JP2002138386A - Activated carbon fiber sheet and method for producing the same - Google Patents

Activated carbon fiber sheet and method for producing the same

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Publication number
JP2002138386A
JP2002138386A JP2000330646A JP2000330646A JP2002138386A JP 2002138386 A JP2002138386 A JP 2002138386A JP 2000330646 A JP2000330646 A JP 2000330646A JP 2000330646 A JP2000330646 A JP 2000330646A JP 2002138386 A JP2002138386 A JP 2002138386A
Authority
JP
Japan
Prior art keywords
activated carbon
carbon fiber
sheet
fiber
component
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
JP2000330646A
Other languages
Japanese (ja)
Inventor
Keiichi Asami
圭一 浅見
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP2000330646A priority Critical patent/JP2002138386A/en
Publication of JP2002138386A publication Critical patent/JP2002138386A/en
Pending legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Paper (AREA)

Abstract

PROBLEM TO BE SOLVED: To prepare a high-density activated carbon fiber sheet having excellent handleability, causing neither break nor crack in formation in post processing, in application, or the like, and to provide a method for producing the same. SOLUTION: This activated carbon fiber sheet is a sheet consisting essentially of an activated carbon fiber and a conjugate fiber comprising a high-melting polymer as a core component and a low-melting polymer as a sheath component. The activated carbon fiber is bonded to the sheath component by its fusion with the sheath component of the conjugate fiber. The activated carbon fiber sheet comprises 10-90 mass % of the activated carbon fiber and has 20-300 g/m2 weight and >=0.10 g/cm3 density.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、活性炭繊維を主成
分として湿式抄紙法で得られる、脱臭用フィルターとし
て好適な活性炭繊維シートとその製造法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an activated carbon fiber sheet which is obtained by a wet papermaking method using activated carbon fibers as a main component and is suitable as a deodorizing filter and a method for producing the same.

【0002】[0002]

【従来の技術】ポリアクリロニトリル系、フェノール
系、レーヨン系、ピッチ系等の繊維状物から得られた活
性炭繊維は、粒状活性炭に比べて吸脱着速度が速いた
め、気相系や液相系での悪臭成分除去、溶剤回収の分野
等に広く利用されている。しかし、活性炭繊維をそのま
まの状態で使用することは、汚染性や取扱い性等で実用
上問題となる場合が多い。
2. Description of the Related Art Activated carbon fibers obtained from fibrous materials such as polyacrylonitrile, phenol, rayon, and pitch have a higher adsorption and desorption speed than granular activated carbon, and therefore are not suitable for gas-phase or liquid-phase systems. It is widely used in fields such as removal of odorous components and solvent recovery. However, using the activated carbon fiber as it is often poses a practical problem due to contamination, handling properties, and the like.

【0003】そこで、バインダー等を用いて活性炭繊維
をシート状等の成形体にしたものが提案されている。例
えば、特開昭63−283749号公報では、活性炭繊
維と熱融着性合成樹脂を含む均一な水性スラリーを型内
で脱水成形した後、加熱して活性炭繊維と熱融着性合成
樹脂とを接合させた吸着体が提案されている。しかし、
熱融着性合成樹脂を使用するため、活性炭繊維同士を接
着させるためには配合量を多くする必要があり、その結
果として吸着体中の活性炭繊維の含有率が低くなり、吸
着性能が低下するという問題があった。
[0003] Therefore, there has been proposed a material in which activated carbon fibers are formed into a sheet or the like using a binder or the like. For example, in JP-A-63-283949, a uniform aqueous slurry containing activated carbon fibers and a heat-fusible synthetic resin is dehydrated in a mold, and then heated to form the activated carbon fibers and the heat-fusible synthetic resin. A bonded adsorbent has been proposed. But,
In order to use the heat-fusible synthetic resin, it is necessary to increase the blending amount in order to bond the activated carbon fibers to each other. As a result, the content of the activated carbon fibers in the adsorbent becomes low, and the adsorption performance is reduced. There was a problem.

【0004】また、特開平4−197437号公報で
は、活性炭繊維と熱融着性合成樹脂及び紙力増強材を含
む均一な水性スラリーを型内で脱水成形した後、加熱し
て活性炭繊維と熱融着性合成樹脂とを接合させた吸着体
が提案されている。しかし、この吸着体は、熱融着性合
成樹脂の配合量が少ないため密着性が弱く、活性炭繊維
が吸着体から脱落したり、強度不足で作業時の取扱いに
問題を生じることがあった。
[0004] In Japanese Patent Application Laid-Open No. 4-197737, a uniform aqueous slurry containing activated carbon fibers, a heat-fusible synthetic resin, and a paper strength enhancing material is dewatered in a mold, and then heated to form activated carbon fibers and heat. An adsorbent in which a fusible synthetic resin is bonded has been proposed. However, this adsorbent has a low adhesiveness due to a small amount of the heat-fusible synthetic resin, and the activated carbon fiber may fall off the adsorbent, or the strength may be insufficient, which may cause a problem in handling during operation.

