JPH0543346A - Production of active carbon structure - Google Patents

Production of active carbon structure

Info

Publication number
JPH0543346A
JPH0543346A JP3196888A JP19688891A JPH0543346A JP H0543346 A JPH0543346 A JP H0543346A JP 3196888 A JP3196888 A JP 3196888A JP 19688891 A JP19688891 A JP 19688891A JP H0543346 A JPH0543346 A JP H0543346A
Authority
JP
Japan
Prior art keywords
carbon
activated carbon
activation
gas
activating
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
JP3196888A
Other languages
Japanese (ja)
Inventor
Jiro Fujimura
次郎 藤村
Shinro Katsura
真郎 桂
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP3196888A priority Critical patent/JPH0543346A/en
Publication of JPH0543346A publication Critical patent/JPH0543346A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/008Bodies obtained by assembling separate elements having such a configuration that the final product is porous or by spirally winding one or more corrugated sheets

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

(57)【要約】 【目的】 ブロック状活性炭の賦活時の問題である、割
れを発生せず、迅速かつ均一に賦活する方法を提供す
る。 【構成】 残炭率の高い重合体を炭化、賦活して活性炭
構造物を製造する方法において、賦活する際、被賦活物
を、炭素を主成分とする層状物で包み込んで賦活するこ
とを特徴とする活性炭構造物の製造方法である。
(57) [Abstract] [Purpose] To provide a method for activating block-type activated carbon quickly and uniformly without causing cracking, which is a problem during activation. [Structure] In a method for producing an activated carbon structure by carbonizing and activating a polymer having a high residual carbon ratio, when activating, a substance to be activated is wrapped with a layered material containing carbon as a main component to activate. Is a method for manufacturing an activated carbon structure.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は活性炭構造物の製造方法
に関する。更に詳しくは本発明は反り、割れの少ない活
性炭構造物の製造方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing an activated carbon structure. More specifically, the present invention relates to a method for producing an activated carbon structure with less warpage and cracking.

【0002】[0002]

【従来の技術】活性炭は排水処理や脱臭処理等の用途に
広く使用されている。更に最近では電気二重層コンデン
サの電極として使用されはじめている。この用途に使用
される活性炭は、コンデンサの性能向上、特に高静電容
量と低内部抵抗の2つの性能向上の要求を満たすため、
高密度、ブロック状、かつ電解液の含浸性の良いことが
要求されている。
2. Description of the Related Art Activated carbon is widely used for applications such as wastewater treatment and deodorization treatment. More recently, they have begun to be used as electrodes of electric double layer capacitors. The activated carbon used for this purpose satisfies the requirements for improved performance of capacitors, especially high performance and low internal resistance.
It is required to have high density, block shape, and good impregnation property with an electrolytic solution.

【0003】一般に活性炭を製造する方法としては、石
炭または、椰子殻等の原料を粉砕して、粒状体、あるい
は粉状体とし、必要に応じて更に造粒してペレット状と
した後、炭化、賦活する方法が採られる。このような粉
体では、ロータリーキルンで原料を回転しながら賦活す
る方法等により、品質の安定した製品を得ることができ
る。しかし、ブロック状活性炭の製造はこの様な方法を
とることはできない。
Generally, as a method for producing activated carbon, raw materials such as coal or coconut shells are crushed into granules or powder, and if necessary, further granulated into pellets and then carbonized. , The method of activation is adopted. With such a powder, a product of stable quality can be obtained by a method of activating the raw material while rotating it with a rotary kiln. However, the block-like activated carbon cannot be manufactured by such a method.

