JPH02160042A - Air cleaner - Google Patents

Air cleaner

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Publication number
JPH02160042A
JPH02160042A JP63314475A JP31447588A JPH02160042A JP H02160042 A JPH02160042 A JP H02160042A JP 63314475 A JP63314475 A JP 63314475A JP 31447588 A JP31447588 A JP 31447588A JP H02160042 A JPH02160042 A JP H02160042A
Authority
JP
Japan
Prior art keywords
aniline
activated carbon
phosphoric acid
impregnated
active 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
JP63314475A
Other languages
Japanese (ja)
Other versions
JPH0616838B2 (en
Inventor
Shuzo Tokumitsu
修三 徳満
Noboru Naruo
成尾 昇
Yasushi Takano
鷹野 泰
Teruhiro Okada
輝弘 岡田
Hiroshi Uchida
浩史 内田
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
Panasonic Holdings Corp
Original Assignee
Kuraray Chemical Co Ltd
Matsushita Electric Industrial 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, Matsushita Electric Industrial Co Ltd filed Critical Kuraray Chemical Co Ltd
Priority to JP63314475A priority Critical patent/JPH0616838B2/en
Publication of JPH02160042A publication Critical patent/JPH02160042A/en
Publication of JPH0616838B2 publication Critical patent/JPH0616838B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To enhance odorous component adsorbability and durability by using a mixture composed of an active carbon carrying aniline phosphate salt and active carbon carrying phosphoric acid or further a mixture composed thereof and non-carrying active carbon, etc., as the air cleaner. CONSTITUTION:The air cleaner is formed by adding and mixing the active carbon carrying the aniline phosphate salt and the active carbon carrying the phosphoric acid and if desired, the non-carrying active carbon. The air cleaner is also formed by mixing the active carbon carrying the aniline phosphate salt, the active carbon carrying the phosphoric acid and the active carbon carrying the aniline. Further, the air cleaner is formed by mixing the active carbon carrying the aniline phosphate salt and aniline, the active carbon carrying the phosphoric acid and if desired, the non-carrying active carbon. These air cleaners have the excellent adsorbing power of all the odorous components and have the well balanced performance in the sustaining property of the adsorbing power.

Description

【発明の詳細な説明】 産業上の利用分野 本発明はオフィス、家庭等の室内空気の臭気除去に有効
な空気浄化剤 ≠壬賽善→44に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an air purifying agent≠Misaisen→44 that is effective for removing odor from indoor air in offices, homes, and the like.

従来の技術 オフィス、家庭等の生活空間で発生する悪臭には、組成
的にはアセトアルデヒドなどの低級脂肪族アルデヒド、
アンモニア、低級アミン、法化水素、硫化水素、メチル
メルカプタン等が含まれている。その代表的なものとし
て、たばこを喫煙したときに発生する臭気がある。
Conventional technology The bad odors that occur in offices, homes, and other living spaces are composed of lower aliphatic aldehydes such as acetaldehyde,
Contains ammonia, lower amines, hydrogen chloride, hydrogen sulfide, methyl mercaptan, etc. A typical example is the odor that occurs when smoking cigarettes.

一方、−船釣に空気浄化剤としては、活性炭が良く使用
される。活性炭は無極性吸着剤として極めて優れた吸着
性を有する特異な材質で、はとんどすべてのガス状物質
に対して高い吸着性を示す。
On the other hand, activated carbon is often used as an air purifying agent for boat fishing. Activated carbon is a unique material that has extremely excellent adsorption properties as a non-polar adsorbent, and exhibits high adsorption properties for almost all gaseous substances.

しかし、通常の活性炭では上記悪臭のなかで低級脂肪族
アルデヒドやアンモニア、低級アミンを除去することが
困難である。
However, with ordinary activated carbon, it is difficult to remove lower aliphatic aldehydes, ammonia, and lower amines among the above-mentioned foul odors.

上記活性炭の欠点を解決する方法として、活性炭にアニ
リンを添着した吸着剤は特公昭60−54095号公報
に開示され、活性炭100部にア= 1771〜30部
を添着し九ものは気相中のアセトアルデヒドなどの低級
脂肪族アルデヒドの吸着に有効であると記載されている
As a method to solve the above-mentioned drawbacks of activated carbon, an adsorbent in which activated carbon is impregnated with aniline is disclosed in Japanese Patent Publication No. 60-54095, in which 100 parts of activated carbon is impregnated with 30 parts of A=1771 to 30 parts. It is described as being effective in adsorbing lower aliphatic aldehydes such as acetaldehyde.

