JP2862909B2 - Method for producing carbon molded body - Google Patents
Method for producing carbon molded bodyInfo
- Publication number
- JP2862909B2 JP2862909B2 JP1230780A JP23078089A JP2862909B2 JP 2862909 B2 JP2862909 B2 JP 2862909B2 JP 1230780 A JP1230780 A JP 1230780A JP 23078089 A JP23078089 A JP 23078089A JP 2862909 B2 JP2862909 B2 JP 2862909B2
- Authority
- JP
- Japan
- Prior art keywords
- carboxymethylcellulose
- ammonium salt
- molded body
- carbon
- aqueous solution
- 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 - Lifetime
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、機械的強度と耐水性を有する炭素成形体の
製造方法に関するものである。The present invention relates to a method for producing a carbon molded body having mechanical strength and water resistance.
活性炭はその優れた吸着能により気相及び液相用の吸
着材として広く利用されている。Activated carbon is widely used as an adsorbent for gas and liquid phases due to its excellent adsorption ability.
例えば、空気の清浄化、脱臭、気相中の溶剤の回収又
は水の浄化、脱色、溶解、不純物の除去、ガス分離など
に使用される。For example, it is used for air purification, deodorization, recovery of a solvent in a gas phase or purification of water, decolorization, dissolution, removal of impurities, gas separation, and the like.
この様な用途には、活性炭を均一な通気性、通液性を
有する均質緻密な構造を持ち、かつ機械的強度、耐水性
等の優れた成形体とすることが必要である。For such uses, it is necessary to make the activated carbon into a molded article having a uniform and dense structure having uniform air permeability and liquid permeability, and excellent in mechanical strength, water resistance and the like.
この様な目的で従来行われている活性炭成形体、特に
活性炭繊維成形体の製造方法としては、活性炭繊維とポ
リアクリロニトリルなどの熱溶融性合成樹脂繊維と混合
した後加熱融着させ成形体を得る方法、アクリル繊維等
の合成繊維をフェルト状又は織物状とした後熱処理又は
薬品処理により活性炭化する方法、炭素繊維をフェルト
状又は織物状とした後熱処理又は薬品処理により活性炭
化する方法などが挙げられる。As a method for producing an activated carbon molded body, particularly an activated carbon fiber molded body, conventionally carried out for such a purpose, a molded article is obtained by mixing activated carbon fiber and a heat-fusible synthetic resin fiber such as polyacrylonitrile and then heat-fusing the mixture. Method, a method in which synthetic fibers such as acrylic fiber or the like are made into a felt shape or a woven shape and then activated carbonization by heat treatment or chemical treatment, and a method in which carbon fibers are made into a felt or woven shape and then activated carbonization by heat treatment or chemical treatment. Can be
しかし、これらの方法では均質緻密な構造の吸着体が
得られないこと、十分な機械的強度を有する成形体が得
られないこと、所定形状への再加工が必要であるなど、
多くの実用上の欠点があった。However, with these methods, it is not possible to obtain an adsorbent having a homogeneous and dense structure, a molded body having sufficient mechanical strength cannot be obtained, and it is necessary to rework to a predetermined shape.
There were many practical disadvantages.
又炭素繊維、カーボンブラック、球状炭素微粒子、そ
の他の各種の炭素材料からなる機械的強度、耐水性の優
れた炭素成形体を製造する方法も望まれていた。There has also been a demand for a method for producing a carbon molded body made of carbon fiber, carbon black, spherical carbon fine particles, and other various carbon materials having excellent mechanical strength and water resistance.
本発明者らはカルボキシルメチルセルロースアンモニ
ウム塩の熱分解法と熱架橋性に着目し、これを炭素材
料、特に活性炭繊維の成形方法に応用すべく鋭意研究を
重ねた結果、本発明をなすに至ったものである。The present inventors have focused on the thermal decomposition method and thermal crosslinkability of carboxymethylcellulose ammonium salt, and as a result of diligent research to apply this to a method for forming a carbon material, particularly an activated carbon fiber, came to the present invention. Things.
