JPH0259018A - Air cleaner - Google Patents
Air cleanerInfo
- Publication number
- JPH0259018A JPH0259018A JP63212105A JP21210588A JPH0259018A JP H0259018 A JPH0259018 A JP H0259018A JP 63212105 A JP63212105 A JP 63212105A JP 21210588 A JP21210588 A JP 21210588A JP H0259018 A JPH0259018 A JP H0259018A
- Authority
- JP
- Japan
- Prior art keywords
- ion
- fiber
- exchange fiber
- exchange
- adsorption
- 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
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は小事業場や一般家庭など比較的小さな生活空間
において、快的な居住環境を維持するにあたり、最も重
要な要件であるきれいな空気、即ち悪臭がなく浮遊粒子
のない空気を製造する空気清浄器に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention provides clean air, which is the most important requirement in maintaining a comfortable living environment in relatively small living spaces such as small businesses and general households. That is, it relates to an air purifier that produces air that is odor-free and free of suspended particles.
(従来の技術)
空気の汚染形態はガス成分に由来する臭いと浮遊粒子の
ちりによるものとに大別され、その除去方法は全く異な
っている。(Prior Art) Types of air pollution are broadly classified into odors originating from gas components and those due to suspended particles, and the methods for removing them are completely different.
脱臭方法として従来より行われてきた方法には、中和、
酸化、還元等を利用した化学的脱臭、活性炭やゼオライ
ト等を吸着剤として利用した物理的脱臭、細菌や酵素を
用いる生物脱臭などがある。Traditional methods of deodorization include neutralization,
These include chemical deodorization using oxidation, reduction, etc., physical deodorization using activated carbon or zeolite as an adsorbent, and biological deodorization using bacteria or enzymes.
化学的脱臭では塩酸、硫酸、水酸化ナトリウム水溶液の
ように酸性やアルカリ性の水溶液を用いたり、次亜塩素
酸ソーダ水溶液等を酸化剤として用いた薬液洗浄方法が
知られているが、これ等は大きな装置が必要であるばか
りでなく危険な薬品も取扱うので小事業場や一般家庭に
は向いていない、生物脱臭についても同様のことが言え
る。For chemical deodorization, chemical cleaning methods are known that use acidic or alkaline aqueous solutions such as hydrochloric acid, sulfuric acid, or sodium hydroxide aqueous solutions, or chemical cleaning methods that use sodium hypochlorite aqueous solutions as oxidizing agents. The same can be said of biological deodorization, which not only requires large equipment but also uses dangerous chemicals, making it unsuitable for small businesses or households.
物理的脱臭では活性炭を吸着剤として使用する方法が最
も一般的であるが、粒状活性炭では吸着速度および利用
率がそれほど高くないため、そのままの形状で使用する
には無理がある。むしろ充填塔方式で大量処理する場合
に適している。吸着速度を上げるため粒状活性炭を粉砕
し微粒子とする考えもあるが取扱いがかえって不便にな
っている。粉末活性炭なみの表面積を有している活性炭
素繊維がマット状、不織布状等の成型体の形状で最近市
販されており、プリーツ状等への加工が容易であるため
、小事業場や一般家庭等のようにコンパクトな装置が必
要とされている場所では、粒子の濾過作用とガス成分の
吸着の両方の機能を有するので一定の評価を受けている
。ただし、活性炭は中性ガスの吸着性能に優れているが
、酸性ガスや塩基性ガスの吸着能力に乏しく、いずれの
形状の活性炭を使用しても、この限界を克服するもので
はない、特に、トイレ臭や魚の腐った臭いの主なる原因
物質であるアンモニアやトリメチルアミンは塩基性ガス
に属しており、これらに対する吸着能力が極めて悪い。The most common method for physical deodorization is to use activated carbon as an adsorbent, but since the adsorption rate and utilization rate of granular activated carbon are not very high, it is difficult to use it in its original form. Rather, it is suitable for large-scale processing using a packed column method. In order to increase the adsorption rate, there is an idea to crush granular activated carbon into fine particles, but this makes handling more inconvenient. Activated carbon fibers, which have a surface area comparable to that of powdered activated carbon, have recently been commercially available in molded forms such as mats and non-woven fabrics, and are easy to process into pleated shapes, etc., making them suitable for small businesses and general households. In places where a compact device is required, such as in the United States, it has received a certain amount of praise because it has both the functions of filtering particles and adsorbing gas components. However, although activated carbon has excellent adsorption performance for neutral gases, it has poor adsorption ability for acidic gases and basic gases, and no matter which form of activated carbon is used, this limitation cannot be overcome. Ammonia and trimethylamine, which are the main causes of toilet odor and rotten fish odor, belong to basic gases, and the adsorption ability for them is extremely poor.
