JPS6031826A - Deodorizing method and apparatus - Google Patents

Deodorizing method and apparatus

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Publication number
JPS6031826A
JPS6031826A JP58140316A JP14031683A JPS6031826A JP S6031826 A JPS6031826 A JP S6031826A JP 58140316 A JP58140316 A JP 58140316A JP 14031683 A JP14031683 A JP 14031683A JP S6031826 A JPS6031826 A JP S6031826A
Authority
JP
Japan
Prior art keywords
deodorizing
deodorizing material
clay
mixed
mixing
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
JP58140316A
Other languages
Japanese (ja)
Other versions
JPS6361052B2 (en
Inventor
Shiyunichi Sumioka
隈岡 俊一
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.)
FUIRUTON INTERNATL KK
Original Assignee
FUIRUTON INTERNATL KK
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 FUIRUTON INTERNATL KK filed Critical FUIRUTON INTERNATL KK
Priority to JP58140316A priority Critical patent/JPS6031826A/en
Publication of JPS6031826A publication Critical patent/JPS6031826A/en
Publication of JPS6361052B2 publication Critical patent/JPS6361052B2/ja
Granted legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To perform the adsorptive removal of a malodorous component, by mixing a void forming material with a base material consisting of clay and silica rock while baking the resulting mixture. CONSTITUTION:65-35pts.wt. of silica rock and 35-65pts.wt. of clay are put in a pot mill to be mixed and, after saw dust is added to the resulting mixture so as to be uniformly dispersed therein, water is added and mixed to form a compound which is, in turn, introduced into a mold frame having a desired shape while the molded one is dried and baked at 1,200-1,850 deg.C to obtain a deodorizing material A. This deodorizing material A is immersed in an aqueous solution containing 0.2% of a silicone water repellent to be impregnated with a hydrophobic agent and, thereafter, the impregnated one is heated at 130-300 deg.C to obtain a deodorizing material. In addition, a deodorizing material C is obtained by mixing the deodorizing material A and the deodorizing material B with activated carbon. These deodorizing materials A, B, C are used independently or in a mixed state.

Description

【発明の詳細な説明】 本発明はアンモニア、硫化ガス等の工場排ガスは熱論の
こと室内のタバコ臭、冷蔵庫内の食品臭突に、し尿臭又
は自動車排ガス中の油臭、燃焼具等の気体中に含まれる
あらゆる臭成分の除去、減少を目的とする脱臭方法とこ
れを具体化した脱臭装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention is applicable to industrial exhaust gases such as ammonia and sulfide gases, which can be used to produce heat, tobacco odors in rooms, food odors in refrigerators, human waste odors, oil odors in automobile exhaust gas, gases from combustion tools, etc. The present invention relates to a deodorizing method for the purpose of removing and reducing all odor components contained therein, and a deodorizing device embodying the method.

従来の脱臭方法及び脱臭装置においては脱臭材として活
性炭素を利用して臭成分の吸着除去を行うことを基本と
するものでおるが、活性炭素単独で用いる場合には臭成
分によっては除去不能であり、又除去可能な場合におい
て脱臭効果を高めるには活性炭素の脱臭ガス畳二対する
接触表面積を大となして吸着能力を高めることで可能で
あるも活性炭素の原材料、焼成条件等に問題があって、
脱臭容量の増大にはおのずと限度があり良好な脱臭効果
を持続することが困難であるうえに脱臭容量の限度まで
臭成分を吸着した活性炭素を再使用可能に再活性化する
ことは技術、コスト的薔:困難であった。史(二脱臭ガ
スが脱臭成分と空電のみの混合ガス体であることは殆l
しど考えられず実際の脱臭ガスは水蒸気又は微粒化1.
た油成分(3臭成分が付着又は溶解して空気中4二存在
することが多(、このような場合4二は接触表面積大で
高活性度の活性炭素を用いても臭成分の吸着除去を水分
又は油成分の存在が阻害して臭成分の除去が不可能若し
くFi脱臭能力の極端な低下を来たすという問題が残さ
れていた。
Conventional deodorizing methods and deodorizing equipment basically use activated carbon as a deodorizing material to adsorb and remove odor components, but when activated carbon is used alone, some odor components cannot be removed. In cases where deodorizing gas can be removed, it is possible to increase the deodorizing effect by increasing the contact surface area of activated carbon with the deodorizing gas tatami mat to increase its adsorption capacity, but there are problems with the activated carbon raw materials, firing conditions, etc. There it is,
There is a natural limit to the increase in deodorizing capacity, making it difficult to maintain a good deodorizing effect, and it is difficult to reactivate activated carbon that has absorbed odor components up to its deodorizing capacity so that it can be reused. Matobara: It was difficult. History (2) Most deodorizing gases are a mixture of only deodorizing components and static electricity.
However, it is difficult to imagine that the actual deodorizing gas is water vapor or atomized 1.
Odor components often exist in the air as adhering or dissolving odor components (42). The problem remains that the presence of water or oil components inhibits the removal of odor components, or that the Fi deodorizing ability is extremely reduced.