即ち本発明は、炭素材料にカルボキシメチルセルロー
スアンモニウム塩の水溶液を含浸させ成形した後、100
〜300℃で3〜0.5時間加熱することによりカルボキシメ
チルセルロースアンモニウム塩を熱分解してカルボキシ
メチルセルロースに変化させ、さらにカルボキシメチル
セルロース分子間で架橋反応させることを特徴とする炭
素成形体の製造方法である。That is, the present invention is to impregnate the carbon material with an aqueous solution of carboxymethylcellulose ammonium salt, mold it,
This is a method for producing a carbon molded body, wherein a carboxymethylcellulose ammonium salt is thermally decomposed into carboxymethylcellulose by heating at 300300 ° C. for 3 to 0.5 hours, followed by a crosslinking reaction between carboxymethylcellulose molecules.
本発明の炭素材料には、繊維状、粉状のいかなる炭素
材料も用いることができる。As the carbon material of the present invention, any fibrous or powdery carbon material can be used.
繊維状の炭素材料としては、レーヨン系、ポリアクリ
ロニトリル系、フェノール樹脂系、石炭ピッチ系、石油
ピッチ系等の各種の炭素繊維及びこれを活性化した活性
炭繊維を挙げることができる。その繊維形状等は成形体
の使用目的に応じて適宜選択すればよい。活性炭繊維の
場合通常使用されるものは、繊維直径2〜30μm、繊維
長0.2〜20mm、比表面積300〜3500m2/g程度のものであ
る。Examples of the fibrous carbon material include rayon-based, polyacrylonitrile-based, phenolic resin-based, coal pitch-based, and petroleum pitch-based carbon fibers and activated carbon fibers obtained by activating the carbon fibers. The fiber shape and the like may be appropriately selected according to the purpose of use of the molded article. In the case of activated carbon fibers, those usually used have a fiber diameter of 2 to 30 μm, a fiber length of 0.2 to 20 mm, and a specific surface area of about 300 to 3500 m 2 / g.
粉状の炭素材料には、カーボンブラック、石炭、石炭
コークス、ピッチ、ピッチコークス、黒鉛、木炭、ヤシ
ガラ炭等の粉状、粒状のもの、及びこれらを活性化した
各種の活性炭の粉状、粒状のものを挙げることができ
る。その形状は真球に近いものから無定形のものまで、
その粒径も成形体の使用目的に応じて適宜選択すること
ができる。Powdered carbon materials include powdered and granular materials such as carbon black, coal, coal coke, pitch, pitch coke, graphite, charcoal, and coconut charcoal, and various activated carbon powders and granules activated from these. Can be mentioned. Its shape ranges from almost spherical to amorphous.
The particle size can also be appropriately selected according to the purpose of use of the molded article.
本発明に使用するカルボキシメチルセルロースアンモ
ニウム塩とは、カルボキシメチルセルロースのカルボキ
シメチル基の末端にアンモニウム基を結合させたもの
で、その化学構造の一例を下記に示す。The carboxymethylcellulose ammonium salt used in the present invention is a carboxymethylcellulose in which an ammonium group is bonded to the terminal of a carboxymethyl group, and an example of the chemical structure is shown below.
本発明の方法には市販の粉末状又は顆粒状のいずれの
ものでも使用し得る。その1%水溶液の25℃,60rpm B型
粘度計による粘度は1〜2000cpsのものが使用できる
が、好ましくは1〜500cpsの範囲のものを使用するのが
よい。その水溶液の炭素材料への含浸操作が容易であ
り、適度のバインダー機能を有するからである。 In the method of the present invention, any of commercially available powdery or granular forms can be used. The viscosity of the 1% aqueous solution measured by a B-type viscometer at 25 ° C. and 60 rpm can be from 1 to 2,000 cps, and preferably from 1 to 500 cps. This is because the operation of impregnating the aqueous solution with the carbon material is easy and has an appropriate binder function.
