and therefore the oxidation time can be significantly shortened. (2) Even at the same oxidation temperature as the conventional method, the oxidation rate is faster and the treatment time is shorter than the conventional method. (3) Oxidized fibers with higher strength and better crimpability than conventional methods can be obtained. (4) Activation time is shortened and activation yield is improved compared to conventional methods. (5) ACF with higher strength and workability than conventional methods can be obtained. As described above, according to the method of the present invention, productivity and quality are significantly improved, especially in the oxidation step. For example, Al2
A water-soluble basic aluminum complex salt with a composition of (OH) 3 Cl 1.7 (PO 4 ) 0.3 is 0.05 as aluminum.
Table 1 shows a comparison of the case where aluminum is deposited in a weight percent and subjected to two-stage oxidation treatment with the conventional method which does not contain aluminum.

【表】 第1表の結果より明らかなように水溶性の塩基
性アルミニウム複合塩を付着させたアクリロニト
リル系繊維は初期温度を高くしても糸条の燃焼を
惹起せず、しかも酸化速度が速いため酸化工程に
要する時間を従来法の約1/2以下に短縮し得て、
それでいて加工性に優れた酸化繊維を得ることが
できる。 本発明において水溶性の塩基性アルミニウム複
合塩を付着させたアクリロニトリル系繊維は酸化
繊維の平衝水分率が10〜13%の範囲に達するまで
処理されるのが、得られるACFの賦活収率、繊
維強度が高いので望ましい。 以上の酸化処理を終えた酸化繊維は続いて賦活
処理に付される。賦活化は公知の方法で行なうこ
とができ水蒸気、炭酸ガス、アンモニア等の雰囲
気中700℃以上、好ましくは800〜950℃の温度で
数秒から2時間加熱して行なわれる。この工程で
は酸化繊維中に残存するアルミニウムとリン化合
物が賦活反応を促進して従来方法より賦活時間を
短縮し賦活収率を向上させる。 本発明の特徴はこのように水溶性の塩基性アル
ミニウム複合を付着させたアクリロニトリル系繊
維を使用することによつて酸化工程、賦活工程が
同時に改善されるため従来法より著しくACFの
製造コストを低減できることにある。以下に本発
明を実施例によつて説明するが、本発明はこれら
により限定されるものではない。 実施例 1 水酸化アルミニウム微粉末に塩酸と燐酸とさら
に適量の水とを加えてオートクレーブ中110℃で
加熱することにより組成がAl2(OH)2.1Cl2.4(PO4
0.5からなる塩基性アルミニウム複合塩の水溶液を
調製した。この水溶液を適宜希釈してアクリロニ
トリル94.7重量%、アクリル酸メチル5.3重量%
からなる単繊維繊度3デニール、トータルデニー
ル54万弐共重合繊維トウを室温で浸漬して繊維重
量に対しアルミニウムとして0.01〜6.5重量%付
着するように調製した。ただし5重量%を越える
場合は比較例である。 これらの繊維束を空気中で初期250℃で1時間、
次いで270℃で1.5時間の2段階で酸化処理を行な
つた。 比較のため上記と同一繊維でアルミニウムを付
着しない場合についても同様の処理を行なつた。
この結果を第2表に示す。上記の酸化繊維を次い
で910℃で過熱水蒸気中賦活処理して、比表面積
が900m2/gのACFを得る場合について賦活収率
および性能をまとめて第3表に示す。
[Table] As is clear from the results in Table 1, acrylonitrile fibers coated with water-soluble basic aluminum complex salts do not cause yarn combustion even at high initial temperatures, and their oxidation rate is fast. Therefore, the time required for the oxidation process can be reduced to less than half of the conventional method.
However, oxidized fibers with excellent processability can be obtained. In the present invention, the acrylonitrile fibers to which a water-soluble basic aluminum composite salt is attached are treated until the average moisture content of the oxidized fibers reaches a range of 10 to 13%, which increases the activation yield of the resulting ACF. Desirable because of its high fiber strength. The oxidized fibers that have undergone the above oxidation treatment are then subjected to activation treatment. Activation can be carried out by a known method, and is carried out by heating at a temperature of 700° C. or higher, preferably 800 to 950° C., for several seconds to 2 hours in an atmosphere of steam, carbon dioxide, ammonia, or the like. In this step, the aluminum and phosphorus compounds remaining in the oxidized fibers promote the activation reaction, shortening the activation time and improving the activation yield compared to conventional methods. The feature of the present invention is that by using acrylonitrile fibers to which a water-soluble basic aluminum composite is attached, the oxidation process and activation process are simultaneously improved, which significantly reduces ACF production costs compared to conventional methods. It's all about what you can do. EXAMPLES The present invention will be explained below using Examples, but the present invention is not limited thereto. Example 1 Hydrochloric acid, phosphoric acid, and an appropriate amount of water are added to aluminum hydroxide fine powder, and the mixture is heated at 110°C in an autoclave to change the composition to Al 2 (OH) 2.1 Cl 2.4 (PO 4 ).
An aqueous solution of basic aluminum complex salt consisting of 0.5 was prepared. This aqueous solution was appropriately diluted to produce 94.7% by weight of acrylonitrile and 5.3% by weight of methyl acrylate.
A copolymer fiber tow with a single fiber fineness of 3 denier and a total denier of 540,000 denier was prepared by soaking at room temperature so that 0.01 to 6.5% by weight of aluminum was attached to the weight of the fiber. However, cases where it exceeds 5% by weight are comparative examples. These fiber bundles were incubated in air at an initial temperature of 250°C for 1 hour.
Next, oxidation treatment was performed in two stages at 270°C for 1.5 hours. For comparison, the same treatment was performed on the same fibers as above but without aluminum attached.
The results are shown in Table 2. The above oxidized fibers were then activated in superheated steam at 910° C. to obtain ACF with a specific surface area of 900 m 2 /g, and the activation yield and performance are summarized in Table 3.