【0005】さらに、特許第3046347号公報に
は、高融点合成樹脂を芯成分とし、かつ、低融点合成樹
脂を鞘成分とする複合繊維と活性炭素繊維を必須成分と
し、これらの繊維を含有する水性スラリーを湿式抄紙法
により抄紙し、鞘成分の融点より高く、芯成分の融点よ
り低い温度で乾燥し、活性炭素繊維と複合繊維を融着さ
せた後、得られたシートを乾燥温度より高く、複合繊維
の芯成分の融点より低い温度で熱処理する工程を経て得
られたフィルター濾材であって、シート重量に対し活性
炭素繊維を50〜97質量%含有し、坪量が50〜300g/m2
範囲で、密度が0.08g/cm3 以下である脱臭用フィルター
濾材及びその製造法が開示されている。しかし、この濾
材は、脱臭用フィルターとしてコルゲート、コルウェー
ブ等に加工する場合、密度が低すぎて成型が非常に困難
である。また、抄紙後に、鞘成分の融点より高く芯成分
の融点より低い温度で乾燥し、活性炭素繊維と複合繊維
を融着させた後、得られたシートを乾燥温度より高く、
複合繊維の芯成分の融点より低い温度で熱処理するとい
う複雑な工程を経るため、コストが高くなるという欠点
を有している。
Further, Japanese Patent No. 3046347 discloses that a composite fiber having a high melting point synthetic resin as a core component and a low melting point synthetic resin as a sheath component and an activated carbon fiber are essential components, and these fibers are contained. The aqueous slurry is made by a wet papermaking method, dried at a temperature higher than the melting point of the sheath component and lower than the melting point of the core component, and after fusion of the activated carbon fibers and the composite fibers, the obtained sheet is heated to a temperature higher than the drying temperature. A filter medium obtained through a step of heat-treating at a temperature lower than the melting point of the core component of the composite fiber, wherein the filter medium contains 50 to 97% by mass of activated carbon fibers based on the sheet weight, and has a basis weight of 50 to 300 g / m. 2, a filter medium for deodorization having a density of 0.08 g / cm 3 or less and a method for producing the same are disclosed. However, when this filter medium is processed into a corrugate, a corrugate, or the like as a deodorizing filter, the density is too low and it is very difficult to mold. Further, after papermaking, drying at a temperature higher than the melting point of the sheath component and lower than the melting point of the core component, and after fusing the activated carbon fiber and the composite fiber, the obtained sheet is higher than the drying temperature,
The heat treatment is performed at a temperature lower than the melting point of the core component of the conjugate fiber, so that the cost is increased.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記の問題
を解決し、活性炭繊維と、高融点ポリマーを芯成分と
し、低融点ポリマーを鞘成分とする複合繊維とを主成分
とし、後加工における成型時や施工時等に折れや割れが
なく、取扱い性に優れた高密度の活性炭繊維シートとそ
の製造法を提供することを技術的な課題とするものであ
る。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems, and comprises, as main components, an activated carbon fiber and a composite fiber having a high melting polymer as a core component and a low melting polymer as a sheath component. It is an object of the present invention to provide a high-density activated carbon fiber sheet which is free from breakage or cracking at the time of molding or construction and has excellent handleability and a method for producing the same.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記の課
題を解決するために鋭意検討した結果、活性炭繊維と、
高融点ポリマーを芯成分とし、低融点ポリマーを鞘成分
とする複合繊維とを主成分として湿式抄紙した後、複合
繊維の鞘成分の融点以上の温度で熱処理をすることによ
り、得られるシートが高密度で加工性が良好であること
を見出して本発明に到達した。
Means for Solving the Problems The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, have found that activated carbon fibers and
After wet papermaking with a high-melting-point polymer as a core component and a composite fiber having a low-melting-point polymer as a sheath component as a main component, the resulting sheet is subjected to a heat treatment at a temperature equal to or higher than the melting point of the sheath component of the composite fiber. The inventors have found that the workability is good at the density, and arrived at the present invention.