活性炭に含浸させるカルボキシメチルセルロースアン
モニウム塩水溶液の濃度は1〜20%の範囲、好ましくは
2〜5%の範囲である。1%以下では炭素材料の接着強
度が十分でなく、5%以上では活性炭への含浸操作が水
溶液の粘性のため、作業性が悪くなる。The concentration of the aqueous solution of carboxymethylcellulose ammonium salt impregnated in the activated carbon is in the range of 1 to 20%, preferably in the range of 2 to 5%. If it is 1% or less, the bonding strength of the carbon material is not sufficient.
炭素材料へのカルボキシメチルセルロースアンモニウ
ム塩水溶液の含浸並びに成形は各種の方法で行うことが
できる。例えば、(1)成形型内において、カルボキシ
メチルセルロースアンモニウム塩水溶液に炭素材料を懸
濁させた後吸引脱水して成形する方法、(2)成形型内
に充填した炭素材料にカルボキシメチルセルロースアン
モニウム塩水溶液を注加含浸後吸引脱水して成形する方
法、(3)(1)又は(2)の方法で吸引脱水の代わり
に遠心脱水して成形する方法、(4)炭素材料にカルボ
キシメチルセルロースアンモニウム塩水溶液を添加して
混練後押出し成形する方法、(5)或いは加圧成形する
方法などを挙げることができるが、これらに限定される
ものではない。The carbon material can be impregnated with the carboxymethylcellulose ammonium salt aqueous solution and formed by various methods. For example, (1) a method in which a carbon material is suspended in an aqueous solution of carboxymethylcellulose ammonium salt in a molding die and then molded by suction dehydration, and (2) an aqueous solution of carboxymethylcellulose ammonium salt is added to the carbon material filled in the molding die. (3) a method of forming by centrifugal dehydration instead of suction dehydration by the method of (1) or (2), and (4) an aqueous carboxymethylcellulose ammonium salt solution on a carbon material. Extrusion molding after addition and kneading, (5) or a method of pressure molding can be mentioned, but the method is not limited thereto.
カルボキシメチルセルロースアンモニウム塩水溶液を
含浸させ成形した炭素材料成形体は、次いで加熱する。
加熱温度は100〜300℃の範囲、好ましくは150〜250℃の
範囲である。これはカルボキシメチルセルロースアンモ
ニウム塩が熱分解により遊離カルボキシル基(−COOH)
を有するカルボキシメチルセルロースに変化する温度領
域に対応する。さらに次式に示す如く分解して生成した
遊離カルボキシル基 は隣のカルボキシメチルセルロース分子鎖中の水酸基
(−OH)とエステル結合することにより架橋構造を形成
して相互に強固に固着する。このアンモニウム塩の分解
により生成した遊離カルボキシル基を有するカルボキシ
メチルセルロース及び更にそのエステル化架橋体は水に
不溶となり、成形体に優れた耐水性を賦与することにな
る。The formed carbon material molded article impregnated with the aqueous solution of carboxymethyl cellulose ammonium salt is then heated.
The heating temperature is in the range of 100-300C, preferably in the range of 150-250C. This is because carboxymethyl cellulose ammonium salt is free carboxyl group (-COOH) by thermal decomposition
Corresponds to a temperature range that changes to carboxymethylcellulose having Free carboxyl group formed by decomposition as shown in the following formula Is ester-bonded to a hydroxyl group (—OH) in the adjacent carboxymethylcellulose molecular chain to form a crosslinked structure and firmly adhere to each other. The carboxymethylcellulose having a free carboxyl group formed by the decomposition of the ammonium salt and the esterified crosslinked product thereof become insoluble in water, and impart excellent water resistance to the molded article.