【0004】[0004]

【発明が解決しようとしている問題点】本出願人等は先
にフェノール樹脂発泡体を原料とし、それを炭化、賦活
することにより活性炭構造物を製造する方法を提案して
いる。この様な構造物の場合、粉体の賦活と異なり(1)
賦活が構造物の部位により不均一になる、(2) 反り、割
れを生じ易い、(3)賦活速度が遅い という問題点があ
る。(3) の点を改良する方法としては、賦活温度を高く
する、あるいは水蒸気濃度を上げる等の手段が考えられ
るが、これらの方法では、被賦活物の割れや反りを招い
てしまう。
[Problems to be Solved by the Invention] The present applicant has previously proposed a method for producing an activated carbon structure by using a phenol resin foam as a raw material and carbonizing and activating it. In the case of such a structure, unlike the activation of powder (1)
There are problems that activation becomes uneven depending on the site of the structure, (2) warpage and cracking are likely to occur, and (3) activation speed is slow. As a method for improving the point (3), it is conceivable to increase the activation temperature or increase the water vapor concentration, but these methods lead to cracking or warpage of the activated material.

【0005】本発明者らはブロック状活性炭の賦活時の
問題である、割れを発生せず、迅速かつ均一に賦活する
方法を見出すべく鋭意検討した結果、本発明に到達し
た。
The present inventors have arrived at the present invention as a result of extensive studies to find a method for activating block-like activated carbon rapidly and uniformly without cracking, which is a problem during activation.

【0006】[0006]

【課題を解決するための手段】すなわち、本発明は残炭
率の高い重合体を炭化、賦活して活性炭構造物を製造す
る方法において、賦活する際、被賦活物を、炭素を主成
分とする層状物で包み込んで賦活することを特徴とする
活性炭構造物の製造方法である。
Means for Solving the Problems That is, the present invention is a method for producing an activated carbon structure by carbonizing and activating a polymer having a high residual carbon ratio. The method for producing an activated carbon structure is characterized in that the activated carbon structure is encased in a layered product and activated.

【0007】本発明を更に詳しく説明する。本発明にお
ける残炭率の高い重合体とは、例えば、フェノール樹
脂、フラン樹脂、ポリ塩化ビニル樹脂等不活性雰囲気下
で500℃以上の高温で処理した際、炭素として残存す
る割合が元の重合体の20%以上ある重合体をいう。本
発明ではそのうちでもフェノール樹脂が好ましく、特に
レゾール型フェノール樹脂を好ましく使用できる。この
ようなレゾール型フェノール樹脂を用いた樹脂組成物と
しては、例えば、レゾール型フェノール樹脂と蒸発型発
泡剤、硬化剤とを混合後、発泡、硬化して製造する方
法、あるいは、レゾール型フェノール樹脂と、残炭率の
低い、液状および/または、粉末状物とを混合、硬化す
ることにより得ることができる。
The present invention will be described in more detail. The polymer having a high residual carbon ratio in the present invention is, for example, a phenol resin, a furan resin, a polyvinyl chloride resin, etc. When treated at a high temperature of 500 ° C. or higher in an inert atmosphere, the ratio of carbon residue remains as the original weight. It refers to a polymer that is 20% or more of the coalescence. In the present invention, a phenol resin is preferable among them, and a resol type phenol resin can be particularly preferably used. As a resin composition using such a resol-type phenol resin, for example, a method of mixing the resol-type phenol resin with an evaporative foaming agent, a curing agent, followed by foaming and curing, or a resol-type phenol resin And a liquid and / or powdery material having a low residual carbon rate and mixed and cured.

【0008】本発明では樹脂組成物を炭化、賦活して活
性炭構造物を製造する。この際、被賦活物を、炭素を主
成分とする層状物で包み込んで賦活を行う。
In the present invention, the resin composition is carbonized and activated to produce an activated carbon structure. At this time, the material to be activated is wrapped with a layered material containing carbon as a main component for activation.

【0009】炭化は不活性雰囲気下で行う。非酸化性雰
囲気とは、例えば、Arガス、Heガス、N2 ガス、ハ
ロゲンガス、アンモニアガス、COガス、水素ガス、あ
るいはこれらの混合ガス、水性ガス等をいう。炭化のた
めの温度は、好ましくは、500℃〜1200℃、特に
600〜900℃の範囲が好ましい。
Carbonization is carried out in an inert atmosphere. The non-oxidizing atmosphere means, for example, Ar gas, He gas, N2 gas, halogen gas, ammonia gas, CO gas, hydrogen gas, a mixed gas thereof, a water gas or the like. The temperature for carbonization is preferably in the range of 500 ° C to 1200 ° C, particularly 600 to 900 ° C.