以上のような従来の活性炭素による脱臭(3残された諸
量Mを解決すべく開発した本発明の脱臭方法の要旨とす
るところは粘土、珪石、気孔形成材料を混合、焼成して
粘土と珪石を焼結するとともに気孔形成材料を焼去し、
その焼去跡を空胴となすととも4二粘土と珪石の焼結構
造部分番二熱数の微細な気孔を形成したポーラスな無機
質物を焼成時の形状で若しくは粉砕して粉体又は粒体と
なして脱臭材とし°〔用いること6二あり、以下群#I
に説明すれば本発明(:保る脱臭方法は、粘土、珪石を
基材として、これ(:気孔形成材料を混合したものを焼
成して作成したポーラスなセラミックスを基本物質とし
、この基本物質をそのままで脱臭材Aとして用い、若し
くは基本物質に疎水処理を施した脱臭材Bとして用い、
又はこの脱臭材A及び/又は脱臭材Bと活性炭素を混合
した脱臭材Cを夫々別々番二若しくは各脱臭材A、B、
Cを所定形状に成型しこれを多層(二組合せて又は各脱
臭材A、BCを粉又は粒体となして所望量づつ混合した
状態で除去を目的とする臭成分を含む脱臭ガス1′、接
触させ、例えばこれ等の脱臭材を充填したカラム中に脱
臭ガスを自然4二又は強制的I:通過させること6二よ
って臭成分を除去するものである。
The gist of the deodorizing method of the present invention, which was developed to solve the conventional deodorizing method using activated carbon (3) as described above, is that clay, silica stone, and pore-forming materials are mixed and fired to form clay. Sintering the silica stone and burning off the pore-forming material,
The burned residue is made into a cavity, and the porous inorganic material with fine pores of 42 clay and silica stone sintered structure part number 2 heat number is made into powder or grains in the shape at the time of firing or by crushing. As a deodorizing material [there are 62 uses, below group #I]
To explain this invention, the deodorizing method according to the present invention uses clay and silica stone as a base material, and uses porous ceramics created by firing a mixture of clay and silica stone as a basic material, and uses this basic material as a base material. Use it as a deodorizing material A as it is, or use it as a deodorizing material B in which the basic substance has been subjected to hydrophobic treatment,
Alternatively, the deodorizing material A and/or the deodorizing material B and the deodorizing material C mixed with activated carbon may be used separately or each of the deodorizing materials A, B,
A deodorizing gas 1' containing the odor components to be removed is formed by molding C into a predetermined shape and forming a multilayer (combining two or mixing desired amounts of each deodorizing material A and BC as powder or granules). Odor components are removed by bringing the deodorizing gas into contact with the deodorizing material and passing the deodorizing gas naturally or forcefully through a column filled with such a deodorizing material, for example.

ここで基本物質としてのポーラスなセラミックで混練し
、との混練物をブロック状、筒状等の適当な形状となし
て乾燥し、次いで焼成することによって粘土と珪石を焼
結させるとともに気孔形成材料を焼去してその焼去跡を
連続気孔となした無機質物であり、脱臭材Aの具体例と
しては珪石500 K?%粘土5009、気孔形成材料
としてのオガクズ1000Hz、水85006を用意し
、まず珪石、粘土をポットミル等に入れて混合し、これ
にオガクズを入れて均−6二分散するよう4二混合した
後、水を加えて混合して所望形状の型枠畳二人れて自然
乾燥又は強制乾燥等で一定状態まで乾燥した後、温度1
200℃〜1B50″Cで焼成することでSiO□ 並
び+’:、 Ae2o、を主成分とするポーラスなセラ
ミックスからなる脱臭+A Aを得る。ここで珪石と粘
土の混合比率は珪石約65〜85市量部、粘土約85〜
65重量部から選択1.た組合せで全体を100重量部
となす比率であれば本発明における脱臭に使用可能でら
り、」3記の製造例では粘土としてAl2O8重量40
%SiO□40重量%含有のものを使用したが粘土とし
て5i02かAJ?20.の8倍の含有量のものを用い
た場合4二は焼成物の微細な気孔形成が十分でなく脱臭
剤と[、て使用不能であつfco弥生詐各椿↓喘′4τ
襦灼井釈士≠湘 − 史に焼成物中の5i02並び(二Al2O,1′一つい
ては、S i02が80〜45重量%、AI!20.i
二ついては15〜40重量%の範囲が望ましく、夫々の
下限値即ちSiO□が45重量%以下、AI!20Il
が15重量%以下の状態では本願発明に用いるI:好ま
しいポーラスなセラミックスを得ることが出来ず、又5
i0280重量%以上、Al2O,が40重量%以上の
場合でも同様の理由から好ましくないことが知見された
Here, the porous ceramic as the basic substance is kneaded, the kneaded material is made into an appropriate shape such as a block or a cylinder, dried, and then fired to sinter the clay and silica stone and create a pore-forming material. A specific example of deodorizing material A is silica stone 500K? % clay 5009, sawdust as a pore-forming material 1000 Hz, and water 85006. First, silica stone and clay were mixed in a pot mill, etc., and sawdust was added to this and mixed for 42 hours so that it was evenly dispersed. Add water, mix it, form the desired shape, dry it to a certain state by natural drying or forced drying, etc., and then dry it at a temperature of 1.
By firing at 200°C to 1B50''C, deodorized +A made of porous ceramics mainly composed of SiO City weight department, clay approx. 85~
Select from 65 parts by weight 1. If the ratio of the combinations is 100 parts by weight, it can be used for deodorization in the present invention.
I used clay containing 40% SiO□, but was it 5i02 or AJ as clay? 20. When using a product with a content 8 times that of 42, the formation of fine pores in the fired product is insufficient, making it impossible to use it as a deodorizer.
Shakui Shakushi≠Shi - Historically, the 5i02 arrangement in the fired product (with one Al2O,1', Si02 is 80 to 45% by weight, AI!20.i
For both, a range of 15 to 40% by weight is desirable, and the lower limit of each, that is, SiO□ is 45% by weight or less, AI! 20Il
If I is less than 15% by weight, it is not possible to obtain the preferred porous ceramics of I used in the present invention, and
It has been found that cases where iO2 is 80% by weight or more and Al2O is 40% by weight or more are not preferable for the same reason.

次に脱臭材Bは、上記した脱臭材Aと同様にして生成し
たポーラスなセラミックス(二線水処理を施したもので
、具体例としては前記した実施例によ゛りて得たポーラ
スなセラミックスをシリコーン糸撲水剤の0.2%水溶
液中1こ浸漬し疎水剤を含浸させた後、引き上げて乾燥
し、次いで180〜aoo t’で2時間以上加熱して
熱処理したものである。
Next, deodorizing material B is a porous ceramic produced in the same manner as the above-mentioned deodorizing material A (treated with two-line water; a specific example is a porous ceramic obtained in accordance with the above-mentioned example). The material was immersed once in a 0.2% aqueous solution of silicone thread repellent to impregnate it with a hydrophobic agent, then pulled out and dried, and then heat-treated by heating at 180 - aoot' for 2 hours or more.