最適加熱時間は、過熱温度によって異なるが0.5〜3
時間の範囲であり、上記熱分解とエステル化架橋反応が
十分に起る適当な温度と時間を選べばよい。高温に加熱
するほど短時間でよいが、同時にカルボキシメチルセル
ロースの熱分解も起るので、180℃で2時間程度行うの
が最も好ましい。この加熱処理において、カルボキシメ
チルセルロースアンモニウム塩の熱分解によりアンモニ
アガスが発生するが、このガス発生は炭素成形体に均一
な通気性、通液性を賦与するのに役立つものである。The optimal heating time depends on the superheat temperature, but is 0.5 to 3
It is within a range of time, and an appropriate temperature and time at which the thermal decomposition and the esterification crosslinking reaction sufficiently occur may be selected. Heating to a high temperature requires a shorter time, but at the same time, thermal decomposition of carboxymethylcellulose occurs. Therefore, it is most preferable to perform the reaction at 180 ° C. for about 2 hours. In this heat treatment, ammonia gas is generated by thermal decomposition of carboxymethylcellulose ammonium salt, and this gas generation is useful for imparting uniform air permeability and liquid permeability to the carbon molded body.
本発明の炭素成形体、特に活性炭繊維成形体にあって
は、活性炭繊維単独のほかに、炭素繊維、ガラス繊維、
アルミナ繊維等の無機繊維、ポリアミド繊維、高融点ポ
リエチレン繊維、高融点ポリプロピレン繊維、高融点ポ
リアクリロニトリル繊維等の合成繊維、レーヨン等の半
合成繊維、パルプ繊維等を目的に応じて適当量混合して
製造することもできることは言うまでもない。In the carbon molded article of the present invention, particularly in the activated carbon fiber molded article, in addition to the activated carbon fiber alone, carbon fiber, glass fiber,
Mix appropriate amounts of inorganic fibers such as alumina fibers, polyamide fibers, high melting point polyethylene fibers, high melting point polypropylene fibers, synthetic fibers such as high melting point polyacrylonitrile fibers, semi-synthetic fibers such as rayon, and pulp fibers according to the purpose. Needless to say, it can be manufactured.
本発明の炭素成形体の製造法によれば、均質緻密で機
械的強度の大きい、耐水性の成形体が得られる。特に活
性炭繊維や炭素繊維の成形体では均一な通気性と通液性
を有するので、この成形体は浄水器フィルター、空気清
浄器やエアコンディショナーのフィルター、気相中の溶
剤回収吸着材などとして広く利用され得る。ADVANTAGE OF THE INVENTION According to the manufacturing method of the carbon molded object of this invention, a water-resistant molded object with high uniformity and high mechanical strength is obtained. In particular, since activated carbon fiber and carbon fiber molded products have uniform air permeability and liquid permeability, these molded products are widely used as filters for water purifiers, filters for air purifiers and air conditioners, and adsorbents for solvent recovery in the gas phase. Can be used.
以下に実施例により本発明をさらに詳しく説明する。 Hereinafter, the present invention will be described in more detail with reference to Examples.
実施例1 1%水溶液粘度(25℃,B型粘度計,60rpm)が10cps以
下の粉末状カルボキシメチルセルロースアンモニウム塩
(ダイセル化学工業(株)製、CMCダイセル〈アンモニ
ウム〉DN−LL)を水に溶解して5%の水溶液を調製し
た。Example 1 A powdery carboxymethyl cellulose ammonium salt (CMC Daicel <Ammonium> DN-LL, manufactured by Daicel Chemical Industries, Ltd.) having a 1% aqueous solution viscosity (25 ° C., B-type viscometer, 60 rpm) of 10 cps or less is dissolved in water. Thus, a 5% aqueous solution was prepared.
このカルボキシメチルセルロースアンモニウム塩水溶
液1000mlを業務用カッターミキサーにとり、この中に綿
状活性炭繊維(繊維径10〜15μm、比表面積700〜2500m
2/g、ピッチ系)100gを投入し、業務用カッターミキサ
ーを攪拌して綿状活性炭繊維を繊維長1〜5mmとなるよ
う叩解しつつ、カルボキシメチルセルロースアンモニウ
ム塩水溶液中に分散懸濁させ、均一なスラリーを得た。1000 ml of this carboxymethylcellulose ammonium salt aqueous solution is placed in a commercial cutter mixer, into which flocculent activated carbon fiber (fiber diameter 10-15 μm, specific surface area 700-2500 m
100 g of 2 / g, pitch type), disperse and suspend in a carboxymethylcellulose ammonium salt aqueous solution while stirring the flocculent activated carbon fiber to a fiber length of 1 to 5 mm by stirring a commercial cutter mixer A good slurry was obtained.