【0008】すなわち、本発明は、次の構成をその要旨
とするものである。 (1) 活性炭繊維と、高融点ポリマーを芯成分とし、低融
点ポリマーを鞘成分とする複合繊維とを主成分とするシ
ートであって、活性炭繊維は複合繊維の鞘成分との融着
により結合されており、活性炭繊維を10〜90質量%
含有し、かつ、坪量が20〜300g/m2、密度が0.1
0g/cm3 以上であることを特徴とする活性炭繊維シー
ト。 (2) 活性炭繊維と、高融点ポリマーを芯成分とし、低融
点ポリマーを鞘成分とする複合繊維とを主成分とする水
性スラリーを湿式抄紙法により抄紙し、次いで、前記複
合繊維の鞘成分の融点以上、(芯成分の融点−20)℃
以下の温度で熱処理することを特徴とする上記(1) 記載
の活性炭繊維シートの製造法。
That is, the gist of the present invention is as follows. (1) A sheet mainly composed of activated carbon fibers and a composite fiber having a high-melting polymer as a core component and a low-melting polymer as a sheath component, wherein the activated carbon fibers are bonded by fusion with the sheath component of the composite fiber. 10 to 90% by mass of activated carbon fiber
Containing, and having a basis weight of 20 to 300 g / m 2 and a density of 0.1
An activated carbon fiber sheet characterized by being at least 0 g / cm 3 . (2) Activated carbon fiber and a high-melting polymer as a core component, an aqueous slurry containing a composite fiber having a low-melting polymer as a sheath component as a main component is formed by a wet papermaking method, and then the sheath component of the composite fiber is produced. Above the melting point, (melting point of core component -20) ° C
The method for producing an activated carbon fiber sheet according to the above (1), wherein the activated carbon fiber sheet is heat-treated at the following temperature.

【0009】[0009]

【発明の実施の形態】以下、本発明について詳細に説明
する。本発明の活性炭繊維シートは、活性炭繊維と、高
融点ポリマーを芯成分とし、低融点ポリマーを鞘成分と
する複合繊維(以下、バインダー繊維という。)とを主
成分とし、活性炭繊維が好ましくは均一な分散状態でバ
インダー繊維の鞘成分との融着により結合されたもので
ある。なお、本発明において、低融点ポリマーとは、基
本的には高融点ポリマーより融点の低いポリマーをいう
が、明瞭な融点を示さないポリマーの場合は、高融点ポ
リマーより低軟化点のポリマーをいう。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. The activated carbon fiber sheet of the present invention comprises, as main components, activated carbon fibers and composite fibers (hereinafter, referred to as binder fibers) having a high-melting polymer as a core component and a low-melting polymer as a sheath component, and the activated carbon fibers are preferably uniform. It is bonded by fusion to the sheath component of the binder fiber in a dispersed state. In the present invention, the low-melting polymer basically refers to a polymer having a lower melting point than the high-melting polymer, but in the case of a polymer not showing a clear melting point, a polymer having a lower softening point than the high-melting polymer. .

【0010】本発明において、活性炭繊維シートの坪量
は20〜300g/m2であることが必要であり、特に30
〜250g/m2が好ましい。シートの坪量が20g/m2未満で
は、シートの目付バラツキが大きくなるため均一なシー
トが得られない。また、300g/m2を超えると、湿式抄
紙した後の熱処理が難しくなり、さらには後加工が困難
になる。次に、シートの密度は0.10g/cm3 以上、好まし
くは0.12〜0.30g/cm3 であることが必要であり、0.10g/
cm3 未満になると、後加工が非常に困難になる。
In the present invention, the basis weight of the activated carbon fiber sheet needs to be 20 to 300 g / m 2 , especially 30 g / m 2.
~250g / m 2 is preferred. If the basis weight of the sheet is less than 20 g / m 2 , the uniform weight of the sheet will increase, and a uniform sheet cannot be obtained. On the other hand, if it exceeds 300 g / m 2 , heat treatment after wet papermaking becomes difficult, and further post-processing becomes difficult. Then, the density of the sheet is 0.10 g / cm 3 or more, preferably must be a 0.12~0.30g / cm 3, 0.10g /
If it is less than cm 3 , post-processing becomes very difficult.

【0011】本発明で使用されるバインダー繊維として
は、例えば、芯部がポリプロピレンで鞘部が変性ポリエ
チレンからなるポリオレフィン系、芯部がポリエチレン
テレフタレートで鞘部がポリオレフィンからなる繊維、
芯部がポリエチレンテレフタレートで鞘部が低融点(低
軟化点)ポリエステルからなるポリエステル系等の、鞘
部の融点(軟化点)が芯部の融点より低い芯鞘構造複合
繊維が挙げられる。これらの中では、ユニチカファイバ
ー株式会社からメルティーの商標で上市されているポリ
エステル系複合繊維が好ましい。
The binder fibers used in the present invention include, for example, a polyolefin fiber having a core of polypropylene and a sheath of modified polyethylene, a fiber having a core of polyethylene terephthalate and a sheath of polyolefin,
Core-sheath composite fibers having a core having a melting point (softening point) lower than the core melting point, such as a polyester-based polyester having a core made of polyethylene terephthalate and a sheath made of polyester having a low melting point (low softening point). Among these, polyester-based composite fibers marketed by Unitika Fiber Co., Ltd. under the trademark of Melty are preferred.

