JPH05147913A - Production of activated carbon made of spherical fiber lump - Google Patents

Production of activated carbon made of spherical fiber lump

Info

Publication number
JPH05147913A
JPH05147913A JP3319319A JP31931991A JPH05147913A JP H05147913 A JPH05147913 A JP H05147913A JP 3319319 A JP3319319 A JP 3319319A JP 31931991 A JP31931991 A JP 31931991A JP H05147913 A JPH05147913 A JP H05147913A
Authority
JP
Japan
Prior art keywords
pitch
binder
fiber
spherical
activated carbon
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
JP3319319A
Other languages
Japanese (ja)
Inventor
Minoru Yoshida
稔 吉田
Seiji Hanatani
誠二 花谷
Masayuki Sumi
誠之 角
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.)
CHIKIYUU KANKYO SANGYO GIJUTSU
CHIKIYUU KANKYO SANGYO GIJUTSU KENKYU KIKO
JFE Steel Corp
Original Assignee
CHIKIYUU KANKYO SANGYO GIJUTSU
CHIKIYUU KANKYO SANGYO GIJUTSU KENKYU KIKO
Kawasaki Steel Corp
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 CHIKIYUU KANKYO SANGYO GIJUTSU, CHIKIYUU KANKYO SANGYO GIJUTSU KENKYU KIKO, Kawasaki Steel Corp filed Critical CHIKIYUU KANKYO SANGYO GIJUTSU
Priority to JP3319319A priority Critical patent/JPH05147913A/en
Publication of JPH05147913A publication Critical patent/JPH05147913A/en
Pending legal-status Critical Current

Links

Landscapes

  • Carbon And Carbon Compounds (AREA)
  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To improve a binder to be used for producing activated carbon made of a spherical fiber lump by using tar pitch as a raw material. CONSTITUTION:Pitch fiber obtained by melt spinning is made infusible and the obtained infusible fiber is cut or crashed and sphered. In this stage, coal- based and/or petroleum-based fine powdery pitch especially the same having 5-20mum average particle diameter is used as a binder. This fine powdery pitch is mixed with the infusible fiber. Water is added to the mixture containing fine powdery pitch at 5-30wt.% and the obtained mixture is sphered. Thereby productivity is improved in comparison with a conventional method wherein a resin solution is used as the binder and with a method for using suspension in which fine powdery pitch is dispersed in water. Besides, activated carbon made of a spherical fiber lump having stable quality is produced industrially and favorably at low cost.

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、タールピッチを原料と
して球状繊維塊活性炭を製造する方法、特に分離、除
去、精製、回収、消臭、脱臭、触媒などの分野に用いら
れる球状繊維塊活性炭の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a spherical fiber lump activated carbon from tar pitch as a raw material, particularly a spherical fiber lump activated carbon used in the fields of separation, removal, purification, recovery, deodorization, deodorization, catalysts and the like. The present invention relates to a manufacturing method of.

【0002】[0002]

【従来の技術】活性炭素繊維は、吸着速度が高い上に単
位重量当りの比表面積も大きいため、フィルターなどと
して気相吸着および液相吸着に使用されている。しか
し、活性炭素繊維は特開昭61-132629 号公報、特開昭63
-53294号公報などに見られる様にフェルト状あるいはマ
ット状であるため、重量の割に嵩が高く、取り扱いがむ
ずかしく、また吸着塔等に充填した場合に圧力損失が増
加するといった問題点がある。そこで、従来、フェルト
状活性炭素繊維を樹脂で成形する方法、抄紙法で成形す
る方法、活性炭素繊維を樹脂で固め直径10〜20mmの球状
にして所望の物質を吸着させる方法などがとられてい
る。さらに、上述の問題点を解決するために、特開平2
-38374号公報に、屑状の不融化ピッチ系繊維と炭素含有
樹脂を含む液とを混合し、これを押出造粒して塊状物を
得、これを賦活して活性炭素繊維塊を得る方法が開示さ
れているが、球状化の手法は明示されていない。
2. Description of the Related Art Activated carbon fibers have a high adsorption rate and a large specific surface area per unit weight, and are therefore used as filters and the like for gas phase adsorption and liquid phase adsorption. However, activated carbon fibers are disclosed in JP-A-61-132629 and JP-A-63.
As it is felt-like or mat-like as seen in -53294 publication, there are problems that it is bulky relative to its weight, is difficult to handle, and increases pressure loss when it is packed in an adsorption tower, etc. .. Therefore, conventionally, a method of molding a felt-like activated carbon fiber with a resin, a method of molding with a papermaking method, a method of adsorbing a desired substance into a spherical shape having a diameter of 10 to 20 mm by solidifying the activated carbon fiber with a resin, etc. have been adopted. There is. Furthermore, in order to solve the above-mentioned problems, Japanese Patent Application Laid-Open No. Hei 2
-38374 publication, a method of obtaining a block of infusible pitch-based fibers and a liquid containing a carbon-containing resin, and extruding and granulating the mixture to obtain a lump, and activating this to obtain an activated carbon fiber lump. However, the method of spheroidizing is not specified.