次いで、このスラリーを底部に吸引脱水用の多孔板を
備えた中空円筒状の成形用型(外径30mm、内径18mm、中
空部系14mm、高さ300mm)に注入した後、底部より吸引
脱水して成形した。成形された浸潤状態の中空円筒体を
型から取り出し100℃で2時間乾燥後、180℃で2時間加
熱した。Next, the slurry was poured into a hollow cylindrical molding die (outside diameter 30 mm, inside diameter 18 mm, hollow section system 14 mm, height 300 mm) equipped with a perforated plate for suction dehydration at the bottom, and then suction dewatered from the bottom. Molded. The formed infiltrated hollow cylindrical body was taken out of the mold, dried at 100 ° C. for 2 hours, and heated at 180 ° C. for 2 hours.
得られた活性炭繊維成形体の寸法は、内径18.7mm、外
径29.9mm、長さ107.5mmであり、その物性は嵩密度0.234
g/cc、圧壊強度24.0kg/cm2であった。The dimensions of the obtained activated carbon fiber molded body were 18.7 mm in inner diameter, 29.9 mm in outer diameter, and 107.5 mm in length, and its physical properties were bulk density of 0.234.
g / cc and crushing strength 24.0 kg / cm 2 .
実施例2 カルボキシメチルセルロースアンモニウム塩水溶液の
濃度を3%とする以外は、実施例1と同様の方法で中空
円筒状の活性炭繊維成形体を製造した。Example 2 A hollow cylindrical activated carbon fiber molded body was produced in the same manner as in Example 1, except that the concentration of the carboxymethylcellulose ammonium salt aqueous solution was changed to 3%.
得られた成形体の寸法は、内径18.3mm、外径29.5mm、
長さ92.1mm、嵩密度0.214g/cc、圧壊強度21.1kg/cm2で
あった。The dimensions of the obtained molded body are 18.3 mm in inner diameter, 29.5 mm in outer diameter,
The length was 92.1 mm, the bulk density was 0.214 g / cc, and the crushing strength was 21.1 kg / cm 2 .
実施例3 1%水溶液粘度(25℃,B型粘度計の,60rpm)が10cps
以下の粉末状カルボキシメチルセルロースアンモニウム
塩(ダイセル化学工業(株)製、CMCダイセル〈アンモ
ニウム〉DN−LL)を水に溶解して3%の水溶液を調製し
た。Example 3 The viscosity of a 1% aqueous solution (25 ° C., B-type viscometer, 60 rpm) was 10 cps.
The following powdery carboxymethylcellulose ammonium salt (CMC Daicel <ammonium> DN-LL, manufactured by Daicel Chemical Industries, Ltd.) was dissolved in water to prepare a 3% aqueous solution.
このカルボキシメチルセルロースアンモニウム塩水溶
液1000mlを業務用カッターミキサーにとり、この中に綿
状活性炭繊維(繊維径10〜15μm、比表面積700〜2500m
2/g、ピッチ系)50gと綿状炭素繊維(繊維径13μm、引
張り強度80kg/mm2、比重1.65、ピッチ系)50gとを投入
し、業務用カッターミキサーを攪拌して繊維長が1〜5m
mとなるよう叩解しつつ、カルボキシメチルセルロース
アンモニウム塩水溶液中に分散懸濁させ、均一なスラリ
ーを得た。1000 ml of this carboxymethylcellulose ammonium salt aqueous solution is placed in a commercial cutter mixer, into which flocculent activated carbon fiber (fiber diameter 10-15 μm, specific surface area 700-2500 m
50 g of 2 / g, pitch type) and 50 g of flocculent carbon fiber (fiber diameter: 13 μm, tensile strength: 80 kg / mm 2 , specific gravity: 1.65, pitch type) 5m
While beating to obtain m, the mixture was dispersed and suspended in an aqueous solution of carboxymethylcellulose ammonium salt to obtain a uniform slurry.
