WO1996022827A1 - Deodorant material, process for producing the same, and method of deodorization - Google Patents

Deodorant material, process for producing the same, and method of deodorization Download PDF

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Publication number
WO1996022827A1
WO1996022827A1 PCT/JP1996/000140 JP9600140W WO9622827A1 WO 1996022827 A1 WO1996022827 A1 WO 1996022827A1 JP 9600140 W JP9600140 W JP 9600140W WO 9622827 A1 WO9622827 A1 WO 9622827A1
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WIPO (PCT)
Prior art keywords
deodorizing
silver nitrate
weight
activated carbon
copper oxide
Prior art date
Application number
PCT/JP1996/000140
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French (fr)
Japanese (ja)
Inventor
Shinya Kitaguchi
Koichi Yamamoto
Junichi Miyake
Original Assignee
Nippon Shokubai Co., Ltd.
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Publication date
Application filed by Nippon Shokubai Co., Ltd. filed Critical Nippon Shokubai Co., Ltd.
Priority to KR1019960705113A priority Critical patent/KR970701583A/en
Publication of WO1996022827A1 publication Critical patent/WO1996022827A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8933Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/8986Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with manganese, technetium or rhenium

Definitions

  • Deodorizing material its production method and deodorizing method
  • the present invention relates to a deodorizing material used for removing malodorous components from a gas containing various malodorous components such as hydrogen sulfide, various mercaptans, ammonia and amines, a production method thereof, and a deodorizing method.
  • the deodorization method can be widely used for deodorization in refrigerators, toilets, animal breeding houses, sewage treatment plants, and the like.
  • Conventional technology
  • the adsorption method of adsorbing odorous components on adsorbents mainly composed of activated carbon and the method of oxidizing and decomposing odorous components using ozone and a catalyst have been mainly used.
  • the former uses the adsorption action of activated carbon and has a limited adsorption capacity.
  • the activated carbon When used for a long time or when the concentration of odorous components is high, the activated carbon must be replaced frequently.
  • the latter uses the oxidizing power of ozone, and can be semi-permanently deodorized by proper combination with a catalyst, but requires special equipment such as an ozone generator and high-pressure transformer. It is pointed out that the cost and operating cost increase.
  • the present invention has been made in view of such problems of the prior art.
  • the purpose of the present invention is to provide a direct reaction for a long period of time not only for malodorous components having high reactivity but also malodorous components having low reactivity. It is an object of the present invention to provide a deodorizing material which can stably maintain an excellent deodorizing effect, a production method thereof, and a deodorizing method.
  • the deodorizing material of the present invention is characterized in that a deodorizing component comprising copper oxide, manganese oxide and silver nitrate is carried on a carrier material containing activated carbon.
  • Copper oxide in the deodorizing material preferable composition ratio of manganese oxide and silver nitrate, copper oxide:. 0 C u 0 Convert 5-1 0 part by weight, manganese oxide: M n 0 2 terms at 1-2 0 parts by weight , silver nitrate: a g N 0 3 ranges from 1 to 2 0 parts by weight in terms, also copper oxide occupied in the deodorizing material, the total content of manganese oxide and silver nitrate ranges from 3 3 0 wt% Is preferred.
  • the deodorizing component consisting of copper oxide, manganese oxide and silver nitrate is carried on a carrier material containing activated carbon as a main component.
  • the content of the activated carbon in the carrier material is 30 to 70% by weight.
  • the specific surface area as a deodorant is preferably 250 m 2 / or more. If this deodorizing material is used to treat a gas containing malodorous components such as hydrogen sulfide, various mercaptans, ammonia, and amines, these malodorous components are removed and the deodorization can be performed efficiently.
  • a feature of the method for producing a deodorizing material according to the present invention is that after a carrier material containing activated carbon is formed into a predetermined shape, copper oxide and manganese oxide are added thereto. And a solution containing silver nitrate or their precursors are applied or impregnated, and calcined in a non-oxidizing atmosphere at a temperature lower than the decomposition temperature of silver nitrate. Deodorizing material can be obtained.
  • a more preferable method for producing a deodorizing material is to add a solution containing copper oxide, manganese oxide, silver nitrate or a precursor thereof to citric acid in an amount of 1 to 3 mol with respect to silver nitrate to form an activated carbon-containing carrier.
  • the present inventors have developed a method of converting not only highly reactive malodor components but also less reactive malodor components without using costly ozone or the like and without requiring heat treatment.
  • various researches have been conducted with the aim of developing a deodorizing material that can stably maintain an excellent deodorizing effect over a long period of time.
  • the three components of copper oxide, manganese oxide, and silver nitrate are used in combination as the main deodorizing active components, and activated carbon is used as the main carrier material for holding or supporting them, a deodorizing material with excellent performance can be obtained. I knew that it could be done.
  • copper oxide has a large amount of surface oxygen and exerts the effect of oxidizing and decomposing hydrogen sulfide / methyl mercaptan at room temperature.
  • the oxygen consumed in this oxidative decomposition reaction is Since it is gradually supplemented by the oxygen contained in the air, its deodorizing effect is maintained for a long time.
  • manganese oxide effectively exerts the deodorizing effect on the above-mentioned various odorous gases, but in particular, suppresses the conversion of methyl mercaptan into methyl disulfide caused by the copper oxide. It works effectively in doing so. To effectively exhibit such effects, arbitrariness preferred that the weight ratio of M n 0 2 / C u 0 and 2 or more blending ratio against copper oxide.
