JPH0716606B2 - Deodorant - Google Patents
DeodorantInfo
- Publication number
- JPH0716606B2 JPH0716606B2 JP28669286A JP28669286A JPH0716606B2 JP H0716606 B2 JPH0716606 B2 JP H0716606B2 JP 28669286 A JP28669286 A JP 28669286A JP 28669286 A JP28669286 A JP 28669286A JP H0716606 B2 JPH0716606 B2 JP H0716606B2
- Authority
- JP
- Japan
- Prior art keywords
- deodorant
- gas
- polyallylamine
- activated carbon
- treatment
- 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
Links
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は新規な脱臭剤に関する。TECHNICAL FIELD The present invention relates to a novel deodorant.
(従来の技術) 排ガスの脱臭、あるいは環境空気の脱臭法としては、極
めて多くの方法がある。例えば、芳香性物質によるマス
キング、吸着による脱臭、化学反応を利用する脱臭、細
菌や酵母等微生物を作用させる方法、あるいはこれらの
複合による方法などが挙げられる。(Prior Art) There are numerous methods for deodorizing exhaust gas or deodorizing ambient air. For example, masking with an aromatic substance, deodorization by adsorption, deodorization using a chemical reaction, a method of allowing a microorganism such as a bacterium or yeast to act, or a method of a combination thereof is used.
これらの方法のうち、マスキングは、本質的に臭気を除
去するものではなく、有害なガスの濃度を減少せしめ得
るものでもない。Of these methods, masking does not inherently remove odors nor can it reduce the concentration of harmful gases.
これ以外の方法は、また、実施する方式から、固体によ
る処理と液体による処理に大別される。The method other than this is roughly classified into a solid treatment and a liquid treatment, depending on the method used.
固体による処理は、粒状又は粉状の固体を充填した塔に
被処理ガスを通ずる大規模な方式と、固体を充填した容
器を冷蔵庫などの被処理空間に放置する小規模な方式が
あり、液体による方式は、充填塔あるいは空塔中のシヤ
ワーなどを用いて液体と被処理ガスを接触せしめたり、
液中に被処理ガスを導入してバブリングせしめるなどの
方式がある。There are two types of treatment with solids: a large-scale system in which the gas to be treated is passed through a column filled with granular or powdery solids, and a small-scale system in which a container filled with solids is left in a treated space such as a refrigerator. Is a method of bringing the liquid and the gas to be treated into contact with each other using a packed tower or a shower in the empty tower,
There is a method in which a gas to be treated is introduced into the liquid to cause bubbling.
この他、家庭では、スプレーなどにより液を噴霧して処
理することもあるが、これは一時的な処理に止まる。In addition, at home, the liquid may be sprayed and processed, but this is only a temporary process.
これらの方式のうち、液体による処理は、大規模の場合
使用済の液体の処置に問題があり、家庭用としては、継
続的な処理に不向きであるという欠点がある。Among these methods, the treatment with liquid has a problem that treatment of the used liquid is problematic on a large scale, and is not suitable for continuous treatment for household use.