次いで、このスラリーを底部に吸引脱水用の多孔板を
備えた中空円筒状の成形用型(外径46mm、内径16mm、中
空部径12mm、高さ300mm)に注入した後、底部より吸引
脱水して成形した。成形した湿潤状態の中空円筒体を型
から取り出し、100℃で2時間乾燥後、180℃で2時間加
熱焼結した。Next, the slurry is poured into a hollow cylindrical molding die (outer diameter 46 mm, inner diameter 16 mm, hollow part diameter 12 mm, height 300 mm) provided with a perforated plate for suction dehydration at the bottom, and then suction dewatered from the bottom. Molded. The molded wet hollow cylindrical body was taken out of the mold, dried at 100 ° C. for 2 hours, and heated and sintered at 180 ° C. for 2 hours.
得られた炭素繊維配合活性炭繊維成形体の寸法は、内
径16.0mm、外径45.2mm、嵩密度0.248g/cc、圧壊強度32k
g、6.8kg/cm2、通液抵抗は4l/分の流量で、0.08kg/cm2
であった。The dimensions of the obtained carbon fiber-containing activated carbon fiber molded body were 16.0 mm in inner diameter, 45.2 mm in outer diameter, 0.248 g / cc in bulk density, and 32 k in crushing strength.
g, 6.8 kg / cm 2 , flow resistance is 4 l / min, 0.08 kg / cm 2
Met.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C01B 31/02──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) C01B 31/02
Claims (1)
ンモニウム塩の水溶液を含浸させ成形した後、100〜300
℃で3〜0.5時間加熱することによりカルボキシメチル
セルロースアンモニウム塩を熱分解してカルボキシメチ
ルセルロースに変化させ、さらにカルボキシメチルセル
ロース分子間で架橋反応させることを特徴とする炭素成
形体の製造方法。1. A carbon material which is impregnated with an aqueous solution of carboxymethylcellulose ammonium salt and molded, and then 100-300
A method for producing a carbon molded body, wherein a carboxymethylcellulose ammonium salt is thermally decomposed into carboxymethylcellulose by heating at a temperature of 3 to 0.5 hours for 3 to 0.5 hours, and a cross-linking reaction is performed between carboxymethylcellulose molecules.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1230780A JP2862909B2 (en) | 1989-09-06 | 1989-09-06 | Method for producing carbon molded body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1230780A JP2862909B2 (en) | 1989-09-06 | 1989-09-06 | Method for producing carbon molded body |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0393615A JPH0393615A (en) | 1991-04-18 |
JP2862909B2 true JP2862909B2 (en) | 1999-03-03 |
Family
ID=16913149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1230780A Expired - Lifetime JP2862909B2 (en) | 1989-09-06 | 1989-09-06 | Method for producing carbon molded body |
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JP (1) | JP2862909B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1272241C (en) * | 2001-04-11 | 2006-08-30 | 米德韦斯特瓦科公司 | Shaped activated carbon |
US6696384B2 (en) | 2001-04-11 | 2004-02-24 | Meadwestvaco Corporation | Method of making shaped activated carbon |
US6573212B2 (en) | 2001-04-11 | 2003-06-03 | Meadwestvaco Corporation | Method of making shaped activated carbon |
JP2015181989A (en) * | 2014-03-20 | 2015-10-22 | 日東電工株式会社 | Method for manufacturing carboxymethyl cellulose composite separation membrane |
JP2015181990A (en) * | 2014-03-20 | 2015-10-22 | 日東電工株式会社 | Carboxymethyl cellulose composite separation membrane and film separation method using the same |
Family Cites Families (1)
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JPH0795324B2 (en) * | 1984-08-22 | 1995-10-11 | 株式会社日立製作所 | Search method and device |
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1989
- 1989-09-06 JP JP1230780A patent/JP2862909B2/en not_active Expired - Lifetime
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JPH0393615A (en) | 1991-04-18 |
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