さらに、活性炭等の多孔性物質に硫酸やリン酸などの無
機酸を添着させて脱臭剤に使用するものは既に公知の技
術であり、アンモニア及び低級アミンの優れた吸着剤と
して実用化されている。
Furthermore, the use of porous materials such as activated carbon as impregnated with inorganic acids such as sulfuric acid and phosphoric acid as deodorizers is already a well-known technology and has been put into practical use as an excellent adsorbent for ammonia and lower amines. .

発明が解決しようとする課題 しかして、上記糧々の活性炭を混合することによって、
生活空間の悪臭はおおよそ除去できる。
Problem to be Solved by the Invention However, by mixing the above-mentioned types of activated carbon,
Most bad odors in living spaces can be removed.

しかし、上記従来の活性炭のなかで、アニリンを添着し
た活性炭は耐久性において課題があった。
However, among the above conventional activated carbons, activated carbon impregnated with aniline has a problem in durability.

それは、アニリンの活性炭への吸着保持力が弱いため、
多量に添着しても熱などが加わることKよって脱離し、
低級脂肪族アルデヒドの吸着力が弱くなるという課題が
あった。
This is because the adsorption and retention power of aniline to activated carbon is weak.
Even if a large amount is attached, it will detach due to the addition of heat, etc.
There was a problem that the adsorption power of lower aliphatic aldehydes became weaker.

そこで、本発明はいかなる臭気も除去でき、且つ耐久性
に優れた空気浄化剤に≠拐1−−組←起を得ることt訃
十力目的と している。
Therefore, the object of the present invention is to create an air purifying agent that can remove any odor and has excellent durability.

課題を解決するための手段 これらの目的を達成するために本発明は、リン酸アニリ
ン塩を添着した活性炭、リン酸を添着した活性炭を混合
せしめてなる空気浄化剤、リン酸アニリン塩を添着した
活性炭、リン酸を添着した活性炭および無添着活性炭を
混合せしめてなる空気浄化剤、リン酸アニ177塩を添
着した活性炭、リン酸を添着した活性炭およびアニリン
を添着した活性炭を混合せしめてなる空気浄化剤、リン
酸アニリン塩とアニリンの双方を添着した活性炭、リン
酸を添着した活性炭を混合せしめてなる空気浄化剤、リ
ン酸アニリン塩とアニリンの双方を添着した活性炭、リ
ン酸を添着した活性炭および無添着活性炭を混合せしめ
てなる空気浄化剤、あるいはリン酸アニリン塩とアニリ
ンの双方を添着した活性炭、リン酸を添着した活性炭お
よびアニリンを添着した活性炭を混合せしめてなる空気
浄化剤としたものである。
Means for Solving the Problems In order to achieve these objects, the present invention provides activated carbon impregnated with aniline phosphoric acid salt, an air purifying agent made by mixing activated carbon impregnated with phosphoric acid, and an air purifying agent impregnated with aniline phosphoric acid salt. Air purification agent made by mixing activated carbon, activated carbon impregnated with phosphoric acid, and activated carbon without impregnation; Air purification made by mixing activated carbon impregnated with ani-177 phosphate, activated carbon impregnated with phosphoric acid, and activated carbon impregnated with aniline. activated carbon impregnated with both phosphoric acid aniline salt and aniline, air purifying agent made by mixing activated carbon impregnated with phosphoric acid, activated carbon impregnated with both phosphoric acid aniline salt and aniline, activated carbon impregnated with phosphoric acid, and An air purifying agent made by mixing non-impregnated activated carbon, or an air purifying agent made by mixing activated carbon impregnated with both phosphoric acid aniline salt and aniline, activated carbon impregnated with phosphoric acid, and activated carbon impregnated with aniline. be.

