JPS591803B2 - Method for manufacturing activated carbon fiber - Google Patents
Method for manufacturing activated carbon fiberInfo
- Publication number
- JPS591803B2 JPS591803B2 JP53078654A JP7865478A JPS591803B2 JP S591803 B2 JPS591803 B2 JP S591803B2 JP 53078654 A JP53078654 A JP 53078654A JP 7865478 A JP7865478 A JP 7865478A JP S591803 B2 JPS591803 B2 JP S591803B2
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- fibers
- flame
- fiber
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Description
【発明の詳細な説明】
本発明は、アクリロニトリル系繊維を原料として得られ
た耐炎繊維から、高い賦活収率で、しかも吸着性能の優
れた活性炭素繊維(ACF)を製造する方法に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing activated carbon fiber (ACF) with a high activation yield and excellent adsorption performance from flame-resistant fibers obtained using acrylonitrile fibers as raw materials. .
従来、ACF製造のための原料としては、セルローズ繊
維、ピッチを溶融して作られた繊維、ノボラック繊維、
アクリロニトリル系繊維等が知られている。Conventionally, raw materials for ACF production include cellulose fibers, fibers made by melting pitch, novolac fibers,
Acrylonitrile fibers are known.
セルローズ繊維を原料とする場合は、吸着性の高いAC
Fが得られやすいが、賦活収率が低く問題がある。When using cellulose fiber as raw material, AC with high adsorption
Although it is easy to obtain F, there is a problem in that the activation yield is low.
ノボラック繊維を原料とする場合は、ACFは賦活収率
が高く、吸着性も優れているが、原料コストが高い。When using novolac fiber as a raw material, ACF has a high activation yield and excellent adsorption properties, but the raw material cost is high.
一方アクリロニトリル系繊維から製造する場合は、原料
が比較的安価に入手できること、ACFに窒素原子が含
まれることがらメルカプタン、硫黄酸化物、窒素酸化物
の吸着に優れていること等の長所があるが、しかし賦活
収率の点からみると必ずしも満足すべきものではない。On the other hand, manufacturing from acrylonitrile fibers has advantages such as the raw materials are relatively inexpensive to obtain, and since ACF contains nitrogen atoms, it is excellent at adsorbing mercaptans, sulfur oxides, and nitrogen oxides. However, it is not necessarily satisfactory from the point of view of activation yield.
吸着性の改善については特開昭40−
116332号公報において、原料アクリロニトリル系
繊維を酸化雰囲気中にて無緊張で酸化し、次いで無緊張
下でガス賦活する方法が提案されている。As for improving adsorption properties, JP-A-40-116332 proposes a method in which raw acrylonitrile fibers are oxidized in an oxidizing atmosphere without tension, and then gas is activated under tension.
しかしこの方法では吸着性は改善されるが、ACFは機
械的性質が非常に劣り使用に耐えない。However, although this method improves adsorption properties, ACF has very poor mechanical properties and cannot be used.
本発明者等は、さきに特開昭51−132193号公報
において、アクリロニトリル系繊維を酸化雰囲気で耐炎
化(酸化)するに当り十分に酸化する方法や、塩化亜鉛
な耐炎繊維に付着させる方法などによって吸着性、機械
的性質に優れたACFを得ることを提案した。The present inventors previously disclosed in Japanese Unexamined Patent Publication No. 51-132193 a method for sufficiently oxidizing acrylonitrile fibers to make them flame resistant (oxidation) in an oxidizing atmosphere, and a method for adhering zinc chloride to flame resistant fibers. We proposed that ACF with excellent adsorption and mechanical properties could be obtained by the following method.
われわれは、更に研究を進めた結果、高い賦活収率で、
しかも吸着性能、機械的性質に優れた繊維を得ることに
成功し、本発明に達するにいたった。As a result of further research, we found that with high activation yield,
Moreover, they succeeded in obtaining fibers with excellent adsorption performance and mechanical properties, leading to the present invention.
