JPH02233140A - Adsorbing material - Google Patents

Adsorbing material

Info

Publication number
JPH02233140A
JPH02233140A JP1054679A JP5467989A JPH02233140A JP H02233140 A JPH02233140 A JP H02233140A JP 1054679 A JP1054679 A JP 1054679A JP 5467989 A JP5467989 A JP 5467989A JP H02233140 A JPH02233140 A JP H02233140A
Authority
JP
Japan
Prior art keywords
adsorbent
plastic
adsorbing material
powder
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.)
Granted
Application number
JP1054679A
Other languages
Japanese (ja)
Other versions
JPH0790168B2 (en
Inventor
Eiji Tanaka
栄治 田中
Takeshi Tanii
谷井 健
Tsuneo Genma
玄馬 恒夫
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.)
Kuraray Chemical Co Ltd
Original Assignee
Kuraray Chemical Co 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 Kuraray Chemical Co Ltd filed Critical Kuraray Chemical Co Ltd
Priority to JP1054679A priority Critical patent/JPH0790168B2/en
Publication of JPH02233140A publication Critical patent/JPH02233140A/en
Publication of JPH0790168B2 publication Critical patent/JPH0790168B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To improve the appearance of an adsorbing material without lowering adsorbability by forming the adsorbing material by coating the adsorbing material composed of activated carbon with plastic such as a thermoplastic polymer so as not to damage the adsorbability thereof. CONSTITUTION:Plastic coating is applied to an adsorbing material composed of activated carbon so as not to damage the adsorbability thereof while heating, far infrared rays, ultrasonic waves, a microwave, high frequency and static electricity are simultaneously applied to the adsorbing material to obtain a coated adsorbing material. In this case, a method for coating the surface of the adsorbing material with a color component powder and a plastic fine powder or a method for coating the surface of the adsorbing material with a conductive powder and a plastic fine powder is pref. As the adsorbing material to be used, one having a surface area of several 100m or more per 1g like activated carbon is pref. As the aforementioned plastic, there are a thermoplastic resin and a thermosetting resin.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、脱臭剤、浄水剤等として使用することのでき
る吸着材に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an adsorbent that can be used as a deodorizing agent, a water purifying agent, and the like.

[従来の技術] 吸着材は脱臭剤、浄水剤等の一般消費剤として広く使用
さわている。しかし、その表面は外観が悪く、色調も白
や黒色などの味気ない色をしている。
[Prior Art] Adsorbents are widely used as general consumer products such as deodorizers and water purifiers. However, the surface has a poor appearance and the color tone is bland, such as white or black.

例えば活性炭では、黒色で外観、光沢共に美麗でないた
めに、活性炭が外部から直接見えるような状態で使用す
ることに対する障害となり、また手で触れた場合手が黒
くなり、または動かしたとき摩擦による摩耗で黒いほこ
りが出る等の問題がある。
For example, activated carbon is black and does not have a beautiful appearance or gloss, which is an obstacle to using activated carbon in a state where it can be seen directly from the outside.Also, if you touch it with your hand, your hand will turn black, or it will wear out due to friction when you move it. There are problems such as black dust coming out.

[発明が解決しようとする課題] 本発明は上記のような問題を解決し、更に用途の拡大を
はかることを課雇としている.[課題を解決するための
手段] 上記課題を解決するために、本発明は吸着材にその吸着
性を損なわないようにプラスチックをコーテ4ングした
吸着材右よびその好適な製法を提供する。以下、こわに
ついて詳細に説明する。
[Problems to be Solved by the Invention] The purpose of the present invention is to solve the above-mentioned problems and to further expand its applications. [Means for Solving the Problems] In order to solve the above problems, the present invention provides an adsorbent in which the adsorbent is coated with plastic so as not to impair its adsorption properties, and a suitable manufacturing method thereof. Stiffness will be explained in detail below.

(吸着材) 吸着材としては、活性炭、ゼオライト、シリカゲル、ア
ルミナゲル等通常用いられる吸着材なら何でも使用可能
である。
(Adsorbent) As the adsorbent, any commonly used adsorbent such as activated carbon, zeolite, silica gel, alumina gel, etc. can be used.

本発明に用いる吸着材の粒子はどのようなものでもよく
、粒子径が数μI〜数一■まで種々の粒径が使用可能で
あるが、これに限定されるものではない。
The particles of the adsorbent used in the present invention may be of any kind, and various particle sizes can be used, ranging from several micrometers to several micrometers, but the particle size is not limited thereto.

ここで使用する吸着材は、通常1g当たり例えば活性炭
のような数100m 或はそれ以上の大きな表面積を有
し、高い吸着性を示す材料であれば広範囲に使用できる
The adsorbent used here usually has a large surface area of several hundred square meters or more per gram, such as activated carbon, and can be used in a wide range of materials as long as it exhibits high adsorption properties.

例えば活性炭では、材料は通常椰子殻または木材等の炭
化物或は石炭が使用されるがいずれでもよい。また賦活
法も水蒸気或は二酸化炭素により高温または塩化亜鉛、
燐酸、農硫酸処理のいずれの方法により得られたもので
もよい。
For example, in the case of activated carbon, the material used is usually carbonized material such as coconut shell or wood, or coal, but any material may be used. The activation method also uses water vapor or carbon dioxide at high temperature or zinc chloride,
It may be obtained by either phosphoric acid or agricultural sulfuric acid treatment.