【0003】また、上記特開平2-38374号公報に記載さ
れている塊状物の場合について説明すれば、製造工程が
複雑になるほか、塊状物を得るために炭素繊維を圧縮す
ると共に切断又は分断する必要があるので、比較的脆弱
な原料繊維は粉末化又は短繊維化してしまう。また、バ
インダーとして使用する炭素材であるフェノール樹脂、
エポキシ樹脂などは高価であり、コストに与える影響は
小さくない。本発明者等は、先にピッチ繊維をバインダ
ーを含む媒体で解砕造粒あるいは押出造粒して得た造粒
物に転動処理を施し、次いで乾燥、不融化、炭化、賦活
処理を施して得られる球状繊維塊活性炭およびその製造
方法を提供した(特願平2-129247 号公報) 。この球状
繊維塊活性炭は吸着能力が高く、吸脱着速度が速く、取
り扱い性および形状維持性に優れ、流体通過抵抗が極め
て低いという利点を有するが、この製造方法も工程が複
雑であり、改良の余地が残されている。
Explaining the case of the lump described in the above-mentioned Japanese Patent Laid-Open No. 2-38374, the manufacturing process becomes complicated, and the carbon fiber is compressed and cut or divided to obtain the lump. Therefore, the relatively fragile raw material fiber is pulverized or shortened. Also, phenolic resin, which is a carbon material used as a binder,
Epoxy resin and the like are expensive, and their cost impact is not small. The present inventors have previously subjected the granulated material obtained by crushing granulation or extrusion granulation of the pitch fiber in a medium containing a binder to rolling treatment, and then subjecting it to drying, infusibilization, carbonization, and activation treatment. A spherical fiber lump activated carbon obtained as described above and a method for producing the same were provided (Japanese Patent Application No. 2-129247). This spherical fibrous lump activated carbon has the advantages of high adsorption capacity, fast adsorption / desorption rate, excellent handleability and shape retention, and extremely low fluid passage resistance, but this manufacturing method also has complicated steps and There is room left.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上述の問題
点を解決し、かつ強度の大きな球状繊維塊活性炭を簡単
な工程で製造することができる方法を提供することを目
的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above problems and to provide a method capable of producing a spherical fiber lump activated carbon having a high strength in a simple process.

【0005】[0005]

【課題を解決するための手段】本発明においては、複数
本の活性炭素繊維をピッチバインダーと混合した後、水
を添加して球状化することにより、上述の問題を解決で
きることを見い出した。すなわち、本発明は、タールピ
ッチを原料として紡糸用ピッチを調製し、該ピッチを溶
融紡糸によりピッチ繊維とし、これを酸化性雰囲気中で
不融化処理し、ついで複数本の該不融化繊維をバインダ
ーの存在下に球状化し、生成した球状炭素繊維を賦活処
理することにより球状繊維塊活性炭を製造するにあた
り、球状化の際に前記バインダーとしてピッチ微粉末を
使用し、前記不融化繊維に前記ピッチ微粉末を混合し、
生成した混合物に水を添加して球状化を行うことを特徴
とする球状繊維塊活性炭の製造方法を提供する。
In the present invention, it has been found that the above problems can be solved by mixing a plurality of activated carbon fibers with a pitch binder and then adding water to make the particles spherical. That is, the present invention prepares a pitch for spinning using tar pitch as a raw material, melt-spins the pitch into pitch fibers, infusibilizes the same in an oxidizing atmosphere, and then binds a plurality of the infusible fibers with a binder. Spheroidized in the presence of, to produce a spherical fiber lump activated carbon by activating the generated spherical carbon fiber, using fine pitch powder as the binder during spheroidization, the fine pitch powder in the infusible fiber Mix the powders,
Provided is a method for producing a spherical fiber lump activated carbon, which comprises adding water to the produced mixture to effect spheroidization.