即ち本発明は、アクリロニトリル系繊維を原料として張
力下で耐炎化処理して得られたMg、Zn、Sb、Ca
又はPを含む化合物の何れか一種又は二種以上を該金
属換算にして0.01〜1%(重量)含む耐炎繊維を、
300〜800°Cにて不活性雰囲気中で熱処理し、次
いで張力下700〜1000°Cの温度でガス賦活する
ACFの製造方法である。That is, the present invention uses Mg, Zn, Sb, and Ca obtained by flame-retardant treatment under tension using acrylonitrile fiber as a raw material.
or a flame-resistant fiber containing 0.01 to 1% (weight) of one or more compounds containing P in terms of the metal,
This is a method for producing ACF in which heat treatment is performed at 300 to 800°C in an inert atmosphere, and then gas activation is performed under tension at a temperature of 700 to 1000°C.
従来、アクリロニトリル系繊維に金属類を付着させる方
法としては、特公昭48−42813号公報において、
リン化合物で処理することによりナトリウム、カリウム
が共存するアクリロニトリル系繊維の耐炎化を容易にす
る方法が提案されているが、この方法で耐炎化し次いで
賦活した場合は、ACFの賦活収率が極めて低く、また
吸着性能が低い。Conventionally, as a method for attaching metals to acrylonitrile fibers, Japanese Patent Publication No. 48-42813 describes
A method has been proposed to make it easier to make acrylonitrile fibers containing sodium and potassium coexisting flame resistant by treating them with a phosphorus compound, but if this method is used to make them flame resistant and then activated, the activation yield of ACF is extremely low. , and the adsorption performance is low.
また特開昭50−72892号公報には、塩化亜鉛を多
量に使用し、賦活する方法が提案されているが、この方
法で得られたACFは繊維状態を保つことが極めて困難
である。Further, JP-A-50-72892 proposes a method of activating ACF using a large amount of zinc chloride, but it is extremely difficult to maintain the fibrous state of ACF obtained by this method.
本発明によると、耐炎繊維にマグネシウム(Mg )、
亜鉛(Zn)、アンチモン(Sb )、カルシウム(C
a)又はリン(P)の何れか一種又は二種以上を特定量
付着させ、これを不活性ガス中にて耐炎化温度より高い
300〜soo’cで、好ましくはこの範囲内の賦活温
度より低い温度で熱処理し、次いで張力下700〜10
00℃でガス賦活することによって、高い賦活収率で、
しかも吸着性能の優れたACFが得られる。According to the present invention, magnesium (Mg) is added to the flame-resistant fiber.
Zinc (Zn), antimony (Sb), calcium (C
a) or phosphorus (P) in a specific amount, and heat it in an inert gas at 300 to soo'c higher than the flameproofing temperature, preferably at an activation temperature within this range. Heat treated at low temperature and then under tension 700~10
By performing gas activation at 00°C, high activation yield is achieved.
Moreover, ACF with excellent adsorption performance can be obtained.
本発明で用いられるアクリロ・ニトリル系繊維とはアク
リロニトリル60重量%以上を含有する単独重合体もし
くは共重合体又はこれら重合物の混合物を意味し、共重
合成分はアクリロニトリルと共重合可能なエチレン系不
飽和化合物である。The acrylonitrile fiber used in the present invention means a homopolymer or copolymer containing 60% by weight or more of acrylonitrile, or a mixture of these polymers, and the copolymer component is an ethylene-based fiber that can be copolymerized with acrylonitrile. It is a saturated compound.
アクリロニトリル系繊維の形態としてはフェルト状、ト
ウ状、編物状、織物状のものがある。The forms of acrylonitrile fibers include felt, tow, knit, and woven fabrics.
アクリロニ) IJル系繊織繊維耐炎化た後あるいは更
に賦活した後に不織布製造装置により、これらの形態に
することができる。After flame-retardant or further activation of the IJ-based woven fibers, they can be made into these forms using a nonwoven fabric manufacturing device.
アクリロニトリル系繊維は酸化雰囲気中で200〜30
0℃の温度で酸化(耐炎化)される。Acrylonitrile fiber has 200-30% in oxidizing atmosphere.
Oxidized (flame resistant) at a temperature of 0°C.
酸化の程度は特開昭50−57762号、特開昭53−
45426号の各公報で提案されているように、その酸
化温度での飽和酸素結合量の75〜85%まで酸化する
ことが、優れた吸着性を有する活性炭素繊維を得る上で
好ましい。The degree of oxidation is shown in JP-A-50-57762 and JP-A-53-
As proposed in each publication of No. 45426, it is preferable to oxidize to 75 to 85% of the saturated oxygen bond amount at the oxidation temperature in order to obtain activated carbon fibers having excellent adsorption properties.