【表】【table】

【表】【table】

【表】 以上の結果より明らかなように水溶性の塩基性
アルミニウム複合塩を付着させることにより酸化
工程、品質を著しく改善し、しかも高収率で
ACFを得ることができる。 実施例 2 アクリロニトリル91重量%、アクリル酸メチル
9重量%からなる単繊維3デニール、トータルデ
ニール56万デニールの共重合体繊維トウを実施例
1と同一の塩基性アルミニウム複合塩水溶液に浸
漬した後、乾燥してアルミニウムとして0.03重量
%付着させた繊維を得た。 この繊維を第4表に記載の条件下空気中で酸化
処理した。得られた酸化繊維トウを、クリンパー
にニツプ圧2Kg/cm2、スタフイング圧1Kg/cm2
供給速度80m/hrで通してクリンプを付与した
後、綿長が102mmになるようにカツターで切断し
た。 次いでこの酸化繊維ステープルを不織布製造装
置に供給して目付500g/m2の酸化繊維フエルト
に加工した。 比較のため上記と同一組成でアルミニウムを付
着してない場合についても同様の処理を行なつ
た。 酸化繊維およびそのフエルトの特性等について
の結果をまとめて第4表に示す。 さらに、これらの酸化繊維フエルトを930℃で
水蒸気中賦活処理した。得られたACFフエルト
の収率、性能を第5表に示す。
[Table] As is clear from the above results, the oxidation process and quality were significantly improved by attaching a water-soluble basic aluminum complex salt, and a high yield was obtained.
ACF can be obtained. Example 2 A copolymer fiber tow with a single fiber of 3 denier and a total denier of 560,000 denier consisting of 91% by weight of acrylonitrile and 9% by weight of methyl acrylate was immersed in the same basic aluminum composite salt aqueous solution as in Example 1. After drying, a fiber having 0.03% by weight of aluminum deposited was obtained. This fiber was oxidized in air under the conditions listed in Table 4. The obtained oxidized fiber tow was applied to a crimper at a nip pressure of 2 Kg/cm 2 and a stuffing pressure of 1 Kg/cm 2 .
The material was crimped by feeding at a feed rate of 80 m/hr, and then cut with a cutter to a length of 102 mm. Next, this oxidized fiber staple was supplied to a nonwoven fabric manufacturing apparatus and processed into an oxidized fiber felt having a basis weight of 500 g/m 2 . For comparison, the same treatment was carried out on a case having the same composition as above but without aluminum attached. Table 4 summarizes the results regarding the characteristics of the oxidized fibers and their felts. Furthermore, these oxidized fiber felts were activated in steam at 930°C. Table 5 shows the yield and performance of the obtained ACF felt.

