JPH0555183B2 - - Google Patents

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Publication number
JPH0555183B2
JPH0555183B2 JP62117614A JP11761487A JPH0555183B2 JP H0555183 B2 JPH0555183 B2 JP H0555183B2 JP 62117614 A JP62117614 A JP 62117614A JP 11761487 A JP11761487 A JP 11761487A JP H0555183 B2 JPH0555183 B2 JP H0555183B2
Authority
JP
Japan
Prior art keywords
activated carbon
adsorbent
fibers
weight
synthetic resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP62117614A
Other languages
Japanese (ja)
Other versions
JPS63283749A (en
Inventor
Hisamatsu Muto
Shinichiro Shoji
Minoru Izawa
Hiroshi Nagata
Yoshitaka Nakahigashi
Tadayuki Inamori
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP11761487A priority Critical patent/JPS63283749A/en
Publication of JPS63283749A publication Critical patent/JPS63283749A/en
Publication of JPH0555183B2 publication Critical patent/JPH0555183B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、活性炭繊維を用いた立体構造の一体
的に成形された形成吸着体の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Field of Application> The present invention relates to a method for producing a three-dimensional, integrally formed adsorbent using activated carbon fibers.

<従来技術及びその問題点> 昭和50年頃から活性炭繊維(活性炭素繊維、繊
維状活性炭ともいう)が吸着材として使用される
ようになつた。活性炭繊維は従来から使用されて
いる粒状活性炭に較べて単位重量あたりの表面積
が大きいこと、細孔直径が粒状活性炭に比して小
さくかつその分布がシヤープである特徴があり、
吸着特性が優れているため新しい吸着材として注
目されている。
<Prior art and its problems> Activated carbon fibers (also referred to as activated carbon fibers or fibrous activated carbon) have been used as adsorbents since around 1975. Activated carbon fibers have a larger surface area per unit weight than conventionally used granular activated carbon, and have smaller pore diameters and a sharper distribution.
Due to its excellent adsorption properties, it is attracting attention as a new adsorbent.

しかし、活性炭繊維は、 (1) 嵩密度が小さく、単位体積あたりの吸着量を
大きくすることが難しい。
However, activated carbon fibers (1) have a low bulk density, making it difficult to increase the amount of adsorption per unit volume;

(2) 活性炭繊維は直径2〜30ミクロンの細い繊維
の表面にオングストローム単位の細孔が無数に
あるため非常に弱い。例えば、1〜2回指先で
擦ると容易に粉末状になる。
(2) Activated carbon fibers are extremely weak because there are countless angstrom-sized pores on the surface of the thin fibers with a diameter of 2 to 30 microns. For example, if you rub it once or twice with your fingertips, it will easily become powdery.

このため、機械的性質が弱く、嵩密度が小さい
という性質を有する活性炭繊維を使用した嵩密度
の大きい成形吸着体の製法の確立が望まれてい
る。
Therefore, it is desired to establish a method for manufacturing a shaped adsorbent having a high bulk density using activated carbon fibers having weak mechanical properties and low bulk density.

活性炭繊維を使用した気相及び液相用の吸着材
としては次のものが知られているが、いずれも上
記の課題を達成できていない。
The following are known as gas phase and liquid phase adsorbents using activated carbon fibers, but none of them have been able to achieve the above-mentioned problems.

(1) 活性炭繊維と熱溶融性合成樹脂繊維とを混紡
又は混合した後、加熱して、両者を融着もしく
は接着一体化させた吸着材がある(例えば特開
昭56−24151号公報参照)。
(1) There is an adsorbent in which activated carbon fibers and thermofusible synthetic resin fibers are blended or mixed and then heated to fuse or bond them together (for example, see Japanese Patent Application Laid-Open No. 56-24151). .

得られた吸着材は、空気の脱臭及び浄化、気
相からの溶剤の回収及び溶剤の濃縮、液相処理
(塩素等の除去、脱色、脱臭など)、単体ガスの
分離(分子ふるい)等に使用される。
The obtained adsorbent can be used for deodorizing and purifying air, recovering and concentrating solvents from the gas phase, liquid phase processing (removal of chlorine, decolorization, deodorization, etc.), separation of simple gases (molecular sieves), etc. used.

しかしながら、この方法では嵩密度の高い、
緻密な立体構造の吸着体の製造は困難である。
さらに切断加工時にロスが発生するし、所定形
状への再加工を必要とするのでコスト高とな
る。
However, this method has a high bulk density.
It is difficult to produce adsorbents with a dense three-dimensional structure.
Furthermore, a loss occurs during the cutting process, and reprocessing to a predetermined shape is required, resulting in high costs.

(2) アクリル繊維、フエノール樹脂繊維等の有機
繊維をニードルパンチ加工してフエルト状又は
不織布とするか、又はこれら繊維を糸状とし、
次いで織物とした後、熱処理又は薬品処理によ
り活性炭化させた吸着材がある。
(2) Organic fibers such as acrylic fibers and phenolic resin fibers are needle-punched into felt or non-woven fabrics, or these fibers are made into threads;
There are adsorbents that are made into textiles and then activated carbonized by heat treatment or chemical treatment.