一方、微粒子の除去方法には、繊維状又は多孔質の素材
をフィルタに用い濾過する方法や微粒子の帯電を利用し
て電気的に吸着する方法、またはそれ等を組合わせた方
法が知られているが、小容量処理にはフィルタで濾過す
る方法が適している。On the other hand, known methods for removing particulates include filtration using a fibrous or porous material as a filter, electrical adsorption using electrification of the particulates, or a combination of these methods. However, filtering is suitable for small volume processing.
濾過で微粒子を除去する場合、除去率を上げるには、目
開きや充填率を上げる必要があるため、フィルタ部での
差圧が大きくなり、風量不足を招いてしまう。When removing particulates by filtration, in order to increase the removal rate, it is necessary to increase the opening and filling rate, which increases the differential pressure at the filter section, resulting in insufficient air volume.
このように、あらゆる種類の有害ガス成分と微粒子とを
効率的に除去できる空気清浄器は未だ見当らない。As described above, an air purifier that can efficiently remove all kinds of harmful gas components and particulates has not yet been found.
本発明の目的はあらゆる種類の有害ガス成分と微粒子を
完全に除去できるコンパクトな空気清浄器を提供するこ
とである。The object of the present invention is to provide a compact air purifier that can completely remove all kinds of harmful gas components and particulates.
(課題を解決するための手段)
本発明による空気清浄器は活性炭素繊維およびイオン交
換繊維を吸着部として有しており、両者の複合的効果を
特徴としている。(Means for Solving the Problems) The air cleaner according to the present invention has activated carbon fibers and ion exchange fibers as adsorption parts, and is characterized by the combined effects of both.
ここで用いる活性炭素繊維味いかなるものでも良いが、
短繊維は取扱いが難しく、織布、不織布やマント状等の
成型品の形状が望ましい。Any type of activated carbon fiber can be used here, but
Short fibers are difficult to handle and are preferably in the form of woven fabrics, non-woven fabrics, or molded products such as cloak-like shapes.
イオン交換繊維の形状も織布、不織布やマット状が好ま
しいが、短繊維のみが市販されているにすぎず、このよ
うな形状で入手するのは不可能である。その点数射線グ
ラフト重合は、基材の特徴を生かしながら、官能基を導
入することができるので、短繊維や長繊維のみならずそ
の成形品である織布、不織布やマット状の基材を使用す
れば、その形状のままでイオン交換繊維ができあがる。The shape of the ion-exchange fibers is preferably woven fabric, non-woven fabric, or matte, but only short fibers are commercially available, and it is impossible to obtain them in such shapes. Point ray graft polymerization can introduce functional groups while taking advantage of the characteristics of the base material, so it can be used not only for short fibers and long fibers, but also for their molded products such as woven fabrics, non-woven fabrics, and mat-like base materials. Then, the ion-exchange fiber will be created in that shape.
なお、ここで用いる放射線はγ線、α線、β線、電子線
などがあり、いずれも使用できるが、γ線や電子線が本
発明には特に適している。放射線グラフト重合方法には
照射方法により同時照射法と前照射法、基材とモノマー
の接触の仕方により液相グラフト重合と気相グラフト重
合に分けられるなど種々の方法があるが、本発明には前
照射気相グラフト重合が、コストが小さいおよび官能基
分布の点で好ましい。Note that the radiation used here includes gamma rays, alpha rays, beta rays, electron beams, etc., and any of them can be used, but gamma rays and electron beams are particularly suitable for the present invention. There are various methods for radiation graft polymerization, such as simultaneous irradiation method and pre-irradiation method depending on the irradiation method, and liquid phase graft polymerization and gas phase graft polymerization depending on the method of contact between the base material and the monomer. Pre-irradiation gas phase graft polymerization is preferred due to its low cost and functional group distribution.
