JPH0538414A - Deodorizing filter - Google Patents

Deodorizing filter

Info

Publication number
JPH0538414A
JPH0538414A JP3196890A JP19689091A JPH0538414A JP H0538414 A JPH0538414 A JP H0538414A JP 3196890 A JP3196890 A JP 3196890A JP 19689091 A JP19689091 A JP 19689091A JP H0538414 A JPH0538414 A JP H0538414A
Authority
JP
Japan
Prior art keywords
activated carbon
weight
deodorizing filter
parts
deodorizing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP3196890A
Other languages
Japanese (ja)
Inventor
Shinro Katsura
真郎 桂
Jiro Fujimura
次郎 藤村
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP3196890A priority Critical patent/JPH0538414A/en
Publication of JPH0538414A publication Critical patent/JPH0538414A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a long-life deodorizing filter having a low pressure loss and a high deodorization capacity as compared with conventional deodorizing filters using an activated carbon structure of carbonized foamed plastics and having a bulk density at most 0.4g/cm<3> and a relatively short life. CONSTITUTION:A cured product of a composition comprising 100 pts.wt. of a resol-type phenolic resin (a), 1-100 pts.wt. of a lipophilic compound (b) which is liquid at room temperature and has a boiling point of 100 deg.C or higher, and 1-100 pts.wt. of a hydrophilic liquid compound (c) having a boiling point of 100 deg.C or higher is carbonized and activated to obtain a porous structure of activated carbon. The structures are allocated in the air passage of a deodorizing filter.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、空気清浄器やエアコン
などに用いられる脱臭フィルターに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing filter used in air purifiers, air conditioners and the like.

【0002】[0002]

【従来の技術】近年健康への関心、特に喫煙によって生
じる煙に対する問題意識が高まり、煙草の煙を装置的に
除去して室内を浄化したいという要請が強くなってき
た。このような要請に答えるべく、様々な空気清浄器が
販売されており、最近では脱臭性能を持たせたエアコン
も使用され初めている。ところで、空気清浄用のフィル
ターは、空気中の塵、微生物、煙などを除去する集塵型
と、悪臭成分を除去する脱臭型とに大別される。このう
ち脱臭フィルターには、従来より、活性炭素繊維、粒状
活性炭等が使用されていた。
2. Description of the Related Art In recent years, interest in health, particularly awareness of smoke caused by smoking, has increased, and there has been a strong demand to clean the room by removing cigarette smoke from a device. A variety of air purifiers have been sold to meet such demands, and recently, air conditioners having a deodorizing performance have begun to be used. By the way, air cleaning filters are roughly classified into a dust collecting type that removes dust, microorganisms, smoke, and the like in the air, and a deodorizing type that removes malodorous components. Of these, deodorizing filters have conventionally used activated carbon fibers, granular activated carbon, or the like.

【0003】しかし、活性炭素繊維を吸着剤として用い
たフィルターは、圧力損失が高く、しかも嵩密度が小さ
いため、脱臭フィルターとしての寿命が短いという問題
があった。また、粒状活性炭は嵩密度が高いけれども自
己形状保持性がないため、これを支持する構造物が必要
であり、その結果圧力損失が高くなるため、極めて低い
圧力損失が要求されるエアコン用のフィルターとして用
いることができなかった。
However, the filter using activated carbon fiber as an adsorbent has a problem that the life as a deodorizing filter is short because of high pressure loss and low bulk density. In addition, granular activated carbon has a high bulk density but does not have a self-shape-retaining property, so a structure supporting it is required. As a result, the pressure loss becomes high. Could not be used as.

【0004】他方、活性炭を担持したウレタンフォーム
を脱臭フィルターとした場合には、ウレタンフォームに
担持させた活性炭の量を多くすると、圧力損失が高くな
り、逆に活性炭の量を少なくすると圧力損失は低くでき
るものの、悪臭成分の吸着能力も低下し、脱臭フィルタ
ーとしての寿命が短くなり、短期間のうちに脱臭性能を
失う等の問題があった。
On the other hand, when a urethane foam carrying activated carbon is used as a deodorizing filter, increasing the amount of activated carbon supported on the urethane foam increases the pressure loss, and conversely, decreasing the amount of activated carbon causes the pressure loss to decrease. Although it can be lowered, there is a problem that the ability to adsorb malodorous components is also reduced, the life of the deodorizing filter is shortened, and the deodorizing performance is lost within a short period of time.

【0005】一般に脱臭フィルターの脱臭性能は、フィ
ルターを構成している活性炭の単位重量当りの吸着性能
x 活性炭の総重量に依存すると考えられている。ま
た、脱臭フィルターの圧力損失は気体流がフィルターを
通過する際のフィルターの抵抗の大きさ、言い替えると
通路の大きさ、つまり開口率に依存すると考えられてい
る。このため、これまで多くの試みがなされているがこ
れまでに満足のいく脱臭フィルターは得られていない。
It is generally considered that the deodorizing performance of a deodorizing filter depends on the adsorption performance per unit weight of the activated carbon constituting the filter x the total weight of the activated carbon. Further, it is considered that the pressure loss of the deodorizing filter depends on the magnitude of the resistance of the gas flow passing through the filter, in other words, the size of the passage, that is, the aperture ratio. Therefore, many attempts have been made so far, but no satisfactory deodorizing filter has been obtained so far.