固体による処理法では、活性炭、ゼオライト、活性白土
シリカゲル等による吸着法が汎用されているが、なかで
も活性炭は他の吸着剤に比して吸着容量が大きく、最も
よく利用されている。しかし、活性炭は極性の大きなガ
ス、例えばアンモニア、硫化水素、アルデヒドなどの吸
着速度が小さく、排ガスの通過速度を小さくする必要が
あり、このため処理装置の容量を大きくしなければなら
ないという欠点があつた。In the treatment method with a solid, an adsorption method using activated carbon, zeolite, activated clay silica gel, etc. is generally used. Among them, activated carbon has a large adsorption capacity as compared with other adsorbents and is most used. However, activated carbon has a drawback that it has a low adsorption rate for highly polar gases such as ammonia, hydrogen sulfide, and aldehydes, and needs to have a low exhaust gas passage rate. It was
固体による処理法のうち化学反応を利用する方法には、
対象とされる被処理ガスにより、多くの種類があり、例
えばアンモニアや低級アミンに対して、スルフオン化石
炭を用いる方法、自動車の排ガス、フアンヒーター等の
排ガス、煙草の煙等の燃焼排ガスに対しては、チオ硫酸
ナトリウムや亜硫酸ナトリウムを含浸せしめた活性炭を
用いる方法、酸性ガスやアルカリ性ガスに対して陽イオ
ン交換樹脂や陰イオン交換樹脂を用いる方法などが挙げ
られるが、いずれも吸着容量が小さい。Among the treatment methods using solids, the methods utilizing chemical reactions include
There are many types depending on the target gas to be treated. For example, for ammonia and lower amines, a method using sulfonated coal, exhaust gas of automobiles, exhaust gas of fan heaters, and combustion exhaust gas of cigarette smoke. Examples include a method of using activated carbon impregnated with sodium thiosulfate or sodium sulfite, a method of using a cation exchange resin or anion exchange resin for an acidic gas or an alkaline gas, but each has a small adsorption capacity. .
また特殊な例としては、低級アルデヒドを除去する目的
で、活性炭にヒドラジンやアニリンを吸着せしめたもの
や、粘土鉱物にアニリンやベンジルアミンを担持せしめ
たものが提案されているが、これらも対象ガスが限定さ
れるほか含水時の吸着能の低下や、吸着速度が小さいな
どの欠点があり、満足しうるものではなかつた。In addition, as a special example, for the purpose of removing lower aldehydes, it has been proposed to adsorb hydrazine or aniline on activated carbon or to adsorb aniline or benzylamine on a clay mineral, but these are also the target gas. However, there are drawbacks such as a decrease in adsorption capacity when water is contained and a low adsorption rate, which is not satisfactory.
(解決しようとする問題点) 本発明は、上記の欠点を解決した 吸着速度が大きく、
吸着容量の大きな脱臭剤を提供するものである。(Problems to be Solved) The present invention solves the above-mentioned drawbacks and has a high adsorption rate,
The deodorant has a large adsorption capacity.
(問題点を解決する手段) 本発明は、Si,Al及びMgの酸化物の少なくとも一種より
なる酸化物又は複合酸化物を構成成分とする多孔性の粘
土鉱物又は炭素にポリアリルアミンを担持せしめて成る
吸着剤である。(Means for Solving Problems) The present invention is to support polyallylamine on a porous clay mineral or carbon containing an oxide or a composite oxide composed of at least one of Si, Al and Mg oxides as a constituent component. Is an adsorbent.
本発明に用いられるSi,Al及びMgの酸化物もしくは複合
酸化物としては、SiO2,Al2O3,MgOのような酸化物、SiO
2・nH2O(シリカゲル)、Al2O3・nH2O(アルミナゲル)
のような含水酸化物、Al2O3・mSiO2・nH2OやAl2(Si
O3)3(即ちAl2O3・3SiO2)、Mg2Si3O8・nH2O(即ち2M
gO・3SiO2・nH2O)、が例示され、具体的にはモンモリ
ロナイト、カオリナイト、ハロサイト、ゼオライト、ア
タパルジヤイト、セピオライト、タルク、アロフエン等
が例示される。The oxides or complex oxides of Si, Al and Mg used in the present invention include oxides such as SiO 2 , Al 2 O 3 and MgO, and SiO.
2・ nH 2 O (silica gel), Al 2 O 3・ nH 2 O (alumina gel)
Hydrous oxides such as Al 2 O 3 · mSiO 2 · nH 2 O and Al 2 (Si
O 3 ) 3 (ie Al 2 O 3 · 3SiO 2 ), Mg 2 Si 3 O 8 · nH 2 O (ie 2M
gO · 3SiO 2 · nH 2 O), and specific examples thereof include montmorillonite, kaolinite, halosite, zeolite, attapulgite, sepiolite, talc, and allophene.
炭素としては、活性炭、無定形炭素等を利用しうる。As carbon, activated carbon, amorphous carbon or the like can be used.