このようにして得られた活性炭繊維構造体
は、極めて多数の細孔直径10〜40オングストロ
ーム程度のミクロポアーを備え、その比表面積
は、700〜2500m2/g程度となつている。その
ため、該構造体の強度は、当初のフエルト状又
は織物状態の強度の1/10程度にまで大幅に低下
しており、使用時に崩壊又は破損しやすい。
The activated carbon fiber structure thus obtained has an extremely large number of micropores with a diameter of about 10 to 40 angstroms, and a specific surface area of about 700 to 2500 m 2 /g. Therefore, the strength of the structure is significantly reduced to about 1/10 of the strength of the original felt-like or woven structure, and it is likely to collapse or break during use.

この方法でも嵩密度の高い、緻密な立体構造
の吸着体の製法は困難である。
Even with this method, it is difficult to produce an adsorbent with a high bulk density and a dense three-dimensional structure.

(3) 炭素繊維をニードルパンチ加工してフエルト
状又は不織布とするか、又は糸状とし、次いで
織物とした後、熱処理又は薬品処理により活性
炭化させ、吸着材とする。
(3) Carbon fibers are needle-punched to make felt or non-woven fabric, or thread-like, then made into woven fabric, and then activated carbonized by heat treatment or chemical treatment to make an adsorbent.

この場合にも、得られる構造体の強度が低い
ので、上記(2)におけると同様の実用上の難点が
あるし、嵩密度の高い、緻密な立体構造の吸着
体の製造は困難である。
In this case as well, since the strength of the obtained structure is low, there are practical difficulties similar to those in (2) above, and it is difficult to produce an adsorbent with a dense three-dimensional structure and a high bulk density.

<問題点を解決する為の手段> 活性炭繊維は優れた吸着特性を有する機械的強
度が弱く、嵩密度が小さい。本発明者は、このよ
うな性質を有する活性炭繊維を使用した嵩密度の
大きい緻密な立体構造の成形吸着体を開発すべく
種々研究を重ねた結果、吸着機能を発揮すべき活
性炭繊維及び該繊維を互いに接合する為の接合材
料となるべき熱溶融性合成樹脂(形状は繊維上及
びパウダー状のいずれでも良い。以下同じ)を含
む水性スラリーを調製し、多数の吸引用小孔を有
する成形型で吸引成形し、脱水した後、加熱する
ことによつて、熱溶融性合成樹脂の溶融を行なう
場合には、従来技術の問題点を実質的に解決若し
くは大幅に軽減し得る成形吸着体が得られること
を見出した。
<Means for Solving the Problems> Activated carbon fibers have excellent adsorption properties, low mechanical strength, and low bulk density. The present inventor has conducted various studies to develop a molded adsorbent with a high bulk density and a dense three-dimensional structure using activated carbon fibers having such properties. An aqueous slurry containing a heat-melting synthetic resin (which may be in the form of fibers or powder; the same applies hereinafter) to be used as a bonding material for bonding the When a hot-melt synthetic resin is melted by suction molding, dehydration, and heating, a molded adsorbent that can substantially solve or significantly alleviate the problems of the prior art can be obtained. I found out that it can be done.

即ち、本発明は、以下の如き成形吸着体の製造
方法を提供するものである: 活性炭繊維と熱溶融性合成樹脂を含み、活性炭
繊維100重量部に対する熱溶融性合成樹脂の含有
量が0.2重量部以上40重量部以下である均一なス
ラリーを、多数の吸引用小孔を有する成形型で吸
引成形し、脱水した後、加熱することによつて、
活性炭繊維が熱溶融性合成樹脂によりランダムに
接合保持された抄紙構造を有する立体構造の一体
的に成形された成形吸着体の製造方法」。
That is, the present invention provides a method for producing a shaped adsorbent as follows: Contains activated carbon fibers and a heat-melting synthetic resin, and the content of the heat-melting synthetic resin is 0.2 parts by weight per 100 parts by weight of the activated carbon fibers. By suction-molding a homogeneous slurry having an amount of at least 40 parts by weight using a mold having a large number of suction holes, dehydrating it, and then heating it,
A method for producing an integrally molded adsorbent with a three-dimensional structure having a papermaking structure in which activated carbon fibers are randomly bonded and held by a heat-melting synthetic resin.

本発明において、 抄紙構造の吸着体とは、吸着体を構成する繊維
が厚手の和紙の如くランダムに配置された構造で
あつてかつ緻密な構造を有する吸着体をいう。
In the present invention, an adsorbent having a paper-making structure refers to an adsorbent having a dense structure in which the fibers constituting the adsorbent are randomly arranged like thick Japanese paper.