史(二脱臭材Cは適度の径の粉体又は粒体となした上記
脱臭材A、脱臭材Bの何れか又は両方と活性炭素を混合
し虎ものであり、その混合比は吸着除去を目的とする臭
成分6二よって異なり活性炭素混合量を多くずれば食品
具等の単−又は2〜3の臭成分を含む場合の吸着除去効
果は高くなるが、し尿臭等のよう(二°rンモニア、メ
ルカプタン類。
History (2) Deodorizing material C is a mixture of either or both of the above deodorizing material A and deodorizing material B in the form of powder or granules of an appropriate diameter and activated carbon, and the mixing ratio is such that it is suitable for adsorption and removal. Depending on the target odor component, if the amount of activated carbon mixed is increased, the adsorption removal effect will increase when food ingredients contain one or two or three odor components. rmonia, mercaptans.

チオエーテル類、アルデヒド類、インドール等の多種の
有機化合物臭気成分を含む場合の脱臭効果が低下するこ
ととなり、又活性炭素混合量が極端に少なくなれば単−
臭の吸着除去効果を減することとなる為に通常d脱臭材
A及び/又は脱臭材Bを約50〜75重量%、活性炭素
を約50〜25重量%となすことが望ま11.い。又混
合方法は前述のよう−1焼成済み脱臭材A及び/又は脱
臭材Bの粉体又は粒体と活性炭素を混合するばかりでな
く、脱臭材A及び/又は脱臭材Bと活性炭素を夫々板状
又は筒状となして重合状態に一体化して脱臭材C管構成
したり、所定形状◆1成型し喪脱臭材A又はBの表面に
活性炭素を吹き付けて構成することも可能である。
The deodorizing effect will be reduced if it contains various organic compound odor components such as thioethers, aldehydes, and indoles, and if the amount of active carbon mixed is extremely small, the deodorizing effect will be reduced.
11. In order to reduce the odor adsorption and removal effect, it is usually desirable to make the amount of deodorizing material A and/or deodorizing material B about 50 to 75% by weight and the amount of activated carbon about 50 to 25% by weight.11. stomach. In addition, the mixing method is not only as described above-1 by mixing the powder or granules of fired deodorizing material A and/or deodorizing material B with activated carbon, but also by mixing deodorizing material A and/or deodorizing material B and activated carbon, respectively. It is also possible to form a plate-like or cylindrical shape and integrate them in a polymerized state to form a deodorizing material C tube, or to form the deodorizing material A or B into a predetermined shape and spray activated carbon onto the surface of the deodorizing material A or B.

次(二本発明脱臭方法の具体実施例について述べると、
先づ脱臭カラム及び試料ガスを以−トの如く調製する。
Next (2) Describing specific examples of the deodorizing method of the present invention,
First, a deodorizing column and sample gas are prepared as follows.

襲のガラヌ管噛二〇、9y充填(充填密度0.05 P
/cdl )し両端を綿で封止する。
Galanu tube 20, 9y filling (filling density 0.05 P)
/cdl) and seal both ends with cotton.

試料ガヌ: タバコ臭士タバコ煙(ピース及びハイライト約1本分)
を101のテトラ−バッグに送入後、清浄空気で希釈し
て104’の試料ガスを調製する。
Sample Ganu: Tobacco smeller tobacco smoke (approximately 1 piece and highlight)
is introduced into the Tetra bag 101 and then diluted with clean air to prepare a sample gas 104'.

アンモニア臭;上記タバコ臭と同条件で調製する。Ammonia odor: Prepared under the same conditions as the tobacco odor above.

) ftvイy−ffルpr ) y (MIBK) 
; MIBKlOμJを、十分に減圧した1gの真空採
取びんに注入して気化後、清浄空気で常圧として試料ガ
ヌを調製する。
) ftv iy-ffpr) y (MIBK)
; MIBKlOμJ is injected into a 1 g vacuum collection bottle that is sufficiently depressurized, and after vaporization, the pressure is brought to normal pressure with clean air to prepare a sample.

二硫化メチル;上記MIBKと同条件で調製する。Methyl disulfide: Prepared under the same conditions as MIBK above.

実施例1.(試料ガスの流速による変化試験)第1図に
示すように脱臭カラムaに10gテトラ−パックbとポ
ンプc1フローメーターdを接続して試料ガスの流速を
0.2 + 0.5 + 1.01/rninと変化さ
せて各流速状態下・二おいて脱臭カラムaがら流出され
る試料ガスを捕集袋eで捕集してこれを分析した。尚分
析はタバコ臭、アンモニア臭については三点比較式臭袋
法(環境庁大気保全局特殊公害課発行の昭和52年度官
能試験法調査報告書による。)を用い、パネラ−は6名
として分析するものとし、MIBK及び二硫化メチルに
ついてはガククロマトグラフ法I:よる定量分析を行っ
た。
Example 1. (Test on changes due to flow rate of sample gas) As shown in Figure 1, a 10g Tetra-Pak b, a pump c1, and a flow meter d were connected to the deodorizing column a, and the flow rate of the sample gas was adjusted to 0.2 + 0.5 + 1. The sample gas flowing out of the deodorizing column a was collected by the collection bag e under each flow rate condition of 01/rnin and analyzed. For the analysis of tobacco and ammonia odors, the three-point comparison odor bag method (according to the 1976 Sensory Test Method Investigation Report published by the Special Pollution Division, Air Quality Conservation Bureau, Environment Agency) was used, and the analysis was conducted with six panelists. MIBK and methyl disulfide were quantitatively analyzed using Gaku chromatography method I.

結果第8図イル二に表記した通りのグラフに示される夾
験値が得られた。各グラフ中Aは脱臭材Aを、Cは脱臭
材0を示り7.又第8図イ2口における脱臭率とは下記
の式噛二で算出されたものである。
As a result, the experimental values shown in the graph shown in Figure 8 were obtained. In each graph, A indicates deodorizing material A, and C indicates deodorizing material 0.7. In addition, the deodorization rate at 2 mouths in Figure 8A is calculated using the following formula.