また形状は破砕炭、造粒炭、顆粒炭或は吸着材繊維、吸
着材フエルト、吸着材織物、吸着材シート等のいずれの
形態の吸着材も使用することができる。圧損および入替
えなどの取扱上、造粒炭、または吸着材を添着したシー
ト状吸着材が便利な場合がある。
Moreover, any form of adsorbent such as crushed charcoal, granulated charcoal, granulated charcoal, adsorbent fiber, adsorbent felt, adsorbent fabric, or adsorbent sheet can be used. For handling purposes such as pressure loss and replacement, it may be convenient to use granulated charcoal or a sheet adsorbent with an adsorbent attached.

造粒炭は常法に従って炭素材料100部に30〜60部
の石油ピッチ或はコールタール等をバインダーとして加
え混和成形後、賦活して調整されゼオライトでは、天然
ゼオライト、合成ゼオライト等いずれも使用可能である
Granulated coal is prepared by adding 30 to 60 parts of petroleum pitch or coal tar as a binder to 100 parts of carbon material as a binder, mixing and forming the coal, and activating it according to the conventional method.For zeolite, both natural zeolite and synthetic zeolite can be used. It is.

(接着材) 吸着材の表面をコーティングするプラスチックとしては
、熱可塑性プラスチック、メソフィーズピッチ等、水や
有機溶剤を用いずに加熱融着できるものが適している。
(Adhesive material) Suitable plastics for coating the surface of the adsorbent include thermoplastics, mesophyz pitch, and other materials that can be heat-fused without using water or organic solvents.

本発明にかかるプラスチックは、吸着材表面に添着した
場合、着色性や接着性、導電性を付与し得るものでもよ
い。
The plastic according to the present invention may be one that can impart colorability, adhesiveness, and conductivity when attached to the surface of the adsorbent.

更にプラスチック類を選択することによりその物質と吸
着材との複合機能を付与できれば、更に新しい用途の展
開が可能になる。ここでプラスチックとは、熱可塑性樹
詣、熱硬化性樹脂、親木性樹詣、導電性樹脂等を言う。
Furthermore, by selecting plastics, it is possible to impart a composite function between the material and the adsorbent, making it possible to develop even newer uses. Here, plastic refers to thermoplastic resin, thermosetting resin, tree-like resin, conductive resin, and the like.

熱可塑性樹脂としてはポリエチレン、ボリブロピレン、
ABS% PET、ナイロン、PBT,エチレンアクリ
ル樹脂、PMMA@詣、メソフエーズピッチ等が使用可
能である。
Thermoplastic resins include polyethylene, polypropylene,
ABS% PET, nylon, PBT, ethylene acrylic resin, PMMA@Mari, mesophase pitch, etc. can be used.

熱硬化性樹脂としてはフラン樹脂、フェノール樹脂等が
ある。
Examples of thermosetting resins include furan resins and phenol resins.

親水性樹脂としてはポリビニルアルコール樹脂、エバー
ル樹脂がある。
Hydrophilic resins include polyvinyl alcohol resin and EVAL resin.

導電性樹脂としてはポリビニルピロール、ポリアセチレ
ン等がある。
Examples of the conductive resin include polyvinylpyrrole and polyacetylene.

これらのプラスチック樹脂は、使用目的に応じて使い分
けるのが好ましい。すなわち、水溶液の吸着に用いる場
合は親水性ポリマーを接着材とするのが最適で、また油
、有機溶剤等のろ過に用いる場合は疎水性ポリマーを吸
着材にするのがその対照物質に対する親和性の点で好ま
しい。
It is preferable to use these plastic resins depending on the purpose of use. In other words, when used to adsorb aqueous solutions, it is best to use a hydrophilic polymer as an adhesive, and when used to filter oils, organic solvents, etc., it is best to use a hydrophobic polymer as an adsorbent because of its affinity for the target substance. It is preferable in this respect.

(製法) 添着の方法としてはプラスチック粉末と吸着材粒子を、
所定の比率で混和することにより製造可能である. 以下、具体的なコーティング吸着材の製法について述べ
る。
(Manufacturing method) The impregnation method involves adding plastic powder and adsorbent particles.
It can be manufactured by mixing in a predetermined ratio. A specific method for producing the coated adsorbent will be described below.

吸着材に対するプラスチックの使用割合は、吸着材の粒
子や比重によって異なるが、吸着材100重量部に対し
てプラスチック1〜100重量部が好ましいが、吸着能
低下を防ぐ点から必要最低限であることが良い。
The ratio of plastic to adsorbent varies depending on the particles and specific gravity of the adsorbent, but it is preferably 1 to 100 parts by weight of plastic per 100 parts by weight of adsorbent, but it should be the minimum necessary from the viewpoint of preventing a decrease in adsorption capacity. is good.

添着する方法は、混合することにより添着できるが、そ
の混合方法としては、通常の工業的混合方法、例えばミ
キサー、リボンミキサー、スタティックミキサー、ボー
ルミル、サンプルミル、ニーダー等が使用できるがこの
限りではない。混合のみでも付着させることができるが
、プラスチックと吸着材の接着をより強固にするために
、混合の際簡単な加熱を行なうのがよい。熱源としては
静電気の発生下、或はマイクロ波、赤外線、遠赤外線、
高周波等の混合の際同時に照射することにより接着をよ
り強固にすることができるが、これらを用いなくてもよ
い。このような操作により、剥離が起こらない程度の強
度で付着せしめることができる。
The impregnation method can be achieved by mixing, and the mixing method can be a normal industrial mixing method such as a mixer, ribbon mixer, static mixer, ball mill, sample mill, kneader, etc., but is not limited to this. . Adhesion can be achieved by mixing alone, but in order to strengthen the adhesion between the plastic and the adsorbent, it is recommended to perform simple heating during mixing. Heat sources include static electricity, microwaves, infrared rays, far infrared rays,
Although the adhesion can be made stronger by simultaneously irradiating high frequency waves or the like during mixing, it is not necessary to use these. By such an operation, the adhesive can be attached with sufficient strength to prevent peeling.