【0006】本発明方法においては、ピッチ繊維を酸化
性雰囲気中で不融化処理し、ついで複数本の不融化繊維
にバインダーとして石炭系および/又は石油系のピッチ
微粉末を添加して混合する。なお、ここに乾燥状態のピ
ッチ微粉末とは、水無添加のピッチ微粉末を意味する。
次いで、この混合物に水を添加しながら、例えば、転動
造粒機によって球状化し、生成した球状物を乾燥し、硬
化させた後に賦活処理する。ピッチを平均粒径5〜20μ
m に微粉砕し、該微粉末を乾燥状態で原料である不融化
繊維と混合し、生成する混合物中に前記ピッチ微粉末を
5〜30wt%、好ましくは10〜25wt%含有させる。次い
で、この混合物を定量フィーダーにて転動式造粒機に供
給し、水を添加しながら直径1〜10mmの球状繊維塊を得
る。バインダーとして使用するピッチ微粉末の平均粒径
は、5μm 未満の場合には、バインダーの製造コストが
高くなり、また20μm 超の場合にはバインダーとしての
結合効果が弱い。ピッチ微粉末は、5wt%未満の場合に
はバインダーとしての効果が弱く、30wt%超の場合には
強度は向上するが、ピッチの軟化溶融時にピッチが繊維
間の空隙を小さくするため、活性炭素繊維としての特性
が低下する。水の添加量は不融化繊維100 重量部に対し
て30〜60重量部が好ましい。30重量部未満または60重量
部超の場合には球状化が困難となる。
In the method of the present invention, pitch fibers are infusibilized in an oxidizing atmosphere, and then coal-based and / or petroleum-based fine pitch powders are added as a binder to a plurality of infusible fibers and mixed. The pitch fine powder in a dry state here means pitch fine powder without water.
Next, while adding water to this mixture, for example, it is spheroidized by a tumbling granulator, and the generated spheres are dried and cured, and then activated. Pitch average particle size 5-20μ
The fine powder is pulverized into m, and the fine powder is mixed in a dry state with the infusible fiber as a raw material, and the pitch fine powder is contained in the resulting mixture in an amount of 5 to 30 wt%, preferably 10 to 25 wt%. Then, this mixture is fed to a tumbling type granulator by a quantitative feeder to obtain spherical fiber lumps having a diameter of 1 to 10 mm while adding water. If the average particle size of the pitch fine powder used as a binder is less than 5 μm, the manufacturing cost of the binder will be high, and if it exceeds 20 μm, the binding effect as a binder will be weak. If the pitch fine powder is less than 5 wt%, the effect as a binder is weak, and if it exceeds 30 wt%, the strength is improved. The properties of the fiber deteriorate. The amount of water added is preferably 30 to 60 parts by weight with respect to 100 parts by weight of the infusible fiber. If it is less than 30 parts by weight or more than 60 parts by weight, spheroidization becomes difficult.

【0007】なお、生成した球状繊維塊は所要に応じて
整球機によって処理して、真球度の増加および密度の増
加を行っても良い。その後に、前記球状炭素繊維塊を15
0 〜200 ℃の温度において60〜120 分間加熱した後に冷
却することにより硬化させ、その後に薬品賦活、ガス賦
活、水蒸気賦活などの既知方法によって賦活処理を施
す。なお、バインダーに使用するピッチ微粉末として
は、110 ℃以下の軟化点を有する安価で入手し易い通常
の石炭系ピッチおよび石油系ピッチを使用することがで
きる。
The produced spherical fiber lumps may be treated with a ball sphering machine as required to increase the sphericity and the density. Then, the spherical carbon fiber mass was
It is heated at a temperature of 0 to 200 ° C. for 60 to 120 minutes and then cooled to be cured, and then activated by a known method such as chemical activation, gas activation, and water vapor activation. As the pitch fine powder used for the binder, it is possible to use ordinary coal-based pitch and petroleum-based pitch that have a softening point of 110 ° C. or less and are easily available.