吸着部における活性炭素繊維とイオン交換繊維の構成は
両者が織布、不織布等の場合はそのまま枠等に張り付け
て使用することが可能である。また、他の高分子繊維を
サポート剤として併用しても良く、短繊維の場合等に有
効である。When the activated carbon fibers and ion exchange fibers in the adsorption part are both made of woven fabric, nonwoven fabric, etc., they can be used as they are by being attached to a frame or the like. Further, other polymeric fibers may be used in combination as a support agent, which is effective in the case of short fibers.
(作用)
このように、活性炭素繊維とイオン交換繊維を吸着部と
して有する空気清浄器を利用すれば、従来より問題とな
っていた活性炭素繊維の塩基性ガスおよび酸性ガスに対
する吸着能力の低い点をイオン交換繊維によって補うこ
とができる。さらに、イオン交換繊維の表面がカチオン
交換繊維の場合にe、アニオン交換繊維の場合にeに帯
電していン
るため、反対符号の微粒子も静電吸着で除去することが
でき、微粒子除去用フィルタの負荷を軽減または肩がわ
りすることができる。または微粒子除去用フィルタ自体
に放射線グラフト重合を利用してイオン交換基を導入す
れば、差圧を増大させることなく、微粒子の除去率を大
幅に上昇させることができる。(Function) In this way, if you use an air purifier that has activated carbon fibers and ion exchange fibers as adsorption parts, you can solve the problem of activated carbon fiber's low adsorption ability for basic gases and acidic gases, which has been a problem in the past. can be supplemented by ion exchange fibers. Furthermore, since the surface of the ion-exchange fiber is charged to e in the case of cation-exchange fiber and e in the case of anion-exchange fiber, it is possible to remove particles of the opposite sign by electrostatic adsorption, and the particle removal filter The load can be reduced or shouldered. Alternatively, if an ion exchange group is introduced into the particulate removal filter itself using radiation graft polymerization, the particulate removal rate can be significantly increased without increasing the differential pressure.
(実施例) 以下、本発明を実施例によって説明する。(Example) Hereinafter, the present invention will be explained by examples.
実施例1
直径的30amのポリプロピレン製不織布(目付100
g/m”) 2枚に加速電子線を窒素雰囲気で20M
rad照射した後、1枚にスチレンをグラフト重合し、
次いでスルホン化を行って、イオン交換容量3meg/
gの強酸性カチオン交換繊維よりなる不織布を得た。他
の1枚にはクロルメチルスチレンをグラフト重合し、次
いで4級アンモニウム化を行って、イオン交換容量2.
5 meg / Hの強塩基性アニオン交換繊維よりな
る不繊布を得た。Example 1 Polypropylene nonwoven fabric with a diameter of 30 am (fabric weight 100
g/m”) Accelerated electron beam is applied to two sheets at 20M in nitrogen atmosphere.
After rad irradiation, styrene was graft-polymerized on one sheet,
Next, sulfonation is performed to increase the ion exchange capacity to 3 meg/
A nonwoven fabric made of strongly acidic cation exchange fibers was obtained. The other one was graft-polymerized with chloromethylstyrene, and then converted into quaternary ammonium, resulting in an ion exchange capacity of 2.
A nonwoven fabric made of strongly basic anion exchange fibers having a strength of 5 meg/H was obtained.
以上2枚の不織布とさらに直径約25μmの活性炭素繊
維よりなる不織布(目付40g/m”)を直径5C11
の円形に切り、同内径のガラス製カラムに上からカチオ
ン交換繊維、アニオン交換繊維、活性炭素繊維の順に充
填した。このカラムに線香の煙を含有した空気を21/
l1inの流量で流したところ、除去率は重量で88%
であり、1時間後も除去率の低下は認められなかった。The above two nonwoven fabrics and a nonwoven fabric (weighing 40g/m") made of activated carbon fibers with a diameter of about 25μm are 5C11 in diameter.
The fibers were cut into circular shapes and packed into a glass column with the same inner diameter in the order of cation exchange fiber, anion exchange fiber, and activated carbon fiber from above. Air containing incense smoke is introduced into this column at 21/
When flowed at a flow rate of 1 inch, the removal rate was 88% by weight.
No decrease in removal rate was observed even after 1 hour.
比較例1
強酸および強塩基性イオン交換繊維のかわりに基材のポ
リプロピレン製繊維の不繊布を使用した以外は実施例1
と同様の条件で線香の煙を除去したところ、除去率は最
初から45%と低く、約15分経過した時点で18%に
まで低下した。Comparative Example 1 Example 1 except that a nonwoven fabric made of polypropylene fiber as a base material was used instead of the strong acid and strong basic ion exchange fiber.