このような方法でプラスチック成分を吸着材表面にコー
ティングすることにより、吸着材の吸着能を低下するこ
となくプラスチックコーティング吸着材を得ることがで
きる。
By coating the surface of the adsorbent with a plastic component using such a method, a plastic-coated adsorbent can be obtained without reducing the adsorption capacity of the adsorbent.

吸着材の吸着性は通常一定温度のベンゼン或はアセトン
の飽和蒸気を平衡吸着せしめた場合の吸着量で表示され
る(JIS Kl474)。ここで、「吸着性を損なわ
ないように」とは、プラスチックコーティング吸着材を
吸着材として使用した場合使用できる程度に、との意味
である。吸着材をまったく損なうことなしに添着するこ
とが望ましいが、実際には困難な場合が多い。しかし、
吸着量が未添着吸着材の約50%以上あわば、通常の目
的には充分使用可能であり、用途によっては更に低くて
も使用できる。吸着材に添着せしめた場合、上記のよう
な吸着性の吸着性が保持できるように添着できるもので
あれば、どのようなプラスチック材でもよい。
The adsorptivity of an adsorbent is usually expressed as the amount of adsorption when saturated vapor of benzene or acetone is adsorbed in equilibrium at a constant temperature (JIS Kl474). Here, "so as not to impair the adsorptivity" means to the extent that it can be used when the plastic coated adsorbent is used as an adsorbent. Although it is desirable to attach the adsorbent without damaging it at all, this is often difficult in practice. but,
If the adsorbed amount is about 50% or more of the unimpregnated adsorbent, it can be used sufficiently for normal purposes, and depending on the application, it can be used even if it is even lower. Any plastic material may be used as long as it can be attached to the adsorbent in a manner that maintains the above-mentioned adsorption properties.

このようにして得られたプラスチックコーティング吸着
材は、堅牢にプラスチック成分が固着され、摩擦しても
プラスチックは剥げず堅牢であった。また、吸着性能の
低下も殆どなかった。
The plastic-coated adsorbent thus obtained had the plastic components firmly adhered to it, and the plastic did not peel off even when rubbed. Furthermore, there was almost no decrease in adsorption performance.

なお、これらの粒子を互いに接着して成形体とすること
も可能であり、さらには多層構造とすることも可能であ
る。
In addition, it is also possible to make a molded object by adhering these particles to each other, and furthermore, it is also possible to make a multilayer structure.

[発明の効果] 本発明によるプラスチックコーティング吸着材は吸着材
の吸着性を損なわずに吸着材の外観を良くすることがで
きるもので、吸着材表面に着色物質を添着することによ
り、いろいろな美麗な色彩を与えることができるのみな
らず、表面の性状も平滑面、ビロード状等いろいろな外
観をも持たすとかできる。
[Effects of the Invention] The plastic-coated adsorbent according to the present invention can improve the appearance of the adsorbent without impairing its adsorption properties, and by attaching a colored substance to the surface of the adsorbent, various aesthetic effects can be achieved. Not only can it provide a variety of colors, but it can also have a variety of surface textures such as smooth and velvety.

また、吸着材が活性炭の場合は、その表面にプラスチッ
クをコーティングすることにより吸着材に直接触れても
手が黒くならず、或は摩擦による摩πで黒いほこりが発
生することを大幅に防止することができる。これによっ
て、例えば従来の活性炭吸着材が黒色で外観、光沢も美
麗でなく、また黒いほこりが出やすいため、直接外部か
ら見えるような状態で使用したり、或は手に触れるよう
な状態で使用できなかフだのが、本発明により使用可能
となり、脱臭材、吸着材等広範囲な用途に使用できるよ
うになる。
In addition, if the adsorbent is activated carbon, coating its surface with plastic will prevent your hands from turning black even if you touch the adsorbent directly, or will significantly prevent black dust from being generated due to friction. be able to. As a result, for example, conventional activated carbon adsorbents are black and do not have a beautiful appearance or gloss, and they tend to generate black dust, so they cannot be used in situations where they can be seen directly from the outside or where they can be touched. However, the present invention makes it possible to use it in a wide range of applications such as deodorizing materials and adsorbents.

更に着色物質の性質によっては吸着材基材との相乗効果
による高い吸着性、吸着の度合を示すインジケーターと
しての効果、或は更に第3の物質を添着させて特殊な効
果を期待することができる。
Furthermore, depending on the properties of the colored substance, it is possible to expect high adsorption due to a synergistic effect with the adsorbent base material, an effect as an indicator of the degree of adsorption, or a special effect by adding a third substance. .

[実施例] (実施例1.1) 中心粒子径20μmのポリエチレン20重量部と粒子径
10〜32メッシュの椰子殻活性炭(ベンゼン吸着能5
8wt%)100重量部をミキサーに入れ10分間撹拌
した後取り出すと、プラスチックは殆んど付着していて
剥離がなめじた。これを熱風中流動加熱すると白い粉が
透明になり、冷却するとツルツルした被覆活性炭が得ら
れた。
[Example] (Example 1.1) 20 parts by weight of polyethylene with a center particle diameter of 20 μm and coconut shell activated carbon with a particle diameter of 10 to 32 mesh (benzene adsorption capacity 5
When 100 parts by weight (8wt%) of the mixture was put into a mixer and stirred for 10 minutes, the plastic was mostly adhered and peeled off easily. When this was fluidized and heated in hot air, the white powder became transparent, and when it was cooled, a slippery coated activated carbon was obtained.