【0008】本発明方法においては、不融化繊維を球状
化する際に繊維のバインダーとしてピッチ微粉末を使用
しているので、球状化処理後の乾燥過程においてバイン
ダー用ピッチが溶融して個々の繊維間の結合力を増大さ
せるため乾燥後の工程における取り扱いが容易になるほ
か、賦活工程においてバインダーが炭化して生成する炭
化材の表面にも多数の細孔が形成されるため球状繊維塊
活性炭の集合体全体としての比表面積が増大する。また
バインダー用ピッチは汎用ピッチを原料としているの
で、安価であり、球状繊維塊活性炭の製造コストを安く
することができる。
In the method of the present invention, since fine pitch powder is used as a fiber binder when the infusible fiber is spheroidized, the pitch for binder is melted in the drying process after the spheroidizing treatment, so that the individual fibers are melted. In addition to facilitating handling in the post-drying step because it increases the binding force between the two, since many pores are also formed on the surface of the carbonized material produced by the binder carbonization in the activation step The specific surface area of the whole assembly increases. Further, since the pitch for binder is made of general-purpose pitch as a raw material, it is inexpensive and the manufacturing cost of the spherical fiber lump activated carbon can be reduced.

【0009】また、本発明方法においては、バインダー
用ピッチ微粉末と不融化繊維との混合物に水を添加して
いるので、ピッチ微粉末を水に懸濁させた懸濁液を使用
した場合に起り易い配管系統におけるピッチ微粉末の沈
降、閉塞を防止することができ、しかも球状化、乾燥硬
化後に得られる球状炭素繊維粒子の圧壊荷重が優れてい
ることが分かった。得られる球状炭素繊維粒子の圧壊荷
重がピッチ微粉末懸濁液を使用した場合に比べて優れて
いる原因としては、得られる球状炭素繊維粒子中にバイ
ンダーとしてのピッチが均一に分布されていることが考
えられる。なお、バインダー用ピッチ微粉末は微細な方
が好ましく、原料炭素繊維直径の 1/5〜5/5 程度である
のが好ましい。これより細粒ではバインダーの製造コス
トが高くなり、またこれより粗粒ではバインダーとして
の結合効果が弱くなり、球状繊維塊活性炭粒子の強度が
小さくなる。
Further, in the method of the present invention, since water is added to the mixture of the pitch fine powder for binder and the infusible fiber, when a suspension of the fine pitch powder in water is used. It was found that the fine pitch powder in the piping system, which tends to occur easily, can be prevented from settling and clogging, and that the spherical carbon fiber particles obtained after spheroidizing and drying and hardening have an excellent crushing load. The reason why the crushing load of the obtained spherical carbon fiber particles is superior to the case where the pitch fine powder suspension is used is that the pitch as a binder is uniformly distributed in the obtained spherical carbon fiber particles. Can be considered. The pitch fine powder for binder is preferably fine, and is preferably about 1/5 to 5/5 of the diameter of the raw material carbon fiber. Finer particles will increase the manufacturing cost of the binder, and coarser particles will weaken the binding effect as a binder, and will reduce the strength of the spherical fibrous activated carbon particles.

【0010】次に、本発明を実施例および比較例につい
て説明する。実施例1 高度に精製された軟化点230 ℃のコールタールピッチを
溶融紡糸してピッチ繊維を得、これを空気中にて300 ℃
において不融化し、次いでギロチン式自動繊維切断機に
よって平均長さ0.6 mmに切断し、平均粒径5μm のピッ
チ微粉末(軟化点:94℃の石炭ピッチ、川崎製鉄(株)
製PK−E)と混合した後に、回転円板型コーヒーミル
式粉砕機によって解砕処理した。生成した繊維に乾燥状
態でピッチ微粉末を混合して得た混合物を直径300 mmの
小型皿式造粒機において、これに水を添加しながら球状
化し、平均粒径3.1 mmの球状繊維塊を得た。この球状繊
維塊を 150℃にて2時間乾燥硬化させた後に、球状炭素
繊維粒子の圧壊荷重を測定した。
Next, the present invention will be described with reference to Examples and Comparative Examples. Example 1 Highly refined coal tar pitch having a softening point of 230 ° C. is melt-spun to obtain pitch fiber, which is 300 ° C. in air.
Infusible, and then cut to an average length of 0.6 mm by a guillotine-type automatic fiber cutting machine, and a fine pitch powder with an average particle size of 5 μm (softening point: 94 ° C. coal pitch, Kawasaki Steel Co.
PK-E), and then crushed by a rotary disk type coffee mill grinder. A mixture obtained by mixing fine pitch powder in a dry state with the produced fiber was spheroidized while adding water to a small dish granulator with a diameter of 300 mm to form a spherical fiber mass with an average particle diameter of 3.1 mm. Obtained. After the spherical fiber mass was dried and cured at 150 ° C. for 2 hours, the crushing load of the spherical carbon fiber particles was measured.