【0006】本発明者らは先にプラスチック発泡体が炭
化、賦活されてなる活性炭構造物を脱臭フィルターに用
いると自己形状保持性があるため、開口率を大きくとる
ことができること、及び嵩密度が活性炭担持ウレタンフ
ォームや活性炭素繊維に比べて高いことから上記2つ要
求性能を満たし得ることを見いだし提案した。しかし、
この方法で安定的に製造しうる活性炭素多孔体の嵩密度
は0.4g/cm3 が限界であり、それ以上の嵩密度の活
性炭を工業的に製造しようとする場合、炭化、賦活工程
においてしばしば割れや爆裂を生じることが判明した。
The present inventors have found that when an activated carbon structure obtained by carbonizing and activating a plastic foam is used for a deodorizing filter, it has a self-shape-retaining property, so that it is possible to obtain a large aperture ratio and a bulk density. Since it is higher than activated carbon-supporting urethane foam and activated carbon fiber, we have found and proposed that the above two requirements can be satisfied. But,
The activated carbon porous material that can be stably produced by this method has a limit of 0.4 g / cm3 in bulk density, and when industrially producing activated carbon having a bulk density higher than that, it is often used in the carbonization and activation steps. It was found to crack and explode.

【0007】[0007]

【発明が解決しようとする問題点】本発明はより低い圧
力損失と高脱臭性能を有し、かつ寿命の長い脱臭フィル
ターにつき更に検討した結果、本発明に到達した。
The present invention has reached the present invention as a result of further studies on a deodorizing filter having lower pressure loss and high deodorizing performance and having a long life.

【0008】[0008]

【課題を解決するための手段】すなわち本発明は、レゾ
ール型フェノール樹脂(a) 100重量部、親油性で10
0℃以上の沸点を有する常温で液状の化合物(b) 1ない
し100重量部、親水性で100℃以上の沸点を有する
液状の化合物(c) 1ないし100重量部とからなる組成
物の硬化物を炭化、賦活して得た活性炭素多孔体構造物
が空気の通路に配設されていることを特徴とする脱臭フ
ィルターである。
Means for Solving the Problems That is, the present invention is based on 100 parts by weight of a resol type phenolic resin (a) and 10 parts by lipophilicity.
A cured product of a composition comprising 1 to 100 parts by weight of a liquid compound (b) having a boiling point of 0 ° C. or higher at room temperature and 1 to 100 parts by weight of a hydrophilic liquid compound (c) having a boiling point of 100 ° C. or higher. The deodorizing filter is characterized in that the activated carbon porous body structure obtained by carbonizing and activating is disposed in an air passage.

【0009】本発明を更に詳しく説明する。本発明で用
いられるレゾール型フェノール樹脂(a) とは、例えばフ
ェノール1モルとホルマリン1〜3モルをアルカリ性触
媒、例えばNaOH、KOH、Ca(OH)2、Ba
(OH)2、NH2(CH2CH3) 等の存在下で80〜
100℃に加熱することにより縮合させ、次いで固形分
が60〜80%になるまで減圧下で水を留去して得られ
た、常温での粘度が1000〜20000cpsの液体
である。
The present invention will be described in more detail. The resol type phenolic resin (a) used in the present invention means, for example, 1 mol of phenol and 1 to 3 mol of formalin as an alkaline catalyst such as NaOH, KOH, Ca (OH) 2, Ba.
In the presence of (OH) 2, NH2 (CH2CH3), etc.
It is a liquid having a viscosity at room temperature of 1000 to 20000 cps, which is obtained by condensing by heating at 100 ° C. and then distilling off water under reduced pressure until the solid content becomes 60 to 80%.

【0010】本発明における親油性で100℃以上の沸
点を有する常温で液状の化合物とは、例えば、オクタ
ン、ノナン、デカン、ウンデカン、ドデカン、灯油、鉱
物油、流動パラフィン等の直鎖状、または分岐状アルキ
ル化合物、トルエン、キシレン等の環状アルキレン化合
物等を挙げることができる。これらのうちでは、流動パ
ラフィンがレゾールとの粘度が近似し、混合した際安定
な水中油型分散系を作ることが出来るため、好ましい。
In the present invention, the lipophilic compound having a boiling point of 100 ° C. or higher and liquid at room temperature is, for example, a straight-chain compound such as octane, nonane, decane, undecane, dodecane, kerosene, mineral oil, liquid paraffin, or the like. Examples thereof include branched alkyl compounds and cyclic alkylene compounds such as toluene and xylene. Among these, liquid paraffin is preferable because it has a viscosity similar to that of resole and a stable oil-in-water dispersion system can be prepared when mixed.