ポリアリルアミンは、平均分子量2,000〜150,000程度の
ものが普通であるが、これに限定されず、また若干のア
リルアミン単量体やオリゴマーを含有していてもよい。The polyallylamine generally has an average molecular weight of about 2,000 to 150,000, but is not limited thereto, and may contain a small amount of allylamine monomer or oligomer.
ポリアリルアミンを担持せしめるには、ポリアリルアミ
ンを水溶液として担持体に噴霧、浸漬するなどし、次で
乾燥する方法、ポリアリルアミン塩酸塩などの塩を担持
せしめてから中和する方法など任意の方法でよい。To support the polyallylamine, the polyallylamine may be sprayed as an aqueous solution on the carrier, immersed, and then dried, or any method such as a method of carrying a salt such as polyallylamine hydrochloride and then neutralizing it may be used. Good.
本発明脱臭剤は、大規模には、塔に充填して被処理ガス
を流通せしめ、小規模には有孔の容器中に収容して、被
処理空間に放置するのが便利である。It is convenient that the deodorant of the present invention is packed in a column to allow the gas to be processed to flow therethrough on a large scale, and is stored in a perforated container on a small scale and left in the space to be processed.
実施例1 (脱臭剤の調製方法) 脱臭剤A ヤシ殻活性炭(粒径16〜32メツシユ)10gに分子量10,00
0のポリアリルアミン水溶液(16.6重量%)6gを添加し
て混合し、60℃で3時間真空乾燥して脱臭剤Aを得た。Example 1 (Method for preparing deodorant) Deodorant A Cocoa shell activated carbon (particle size 16 to 32 mesh) 10 g molecular weight 10,00
6 g of an aqueous polyallylamine solution (16.6% by weight) of 0 was added and mixed, and vacuum dried at 60 ° C. for 3 hours to obtain a deodorant A.
脱臭剤B やし殻活性炭に代えてアロフエン(mSiO2・Al2O3・nH
2O)(品川化成(株)製商品名セカードK−3)を用い
た他脱臭剤Aと同様に処理して脱臭剤Bを得た。Deodorant B Allophane (mSiO 2 · Al 2 O 3 · nH) instead of palm shell activated carbon
2 O) (trade name SECARD K-3 manufactured by Shinagawa Kasei Co., Ltd.) was used and treated in the same manner as other deodorant A to obtain deodorant B.
ついでガス流通用のノズルを付した以外密閉した容積約
2000mlのナイロン/ポリエチレンラミネート袋に臭気成
分として硫化水素及びアセトアルデヒドを夫々50ppm及
び625ppm混入した空気1500mlを充填し、内径5.5mmφ、
長さ150mmのガラス管に脱臭剤1gを充填したカラムの一
端を前記ノズルに接続し、カラムの他端にガス検知管、
吸引ポンプ((株)ガステツク製のガス採取器)の順に
接続した。Next, except for the gas flow nozzle, the sealed volume is approx.
A 2000 ml nylon / polyethylene laminate bag was filled with 1500 ml of air containing hydrogen sulfide and acetaldehyde as odorous components of 50 ppm and 625 ppm, respectively, and an inner diameter of 5.5 mmφ,
One end of a column filled with 1 g of a deodorant in a glass tube having a length of 150 mm was connected to the nozzle, and a gas detection tube was attached to the other end of the column.
A suction pump (a gas collector manufactured by Gastec Co., Ltd.) was connected in this order.
吸引ポンプを作動させ、100ml/30秒の速度で吸引し、最
初の100mlを吸引した時の検知管測定値を読みとる(測
定値(1))。次で、そのまゝ800ml吸引した後、検知
管をとりかえてさらに100ml吸引した時の検知管測定値
を読みとる(測定値(2))。結果を第1表に示す。Operate the suction pump, suction at a speed of 100 ml / 30 seconds, and read the measurement value of the detector tube when the first 100 ml was sucked (measurement value (1)). Next, after sucking 800 ml, the detector tube is replaced, and the measured value of the detector tube when 100 ml is sucked is read (measurement value (2)). The results are shown in Table 1.
