JPH03122008A - Activated carbon sheet and its manufacturing method - Google Patents
Activated carbon sheet and its manufacturing methodInfo
- Publication number
- JPH03122008A JPH03122008A JP1260896A JP26089689A JPH03122008A JP H03122008 A JPH03122008 A JP H03122008A JP 1260896 A JP1260896 A JP 1260896A JP 26089689 A JP26089689 A JP 26089689A JP H03122008 A JPH03122008 A JP H03122008A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- sheet
- fluororesin
- carbon sheet
- manufacturing
- 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
Links
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、粉末活性炭の吸着性能を保持した高機能性の
活性炭シートとその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a highly functional activated carbon sheet that retains the adsorption performance of powdered activated carbon, and a method for producing the same.
吸着剤として汎用されている活性炭は、粉末、粒状、繊
維状などの形態で製造される。これらのうち、粉末およ
び粒状の活性炭は本質的にカーボンの集合体であるため
、汚染性があって取扱いに不便である。この点炭素繊維
を活性化して得られる繊維状の活性炭は、汚染性が少な
いうえに可撓性があるためハンドリングに至便であるが
、吸着容量が小さいという性能上の欠点がある。Activated carbon, which is commonly used as an adsorbent, is produced in the form of powder, granules, fibers, etc. Among these, powdered and granular activated carbon are essentially aggregates of carbon, so they are polluting and inconvenient to handle. In this respect, fibrous activated carbon obtained by activating carbon fibers is easy to handle due to its low contamination and flexibility, but it has a performance drawback in that it has a small adsorption capacity.
粉末活性炭は吸着能に優れているため、そのままの性能
を保持したままンート状に形成することができれば用途
範囲が著しく拡大する要素がある。Powdered activated carbon has excellent adsorption ability, so if it could be formed into a pellet while maintaining its performance, the range of its uses would be significantly expanded.
従来、粉末活性炭を利用したノートとしては、例えば陽
イオン無機繊維、活性炭粉末およびアニオン性バインダ
ーを必須成分とし、その他必要に応して適宜の副材料を
添加して得られる分11ケスラリ−を湿式抄紙法で抄造
する方法(特開昭56−48242号公報)、粉末活性
炭を捲絹sg 1lat織′t14物層の中間に不離一
体構造として介在させたシート構造物および製造方法(
特開昭62−289659号公報)が提案されている。Conventionally, notebooks using powdered activated carbon have been produced by wet-processing a slurry obtained by making cationic inorganic fibers, activated carbon powder, and anionic binder as essential components, and adding appropriate auxiliary materials as necessary. A method of making paper using a papermaking method (Japanese Patent Application Laid-Open No. 56-48242), a sheet structure in which powdered activated carbon is interposed as an inseparable integral structure between layers of rolled silk sg1lat woven material, and a manufacturing method (
JP-A-62-289659) has been proposed.
しかしながら、特開昭56−48242号の方法による
ものは粉末活性炭の含有量が少ない関係で破過(吸着千
倹i)寿命が短く、また特開昭62−289659号の
シート構造物はガス臭気や有害蒸気の吸着を対象として
いるため液相での使用に難点がある。However, the method of JP-A-56-48242 has a short breakthrough (adsorption) life due to the small content of powdered activated carbon, and the sheet structure of JP-A-62-289,659 has a gas odor. It is difficult to use in the liquid phase because it targets the adsorption of harmful vapors.
本発明の目的は、粉末活性炭の高吸着能を損ねずにシー
ト化された気液、高低温での使用が可能であり、そのう
え優れた非lη染性、可1尭性を有する活性炭シートと
その製造方法を提供するところにある。The object of the present invention is to create an activated carbon sheet that can be used in gas-liquid sheets and at high and low temperatures without impairing the high adsorption capacity of powdered activated carbon, and that also has excellent non-dyeability and dyeability. The purpose is to provide a manufacturing method.