【0012】上記バインダー繊維の平均繊維長としては
1〜50mmが望ましく、特に3〜25mmが好まし
い。平均繊維長が1mmより短いと、シートの強度が低
下しやすく、50mmを超えると水中での分散状態が悪
くなり、活性炭繊維とバインダー繊維の均一性が低下す
る。また、バインダー繊維の平均繊維径は2〜100μ
m、特に5〜50μmが好ましい。平均繊維径が100
μmを超えると、融着させても活性炭繊維を十分に捕捉
し難くなる。
The average fiber length of the binder fibers is desirably 1 to 50 mm, and particularly desirably 3 to 25 mm. If the average fiber length is shorter than 1 mm, the strength of the sheet tends to decrease. If the average fiber length exceeds 50 mm, the dispersion state in water deteriorates, and the uniformity of the activated carbon fibers and the binder fibers decreases. The average fiber diameter of the binder fiber is 2 to 100 μm.
m, particularly preferably 5 to 50 μm. Average fiber diameter is 100
When the thickness exceeds μm, it becomes difficult to sufficiently capture activated carbon fibers even when fusion is performed.

【0013】次に、本発明で使用される活性炭繊維は、
その種類が特に限定されるものではなく、シートの使用
分野等の目的に応じて選択することができる。例えばポ
リアクリロニトリル系、レーヨン系、フェノール樹脂
系、石炭ピッチ系、石油ピッチ系等の繊維を不融化し、
所望により炭化処理した後、水蒸気、二酸化炭素を含有
する雰囲気中、所定温度で所定時間保持することによっ
て賦活することにより製造される任意の活性炭繊維を採
用することができるが、中でも石炭ピッチや石油ピッチ
を原料とした活性炭繊維は理論炭化収率が高い点で有利
である。また、酸性ガス除去用活性炭繊維、アルカリガ
ス除去用活性炭繊維、低級アルデヒド類除去用活性炭繊
維等の薬剤を添着した特殊活性炭繊維、あるいは抗菌性
やその他の特性を付与するため、銀や白金等の金属を添
着した活性炭繊維も目的に応じて使用できる。
Next, the activated carbon fibers used in the present invention are:
The type is not particularly limited and can be selected according to the purpose such as the field of use of the sheet. For example, polyacrylonitrile type, rayon type, phenolic resin type, coal pitch type, petroleum pitch type etc.
After carbonization as desired, any activated carbon fiber produced by activating by holding at a predetermined temperature and for a predetermined time in an atmosphere containing water vapor and carbon dioxide can be used. Activated carbon fibers made from pitch are advantageous in that the theoretical carbonization yield is high. In addition, activated carbon fibers for removing acidic gases, activated carbon fibers for removing alkaline gases, activated carbon fibers for removing lower aldehydes, etc., or special activated carbon fibers impregnated with agents such as silver or platinum for imparting antibacterial properties and other properties. Activated carbon fibers impregnated with a metal can also be used according to the purpose.

【0014】上記活性炭繊維の平均繊維径としては、3
0μm以下、特に5〜20μmが好ましい。平均繊維径が
30μmを超えると折損しやすくなり、成形加工し難く
なる。また、活性炭繊維の平均繊維長は0.5〜50m
mが望ましく、特に3〜25mmが好ましい。平均繊維
長が0.5mmより短いとシートに十分な強度が付与さ
れ難く、50mmを超えると水中での分散が悪くなり、
活性炭繊維とバインダー繊維の混合の均一性が低下しや
すくなる。
The average fiber diameter of the activated carbon fibers is 3
It is preferably 0 μm or less, particularly preferably 5 to 20 μm. If the average fiber diameter exceeds 30 μm, breakage is likely to occur, and molding processing becomes difficult. The average fiber length of the activated carbon fiber is 0.5 to 50 m.
m is desirable, and particularly preferably 3 to 25 mm. If the average fiber length is less than 0.5 mm, it is difficult to impart sufficient strength to the sheet, and if it exceeds 50 mm, dispersion in water becomes worse,
The uniformity of mixing of the activated carbon fiber and the binder fiber is likely to be reduced.

【0015】さらに、本発明の活性炭繊維シートにおけ
る活性炭繊維の含有量は、10〜90質量%、好ましく
は40〜80質量%であることが必要である。活性炭繊
維の含有量が10質量%未満では吸着性能が不足し、9
0質量%を超えると、吸着性能はよいが強度が不足す
る。
Further, the content of the activated carbon fiber in the activated carbon fiber sheet of the present invention must be 10 to 90% by mass, preferably 40 to 80% by mass. When the content of the activated carbon fiber is less than 10% by mass, the adsorption performance is insufficient, and
If it exceeds 0% by mass, the adsorption performance is good but the strength is insufficient.