作用 リン酸ア= リン塩を添着した活性炭においては、アニ
リンとアルデヒドの付加反応により低級脂肪族アルデヒ
ドの吸着性にすぐれ、またアニリンガスの脱離が無いた
め、その耐久性においてもすぐれている。さらにリン酸
アニリン塩は活性炭のマクロポア、割れ目あるいは表面
部分に添着されるので、ミクロポアの活性の低下が少な
く、炭化水素の吸着性にも比較的硬れている。リン酸ア
ニ+7ン塩の添着量が多すぎて約12重量・%を越える
とアルデヒドの吸着速度が徐々に遅くなり、また約6重
量%を越えるとPHが酸性になって硫化水素、メチルメ
ルカプタンの吸着性あるいは触媒分解性が悪くなる。そ
こで、アルデヒドの吸着能力を東に良くしたい場合は、
更にアニリンを添着するか、もしくはアニリンを少量添
着した活性炭を別に混合する。一方硫化水素、メチルメ
ルカプタンの吸着性あるいは触媒分解性や、炭化水素の
吸着性を更に良くしたい場合は、無添着活性炭かアユ1
,1ンを少量添着した活性炭を別に混合する。リン酸を
添着した活性炭は、リン酸との中和反応によりアンモニ
アや低級アミンの吸着性に優れている。したがって、こ
れらの活性炭を対象とする臭気の性質に応じて混合する
ことによって、あらゆる臭気を除去でき、優れた高い性
能を長く持続できるものである。またこれらは、吸着速
度が早いので空気浄化フィルタに有効であり、これを使
った空気清浄装置は優れた脱臭性能とすることができる
Activated carbon impregnated with functional phosphoric acid salt has excellent adsorption properties for lower aliphatic aldehydes due to the addition reaction between aniline and aldehyde, and also has excellent durability because there is no desorption of aniline gas. Furthermore, since the phosphoric acid aniline salt is attached to the macropores, cracks, or surface portions of the activated carbon, there is little reduction in the activity of the micropores, and the adsorption of hydrocarbons is relatively hard. If the amount of phosphoric acid anion+7 salt impregnated is too large and exceeds about 12% by weight, the adsorption rate of aldehyde will gradually slow down, and if it exceeds about 6% by weight, the pH will become acidic and hydrogen sulfide and methyl mercaptan will be absorbed. adsorption or catalytic decomposition become worse. Therefore, if you want to improve the adsorption capacity of aldehyde,
Furthermore, aniline is impregnated, or activated carbon impregnated with a small amount of aniline is separately mixed. On the other hand, if you want to improve the adsorption or catalytic decomposition of hydrogen sulfide and methyl mercaptan, or the adsorption of hydrocarbons, use unimpregnated activated carbon or Ayu 1.
, 1 ton of activated carbon impregnated with a small amount is separately mixed. Activated carbon impregnated with phosphoric acid has excellent adsorption properties for ammonia and lower amines due to the neutralization reaction with phosphoric acid. Therefore, by mixing these activated carbons according to the nature of the target odor, all kinds of odors can be removed and excellent high performance can be maintained for a long time. Furthermore, these are effective in air purification filters because of their fast adsorption speed, and air purification devices using them can have excellent deodorizing performance.

実施例 以下実施例を挙げて具体的に本発明を説明するが、これ
らの実施例は本発明を何等限定するものではない。
EXAMPLES The present invention will be specifically explained with reference to Examples below, but these Examples are not intended to limit the present invention in any way.

実施例1 ここで使用する活性炭は、通常1督あたり数百dl)る
いはそれ以上の大きな表面積を有し、高い吸着性を示す
法案材料であれば広範囲に使用できる。活性炭の原料は
通常椰子殻又は木材等の炭化物あるいは右脚が使用され
るがいずれでも嵐い。
Example 1 The activated carbon used here usually has a large surface area of several hundred dl per cylinder or more, and can be used in a wide range of materials as long as it exhibits high adsorption properties. The raw material for activated carbon is usually coconut shells, charred materials such as wood, or carbonized charcoal, but either method is acceptable.

又賦活法も水蒸気あるいは二酸化炭素により高温で又は
塩化亜鉛、リン歳、濃硫酸処理等いづれの方法により得
られたものでもよいが、ここでは水蒸気賦活法が望まし
い。また形状は破砕炭、造粒炭あるいは顆粒法のいづれ
でも効果は認められるが、圧損失及び入替え等取り扱い
上、造粒炭または活性炭を添着したシート状吸着層が便
利である。
Also, the activation method may be one obtained by using steam or carbon dioxide at high temperature, or by treatment with zinc chloride, phosphorus, concentrated sulfuric acid, etc., but the steam activation method is preferred here. Furthermore, although the effect can be recognized in any shape such as crushed coal, granulated coal, or granulation method, a sheet-like adsorption layer impregnated with granulated carbon or activated carbon is convenient in terms of handling such as pressure loss and replacement.