、−−−X100 第8図イル二のグラフによれば先づ第8図イのタバコ臭
については脱臭材Cの脱臭率は流速0.21!/min
からl、 Ol/1ninの範囲での変化は見られず、
はぼ100%の脱臭率を示し、脱臭材Aについては0.
5i/111in以下の流速では和尚の脱臭率を示すが
、流速大となるにしたがって脱臭効果が低下することが
認められた。
, - - /min
No change was observed in the range from l to Ol/1nin,
Deodorizing material A showed a deodorizing rate of 100%, and deodorizing material A had a deodorizing rate of 0.
At a flow rate of 5 i/111 inch or less, the deodorizing efficiency was as high as Osho, but it was observed that as the flow rate increased, the deodorizing effect decreased.

第8図口のアンモニア臭の場合脱臭材A、脱臭材C共に
脱臭率が約lO〜40%と低い値であるも、流速の変化
4二は殆んど影響されず、特に流速0.5〜L、 Ol
/minの範囲では一定の脱臭率を示すことが確認され
た。
Figure 8 In the case of ammonia odor at the mouth, although the deodorizing efficiency of both deodorizing material A and deodorizing material C is low at about 10 to 40%, the change in flow rate 42 is hardly affected, especially at flow rate 0.5 ~L, Ol
It was confirmed that a constant deodorization rate was exhibited within the range of /min.

第81[ハのMIBK、第8図1の二硫化メチルの脱臭
実験は流速の変化(1伴なう濃度変化を測定するもので
、グラフ中縦軸重ニブロットした濃度は入口濃度を11
00pp とし出口濃度をppmで表示したものであり
、第8Nb6二≠よれば脱臭材Cの脱臭効果は流速4二
影響されず、分析値は何れの流速においてもl ppm
以下と極めて良好であり、脱臭材Aについては流速が大
となるに従って脱臭効果が低下することを示している。
The deodorizing experiment of methyl disulfide in MIBK, Fig. 8, 1 was to measure the concentration change accompanying the change in flow rate (1).
00pp and the outlet concentration is expressed in ppm. According to No. 8Nb62≠, the deodorizing effect of deodorizing material C is not affected by the flow rate 42, and the analytical value is 1 ppm at any flow rate.
The results are extremely good, indicating that the deodorizing effect of deodorizing material A decreases as the flow rate increases.

又第8図1の二硫化メチルも上記第8図八のMIBKの
場合と略々同様傾向の結果が確認される。
Furthermore, the results for methyl disulfide shown in FIG. 8 1 are also confirmed to be approximately the same as those for MIBK shown in FIG. 8 8 above.

実施例2.(循環6二よる脱臭試験) 第2図に示すよう6二脱臭カラムa(二IOI!テトラ
−バッグbとポンプC,フローメーターdを接続して、
試料ガスを流速0.54!/1ninで循環させて一定
時間毎6二試料ガスを採取して分析を行った。尚試料ガ
ス調製、脱臭材の充填及び分析法更鴫二は脱臭率、濃度
の算出法等(二ついては実施例1.と同条件となすもの
とする。
Example 2. (Deodorization test using circulation 62) As shown in Figure 2, connect 62 deodorizing columns a (2 IOI! Tetra bag b, pump C, and flow meter d,
Sample gas flow rate 0.54! The gas was circulated at a rate of /1 nin, and 62 sample gases were sampled at regular intervals for analysis. In addition, sample gas preparation, filling of deodorizing material, analysis method, deodorization rate, concentration calculation method, etc. (two conditions shall be the same as in Example 1.).

結果第4図イに示すタバコ臭の場合脱臭材Cについては
循環後20分で脱臭率が100九となり、脱臭材Aでは
循環後20分では脱臭率lO%と低い値であるが、婆ら
1−循環を続行すれは脱臭率は急激・二高くなった。第
4図口のアンモニア臭については約40分位で脱県材A
%C共6二脱臭率が高まるが、脱臭材Aは脱臭材Cに比
べて10〜20%脱臭率が低いことが明らかとなった。
Results In the case of the tobacco odor shown in Figure 4A, deodorizing material C has a deodorizing rate of 1009 20 minutes after circulation, and deodorizing material A has a low deodorizing rate of 10% 20 minutes after circulation. 1-If the circulation was continued, the deodorization rate suddenly increased. Figure 4: Regarding the ammonia odor at the mouth, it will be removed after about 40 minutes.
It became clear that the deodorizing rate of deodorizing material A was 10 to 20% lower than that of deodorizing material C, although the deodorizing rate of both %C and 62 increased.

又MIBK及び二(流化メチル1:ついては第4図、ハ
、二に示すよう番二脱具材A、脱臭材C共に循環時間の
経過番二伴って臭成分の濃度を減少させ得ることを示し
ている。
In addition, MIBK and 2 (fluidized methyl 1: as shown in Figure 4, It shows.

実施例8.(脱臭材を試料ガス中に放置した場合の脱臭
試験) 脱臭材A1脱婁材Cの各々lOyを通気性を有する分析
用ティシュペーパー製の袋に充填して、これを試料ガス
雰囲気中6二放置し、一定時間経過ととl二試料ガスを
採取して分析を行った。
Example 8. (Deodorizing test when deodorizing material is left in sample gas) 1 Oy of each of deodorizing material A and deodorizing material C was filled into a bag made of breathable analytical tissue paper, and this was placed in the sample gas atmosphere for 6 seconds. After leaving it for a certain period of time, two sample gases were collected and analyzed.

結果タバコ臭6二ついては第5図イ番二示すように脱臭
材Cの場合約6時間経過すれば脱臭率100%となり高
脱臭効果を発揮するが脱臭材Aは脱臭率約5%:′−と
どまることから試料ガスを流動させる必要があることが
明らかである。アンモニア臭については第5図口に示す
よう1こ脱臭材A%C共に6時間経過後に80〜90%
の脱臭率となり、比較的良好な脱臭効果が示された。
As a result, when there are 6 cigarette smells, as shown in Figure 5, No. 2, in the case of deodorizing material C, the deodorizing rate reaches 100% after about 6 hours, demonstrating a high deodorizing effect, but in the case of deodorizing material A, the deodorizing rate is about 5%:'- It is clear that the sample gas needs to flow. Regarding ammonia odor, as shown in Figure 5, 80-90% of deodorizing material A%C after 6 hours.
The deodorizing rate was , indicating a relatively good deodorizing effect.