【0011】この親油性化合物(b) のレゾール型フェノ
ール樹脂(a) 100重量部に対する配合量は通常1〜1
00重量部、好ましくは、10〜60重量部の範囲であ
る。親油性化合物(b) の量が少なすぎると、活性炭素多
孔体の多孔構造が少なくなって、吸着性能、液含浸性が
劣るようになる。また、炭化、賦活中に爆裂を生じ、活
性炭を製造しずらくなる。一方上記量を越えると、レゾ
ールの硬化特性が劣るようになる。また、炭化時に硬化
物の収縮が大きく、割れを生じ易くなる。
The lipophilic compound (b) is usually added in an amount of 1 to 1 with respect to 100 parts by weight of the resol type phenol resin (a).
00 parts by weight, preferably 10 to 60 parts by weight. If the amount of the lipophilic compound (b) is too small, the porous structure of the activated carbon porous body will be small, resulting in poor adsorption performance and liquid impregnation property. In addition, explosion occurs during carbonization and activation, making it difficult to produce activated carbon. On the other hand, when the amount exceeds the above range, the curing property of the resole becomes poor. In addition, the shrinkage of the cured product is large during carbonization, and cracking is likely to occur.

【0012】本発明における親水性で100℃以上の沸
点を有する液状の化合物(c) とは、例えば、重合度2以
上のオキシアルキレン化合物、例えば、ジエチレングリ
コール、トリエチレングリコール、分子量1000未満
のポリエチレングリコール、ジプロピレングリコール、
分子量1000未満のポリプロピレングリコール、ある
いはグリセリンを挙げることが出来る。これらのうちで
は、レゾールの粘度に比較的近く、かつ適度な相溶性が
ある点から分子量が400〜600のポリエチレングリ
コール、または、ジプロピレングリコールが好ましい。
The liquid compound (c) having a boiling point of 100 ° C. or higher in the present invention means, for example, an oxyalkylene compound having a degree of polymerization of 2 or higher, such as diethylene glycol, triethylene glycol, polyethylene glycol having a molecular weight of less than 1000. , Dipropylene glycol,
Examples thereof include polypropylene glycol having a molecular weight of less than 1000 or glycerin. Among these, polyethylene glycol having a molecular weight of 400 to 600 or dipropylene glycol is preferable because it is relatively close to the viscosity of the resole and has a suitable compatibility.

【0013】この親水性で100℃以上の沸点を有する
液状の化合物(c) のレゾール型フェノール樹脂(a) 10
0重量部に対する配合量は、通常1ないし100重量
部、好ましくは10〜60重量部の範囲である。親水性
化合物(c) の量が少なすぎると、親油性化合物(b) の分
散安定性が劣り、相分離を生じ易くなり、一方上記量を
越えるとレゾールの硬化特性が損なわれ、かつ親水性化
合物とレゾールとが相分離しやすくなる。
Resol type phenolic resin (a) 10 of this liquid compound (c) having a boiling point of 100 ° C. or higher
The compounding amount with respect to 0 part by weight is usually 1 to 100 parts by weight, preferably 10 to 60 parts by weight. When the amount of the hydrophilic compound (c) is too small, the dispersion stability of the lipophilic compound (b) is poor, and phase separation easily occurs. On the other hand, when the amount exceeds the above range, the curing property of the resole is impaired, and the hydrophilicity is high. The compound and the resole are easily phase separated.

【0014】本発明では親油性化合物(b) と、親水性化
合物(c) との配合比は、0.3〜3の範囲にすることが
好ましく、この範囲を外れると混合物が相分離し易くな
る。
In the present invention, the compounding ratio of the lipophilic compound (b) and the hydrophilic compound (c) is preferably in the range of 0.3 to 3. If it is out of this range, the mixture is likely to undergo phase separation. Become.

【0015】本発明でレゾール型フェノール樹脂(a) の
硬化に用いられる硬化剤としては、公知の種々の強酸性
化合物、例えば塩酸、硫酸、硝酸、リン酸、ピロリン
酸、ポリリン酸等の無機酸、フェノールスルホン酸、ベ
ンゼンスルホン酸、トルエンスルホン酸、メタクレゾー
ルスルホン酸等の有機酸、あるいはこれらの混合物を挙
げることが出来る。硬化剤の使用量は、通常レゾール型
フェノール樹脂100重量部に対し通常1〜30重量部
の範囲である。
As the curing agent used for curing the resol type phenolic resin (a) in the present invention, various known strongly acidic compounds, for example, inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, pyrophosphoric acid and polyphosphoric acid are used. , Organic acids such as phenolsulfonic acid, benzenesulfonic acid, toluenesulfonic acid, and metacresolsulfonic acid, or a mixture thereof. The amount of the curing agent used is usually in the range of 1 to 30 parts by weight with respect to 100 parts by weight of the resol type phenol resin.