次にここで使用する第1表に示した活性炭の調整方法に
ついて説明する。A1−A3の活性炭は、通常の吸着能
力を持つ6〜12メツシユの破砕状椰子殻活性炭100
部に対しリン酸アニリン塩結晶を100メツシユ以下に
粉砕した微粉末6部、12部、15部をそれぞれ水20
部に懸濁させた液を作り、活性炭を良くかき交ぜながら
リン酸アニリン塩の懸濁液を少量づつ良くかき交ぜふり
かけた。その後添着した活性炭を、温度120℃の乾燥
機中で3時間乾燥した。A4はA1−A3と同じ方法で
リン酸アニリン塩を添着したものを密閉した容器に取り
、アニリンを4部ふりかけ、密閉状部で温度40℃の恒
温槽[40時間放置し、アニリンを活性炭全体に平均的
に添着させた。次に比較試料として活性炭100部を密
閉した容器に取り、アニリンを4部、8部ふりかけ、密
閉状態で温度40℃の恒温槽に40時間放置し、アニリ
ンを活性炭全体に平均的に添着させ九B1、B2と無添
着炭B3を用意した。これらの試料を用いて下記の実験
を行った。
Next, a method for preparing the activated carbon shown in Table 1 used here will be explained. Activated carbon of A1-A3 is crushed coconut shell activated carbon 100 of 6 to 12 meshes with normal adsorption capacity.
1 part, 6 parts, 12 parts, and 15 parts of fine powder obtained by crushing phosphoric acid aniline salt crystals to 100 mesh or less, respectively, and 20 parts of water.
A suspension of phosphoric acid aniline salt was prepared little by little while stirring the activated carbon. Thereafter, the attached activated carbon was dried for 3 hours in a dryer at a temperature of 120°C. For A4, put the phosphoric acid aniline salt impregnated in the same way as A1-A3 into a sealed container, sprinkle 4 parts of aniline, and leave it in a thermostatic bath at a temperature of 40°C in the sealed container for 40 hours. was attached on average. Next, as a comparison sample, 100 parts of activated carbon was placed in a sealed container, sprinkled with 4 parts and 8 parts of aniline, and left in a sealed state in a constant temperature bath at a temperature of 40°C for 40 hours. B1, B2 and non-impregnated charcoal B3 were prepared. The following experiment was conducted using these samples.

第  1  表 カラムとダイヤ7−yムポングとを連結した循環系の吸
着速度測定装置を用いた。濃度40〜70ppmのアセ
トアルデヒドガスあるいは硫化水素ガスを前記ガラス瓶
に調整し、試料2.8gをカラムに充填する。流速45
 cs / Beeでガスを循環し活性炭に吸着させる
。一定時間毎にガラス瓶内のガスをサンプリングして、
アセトアルデヒドの濃度をFより (flame 1o
nization detector )付き高感度ガ
スクロマトグラフで、硫化水素はFPD(flame 
photometri、c d@tector )付き
高感度ガスクロマトグラフで分析した。7つの試料にり
いてのアセトアルデヒドおよび硫化水素の吸着減衰曲線
を第1図、第2図に示す。アセトアルデヒドの吸着速度
はアニリン添着よりもリン酸アニリン塩添着のほうが早
いが、リン酸アニリン塩15wt%よりも19wt%の
ほうが早い。硫化水素の吸着速度はアニリン添着よりも
リン酸アニリン塩添着の方が遅く、特KQwt%を越え
ると急に遅くなる。
Table 1 A circulation system adsorption rate measuring device was used in which a column and a 7-diameter pump were connected. Acetaldehyde gas or hydrogen sulfide gas having a concentration of 40 to 70 ppm is prepared in the glass bottle, and 2.8 g of the sample is packed into the column. flow rate 45
Gas is circulated using cs/bee and adsorbed onto activated carbon. Sample the gas in the glass bottle at regular intervals,
The concentration of acetaldehyde is determined from F (flame 1o
Hydrogen sulfide is detected using a highly sensitive gas chromatograph equipped with a FPD (flame detector).
It was analyzed using a high-sensitivity gas chromatograph equipped with photometry (CD@tector). Figures 1 and 2 show the adsorption decay curves of acetaldehyde and hydrogen sulfide for seven samples. The adsorption rate of acetaldehyde is faster when impregnated with aniline phosphate than when aniline is impregnated, but it is faster when aniline phosphate is impregnated with 19 wt% than with 15 wt%. The adsorption rate of hydrogen sulfide is slower when impregnated with aniline phosphate than when impregnated with aniline, and becomes suddenly slower when KQwt% is exceeded.

実施例2 実施例1で調整したA2.A4.B2の試料を用いてア
ニリンの脱離性を調べた。温度50°Cの恒温層内にセ
ットした内径50鍾のガラス管力2ムに試料100sを
充填し、温度50℃の7レツシエ空気を流量470 w
/ minで通し、出口ガス中のアニリンガス濃度をF
ID付き高感度ガスクロマトグラフで測定した結果を図
3に示す。アニリンgwt%添着したB2から脱離する
アニリン量が圧倒的に多い。
Example 2 A2. prepared in Example 1. A4. The removability of aniline was investigated using sample B2. A 2mm glass tube with an inner diameter of 50mm set in a thermostatic chamber at a temperature of 50°C was filled with 100 seconds of the sample, and 7 liters of air at a temperature of 50°C was heated at a flow rate of 470W.
/min, and the aniline gas concentration in the outlet gas is F.
The results of measurement using a high-sensitivity gas chromatograph with ID are shown in FIG. The amount of aniline released from B2 impregnated with gwt% of aniline is overwhelmingly large.