立体構造の吸着体とは、シート状またはテープ
状等の可撓性のある厚さ3mm程度以下の薄い吸着
材以外の形状の吸着体をいう。具体的には、円柱
状、角柱材、楕円柱状、円錐台状、角錐台状、ペ
レツト状、直方体状、立方体状等の形状をしたも
のや、これらに孔を有する形状(例.前記柱状体
の上下面に開口し該柱状体の中心軸を中心軸とす
る貫通孔を有する円筒状のもの)の吸着体をい
う。
The adsorbent having a three-dimensional structure refers to an adsorbent having a shape other than a flexible thin adsorbent having a thickness of approximately 3 mm or less, such as a sheet or tape shape. Specifically, the shapes include cylinders, prismatic materials, elliptical cylinders, truncated cones, truncated pyramids, pellets, rectangular parallelepipeds, cubes, etc., and shapes with holes in these (for example, the above-mentioned columnar materials). A cylindrical adsorbent having a through hole that is open on the upper and lower surfaces of the columnar body and whose central axis is the central axis of the columnar body.

一体的に成形された吸着体とは、シート状、テ
ープ状等の吸着体を接着剤等を使用して積層して
作つた吸着体を排除するものであり、より具体的
には立体構造の吸着体の全部または一部を一度に
成形して得られたものをいう。成形吸着体とは、
その吸着体の製造時に成形型を用いて形状付与を
行つたものをいう。
An integrally formed adsorbent excludes adsorbents made by laminating sheet-like, tape-like, etc. adsorbents using adhesives, etc., and more specifically, adsorbents with a three-dimensional structure. Refers to something obtained by molding all or part of an adsorbent at once. What is a shaped adsorbent?
This means that the adsorbent is shaped using a mold during manufacture.

本発明においては、活性炭繊維としては特に限
定されず、吸着体の使用分野等に応じて適宜選択
すればよいが、通常繊維直径2〜30μm程度、繊
維長さ0.5〜10mm程度、細孔直径8〜20オングス
トローム程度の微細孔を有し、比表面積500〜
2500m2/g程度のものを使用することが好まし
い。また、その由来についても限定されず、レー
ヨン系、ポリアクリロニトリル系、フエノール樹
脂系、石炭ピツチ系、石油ピツチ系等のいずれで
あつても良い。
In the present invention, activated carbon fibers are not particularly limited and may be selected appropriately depending on the field of use of the adsorbent, but usually the fiber diameter is about 2 to 30 μm, the fiber length is about 0.5 to 10 mm, and the pore diameter is 8. ~Has micropores of about 20 angstroms and a specific surface area of 500~
It is preferable to use one with a surface area of about 2500 m 2 /g. Further, its origin is not limited either, and it may be any one of rayon-based, polyacrylonitrile-based, phenol resin-based, coal pitch-based, petroleum pitch-based, and the like.

活性炭繊維を接合させて一体化させる熱溶融性
合成樹脂としては、融点が50〜200℃程度のもの
が好適であり、ポリエチレン、ポリプロピレン、
ポリビニルアルコール、ポリアクリロニトリル、
ポリエステル等が例示され、特にポリアクリロニ
トリルが最も適している。熱溶融性合成樹脂とし
ては、糸状(繊維状)のものを使用すると、活性
炭の細孔を塞ぐことが少ないので、より好まし
い。熱溶融性合成樹脂糸としては、糸径5〜
100μm程度、長さ0.5〜10mm程度のものが好まし
い。熱溶融性合成樹脂糸としては、成形吸着体製
造時の加熱温度で溶融若しくは変質しない高融点
繊維糸の表面に熱溶融性合成樹脂を被覆した構造
のものを使用しても良い。
The heat-melting synthetic resin used to join and integrate the activated carbon fibers is preferably one with a melting point of about 50 to 200°C, such as polyethylene, polypropylene,
polyvinyl alcohol, polyacrylonitrile,
Examples include polyester, and polyacrylonitrile is particularly suitable. As the heat-melting synthetic resin, it is more preferable to use a filamentous (fiber-like) resin because it less likely blocks the pores of the activated carbon. As the heat-melting synthetic resin thread, the thread diameter is 5~
Preferably, the thickness is about 100 μm and the length is about 0.5 to 10 mm. As the heat-melting synthetic resin thread, one having a structure in which the surface of a high-melting point fiber thread that does not melt or change in quality at the heating temperature during production of the molded adsorbent body is coated with a heat-melting synthetic resin may be used.

活性炭繊維100重量部に対する熱溶融性合成樹
脂の配合量は、0.2〜40重量部程度、好ましくは
0.2〜20重量部程度とする。熱溶融性合成樹脂の
配合量が少なすぎる場合には、成形吸着体の強度
が低くなり、配合量が多すぎる場合には、活性炭
繊維の細孔が塞がれて気孔率が減少する。成形体
がある程度の強度を必要とし、かつ活性炭繊維の
含有量が多く、その特性を発揮させることが必要
とする場合の熱溶融性合成樹脂の配合量は、5重
量部前後が適切である。
The blending amount of the heat-melting synthetic resin to 100 parts by weight of activated carbon fiber is about 0.2 to 40 parts by weight, preferably
The amount should be approximately 0.2 to 20 parts by weight. If the amount of the heat-melting synthetic resin is too small, the strength of the molded adsorbent will be low, and if the amount is too large, the pores of the activated carbon fibers will be blocked and the porosity will decrease. When the molded article requires a certain degree of strength, contains a large amount of activated carbon fiber, and exhibits its properties, the appropriate amount of the hot-melt synthetic resin is about 5 parts by weight.