また酸化は、その酸化温度での自由収縮率の50〜90
%の張力下で行うことが、繊維の強度を高め、かつ酸化
工程の生産効率を高める上から望ましい。Oxidation also reduces the free shrinkage rate from 50 to 90 at the oxidation temperature.
% tension is desirable from the viewpoint of increasing the strength of the fibers and increasing the production efficiency of the oxidation process.
本発明において、耐炎繊維に金属を含む金属化合物を付
着させる方法は大きく分けて次の二つがある。In the present invention, there are roughly two methods for attaching a metal compound containing a metal to the flame-resistant fibers.
第1の方法は原料アクリロニトリル系繊維の製造前の紡
糸液又は製造後の原料繊維に付与させる方法である。The first method is to apply it to the spinning solution before producing the raw material acrylonitrile fiber or to the raw material fiber after producing it.
即ち紡糸前の重合溶液中に金属化合物を添加するか又は
、紡糸、水洗あるいはその後の処理工程等の原糸製造工
程中において、もしくは原糸製造後において金属化合物
を付着させる。That is, the metal compound is added to the polymerization solution before spinning, or the metal compound is attached during the yarn production process such as spinning, water washing, or subsequent treatment steps, or after the yarn production.
製造工程中で金属を入れる場合は糸条中に金属化合物を
均一に付着させることができ、そのため付着量が少くて
すむなどの利点がある。When metal is added during the manufacturing process, the metal compound can be uniformly adhered to the yarn, which has the advantage that the amount of adhesion can be small.
第2の方法は原糸又はその二次形態物を耐炎化して得た
耐炎繊維に、金属を含む金属化合物の溶液を含浸させる
方法がある。The second method is to impregnate flame-resistant fibers obtained by flame-resistant fibers or secondary forms thereof with a solution of a metal compound containing a metal.
この方法は原糸に金属化合物が付着していないため耐炎
化に当り糸条の膠着を招(ことがあるので、第1の方法
が好ましいが、第1の方法と第2の方法を組合せること
によって膠着を防止することもできる。This method does not have metal compounds attached to the raw yarn, which may cause the yarn to stick together when making it flame resistant.The first method is preferable, but the first method and the second method may be combined. This can also prevent sticking.
また、アクリロニトリル系繊維の共重合体に金属反応性
官能基、例えばスルホン酸、カルボン酸等の基が存在す
る場合には、それに金属を結合させることも、均一に金
属を導入することから好ましい。Furthermore, when a metal-reactive functional group, such as a sulfonic acid or carboxylic acid group, is present in the copolymer of acrylonitrile fibers, it is also preferable to bond the metal thereto, since this allows the metal to be introduced uniformly.
本発明において、金属は種々の化合物の形で入れられる
が、一般には塩化物、酸化物、硝酸塩、硫酸塩、炭酸塩
等のものがある。In the present invention, metals are introduced in the form of various compounds, generally chlorides, oxides, nitrates, sulfates, carbonates, etc.
またリン化合物としてはリン酸、メタリン酸、リン酸ア
ンモニウム、リン酸二水素アンモニウム、ポリリン酸、
リン酸水素ニアンモニア、有機リン酸等が用いられる。In addition, phosphorus compounds include phosphoric acid, metaphosphoric acid, ammonium phosphate, ammonium dihydrogen phosphate, polyphosphoric acid,
Hydrogen phosphate, ammonia, organic phosphoric acid, etc. are used.
金属化合物の付着量は金属の種類によって異なるが、耐
炎繊維を基準にすると金属換算にして0.05〜1重量
%の範囲である。The amount of the metal compound deposited varies depending on the type of metal, but is in the range of 0.05 to 1% by weight in terms of metal, based on the flame-resistant fiber.
この範囲をはずれると所期の効果が得られない(後記第
1表参照)。If it deviates from this range, the desired effect will not be obtained (see Table 1 below).
この場合二種以上の金属化合物を組合せてもよい。In this case, two or more types of metal compounds may be combined.