又MIBK、硫化メチル冬二ついては第5図ハ、=に示
すよう番二脱臭材Cの場合時間経過ととも番二臭濃度が
低下して良好な脱臭効果を示し、脱臭材Aの場合脱臭効
果は殆/しど期待できないことを示し“Cいる。
As for MIBK and methyl sulfide Fuyu, as shown in Figure 5 (c), in the case of No. 2 deodorizing material C, the No. 2 odor concentration decreased over time, showing a good deodorizing effect, and in the case of deodorizing material A, the deodorizing effect was low. "C" means that there is little or no expectation.

実施例4゜ 脱臭材A4二疎水処理を施した脱水材Bに゛りい°C前
記しfc実施例1〜8と同条件で実験を行−ったとこる
各実施例における脱臭材Aと略々同様の結果が得られる
ことを確認した。
Example 4: Deodorizing material A4 was heated to dehydrating material B, which had been subjected to hydrophobic treatment.Experiments were conducted under the same conditions as Examples 1-8. It was confirmed that almost the same results were obtained.

実施例5゜ 脱臭材A及び/又は脱臭材Bと脱臭材Cを所定の比率で
混合(7°C曲記東施例1〜8と同条件で脱具央験を行
−りたとこる混合比率4二応じて各脱臭材を単独で使用
1.た場合の中間値を示すことか知見された。
Example 5: Mixing deodorizing material A and/or deodorizing material B and deodorizing material C at a predetermined ratio (7° C.) A deodorizing experiment was conducted under the same conditions as Examples 1 to 8. It was found that depending on the mixing ratio of 42, each deodorizing material showed an intermediate value when used alone.

実施例6゜ 試料ガスを油性雰囲気例えはガソリン等の揮発油を霧状
となし°C試判ガヌ中番二混合させた状態で各脱臭材A
 、 B 、 Cについて夫々別個に実施例2の条件に
て実験を行ったところ、脱臭材A及び脱臭材C1:つい
ては前記した第4図イル二に示した脱臭効果を大幅に「
回るが、脱臭材Bについては脱臭効果鴫二殆んど悪影#
を及はさないことが明らかとηつた。
Example 6: Each deodorizing material A was mixed with the sample gas in an oily atmosphere, for example, a volatile oil such as gasoline.
, B, and C were separately tested under the conditions of Example 2, and it was found that the deodorizing effect shown in FIG.
However, for deodorizing material B, the deodorizing effect is almost negative #
It is clear that this will not affect the

例えば気高28℃、排ガス流度80℃の温度条件で尿尿
バキューム車を利用し、バキューム時の排ガス出口:′
:、従来よりIIV (−1けである活性炭槽内に、本
発明の脱臭材Bと脱臭材Cの混合物を充填した場合と従
来の活性法を充填した場合の脱臭効果の比較実験を行っ
た。
For example, if you use a urine/urine vacuum truck at a temperature of 28°C in altitude and 80°C in exhaust gas flow rate, the exhaust gas outlet during vacuuming:'
:, We conducted a comparative experiment on the deodorizing effect when a mixture of deodorizing material B and deodorizing material C of the present invention was filled in an activated carbon tank which was conventionally IIV (-1) and when it was filled using the conventional activation method. .

結果、原臭の場合170000 倍に希釈して無臭状態
となる尿尿ガスが従来の活性PG二よる脱臭の場合は脱
臭後のガスを70000倍に希釈しなければ無臭状態と
ならなかったが1本発明の場合には脱臭後のガスt−a
oooo倍に希釈すれは無臭状態となった。従って本発
明の脱臭方法(二よれに上述のように脱臭材の使用量を
約」15となしても従来の活性戻素による脱臭方法に比
して2倍強の脱臭効果を有することが明らかであり、又
呆尿ガヌ中に含まれるオイルミヌトによって従来の活性
戻素を用いた場合は活性次素の長時間使用ができなかっ
たが、本発明の場合親油性の脱臭材B′tl−混合した
ことによって従来例よりも長時間6二わたって使用し得
ることが明らかとなった。
As a result, in the case of the original odor, urine gas becomes odorless after being diluted 170,000 times, whereas in the case of conventional deodorization using active PG2, the deodorized gas must be diluted 70,000 times to become odorless.1 In the case of the present invention, the gas t-a after deodorization
When diluted oooo times, it became odorless. Therefore, it is clear that the deodorizing method of the present invention has a deodorizing effect more than twice that of the conventional deodorizing method using activated return elements even if the amount of deodorizing material used is approximately 15% as described above. In addition, when using the conventional reactivating element, the active element could not be used for a long time due to the oil minut contained in the urinary urinary substance, but in the case of the present invention, the lipophilic deodorizing material B'tl- It has become clear that the mixture can be used for a longer period of time than in the conventional example.

実施例7゜ 試料ガスに水蒸気を混入して実施例2の条件下で各脱臭
材A、B、Cの脱臭効果比較実験を行ったところ、脱臭
材Bは親油性即ち疎水性を付与され”Cいる為に殆んど
脱臭効果を示さないが、脱臭材A、脱臭材C1二ついて
は水分の存在は脱臭効果l:殆んど悪影響を及はさない
ことを知見した。
Example 7: An experiment was conducted to compare the deodorizing effects of deodorizing materials A, B, and C under the conditions of Example 2 by mixing water vapor into the sample gas, and it was found that deodorizing material B was given lipophilicity, that is, hydrophobicity. However, it was found that the presence of moisture had almost no adverse effect on the deodorizing effect for the two deodorizing materials A and C1.