【0010】以上のようにして得られた炭素多孔体は、
更に賦活処理を施して活性化する。賦活工程は、炭化工
程に連続していてもよいし、炭化工程と別個の工程とし
てもよい。炭素多孔体の賦活は炭素多孔体を酸化性ガ
ス、または酸化性ガスと不活性ガスとの混合気体の雰囲
気下で加熱して行われる。
The carbon porous body obtained as described above is
Further, activation treatment is applied to activate. The activation step may be continuous with the carbonization step or may be a step separate from the carbonization step. Activation of the carbon porous body is performed by heating the carbon porous body in an atmosphere of an oxidizing gas or a mixed gas of an oxidizing gas and an inert gas.

【0011】重合体を賦活するための酸化性ガスとして
は、公知の酸化性ガス、例えば、空気、水蒸気、炭酸ガ
ス、水性ガス等を採用することができる。重合体を炭
化、賦活して、活性炭を製造する際の温度としては、賦
活ガスの種類、濃度にもよるが、通常は600ないし1
200℃、好ましくは750ないし1000℃の範囲が
採用される。
As the oxidizing gas for activating the polymer, known oxidizing gases such as air, water vapor, carbon dioxide gas, water gas and the like can be adopted. The temperature at which activated carbon is produced by carbonizing and activating the polymer is usually 600 to 1 although it depends on the type and concentration of the activating gas.
A range of 200 ° C., preferably 750 to 1000 ° C. is adopted.

【0012】本発明における炭素を主成分とする層状物
とは、例えば、黒鉛板、炭素繊維の織布、不織布、さら
にそれらに樹脂を含浸した後再度炭化することにより製
造される、いわゆるC/Cコンポジット、あるいは炭素
繊維を紙状にしたものからハニカムを形成するなどの方
法で厚みを持たせたもの、あるいは、先に説明したよう
な残炭率の高い重合体の発泡体を炭化して得られる炭素
多孔体等を使用出来る。これらのうちではガス透過性が
あり、かつ表面積が大きい炭素繊維不織布、C/Cコン
ポジットが好ましい。
The layered product containing carbon as a main component in the present invention is, for example, a graphite plate, a woven or non-woven fabric of carbon fibers, or so-called C /, which is produced by impregnating them with a resin and then carbonizing them again. C composite, or a carbon fiber made into a paper shape to have a thickness by a method such as forming a honeycomb, or a polymer foam having a high residual carbon ratio as described above is carbonized. The obtained carbon porous material or the like can be used. Among these, carbon fiber non-woven fabric and C / C composite having gas permeability and large surface area are preferable.

【0013】層状物の必要厚さとしては、賦活性ガスの
濃度、風速にも依るが、好ましくは、1ないし50mm
の範囲にある。反り防止を目的とする場合は、炭素層状
物は剛性のあるセラミック発泡体と併用するとより好ま
しい。
The required thickness of the layered material depends on the concentration of the activating gas and the wind speed, but is preferably 1 to 50 mm.
Is in the range. For the purpose of preventing warpage, the carbon layered material is more preferably used together with a rigid ceramic foam.

【0014】被賦活物を包み込む方法としては、炭素層
状物からなる箱状物を作製し、被賦活物ををその中にお
く方法、額縁状物を作製し、被賦活物をそれで挟み込む
方法等が採用できる。層状物の役割は、酸化性ガスを制
限された速度で透過させる働きをする。また、明確では
ないが、本発明の端部の割れが少なく、かつ全体の賦活
速度が向上するという効果からみて、炭素層状物は酸化
性ガスと反応して、系内を炭酸ガスにし、この炭酸ガス
と重合体板状物との局部的な暴走反応をやわらげ、かつ
全体には賦活反応を促進する働きをしていると推定され
る。
As a method for wrapping the activator, a box-shaped product made of a carbon layered product is prepared, the activator is placed therein, a frame-shaped product is prepared, and the activator is sandwiched between them. Can be adopted. The role of the layered material serves to allow the oxidizing gas to permeate at a limited rate. Further, although not clear, the carbon layered material reacts with the oxidizing gas to form carbon dioxide gas in the system in view of the effect that the number of cracks at the end of the present invention is small and the activation rate of the whole is improved. It is presumed that it acts to soften the local runaway reaction between the carbon dioxide gas and the polymer plate-like material and to promote the activation reaction as a whole.