本発明の成形吸着体の製造方法を、以下に具体
的に説明する。
The method for manufacturing the shaped adsorbent of the present invention will be specifically explained below.

まず、所定の割合で活性炭繊維及び熱溶融性合
成樹脂を含有する均一な水性スラリーを調製す
る。水性スラリー中の個型分濃度は、特に限定さ
れないが、取扱いの容易さ、成形の容易さ等の観
点からは、0.1〜2重量%程度とすることが好ま
しい。スラリーの調製に際しては、必要に応じて
定法に従つて機械的分散ないし攪拌を行う。ま
た、成形吸着体の性能を阻害しない限り、分散
剤、安定剤、粘度調整剤、紙力増強剤、歩留向上
剤等を添加しても良い。かくして得られた均一な
水性スラリーを成形する。
First, a uniform aqueous slurry containing activated carbon fibers and a heat-melting synthetic resin in a predetermined ratio is prepared. The concentration of individual particles in the aqueous slurry is not particularly limited, but from the viewpoint of ease of handling, ease of molding, etc., it is preferably about 0.1 to 2% by weight. When preparing the slurry, mechanical dispersion or stirring is performed according to a conventional method, if necessary. Further, dispersants, stabilizers, viscosity modifiers, paper strength enhancers, retention aids, etc. may be added as long as they do not impede the performance of the shaped adsorbent. The homogeneous aqueous slurry thus obtained is shaped.

成形は、例えば、吸引成形の如く、減圧下に予
備脱水しつつ行なうことが好ましい。より具体的
には、例えば、円筒体を製造する場合には両端が
目くらフランジで密閉された表面に多数の吸引用
小孔を有する円筒状の芯体を有する成形型を前記
スラリー中に浸漬し、フランジの一端に設けられ
た吸引用ノズルを介してスラリーをポンプで吸引
することによつて芯体の表面に繊維成分をランダ
ムに集積成形する。円筒体製品の長さが短い場合
は、端面から吸引して繊維成分をランダムに集積
成形することも可能である。孔のない立体構造の
成形吸着体の場合は少なくとも1面に吸引用小孔
を有する成形型を使用して吸引することによつて
成形できる。吸引成形は成形型をスラリー中に埋
設することなく成形型にスラリーを供給して脱水
することによつて行うことも可能である。
The molding is preferably carried out under reduced pressure while preliminary dehydration is performed, such as by suction molding. More specifically, for example, in the case of manufacturing a cylindrical body, a mold having a cylindrical core body sealed at both ends with blind flanges and having a large number of suction holes on the surface is immersed in the slurry. Then, by sucking the slurry with a pump through a suction nozzle provided at one end of the flange, fiber components are randomly integrated and formed on the surface of the core body. If the length of the cylindrical product is short, it is also possible to form the fibrous components randomly by suctioning from the end face. In the case of a molded adsorbent having a three-dimensional structure without holes, it can be molded by suction using a mold having small suction holes on at least one side. Suction molding can also be carried out by supplying slurry to a mold and dewatering it without embedding the mold in the slurry.

成形された湿潤状態の成形体は所望の脱水をし
て、次いで、成形体を使用する熱溶融性合成樹脂
に応じた温度で加熱し、合成樹脂の溶融による成
形体の一体化及び乾燥を行なつて、本発明の成形
吸着体を得る。加熱温度は樹脂に接着性の出てく
る温度、使用する樹脂によつて変わるが軟化点よ
り40〜60℃程度高い温度が好ましい。
The molded body in a wet state is dehydrated as desired, and then heated at a temperature depending on the heat-melting synthetic resin used, and the molded body is integrated by melting the synthetic resin and dried. Thus, a shaped adsorbent of the present invention is obtained. The heating temperature varies depending on the temperature at which the resin becomes adhesive and the resin used, but it is preferably about 40 to 60°C higher than the softening point.

尚、本製造法によるとある程度の強度がありそ
のままで実用できる成形吸着体が得られる。熱溶
融性樹脂の使用量が少ないにもかかわらず、強度
のある成形吸着体が得られるのは、本発明で得ら
れる成形吸着体は、繊維がランダムに存在するた
めである。即ち、吸引面近傍では、繊維は吸引面
にほぼ平行にランダムに配向しているが、吸引面
から遠ざかると、繊維の一部は吸引面に種々の角
度をもつてランダムに吸引集積されている。この
角度を持つて吸引された繊維が保形作用に寄与し
ているためと思われる。しかし、それでも活性炭
繊維は本来的に弱い物質であるため、活性炭繊維
と熱溶融性合成樹脂のみを原料として得られる成
形吸着体は、使用目的によつては強度が不足す
る。この場合は、形成吸着体をケースに収容した
状態で使用しなければならないことがある。従つ
て、より強度の高い成形吸着体を得るには、非熱
溶融性繊維を補強材として使用することが望まし
い。
In addition, according to this manufacturing method, a shaped adsorbent body that has a certain degree of strength and can be used for practical use as it is can be obtained. The reason why a strong molded adsorbent can be obtained despite the small amount of hot-melt resin used is that fibers are randomly present in the molded adsorbent obtained by the present invention. That is, near the suction surface, the fibers are randomly oriented almost parallel to the suction surface, but as they move away from the suction surface, some of the fibers are randomly attracted and accumulated on the suction surface at various angles. . This seems to be because the fibers sucked at this angle contribute to the shape-retaining effect. However, since activated carbon fibers are inherently weak substances, molded adsorbents obtained using only activated carbon fibers and thermofusible synthetic resin as raw materials may lack strength depending on the purpose of use. In this case, the formed adsorbent may have to be used while being housed in a case. Therefore, in order to obtain a molded adsorbent with higher strength, it is desirable to use non-thermofusible fibers as a reinforcing material.