以上のようになる本発明の脱臭方法(二よれば、粘土、
珪石を主組成物とし、これを焼結してなる脱臭材Aを基
本とし、この脱臭材At二二本水処理施してなる脱臭材
B、脱臭材A及び/又は脱臭材Bに活性炭素を混合しC
なる脱臭材Cを夫々別々畳重又は選択組合せ【7て除去
を目的とする臭成分を含む気体畳重流速を選択した強制
送気6二よって若しくは気体中への放置1二よって自然
接触させることで効果的な脱臭を行うことができ、特(
二湿完、油分を含まず車番口臭成分だけを含む餓体から
の脱臭につい°Cは脱臭材Cの脱臭効果が棒立っており
、又この脱臭材Cはホーラフなセラミックによる脱臭効
果と活性炭素による脱臭効果が相乗曲番二作用すること
で脱臭可能な臭成分の範囲を広げることが可能である。
The deodorizing method of the present invention as described above (according to Part 2, clay,
Based on deodorizing material A made by sintering silica stone as a main composition, deodorizing material B made by water-treating two or more of this deodorizing material At, activated carbon is added to deodorizing material A and/or deodorizing material B. Mix C
The deodorizing materials C are stacked separately or in a selected combination [7] A gas containing the odor components to be removed is folded and forced into air at a selected flow rate, or left in the gas (12) to bring them into natural contact. Effective deodorization can be performed with
Regarding the deodorization of starved bodies that do not contain any oil and only contain bad breath components, the deodorizing effect of deodorizing material C is outstanding in °C, and this deodorizing material C has the deodorizing effect and activity due to the hollow ceramic. The synergistic effect of the deodorizing effect of carbon makes it possible to expand the range of odor components that can be deodorized.

湿気を含む気体の場合には脱臭材A、脱臭材Cが良好で
、油性気体の場合(二は脱臭材Bが効果を発揮すること
から脱臭気体の雰囲気に応じて、これ等の各脱臭材を選
択、組合せて用いればより効果的な脱臭を行えるのであ
る。又各脱臭材は粘土と珪石の焼結体をベースとするホ
ーラフなセラミックヌであることから脱臭後(2所定温
度(通常は吸着温度以上)畳重加熱すれば容易に吸着し
た臭成分を取除いて再使用可能6二活性化することがで
きる利点がある。
In the case of gas containing moisture, deodorizing material A and deodorizing material C are good, and in the case of oily gas (deodorizing material B is effective), depending on the atmosphere of the deodorizing gas, each of these deodorizing materials If selected and used in combination, more effective deodorization can be achieved.In addition, each deodorizing material is a hollow ceramic material based on a sintered body of clay and silica stone, so after deodorizing (2 predetermined temperatures (usually There is an advantage that the adsorbed odor components can be easily removed by folding and heating (above the adsorption temperature) and the adsorbed odor components can be activated for reuse.

次鴫二本願の他の発明1:係る脱臭装置を具体例に基づ
き説明すれば、入口5と出口8のみを開口となし、内部
を中空部2となして脱臭材を充填可能とした容器1内に
、粘土、珪石、気孔形成材料を混合、焼成してなる親水
性の脱臭材A1該脱臭材A6ニシ11コーン系撥水剤に
て疎水処理を施した親油性の脱臭材B、当該脱臭材A及
び/又は脱臭材Bの粉、粒体畳重活性炭素を混合してな
る脱臭材Cを夫々所定形状4二成型して若しくは粉、粒
体となし°C各々区−!11.て’l +i 21を合
して充填するものであり、第6図の実施例によれば容器
1は、内部を中空部2となし、たllll11部6と入
口5及び入口空間6をイjする入[“]曽4、出口8及
び出口空間9を有する出口蓋7の組合せ4二で構成し、
胴部6の中空部2は隔壁1旧こよって三重筒構造6二区
画するととも畳重内筒11の入口側端(図中下端)に形
成した通孔12(二て該内筒11内と入口蓋4内の入口
空間6を連通させ、かつ出口側端lこ設けた切欠部16
を通じて中筒14と連通させており、該中筒14は下端
に形成した切欠部15を通じて外筒16下端と連通させ
、又外筒16内は上端の開1’:] 17 Th通じて
出口蓋7内の出口空間9・二連通可能に構成され、各筒
体内畳重は脱臭材A。
Next Shishiji Other invention 1 of the present application: To explain the deodorizing device based on a specific example, a container 1 has only an inlet 5 and an outlet 8 as openings, and has a hollow part 2 inside so that it can be filled with a deodorizing material. A hydrophilic deodorizing material obtained by mixing and firing clay, silica stone, and pore-forming material A1 The deodorizing material A6 Nishi11 A lipophilic deodorizing material B subjected to hydrophobic treatment with a corn-based water repellent; Deodorizing material C, which is a mixture of powder and granular activated carbon of material A and/or deodorizing material B, is molded into a predetermined shape 42, or powdered or granular. 11. According to the embodiment shown in FIG. 6, the container 1 has a hollow part 2 inside, and a hollow part 6, an inlet 5, and an inlet space 6. Consisting of a combination 42 of an outlet lid 7 having an inlet 4, an outlet 8 and an outlet space 9,
The hollow part 2 of the body part 6 has a partition wall 1 which divides the triple cylinder structure 6 into two sections, and a through hole 12 formed at the entrance side end (lower end in the figure) of the folded inner cylinder 11 (the inner cylinder 11 and the inside of the inner cylinder 11). A notch 16 that connects the inlet space 6 in the inlet lid 4 and has an outlet side end.
The middle cylinder 14 communicates with the lower end of the outer cylinder 16 through the notch 15 formed at the lower end, and the inside of the outer cylinder 16 has an opening 1' at the upper end. The outlet space 9 in the cylinder 7 is configured to be able to communicate with each other, and the deodorizing material A is stacked inside each cylinder.