【表】【table】

【表】 の値を示す。
(2): No.20、21は比較例(アルミニウム付着な
し)を示す。 以上のように、本発明例では、酸化温度を高く
できるために、酸化時間を短縮しうると同時に酸
化速度も速くなり、また得られた酸化繊維のクリ
ンプ状態が優れ、したがつて最終製品のACFの
強度も高いことがわかる。 実施例 3 アクリリロニトリル92重量%、酢酸ビニル8重
量%からなる共重合繊維トウ(単繊維繊度2デニ
ール、構成本数280000本)にAl2(OH)2.8Cl1.7
(PO40.5の組成からなる水溶性塩基性アルミニウ
ム複合塩をアルミニウムとして、0.2重量%付着
させた。 このトウを空気中にて、245℃で1.5時間、次い
で265℃で2時間連続して酸化処理した後クリン
パーに通してクリンプを付与した。得られた酸化
繊維のクリンプ数は13.8ケ、引張強度26.3Kg/
mm2、伸度15.6%、平衡水分率11.3%で良好なクリ
ンプ特性と優れた繊維性能を有していた。 さらに、この酸化繊維を水蒸気中900℃で10分
間処理して賦活収率25%で比表面積1000m2/g、
引張強度25.8Kg/mm2、クリンプ数6.3ケ良好な
ACFを得た。 比較のため、上記と同一組成の繊維トウに前記
アルミニウム複合塩の代りに硫酸アルミニウムを
アルミニウムとして同一量となるように付着させ
て同様な酸化処理を行なつた。得られた酸化繊維
の性能は、クリンプ数4.1ケ、引張強度10.2Kg/
mm2、伸度8.2%、平衡水分率10.1%であり、加工
性、酸化時間の短縮に全く効果が認められなかつ
た。 さらに同一条件下賦活して得たACFは賦活収
率23%、比表面積900m2/g、引張強度15.1Kg/
mm2、クリンプ数3.8ケといずれの性能も本発明の
場合に比し劣つていた。
[Table] Shows the values.
(2): No. 20 and 21 show comparative examples (no aluminum adhesion). As described above, in the examples of the present invention, since the oxidation temperature can be increased, the oxidation time can be shortened and the oxidation rate can also be increased, and the crimped state of the obtained oxidized fibers is excellent, thus improving the quality of the final product. It can be seen that the strength of ACF is also high. Example 3 Copolymer fiber tow (single fiber fineness 2 denier, number of constituent fibers 280,000) consisting of 92% by weight of acrylonitrile and 8% by weight of vinyl acetate was coated with Al 2 (OH) 2.8 Cl 1.7
A water-soluble basic aluminum composite salt having a composition of (PO 4 ) 0.5 was deposited as aluminum in an amount of 0.2% by weight. This tow was oxidized in air at 245° C. for 1.5 hours and then at 265° C. for 2 hours, and then passed through a crimper to be crimped. The number of crimps of the obtained oxidized fiber was 13.8, and the tensile strength was 26.3 kg/
mm 2 , elongation of 15.6%, and equilibrium moisture content of 11.3%, it had good crimp properties and excellent fiber performance. Furthermore, this oxidized fiber was treated in steam at 900°C for 10 minutes to obtain an activation yield of 25% and a specific surface area of 1000 m 2 /g.
Tensile strength 25.8Kg/mm 2 , number of crimps 6.3 Good
Got ACF. For comparison, a fiber tow having the same composition as above was subjected to the same oxidation treatment by attaching aluminum sulfate in the same amount as aluminum instead of the aluminum composite salt. The performance of the obtained oxidized fiber is as follows: number of crimps is 4.1, tensile strength is 10.2 kg/
mm 2 , elongation of 8.2%, and equilibrium moisture content of 10.1%, and no effect was observed on processability or shortening of oxidation time. Furthermore, ACF obtained by activation under the same conditions had an activation yield of 23%, a specific surface area of 900 m 2 /g, and a tensile strength of 15.1 kg/g.
mm 2 and number of crimps of 3.8, both performances were inferior to those of the present invention.