【0016】本発明の脱臭フィルターに用いる活性炭素
多孔体構造物の原料として使用しうる樹脂組成物は、上
記成分を必須成分とするが、上記以外の少量の他の成
分、例えば活性炭素多孔体の気体吸着性能を向上するた
めの孔形成剤として、例えば、消失性フィラー、例えば
ポリエチレン、小麦粉等、細孔径を多様化するための他
の炭素材料、例えば活性炭、カーボンブラック、メソフ
ェーズピッチ粉、黒鉛粉等、賦活を促進するための金属
塩化合物等を含んでいてもよい。
The resin composition that can be used as a raw material for the activated carbon porous material structure used in the deodorizing filter of the present invention contains the above-mentioned components as essential components, but a small amount of other components other than the above, for example, activated carbon porous material. As a pore forming agent for improving the gas adsorption performance of, for example, fugitive fillers, such as polyethylene, flour, etc., other carbon materials for diversifying the pore size, such as activated carbon, carbon black, mesophase pitch powder, graphite It may contain a metal salt compound or the like for promoting activation, such as powder.

【0017】本発明では、上記レゾール型フェノール樹
脂(a) 親油性で100℃以上の沸点を有する常温で液状
の化合物(b) 、親水性で100℃以上の沸点を有する液
状の化合物(c) 必要に応じて更に界面活性剤、他の充填
剤等を配合したものを攪拌、混合し、ついで/または同
時に硬化剤を混合する。上記成分を混合する方法として
は、好ましくは、高速で回転する攪拌翼を持ったミキサ
ー等で連続的にまたは、回分的に逐次、または同時に混
合する方法を採用することができる。
In the present invention, the resol type phenolic resin (a) is a lipophilic compound having a boiling point of 100 ° C. or higher and liquid at room temperature (b), and a hydrophilic liquid compound having a boiling point of 100 ° C. or higher (c). If necessary, a mixture of a surfactant, other filler, etc. is stirred and mixed, and / or at the same time, a curing agent is mixed. As a method of mixing the above components, a method of continuously, batchwise, or simultaneously using a mixer having a stirring blade that rotates at high speed can be preferably used.

【0018】本発明の脱臭フィルターにおいては、攪
拌、混合された直後の樹脂組成物の粘度は通常5万cp
s以下の粘度となる。このような低粘度故に攪拌時に気
泡を混入せず、嵩密度等の点で均質な活性炭素多孔体構
造物を得ることができる。
In the deodorizing filter of the present invention, the viscosity of the resin composition immediately after stirring and mixing is usually 50,000 cp.
The viscosity is s or less. Due to such a low viscosity, bubbles can not be mixed during stirring, and a homogeneous activated carbon porous material structure can be obtained in terms of bulk density and the like.

【0019】本発明の脱臭フィルター用活性炭素多孔体
構造物ではこのようにして得た樹脂硬化物をそのまま、
もしくは切削して板状体とした後、非酸化性雰囲気下で
炭化して炭素多孔体とする。非酸化性雰囲気とは、例え
ば、Arガス、Heガス、N2 ガス、ハロゲンガス、ア
ンモニアガス、COガス、水素ガス、あるいはこれらの
混合ガス、水性ガス等をいう。炭化のための温度は、好
ましくは、500℃〜1200℃、特に600〜900
℃の範囲が好ましい。
In the activated carbon porous material structure for a deodorizing filter of the present invention, the resin cured product thus obtained is used as it is,
Alternatively, after cutting into a plate-like body, it is carbonized in a non-oxidizing atmosphere to form a carbon porous body. The non-oxidizing atmosphere means, for example, Ar gas, He gas, N2 gas, halogen gas, ammonia gas, CO gas, hydrogen gas, a mixed gas thereof, a water gas or the like. The temperature for carbonization is preferably from 500 ° C to 1200 ° C, especially from 600 to 900.
The range of ° C is preferred.

【0020】以上のようにして得られた炭素多孔体は、
更に賦活処理を施して活性化する。賦活工程は、炭化工
程に連続していてもよいし、炭化工程と別個の工程とし
てもよい。炭素多孔体の賦活は炭素多孔体を酸化性ガ
ス、または酸化性ガスと不活性ガスとの混合気体の雰囲
気下で加熱して行われる。加熱温度は600℃〜120
0℃、好ましくは750〜1000℃がよい。酸化性ガ
スとしては、公知の酸化性ガス、例えば、水蒸気、二酸
化炭素、酸素、空気等が用いられる。これらは通常調節
しやすいように不活性ガスN2 等と混合して用いる。
The carbon porous body obtained as described above is
Further, activation treatment is applied to activate. The activation step may be continuous with the carbonization step or may be a step separate from the carbonization step. Activation of the carbon porous body is performed by heating the carbon porous body in an atmosphere of an oxidizing gas or a mixed gas of an oxidizing gas and an inert gas. Heating temperature is 600 ° C-120
The temperature is 0 ° C, preferably 750 to 1000 ° C. As the oxidizing gas, known oxidizing gases such as water vapor, carbon dioxide, oxygen, air and the like are used. These are usually mixed with an inert gas such as N2 for easy control.

【0021】以上の方法により製造される活性炭素多孔
体は、嵩密度が好ましくは0.3g/cm3 以上、特に
0.4g/cm3 以上、0.7g/cm 3以下であり、
比表面積が700m2/g以上のものである。
The activated carbon porous material produced by the above method has a bulk density of preferably 0.3 g / cm 3 or more, particularly 0.4 g / cm 3 or more and 0.7 g / cm 3 or less,
It has a specific surface area of 700 m 2 / g or more.