補強材としての非熱溶融性繊維としては、成形
吸着体製造時の加熱温度で溶融若しくは変質しな
いものであれば特に限定されないが、通常ガラス
繊維、アルミナ繊維等の無機繊維;ポリアミド繊
維、高融点のポリエチレン繊維、高融点のポリプ
ロピレン繊維、高融点のポリアクリルニトリル繊
維等の合成繊維;レイヨン等の半合成繊維、パル
プ繊維等が使用される。非熱溶融性繊維の糸径
は、補強材としての効果の観点から、2〜100μ
m程度とすることが好ましく、また、長さは、吸
着体製造時に使用する水性スラリーへの分散性及
び補強材としての効果の観点から、0.5〜10mm程
度とすることが好ましい。非熱溶融性繊維は、活
性炭繊維100重量部に対し、5〜80重量部程度配
合することが好ましい。配合量があまりに多すぎ
ると、活性炭繊維の量が相対的に減少するので、
吸着体としての性能が低下する。
Non-thermofusible fibers used as reinforcing materials are not particularly limited as long as they do not melt or change in quality at the heating temperature during production of the molded adsorbent, but usually include inorganic fibers such as glass fibers and alumina fibers; polyamide fibers, and high melting point fibers. Synthetic fibers such as polyethylene fibers with a high melting point, polypropylene fibers with a high melting point, and polyacrylonitrile fibers with a high melting point; semi-synthetic fibers such as rayon, pulp fibers, etc. are used. The diameter of the non-thermofusible fiber is 2 to 100 μm from the viewpoint of effectiveness as a reinforcing material.
The length is preferably about 0.5 to 10 mm, and the length is preferably about 0.5 to 10 mm from the viewpoint of dispersibility in the aqueous slurry used in producing the adsorbent and effectiveness as a reinforcing material. It is preferable that the non-thermofusible fiber is blended in an amount of about 5 to 80 parts by weight per 100 parts by weight of activated carbon fiber. If the blending amount is too large, the amount of activated carbon fiber will decrease relatively.
The performance as an adsorbent will deteriorate.

活性白土、イオン交換繊維、モレキユラーシー
ブ、硅素土、ゼオライト、銀添着活性炭、粒状活
性炭、粉末状活性炭等の吸着性のある第三材料を
更に添加してもよい。
A third adsorbent material such as activated clay, ion exchange fiber, molecular sieve, silica earth, zeolite, silver-impregnated activated carbon, granular activated carbon, powdered activated carbon, etc. may be further added.

湿式で吸引成形した本発明の成形体を使用する
場合、被吸着物質含有流体は成形時の吸引方向に
流すことが好ましい。熱溶融性合成樹脂の使用量
が少ない場合でも、層間剥離が起こりにくくなる
からである。
When using the molded article of the present invention that has been wet suction molded, it is preferable that the fluid containing the adsorbed substance be allowed to flow in the suction direction during molding. This is because even when the amount of heat-melting synthetic resin used is small, delamination is less likely to occur.

<発明の効果> 本発明の方法によつて得られる立体構造の成形
吸着体は、強度が弱く、嵩密度が小さい活性炭繊
維を使用しつつ、下記の性能を発現している。
<Effects of the Invention> The shaped adsorbent having a three-dimensional structure obtained by the method of the present invention exhibits the following performance while using activated carbon fibers having low strength and low bulk density.

(1) 嵩密度が通常0.08〜0.25g/cm3程度(実施例
では0.222g/cm3、0.165g/cm3)の吸着体が得
られる。
(1) An adsorbent having a bulk density of about 0.08 to 0.25 g/cm 3 (0.222 g/cm 3 and 0.165 g/cm 3 in the examples) can be obtained.

第三繊維の使用の仕方によつては、0.40g/
cm3もの嵩密度の吸着体を得ることも可能であ
る。
Depending on how the third fiber is used, 0.40g/
It is also possible to obtain adsorbents with bulk densities as high as cm 3 .

(2) 嵩密度が高く緻密な構造であるため、単位体
積当りの吸着量を大きくでき、装置の小型化が
でき、使用時に被吸着物質含有流体がシヨート
パスすることがなく、被吸着物質含有流体の流
速を高くできる。
(2) Due to its high bulk density and dense structure, the amount of adsorption per unit volume can be increased, the device can be made more compact, and the fluid containing the adsorbed substance does not pass through during use. The flow rate can be increased.

(3) 一体的に成形したものであるため、取扱やす
い。
(3) Since it is integrally molded, it is easy to handle.