【0011】表1に球状化処理の条件および得られた圧
壊荷重を示し、表2に球状化処理に使用した皿式造粒機
における処理条件を示した。圧壊荷重の測定はオートグ
ラフ((株)島津製作所製DCS−500)によって行った。
なお、表1のバインダー添加率(重量比)の計算式にお
いて、バインダー残炭分とは、バインダーとして使用し
たピッチ微粉末を不活性雰囲気中で室温から800℃まで
加熱した際の残留炭素の重量である。
Table 1 shows the conditions for the spheroidizing treatment and the obtained crushing load, and Table 2 shows the treating conditions for the dish type granulator used for the spheroidizing treatment. The crush load was measured by an autograph (DCS-500 manufactured by Shimadzu Corporation).
In the formula for calculating the binder addition rate (weight ratio) in Table 1, the binder residual carbon content is the weight of residual carbon when the pitch fine powder used as the binder is heated from room temperature to 800 ° C in an inert atmosphere. Is.

【0012】表1:不融化繊維に乾燥状態でピッチ微粉
末バインダーを混合し、この混合物に水を添加して行っ
た球状化処理(ピッチ微粉末の平均粒径5μm)
Table 1: Spheroidizing treatment performed by mixing pitch fine powder binder in a dry state with infusible fiber and adding water to the mixture (average particle size of pitch fine powder 5 μm)

【表1】 [Table 1]

【0013】表2:皿式造粒機における球状化処理条件Table 2: Spheroidizing conditions in the dish granulator

【表2】 [Table 2]

【0014】最後に、上述のようにして得た平均粒径3.
1 mmの球状繊維塊を、縦200 mm、横200 mm、高さ 200mm
の箱型炉内に 100mmの高さまで充填し、33%の水蒸気雰
囲気中で 900℃において 2.5時間賦活処理を行い、BET
比表面積1500 m2/g の球状繊維塊活性炭を得た。なお、
比表面積の測定は(株)島津製作所製,アサップ2400
(商品名)を用いて行った。
Finally, the average particle size obtained as described above 3.
200 mm long, 200 mm wide, 200 mm high with 1 mm spherical fiber mass
It was filled up to a height of 100 mm in a box-shaped furnace of, and activated for 2.5 hours at 900 ° C in a 33% steam atmosphere.
A spherical fiber lump activated carbon having a specific surface area of 1500 m 2 / g was obtained. In addition,
Specific surface area is measured by Shimadzu Corporation, Asap 2400
(Trade name) was used.

【0015】比較例1 バインダーであるピッチ微粉末を乾燥状態で不融化繊維
と混合する代わりに、ピッチ微粉末を水に分散させた懸
濁液を使用した点を除き、実施例1と同様にして平均粒
径 3.1mmの球状炭素繊維塊を得、次いでこれを乾燥硬化
させた後に圧壊荷重を測定した。皿式造粒機における処
理条件は表2に示す条件と同じである。表3に球状化処
理の条件および得られた球状炭素繊維粒子の圧壊荷重を
示した。なお、表3のバインダー添加率(重量比)の計
算式において、バインダー残炭分とは、使用したバイン
ダー懸濁液を不活性雰囲気中で800 ℃まで加熱した際の
残留炭素の重量である。表1および表3に示す球状炭素
繊維粒子の圧壊荷重の値から、ピッチ微粉末バインダー
を水に分散させた懸濁液として添加した場合の圧壊荷重
は、ピッチ微粉末バインダーを乾燥状態で不融化繊維と
混合した場合の約70%にすぎないことが分かる。
Comparative Example 1 The same as Example 1 except that a suspension of pitch fine powder in water was used instead of mixing pitch fine powder as a binder in a dry state with infusible fibers. As a result, a spherical carbon fiber mass having an average particle diameter of 3.1 mm was obtained, which was then dried and cured, and then the crush load was measured. The processing conditions in the dish granulator are the same as those shown in Table 2. Table 3 shows the conditions of the spheroidizing treatment and the crushing load of the obtained spherical carbon fiber particles. In the formula for calculating the binder addition rate (weight ratio) in Table 3, the binder residual carbon content is the weight of residual carbon when the binder suspension used is heated to 800 ° C. in an inert atmosphere. From the values of the crushing load of the spherical carbon fiber particles shown in Table 1 and Table 3, the crushing load when the pitch fine powder binder was added as a suspension in which water was dispersed was infusibilized in the dry state. It can be seen that it is only about 70% when mixed with fiber.