Claims (1)

【特許請求の範囲】 1 下記一般式 Al2(OH)xCly(PO4)z 式中x,y,z:整数または小数 5.6≦x+y+3z≦6 0.4≦x/x+y+z≦0.9 で示される水溶性の塩基性アルミニウム複合塩を
繊維重量に対しアルミニウムとして0.01〜5重量
%付着させたアクリロニトリル系繊維を酸化性雰
囲気中で酸化処理した後、賦活ガス中700℃以上
で処理することを特徴とする繊維状活性炭の製造
法。
[Claims] 1 A water-soluble compound represented by the following general formula Al 2 (OH) A fibrous material characterized by oxidizing acrylonitrile fibers to which a basic aluminum composite salt is attached in an amount of 0.01 to 5% by weight of aluminum based on the weight of the fibers in an oxidizing atmosphere, and then treating the fibers at 700°C or higher in an activating gas. Method of manufacturing activated carbon.
JP56214089A 1981-12-24 1981-12-24 Manufacture of fibrous activated carbon Granted JPS58130110A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP56214089A JPS58130110A (en) 1981-12-24 1981-12-24 Manufacture of fibrous activated carbon
US06/452,489 US4460650A (en) 1981-12-24 1982-12-23 Acrylonitrile fibers, a process for producing acrylonitrile fibers, as well as producing peroxidized fibers, fibrous active carbon or carbon fibers therefrom
FR8221667A FR2522697B1 (en) 1981-12-24 1982-12-23 ACRYLONITRILE FIBERS, PROCESS FOR PRODUCING ACRYLONITRILE FIBER AND MANUFACTURE OF PREOXIDIZED FIBER, FIBROUS ACTIVE CARBON OR CARBON FIBER FROM THE SAME
DE3248040A DE3248040C2 (en) 1981-12-24 1982-12-24 Acrylonitrile fibres and their use for the production of pre-oxidised fibres, fibrous active carbon or carbon fibres
GB08236749A GB2116592B (en) 1981-12-24 1982-12-24 Acrylonitrile fibers, a process for producing acrylonitrile fibers, as well as producing preoxidized fibers, fibrous active carbon or carbon fibers therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56214089A JPS58130110A (en) 1981-12-24 1981-12-24 Manufacture of fibrous activated carbon

Publications (2)

Publication Number Publication Date
JPS58130110A JPS58130110A (en) 1983-08-03
JPS6325085B2 true JPS6325085B2 (en) 1988-05-24

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP56214089A Granted JPS58130110A (en) 1981-12-24 1981-12-24 Manufacture of fibrous activated carbon

Country Status (1)

Country Link
JP (1) JPS58130110A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6328449A (en) * 1986-07-22 1988-02-06 Toho Rayon Co Ltd Filter element for deodorization
JPH01266222A (en) * 1988-04-16 1989-10-24 Oji Paper Co Ltd Method for manufacturing porous carbon molded body
JP4898144B2 (en) * 2005-05-27 2012-03-14 大明化学工業株式会社 Alumina composite precursor, method for producing alumina composite, and method for producing sintered alumina composite

Also Published As

Publication number Publication date
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