実施例3 実施例1で用いた活性炭にリン酸を添着した活第 表 性炭を加えて、第2表に示す割合で変えて、代表的な悪
臭成分であるアセトアルデヒド、アンモニア、硫化水素
、ベンゼンの平衡吸着量を測定した。
Example 3 Activated superficial carbon impregnated with phosphoric acid was added to the activated carbon used in Example 1, and the proportions shown in Table 2 were changed to produce typical malodorous components such as acetaldehyde, ammonia, hydrogen sulfide, and benzene. The equilibrium adsorption amount of was measured.

また比較例として第3表に示す配合についても測定した
Further, as a comparative example, the formulations shown in Table 3 were also measured.

リン酸を添着するには、リン酸27部の溶液中に浸漬し
て、活性炭の細孔中に十分吸着せしめた後、ろ別乾燥す
るかあるいは溶液をふりかけて十分に含浸させたものを
乾燥しても良い。
To impregnate phosphoric acid, immerse the activated carbon in a solution of 27 parts of phosphoric acid so that it is fully adsorbed into the pores of the activated carbon, and then filter and dry it, or sprinkle the solution on it to fully impregnate it and then dry it. You may do so.

次にアセトアルデヒドの平衡吸着量の測定方法について
説明する。第・2表、第3表のように配合したものをそ
れぞれ29とって容量3.971のガラス瓶に入れた後
、所定のアセトアルデヒド溶液を注入し気化させる。次
に25℃、RH60%の恒温恒湿槽中に放置し、アセト
アルデヒド濃度をガス検知管で測定した。平衡に達した
場合のアセトアルデヒド吸着量とガス濃度の関係を調べ
等温吸着線を測定した。そして、ガス濃度I Qppm
の時の吸着量を平衡吸着量とした。同様にしてアンモニ
アは101)pln、硫化水素はlppm、ベンゼンは
5111mの平衡吸着量を求めた。これらの結果を第2
表、第3表に示す。比較例に比べて実施例はアセトアル
デヒド罠対して優れており、全体のバランスがとれた性
能となっている。またそれぞれの活性炭の配合を少しず
つ変えるととKよって、アセトアルデヒド、硫化水素、
ベンゼンに対する性能を変えることができる。ここでは
リン酸添着炭の量を一定にしたが、この量も増減させる
ことによって、アンモニアや他のガスに対する性能もも
っと変化を持たせることができる。
Next, a method for measuring the equilibrium adsorption amount of acetaldehyde will be explained. After taking 29 grams of each of the mixtures as shown in Tables 2 and 3 and placing them in a glass bottle with a capacity of 3.971 cm, a specified acetaldehyde solution was poured into the bottle and vaporized. Next, it was left in a constant temperature and humidity chamber at 25° C. and RH 60%, and the acetaldehyde concentration was measured using a gas detection tube. The relationship between the amount of acetaldehyde adsorbed and the gas concentration when equilibrium was reached was investigated, and the isothermal adsorption line was measured. And gas concentration I Qppm
The amount of adsorption at the time was taken as the equilibrium adsorption amount. Similarly, the equilibrium adsorption amounts of ammonia (101) pln, hydrogen sulfide (lppm), and benzene (5111m) were determined. These results are the second
Table 3 shows the results. Compared to the comparative example, the example is superior to the acetaldehyde trap, and has a well-balanced overall performance. Furthermore, if the composition of each activated carbon is slightly changed, acetaldehyde, hydrogen sulfide,
Performance against benzene can be changed. Here, the amount of phosphoric acid-impregnated carbon was kept constant, but by increasing or decreasing this amount, the performance against ammonia and other gases can also be varied.

例えばアルデヒド類の多いたばこ臭等に対してはA1や
A4を多く、アミン類、アンモニアの多い魚臭、ペット
臭等に対してはリン酸添着炭を多く、含硫黄化合物、炭
化水素の多い野菜などの生ごみ臭、トイレ臭、皮革臭等
に対してはBl−?B3を多く配合すれば良い。
For example, use more A1 or A4 for tobacco odors that are rich in aldehydes, use more phosphoric acid-impregnated charcoal for fish odors, pet odors, etc. that are rich in amines and ammonia, and use vegetables that are rich in sulfur-containing compounds and hydrocarbons. Bl-? It is sufficient to mix a large amount of B3.