〔課題を解決するための手段)
上記の目的を達成するための本発明による活性炭シート
は、活性炭組織にフィブリル化したフッ素樹脂が分tf
t介在した組成形態からなることを構成上の特徴として
いる。[Means for Solving the Problems] The activated carbon sheet according to the present invention for achieving the above object has a fibrillated fluororesin in the activated carbon structure.
Its structural feature is that it has a compositional form with t intervening.
本発明を構成する活性炭組織は、例えば、椰子殻、おが
屑、バルブ、石炭、カーボンブランク等からなる原料炭
を賦゛活して作製した通常の粉末状活性炭で、粒度が5
0μm以下の微粉末であることが好適である。The activated carbon structure constituting the present invention is, for example, ordinary powdered activated carbon made by activating raw coal made of coconut shells, sawdust, bulbs, coal, carbon blanks, etc., and has a particle size of 5.
It is preferable that the powder be a fine powder of 0 μm or less.
フィブリル化したフッ素樹脂とは、混練処理によって繊
維状に転化したフッ素樹脂を指し、このような性質をも
つフッ素樹脂の種類としては、フィブリル化性を有する
ポリテトラフルオロエチレン、ポリトリフルオロエチレ
ン、ポリ弗化ビニリデン、ポリオレフィンなどが挙げら
れる。A fibrillated fluororesin refers to a fluororesin that has been converted into a fibrous form through a kneading process. Types of fluororesin with such properties include polytetrafluoroethylene, polytrifluoroethylene, and polyethylene that have fibrillation properties. Examples include vinylidene fluoride and polyolefin.
したがって、本発明の活性炭シートIJI成は、組織中
に分散介在するフッ素樹脂が微細な繊維形態を呈して絡
み合い、粉末活性炭を繊維網で捕捉する状態に結合する
複合体として形成されている。Therefore, the activated carbon sheet IJI composition of the present invention is formed as a composite in which the fluororesin dispersed in the tissue is intertwined in the form of fine fibers, and the powdered activated carbon is captured in a fiber network.
上記の活性炭シートを得るための本発明による製造方法
は、粒度50μm以下の活性炭粉末100重里部にフィ
ブリル化性のフッ素樹脂1〜10重量部を配合し、水ま
たは/およびアルコールを混練助剤として前記フッ素樹
脂がフィブリル化するまで混練したのちシートに形成す
ることを特徴とする。The manufacturing method according to the present invention for obtaining the above activated carbon sheet includes blending 1 to 10 parts by weight of a fibrillating fluororesin with 100 parts by weight of activated carbon powder having a particle size of 50 μm or less, and using water or/and alcohol as a kneading aid. The method is characterized in that the fluororesin is kneaded until fibrillated and then formed into a sheet.
吸着基材となる粉末活性炭は粒度50μm以下に微粉砕
したものを用いることが重要で、粒度が50μmを上潮
るとフッ素樹脂の円滑なフィブリル化が阻害されて得ら
れるシートが脆弱となる。It is important to use powdered activated carbon that serves as an adsorption base material that has been finely pulverized to a particle size of 50 μm or less; if the particle size exceeds 50 μm, smooth fibrillation of the fluororesin is inhibited and the resulting sheet becomes brittle.
フィブリル化性のフッ素樹脂を活性炭粉末100重量部
当たり1〜10重猾部の範囲で配合する理由は、この配
合量が1重量部未満では繊維網の絡合形成が不十分とな
って強固なシートが成形できず、また10重量部を越え
ると吸着容量を低下させるとともに、シート表面が!9
水性となって濡れを悪化させるからである。The reason why a fibrillating fluororesin is blended in the range of 1 to 10 parts by weight per 100 parts by weight of activated carbon powder is that if the blending amount is less than 1 part by weight, the entanglement of the fiber network will be insufficient and the structure will not be strong. The sheet cannot be formed, and if it exceeds 10 parts by weight, the adsorption capacity will decrease and the sheet surface will deteriorate! 9
This is because it becomes water-based and worsens wetting.