B、C,を選択的鴫二嵌合設置するものである。例えば
、脱臭ガスが、油分を含む場合6二は全筒体6二親油性
の脱臭材Bを嵌合したり、内筒11に脱臭材Bを嵌合1
.中筒14及び外筒16には脱臭材A又は脱臭材Cを選
択的に嵌合することによって入口5から流入するガス中
の油分を臭成分ととも(口先づ脱臭材Bで除去した後、
史6二外側に位置する脱臭材A又はCによって臭成分の
除去を行い脱臭効果を高めるとともに油分−1よって脱
臭材A又は脱臭材Cの脱臭能力が低下するのを防止した
り、脱臭ガスが水蒸気を含んで臭成分が水滴に付着著し
くは水溶状態となっている場合鴫二は脱臭材Aを内筒1
1内に嵌合して中筒14外筒16内番二は脱臭力の高い
脱臭材Cを嵌合すること畳重よつ°C水分・二よる脱臭
材C中の活性炭素の活性減衰を防止するようになすもの
である。熱論、本発明の脱臭装置は、上述のような多重
筒構造6二限ることなく中空部2内を複数の重ね合せ状
の区画室6二区分して各区画室間の隔壁をメツシュネッ
トにて形成し区画室内には適度の粒体となした各脱臭材
A、B、Cを選択的に充填しても、又中空部2内を単−
室となして各脱臭材A、B、Cを夫々通気可能な布地製
の袋毫二充填して、所望数の袋を適当な順番6二積重ね
状又は並立状に内設することも可能である。
B and C are selectively fitted together. For example, if the deodorizing gas contains oil, the whole cylinder 62 may be fitted with a lipophilic deodorizing material B, or the inner cylinder 11 may be fitted with a deodorizing material B.
.. By selectively fitting the deodorizing material A or the deodorizing material C into the inner cylinder 14 and the outer cylinder 16, the oil content in the gas flowing in from the inlet 5 is removed together with odor components (after being removed by the deodorizing material B,
History 62 The deodorizing material A or C located on the outside removes odor components and enhances the deodorizing effect, and also prevents the deodorizing ability of the deodorizing material A or C from decreasing due to oil-1, and prevents the deodorizing gas from decreasing. If odor components containing water vapor adhere to water droplets and are significantly dissolved in water, Shiji will add deodorizing material A to the inner cylinder 1.
The inner cylinder 14 and the inner cylinder 16 are fitted with a deodorizing material C with high deodorizing power. It is intended to prevent this. In theory, the deodorizing device of the present invention has a multi-tubular structure 6 as described above, and the interior of the hollow portion 2 is divided into a plurality of stacked compartments 6, and the partition wall between each compartment is formed of mesh net. Even if the compartment is selectively filled with deodorizing materials A, B, and C in appropriate granular form, the interior of the hollow portion 2 is
It is also possible to fill two bags made of breathable fabric with each of the deodorizing materials A, B, and C as a chamber, and to place the desired number of bags in an appropriate order in a stacked or side-by-side manner. be.

このよう6二本発明・2係る脱臭装M1:よれば入口5
、L:出口8を有する容器1内6二粘土、珪石の焼結体
をベースとする脱臭材を充填するだけで各種の臭成分の
吸着除去を行え、しかも焼成によって各脱臭材の再活性
化を容易に行うことができるのである。更に脱臭ガスの
雰囲気(口広じて親水性脱臭材A、親油性脱臭材B、活
性次素混入により高脱臭能力となLfc脱臭材Cを選択
的に単独で茶しくけ組合せて容器内6二嵌合装置するこ
とによって脱臭ガス中の水分、油分に付着し又は溶解し
た臭成分の効果的な吸着除去を可能4こなすとともに、
この水分、油分によって脱臭材A又はB特に脱臭材Cの
脱臭能力低下を防止することができるのである。
In this way, the deodorizing device M1 according to the present invention/2: According to the inlet 5
, L: Inside a container 1 having an outlet 8, various odor components can be adsorbed and removed by simply filling a deodorizing material based on a sintered body of clay or silica stone, and each deodorizing material can be reactivated by firing. can be done easily. Furthermore, an atmosphere of deodorizing gas (hydrophilic deodorizing material A, lipophilic deodorizing material B, and LFC deodorizing material C, which has a high deodorizing ability due to the addition of active elements) are selectively combined in the container 6. By using a two-fitting device, it is possible to effectively adsorb and remove odor components attached to or dissolved in moisture and oil in deodorized gas.
This water and oil content can prevent the deodorizing ability of the deodorizing material A or B, especially the deodorizing material C, from decreasing.

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

第1図、第2図は本発明の脱臭方法の実施例を示すフロ
ーシート、第8図は脱臭ガスの流速と脱臭効果の関係を
示すグラフで、イはタバコ臭、口はアンモニア臭、ハは
MIBK、二は二硫化メチルを臭成分として含むもので
ある。 第4図は強制送電による脱臭ガスと脱臭材との接触時間
と脱切効果の関係を示すグラフで、イはタバコ臭%口は
アンモニア臭、ハHMIBK、二は二硫化メチルを臭成
分として含むものである。 第6図は自然接触−二よる脱臭ガスと脱臭材の接触時間
と脱臭効果の関係を示すグラフで、イはタバコ臭、口は
アンモニア臭、ハはMIBK 、二は二硫化メチルを臭
成分として含むものである。 第6図は本発明脱臭装置の実施例を示す断面図である。 A:親水性脱臭材、B:親油性脱臭材、C:活性炭素混
合脱臭材。 1:容器、2:中空部、6:胴部、4:入口蓋、5:入
口、6:入口空間、7:出口蓋、8:出口、9:出口空
間、10:隔壁、11:内筒、12:通孔、16:切欠
部、14:中筒、15:切欠部、16:外筒、17:開
口。 特許出願人 フィルトンインターナショナル株式会社第
 3図 (ハ) (イ) (」ビ/m1n) 仁) (2)) 第4図 υ\) (イ) 仁) (ロ)) 第5図 (八 (イ) 仁) (ロ) 86図 8 手続補正書 昭和58年9月19日 1、事件の表示 特願昭58−140816号 2、発明の名称 脱臭方法並びに脱臭装置 3、補正をする者 事件との関係 特許出願人 東京都港区西新橋1丁目4番9号 東ロステーションビル 自発的 6、補正の対象 明細書中の発明の詳細な説明の欄 7、補正の内容 l)明細書第5頁第12〜18行目ノ「Al2O2重童
40%Si、0Q40重量%含有」とあるを、rAt!
lOa Tt 40重31 % Si、Oi t−40
*&有」と補正する。
Figures 1 and 2 are flow sheets showing examples of the deodorizing method of the present invention, and Figure 8 is a graph showing the relationship between the flow rate of the deodorizing gas and the deodorizing effect. 1 contains MIBK, and 2 contains methyl disulfide as an odor component. Figure 4 is a graph showing the relationship between the contact time of the deodorizing gas and the deodorizing material by forced power transmission and the deodorizing effect. It is something that Figure 6 is a graph showing the relationship between the contact time of deodorizing gas and deodorizing material and the deodorizing effect according to natural contact.A is tobacco odor, mouth is ammonia odor, C is MIBK, and 2 is methyl disulfide as an odor component. It includes. FIG. 6 is a sectional view showing an embodiment of the deodorizing device of the present invention. A: Hydrophilic deodorizing material, B: Lipophilic deodorizing material, C: Activated carbon mixed deodorizing material. 1: Container, 2: Hollow part, 6: Body part, 4: Inlet cover, 5: Inlet, 6: Inlet space, 7: Outlet cover, 8: Outlet, 9: Outlet space, 10: Partition, 11: Inner cylinder , 12: through hole, 16: notch, 14: middle cylinder, 15: notch, 16: outer cylinder, 17: opening. Patent applicant: Filton International Co., Ltd. Figure 3 (c) (a) (''BI/m1n) jin) (2)) Figure 4 υ\) (a) jin) (b)) Figure 5 (eight) B) Jin) (B) 86 Figure 8 Procedural amendment September 19, 1981 1, Indication of the case Patent Application No. 140816/1982 2, Name of the invention Deodorizing method and deodorizing device 3, Person making the amendment Case and Relationship between: Patent applicant Toro Station Building, 1-4-9 Nishi-Shinbashi, Minato-ku, Tokyo Voluntary 6, Detailed explanation of the invention in the specification subject to amendment 7, Contents of the amendment l) Specification No. 5 The line 12-18 of the page "Contains 40% Si, 0Q 40% by weight" is replaced by rAt!
lOa Tt 40 weight 31% Si, Oit-40
*& Yes” is corrected.