実施例4 次に本発明の空気浄化剤を使った空気浄化フィルター及
び空気清浄装置について実施例を挙げて説明する。ここ
で用いる空気浄化剤は配合x1゜X4.X6および比較
例Y2である。第4図は本発明の空気浄化フィルタの全
体図であり、第5図はその一部拡大図である。lはクラ
フト紙等で出来タハニカム状基材である。ここではセル
寸法12鵬、厚み7■の物を用いた。2は配合x1ある
いは配合Yの空気浄化剤でハニカム状基剤の中に1各々
300g均一に充填する。空気浄化剤2の粒子は、6〜
12メツシユの破砕状のものを使用した。又3は不織布
であり、°ポリエステル、アクリル、pp、pg等の熱
可塑性樹脂からなる繊維状不織布で、綿のように弾性を
幾分残しているもので、目付重量10〜50s/d、風
速1m/SeOの時の圧損1 wm A q以下のもの
を使用する。ノにカム状基材1と不織布3を接合するた
めの接着シート4として、無溶剤型で熱融着型樹脂(ナ
イロン系、アクリル系など)を繊維状にし、かつ開口率
の高い不織布すなわちくもの巣状接着シートを用いる。
Example 4 Next, an air purifying filter and an air purifying device using the air purifying agent of the present invention will be described with reference to an example. The air purifying agent used here has a composition of x1° x4. X6 and Comparative Example Y2. FIG. 4 is an overall view of the air purifying filter of the present invention, and FIG. 5 is a partially enlarged view thereof. 1 is a honeycomb-shaped base material made of kraft paper or the like. Here, a cell with a cell size of 12 cm and a thickness of 7 cm was used. 2 is an air purifying agent of blend x1 or blend Y, and 300 g of each of the air purifying agents is uniformly filled into a honeycomb-shaped base. The particles of air purifying agent 2 are 6~
A crushed piece of 12 meshes was used. 3 is a nonwoven fabric, which is a fibrous nonwoven fabric made of thermoplastic resin such as polyester, acrylic, PP, PG, etc., which retains some elasticity like cotton, has a basis weight of 10 to 50 s/d, and has a wind speed of 10 to 50 s/d. Use one with a pressure loss of 1 wm A q or less at 1 m/SeO. As the adhesive sheet 4 for bonding the cam-shaped base material 1 and the nonwoven fabric 3, a nonwoven fabric made of solvent-free heat-sealing resin (nylon, acrylic, etc.) and having a high aperture ratio is used. A nest-like adhesive sheet is used.

加工の手順としては、まずハニカム状基材1と不織布3
をくもの巣状接着シート4でホットプレス等により片面
のみを接合し、ついで、空気浄化剤2を均一にその上か
ら散布する。ついでその上からくもの巣状接着シート4
を置き、ホットプレス等で加熱することでフィルタSが
完成する。
As for the processing procedure, first, a honeycomb-shaped base material 1 and a nonwoven fabric 3 are
are bonded together on one side using a spider web-like adhesive sheet 4 using a hot press or the like, and then the air purifying agent 2 is uniformly sprinkled thereon. Then apply spider web adhesive sheet 4 on top of it.
The filter S is completed by placing the filter and heating it with a hot press or the like.

このようにして得られた空気浄化フィルタSは第6図に
示すように実際の空気清浄装置に使用される。5は空気
吸い込み口、6は空気吹き出し口、7はコントロール部
、8はフィルタをセットする治具である。この空気清浄
装置の上から見た内部構造を第7図に示す。空気浄化フ
ィルタSは治具8により第7図のようにセットされる。
The air purifying filter S thus obtained is used in an actual air purifying device as shown in FIG. 5 is an air inlet, 6 is an air outlet, 7 is a control section, and 8 is a jig for setting a filter. FIG. 7 shows the internal structure of this air purifying device viewed from above. The air purifying filter S is set using a jig 8 as shown in FIG.

9は空気中の大きい粉塵を除去するプレフィルタ、10
は静電集塵用フィルタ、11はモータ、1zはファン部
、13は空気の流路を示す。14は電気集塵のための高
電圧発生用の陽極の放電極、15は対極としての金属板
、16は静電集塵フィルタ10を分極させるために静電
集塵フィルタ10の後にセットしたラス金網等の導電体
の接地極である。
9 is a pre-filter that removes large dust particles from the air, 10
11 is a motor, 1z is a fan section, and 13 is an air flow path. 14 is a discharge electrode of an anode for generating high voltage for electrostatic precipitate, 15 is a metal plate as a counter electrode, and 16 is a lath set after the electrostatic precipitator filter 10 to polarize the electrostatic precipitator filter 10. This is a grounding electrode for a conductor such as a wire mesh.

このようにして得られた空気清浄装置を、ガラス製の1
−ボックスに入れ、同時に火をつけたたばこ(セブンス
ター)10本を入れて自然燃焼させながら、空気清浄装
置を運転して煙及び臭いを吸着させた。煙及び臭いの濃
度がほぼ一定になったところでさらにたばこ10本を入
れて燃焼させた。この様にして1日に30本のたばこを
吸着させ、約20時間経過後さらに30本吸着させる。
The air purifying device obtained in this way was
- 10 lighted cigarettes (Seven Stars) were placed in a box and allowed to burn naturally, while an air purifier was operated to absorb smoke and odor. When the concentration of smoke and odor became almost constant, 10 more cigarettes were added and burned. In this way, 30 cigarettes are adsorbed in one day, and after about 20 hours, an additional 30 cigarettes are adsorbed.