これを摩擦しても炭塵は発生しなかった。Even when this was rubbed, no coal dust was generated.

これを内寸が50a+mφxloma+Hの型枠内に流
し込み、100℃で30分間、10kg/cm”の加圧
下で圧着した。
This was poured into a mold having an inner dimension of 50a+mφxloma+H, and crimped at 100°C for 30 minutes under a pressure of 10kg/cm''.

これを冷却後取り出して、吸着性能と強度を測定した。After cooling, it was taken out and its adsorption performance and strength were measured.

ベンゼン吸着能は55wt%/で、圧縮強度は20kg
であった。
Benzene adsorption capacity is 55wt%/, compressive strength is 20kg
Met.

比較のため、同じ活性炭に酢ビエマルジョンを10重量
%混合して成形し,これを乾燥後吸着性能と強度を測定
した。ベンゼン吸着性能は40%で、強度は0.1kg
であった。
For comparison, 10% by weight of vinegar emulsion was mixed with the same activated carbon and molded, and after drying, the adsorption performance and strength were measured. Benzene adsorption performance is 40%, strength is 0.1kg
Met.

(実施例1.2) 中心粒子径150μmのボリプロビレン7重量部と粒子
径8〜32メッシュのシリカゲル(水分吸着能43wt
%)100重量部をミキサーに入れ、赤外線を照射しな
がらlO分間撹拌した後取り出すと、プラスチックは殆
んど付着していて剥離がなかフた。均一にコーティング
ができた。こわを熱風中で流動加熱すると白い粉が透明
になり、冷却するとツルツルした被覆シリカゲルが得ら
れた.微粉は発生しなかった。
(Example 1.2) 7 parts by weight of polypropylene with a center particle size of 150 μm and silica gel with a particle size of 8 to 32 mesh (water adsorption capacity 43 wt)
%) was placed in a mixer and stirred for 10 minutes while irradiated with infrared rays. When taken out, most of the plastic was attached and there was little peeling. A uniform coating was achieved. When the powder was fluidized and heated in hot air, the white powder became transparent, and when it was cooled, a smooth coated silica gel was obtained. No fine powder was generated.

これを内寸が1 0 0++nX 1 0 0ms+X
 1 0+amHの型枠内に流し込み、100℃で30
分間、10kg/cm”の加圧下で圧着した。
The inner dimension of this is 1 0 0++nX 1 00ms+X
1 Pour into a 0+amH mold and heat at 100°C for 30
The bonding was carried out under a pressure of 10 kg/cm'' for 1 minute.

これを冷却後取り出して、吸着性能と強度を測定した.
水分吸着能は40wt%、圧縮強度は25kgであった
After cooling, it was taken out and its adsorption performance and strength were measured.
The water adsorption capacity was 40 wt%, and the compressive strength was 25 kg.

比較のため、同じシリカゲルにアクリルエマルジジンを
10wt%添加して成形し、これを乾燥後、吸着性能、
強度を測定した。水分吸着能は21%、強度は0.1k
gであった。
For comparison, 10 wt% of acrylic emulsion was added to the same silica gel and molded, and after drying, the adsorption performance,
The strength was measured. Moisture adsorption capacity is 21%, strength is 0.1k
It was g.

(実施例1.3) 中心粒子径10μmのポリエチレン30重量部と粒子径
3IIII1のゼオライト(アンモニア吸着能15wt
%)100重量部をボールミルに入れ60分間撹拌した
後取り出すと、プラスチックは殆んど付着していて剥離
がなかった。これを熱風中で流動加熱すると白い粉が透
明になり、冷却するとツルツルしたポリエチレン被覆ゼ
オライトが得られた。これを摩擦しても粉塵は発生しな
かった。
(Example 1.3) 30 parts by weight of polyethylene with a center particle diameter of 10 μm and zeolite with a particle diameter of 3III1 (ammonia adsorption capacity 15 wt.
%) was put into a ball mill, stirred for 60 minutes, and then taken out. Most of the plastic was attached and there was no peeling. When this was fluidized and heated in hot air, the white powder became transparent, and when cooled, a smooth polyethylene-coated zeolite was obtained. Even when this was rubbed, no dust was generated.

これを内寸が50no++φxlommHの型枠内に流
し込み、120℃で30分間、10kg/c■1の加圧
下で圧着した。
This was poured into a mold having an inner dimension of 50 mmH and crimped at 120° C. for 30 minutes under a pressure of 10 kg/cm1.

これを冷却後取り出しで、吸着性能と強度を測定した.
アンモニア吸着能は13wt%で、圧縮強度は25kg
であった。
After cooling, it was taken out and its adsorption performance and strength were measured.
Ammonia adsorption capacity is 13wt%, compressive strength is 25kg
Met.

比較のため、同じゼオライトに塩ビエマルジョンを10
%用いて成形し、これを乾燥後吸着性能、強度を測定し
た。アニモニア吸着量は8wt%、強度は0.2kgで
あった。
For comparison, 10% of PVC emulsion was added to the same zeolite.
After drying, the adsorption performance and strength were measured. The amount of animonia adsorbed was 8 wt%, and the strength was 0.2 kg.