例えば亜鉛とリンの組合せや、亜鉛とリンとカルシウム
等の組合せ等である。For example, a combination of zinc and phosphorus, a combination of zinc, phosphorus, calcium, etc.
特にリンと亜鉛又はリンとカルシウムを組合せた場合は
耐熱酸化性が向上するという利点もある。In particular, a combination of phosphorus and zinc or phosphorus and calcium has the advantage of improved thermal oxidation resistance.
このようにして金属を一種以上含む金属化合物が付着し
ている耐炎繊維は、次いで不活性ガス雰囲気中で熱処理
される。The flame-resistant fiber to which the metal compound containing one or more metals is attached in this way is then heat-treated in an inert gas atmosphere.
不活性ガス雰囲気は窒素ガス、アルゴンガス、ヘリウム
ガス等のいずれか又はこれらの組合せである。The inert gas atmosphere is nitrogen gas, argon gas, helium gas, etc., or a combination thereof.
このような不活性ガス雰囲気中にて金属を含む耐炎繊維
は300〜800°Cの温度で通常10分〜180分処
理される。Flame-resistant fibers containing metal are treated in such an inert gas atmosphere at a temperature of 300 to 800°C for usually 10 minutes to 180 minutes.
この熱処理工程は本発明では非常に重要な意味をもつ。This heat treatment step has a very important meaning in the present invention.
即ち、この熱処理によって、直ちに細孔が形成されてい
るのではなく、金属が触媒的に作用して繊維構造に変化
を与え、賦活されやすい構造になると考えられる。That is, it is thought that through this heat treatment, pores are not immediately formed, but the metal acts catalytically to change the fiber structure, resulting in a structure that is easily activated.
通常の活性炭の薬品賦活の場合は薬品を含浸させて熱処
理することによって細孔が発達し、比表面積が800〜
1000 rri:/f?になるのであるが、本発明の
金属を含む耐炎繊維を300〜800℃で不活性ガス雰
囲気中で熱処理しても、細孔は発達せず、比表面積は零
であった。In the case of ordinary chemical activation of activated carbon, pores are developed by impregnating it with chemicals and heat-treating it, resulting in a specific surface area of 800~
1000 rri:/f? However, even when the flame-resistant fiber containing the metal of the present invention was heat-treated at 300 to 800°C in an inert gas atmosphere, pores did not develop and the specific surface area was zero.
本発明での熱処理温度の影響を示すと第1図の通りであ
る。FIG. 1 shows the influence of heat treatment temperature in the present invention.
この図は、アクリロニトリル系繊維製造工程中の水洗工
程で亜鉛量をコントロールし※て塩化亜鉛を亜鉛として
0.15%になるよう付着させ、原料繊維としてアクリ
ロニトリル93%、アクリル酸メチル5%、アクリルア
ミド2%の共重合体よりなる繊維を使用し、耐炎化処理
後窒素気流中20分間、約300〜800℃の範囲で温
度を変えて熱処理し、次いで比表面積が約1000rn
:/?になるよう時間を調整し水蒸気中(供給速度21
/分)800℃にて賦活処理したときのものである。This figure shows that the amount of zinc is controlled* in the water washing process during the acrylonitrile fiber manufacturing process, and zinc chloride is deposited at 0.15% as zinc, and the raw material fibers are 93% acrylonitrile, 5% methyl acrylate, and acrylamide. Fibers made of 2% copolymer were used, and after flame-retardant treatment, they were heat-treated in a nitrogen stream for 20 minutes at varying temperatures in the range of about 300 to 800°C, and then the specific surface area was about 1000rn.
:/? Adjust the time so that
/min) after activation treatment at 800°C.
第1図はこのときの熱処理温度と賦活収率の関係を示し
たものである。FIG. 1 shows the relationship between the heat treatment temperature and the activation yield at this time.
賦活収率とは耐炎繊維よ’)ACFを得る割合のことで
、下記の式で示される。Activation yield is the rate at which ACF is obtained from flame-resistant fibers, and is expressed by the following formula.
大きな比表面積のACFを得ようとする程賦活収率は小
となり賦活収率は変動するから、賦活収率の比較は比表
面積のほぼ同じもの相互間で対比する(後記第2表参照
)。The activation yield decreases as the ACF with a larger specific surface area is obtained, and the activation yield fluctuates, so the activation yields are compared between those with approximately the same specific surface area (see Table 2 below).