これ、を繰り返して合計60本のたばこを吸着させた。This was repeated to adsorb a total of 60 cigarettes.

この空気浄化フィルタSをポリエチレンの袋に入れて約
20時間放置した後、空気清浄装置にセットしてたばこ
の臭い及び硫化水素の吸着減衰曲線を測定した。その測
定方法は、空気清浄装置を中に置いたガラス製の1−ボ
ックスに火をつけたたばこ(セブンスター)1本を入れ
、ボックス内を77−ンで攪拌してたばこを燃焼させる
と共に、中の煙及び臭いを均一に分散させる。たばこが
全部燃焼したところで初期値を測定し、その後空気清浄
装置を運転して、運転時間と残存臭気量の関係を調べ吸
着減衰曲線を測定した。硫化水素の場合は、上記のたば
この代わりに約1%の硫化水素の標準ガスを入れ、初期
濃度を約zoppmに調整して行った。ガス濃度の分析
は、たばこ臭の中の沸点−70℃以上の脂肪族炭化水素
、芳香族炭化水素、ケトン類、アルデヒド類、方々ボン
酸、ニコチンやピリジンの窒素化合物等のトータル(は
とんど無臭の成分も含む。これをFよりトータルと呼ぶ
。)、およびアセトアルデヒドをFID付き高感度ガス
クロマトグラフで、またたばこ具申のアンモニアの濃度
はガス検知管で、さらに硫化水素はFPD付き高感度ガ
スクロマトグラフで行った。空気清浄装置は風量2.8
 j/mi、nで運転した。この結果を第4表に示す。
This air purifying filter S was placed in a polyethylene bag and left for about 20 hours, and then set in an air purifying device and the adsorption decay curves of tobacco odor and hydrogen sulfide were measured. The measurement method is to put one lit cigarette (Seven Star) in a glass box with an air purifier placed inside, and stir the inside of the box at 77-tons to burn the cigarette. Evenly disperses smoke and odors inside. The initial value was measured when all the cigarettes were burned, and then the air purifier was operated to examine the relationship between the operating time and the amount of residual odor and measure the adsorption decay curve. In the case of hydrogen sulfide, a standard gas of about 1% hydrogen sulfide was introduced in place of the tobacco described above, and the initial concentration was adjusted to about zoppm. Gas concentration analysis is based on the total amount of aliphatic hydrocarbons, aromatic hydrocarbons, ketones, aldehydes, various bonic acids, nitrogen compounds such as nicotine and pyridine, etc. with a boiling point of -70°C or higher in tobacco odor. (This is called total rather than F) and acetaldehyde are measured using a high-sensitivity gas chromatograph with FID, the concentration of ammonia in tobacco products is measured using a gas detection tube, and hydrogen sulfide is detected using a high-sensitivity gas chromatograph with FPD. I went with a tograph. The air purifier has an air volume of 2.8
I drove at j/mi, n. The results are shown in Table 4.

第   4   表 これらから明らかなように、本発明の実施例の配合にお
いては、他の臭気成分の吸着能力をほぼ維持しながら、
アセトアルデヒドの吸着能力の耐久寿命が優れたものと
なっている。
Table 4 As is clear from these figures, in the formulations of the examples of the present invention, while almost maintaining the adsorption ability of other odor components,
The durability of the acetaldehyde adsorption ability is excellent.

発明の効果 上記した各実施例から明らかなように、本発明の空気浄
化剤及び空気浄化フィルタ並びに空気清浄装置は、いか
なる臭気も除去でき、かつ耐久性に優れたものである。
Effects of the Invention As is clear from the above-mentioned Examples, the air purifying agent, air purifying filter, and air purifying device of the present invention can remove any odor and have excellent durability.

また、臭気に含まれるあらゆる成分の吸着能力に優れ、
さらに吸着能力の持続性においてバランスのとれた性能
を得ることができる。
In addition, it has excellent adsorption ability for all components contained in odors,
Furthermore, it is possible to obtain well-balanced performance in terms of sustainability of adsorption capacity.