When incense stick smoke was removed under similar conditions, the removal rate was low at 45% from the beginning, and dropped to 18% after about 15 minutes.
実施例2
実施例1と同様の条件のカラムを使用し、アンモニア1
0ppmを含む空気を2f/winで流したところ出口
のアンモニア濃度は1時間後も検出しなかった。Example 2 Using a column under the same conditions as Example 1, ammonia 1
When air containing 0 ppm was flowed at 2 f/win, the ammonia concentration at the outlet was not detected even after 1 hour.
比較例2
比較例1と同様のカラムに実施例2と同様のアンモニア
を含む空気を流したところ、出口のアンモニア濃度は最
初からapp−程度認められた。Comparative Example 2 When the same ammonia-containing air as in Example 2 was passed through a column similar to that in Comparative Example 1, the ammonia concentration at the outlet was found to be approximately app-− from the beginning.
(発明の効果)
小事業場や、一般家庭向けの従来の空気清浄器はコンパ
クトさ、静粛性、安全性など小型空気清浄器に必要な要
件を損うことなく、ガス成分および微粒子を同時に除去
することが困難であった。(Effect of the invention) Conventional air purifiers for small businesses and general households can simultaneously remove gas components and particulates without sacrificing the requirements necessary for small air purifiers, such as compactness, quietness, and safety. It was difficult to do so.
本発明により、除去対象ガス成分の範囲が飛擢的に増加
し、はぼあらゆるガス成分に対して有効となっただけで
なく、微粒子の除去効率も上昇し、快適な居住環境が容
易に得られるようになった。The present invention not only dramatically increases the range of gas components to be removed and becomes effective against almost all gas components, but also improves the removal efficiency of particulates, making it easier to create a comfortable living environment. Now you can.
Claims (1)
有する空気清浄器。 2、前記イオン交換繊維は放射線グラフト重合より製造
されたものである特許請求の範囲第1項記載の空気清浄
器。[Claims] 1. An air purifier having an adsorption section containing activated carbon fibers and ion exchange fibers. 2. The air purifier according to claim 1, wherein the ion exchange fiber is produced by radiation graft polymerization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63212105A JPH0259018A (en) | 1988-08-26 | 1988-08-26 | Air cleaner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63212105A JPH0259018A (en) | 1988-08-26 | 1988-08-26 | Air cleaner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0259018A true JPH0259018A (en) | 1990-02-28 |
Family
ID=16616964
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63212105A Pending JPH0259018A (en) | 1988-08-26 | 1988-08-26 | Air cleaner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0259018A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002096560A1 (en) * | 2001-05-25 | 2002-12-05 | Ebara Corporation | Anion exchangers and processes for preparing them |
| KR100514380B1 (en) * | 2002-07-24 | 2005-09-30 | 충남대학교산학협력단 | Fabrication of Organic-Inorganic Hybride Ion exchange Filter for Regenerable Gas Scrubber |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS556414A (en) * | 1978-06-26 | 1980-01-17 | Yazaki Corp | Manufacture of selective absorbing plane of solar heat collector |
| JPS6393327A (en) * | 1986-10-07 | 1988-04-23 | Ebara Res Co Ltd | Treatment of waste ozon |
| JPS63190619A (en) * | 1987-01-29 | 1988-08-08 | Ebara Res Co Ltd | Treatment of waste ozone |
-
1988
- 1988-08-26 JP JP63212105A patent/JPH0259018A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS556414A (en) * | 1978-06-26 | 1980-01-17 | Yazaki Corp | Manufacture of selective absorbing plane of solar heat collector |
| JPS6393327A (en) * | 1986-10-07 | 1988-04-23 | Ebara Res Co Ltd | Treatment of waste ozon |
| JPS63190619A (en) * | 1987-01-29 | 1988-08-08 | Ebara Res Co Ltd | Treatment of waste ozone |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002096560A1 (en) * | 2001-05-25 | 2002-12-05 | Ebara Corporation | Anion exchangers and processes for preparing them |
| KR100514380B1 (en) * | 2002-07-24 | 2005-09-30 | 충남대학교산학협력단 | Fabrication of Organic-Inorganic Hybride Ion exchange Filter for Regenerable Gas Scrubber |
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