  • silver nitrate is the most characteristic component in the present invention, and its strong oxidizing ability makes it difficult to remove by conventional techniques. It is a low-reactive-odor component, especially ammonia, trimethylamine, methyl sulfide. Decomposition and removal of acetoaldehyde and the like are possible.
  • silver or silver oxide is used as one of the deodorizing components, but these have a property that they tend to become large particles of metallic silver by heat treatment during the preparation of the deodorizing material. Inactive against odorous gas. Therefore, there have been proposed several methods of supporting silver as a composite oxide, wet oxidation with a peroxide or the like, and supporting silver as a silver oxide on a carrier. In addition, it is difficult to disperse and support in a fine particle state, and a satisfactory deodorizing effect has not been obtained.
  • silver instead of utilizing silver as silver oxide as in the past, silver was utilized in the form of silver nitrate, thereby maximizing the effective use of silver as a deodorizing component. However, it has a great feature.
  • the composition ratio of these three components in the deodorizing material is determined as follows: copper oxide: 0.5 to 100 parts by weight (more preferably 1 to 5 parts by weight) in terms of CuO, manganese oxide: M n 0 2 terms at 1-2 0 parts by weight (more preferably rather is 2-1 0 part by weight), silver nitrate: 1-2 0 parts by weight A g n 0 3 conversion (more preferably 2-1 0 weight). If the amount of copper oxide is less than 0.5 part by weight, the amount of manganese oxide is less than 1 part by weight, and the amount of silver nitrate is less than 1 part by weight, the respective effects become insufficient and the odor components are reduced. The decomposition effect is not sufficiently exhibited, and it is difficult to obtain a satisfactory deodorizing effect.
  • composition ratio of copper oxide exceeds 10 parts by weight
  • the amount of conversion from the malodorous component methyl mercaptan to the other malodorous component methyl disulfide increases, and the deodorizing effect is not effectively exerted. It becomes.
  • the composition ratio of manganese oxide exceeds 20 parts by weight or the composition ratio of silver nitrate exceeds 10 parts by weight
  • no further improvement in the deodorizing effect is observed, and the activated carbon adsorption site This tends to reduce the effect of deodorization on the contrary, which is undesirable.
  • the total content of these three components in the deodorizing material should be 3 to 30% by weight, more preferably 5 to 20% by weight. If the content is less than 2% by weight, the absolute amount as an active ingredient for deodorization tends to be insufficient and the deodorization performance is insufficient, and is particularly satisfactory when applied to a gas having a high concentration of malodorous components. If the deodorizing effect becomes difficult to obtain, and if the total content of the above three components exceeds 30% by weight and becomes excessively large, the absolute amount of activated carbon acting as a carrier component tends to be insufficient, and as described below, the odor is bad. The adsorption site of the components tends to be short, and it is difficult to obtain satisfactory deodorizing performance.
  • the starting materials for copper oxide include copper nitrate, copper sulfate and copper oxide.
  • As a starting material for manganese oxide, manganese nitrate, manganese sulfate, activated manganese dioxide and the like are exemplified as preferable ones.
  • the deodorizing active component used in the present invention essentially contains the above three components.
  • nickel may be used as another deodorizing active component.
  • metal oxides such as iron, cobalt, chromium, zinc, and vanadium, and platinum group metals in appropriate amounts.
  • metallic silver, silver oxide, copper, or a composite oxide of manganese and silver may coexist.
  • the amounts thereof are desirably suppressed to about 5% by weight or less, more preferably about 2% by weight or less in the deodorizing material so as not to dilute the effects of the three components.
  • the carrier material for holding or supporting the active ingredient for deodorization contains activated carbon as an essential ingredient, preferably 30 to 70% by weight, more preferably 40 to 60% by weight. % Is selected.
  • the malodorous component is composed of a mixture of various gases, but in order to decompose and remove the malodorous component, it is necessary to first adsorb and trap the malodorous component on the deodorizing material.
  • ammonia which is a basic gas
  • a carrier such as silica or titania ash with high acidity
  • hydrogen sulfide which is an acid gas
  • Almost no neutral gas, such as methyl sulfide is adsorbed on acidic or basic carriers.
  • zeolite has the effect of adsorbing gas into the pores, but has a poor effect of trapping malodorous components having a small molecular size with small pore size, and the adsorption trap performance is deteriorated by humidity.
  • Activated carbon on the other hand, is neutral in its own right, but has a very large specific surface area and numerous micropores, making it resistant to any acidic, basic, or neutral odorous gas. Also exhibits excellent adsorption trap effect. Such an excellent adsorption trapping effect of the activated carbon is effectively exhibited as an adsorption site for the deodorizing component and the malodorous component.
  • the adsorption site efficiently adsorbs and holds the malodorous component, and simultaneously carries the malodorous component on the adsorption site. It is considered that the malodorous component is promptly decomposed by the action of the deodorizing active component and the deodorization proceeds efficiently.
  • the present inventors have confirmed that, in relation to the deodorizing active ingredient containing the three components selected above, an excellent effect exceeding the above-mentioned effect derived from the excellent adsorption trapping effect of activated carbon is obtained. It has been confirmed that a deodorizing effect can be obtained, and it is considered that some interaction between the specified deodorizing active ingredient and activated carbon acts to further enhance the deodorizing effect. However, the reason has not yet been elucidated.