【0016】次に、本発明の活性炭繊維シートの製造法
について説明する。まず、活性炭繊維とバインダー繊維
とを水中で分散、混合して水性スラリーを調製する。こ
れにより、活性炭繊維と、高融点ポリマーを芯成分と
し、低融点ポリマーを鞘成分とするバインダー繊維とが
充分に分散混合されて、両方の繊維が均一に分散して複
合化した状態となる。
Next, a method for producing the activated carbon fiber sheet of the present invention will be described. First, an activated carbon fiber and a binder fiber are dispersed and mixed in water to prepare an aqueous slurry. As a result, the activated carbon fiber and the binder fiber having the high melting point polymer as the core component and the low melting point polymer as the sheath component are sufficiently dispersed and mixed, and both fibers are uniformly dispersed and composited.

【0017】次いで、水性スラリーを湿式抄紙法により
抄紙し、シートを形成する。すなわち、シートの形成に
は、抄紙機などを用い、抄紙の要領で水中の固形分をシ
ート状となすように固液分離するのがよい。得られた湿
ったシートをバインダー繊維の鞘成分の融点以上、(芯
成分の融点−20)℃以下の温度で熱処理することによ
り、本発明の活性炭繊維シートが得られる。
Next, the aqueous slurry is made into a sheet by a wet papermaking method to form a sheet. That is, it is preferable that the sheet is formed by using a paper machine or the like, and solid-liquid separated in such a manner that solids in water are formed into a sheet in the manner of paper making. The activated carbon fiber sheet of the present invention is obtained by subjecting the obtained wet sheet to a heat treatment at a temperature not lower than the melting point of the sheath component of the binder fiber and not higher than (melting point of the core component−20) ° C.

【0018】本発明では、必要に応じて、熱処理して得
られた活性炭繊維シートの密度を上げるために面圧0.1
kgf/cm2 以上のプレス圧力下に加熱し、次いでプ
レス圧力を保持した状態で冷却することも可能である。
In the present invention, if necessary, to increase the density of the activated carbon fiber sheet obtained by the heat treatment, the surface pressure is set to 0.1.
It is also possible to heat under a pressing pressure of not less than kgf / cm 2 and then cool while maintaining the pressing pressure.

【0019】また、抄紙後のシートの強度を向上させる
ために、水性スラリー中に合成パルプを添加して製造す
ることもできる。合成パルプとは、例えばポリオレフィ
ン系、ポリアクリル系、ポリイミド系、芳香族ポリアミ
ド系、全芳香族ポリエステル系等の熱可塑性ポリマーか
らなるパルプ状多分岐繊維である。これらの合成パルプ
は、水中に分散させた場合に他材料の捕捉力が非常に強
力なため、合成パルプの少量の添加で湿式抄紙法により
強度の高いシートを作製することができる。
Further, in order to improve the strength of the sheet after papermaking, it can be produced by adding synthetic pulp to an aqueous slurry. The synthetic pulp is a pulp-like multibranched fiber made of a thermoplastic polymer such as polyolefin, polyacryl, polyimide, aromatic polyamide, and wholly aromatic polyester. Since these synthetic pulp have a very strong power of capturing other materials when dispersed in water, a sheet having high strength can be produced by a wet papermaking method by adding a small amount of synthetic pulp.

【0020】水性スラリーを調製する際には、必要に応
じて例えば結合剤を用いることもできる。結合剤は固体
成分で3質量%未満、特に1質量%未満を添加させるこ
とが好ましい。結合剤としては、例えば、結合したスル
ホニウム基、イソチオウロニウム基、ピリジニウム基、
第四アンモニウム基、サルフェート基、スルホネート基
又はカルボキシレート基を含有するアクリルポリマー又
はスチレン・ブタジエンポリマーのような結合した陰イ
オンもしくは陽イオン電荷を有する実質的に水に不溶な
有機ポリマーからなるポリマーラテックス等が挙げられ
る。
In preparing the aqueous slurry, for example, a binder may be used as necessary. It is preferable to add less than 3% by weight, especially less than 1% by weight, of the binder as a solid component. Examples of the binder include a bound sulfonium group, an isothiouronium group, a pyridinium group,
Polymer latex comprising a substantially water-insoluble organic polymer having an attached anionic or cationic charge, such as an acrylic polymer or a styrene-butadiene polymer containing quaternary ammonium, sulfate, sulfonate or carboxylate groups. And the like.

【0021】さらに、この結合剤を使用する方法では、
有機凝集剤を併用することが好ましい。適当な有機凝集
剤としては、アルミニウム・ポリクロリド(アルミニウ
ム・ヒドロオキシクロリド)、一部加水分解したポリア
クリルアミド、変性陽イオンポリアクリルアミド、ジア
リルジエチルアンモニウムクロリド等の種々の有機凝集
剤が挙げられる。この凝集剤の添加量はシートの3質量
%未満、好ましくは1質量%未満である。また、分散性
を向上させるために、例えばキサンタンガム等のスラリ
ー粘度調整剤を用いることもできる。このような増粘剤
の添加量は、活性炭繊維シートの2質量%未満であるこ
とが好ましい。
Furthermore, in the method using this binder,
It is preferable to use an organic coagulant in combination. Suitable organic coagulants include various organic coagulants such as aluminum polychloride (aluminum hydroxychloride), partially hydrolyzed polyacrylamide, modified cationic polyacrylamide, diallyldiethylammonium chloride, and the like. The amount of the coagulant added is less than 3% by weight of the sheet, preferably less than 1% by weight. Further, in order to improve dispersibility, a slurry viscosity modifier such as xanthan gum can be used. The amount of such a thickener added is preferably less than 2% by mass of the activated carbon fiber sheet.