【0015】[0015]

【実施例】【Example】

実施例1 レゾール型フェノール樹脂100重量部、硬化剤として
パラトルエンスルホン酸10重量部、及び発泡剤として
フロン123b1.5重量部とを高速ミキサーで十分に
攪拌、混合した。得られた混合物を木型内に流し込み、
蓋をした後、80℃のエアーオーブン内に入れて30分
間加熱して発泡させ発泡体硬化物ブロックを得た。この
ブロックから、外径寸法が縦10cm、横10cm、厚
さ3mmの板を切削した。
Example 1 100 parts by weight of a resol type phenol resin, 10 parts by weight of paratoluene sulfonic acid as a curing agent, and 1.5 parts by weight of Freon 123b as a foaming agent were sufficiently stirred and mixed with a high speed mixer. Pour the resulting mixture into a wooden mold,
After covering with a lid, the product was placed in an air oven at 80 ° C. and heated for 30 minutes for foaming to obtain a foam cured product block. From this block, a plate having an outer diameter of 10 cm in length, 10 cm in width, and 3 mm in thickness was cut.

【0016】この板8枚をそれぞれ内径が縦10.5c
m、横10.5cm、巾4mm厚さが5mmの炭素繊維
不織布(空隙率70%)製の額縁状箱に入れ、更にその
箱8個ををマッフル炉の中央部に入れて、窒素雰囲気
下、昇温速度60℃/時間で温度900℃まで昇温させ
た後、温度を保ちながらN2 ガス/水蒸気の混合モル比
が0.8/0.2である混合ガスを流して3時間処理し
た。
Each of the eight plates has an inner diameter of 10.5c in the vertical direction.
m, width 10.5 cm, width 4 mm, thickness 5 mm, put in a frame box made of carbon fiber non-woven fabric (porosity 70%), and then put 8 of these boxes in the center of the muffle furnace, and under nitrogen atmosphere. After raising the temperature to 900 ° C. at a temperature rising rate of 60 ° C./hour, a mixed gas having a mixed molar ratio of N 2 gas / steam of 0.8 / 0.2 was flowed while maintaining the temperature for 3 hours. ..

【0017】以上の方法で活性炭素多孔体を得た。この
板の反り、割れの有無、中央部と端部のベンゼン吸着度
を測定した。なお、ベンゼン吸着度は熱天秤を用い、試
料約100mg、25℃飽和蒸気下の吸着による重量増加
量を試料の重量で割った値(%)として求めた。結果を
表.1に示す。
An activated carbon porous material was obtained by the above method. The warp of this plate, the presence or absence of cracks, and the benzene adsorption degree at the central portion and the end portion were measured. The benzene adsorption degree was determined by using a thermobalance as a value (%) obtained by dividing the weight increase due to adsorption under a saturated vapor of 25 ° C. at about 100 mg of the sample by the weight of the sample. The results are shown in the table. Shown in 1.

【0018】実施例2 実施例1において賦活温度と賦活時間をそれぞれ850
℃、および5時間に変える以外は実施例1と同様に行っ
た。結果を表.1に示す。
Example 2 In Example 1, the activation temperature and activation time were 850 and 850, respectively.
The same procedure as in Example 1 was repeated except that the temperature was changed to 5 ° C. and the time was changed to 5 hours. The results are shown in the table. Shown in 1.

【0019】実施例3 実施例2において用いた炭素繊維不織布の代わりにC/
Cコンポジットボード(空隙率75%)の箱を用いる以
外は、実施例2と同様に行った。結果を表.1に示す。
Example 3 Instead of the carbon fiber nonwoven fabric used in Example 2, C /
Example 2 was performed in the same manner as in Example 2 except that a C composite board box (porosity 75%) was used. The results are shown in the table. Shown in 1.