  • the content of activated carbon in the carrier material is preferably set in the range of 30 to 70% by weight, more preferably 40 to 60% by weight.
  • the content of the activated carbon is less than 30% by weight, the above-mentioned effects provided by the activated carbon become insufficient, and it becomes difficult to exhibit satisfactory deodorizing performance.
  • the content of activated carbon exceeds 70% by weight, the amount of one component of the binder tends to be relatively short, and the physical strength of the carrier is reduced, causing problems such as breakage and powder peeling during use. Come.
  • a predetermined amount of activated carbon powder is uniformly mixed with a ceramic-based binder such as silica-alumina, silica, alumina, titania, zeolite, titania silica composite oxide, etc. , Plate, honeycomb, etc. Alternatively, it can be obtained by firing under heating in a non-oxidizing atmosphere.
  • the deodorizing material of the present invention is produced by supporting a deodorizing component essentially containing the above-mentioned three components on the above-mentioned carrier by a method as described below. To make the deodorizing effect more effective, deodorizing material is used. It is desirable that the specific surface area of the material be at least 250 m 2 Zg, more preferably at least 350 m 2 Zg. As described above, it is considered that the deodorization of the offensive odor component is, first, that the offensive odor component is adsorbed and trapped on the adsorption site of the deodorant, and is decomposed into the odorless component by the action of the deodorant component in the adsorption site.
  • the deodorizing material In order to enhance the deodorizing effect, it is effective to increase the number of adsorption sites as much as possible. For that purpose, it is effective to increase the specific surface area of the deodorizing material as much as possible. In addition, if a carrier mainly composed of activated carbon is used, the specific surface area of activated carbon is very large, so that a specific surface area of 250 m 2 Zg or more can be easily secured.
  • a method for producing the deodorizing material a method of kneading copper oxide, manganese oxide, silver nitrate, or a precursor thereof and a carrier material containing a predetermined amount of activated carbon to form the pellet, or using a carrier material to pelletize as described above.
  • a method of supporting the deodorizing active component or a precursor thereof can be adopted, but the latter method is preferred, specifically, a carrier material containing activated carbon. Is formed into an arbitrary shape by a conventional method, and then coated or impregnated with a mixed solution of a water-soluble salt containing a precursor of a deodorizing active ingredient, and dried or fired.
  • the aforementioned deodorizing active component will be carried on the adsorption site wall surface of the activated carbon-based carrier.
  • the deodorizing active component will be deodorized to the malodor component adsorbed and trapped on the adsorption site. This is because the components act quickly.
  • the treatment atmosphere is changed to a non-nitrogen atmosphere.
  • the sintering temperature below the decomposition temperature of silver nitrate, preferably in the range of 200 to 400 *.
  • the firing temperature is desirably set to 20 O'C or more from the viewpoint of more securely activating and supporting the deodorizing active component including silver nitrate.
  • silver nitrate is a compound having a high oxidizing property, and is easily passed in the presence of a substance that is easily reduced.
  • a solution containing silver nitrate is impregnated with a carrier containing activated carbon, precipitation of metallic silver is observed on the surface of the carrier.
  • the solution containing the three components is mixed with citric acid in an amount of 1Z3 to 1Z2 mol based on silver nitrate. It was confirmed that when contained, the precipitation of metallic silver was remarkably suppressed, and loading as silver nitrate was more reliably performed.
  • citric acid effectively acts as a competitive adsorbent when the platinum group metal is supported on the carrier. We believe it plays a role in protecting the reaction site with silver nitrate. rnm
  • coconut shell activated carbon powder (specific surface area 1 5 0 0 m 2 / g ) of the clay mineral-based inorganic by Nda (composition: A 1 2 0 a 4 0 wt%, S i 0 2 6 0 by weight%) and cellulose based organic It was kneaded with a binder, extruded, dried and fired to produce a honeycomb-shaped carrier having an activated carbon content of 45% by weight.
  • the resulting honeycomb carrier, copper nitrate, C u O shown manganese nitrate, silver in Tables 1: M n 0 2:.
  • a deodorizing material was produced in the same manner as in Example 1 except that the blended amount of the activated carbon and the content ratio of the deodorizing active component were changed as shown in Table 1.
  • a comparative deodorizing material was produced in the same manner as in Example 1 except that some of the essential components were omitted as shown in Table 1.
  • the 82 cam-shaped carrier produced using activated alumina was impregnated with a mixed aqueous solution of manganese nitrate and silver nitrate, dried, and calcined at 500 C for 2 hours in the air to obtain a comparative deodorizing material.
  • Table 1 shows the composition of the obtained deodorant.
  • Example 1 was the same as Example 1 except that citrate was not added. Similarly, a reference deodorant was obtained.
  • a reference deodorant was obtained in the same manner as in Example 1 except that the firing temperature in a nitrogen atmosphere was changed to 150 at 2 hours.
  • a reference deodorizing material was obtained in the same manner as in Example 1, except that the firing temperature in a nitrogen atmosphere was changed to 500 ° C. for 2 hours.
  • the deodorization performance was measured using a flow-through reactor, collecting gas at the inlet and outlet of the packed bed filled with each deodorant, measuring the odor of each odorous component gas by gas chromatography, and The removal efficiency of the components was determined.
  • Three types of malodorous gases were selected: methyl mercaptan, methyl sulfide, and trimethylamine, with an inlet concentration of lO ppm and a space velocity of 50, 0 at 25 ° C, 50% humidity and 50% RH. Evaluation was made under the condition of 0 0 H r.