(実施例2.1) 中心粒子径20μmのポリエチレン8重量部と赤色のカ
ラーセラミックス粉末3重量部、10〜32メッシュの
椰子殻活性炭(ベンゼン吸着能45wt%)100重量
部をロータリーミキサーに入れ30分間撹拌した後取り
出すと、プラスチックと着色成分が殆んど活性炭に付着
していて剥離がなかった。これを熱風中流動加熱すると
着色成分が強固に接着され、冷却すると美麗な赤色活性
炭が得られた。これを摩擦しても炭塵は発生しなかった
. これを内寸が501IIIφXIOwHの型枠内に流し
込み、100℃で30分間、1 0kg/c+a”の加
圧下で圧着した. これを冷却後取り出して、吸着性能と強度を測定した.
ベンゼン吸着能は42wt%で、圧縮強度は20kgで
あった。
(Example 2.1) 8 parts by weight of polyethylene with a center particle diameter of 20 μm, 3 parts by weight of red colored ceramic powder, and 100 parts by weight of coconut shell activated carbon of 10 to 32 mesh (benzene adsorption capacity 45 wt%) were placed in a rotary mixer for 30 minutes. When taken out after stirring for a minute, most of the plastic and coloring components were attached to the activated carbon and did not peel off. When this was fluidized and heated in hot air, the colored components were firmly adhered, and when it was cooled, beautiful red activated carbon was obtained. Even when this was rubbed, no coal dust was generated. This was poured into a mold with an internal dimension of 501IIIφXIOwH, and crimped at 100°C for 30 minutes under a pressure of 10kg/c+a''. After cooling, it was taken out and its adsorption performance and strength were measured.
The benzene adsorption capacity was 42 wt%, and the compressive strength was 20 kg.

比較のため、同じ活性炭に酢ビエマルジョンを10%用
いて成形し、これを乾燥後吸着性能、強度を測定した。
For comparison, the same activated carbon was molded with 10% vinegar emulsion, and after drying, the adsorption performance and strength were measured.

ベンゼン吸着性能は28%、強度は0.1kgであった
The benzene adsorption performance was 28% and the strength was 0.1 kg.

(実施例2.2) 中心粒子径100μmのボリブロピレン8重量部とベン
ガラ粉末3重量部と10〜32メッシュのゼオライト(
水分吸着能25wt%)100重量部をロータリミキサ
ーに入れ30分間撹拌した後取り出すと、プラスチック
と着色成分が殆んど付着していて剥離がなかった。これ
を熱風中流動加熱すると着色成分が強固に接着され、冷
却すると美麗な赤色ゼオライトが得られた.粉塵は発生
しなかった。
(Example 2.2) 8 parts by weight of polypropylene with a center particle size of 100 μm, 3 parts by weight of red iron powder, and 10 to 32 mesh zeolite (
When 100 parts by weight (moisture adsorption capacity 25 wt%) was put into a rotary mixer and stirred for 30 minutes, it was taken out, and the plastic and coloring components were mostly attached and there was no peeling. When this was fluidized and heated in hot air, the colored components were firmly adhered, and when it was cooled, a beautiful red zeolite was obtained. No dust was generated.

これを内寸が50Il■φxloa+mHの型枠内に流
し込み、100℃で30分間、1 0kg/c+s”の
加圧下で圧着した。赤いブロック状のゼオライトが得ら
れた. これを冷却後取り出して、吸着性能と強度を測定した。
This was poured into a mold with an inner dimension of 50 Il x φ x loa + mH, and crimped at 100°C for 30 minutes under a pressure of 10 kg/c+s''. A red block-shaped zeolite was obtained. After cooling, this was taken out. The adsorption performance and strength were measured.

水分吸着能は23wt%で、圧縮強度は25kgであっ
た。
The water adsorption capacity was 23 wt%, and the compressive strength was 25 kg.

比較のため、同じゼオライトに酢ビエマルジジンを10
%用いて成形し、これを乾燥後吸着性能、強度を測定し
た。水分吸着性能は12%、強度は0.5kgであった
For comparison, 10% of vinegar biemalzidine was added to the same zeolite.
After drying, the adsorption performance and strength were measured. The water adsorption performance was 12% and the strength was 0.5 kg.

(実施例2.3) 中心粒子径5μmのナイロン10重量部と酸化チタン粉
末10重量部と10〜32メッシュの活性炭(ベンゼン
吸着能48wt%)100重量部をロータリミキサーに
入れ30分間撹拌した後取り出すと、プラスチックと着
色成分が殆んど付着していて剥離がなかった。これを熱
風中流動加熱すると着色成分が強固に接着され、冷却す
ると美麗な白色活性炭が得られた。炭塵は発生しなかっ
た。
(Example 2.3) 10 parts by weight of nylon with a center particle diameter of 5 μm, 10 parts by weight of titanium oxide powder, and 100 parts by weight of activated carbon of 10 to 32 mesh (benzene adsorption capacity 48 wt%) were placed in a rotary mixer and stirred for 30 minutes. When I took it out, most of the plastic and coloring components were still attached and there was no peeling. When this was fluidized and heated in hot air, the colored components were firmly adhered, and when it was cooled, beautiful white activated carbon was obtained. No coal dust was generated.

これを内寸が50市φX10mmHの型枠内に流し込み
、100℃で30分間、1 0kg/cm”の加圧下で
圧着した。白いブロック状の活性炭が得られた。
This was poured into a mold with inner dimensions of 50 mm φ x 10 mm H, and pressed at 100° C. for 30 minutes under a pressure of 10 kg/cm. White block-shaped activated carbon was obtained.