【0022】本発明に係わる脱臭フィルターは、このよ
うな活性炭素多孔体を悪臭成分などを含んだ空気の流路
に配設したものである。
The deodorizing filter according to the present invention has such an activated carbon porous body disposed in a flow path of air containing a malodorous component and the like.

【0023】この活性炭素多孔体構造物の形状として
は、各種の形状が考えられ、例えば、板状、棒状、ある
いは、特願平1-96161 号明細書に記載されているような
穴を形成した板状などを挙げることができる。上記した
本発明で用いる樹脂組成物は粘度が低いため、このよう
な複雑な形状であっても容易に注型、その他の成形方法
で作製することができる。
Various shapes are conceivable as the shape of the activated carbon porous material structure, for example, a plate shape, a rod shape, or a hole as described in Japanese Patent Application No. 1-96161. The plate shape may be mentioned. Since the above-mentioned resin composition used in the present invention has a low viscosity, even such a complicated shape can be easily produced by casting or another molding method.

【0024】本発明に係わる脱臭フィルターでは、活性
炭素多孔体構造物は、特願平1-96157 号明細書に記載さ
れるように所定の間隔を開けて複数並べて構成されるグ
リッド構造としてもよい。このようなグリッド構造は、
製造が容易でかつ圧力損失が小さいため好ましく、例え
ば、風速が1m/sで圧力損失が0.5mmH2O以下と
いった基準に達し得る。
In the deodorizing filter according to the present invention, the activated carbon porous material structure may have a grid structure constituted by arranging a plurality of active carbon porous material structures at predetermined intervals as described in Japanese Patent Application No. 1-96157. .. Such a grid structure is
It is preferable because it is easy to manufacture and the pressure loss is small. For example, the standard that the wind speed is 1 m / s and the pressure loss is 0.5 mmH2O or less can be reached.

【0025】[0025]

【実施例】以下、実施例及び比較例により発明を更に具
体的に説明するが、本発明はその要旨を越えない限りこ
れらの実施例になんら制約されるものではない。 実施例1 {活性炭素多孔体構造物の製造}25℃における粘度が
4800cpsのレゾール型フェノール樹脂(略称レゾ
ール)100重量部に界面活性剤として、ヒマシ油のポ
リオキシエチレン2モル付加物の硫酸エステルナトリウ
ム塩5重量部、高沸点親水性化合物として、分子量が6
00のポリエチレングリコール(略称PEG)25重量
部、高沸点親油性化合物として、流動パラフィン(略称
流パラ)25重量部とを3段のピン羽根を有する攪拌器
で6000回転/分の速度で5分間充分に攪拌した。こ
の混合物の粘度は3500cpsであった。
The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples unless it exceeds the gist. Example 1 {Production of activated carbon porous material structure} 100 parts by weight of a resole-type phenol resin (abbreviation: resole) having a viscosity at 25 ° C. of 4800 cps was used as a surfactant, and a sulfuric acid ester of a polyoxyethylene 2 mol adduct of castor oil was used. 5 parts by weight of sodium salt, a high boiling point hydrophilic compound having a molecular weight of 6
25 parts by weight of polyethylene glycol (abbreviated as PEG) of 00 and 25 parts by weight of liquid paraffin (abbreviated as flow para) as a high-boiling lipophilic compound are stirred for 5 minutes at a speed of 6000 rpm with a stirrer having three stages of pin blades. Stir well. The viscosity of this mixture was 3500 cps.

【0026】この混合物に硬化剤としてパラトルエンス
ルホン酸20重量部を加えて同様の攪拌速度で1分間攪
拌、混合後70℃エアーオーブン中に5分間放置後取り
出し、間隔が3mmのロールの間を通過させた後、更に
エアーオーブン中で完全に硬化させることにより重合体
硬化物の板を製造した。
20 parts by weight of paratoluene sulfonic acid was added to this mixture as a curing agent and stirred at the same stirring speed for 1 minute. After mixing, the mixture was left in an air oven at 70 ° C. for 5 minutes and then taken out. After passing, the plate was cured completely in an air oven to prepare a plate of a polymer cured product.

【0027】この重合体硬化物の板を電気炉に入れてN
2 雰囲気で1.5℃/分の速度で700℃まで昇温し、
同温度で1時間保持後冷却した。以上の方法で得られた
炭素多孔体の板を厚さ3mmのセラミックファイバーボ
ードの箱に入れ、更にこの箱を電気炉に入れてN2 雰囲
気3℃/分の速度で900℃まで昇温し、ついでN2/
H2O=9/1の割合で賦活ガスを4時間導入後、冷却
して取り出した。このようにして、比表面積1100g
/m2、嵩密度0.45g/cm3 、厚さ2mmの活性
炭素多孔体Aの板を得た。
The plate of the polymer cured product was placed in an electric furnace and N
2 In an atmosphere, raise the temperature to 700 ° C at a rate of 1.5 ° C / min,
After holding at the same temperature for 1 hour, it was cooled. The carbon porous plate obtained by the above method was placed in a ceramic fiber board box having a thickness of 3 mm, and the box was placed in an electric furnace to raise the temperature to 900 ° C. at a rate of 3 ° C./min N 2 atmosphere, Then N2 /
After introducing the activating gas at a ratio of H2O = 9/1 for 4 hours, it was cooled and taken out. In this way, specific surface area of 1100g
/ M @ 2, bulk density 0.45 g / cm @ 3, and a plate of activated carbon porous body A having a thickness of 2 mm was obtained.