(4) 活性炭繊維が密に集積し、かつ熱溶融性合成
樹脂で接合保持されているため、及び繊維がラ
ンダムに存在し、吸引面に対し任意の角度を有
し保形作用をする繊維が存在するため、非常に
脆い活性炭繊維を使用しているにもかかわら
ず、成形体の形状が崩れにくい。
(4) Because the activated carbon fibers are densely accumulated and bonded and held together by heat-melting synthetic resin, and because the fibers are randomly present, the fibers have a shape-retaining effect and have arbitrary angles to the suction surface. Because of the presence of activated carbon fibers, the shape of the molded product does not easily collapse even though extremely brittle activated carbon fibers are used.

また、該吸着体の新しい製造方法によると、上
記の特性を有する成形体が、 (1) 乾式で成形する場合は、活性炭繊維の粉塵が
発生し作業環境が悪くなるが、本発明の製造方
法は湿式で成形するため、良好な作業環境下で
製造できる。
Furthermore, according to the new manufacturing method of the adsorbent, a molded body having the above-mentioned characteristics can be produced by: (1) When dry molding, activated carbon fiber dust is generated and the working environment is poor; however, the manufacturing method of the present invention Because it is wet-molded, it can be manufactured in a favorable working environment.

(2) 活性炭繊維と熱溶融性合成樹脂を均一に分散
させたスラリーを成形型を用いて強制的に吸引
して成形するため、嵩密度の大きい、即ち緻密
な立体構造の成形体が得られる。緻密な立体構
造を有するが通気性及び通水性良好で、品質の
安定した吸着体が得られる。特に、熱溶融性合
成樹脂を使用すると強度が高く比表面積が実質
的に減少しない成形体が得られる。
(2) Because the slurry in which activated carbon fibers and heat-melting synthetic resin are uniformly dispersed is forcibly sucked into the mold using a mold, a molded product with a high bulk density, that is, a dense three-dimensional structure, can be obtained. . An adsorbent having a dense three-dimensional structure, good air permeability and water permeability, and stable quality can be obtained. In particular, when a hot-melt synthetic resin is used, a molded article with high strength and a specific surface area that does not substantially decrease can be obtained.

更に、補強材として、非熱溶融性繊維を配合す
る場合には、成形吸着体の強度がより向上して、
取扱いが容易となる。
Furthermore, when non-thermofusible fibers are blended as reinforcing materials, the strength of the shaped adsorbent is further improved,
Easy to handle.

さらに、熱溶融性合成樹脂が繊維状である場合
には活性炭の細孔を塞ぐことが少ないのでより好
ましい。
Furthermore, it is more preferable that the heat-melting synthetic resin is in the form of fibers, since it is less likely to block the pores of the activated carbon.

本発明の吸着体は、液相及び気相における固型
分の濾過、微量不純物及び有害成分の吸着除去、
有用成分の吸脱着による濃縮等に有効に使用され
る。より具体的には、浄水器におけるフイルター
として水道水からの鉄錆、悪臭物質、遊離塩素等
の除去;空気清浄器及びエアコンデイシヨナーに
おけるフイルターとして煙、悪臭物質等の除去及
び調湿;化学工場、クリーニング業等における溶
剤回収;鉱物油及び植物油中の固型分の除去等の
広範な分野で使用される。
The adsorbent of the present invention is capable of filtering solid matter in liquid and gas phases, adsorbing and removing trace impurities and harmful components, and
It is effectively used for concentrating useful components by adsorption and desorption. More specifically, it is used as a filter in water purifiers to remove iron rust, malodorous substances, free chlorine, etc. from tap water; as a filter in air purifiers and air conditioners to remove smoke, malodorous substances, etc. and control humidity; chemical It is used in a wide range of fields such as solvent recovery in factories, cleaning industries, etc.; removal of solids from mineral oils and vegetable oils.

<実施例> 以下、実施例及び比較例を示し、本発明の特徴
とするところをより一層明らかにするが、本発明
の技術的範囲は実施例に拘束されるものではな
い。
<Examples> Hereinafter, Examples and Comparative Examples will be shown to further clarify the features of the present invention, but the technical scope of the present invention is not limited to the Examples.

また、各実施例で得られた成形吸着体の吸着性
能は、整形しない活性炭繊維のそれとほぼ同等で
あつた。
Moreover, the adsorption performance of the shaped adsorbent obtained in each example was almost equivalent to that of the unshaped activated carbon fiber.

実施例 1 第1図を用いて説明する。活性炭繊維250重量
部及び木材パルプ50重量部を水槽3の中で水
50000重量部に分散させ、両者の繊維長が0.1〜5
mmとなるまで叩解した後、濃度0.5重量%のポリ
ビニルアルコール(軟化点約60℃)の水溶液100
重量部を加え、均一なスラリー2を得た。
Example 1 This will be explained using FIG. 1. 250 parts by weight of activated carbon fiber and 50 parts by weight of wood pulp were mixed with water in water tank 3.
Dispersed in 50,000 parts by weight, the fiber length of both is 0.1 to 5.
After beating until it becomes
Parts by weight were added to obtain a uniform slurry 2.