  • the gas concentration of methyl disulfide detected at the outlet of the packed bed was also measured. Table 2 shows the measurement results of the deodorizing materials of Examples, Comparative Examples, and Reference Examples 2 hours after the start of gas flow.
  • the deodorizing materials of Examples that satisfy all the requirements of the present invention have higher deodorizing performance against various odorous gases than the deodorizing materials of Comparative Examples. It can be confirmed that excellent deodorizing performance is exhibited by optimizing the mixing ratio of the carrier material and the deodorizing active ingredient. Further, the reference example adopts a production method which deviates from the requirements recommended as preferable conditions in the present invention, and the deodorizing activity of the obtained deodorizing material varies depending on the content of activated carbon in the carrier material and the production conditions. Can be confirmed. The invention's effect
  • the present invention is constituted as described above, and is used not only for malodorous components having high reactivity such as hydrogen sulfide / methyl mercaptan, but also for malodorous components having low reactivity such as methyl sulfide, ammonia and amines. Also has an excellent deodorizing effect, and can efficiently decompose and remove malodorous components without producing by-products other methyl sulfide, methyl disulfide, from methyl mercaptan, so refrigerators, toilets, animal breeding houses, and sewage It can be widely used for deodorization in treatment plants and others.

Abstract

A deodorant material comprising a deodorant component supported on a carrier material mainly comprising activated carbon, wherein the deodorant component comprises 0.5-10 parts by weight (in terms of CuO) of copper oxide, 1-20 parts by weight (in terms of MnO2) of manganese oxide and 1-20 parts by weight (in terms of AgNO3) of silver nitrate, and the total content of copper oxide, manganese oxide and silver nitrate accounts for 3-30 wt.% of the deodorant material as a whole. The material has an excellent performance of eliminating various malodorous components, such as a hydrogen sulfide, mercaptans, ammonia and amines, contained in gases.

Description

明 細 書 発明の名称  Description Name of Invention
脱臭材及びその製法並びに脱臭方法  Deodorizing material, its production method and deodorizing method
本発明は、 硫化水素、 各種メルカブタン類、 アンモニア及びアミ ン類等の各種悪臭成分を含むガスからの悪臭成分の除去に用いられ る脱臭材およびその製法並びに脱臭方法に関するものであり、 この 脱臭剤および脱臭方法は、 冷蔵庫、 トイ レ、 動物飼育舎、 汚水処理 場その他の脱臭に広く活用することができる。 従来の技術 The present invention relates to a deodorizing material used for removing malodorous components from a gas containing various malodorous components such as hydrogen sulfide, various mercaptans, ammonia and amines, a production method thereof, and a deodorizing method. The deodorization method can be widely used for deodorization in refrigerators, toilets, animal breeding houses, sewage treatment plants, and the like. Conventional technology
トイ レゃ冷蔵庫等の脱臭には、 従来より活性炭を主体とする吸着 材に悪臭成分を吸着させる吸着法、 およびオゾンと触媒を用いて悪 臭成分を酸化分解させる方法が主と して利用されてきた。 ところ 力 前者は活性炭の吸着作用を利用するものであって吸着容量に限 界があり、 長時間使用する場合や悪臭成分濃度が高い場合には、 活 性炭を頻繁に交換する必要がある。 また後者は、 オゾンの酸化力を 利用するものであり、 触媒との適正な組合せによつては半永久的な 脱臭が可能であるが、 オゾン発生器や高圧トランス等の専用設備を 必要とし、 設備費や運転経費が嵩むという難点が指摘される。  Conventionally, for deodorizing toy refrigerators, etc., the adsorption method of adsorbing odorous components on adsorbents mainly composed of activated carbon and the method of oxidizing and decomposing odorous components using ozone and a catalyst have been mainly used. Have been. However, the former uses the adsorption action of activated carbon and has a limited adsorption capacity. When used for a long time or when the concentration of odorous components is high, the activated carbon must be replaced frequently. The latter uses the oxidizing power of ozone, and can be semi-permanently deodorized by proper combination with a catalyst, but requires special equipment such as an ozone generator and high-pressure transformer. It is pointed out that the cost and operating cost increase.
ところで最近、 オゾンを添加することなく しかも加熱もせずに常 温で悪臭成分を除去することのできる触媒脱臭法が開発され注目を 集めている。 しかしながらこの方法では、 硫化水素ゃメチルメル力 ブタン等の如く反応性の高い悪臭成分の除去には有効であるが、 メ チルメルカブ夕ンから他の悪臭成分である二硫化メチルを副生した り、 あるいは硫化メチル、 アンモニア、 アミン類等の如く反応性の 低い悪臭成分については脱臭効果が不十分であり、 脱臭性能の改善 が望まれている。 By the way, recently, a catalyst deodorization method capable of removing malodorous components at room temperature without adding ozone and without heating has been developed and is attracting attention. However, this method is effective for the removal of highly reactive malodorous components such as hydrogen sulfide-methyl mercaptan butane, but it produced by-product methyl disulfide, another malodorous component, from methyl mercaptan. Alternatively, malodorous components having low reactivity, such as methyl sulfide, ammonia, and amines, have insufficient deodorizing effects, and improvement in deodorizing performance is desired.