これら成分には混練助剤として水、アルコールまたはこ
れらの混合物を添加して混練する。混練助剤の添加量は
、粉末活性炭100重量部当たり30〜80重量部の範
囲に設定することが好適である。These components are kneaded with water, alcohol, or a mixture thereof added as a kneading aid. The amount of the kneading aid added is preferably set in the range of 30 to 80 parts by weight per 100 parts by weight of powdered activated carbon.
活性炭粉末、フッ素樹脂および混練助剤は、フッ素樹脂
がフィブリル化するまで混練する。混練処理に使用され
る装置には限定はないが、剪断応力下で混練をおこなう
ことが望ましい。The activated carbon powder, fluororesin, and kneading aid are kneaded until the fluororesin is fibrillated. Although there are no limitations on the equipment used for the kneading process, it is desirable to perform the kneading under shear stress.
混練ペーストのシート化には、例えば等速二木ロールを
用いて複数回ロール間を通過させることによりおこなわ
れる。この際の条件としては、常温でロール回転数が1
rpm程度に設定することがフィブリル化した繊維の切
断を伴わずに円滑な成形をおこなううえで好ましい。The kneaded paste is formed into a sheet by, for example, using constant speed Niki rolls and passing between the rolls multiple times. The conditions in this case are that the roll rotation speed is 1 at room temperature.
It is preferable to set the speed to approximately rpm in order to perform smooth molding without cutting the fibrillated fibers.
〔作 用]
本発明の活性炭シートは、直径3〜20μm、長さ10
0〜200μm程度の微細繊維に転化したフィブリル化
フッ素樹脂の絡み合った網目内に活性炭組織が捕捉保持
された結合形態を有し、この特有の形態が粉末活性炭の
高い吸着能を損ねずに取扱いに至便な非汚染性および可
撓性を付与する機能をなす。そのうえ、微細繊維を構成
するフッ素樹脂は耐高温性、耐薬品性に優れているため
、気相、液相あるいは高温、低温等の条件にかかわらず
広く適用することができる。[Function] The activated carbon sheet of the present invention has a diameter of 3 to 20 μm and a length of 10 μm.
It has a bonding form in which the activated carbon structure is captured and held within the entangled network of fibrillated fluororesin that has been converted into fine fibers of approximately 0 to 200 μm, and this unique form makes it easy to handle without impairing the high adsorption capacity of powdered activated carbon. It functions to provide convenient non-contamination and flexibility. Furthermore, the fluororesin that constitutes the fine fibers has excellent high temperature resistance and chemical resistance, so it can be widely applied regardless of conditions such as gas phase, liquid phase, high temperature, low temperature, etc.
また、本発明の製造方法によれば、混練工程でフィブリ
ル化したフッ素樹脂がシート化段階において粉末活性炭
を絡合網目内に巧みに捕捉して一体化し、円滑に上記の
シート組織形態を形成する。Further, according to the manufacturing method of the present invention, the fluororesin fibrillated in the kneading process skillfully captures and integrates the powdered activated carbon within the entangled network in the sheeting stage, and smoothly forms the above-mentioned sheet structure form. .
以下、本発明を実施例に基づいて説明する。 Hereinafter, the present invention will be explained based on examples.
実施例1〜2、比較例1〜2
粒径40μm以下と70μm以下に微粉砕したヤシガラ
炭系の活性炭粉末100重量部に対し、フィブリル化性
のポリテトラフルオロエチレン(PTFE)粉末〔三片
デュポンフロロケミカル■製〕を添加量を変えて配合し
、これに混練助剤として活性炭粉末100重量部当たり
63重量部の水を添加してバブミル型混練機に投入し、
フッ素樹脂がフィブリル化するまで充分に攪拌混合した
。Examples 1-2, Comparative Examples 1-2 Fibrillating polytetrafluoroethylene (PTFE) powder [Mikata DuPont [manufactured by Fluorochemical ■] was mixed in varying amounts, 63 parts by weight of water was added as a kneading aid per 100 parts by weight of activated carbon powder, and the mixture was charged into a bub mill type kneader.