【0022】本発明の活性炭繊維シートは、そのままの
形状でも使用できるが、後加工性と可撓性に優れている
ので、例えば波板状(コルウエーブ状)に成形したり、
コルゲート加工法によってハニカムを作製するのにも好
適に使用できる。
The activated carbon fiber sheet of the present invention can be used as it is, but since it has excellent post-processability and flexibility, it can be formed into, for example, a corrugated sheet (corrugated).
It can also be suitably used for producing a honeycomb by a corrugating method.

【0023】[0023]

【実施例】次に、本発明を実施例により具体的に説明す
るが、本発明は実施例に限定されるものではない。な
お、実施例における各特性の評価は、次の方法で行っ
た。また、実施例において記載の%は、すべて質量%で
ある。 (1) 比表面積 窒素を被吸着物質として用い、BET多点法で測定し
た。 (2) 理論比表面積 シート1g中に含有される活性炭繊維の質量をL、活性
炭繊維の比表面積をTm2 /gとすると、理論比表面積
(m2/gシート)=L×Tにより算出した。 (3) 加工性の評価 コルゲーターによりセルピッチ10mm、セル高さ5mm、条
線幅 0.5mmの台形型のセル形状を加工して評価した。 (4) ヨウ素吸着量 シート1.00gを0.05規定のヨウ素溶液(温度2
8℃)中で30分間振とうし、ヨウ素残留濃度2.5g/
リットルにおけるヨウ素吸着量を測定した。
Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to the examples. The evaluation of each characteristic in the examples was performed by the following method. Further, all the percentages described in the examples are mass%. (1) Specific surface area It was measured by a BET multipoint method using nitrogen as the substance to be adsorbed. (2) Theoretical specific surface area Assuming that the mass of activated carbon fiber contained in 1 g of sheet is L and the specific surface area of activated carbon fiber is Tm 2 / g, the theoretical specific surface area is
(m 2 / g sheet) = L × T. (3) Evaluation of processability A trapezoidal cell shape having a cell pitch of 10 mm, a cell height of 5 mm, and a line width of 0.5 mm was processed by a corrugator and evaluated. (4) Iodine adsorption amount 1.00 g of the sheet was treated with a 0.05N iodine solution (temperature 2).
8 ° C) for 30 minutes, and a residual iodine concentration of 2.5 g /
The iodine adsorption amount in liter was measured.

【0024】実施例1〜3 活性炭繊維(アドールA−10、繊維長6mm、比表面積10
00m2/g、アドール社製)を水中に添加して 0.3%濃度に
調製し、SV型往復反転式攪拌機(島崎製作所製アジタ
−)で分散させた後、鞘部の軟化点が80℃、芯部の融点
が 250℃の芯鞘タイプのポリエステルバインダー繊維
(メルティー4080、2.2dtex ×5mm、ユニチカ社製)を
アジターで攪拌しながら添加混合した。このとき活性炭
繊維/ポリエステルバインダー繊維の混合比を70/30
(実施例1)、65/35(実施例2)、50/50(実施例
3)の3水準で調製した。
Examples 1 to 3 Activated carbon fibers (Adol A-10, fiber length 6 mm, specific surface area 10
00m 2 / g, manufactured by Adol) was added to water to prepare a 0.3% concentration, and the mixture was dispersed with an SV type reciprocating reversing stirrer (Agita, manufactured by Shimazaki Seisakusho). A core-sheath type polyester binder fiber (melt 4080, 2.2 dtex × 5 mm, manufactured by Unitika Ltd.) having a melting point of the core of 250 ° C. was added and mixed while stirring with an agitator. At this time, the mixing ratio of activated carbon fiber / polyester binder fiber was 70/30.
(Example 1), 65/35 (Example 2) and 50/50 (Example 3) were prepared at three levels.

【0025】次いで、このスラリ−に水を加えて各々
0.1%に希釈し、乾燥重量で150g/m2のシ−トを角型手抄
装置(金網80メッシュ−金網寸法25cm×25cm)で抄紙し
た後、脱水プレスし、さらに 160℃の温風乾燥機中で1
0分間熱処理して活性炭繊維シートを得た。
Next, water was added to the slurry, and
Was diluted to 0.1% dry weight of 150 g / m 2 sheets - preparative square handsheet device - after papermaking with (wire mesh 80 mesh screen size 25 cm × 25 cm), dried and pressed, further hot-air drying of 160 ° C. 1 in the plane
Heat treatment was performed for 0 minutes to obtain an activated carbon fiber sheet.