本発明は、 この様な従来技術の問題点に着目してなされたもので あって、 その目的は、 反応性の高い悪臭成分はもとより、 反応性の 低い悪臭成分に対しても、 長期に直たり安定して優れた脱臭効果を 持続し得る様な脱臭材およびその製法、 並びに脱臭方法を提供しよ う とするものである。  The present invention has been made in view of such problems of the prior art. The purpose of the present invention is to provide a direct reaction for a long period of time not only for malodorous components having high reactivity but also malodorous components having low reactivity. It is an object of the present invention to provide a deodorizing material which can stably maintain an excellent deodorizing effect, a production method thereof, and a deodorizing method.
¾日月の ¾ sun moon
本発明の脱臭材は、 酸化銅、 酸化マンガンおよび硝酸銀からなる 脱臭成分が、 活性炭を含む担体素材に担持されたものであるところ にその特徴が存在する。 該脱臭材中における酸化銅、 酸化マンガン および硝酸銀の好ましい組成比は、 酸化銅 : C u 0換算で 0 . 5〜 1 0重量部、 酸化マンガン : M n 0 2 換算で 1〜 2 0重量部、 硝酸 銀 : A g N 0 3 換算で 1 ~ 2 0重量部の範囲であり、 また、 該脱臭 材中に占める酸化銅、 酸化マンガンおよび硝酸銀の総含有率は 3〜 3 0重量%の範囲が好ましい。 更に、 上記酸化銅、 酸化マンガンお よび硝酸銀よりなる脱臭成分は、 活性炭を主成分とする担体素材に 担持されるもので、 該担体素材に占める活性炭の含有量は、 3 0〜 7 0重量%の範囲であることが望ましく、 また脱臭材と しての比表 面積は 2 5 0 m 2 / 以上であるものが好ましい。 そしてこの脱臭 材を用いて、 硫化水素、 各種メルカブタン類、 アンモニア、 ァミ ン 類などの悪臭成分含有ガスを処理すれば、 これら悪臭成分が分解除 去され、 効率よく脱臭を行なうことができる。 The deodorizing material of the present invention is characterized in that a deodorizing component comprising copper oxide, manganese oxide and silver nitrate is carried on a carrier material containing activated carbon. Copper oxide in the deodorizing material, preferable composition ratio of manganese oxide and silver nitrate, copper oxide:. 0 C u 0 Convert 5-1 0 part by weight, manganese oxide: M n 0 2 terms at 1-2 0 parts by weight , silver nitrate: a g N 0 3 ranges from 1 to 2 0 parts by weight in terms, also copper oxide occupied in the deodorizing material, the total content of manganese oxide and silver nitrate ranges from 3 3 0 wt% Is preferred. Further, the deodorizing component consisting of copper oxide, manganese oxide and silver nitrate is carried on a carrier material containing activated carbon as a main component. The content of the activated carbon in the carrier material is 30 to 70% by weight. And the specific surface area as a deodorant is preferably 250 m 2 / or more. If this deodorizing material is used to treat a gas containing malodorous components such as hydrogen sulfide, various mercaptans, ammonia, and amines, these malodorous components are removed and the deodorization can be performed efficiently.
また本発明にかかる脱臭材の製法としての特徴は、 活性炭を含む 担体素材を所定形状に成形した後、 これに、 酸化銅、 酸化マンガン 及び硝酸銀またはそれらの前駆体を含む溶液を塗布または含浸さ せ、 非酸化性雰囲気下に硝酸銀の分解温度より低い温度で焼成する ところにあり、 この方法を採用することによって、 脱臭性能の優れ た脱臭材を得ることができる。 更に好ましい脱臭材の製造法として は、 酸化銅、 酸化マンガン及び硝酸銀またはそれらの前駆体を含む 溶液に、 硝酸銀に対し 1ノ3〜 1 2モル量のクェン酸を加えて活 性炭含有担体に塗布または含浸させ、 非酸化性雰囲気下に硝酸銀の 分解温度よ り低い温度で焼成する方法を採用すれば、 脱臭活性の一 段と優れた脱臭材をより確実に得ることができるので好ましい。 発明を実施するための最良の形態 Further, a feature of the method for producing a deodorizing material according to the present invention is that after a carrier material containing activated carbon is formed into a predetermined shape, copper oxide and manganese oxide are added thereto. And a solution containing silver nitrate or their precursors are applied or impregnated, and calcined in a non-oxidizing atmosphere at a temperature lower than the decomposition temperature of silver nitrate. Deodorizing material can be obtained. A more preferable method for producing a deodorizing material is to add a solution containing copper oxide, manganese oxide, silver nitrate or a precursor thereof to citric acid in an amount of 1 to 3 mol with respect to silver nitrate to form an activated carbon-containing carrier. It is preferable to adopt a method of applying or impregnating and firing in a non-oxidizing atmosphere at a temperature lower than the decomposition temperature of silver nitrate, because a more excellent deodorizing material can be obtained more reliably. BEST MODE FOR CARRYING OUT THE INVENTION
本発明者らは前述の様な従来技術の下で、 コス ト高につく オゾン 等を使用することなく又加熱処理を要することなく、 反応性の高い 悪臭成分はもとより反応性の低い悪臭成分に対しても、 長期に亘た り安定して優れた脱臭効果を持続し得る様な脱臭材の開発を期して 種々研究を進めてきた。  Under the above-mentioned conventional technology, the present inventors have developed a method of converting not only highly reactive malodor components but also less reactive malodor components without using costly ozone or the like and without requiring heat treatment. On the other hand, various researches have been conducted with the aim of developing a deodorizing material that can stably maintain an excellent deodorizing effect over a long period of time.