この図より明らかな通り熱処理温度としては300〜8
00℃特に500〜700℃が望ましい結果を与える。As is clear from this figure, the heat treatment temperature is 300~8
00°C, especially 500-700°C gives desirable results.
処理時間は温度によって変るが、5〜60分で充分であ
る。The treatment time varies depending on the temperature, but 5 to 60 minutes is sufficient.
第2図は、金属の付着量による影響について示したもの
である。FIG. 2 shows the influence of the amount of metal deposited.
金属の付着方法及び処理条件は第1図のときと同一に設
定した。The metal deposition method and processing conditions were set to be the same as in FIG.
図中1は熱処理をしない繊維について、2は、600℃
で20分窒素ガス中熱処理した繊維について、それぞれ
金属の添加量と賦活収率の関係を示したものである。In the figure, 1 is for fibers that are not heat treated, and 2 is for fibers that are heated to 600℃.
The graph shows the relationship between the amount of metal added and the activation yield for fibers heat-treated in nitrogen gas for 20 minutes.
以上の第1図及び第2図に示した結果から明らかな通り
、金属を耐炎繊維に付着して賦活しただけでは効果は少
く、これに加えて賦活前に300〜800℃で熱処理す
ることによって効果が非常に太き(なることが判る。As is clear from the results shown in Figures 1 and 2 above, simply attaching metal to flame-resistant fibers and activating them has little effect; in addition, heat treatment at 300 to 800°C before activation It turns out that the effect is very strong.
次に各種金属による効果を下記第1表に示す。Next, the effects of various metals are shown in Table 1 below.
第1表の結果は、原料繊維としてアクリロニトリル93
%、アクリル酸メチル5%、アクリルアミド2%の共重
合体よりなる繊維を用い、原料繊維の製造工程中の水洗
工程においてそれぞれ塩化亜鉛、リン酸、酸化マグネシ
ウム、酸化アンチモン、塩化カルシウムを第1表に示す
量(金属換算)付着させ、この繊維を耐炎化し、賦活処
理した。The results in Table 1 show that acrylonitrile 93 was used as the raw material fiber.
%, 5% methyl acrylate, and 2% acrylamide copolymer, and zinc chloride, phosphoric acid, magnesium oxide, antimony oxide, and calcium chloride were added in Table 1 in the water washing process during the manufacturing process of the raw fiber. The fibers were made flame resistant and activated by adhering them in the amount shown (metal equivalent).
第1表より判る通り金属化合物の付着量が金属に換算し
て0.05〜1重量%の範囲をはずれた場合や、この範
囲内でも300〜800°Cの熱処理を行わない場合は
、優れた性能のACFを得ることができない。As can be seen from Table 1, if the amount of attached metal compound is outside the range of 0.05 to 1% by weight in terms of metal, or if heat treatment at 300 to 800°C is not performed even within this range, the It is not possible to obtain an ACF with high performance.
賦活は水蒸気ガス、炭酸ガス、アンモニヤガスを含む雰
囲気中700〜1000℃にて行われるが、前段階の不
活性ガス処理温度より高い温度で行うことが望ましい。Activation is performed at 700 to 1000° C. in an atmosphere containing steam gas, carbon dioxide gas, and ammonia gas, but it is desirable to perform activation at a temperature higher than the inert gas treatment temperature in the previous stage.
賦活の時間は通常10〜120分である。The activation time is usually 10 to 120 minutes.
賦活温度が700°Cより低いと時間がかかり、また1
000℃より高いと賦活斑が生ずるので好ましくない。If the activation temperature is lower than 700°C, it will take time and 1
If the temperature is higher than 000°C, activation spots will occur, which is not preferable.
このようにして高い賦活収率で、かつ吸着性能の優れた
活性炭素繊維を得ることができる。In this way, activated carbon fibers with high activation yield and excellent adsorption performance can be obtained.
以下本発明を実施例にて説明する。The present invention will be explained below with reference to Examples.