【0028】{フィルターの製造}上記板状活性炭素多
孔体から長さ100mm、幅10mmの板を切り出し、
プラスチックの枠体に10mmの間隔を開けて9本並べ
て100mmx100mmのグリット構造の脱臭フィルター
を製造した。
{Production of filter} A plate having a length of 100 mm and a width of 10 mm was cut out from the above plate-like activated carbon porous body,
Nine pieces were arranged at intervals of 10 mm on a plastic frame to manufacture a deodorizing filter having a grit structure of 100 mm x 100 mm.

【0029】{性能評価} 〔圧力損失〕チャンバー(内部寸法1mx1mx1.3
m)に上流及び下流が連結している67mmφの導管の一
部に形成されているフィルターホールダーに上記フィル
ター構造物をセットし、更にこのホールダーの上下流側
各々に圧力計を配設するとともに、チャンバーにこの内
部の空気を排出、循環する送風機を付設して、これらの
圧力計と送風機を作動することにより上記フィルター構
造物による圧力損失を下記のようにして測定した。すな
わち、上記ホールダーにフィルター構造物を装着した
後、送風機を駆動してチャンバー内の空気を100cm/
sec の速度で導管を通って排出し、フィルターの上流側
と下流側の圧力を測定し、圧力差を圧力損失(mmH2
O) で示すことにより圧力損失を測定した。
{Performance Evaluation} [Pressure Loss] Chamber (Internal dimensions 1 mx 1 mx 1.3
The filter structure is set in a filter holder formed in a part of a 67 mmφ conduit in which the upstream and the downstream are connected to m), and a pressure gauge is arranged on each of the upstream and downstream sides of the holder, and An air blower for discharging and circulating the air inside the chamber was attached to the chamber, and the pressure loss due to the filter structure was measured as follows by operating these pressure gauges and blowers. That is, after mounting the filter structure on the holder, the blower is driven to move the air in the chamber to 100 cm /
Discharge through the conduit at a speed of sec, measure the pressure on the upstream side and the downstream side of the filter, and measure the pressure difference (mmH2
O) was used to measure the pressure loss.

【0030】〔脱臭性能〕チャンバー内にアセトアルデ
ヒドを系内の濃度が100ppm になるよう導入し、送風
機を作動させて系内の空気を循環する。送風機を停止後
脱臭フィルターをフィルターホールダーに取り付け、直
ちに再び送風機を作動させる。10分経過後のチャンバ
ー内のアセトアルデヒドの濃度をガス検知管により求
め、下記式より初期脱臭率を測定した。 初期脱臭率=(試験前の濃度−10分経過後の濃度)/
試験前の濃度x100 上記脱臭試験の30分経過後に送風機を止め、脱臭フィ
ルターを取り外した後に再び系内にアセトアルデヒドを
導入して、系内のアセトアルデヒドの濃度を100ppm
にした後、試験に供した脱臭フィルターを再び取り付
け、前回同様に試験する。この試験を更にもう一度繰り
返した後、30分後のアセトアルデヒドの濃度をガス検
知管により求め、上記と同様の式で長期脱臭率を求め
た。以上の測定結果を表.1に示す。
[Deodorizing Performance] Acetaldehyde is introduced into the chamber so that the concentration in the system becomes 100 ppm, and the air blower is operated to circulate the air in the system. After stopping the blower, attach the deodorizing filter to the filter holder, and immediately restart the blower. The concentration of acetaldehyde in the chamber after 10 minutes had elapsed was determined by a gas detector tube, and the initial deodorization rate was measured by the following formula. Initial deodorization rate = (concentration before test−concentration after 10 minutes) /
Concentration before test x100 After 30 minutes of the above deodorization test, stop the blower, remove the deodorizing filter, and then introduce acetaldehyde into the system again to adjust the acetaldehyde concentration in the system to 100 ppm.
After that, attach the deodorizing filter used in the test again and repeat the test as before. After repeating this test once again, the concentration of acetaldehyde after 30 minutes was determined by a gas detector tube, and the long-term deodorization rate was determined by the same formula as above. The above measurement results are shown in the table. Shown in 1.

【0031】実施例2 実施例1のフィルター構造物において、スリットの間隔
を15mmに、使用する活性炭素多孔体グリッドの本数
を6本とする以外は実施例1と同様にして、性能評価を
行った。結果を表.1に示す。
Example 2 In the filter structure of Example 1, the performance was evaluated in the same manner as in Example 1 except that the slit spacing was 15 mm and the number of activated carbon porous grids used was 6. It was The results are shown in the table. Shown in 1.