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

第1図は本発明に用いるり/酸アニリン塩添着炭および
リン酸アニリン塩とアニリンの双方の添着炭と従来のア
ニリン添着炭および無添着炭のアセトアルデヒドの吸着
減衰曲線、第2図は第1図と同じ活性炭についての硫化
水素の吸着減衰曲線、第3図はリン酸アニリン塩添着炭
およびリン酸アニリン塩とアニリンの双方の添着炭と従
来のアニリン添着炭に50℃の空気を流通したときに脱
離。 してくるアニリンの量を示すグラフ、第4図は本発明の
空気浄化フィルタの一実施例の断面図、第5図は第4図
の一部分の拡大断面図、第6図、第7図は本発明の空気
浄化フィルタの使用される空気清浄装置の斜視図及び断
面図である。 2−一空気浄化剤  S−一空気浄化フィルタ出瀬人 
クラレケミカル林式会社
Figure 1 shows the acetaldehyde adsorption decay curves of the carbon impregnated with the phosphoric acid aniline salt used in the present invention, the carbon impregnated with both the phosphoric acid aniline salt and aniline, and the conventional aniline-impregnated carbon and non-impregnated carbon. The adsorption decay curve of hydrogen sulfide for the same activated carbon as shown in the figure. Figure 3 shows when air at 50°C is passed through the carbon impregnated with aniline phosphate, the carbon impregnated with both aniline phosphate and aniline, and the conventional aniline impregnated carbon. Detachment to. FIG. 4 is a cross-sectional view of an embodiment of the air purifying filter of the present invention, FIG. 5 is an enlarged cross-sectional view of a portion of FIG. 4, and FIGS. 1 is a perspective view and a sectional view of an air purifying device in which the air purifying filter of the present invention is used. FIG. 2-1 Air purifying agent S-1 Air purifying filter Deseto
Kuraray Chemical Hayashiki Company

Claims (6)

【特許請求の範囲】[Claims] (1)リン酸アニリン塩を添着した活性炭、リン酸を添
着した活性炭を混合せしめてなる空気浄化剤。
(1) An air purifying agent made by mixing activated carbon impregnated with phosphoric acid aniline salt and activated carbon impregnated with phosphoric acid.
(2)リン酸アニリン塩を添着した活性炭、リン酸を添
着した活性炭および無添着活性炭を混合せしめてなる空
気浄化剤。
(2) An air purifying agent made by mixing activated carbon impregnated with phosphoric acid aniline salt, activated carbon impregnated with phosphoric acid, and non-impregnated activated carbon.
(3)リン酸アニリン塩を添着した活性炭、リン酸を添
着した活性炭およびアニリンを添着した活性炭を混合せ
しめてなる空気浄化剤。
(3) An air purifying agent made by mixing activated carbon impregnated with phosphoric acid aniline salt, activated carbon impregnated with phosphoric acid, and activated carbon impregnated with aniline.
(4)リン酸アニリン塩とアニリンの双方を添着した活
性炭、リン酸を添着した活性炭を混合せしめてなる空気
浄化剤。
(4) An air purifying agent made by mixing activated carbon impregnated with both phosphoric acid aniline salt and aniline, and activated carbon impregnated with phosphoric acid.
(5)リン酸アニリン塩とアニリンの双方を添着した活
性炭、リン酸を添着した活性炭および無添着活性炭を混
合せしめてなる空気浄化剤。
(5) An air purifying agent made by mixing activated carbon impregnated with both phosphoric acid aniline salt and aniline, activated carbon impregnated with phosphoric acid, and non-impregnated activated carbon.
(6)リン酸アニリン塩とアニリンの双方を添着した活
性炭、リン酸を添着した活性炭およびアニリンを添着し
た活性炭を混合せしめてなる空気浄化剤。
(6) An air purifying agent made by mixing activated carbon impregnated with both phosphoric acid aniline salt and aniline, activated carbon impregnated with phosphoric acid, and activated carbon impregnated with aniline.
JP63314475A 1988-12-12 1988-12-12 Air purifier Expired - Lifetime JPH0616838B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63314475A JPH0616838B2 (en) 1988-12-12 1988-12-12 Air purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63314475A JPH0616838B2 (en) 1988-12-12 1988-12-12 Air purifier

Publications (2)

Publication Number Publication Date
JPH02160042A true JPH02160042A (en) 1990-06-20
JPH0616838B2 JPH0616838B2 (en) 1994-03-09

Family

ID=18053774

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63314475A Expired - Lifetime JPH0616838B2 (en) 1988-12-12 1988-12-12 Air purifier

Country Status (1)

Country Link
JP (1) JPH0616838B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012249742A (en) * 2011-06-01 2012-12-20 Suminoe Textile Co Ltd Flame retardant deodorizing filter and method of manufacturing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012249742A (en) * 2011-06-01 2012-12-20 Suminoe Textile Co Ltd Flame retardant deodorizing filter and method of manufacturing the same

Also Published As

Publication number Publication date
JPH0616838B2 (en) 1994-03-09

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