実施例 1
60%塩化亜鉛水溶液90部、アクリロニトリル9.3
部、アクリル酸メチル0.7部からなる溶液を均一溶液
重合して得られた重合体溶液を紡糸原液として紡糸し、
水洗工程をコントロールし繊維中の塩化亜鉛量を亜鉛に
して0.3重量%残存した繊維を得た。Example 1 90 parts of 60% zinc chloride aqueous solution, 9.3 parts of acrylonitrile
A polymer solution obtained by homogeneous solution polymerization of a solution consisting of 0.7 parts of methyl acrylate,
By controlling the water washing process, the amount of zinc chloride in the fiber was changed to 0.3% by weight of zinc to obtain a fiber.
この繊維を270°Cにて6時間、空気中にて自由収縮
に対して70%の収縮を与える張力下で、かつ酸素結合
量が飽和酸素結合量に対して85%になるまで十分に酸
化した。The fibers were oxidized at 270°C for 6 hours in air under a tension that caused a contraction of 70% of the free contraction and until the amount of oxygen binding became 85% of the saturated oxygen binding amount. did.
次いで600°Cにて20分窒素ガス雰囲気中で熱処理
し、次いで850°Cにて水蒸気ガス中にて自由収縮率
に対して80%の収縮を与える張力下で賦活処理した。Next, it was heat treated at 600°C for 20 minutes in a nitrogen gas atmosphere, and then activated at 850°C in steam gas under tension to give a shrinkage of 80% of the free shrinkage rate.
結果は第2表の通りである。The results are shown in Table 2.
比較のため、同様にして塩化亜鉛を含まない繊維を耐炎
化処理した後、賦活化した場合についても第2表に記す
。For comparison, Table 2 also shows the case where fibers containing no zinc chloride were similarly flame-retardant treated and then activated.
本発明の場合、得られたACFが比表面積85Qm”/
グのとき賦活収率は35.0%と高く、これに対し比較
例の場合はぼ同じ比表面積900m/?のとき賦活収率
は19.3%と低い。In the case of the present invention, the obtained ACF has a specific surface area of 85Qm”/
The activation yield was as high as 35.0% in the case of the comparative example, whereas in the case of the comparative example, the specific surface area was almost the same, 900 m/? When this happens, the activation yield is as low as 19.3%.
同様に比表面積1100(1120)、1400(13
60)、1s2o(1s1o)m/Pのとき、いずれも
賦活収率は本発明の場合の方が比較例より高い。Similarly, the specific surface area is 1100 (1120), 1400 (13
60), 1s2o (1s1o) m/P, the activation yield in the present invention is higher than that in the comparative example.
本発明品の繊維強度は比表面積s5om”/l?のもの
でa 0.9 kg/m4.比表面積1100m/Pの
もので42.8kg/−と優れていた。The fiber strength of the product of the present invention was excellent: a 0.9 kg/m4 for a product with a specific surface area of s5 om''/l, and 42.8 kg/- for a product with a specific surface area of 1100 m/P.
比較のため(無緊張)、実施例1において、耐炎化処理
及び賦活処理を無緊張下で行い、他は同一条件にて処理
を行ったところ、ACFの賦活収率は比表面積1100
rri:/?にて28%であった。For comparison (no tension), in Example 1, the flame retardant treatment and the activation treatment were performed under no tension, and the other treatments were performed under the same conditions, and the activation yield of ACF was 1100.
rri:/? It was 28%.
このもののベンゼン吸着量は48%で優れていたが、繊
維強度は10.6 kg/ln7?Lと低かった。This product had an excellent benzene adsorption amount of 48%, but the fiber strength was 10.6 kg/ln7? It was as low as L.
比較のため(金属を含まない)、同時に実施例1におい
て塩化亜鉛を完全に水洗し、塩化亜鉛を含まない繊維を
得た。For comparison (not containing metal), the zinc chloride in Example 1 was simultaneously washed completely with water to obtain fibers containing no zinc chloride.
該繊維を耐炎化処理した後700℃にて10分間窒素ガ
ス雰囲気中で熱処理し、850℃の水蒸気ガス中で賦活
処理したところ、賦活収率17.4%で比表面積110
0 rrl/グ、ベンゼン吸着量41%のACFが得ら
れた。After flame-proofing the fibers, they were heat-treated at 700°C for 10 minutes in a nitrogen gas atmosphere and activated in steam gas at 850°C. The activation yield was 17.4% and the specific surface area was 110.