Claims (1)

【特許請求の範囲】 覧)粘土、珪石6二気孔形成材料を添加混合して焼成し
たポーラスな脱臭材A、同じく粘土、珪石、気孔形成材
料を混合して焼成した後疎水処理を施し走脱臭材B、当
該脱良材A又は脱臭材Bの粉体又は粒体に活性炭素を混
合した脱臭材Cを夫々単独で若しくは組合せて気体に接
触させることを特徴とする脱臭方法。 2)粘土、珪石、気孔形成材料を混合焼成してなる脱臭
材A、同じく粘土、珪石、気孔形成材料を混合焼成した
後疎水処理を施した脱臭材B、当該脱臭材A又は脱臭材
Bの粉体又は粒体に活性炭素を混合してなる脱臭材Cを
夫々区分して任意の順番二通気可能な容器内に充填し、
若しくは各脱臭材を混合して容器内6二充填してなる脱
臭装置。
[Claims] See) A porous deodorizing material A made by adding and mixing clay, silica stone, and 62 pore-forming materials and firing, and a porous deodorizing material A made by adding and mixing clay, silica stone, and a pore-forming material, firing it, and then subjecting it to hydrophobic treatment to remove odors. A deodorizing method characterized by contacting a material B, the deodorizing material A, or a deodorizing material C in which activated carbon is mixed with powder or granules of the deodorizing material B, individually or in combination, with a gas. 2) Deodorizing material A made by mixing and firing clay, silica stone, and a pore-forming material; deodorizing material B, which also mixed and firing clay, silica stone, and a pore-forming material and then subjected to hydrophobic treatment; and deodorizing material A or deodorizing material B. The deodorizing material C made by mixing powder or granules with activated carbon is divided into sections and filled in two ventilated containers in any order,
Alternatively, a deodorizing device in which each deodorizing material is mixed and filled into a container.
JP58140316A 1983-07-29 1983-07-29 Deodorizing method and apparatus Granted JPS6031826A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58140316A JPS6031826A (en) 1983-07-29 1983-07-29 Deodorizing method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58140316A JPS6031826A (en) 1983-07-29 1983-07-29 Deodorizing method and apparatus

Publications (2)

Publication Number Publication Date
JPS6031826A true JPS6031826A (en) 1985-02-18
JPS6361052B2 JPS6361052B2 (en) 1988-11-28

Family

ID=15265967

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58140316A Granted JPS6031826A (en) 1983-07-29 1983-07-29 Deodorizing method and apparatus

Country Status (1)

Country Link
JP (1) JPS6031826A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018176096A (en) * 2017-04-17 2018-11-15 株式会社エクセルシア Excrement treatment agent

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5221275A (en) * 1975-08-13 1977-02-17 Hitachi Ltd Removing method of hydrogen sulfide from gas at high temperature
JPS5222837A (en) * 1975-08-15 1977-02-21 Hitachi Ltd Data channel device
JPS557549A (en) * 1978-06-30 1980-01-19 Kouzou Shibata Porous article and its manufacture and use
JPS5531085A (en) * 1979-08-22 1980-03-05 Takasago Corp Preparation of cyclohexadeca-5,9,13-trien-1-one
JPS565372A (en) * 1979-06-25 1981-01-20 Shinfuji Kaseiyaku Kk Manufacture of high hardness porous substance

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5221275A (en) * 1975-08-13 1977-02-17 Hitachi Ltd Removing method of hydrogen sulfide from gas at high temperature
JPS5222837A (en) * 1975-08-15 1977-02-21 Hitachi Ltd Data channel device
JPS557549A (en) * 1978-06-30 1980-01-19 Kouzou Shibata Porous article and its manufacture and use
JPS565372A (en) * 1979-06-25 1981-01-20 Shinfuji Kaseiyaku Kk Manufacture of high hardness porous substance
JPS5531085A (en) * 1979-08-22 1980-03-05 Takasago Corp Preparation of cyclohexadeca-5,9,13-trien-1-one

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018176096A (en) * 2017-04-17 2018-11-15 株式会社エクセルシア Excrement treatment agent

Also Published As

Publication number Publication date
JPS6361052B2 (en) 1988-11-28

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