次いで、両端に盲フランジ5,6が取り付けら
れ、芯体4の周面に多数の吸引用小孔を設けた円
筒状の成形型1(外径29mm、長さ2470mm)を水槽
3の中に浸漬し盲フランジ6に取り付けられた吸
引ホース7を介して吸引ポンプ(図示せず)で芯
体4の内部からスラリーを吸引し、該成形型1の
芯体4の周囲に上記の水性スラリーを付着させた
後、形成された湿潤状態の中空円筒体(内径29
mm、外径60mm、長さ2470mm)を上記型から取外
し、140℃で120分間加熱乾燥した。
Next, a cylindrical mold 1 (outer diameter 29 mm, length 2470 mm) with blind flanges 5 and 6 attached to both ends and a large number of small suction holes provided on the circumferential surface of the core body 4 is placed in the water tank 3. The slurry is sucked from inside the core body 4 by a suction pump (not shown) through a suction hose 7 that is immersed and attached to the blind flange 6, and the aqueous slurry is applied around the core body 4 of the mold 1. After attachment, a wet hollow cylinder (inner diameter 29
mm, outer diameter 60 mm, length 2470 mm) was removed from the mold and dried by heating at 140° C. for 120 minutes.

かくして得られた抄紙構造の成形吸着体の寸法
は、内径28.9mm、外径59.9mm、長さ2468mmであ
り、その物性は、密度0.222g/cm3、透気度
78sec/300c.c.(通過面を直径10mmとした以外は
JIS P 8117に準じて測定)、濾過速度168sec/
100c.c.(JIS P 3801により測定)であつた。
The dimensions of the thus obtained molded adsorbent having a papermaking structure are 28.9 mm in inner diameter, 59.9 mm in outer diameter, and 2468 mm in length, and its physical properties include a density of 0.222 g/cm 3 and an air permeability.
78sec/300c.c. (except that the passing surface is 10mm in diameter)
Measured according to JIS P 8117), filtration speed 168sec/
100 c.c. (measured according to JIS P 3801).

実施例 2 活性炭繊維150重量部、ガラス繊維40重量部及
び軟化点約80℃のポリアクリロニトリル繊維10重
量部を水5000重量部に分散させ、夫々の繊維長が
0.1〜5mmとなるまで叩解して均一なスラリーを
得た後、実施例1と同様にして中空円筒状成形体
を作り、130℃で120分間加熱して、成形吸着体を
得た。
Example 2 150 parts by weight of activated carbon fiber, 40 parts by weight of glass fiber, and 10 parts by weight of polyacrylonitrile fiber with a softening point of about 80°C were dispersed in 5000 parts by weight of water, and each fiber length was
After beating to obtain a uniform slurry to a thickness of 0.1 to 5 mm, a hollow cylindrical molded body was prepared in the same manner as in Example 1, and heated at 130° C. for 120 minutes to obtain a molded adsorbent.

かくして得られた抄紙構造の成形吸着体の寸法
は、内径29.2mm、外径60.2mm、長さ2468mmであ
り、その物性は、坪量2560g/m2、厚さ15.5mm、
密度0.165g/cm3、透気度22sec/300c.c.(実施例
1と同様にして測定)、濾過速度40sec/100c.c.
(実施例1と同様にして測定)であつた。
The dimensions of the thus obtained molded adsorbent having a papermaking structure are 29.2 mm in inner diameter, 60.2 mm in outer diameter, and 2468 mm in length, and its physical properties are as follows: basis weight 2560 g/m 2 , thickness 15.5 mm,
Density 0.165g/cm 3 , air permeability 22sec/300c.c. (measured in the same manner as Example 1), filtration rate 40sec/100c.c.
(measured in the same manner as in Example 1).

秤量は、成形体の重量を側面を展開した平均の
面積π(内径+外径)/2×長さで除して計算す
る。上記製品重量は886g、面積はπ×(2.92+
6.02)/2×246.8=3466cm2であつたため上記の
値になる。
The weight is calculated by dividing the weight of the molded body by the average area π (inner diameter + outer diameter)/2×length when the side surfaces are expanded. The weight of the above product is 886g, and the area is π×(2.92+
6.02) /2×246.8=3466cm2 , so the above value is obtained.

実施例 3 実施例1で用いたポリビニルアルコールの代わ
りに軟化点約80℃のポリアクリロニトリル繊維10
重量部を使用し、かつ木材パルプは使用しなかつ
たこと及び芯体4の長さを500mmとしたこと以外
は実施例1と同様にして円筒状の成形体を得た。
実施例2で得られた成形体よりは強度が弱かつた
が浄水器等の吸着体として十分使用できるもので
あつた。
Example 3 Polyacrylonitrile fiber 10 with a softening point of about 80°C was used instead of the polyvinyl alcohol used in Example 1.
A cylindrical molded article was obtained in the same manner as in Example 1, except that part by weight was used, no wood pulp was used, and the length of the core 4 was 500 mm.
Although the strength was weaker than that of the molded product obtained in Example 2, it could be used satisfactorily as an adsorbent for water purifiers and the like.