これを冷却後取り出して、吸着性能と強度を測定した。After cooling, it was taken out and its adsorption performance and strength were measured.

ベンゼン吸着能は40wt%で、圧縮強度は25kgで
あった。
The benzene adsorption capacity was 40 wt%, and the compressive strength was 25 kg.

比較のため、同じ活性炭にアクリルエマルジョンを10
%用いて成形し、これを乾燥後吸着性能、強度を測定し
た。ベンゼン吸着性能は32%、強度は0.1kgであ
った。
For comparison, 10% of acrylic emulsion was added to the same activated carbon.
After drying, the adsorption performance and strength were measured. The benzene adsorption performance was 32% and the strength was 0.1 kg.

(実施例3.1) 中心粒子径10μmのポリエチレン12.5重量部と中
心粒径10μの黒鉛粉末40重量部と10〜32メッシ
ュの粒状活性炭100重量部を口−タリーミキサーに入
れ30分間撹拌した後取り出すと、プラスチックと導電
性成分が殆んど付着していて剥離がなかった。これを熱
風中流動加熱すると導電成分が強固に接着され、冷却す
ると通電発熱性を有する活性炭が得らわた。炭塵は発生
しなかった。
(Example 3.1) 12.5 parts by weight of polyethylene with a center particle size of 10 μm, 40 parts by weight of graphite powder with a center particle size of 10 μm, and 100 parts by weight of granular activated carbon of 10 to 32 mesh were placed in a mouth-tally mixer and stirred for 30 minutes. When I took it out after doing so, I found that most of the plastic and conductive components were attached and there was no peeling. When this was fluidized and heated in hot air, the conductive component was firmly adhered to it, and when it was cooled, an activated carbon with electricity-generating properties was obtained. No coal dust was generated.

これを内寸が501IIIllφXtO龍Hの型枠内に
流し込み、100℃で30分間、1 0 kg/ Cl
l”の加圧下で圧着した。ブロック状の活性炭が得られ
た.これを冷却後取り出して、吸着性能等を測定した。
This was poured into a mold with an inner dimension of 501IIIllφXtO Dragon H, and heated at 100°C for 30 minutes at 10 kg/Cl.
A block-shaped activated carbon was obtained. After cooling, this was taken out and its adsorption performance etc. was measured.

ベンゼン吸着能は3 8 w t%であった。この成形
体に電気を通したところ、40Vで2.5Aの電流が流
れ、60℃まで温度を上げることができた。また、圧縮
強度は15kgであった。
The benzene adsorption capacity was 38 wt%. When electricity was passed through this molded body, a current of 2.5 A at 40 V flowed, and the temperature could be raised to 60°C. Moreover, the compressive strength was 15 kg.

比較のため、同じ活性炭にアクリルエマルジョンを10
%添加して成形し、これを乾燥後強度を測定した。強度
は0.1kgであった。
For comparison, 10% of acrylic emulsion was added to the same activated carbon.
% was added and molded, and the strength was measured after drying. The strength was 0.1 kg.

(実施例3.2) 中心粒子径30μmのポリエチレン25重量部と中心粒
子径10μの黒鉛粉末25重量部と6〜8メッシュの球
状シリカゲル100重量部をロータリーミキサーに入れ
30分間撹拌した後取り出すと、プラスチックと導電成
分が殆んど付着していて剥離がなかった。これを熱風中
流動加熱すると導電成分が強固に接着され、冷却すると
通電発熱性を有するシリカゲルが得らわた。
(Example 3.2) 25 parts by weight of polyethylene with a center particle size of 30 μm, 25 parts by weight of graphite powder with a center particle size of 10 μm, and 100 parts by weight of 6-8 mesh spherical silica gel are placed in a rotary mixer, stirred for 30 minutes, and then taken out. Most of the plastic and conductive components were adhered to each other and there was no peeling. When this was fluidized and heated in hot air, the conductive component was firmly adhered to it, and when it was cooled, a silica gel having electrical heating properties was obtained.

これを内寸が501IIfflφX10++usl{の
型枠内に流し込み、100℃で30分間、10kg/c
−の加圧下で圧着した。ブロック状のシリカゲルが得ら
れた。
Pour this into a mold with internal dimensions of 501IIfflφX10++usl{10kg/c at 100℃ for 30 minutes.
- It was crimped under a pressure of -. A block-shaped silica gel was obtained.

これを冷却後取り出し、水分を10wt%吸着させた後
、通電しながら空気を5 ,&/mimで流し脱著した
ときの説着曲線を示す。40Vで0.6アンペアの電流
が流ね、60℃まで温度を上げることができ、ピンク色
が青色に戻った。圧縮強度は25kgであった。
This is taken out after cooling, and after adsorbing 10 wt % of water, the adhesion curve is shown when air is flowed at 5, &/min while electricity is applied to remove the adhesion. At 40V, a current of 0.6 ampere was applied, and the temperature was raised to 60°C, and the pink color returned to blue. The compressive strength was 25 kg.

比較のため、同じシリカゲルにエマルジョンを10%用
いて成形し、これを乾燥後吸着性能、強度を測定した。
For comparison, a 10% emulsion was molded into the same silica gel, and after drying, the adsorption performance and strength were measured.

通電できず、通電再生可能なシリカゲルブロックが得ら
れなかった。またその強度は0.1kgであった。
Electricity could not be applied, and a silica gel block that could be regenerated by electricity was not obtained. Moreover, its strength was 0.1 kg.