【0026】実施例4 実施例3と同じ方法で坪量40g/m2の活性炭繊維シートを
得た。
Example 4 An activated carbon fiber sheet having a basis weight of 40 g / m 2 was obtained in the same manner as in Example 3.

【0027】比較例1 特許第3046347号公報の実施例3と同様の方法で
シートを作製した。すなわち、活性炭繊維(アドールA
−10、繊維長6mm、比表面積1000m2/g、アドール社製)
を水中に添加して 0.3%濃度に調製し、SV型往復反転
式攪拌機(島崎製作所製アジタ−)で分散した後、バイ
ンダー繊維として鞘部の軟化点が80℃、芯部の融点が 2
50℃の芯鞘タイプのポリエステルバインダー繊維(メル
ティー4080、2.2dtex ×5mm、ユニチカ社製)をアジタ
ーで攪拌しながら添加混合してスラリーを得た。また、
このとき活性炭素繊維/ポリエステルバインダー繊維の
混合比を70/30とした。
Comparative Example 1 A sheet was prepared in the same manner as in Example 3 of Japanese Patent No. 3046347. That is, activated carbon fiber (Adol A
-10, fiber length 6mm, specific surface area 1000m 2 / g, manufactured by Adol)
Was added to water to adjust the concentration to 0.3%, and dispersed with an SV type reciprocating reversing stirrer (Agita, manufactured by Shimazaki Seisakusho). As a binder fiber, the softening point of the sheath was 80 ° C and the melting point of the core was 2 ° C.
A core-sheath type polyester binder fiber (melty 4080, 2.2 dtex × 5 mm, manufactured by Unitika) at 50 ° C. was added and mixed while stirring with an agitator to obtain a slurry. Also,
At this time, the mixing ratio of activated carbon fiber / polyester binder fiber was set to 70/30.

【0028】次いで、上記スラリ−に水を加えて各々
0.1%に希釈し、乾燥重量で200g/m2のシ−トを角型手抄
装置(金網80メッシュ−金網寸法25cm×25cm)で抄紙し
た後、脱水プレスし、 110℃のシリンダードライヤーを
用いて乾燥した。その後、エアードライヤーを 190℃に
設定し、風速5m/s で熱処理を1分間行い、脱臭用フィ
ルター濾材として好適な活性炭繊維シートを得た。
Next, water was added to the above slurry, and
After diluting to 0.1%, the sheet with a dry weight of 200 g / m 2 was paper-made with a square-shaped hand paper making machine (wire mesh 80 mesh-wire mesh size 25 cm x 25 cm), dewatered and pressed using a 110 ° C cylinder dryer. And dried. Thereafter, an air dryer was set at 190 ° C., and heat treatment was performed at a wind speed of 5 m / s for 1 minute to obtain an activated carbon fiber sheet suitable as a filter medium for deodorization.

【0029】実施例5 実施例2と同じ方法で活性炭繊維シートを作製した。た
だし、バインダー繊維は芯がポリプロピレン(融点 160
℃)、鞘が変性ポリオレフィン(融点 100℃)の繊維
( NBF繊維、Eタイプ、2.2dtex ×5mm、大和紡績社
製)を用い、温風乾燥機温度は 135℃、20分間熱処理
し、目付100g/m2 の活性炭繊維シートを得た。実施例1
〜5及び比較例1で得られた活性炭繊維シートの物性を
表1に示す。
Example 5 An activated carbon fiber sheet was produced in the same manner as in Example 2. However, the core of the binder fiber is polypropylene (melting point 160
℃), using a sheath of modified polyolefin (melting point 100 ℃) fiber (NBF fiber, E type, 2.2 dtex × 5 mm, manufactured by Daiwa Spinning Co., Ltd.), heat treatment at 135 ℃ for 20 minutes, 100 g of basis weight / m 2 of activated carbon fiber sheet was obtained. Example 1
Table 1 shows the physical properties of the activated carbon fiber sheets obtained in Comparative Examples 1 to 5 and Comparative Example 1.

【0030】[0030]

【表1】 [Table 1]

【0031】表1から明らかなように、本発明の活性炭
繊維シートは、密度が高い上に比表面積も多く残ってい
た。そのため、吸着性能、すなわち脱臭能力も損なわれ
ないことがわかる。一方、比較例1では、シートの比表
面積が少なくなっているため、吸着性能が劣っている。
次に、加工性の評価について、実施例1〜5のシート
は、問題なく加工できたが、比較例1のシートは密度が
小さいため強度が不足し、加工中にシートが破れて加工
できなかった。
As is apparent from Table 1, the activated carbon fiber sheet of the present invention has a high density and a large specific surface area. Therefore, it is understood that the adsorption performance, that is, the deodorizing ability is not impaired. On the other hand, in Comparative Example 1, since the specific surface area of the sheet is small, the adsorption performance is inferior.
Next, regarding the evaluation of workability, the sheets of Examples 1 to 5 could be processed without any problem, but the sheet of Comparative Example 1 was insufficient in strength due to low density, and the sheet was broken during processing and could not be processed. Was.