実施例2 (脱臭剤の調製) 脱臭剤C セピオライト(粒径4〜10メツシユ)10gに分子量約70,
000のポリアリルアミン水溶液(15.7重量%)3gを添加
して混合し、60℃で3時間減圧乾燥して脱臭剤Cを得
た。 Example 2 (Preparation of deodorant) Deodorant C Sepiolite (particle size 4 to 10 mesh) 10 g molecular weight of about 70,
3 g of 000 polyallylamine aqueous solution (15.7% by weight) was added and mixed, and dried under reduced pressure at 60 ° C. for 3 hours to obtain a deodorant C.
脱臭剤D セピオライトをゼオライト(粒径8〜12メツシユの球形
のMolecular Sieve 13X)に代えたほか脱臭剤Cと同様
にして脱臭剤Dを得た。Deodorizing agent D A deodorizing agent D was obtained in the same manner as the deodorizing agent C except that zeolite (a spherical Molecular Sieve 13X having a particle size of 8 to 12 mesh) was used in place of sepiolite.
ついで実施例1と同様の袋に脱臭剤C又はDを1g入れ、
この袋に濃度約50ppmに調整した。Then, 1 g of the deodorant C or D was put in the same bag as in Example 1,
The bag was adjusted to a concentration of about 50 ppm.
た酢酸含有空気1,500mlを充満して口を閉じ約20℃の室
内に放置し、袋内の酢酸濃度を経時的に測定した。測定
は酢酸用検知管(検知限度0.2ppm)を使用した。The bag was filled with 1,500 ml of acetic acid-containing air, the mouth was closed, and the bag was left in a room at about 20 ° C., and the acetic acid concentration in the bag was measured over time. For the measurement, an acetic acid detector tube (detection limit 0.2 ppm) was used.
なお、比較のためセピオライト及びゼオライトの夫々単
独を用いた場合についても脱臭性能をテストした。結果
を図1に示す。For comparison, the deodorizing performance was also tested when sepiolite and zeolite were used alone. The results are shown in Fig. 1.
図1に示す結果から本発明の脱臭剤が、脱臭能力に優れ
ていることがわかる。From the results shown in FIG. 1, it can be seen that the deodorant of the present invention has excellent deodorizing ability.
第1図は本発明の脱臭剤C及び脱臭剤Dと、セピオライ
ト及びゼオライトの脱臭能力を示す図である。FIG. 1 is a diagram showing the deodorizing ability of the deodorant C and the deodorant D of the present invention, and sepiolite and zeolite.
Claims (1)
りなる酸化物又は複合酸化物を構成成分とする多孔性の
粘土鉱物又は炭素にポリアリルアミンを担持せしめて成
る脱臭剤。1. A deodorant obtained by supporting polyallylamine on a porous clay mineral or carbon containing an oxide or a complex oxide composed of at least one of oxides of Si, Al and Mg.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28669286A JPH0716606B2 (en) | 1986-12-03 | 1986-12-03 | Deodorant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28669286A JPH0716606B2 (en) | 1986-12-03 | 1986-12-03 | Deodorant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63141642A JPS63141642A (en) | 1988-06-14 |
| JPH0716606B2 true JPH0716606B2 (en) | 1995-03-01 |
Family
ID=17707739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28669286A Expired - Lifetime JPH0716606B2 (en) | 1986-12-03 | 1986-12-03 | Deodorant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0716606B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5395585A (en) * | 1990-07-24 | 1995-03-07 | Aquarium Pharmaceuticals, Inc. | Method for controlling odor |
| US6540936B1 (en) | 2000-06-19 | 2003-04-01 | Toagosei Co., Ltd. | Aldehyde gas absorbent and process for absorbing aldehyde gas |
-
1986
- 1986-12-03 JP JP28669286A patent/JPH0716606B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63141642A (en) | 1988-06-14 |
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