(実施例4.’l) プラスチックコーティングした1 073 2メッシュ
の活性炭(ベンゼン吸着能45wt%)を25■φX7
0mmφx250mmHの筒に成形し、カートリッジに
入れて圧損を測定した。このブロックのベンゼン吸着能
は40%であった。
(Example 4.'l) Plastic-coated 1 073 2 mesh activated carbon (benzene adsorption capacity 45 wt%) was added to 25 φX7
It was molded into a cylinder of 0 mmφ x 250 mmH, placed in a cartridge, and the pressure loss was measured. The benzene adsorption capacity of this block was 40%.

(実施例4.2) 中心粒子径20μmのポリエチレン10重量部と10〜
32メッシュの椰子殻活性炭100重量部をミキサーに
入れ10分間撹拌した後取り出すと、プラスチックは殆
んど付着していて剥離がなかった。これを熱風中流動加
熱すると白い粉が透明になり、冷却するとツルツルした
被覆活性炭が得られた。
(Example 4.2) 10 parts by weight of polyethylene with a center particle diameter of 20 μm and 10 ~
When 100 parts by weight of 32-mesh coconut shell activated carbon was placed in a mixer and stirred for 10 minutes, it was taken out, and most of the plastic was adhered to the mixer, with no peeling. When this was fluidized and heated in hot air, the white powder became transparent, and when it was cooled, a slippery coated activated carbon was obtained.

中心粒子径10μmのポリエチレン10重量部と300
μmのゼオライト100重量部をボールミルに入れ60
分間撹拌した後取り出すと、プラスチックは殆んど付着
していて剥離がなかった。
10 parts by weight of polyethylene with a center particle diameter of 10 μm and 300 parts by weight
Put 100 parts by weight of μm zeolite into a ball mill and
When taken out after stirring for a minute, most of the plastic was still attached and did not peel off.

これを熱風中流動加熱すると白い粉が透明になり、冷却
するとツルツルしたゼオライトが得られた。
When this was fluidized and heated in hot air, the white powder became transparent, and when cooled, a slippery zeolite was obtained.

これら二つのプラスチックコーティング吸着材を内寸が
50mmφX10mmHの型枠内に流し込み、120℃
で30分間、10kg/c♂の加圧下で圧着した。アン
モニアもベンゼンも吸着できる吸着材ブロックが得らわ
た。
These two plastic coated adsorbents were poured into a mold with inner dimensions of 50 mmφ x 10 mmH and heated to 120°C.
Pressure bonding was carried out for 30 minutes under a pressure of 10 kg/c♂. An adsorbent block capable of adsorbing both ammonia and benzene was obtained.

(実施例5.1) 中心粒子径1.5mmφの球状活性炭(ベンゼン吸着能
35%)100重量部に中心粒径3μのゼォライト[モ
レキュラーシーブ3A] (アンモニア吸着能15%)
50重量部および中心粒径10μのポリエチレン微粉末
20重量部をよく混合した後,加熱しながら転勤造粒法
により造粒した。
(Example 5.1) Zeolite [Molecular Sieve 3A] with a center particle diameter of 3μ in 100 parts by weight of spherical activated carbon with a center particle diameter of 1.5 mm (benzene adsorption capacity 35%) (ammonia adsorption capacity 15%)
After thoroughly mixing 50 parts by weight of polyethylene fine powder and 20 parts by weight of polyethylene fine powder having a center particle diameter of 10 μm, the mixture was granulated by a transfer granulation method while being heated.

球形炭の表面にゼオライト粉末が強固に結合された吸着
材が得られた。
An adsorbent with zeolite powder firmly bonded to the surface of spherical charcoal was obtained.

この吸着材の破壊強度は15kg/mm″′で、ベンゼ
ン吸着能が2 0 w t%、アンモニア吸着量は5w
t%であった。
The breaking strength of this adsorbent is 15 kg/mm'', the benzene adsorption capacity is 20 wt%, and the ammonia adsorption amount is 5 w.
It was t%.

出願人 クラレケミカル株式会社Applicant: Kuraray Chemical Co., Ltd.

Claims (10)