その結果、 酸化銅、 酸化マンガン、 硝酸銀の 3成分を主たる脱臭 活性成分として併用すると共に、 これらを保持もしくは担持するた めの主たる担体素材として活性炭を使用すれば、 優れた性能の脱臭 材が得られることを知った。 とりわけ、 脱臭材中に主たる脱臭成分 と して含有させる前記 3成分の組成比を、 酸化銅 : C u O換算で 0 . 5〜 1 0重量部、 酸化マンガン : M n 0 2 換算で 1〜 2 0重量 部、 硝酸銀 : A g N 0 3 換算で 1〜2 0重量部の範囲に設定し、 ま た脱臭材中に占めるこれら 3成分の総含有率を 3〜3 0重量%の範 囲に設定し、 更には、 前記脱臭成分を担持する担体素材における活 性炭の含有量が 3 0〜7 0重量%であるものを使用すれば、 本発明 の目的に叶う優れた脱臭性能を発揮することを見出した。 上記成分のうち酸化銅は多量の表面酸素を保有しており、 硫化水 素ゃメチルメルカブタンを常温で酸化分解する作用を発揮するが、 この酸化分解反応で消費された酸素は、 被処理ガス中に含まれる空 気中の酸素によって逐次補われるので、 その脱臭効果を長期間に亘 つて持続する。 As a result, if the three components of copper oxide, manganese oxide, and silver nitrate are used in combination as the main deodorizing active components, and activated carbon is used as the main carrier material for holding or supporting them, a deodorizing material with excellent performance can be obtained. I knew that it could be done. Especially, the composition ratio of the three components to be contained in the main deodorizing component in the deodorizing material, copper oxide:. 0 5-1 0 weight parts C u O terms, manganese oxide: 1 in M n 0 2 conversion 2 0 parts by weight, of silver nitrate: a g N 0 3 set in the range of 1 to 2 0 parts by weight in terms of, 3 to 3 the total content of these three components occupied in or deodorant 0 wt% range Further, if the activated carbon content of the carrier material supporting the deodorizing component is 30 to 70% by weight, excellent deodorizing performance meeting the object of the present invention is exhibited. I found to do. Of the above components, copper oxide has a large amount of surface oxygen and exerts the effect of oxidizing and decomposing hydrogen sulfide / methyl mercaptan at room temperature.The oxygen consumed in this oxidative decomposition reaction is Since it is gradually supplemented by the oxygen contained in the air, its deodorizing effect is maintained for a long time.
また酸化マンガンは、 前記した様な各種悪臭ガスに対して脱臭効 果を有効に発揮するが、 と りわけ、 上記酸化銅に起因して生じるメ チルメルカブ夕ンから二硫化メチルへの変換を抑制するうえで有効 に作用する。 こうした作用を有効に発揮させるには、 酸化銅に対す る配合比率で M n 0 2 / C u 0の重量比を 2以上とすることが好ま しい。 In addition, manganese oxide effectively exerts the deodorizing effect on the above-mentioned various odorous gases, but in particular, suppresses the conversion of methyl mercaptan into methyl disulfide caused by the copper oxide. It works effectively in doing so. To effectively exhibit such effects, arbitrariness preferred that the weight ratio of M n 0 2 / C u 0 and 2 or more blending ratio against copper oxide.
次に硝酸銀は、 本発明における最も特徴的な成分であり、 その強 力な酸化能力によって、 従来技術では除去困難であった反応性の低 い-悪臭成分、 殊にアンモニア、 卜 リメチルァミン、 硫化メチル、 ァ セトアルデヒ ド等の分解除去が可能となる。  Next, silver nitrate is the most characteristic component in the present invention, and its strong oxidizing ability makes it difficult to remove by conventional techniques. It is a low-reactive-odor component, especially ammonia, trimethylamine, methyl sulfide. Decomposition and removal of acetoaldehyde and the like are possible.
銀や酸化銀を脱臭成分の 1つとして利用することは既に公知であ るが、 これらは脱臭材調製時の熱処理によって金属銀の巨大粒子に なり易い性質を有しており、 この金属銀は悪臭ガスに対して不活性 である。 そこで銀を複合酸化物と して担持させる方法や過酸化物等 によって湿式酸化する方法等を採用し、 酸化銀として担体に担持さ せる方法が幾つか提案されているが、 複雑な工程が必要であるばか りでなく、 微粒子状態での分散担持が困難であり、 満足な脱臭効果 は得られていない。 しかるに本発明では、 従前の様に銀を酸化銀と して活用するのではなく、 これを硝酸銀の形態で活用することによ り、 銀の脱臭成分としての特性を最大限有効に発揮させたところに 大きな特徴を有している。  It is already known that silver or silver oxide is used as one of the deodorizing components, but these have a property that they tend to become large particles of metallic silver by heat treatment during the preparation of the deodorizing material. Inactive against odorous gas. Therefore, there have been proposed several methods of supporting silver as a composite oxide, wet oxidation with a peroxide or the like, and supporting silver as a silver oxide on a carrier. In addition, it is difficult to disperse and support in a fine particle state, and a satisfactory deodorizing effect has not been obtained. However, in the present invention, instead of utilizing silver as silver oxide as in the past, silver was utilized in the form of silver nitrate, thereby maximizing the effective use of silver as a deodorizing component. However, it has a great feature.