【0032】実施例3 実施例1で用いた原料樹脂組成物の代わりに、実施例1
で用いたレゾール100重量部、ヒマシ油のポリオキシ
エチレン2モル付加物の硫酸エステルナトリウム塩5重
量部、、分子量が600のPEG25重量部、流動パラ
25重量部、及びメソフェーズピッチ粉50重量部とか
らなる組成物を用いる以外は、実施例1と同様に行い、
活性炭素多孔体Bを得た。この活性炭素多孔体から実施
例1と同様にして脱臭フィルターを作製し、同様にして
フィルターの性能を評価した。結果を表.1に示す。
Example 3 Instead of the raw material resin composition used in Example 1, Example 1 was used.
100 parts by weight of the resole used in Example 5, 5 parts by weight of sodium sulfate of a polyoxyethylene 2 mol adduct of castor oil, 25 parts by weight of PEG having a molecular weight of 600, 25 parts by weight of liquid para, and 50 parts by weight of mesophase pitch powder. Example 1 was repeated except that the composition consisting of
Activated carbon porous material B was obtained. A deodorizing filter was produced from this activated carbon porous material in the same manner as in Example 1, and the performance of the filter was evaluated in the same manner. The results are shown in the table. Shown in 1.

【0033】比較例1 脱臭フィルターとして市販されている、粉末活性炭が担
持されたウレタンフォーム(UF)を用いて実施例1と
同様の方法で圧力損失、脱臭性能を測定した。結果を表
1に示す。
Comparative Example 1 Using a commercially available urethane foam (UF) carrying powdered activated carbon as a deodorizing filter, pressure loss and deodorizing performance were measured in the same manner as in Example 1. The results are shown in Table 1.

【0034】比較例2 脱臭フィルターとして市販されている、活性炭素繊維
(ACF)を素材とした脱臭フィルターを用いて実施例
1と同様の方法で圧力損失、脱臭性能を測定した。結果
を表1に示す。
Comparative Example 2 Using a commercially available deodorizing filter made of activated carbon fiber (ACF) as a deodorizing filter, pressure loss and deodorizing performance were measured in the same manner as in Example 1. The results are shown in Table 1.

【0035】比較例3 実施例1で用いた原料樹脂組成物の代わりに、実施例1
で用いたレゾール100重量部、硬化剤としてパラトル
エンスルホン酸10重量部、及び発泡剤としてフロン1
23b 2重量部とからなる組成物を原料として攪拌し
た組成物を木型内に注入し、その木型を80℃ エアー
オーブン中に1時間放置して、発泡成形させ、硬化後に
ブロック状硬化物を切断して厚さ7mmの板にする以外
は実施例1と同様に行い、活性炭素多孔体Cを得た。こ
の活性炭素多孔体から実施例1と同様にして脱臭フィル
ターを作り、その性能を評価した。結果を表.1に示
す。
Comparative Example 3 Instead of the raw material resin composition used in Example 1, Example 1 was used.
100 parts by weight of the resol used in step 1, 10 parts by weight of paratoluene sulfonic acid as a curing agent, and CFC 1 as a blowing agent.
23b 2 parts by weight of the composition as a raw material was stirred and poured into a wooden mold, and the wooden mold was left in an air oven at 80 ° C. for 1 hour to be foam-molded and then cured into a block-like cured product. Was cut in the same manner as in Example 1 except that a plate having a thickness of 7 mm was cut to obtain an activated carbon porous body C. A deodorizing filter was made from this activated carbon porous material in the same manner as in Example 1, and its performance was evaluated. The results are shown in the table. Shown in 1.

【0036】[0036]

【表1】 [Table 1]

【0037】[0037]

【発明の効果】本発明の脱臭フィルターは、原料樹脂組
成物としてレゾール/親油性化合物/親水性化合物から
なる組成物用いることにより、流動性が優れた組成物が
得られるため、薄肉の樹脂シートが成形でき、従って厚
さ1mm程度の薄肉や様々な形状とすることができる。
従って、従来より厚さの薄いフィルターであることがで
きる。また、本発明の脱臭フィルターは、本発明で用い
る活性炭素多孔体の嵩比重が高いため、脱臭性能、特に
長期の脱臭性能に優れる。また、主たる構成材料の活性
炭素多孔体の強度が大きいため、強度上の問題を生じな
い。以上の点から本発明の脱臭フィルターは従来のもの
に比べよりコンパクトになり、エアコン、空気清浄器等
において場所をとらないという利点を有する。
INDUSTRIAL APPLICABILITY In the deodorizing filter of the present invention, a composition having excellent fluidity can be obtained by using a composition comprising a resole / lipophilic compound / hydrophilic compound as a raw material resin composition, so that a thin resin sheet is obtained. Can be molded, and thus can be formed into a thin wall having a thickness of about 1 mm and various shapes.
Therefore, the filter can be thinner than before. Further, the deodorizing filter of the present invention is excellent in deodorizing performance, particularly long-term deodorizing performance, because the activated carbon porous material used in the present invention has a high bulk specific gravity. In addition, since the activated carbon porous body, which is the main constituent material, has a large strength, no strength problem occurs. From the above points, the deodorizing filter of the present invention is more compact than conventional ones, and has an advantage that it does not take up much space in an air conditioner, an air purifier or the like.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 レゾール型フェノール樹脂(a) 100重
量部、親油性で100℃以上の沸点を有する常温で液状
の化合物(b) 1ないし100重量部、親水性で100℃
以上の沸点を有する液状の化合物(c) 1ないし100重
量部とからなる組成物の硬化物を炭化、賦活して得た活
性炭素多孔体構造物が空気の通路に配設されていること
を特徴とする脱臭フィルター。
1. Resol type phenolic resin (a) 100 parts by weight, lipophilic compound (b) 1 to 100 parts by weight which is liquid at room temperature and has a boiling point of 100 ° C. or more, hydrophilic 100 ° C.
The activated carbon porous structure obtained by carbonizing and activating the cured product of the composition comprising 1 to 100 parts by weight of the liquid compound (c) having the above boiling point is disposed in the air passage. Characteristic deodorizing filter.
JP3196890A 1991-08-06 1991-08-06 Deodorizing filter Pending JPH0538414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3196890A JPH0538414A (en) 1991-08-06 1991-08-06 Deodorizing filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3196890A JPH0538414A (en) 1991-08-06 1991-08-06 Deodorizing filter