An ACF of 0 rrl/g and a benzene adsorption amount of 41% was obtained.
このものは、本発明例に比し、特に賦活収率が低い。This product has a particularly low activation yield compared to the examples of the present invention.
実施例 2
(イ)実施例1において水洗工程で付着亜鉛量をコント
ロールする代りに水洗、延伸、弛緩後、該繊維を塩化亜
鉛水溶液に浸漬、実施例1と同じ亜鉛量を付着させた。Example 2 (a) Instead of controlling the amount of zinc deposited in the washing step in Example 1, after washing, stretching, and relaxing, the fibers were immersed in an aqueous zinc chloride solution to deposit the same amount of zinc as in Example 1.
(ロ)実施例1において水洗工程で付着亜鉛量をコント
ロールする代りに、水洗、延伸、弛緩、乾燥後、塩化亜
鉛水溶液に該繊維を浸漬させ、実施例1と同じ亜鉛量を
付着させた。(b) Instead of controlling the amount of zinc deposited in the washing step in Example 1, the fibers were immersed in an aqueous zinc chloride solution after washing, stretching, relaxing, and drying, and the same amount of zinc as in Example 1 was deposited.
()→ 実施例1のような水洗工程での金属付着を行う
ことなく、通常の方法でアクリロニトリル系繊維を得た
。( ) → Acrylonitrile fibers were obtained by a normal method without metal attachment in the water washing step as in Example 1.
次いで270°C空気中にて実施例1と同程度の耐炎化
程度まで酸化した後、実施例1と同じ亜鉛量の塩化亜鉛
を付着した。Next, it was oxidized in air at 270° C. to the same degree of flame resistance as in Example 1, and then zinc chloride in the same amount as in Example 1 was deposited.
前記(イ)(O)の場合は、それぞれ引続き、実施例1
と同様の耐炎化条件にて処理した。In the cases of (A) and (O) above, Example 1 is continued.
It was treated under the same flame-retardant conditions.
そして(イ)、(ロ)及びe→とも、いずれも実施例1
の賦活条件にて活性化を行い比表面積約1000m′/
?位のものを得た。And (a), (b) and e→ are all Example 1
The specific surface area is approximately 1000m'/
? I got something like that.
賦活収率とACFの状態を、実施例1とともに示すと第
3表の通りである。The activation yield and the state of ACF are shown in Table 3 together with Example 1.
これら(イ)〜e→のACFは29.6 kg/mA
〜31.2kg/maの繊維強度を有していた。The ACF of these (a) ~ e → is 29.6 kg/mA
It had a fiber strength of ~31.2 kg/ma.
実施例 3
60%塩化亜鉛水溶液90部、アクリロニトリル9.4
部、アクリル酸メチル0.59部、メタアリルスルホン
酸ソーダ0.01部から溶液を均一溶液重合し、得られ
た重合体溶液を紡糸原液とし紡糸し、Zn量として0.
4%のZnCl2を含むアクリロニトリル系繊維とした
。Example 3 90 parts of 60% zinc chloride aqueous solution, 9.4 parts of acrylonitrile
0.59 parts of methyl acrylate, and 0.01 part of sodium metaallylsulfonate were subjected to homogeneous solution polymerization, and the obtained polymer solution was used as a spinning stock solution for spinning, and the amount of Zn was 0.59 parts.
It was an acrylonitrile fiber containing 4% ZnCl2.
この繊維をリン酸水溶液に浸漬しリンとして0,1%の
リン酸を付着させた。This fiber was immersed in a phosphoric acid aqueous solution to adhere 0.1% phosphoric acid as phosphorus.
次いで270℃空気中で5時間、自由収縮率に対して8
0%の収縮を与える張力下で、かつ結合酸素量が飽和酸
素結合量の80%になるまで十分に酸化した。Then, in air at 270°C for 5 hours, the free shrinkage rate was 8
It was sufficiently oxidized under tension to give 0% shrinkage and until the amount of bound oxygen was 80% of the saturated amount of bound oxygen.