【0020】比較例1 実施例1において用いた炭素繊維不織布の箱を用いない
で発泡体硬化物の板をそのままマッフル炉に入れて賦活
する以外は、実施例1と同様に行った。結果を表.1に
示す。
Comparative Example 1 The procedure of Example 1 was repeated, except that the carbon fiber nonwoven fabric box used in Example 1 was not used and the plate of the foamed cured product was placed in a muffle furnace for activation. The results are shown in the table. Shown in 1.

【0021】比較例2 比較例1において賦活温度と賦活時間をそれぞれ850
℃、および5時間に変える以外は比較例1と同様に行っ
た。結果を表.1に示す。
COMPARATIVE EXAMPLE 2 In Comparative Example 1, the activation temperature and activation time were 850 and 850, respectively.
The same procedure as in Comparative Example 1 was repeated except that the temperature was changed to 5 ° C. and the time was changed to 5 hours. The results are shown in the table. Shown in 1.

【0022】比較例3 実施例1において炭素繊維不織布の代わりにセラミック
繊維ボードの箱を用いる以外は、実施例1と同様に行っ
た。結果を表.1に示す。
Comparative Example 3 The procedure of Example 1 was repeated except that a ceramic fiber board box was used instead of the carbon fiber nonwoven fabric in Example 1. The results are shown in the table. Shown in 1.

【0023】比較例4 実施例1において炭素繊維不織布の代わりに耐熱レンガ
の箱を用いる以外は、実施例1と同様に行った。結果を
表.1に示す。
Comparative Example 4 The procedure of Example 1 was repeated, except that a heat-resistant brick box was used instead of the carbon fiber nonwoven fabric. The results are shown in the table. Shown in 1.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【発明の効果】本発明の炭素を主成分とする層状物を用
いて活性炭構造物を製造する方法によれば、従来の層状
物を用いない方法に比べて賦活時の割れが少なく、収率
が向上する。また、賦活速度が向上する。更に構造物全
体の賦活度がより均一になり、構造体全体の吸着性能が
向上する。この結果、特に電気二重層コンデンサの電
極、脱臭フィルターとして有用な高密度、高吸着性能、
かつ液含浸性の優れた活性炭構造物を効率よく製造する
ことができる。
EFFECTS OF THE INVENTION According to the method for producing an activated carbon structure using the layered product containing carbon as a main component of the present invention, cracking during activation is less than that in the conventional method not using the layered product, and the yield is higher. Is improved. In addition, the activation speed is improved. Furthermore, the activation rate of the entire structure becomes more uniform, and the adsorption performance of the entire structure improves. As a result, high density, high adsorption performance, especially useful as electrodes for electric double layer capacitors and deodorizing filters,
In addition, it is possible to efficiently manufacture an activated carbon structure having an excellent liquid impregnation property.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 残炭率の高い重合体を炭化、賦活して活
性炭構造物を製造する方法において、賦活する際に被賦
活物を、炭素を主成分とする層状物で包み込んで賦活す
ることを特徴とする活性炭構造物の製造方法。
1. A method for producing an activated carbon structure by carbonizing and activating a polymer having a high residual carbon rate, in which activation is performed by encapsulating a substance to be activated with a layered material containing carbon as a main component. A method for producing an activated carbon structure, comprising:
【請求項2】 炭素を主成分とする層状物が炭素繊維の
織布、もしくは不織布であることを特徴とする特許請求
の範囲第1項記載の製造方法。
2. The production method according to claim 1, wherein the layered product containing carbon as a main component is a woven or non-woven fabric of carbon fibers.
JP3196888A 1991-08-06 1991-08-06 Production of active carbon structure Pending JPH0543346A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3196888A JPH0543346A (en) 1991-08-06 1991-08-06 Production of active carbon structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3196888A JPH0543346A (en) 1991-08-06 1991-08-06 Production of active carbon structure

Publications (1)

Publication Number Publication Date
JPH0543346A true JPH0543346A (en) 1993-02-23

Family

ID=16365323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3196888A Pending JPH0543346A (en) 1991-08-06 1991-08-06 Production of active carbon structure

Country Status (1)

Country Link
JP (1) JPH0543346A (en)

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