Publications (1)

Publication Number Publication Date
JPH0538414A true JPH0538414A (en) 1993-02-19

Family

ID=16365353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3196890A Pending JPH0538414A (en) 1991-08-06 1991-08-06 Deodorizing filter

Country Status (1)

Country Link
JP (1) JPH0538414A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0755328A1 (en) * 1994-04-15 1997-01-29 Corning Incorporated Activated carbon honeycombs having varying adsorption capacities and method of making same
EP0774296A3 (en) * 1995-11-17 1997-07-30 Corning Inc Method of making activated carbon bodies having improved adsorption properties
EP0930966A4 (en) * 1996-10-11 1999-08-11
US6187713B1 (en) 1996-10-31 2001-02-13 Corning Incorporated Method of making activated carbon bodies having improved adsorption properties
JP2009520173A (en) * 2005-12-19 2009-05-21 ベール ゲーエムベーハー ウント コー カーゲー Sorption heat transfer body wall and sorption heat transfer body
EP1109738A4 (en) * 1998-07-20 2010-08-11 Corning Inc Method of making mesoporous carbon using pore formers

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0755328A1 (en) * 1994-04-15 1997-01-29 Corning Incorporated Activated carbon honeycombs having varying adsorption capacities and method of making same
EP0755328A4 (en) * 1994-04-15 1997-11-12 Corning Inc Activated carbon honeycombs having varying adsorption capacities and method of making same
EP0774296A3 (en) * 1995-11-17 1997-07-30 Corning Inc Method of making activated carbon bodies having improved adsorption properties
EP0930966A4 (en) * 1996-10-11 1999-08-11
US6187713B1 (en) 1996-10-31 2001-02-13 Corning Incorporated Method of making activated carbon bodies having improved adsorption properties
EP1109738A4 (en) * 1998-07-20 2010-08-11 Corning Inc Method of making mesoporous carbon using pore formers
JP2009520173A (en) * 2005-12-19 2009-05-21 ベール ゲーエムベーハー ウント コー カーゲー Sorption heat transfer body wall and sorption heat transfer body

Similar Documents

Publication Publication Date Title
EP0323096A2 (en) Production of articles of bonded particulate material and binder compostions for use therein
JP5894926B2 (en) Phenolic resin foam board
AU2012293256B2 (en) Foamable resol-type phenol resin molding material and phenol resin foam
RU2008139983A (en) CATALYST AND HYDROCLEANING METHOD
JPH0538414A (en) Deodorizing filter
Gong et al. A simple preparation method and characterization of epoxy reinforced microporous phenolic open-cell sound absorbent foam
KR20210146933A (en) A method for producing a porous carbonaceous material, a porous carbonaceous material, and a catalyst formed from the material
CN101076557A (en) Tough-increased phenolic foam
KR20020064170A (en) A molded product of active carbon and a method for production thereof
DE102006051404A1 (en) Use of open-cell foams in vacuum cleaners
JP5246728B2 (en) Production method of phenol resin, phenol resin, phenol resin carbonized material, conductive resin composition, electrode for secondary battery, carbon material for electrode, adsorbent for medicine, electric double layer capacitor polarizable electrode
CN101967254B (en) Medicinal microporous sponge and preparation method thereof
JPH0538415A (en) Filter for decomposing ozone
JP4994860B2 (en) Porous molded body, production method thereof and use thereof
JP2000239336A (en) Low-density cured spherical phenolic resin
JPH0620546B2 (en) Molecular sieving carbon and its manufacturing method
JPH0543345A (en) Production of active carbon porous body
JPH0543348A (en) Production of active carbon porous body
JPH03127607A (en) Activated carbon structure
JPH0543214A (en) Production of porous activated carbon structure
KR101593495B1 (en) Manufacturing Method of Carbon Block Filter for Cleaning Air
JPH02273169A (en) Filter material for tobacco
JPH03329B2 (en)
RU2291103C2 (en) Method of production of the open-porous glass-carbonic material
JPH0543347A (en) Production of active carbon porous body