The mixture was sufficiently stirred and mixed until the fluororesin was fibrillated.
ついで、混練ペーストを等速二本ロール型成形機を用い
、常温、?rpmの回転条件で10回反復して通過させ
ることによりシート成形した。Next, the kneaded paste was molded at room temperature using a constant speed two-roll molding machine. A sheet was formed by repeatedly passing the sample 10 times under rotation conditions of rpm.
成形されたシートを80°Cの温度で乾燥し、厚さ40
0 μ面の活性炭シートを製造した。得られた活性炭シ
ートはハンドリング過程で粉末が飛散することがない良
好な非汚染性を有し、形状変形しゃすい可撓性を備える
ものであった。The formed sheet was dried at a temperature of 80°C to a thickness of 40°C.
An activated carbon sheet with a 0μ surface was manufactured. The obtained activated carbon sheet had good non-contamination properties with no powder scattering during the handling process, and was flexible enough to be easily deformed.
得られた各活性炭シートについて各種の性能を測定し、
製造条件と対比させて表1に示した。Various performances were measured for each activated carbon sheet obtained.
Table 1 shows a comparison with the manufacturing conditions.
表 1 表注:(1)メチレンブルー、(2)よう素。Table 1 Table notes: (1) Methylene blue, (2) Iodine.
実施例3
直径7kmのビレット型ガラス管の中間にステンレス網
(250μm)を敷き、その上に実施例2の活性炭シー
トを1枚重いてスペーサーで固定した。Example 3 A stainless steel net (250 μm) was placed in the middle of a billet-type glass tube with a diameter of 7 km, and one activated carbon sheet of Example 2 was fixed thereon with a heavy spacer.
この状態でガラス管上部からメチレンブルー水溶液(1
χ)をポンプにより20mf/min、で通水し、定時
間ごとにガラス管下部から採取したサンプルを670r
+mの波長で吸光分析して通水量とメチレンブルー(M
B : lppm))吸着量の関係(破過曲線)を測
定した。In this state, a methylene blue aqueous solution (1
χ) was pumped at 20mf/min, and samples were collected from the bottom of the glass tube at regular intervals at 670r.
Absorption analysis was performed at a wavelength of +m to determine the amount of water passing and methylene blue (M
B: lppm)) The relationship between adsorption amount (breakthrough curve) was measured.
得られた破過曲線を図に示した。図示の破過曲線は粉末
活性炭と変わらない高吸着性能を示すものであることが
確認された。The obtained breakthrough curve is shown in the figure. It was confirmed that the breakthrough curve shown in the figure shows the same high adsorption performance as powdered activated carbon.
〔発明の効果]
本発明によれば、粉末活性炭と同等の高吸着性能を備え
、気相、液相、高低温下の条件下で使用が可能であり、
良好な非汚染性と可撓性を有する活性炭シートを提供す
ることができる。[Effects of the Invention] According to the present invention, it has high adsorption performance equivalent to that of powdered activated carbon, and can be used in gas phase, liquid phase, and under high and low temperature conditions.
An activated carbon sheet having good non-staining properties and flexibility can be provided.
したがって、例えば、水道水をはじめとする各種液体の
浄化精製、煙草、調理等から発生する煙ガスの浄化など
気液を対象とした多様の吸着用として有用である。Therefore, it is useful for a variety of adsorption applications targeting gas and liquids, such as purification and purification of various liquids including tap water, and purification of smoke gases generated from smoking, cooking, and the like.
図は本発明の活性炭シートを用いたメチレンブルー水溶
液の破過曲線である。The figure shows a breakthrough curve of a methylene blue aqueous solution using the activated carbon sheet of the present invention.