上記酸化銅、 酸化マンガンぉよび硝酸銀の作用を有効に発揮さ せるには、 脱臭材中におけるこれら 3成分の組成比を、 酸化銅 : C u O換算で 0 . 5〜 ; 1 0重量部 (よ り好ま し く は 1 〜 5重量 部) 、 酸化マンガン : M n 0 2 換算で 1〜 2 0重量部 (より好まし くは 2〜 1 0重量部) 、 硝酸銀 : A g N 0 3 換算で 1〜 2 0重量部 (より好ましくは 2〜 1 0重量部) の範囲に設定するのがよく、 酸 化銅が 0 . 5重量部未満、 酸化マンガンが 1重量部未満、 硝酸銀が 1重量部未満では、 夫々の効果が不十分になって悪臭成分に対する 分解作用が十分に発揮されず、 満足のいく脱臭効果が得られにく く なる。 Effectively exerts the effects of copper oxide, manganese oxide and silver nitrate To achieve this, the composition ratio of these three components in the deodorizing material is determined as follows: copper oxide: 0.5 to 100 parts by weight (more preferably 1 to 5 parts by weight) in terms of CuO, manganese oxide: M n 0 2 terms at 1-2 0 parts by weight (more preferably rather is 2-1 0 part by weight), silver nitrate: 1-2 0 parts by weight A g n 0 3 conversion (more preferably 2-1 0 weight If the amount of copper oxide is less than 0.5 part by weight, the amount of manganese oxide is less than 1 part by weight, and the amount of silver nitrate is less than 1 part by weight, the respective effects become insufficient and the odor components are reduced. The decomposition effect is not sufficiently exhibited, and it is difficult to obtain a satisfactory deodorizing effect.
但し、 酸化銅の組成比が 1 0重量部を超えると、 悪臭成分である メチルメルカブタンから他の悪臭成分である二硫化メチルへの変換 量が増大し、 脱臭効果が有効に発揮されにく くなる。 また、 酸化マ ンガンの組成比が 2 0重量部を超えたり、 硝酸銀の組成比が 1 0重 量部を超えても、 それ以上に脱臭効果の向上が認められないばかり 力 活性炭の吸着サイ 卜が低減して脱臭効果をかえって阻害する傾 向が生じてく るので好ましくない。  However, when the composition ratio of copper oxide exceeds 10 parts by weight, the amount of conversion from the malodorous component methyl mercaptan to the other malodorous component methyl disulfide increases, and the deodorizing effect is not effectively exerted. It becomes. Further, even if the composition ratio of manganese oxide exceeds 20 parts by weight or the composition ratio of silver nitrate exceeds 10 parts by weight, no further improvement in the deodorizing effect is observed, and the activated carbon adsorption site This tends to reduce the effect of deodorization on the contrary, which is undesirable.
また、 これら 3成分の複合による脱臭作用を有効に発揮させるに は、 脱臭材中に占めるこれら 3成分の総含有率を 3〜 3 0重量%、 より好ましくは 5〜 2 0重量%の範囲とするのがよく、 2重量%未 満では脱臭のための活性成分としての絶対量が不足気味となって脱 臭性能が不十分となり、 特に悪臭成分濃度の高いガスに適用したと きに満足な脱臭効果が得られにく くなり、 また上記 3成分の総含有 率が 3 0重量%を超えて過度に多くなると、 担体成分として作用す る活性炭の絶対量が不足気味となり、 後述する如く悪臭成分の吸着 サイ 卜が不足気味となってやはり満足な脱臭性能が得られにく くな る。  In order to effectively exhibit the deodorizing effect of the combination of these three components, the total content of these three components in the deodorizing material should be 3 to 30% by weight, more preferably 5 to 20% by weight. If the content is less than 2% by weight, the absolute amount as an active ingredient for deodorization tends to be insufficient and the deodorization performance is insufficient, and is particularly satisfactory when applied to a gas having a high concentration of malodorous components. If the deodorizing effect becomes difficult to obtain, and if the total content of the above three components exceeds 30% by weight and becomes excessively large, the absolute amount of activated carbon acting as a carrier component tends to be insufficient, and as described below, the odor is bad. The adsorption site of the components tends to be short, and it is difficult to obtain satisfactory deodorizing performance.
尚、 酸化銅の出発原料と しては硝酸銅、 硫酸銅および酸化銅等 力 また酸化マンガンの出発原料としては、 硝酸マンガン、 硫酸マ ンガン、 活性二酸化マンガン等が夫々好ましいものとして例示され る。 The starting materials for copper oxide include copper nitrate, copper sulfate and copper oxide. As a starting material for manganese oxide, manganese nitrate, manganese sulfate, activated manganese dioxide and the like are exemplified as preferable ones.
本発明で用いられる脱臭活性成分は上記 3成分を必須的に含有す るものであるが、 被処理ガス中に含まれる悪臭成分の種類によって は、 必要によ り更に他の脱臭活性成分としてニッケル、 鉄、 コバル ト、 クロム、 亜鉛、 バナジウム等の金属酸化物や白金族金属を適量 含有させることも可能である。 また、 金属銀、 酸化銀あるいは銅ま たはマンガンと銀との複合酸化物等が共存していても差し支えな い。 但しそれらの量は、 前記 3成分の作用効果を希釈することがな い様、 脱臭材中に占める比率で 5重量%程度以下、 より好ましくは 2重量%程度以下に抑えることが望ましい。  The deodorizing active component used in the present invention essentially contains the above three components. However, depending on the type of the malodorous component contained in the gas to be treated, if necessary, nickel may be used as another deodorizing active component. It is also possible to contain metal oxides such as iron, cobalt, chromium, zinc, and vanadium, and platinum group metals in appropriate amounts. In addition, metallic silver, silver oxide, copper, or a composite oxide of manganese and silver may coexist. However, the amounts thereof are desirably suppressed to about 5% by weight or less, more preferably about 2% by weight or less in the deodorizing material so as not to dilute the effects of the three components.