【0016】表3:ピッチ微粉末バインダーを水に分散
させた懸濁液の形態で添加して行った球状化処理
Table 3: Spheronization treatment performed by adding pitch fine powder binder in the form of a suspension in which water is dispersed.

【表3】 [Table 3]

【0017】比較例2 バインダーとして平均粒径30μm のピッチ微粉末を使用
した点を除き、実施例1と同様にして平均粒径3.1 mmの
球状炭素繊維を得、その圧壊荷重を測定した。皿式造粒
機における処理条件は表2に示す条件と同じである。表
4に球状化処理の条件および得られた球状炭素繊維粒子
の圧壊荷重を示した。
Comparative Example 2 A spherical carbon fiber having an average particle diameter of 3.1 mm was obtained in the same manner as in Example 1 except that pitch fine powder having an average particle diameter of 30 μm was used as a binder, and its crush load was measured. The processing conditions in the dish granulator are the same as those shown in Table 2. Table 4 shows the conditions of the spheroidizing treatment and the crushing load of the obtained spherical carbon fiber particles.

【0018】表1および表4に示す球状炭素繊維粒子の
圧壊荷重の値から、平均粒径30μmのピッチ微粉末を使
用した場合の圧壊荷重は、平均粒径5μm のピッチ微粉
末を使用した場合の約80%にすぎないことが分かった。
From the values of the crushing load of the spherical carbon fiber particles shown in Tables 1 and 4, the crushing load when the pitch fine powder having an average particle size of 30 μm is used is the case when the pitch fine powder having an average particle size of 5 μm is used. It turns out that it is only about 80% of.

【0019】表4:不融化繊維に乾燥状態でピッチ微粉
末バインダーを混合し、この混合物に水を添加して行っ
た球状化処理(ピッチ微粉末の平均粒径30μm )
Table 4: Spheroidizing treatment performed by mixing pitch fine powder binder in a dry state with infusibilized fiber and adding water to this mixture (average particle diameter of pitch fine powder 30 μm)

【表4】 [Table 4]

【0020】[0020]

【発明の効果】上述のように、本発明方法においては、
球状繊維塊活性炭を製造する際に、バインダーとして安
価な石炭系および/又は石油系のピッチを微粉末化して
使用し、原料である不融化炭素繊維に乾燥状態で前記ピ
ッチ微粉末を混合し、この混合物に水を添加して球状化
することにより、バインダーとして従来のフェノール
系、エポキシ系などの樹脂を使用する方法、又はピッチ
微粉末を水に分散させた懸濁液として添加する方法と較
べて、生産性を改善することができ、工業的に有利に、
しかも安価に球状繊維塊活性炭を製造することができ、
産業への波及効果は非常に大きいものがある。
As described above, in the method of the present invention,
In producing spherical fiber lump activated carbon, inexpensive coal-based and / or petroleum-based pitch is used as a binder in a finely powdered form, and the infusible carbon fiber as a raw material is mixed with the pitch fine powder in a dry state, Compared with the conventional method of using a resin such as a phenolic or epoxy resin as a binder by adding water to this mixture to make it spherical, or adding it as a suspension in which pitch fine powder is dispersed in water. Therefore, productivity can be improved, and industrially advantageous,
Moreover, it is possible to inexpensively produce spherical fiber lump activated carbon,
The ripple effect on industry is very large.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 花谷 誠二 千葉県千葉市川崎町1番地 川崎製鉄株式 会社技術研究本部内 (72)発明者 角 誠之 千葉県千葉市川崎町1番地 川崎製鉄株式 会社技術研究本部内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Seiji Hanatani 1 Kawasaki-cho, Chiba-shi, Chiba Kawasaki Steel Co., Ltd. Technical Research Division (72) Masayuki Kakuno 1 Kawasaki-cho, Chiba-chi, Kawasaki Steel Co., Ltd. Research headquarters