【0032】[0032]

【発明の効果】本発明の活性炭繊維シートは、密度が高
いために後加工における成型時や施工時等に折れや割れ
がなく、取扱い性に優れたものである。また、本発明の
活性炭繊維シートの製造法によれば、上記の利点を有す
る活性炭繊維シートを安定して製造することが可能とな
る。
The activated carbon fiber sheet of the present invention does not break or crack at the time of molding or construction in post-processing because of its high density, and is excellent in handleability. Further, according to the method for producing an activated carbon fiber sheet of the present invention, it is possible to stably produce an activated carbon fiber sheet having the above advantages.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) D21H 15/10 D21H 15/10 27/08 27/08 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) D21H 15/10 D21H 15/10 27/08 27/08

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 活性炭繊維と、高融点ポリマーを芯成分
とし、低融点ポリマーを鞘成分とする複合繊維とを主成
分とするシートであって、活性炭繊維は複合繊維の鞘成
分との融着により結合されており、活性炭繊維を10〜
90質量%含有し、かつ、坪量が20〜300g/m2、密
度が0.10g/cm3 以上であることを特徴とする活性炭
繊維シート。
1. A sheet mainly comprising activated carbon fibers and a composite fiber having a high-melting polymer as a core component and a low-melting polymer as a sheath component, wherein the activated carbon fibers are fused with the sheath component of the composite fibers. And activated carbon fiber is
An activated carbon fiber sheet containing 90% by mass, having a basis weight of 20 to 300 g / m 2 and a density of 0.10 g / cm 3 or more.
【請求項2】 活性炭繊維と、高融点ポリマーを芯成分
とし、低融点ポリマーを鞘成分とする複合繊維とを主成
分とする水性スラリーを湿式抄紙法により抄紙し、次い
で、前記複合繊維の鞘成分の融点以上、(芯成分の融点
−20)℃以下の温度で熱処理することを特徴とする請
求項1記載の活性炭繊維シートの製造法。
2. An aqueous slurry mainly comprising activated carbon fiber and a composite fiber having a high-melting polymer as a core component and a low-melting polymer as a sheath component is subjected to papermaking by a wet papermaking method. The method for producing an activated carbon fiber sheet according to claim 1, wherein the heat treatment is performed at a temperature not lower than the melting point of the component and not higher than (melting point of the core component-20) ° C.
JP2000330646A 2000-10-30 2000-10-30 Activated carbon fiber sheet and method for producing the same Pending JP2002138386A (en)

Priority Applications (1)

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Publication Number Publication Date
JP2002138386A true JP2002138386A (en) 2002-05-14

Family

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Country Status (1)

Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004290899A (en) * 2003-03-27 2004-10-21 Osaka Gas Co Ltd One-side honeycombed sheet and its manufacturing method
JP2005205291A (en) * 2004-01-21 2005-08-04 Mitsubishi Heavy Ind Ltd Activated carbon fiber sheet and removal method for harmful substance in flue gas or apparatus
JP2006132058A (en) * 2004-11-09 2006-05-25 Lintec Corp Adsorbing filter base paper and method for producing the same
JP2016065340A (en) * 2014-09-25 2016-04-28 住友ベークライト株式会社 Resin sheet, article, and method for producing resin sheet
KR101902463B1 (en) * 2016-09-12 2018-10-01 에코융합섬유연구원 Active carbon fiber paper and manufacturing method thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004290899A (en) * 2003-03-27 2004-10-21 Osaka Gas Co Ltd One-side honeycombed sheet and its manufacturing method
JP4657583B2 (en) * 2003-03-27 2011-03-23 大阪瓦斯株式会社 Single-stage honeycomb sheet and manufacturing method thereof
JP2005205291A (en) * 2004-01-21 2005-08-04 Mitsubishi Heavy Ind Ltd Activated carbon fiber sheet and removal method for harmful substance in flue gas or apparatus
JP2006132058A (en) * 2004-11-09 2006-05-25 Lintec Corp Adsorbing filter base paper and method for producing the same
JP4653458B2 (en) * 2004-11-09 2011-03-16 リンテック株式会社 Adsorption filter base paper and method for producing the same
JP2016065340A (en) * 2014-09-25 2016-04-28 住友ベークライト株式会社 Resin sheet, article, and method for producing resin sheet
KR101902463B1 (en) * 2016-09-12 2018-10-01 에코융합섬유연구원 Active carbon fiber paper and manufacturing method thereof

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