比較例 1 ポリアクリロニトリル繊維を使用しない以外
は、実施例2と同様にして水性スラリーを調製し
た後、実施例1と同様にして成形を行なつたとこ
ろ、成形体は強度が不充分で、直ぐに崩壊した。
Comparative Example 1 An aqueous slurry was prepared in the same manner as in Example 2, except that polyacrylonitrile fibers were not used, and molding was performed in the same manner as in Example 1. However, the strength of the molded product was insufficient, and it immediately collapsed. It collapsed.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の成形体の吸引成形法を示す概
略図である。 1……成形型、2……スラリー、3……水槽、
4……芯体、5,6……盲フランジ、7……吸引
ホース。
FIG. 1 is a schematic diagram showing the suction molding method of a molded article of the present invention. 1...Mold, 2...Slurry, 3...Water tank,
4... Core body, 5, 6... Blind flange, 7... Suction hose.

Claims (1)

【特許請求の範囲】 1 活性炭繊維と熱溶融性合成樹脂を含み、活性
炭繊維100重量部に対する熱溶融性合成樹脂の含
有量が0.2重量部以上40重量部以下である均一な
スラリーを、多数の吸引用小孔を有する成形型で
吸引成形し、脱水した後、加熱することによつ
て、活性炭繊維が熱溶融性合成樹脂によりランダ
ムに接合保持された抄紙構造を有する立体構造の
一体的に成形された成形吸着体の製造方法。 2 活性炭繊維100重量部に対する熱溶融性合成
樹脂の含有量が0.2重量部以上20重量部以下であ
る特許請求の範囲第1項記載の成形吸着体の製造
方法。 3 スラリーが更に非熱溶融性繊維を含む特許請
求の範囲第1または2項記載の成形吸着体の製造
方法。 4 熱溶融性合成樹脂が繊維状である特許請求の
範囲第1、2または3項記載の成形吸着体の製造
方法。
[Claims] 1. A homogeneous slurry containing activated carbon fibers and a heat-melting synthetic resin, in which the content of the heat-melting synthetic resin is 0.2 parts by weight or more and 40 parts by weight or less based on 100 parts by weight of the activated carbon fibers, is By suction molding in a mold with small suction holes, dehydration, and then heating, a three-dimensional structure with a papermaking structure in which activated carbon fibers are randomly bonded and held by a heat-melting synthetic resin is molded into an integral structure. A method for manufacturing a molded adsorbent. 2. The method for producing a shaped adsorbent according to claim 1, wherein the content of the thermofusible synthetic resin is 0.2 parts by weight or more and 20 parts by weight or less based on 100 parts by weight of activated carbon fibers. 3. The method for producing a shaped adsorbent according to claim 1 or 2, wherein the slurry further contains non-thermofusible fibers. 4. The method for producing a shaped adsorbent according to claim 1, 2 or 3, wherein the heat-melting synthetic resin is fibrous.
JP11761487A 1987-05-13 1987-05-13 Molding adsorption material and manufacture of same Granted JPS63283749A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11761487A JPS63283749A (en) 1987-05-13 1987-05-13 Molding adsorption material and manufacture of same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11761487A JPS63283749A (en) 1987-05-13 1987-05-13 Molding adsorption material and manufacture of same

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP1027393A Division JPH0712429B2 (en) 1993-01-25 1993-01-25 Molded adsorbent

Publications (2)

Publication Number Publication Date
JPS63283749A JPS63283749A (en) 1988-11-21
JPH0555183B2 true JPH0555183B2 (en) 1993-08-16

Family

ID=14716113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11761487A Granted JPS63283749A (en) 1987-05-13 1987-05-13 Molding adsorption material and manufacture of same

Country Status (1)

Country Link
JP (1) JPS63283749A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016010749A (en) * 2014-06-27 2016-01-21 株式会社タカギ Method for producing molded adsorbent, molded adsorbent and water purifier using the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4777661B2 (en) * 2005-01-12 2011-09-21 旭ファイバーグラス株式会社 Vacuum insulation

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5138278A (en) * 1974-09-30 1976-03-30 Toyo Boseki JUGAI BUTSUSHITSUKYUDATSUCHAKUSOCHI
JPS556576A (en) * 1979-05-10 1980-01-18 Toyo Boseki Production of blended fiber paper
JPS5624151A (en) * 1979-07-26 1981-03-07 Jiyobu Anshian Ets Barudou Jiy Manufacture of filter structure
JPS5927440A (en) * 1982-08-05 1984-02-13 Mitsubishi Electric Corp Discharge lamp apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5138278A (en) * 1974-09-30 1976-03-30 Toyo Boseki JUGAI BUTSUSHITSUKYUDATSUCHAKUSOCHI
JPS556576A (en) * 1979-05-10 1980-01-18 Toyo Boseki Production of blended fiber paper
JPS5624151A (en) * 1979-07-26 1981-03-07 Jiyobu Anshian Ets Barudou Jiy Manufacture of filter structure
JPS5927440A (en) * 1982-08-05 1984-02-13 Mitsubishi Electric Corp Discharge lamp apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016010749A (en) * 2014-06-27 2016-01-21 株式会社タカギ Method for producing molded adsorbent, molded adsorbent and water purifier using the same

Also Published As

Publication number Publication date
JPS63283749A (en) 1988-11-21

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