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 タールピッチを原料として紡糸用ピッチ
を調製し、該ピッチを溶融紡糸によりピッチ繊維とし、
これを酸化性雰囲気中で不融化処理し、ついで複数本の
該不融化繊維をバインダーの存在下に集合させて球状化
し、生成した球状炭素繊維を賦活処理することにより球
状繊維塊活性炭を製造するにあたり、 球状化の際に前記バインダーとしてピッチ微粉末を使用
して前記不融化繊維に前記ピッチ微粉末を混合し、生成
した混合物に水を添加して球状化を行うことを特徴とす
る球状繊維塊活性炭の製造方法。
1. A pitch for spinning is prepared from tar pitch as a raw material, and the pitch is melt-spun to form a pitch fiber,
This is infusibilized in an oxidizing atmosphere, then a plurality of the infusibilized fibers are aggregated in the presence of a binder to be spheroidized, and the generated spherical carbon fibers are activated to produce a spherical fiber lump activated carbon. At the time of spheroidizing, the pitch fine powder is used as the binder at the time of spheroidizing, the pitch fine powder is mixed with the infusible fiber, and water is added to the resulting mixture to perform spheroidizing. Method for producing lump activated carbon.
【請求項2】 前記バインダーとして使用するピッチ微
粉末の平均粒径が5〜20μm であることを特徴とする請
求項1記載の方法。
2. The method according to claim 1, wherein the fine pitch powder used as the binder has an average particle size of 5 to 20 μm.
【請求項3】 前記バインダーとして使用するピッチ微
粉末が前記不融化繊維と前記ピッチ微粉末との混合物の
5〜30wt%を占めるように、前記不融化繊維と前記ピッ
チ微粉末とを混合することを特徴とする請求項1記載の
方法。
3. Mixing the infusible fiber and the pitch fine powder so that the pitch fine powder used as the binder occupies 5 to 30 wt% of the mixture of the infusible fiber and the pitch fine powder. The method according to claim 1, characterized in that
JP3319319A 1991-12-03 1991-12-03 Production of activated carbon made of spherical fiber lump Pending JPH05147913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3319319A JPH05147913A (en) 1991-12-03 1991-12-03 Production of activated carbon made of spherical fiber lump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3319319A JPH05147913A (en) 1991-12-03 1991-12-03 Production of activated carbon made of spherical fiber lump

Publications (1)

Publication Number Publication Date
JPH05147913A true JPH05147913A (en) 1993-06-15

Family

ID=18108870

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3319319A Pending JPH05147913A (en) 1991-12-03 1991-12-03 Production of activated carbon made of spherical fiber lump

Country Status (1)

Country Link
JP (1) JPH05147913A (en)

Similar Documents

Publication Publication Date Title
US4677086A (en) Shaped wood-based active carbon
US5324703A (en) Method of preparation of gasoline vapor adsorptive activated carbon
US5538932A (en) Preparation of high activity, high density activated carbon with activatable binder
US4857243A (en) Process of making microspherules of activated carbon
JP4855251B2 (en) Spherical activated carbon and method for producing the same
CN108439403B (en) Method for preparing biomass-formed activated carbon by low-temperature pre-pyrolysis and superfine raw materials
JPH01126214A (en) Production of activated carbon
DE4416576C1 (en) Spherical active carbon prodn.
US5209887A (en) Process for manufacturing microspherules of activated carbon
JP5394370B2 (en) Basic magnesium sulfate granular material and method for producing the same
KR100797141B1 (en) Process for preparing spherical activated carbon granule
JPH05147913A (en) Production of activated carbon made of spherical fiber lump
CN113117732B (en) Active carbon composite material with three-dimensional pore channel structure and preparation method thereof
JPH03275139A (en) Globular fiber lump-activated carbon and its production
JP2881875B2 (en) High strength molded activated carbon
JP3064127B2 (en) Volcanic ash adsorbent and method for producing the same
JPH05140820A (en) Production of spherical active carbon fiber
JP2515919B2 (en) Method for producing spherical fiber lump activated carbon
JP2989201B2 (en) Spherical porous carbon particles and method for producing the same
JP3197020B2 (en) Method for producing molecular sieve carbon
JP3006918B2 (en) Carrier for gas chromatography using aggregated carbon particles and method for producing the same
JPH05147914A (en) Production of activated carbon made of spherical fiber lump
JPH08217435A (en) Non-fusion treatment of thermoplastic fine powder, and production of activated carbon with the same
JPH05186210A (en) Production of spherically fibrous lumpy activated carbon
JPS5833172B2 (en) Method for producing granular molecular sieve carbon material from coal