【特許請求の範囲】[Claims] (1)吸着材にその吸着性を損なわないようにプラスチ
ックをコーティングした吸着材。
(1) Adsorbent material coated with plastic so as not to impair its adsorption properties.
(2)プラスチックが導電性ポリマー、及びまたは熱硬
化性ポリマー、及びまたは熱可塑性ポリマー、及びまた
は親水性ポリマーである特許請求の範囲第1項記載の吸
着材。
(2) The adsorbent according to claim 1, wherein the plastic is a conductive polymer, a thermosetting polymer, a thermoplastic polymer, and/or a hydrophilic polymer.
(3)プラスチックが顔料を含んだ着色物である特許請
求の範囲第1項記載の吸着材。
(3) The adsorbent according to claim 1, wherein the plastic is a colored material containing a pigment.
(4)導電性粉末とプラスチック微粉末を吸着材の表面
にコーティングしたことを特徴とする導電性吸着材。
(4) A conductive adsorbent characterized by coating the surface of the adsorbent with conductive powder and fine plastic powder.
(5)紫外線硬化型ポリマーがコーティングされている
特許請求の範囲第1項記載の吸着材。
(5) The adsorbent according to claim 1, which is coated with an ultraviolet curable polymer.
(6)プラスチックコーティングした吸着材粒子を融着
せしめてなる吸着材成形体。
(6) An adsorbent molded body made by fusing adsorbent particles coated with plastic.
(7)複数の異なる吸着材が多層にコーティングされて
いる特許請求の範囲第6項記載の吸着材成形体。
(7) The adsorbent molded article according to claim 6, wherein a plurality of different adsorbents are coated in multiple layers.
(8)加熱、遠赤外線、超音波、マイクロ波、高周波、
静電気を同時に当てながら吸着材にその吸着性を損なわ
ないようにプラスチックコーティングすることを特徴と
する吸着材の製法。
(8) Heating, far infrared rays, ultrasound, microwaves, high frequency,
A method for producing an adsorbent that is characterized by simultaneously applying static electricity and coating the adsorbent with plastic so as not to impair its adsorption properties.
(9)着色成分粉末とプラスチック微粉末を吸着材の表
面にコーティングすることを特徴とする吸着材の製法。
(9) A method for producing an adsorbent, which comprises coating the surface of the adsorbent with colored component powder and fine plastic powder.
(10)導電性粉末とプラスチック微粉末を吸着材の表
面にコーティングすることを特徴とする導電性吸着材の
製法。
(10) A method for producing a conductive adsorbent, which comprises coating the surface of the adsorbent with conductive powder and fine plastic powder.
JP1054679A 1989-03-06 1989-03-06 Adsorbent Expired - Fee Related JPH0790168B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1054679A JPH0790168B2 (en) 1989-03-06 1989-03-06 Adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1054679A JPH0790168B2 (en) 1989-03-06 1989-03-06 Adsorbent

Publications (2)

Publication Number Publication Date
JPH02233140A true JPH02233140A (en) 1990-09-14
JPH0790168B2 JPH0790168B2 (en) 1995-10-04

Family

ID=12977477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1054679A Expired - Fee Related JPH0790168B2 (en) 1989-03-06 1989-03-06 Adsorbent

Country Status (1)

Country Link
JP (1) JPH0790168B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0550059A (en) * 1991-08-26 1993-03-02 Matsushita Electric Ind Co Ltd Method for purifying drinking water
WO2001097965A1 (en) * 2000-06-19 2001-12-27 Bridgestone Corporation Adsorbent, process for producing the same, and applications thereof
WO2002060496A3 (en) * 2000-12-15 2003-01-16 Kimberly Clark Co Coated activated carbon
WO2004039494A1 (en) * 2002-10-29 2004-05-13 Kuraray Chemical Co.,Ltd. Composite adsorbent and method for production thereof, and water purification material and water purifier
WO2008007421A1 (en) * 2006-07-10 2008-01-17 Mitsui Chemical Analysis & Consulting Service Inc. Apparatus for evaluating biodegradability, apparatus for measuring carbon dioxide evolution and utilization of the same
CN102730911A (en) * 2012-07-10 2012-10-17 辽宁大学 Method for degrading phenol in wastewater
WO2026004697A1 (en) * 2024-06-28 2026-01-02 東洋紡エムシー株式会社 Adsorbent and adsorption filter containing adsorbent

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5396985A (en) * 1977-02-04 1978-08-24 Mitsuo Watanabe Granular drying agent
JPS5697539A (en) * 1980-03-31 1981-08-06 Matsushita Electric Works Ltd Adsorbing agent
JPS6074716U (en) * 1984-07-04 1985-05-25 株式会社日本自動車部品総合研究所 activated carbon molded product

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5396985A (en) * 1977-02-04 1978-08-24 Mitsuo Watanabe Granular drying agent
JPS5697539A (en) * 1980-03-31 1981-08-06 Matsushita Electric Works Ltd Adsorbing agent
JPS6074716U (en) * 1984-07-04 1985-05-25 株式会社日本自動車部品総合研究所 activated carbon molded product

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0550059A (en) * 1991-08-26 1993-03-02 Matsushita Electric Ind Co Ltd Method for purifying drinking water
WO2001097965A1 (en) * 2000-06-19 2001-12-27 Bridgestone Corporation Adsorbent, process for producing the same, and applications thereof
US6890373B2 (en) 2000-06-19 2005-05-10 Bridgestone Corporation Adsorbents, process for producing the same, and applications thereof
WO2002060496A3 (en) * 2000-12-15 2003-01-16 Kimberly Clark Co Coated activated carbon
GB2386599A (en) * 2000-12-15 2003-09-24 Kimberly Clark Co Coated activated carbon
US6740406B2 (en) 2000-12-15 2004-05-25 Kimberly-Clark Worldwide, Inc. Coated activated carbon
GB2386599B (en) * 2000-12-15 2005-08-31 Kimberly Clark Co Coated activated carbon
WO2004039494A1 (en) * 2002-10-29 2004-05-13 Kuraray Chemical Co.,Ltd. Composite adsorbent and method for production thereof, and water purification material and water purifier
JPWO2004039494A1 (en) * 2002-10-29 2006-02-23 クラレケミカル株式会社 Composite adsorbent, method for producing the same, water purifier, and water purifier
WO2008007421A1 (en) * 2006-07-10 2008-01-17 Mitsui Chemical Analysis & Consulting Service Inc. Apparatus for evaluating biodegradability, apparatus for measuring carbon dioxide evolution and utilization of the same
CN102730911A (en) * 2012-07-10 2012-10-17 辽宁大学 Method for degrading phenol in wastewater
WO2026004697A1 (en) * 2024-06-28 2026-01-02 東洋紡エムシー株式会社 Adsorbent and adsorption filter containing adsorbent

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