しかる後、550℃にて22分、窒素ガス雰囲気中で熱
処理し、次いで850℃、水蒸気ガス中にて、自由収縮
率に対して80%の収縮を与える張力下で賦活した。Thereafter, it was heat-treated at 550° C. for 22 minutes in a nitrogen gas atmosphere, and then activated at 850° C. in steam gas under tension to give a shrinkage of 80% of the free shrinkage rate.
賦活収率は27.6%、得られたACFO比表面比表面
積1030グ″/グゼン吸着量48.1%、繊維強度3
1kg/−であった。The activation yield was 27.6%, the obtained ACFO specific surface area was 1030 g''/guzen adsorption amount was 48.1%, and the fiber strength was 3.
It was 1 kg/-.
このものの耐熱酸化性を熱重量分析器(理学電気社製)
で空気中にて測定した結果400℃×3時間の重量減少
率は12%であった。The thermal oxidation resistance of this material was measured using a thermogravimetric analyzer (manufactured by Rigaku Denki Co., Ltd.)
As a result of measurement in air at 400° C. for 3 hours, the weight loss rate was 12%.
第1図は、熱処理温度と賦活収率の関係を示したもので
ある。
第2図は、金属添加量と賦活収率の関係を示したもので
ある。FIG. 1 shows the relationship between heat treatment temperature and activation yield. FIG. 2 shows the relationship between the amount of metal added and the activation yield.
Claims (1)
処理して得られたMg1zn、sb、Ca又はPを含む
化合物の何れか一種又は二種以上を該金属換算にして0
.05〜1%(重量)含む耐炎繊維を300〜800℃
にて不活性ガス雰囲気中で熱処理し、次いで張力下70
0〜1000°Cの温度でガス賦活することを特徴とす
る活性炭素繊維の製造方法。1 Any one or two or more compounds containing Mg1zn, sb, Ca or P obtained by flame-retardant treatment under tension using acrylonitrile fiber as a raw material are 0 in terms of the metal.
.. Flame-resistant fiber containing 05-1% (weight) at 300-800℃
heat treated in an inert gas atmosphere and then heated under tension for 70 minutes.
A method for producing activated carbon fiber, characterized by gas activation at a temperature of 0 to 1000°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53078654A JPS591803B2 (en) | 1978-06-30 | 1978-06-30 | Method for manufacturing activated carbon fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53078654A JPS591803B2 (en) | 1978-06-30 | 1978-06-30 | Method for manufacturing activated carbon fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS557534A JPS557534A (en) | 1980-01-19 |
| JPS591803B2 true JPS591803B2 (en) | 1984-01-14 |
Family
ID=13667837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53078654A Expired JPS591803B2 (en) | 1978-06-30 | 1978-06-30 | Method for manufacturing activated carbon fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS591803B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61108842U (en) * | 1984-12-21 | 1986-07-10 | ||
| JP2016535175A (en) * | 2013-10-29 | 2016-11-10 | コーロン インダストリーズ インク | Activated carbon fiber and method for producing the same |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57191328A (en) * | 1981-05-13 | 1982-11-25 | Toho Rayon Co Ltd | Preparation of fibrous active carbon |
| DE10028654A1 (en) | 2000-06-09 | 2001-12-20 | Sandler Helmut Helsa Werke | Reactivation of activated charcoal, used in thin film filter for air purification by adsorption and catalytic reaction of sulfur dioxide, involves heating to activation temperature in gas containing ammonia, carbon dioxide and/or steam |
| WO2026048691A1 (en) * | 2024-09-02 | 2026-03-05 | 株式会社豊田中央研究所 | Carbon fiber bundle, method for producing same, and carbon fiber precursor bundle |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5614608B2 (en) * | 1973-03-13 | 1981-04-06 | ||
| JPS52103530A (en) * | 1976-02-26 | 1977-08-30 | Toho Rayon Co Ltd | Production of acrylic carbon fibers |
| JPS52107328A (en) * | 1976-03-03 | 1977-09-08 | Toho Rayon Co Ltd | Production of carbon fiber from acrylic fiber |
-
1978
- 1978-06-30 JP JP53078654A patent/JPS591803B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61108842U (en) * | 1984-12-21 | 1986-07-10 | ||
| JP2016535175A (en) * | 2013-10-29 | 2016-11-10 | コーロン インダストリーズ インク | Activated carbon fiber and method for producing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS557534A (en) | 1980-01-19 |
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