Claims (1)
在した組成の活性炭シート。 2、粒度50μm以下の活性炭粉末100重量部にフィ
ブリル化性のフッ素樹脂1〜10重量部を配合し、水ま
たは/およびアルコールを混練助剤として前記フッ素樹
脂がフィブリル化するまで混練したのちシートに成形す
ることを特徴とする活性炭シートの製造方法。[Scope of Claims] 1. An activated carbon sheet having a composition in which fibrillated fluororesin is dispersed in an activated carbon structure. 2. Blend 1 to 10 parts by weight of a fibrillating fluororesin with 100 parts by weight of activated carbon powder with a particle size of 50 μm or less, knead with water or/and alcohol as a kneading aid until the fluororesin fibrillates, and then form into a sheet. A method for producing an activated carbon sheet, which comprises forming it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1260896A JPH03122008A (en) | 1989-10-05 | 1989-10-05 | Activated carbon sheet and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1260896A JPH03122008A (en) | 1989-10-05 | 1989-10-05 | Activated carbon sheet and its manufacturing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03122008A true JPH03122008A (en) | 1991-05-24 |
Family
ID=17354262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1260896A Pending JPH03122008A (en) | 1989-10-05 | 1989-10-05 | Activated carbon sheet and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03122008A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07194921A (en) * | 1993-12-28 | 1995-08-01 | Toho Rayon Co Ltd | Adsorption element for electric appliance |
| WO1995033008A1 (en) * | 1994-05-31 | 1995-12-07 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Fluororesin-containing resin composition, process for producing the same, and thermo-forming sheet and foam made therefrom |
| JP2006223463A (en) * | 2005-02-16 | 2006-08-31 | Nichias Corp | Air filter sheet, method for manufacturing the same, and air filter |
| JP3885150B2 (en) * | 2000-05-17 | 2007-02-21 | ダイニック株式会社 | Hygroscopic molded body |
| JP2010255697A (en) * | 2009-04-22 | 2010-11-11 | Tsurumi Soda Co Ltd | Container valve |
| CN101214955B (en) | 2008-01-15 | 2011-11-23 | 青岛华世洁环保科技有限公司 | A kind of hydrophobic honeycomb activated carbon and preparation method thereof |
| JPWO2010150534A1 (en) * | 2009-06-23 | 2012-12-06 | クラレケミカル株式会社 | Liquid-permeable capacitor, deionized water production method, and deionized water production apparatus |
| JP2017196598A (en) * | 2016-04-28 | 2017-11-02 | ダイニック株式会社 | Hygroscopic sheet |
-
1989
- 1989-10-05 JP JP1260896A patent/JPH03122008A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07194921A (en) * | 1993-12-28 | 1995-08-01 | Toho Rayon Co Ltd | Adsorption element for electric appliance |
| EP0661094A3 (en) * | 1993-12-28 | 1995-09-13 | Toho Rayon Kk | Adsorption material comprising activated carbon fiber and polytetrafluoroethylene. |
| WO1995033008A1 (en) * | 1994-05-31 | 1995-12-07 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Fluororesin-containing resin composition, process for producing the same, and thermo-forming sheet and foam made therefrom |
| JP3885150B2 (en) * | 2000-05-17 | 2007-02-21 | ダイニック株式会社 | Hygroscopic molded body |
| JP2006223463A (en) * | 2005-02-16 | 2006-08-31 | Nichias Corp | Air filter sheet, method for manufacturing the same, and air filter |
| CN101214955B (en) | 2008-01-15 | 2011-11-23 | 青岛华世洁环保科技有限公司 | A kind of hydrophobic honeycomb activated carbon and preparation method thereof |
| JP2010255697A (en) * | 2009-04-22 | 2010-11-11 | Tsurumi Soda Co Ltd | Container valve |
| JPWO2010150534A1 (en) * | 2009-06-23 | 2012-12-06 | クラレケミカル株式会社 | Liquid-permeable capacitor, deionized water production method, and deionized water production apparatus |
| JP2017196598A (en) * | 2016-04-28 | 2017-11-02 | ダイニック株式会社 | Hygroscopic sheet |
| WO2017188429A1 (en) * | 2016-04-28 | 2017-11-02 | ダイニック株式会社 | Sheet for absorbing moisture |
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