また、 これら脱臭のための活性成分を保持もしくは担持する担体 素材と しては、 必須成分と して活性炭を含み、 好ま しく は 3 0〜 7 0重量%、 より好ましくは 4 0〜6 0重量%の活性炭を含むもの が選択される。  The carrier material for holding or supporting the active ingredient for deodorization contains activated carbon as an essential ingredient, preferably 30 to 70% by weight, more preferably 40 to 60% by weight. % Is selected.
ここで、 活性炭を選択する理由は次の通りである。 即ち悪臭成分 は種々のガスの混合物からなるものであるが、 それら悪臭成分を分 解除去するには、 最初に悪臭成分を脱臭材に吸着トラップさせる必 要がある。 例えば塩基性ガスであるアンモニア等は、 酸性度の高い シリカやチタ二アーシリ力等の担体には吸着し易いが、 酸性ガスで ある硫化水素等は吸着されにく く、 塩基性の高い担体ではその逆と なる。 また中性ガスである硫化メチル等は酸性、 塩基性いずれの担 体にも殆んど吸着されない。 またゼォライ 卜等は、 細孔内にガスを 吸着する作用を有しているが、 細孔径ょりも小さい分子サイズの悪 臭成分をトラップする作用に乏しく、 また湿度により吸着トラップ 性能が劣化するという難点がある。 これに対し活性炭は、 それ自身中性であるが比表面積が非常に大 き くて微細な細孔を無数に有しているので、 酸性 · 塩基性 · 中性の いずれの悪臭成分ガスに対しても優れた吸着トラッブ効果を示す。 そして、 こう した活性炭の優れた吸着トラップ作用が前記脱臭成分 および悪臭成分の吸着サイ トとして有効に発揮され、 該吸着サイ ト に悪臭成分を効率よく吸着保持すると共に、 該吸着サイ トに担持さ れた前記脱臭活性成分の作用によって該悪臭成分が速やかに分解さ れ、 効率よく脱臭が進行するものと考えられる。 Here, the reason for choosing activated carbon is as follows. That is, the malodorous component is composed of a mixture of various gases, but in order to decompose and remove the malodorous component, it is necessary to first adsorb and trap the malodorous component on the deodorizing material. For example, ammonia, which is a basic gas, is easily adsorbed on a carrier such as silica or titania ash with high acidity, but hydrogen sulfide, which is an acid gas, is not easily adsorbed. The opposite is true. Almost no neutral gas, such as methyl sulfide, is adsorbed on acidic or basic carriers. In addition, zeolite has the effect of adsorbing gas into the pores, but has a poor effect of trapping malodorous components having a small molecular size with small pore size, and the adsorption trap performance is deteriorated by humidity. There is a disadvantage. Activated carbon, on the other hand, is neutral in its own right, but has a very large specific surface area and numerous micropores, making it resistant to any acidic, basic, or neutral odorous gas. Also exhibits excellent adsorption trap effect. Such an excellent adsorption trapping effect of the activated carbon is effectively exhibited as an adsorption site for the deodorizing component and the malodorous component. The adsorption site efficiently adsorbs and holds the malodorous component, and simultaneously carries the malodorous component on the adsorption site. It is considered that the malodorous component is promptly decomposed by the action of the deodorizing active component and the deodorization proceeds efficiently.
しかも本発明者らが確認したところによると、 前記で選択した 3 種の成分を含有する脱臭活性成分との関連においては、 活性炭の優 れた吸着トラッブ作用に由来する上記の効果を超える優れた脱臭効 果が得られることを確認しており、 前記特定された脱臭活性成分と 活性炭との間で何らかの相互作用が働いて脱臭効果を一段と高めて いるものと考えられる。 但しその理由については、 現在のところ未 解明である。  Moreover, the present inventors have confirmed that, in relation to the deodorizing active ingredient containing the three components selected above, an excellent effect exceeding the above-mentioned effect derived from the excellent adsorption trapping effect of activated carbon is obtained. It has been confirmed that a deodorizing effect can be obtained, and it is considered that some interaction between the specified deodorizing active ingredient and activated carbon acts to further enhance the deodorizing effect. However, the reason has not yet been elucidated.
こう した活性炭の作用効果を有効に発揮させるには、 担体素材中 の活性炭含有率を 3 0〜7 0重量%、 より好ましくは 4 0〜 6 0重 量%の範囲に設定するのがよく、 活性炭の含有量が 3 0重量%未満 であるときは、 活性炭によってもたらされる上記の作用が不十分と なって満足のいく脱臭性能が発揮されにく くなる。 一方活性炭の含 有率が 7 0重量%を超えると、 相対的にバインダ一成分の量が不足 気味となって担体の物理強度が低下し、 使用時に破損や粉末剥離を 起こす等の問題が生じてくる。  In order to effectively exert such an effect of activated carbon, the content of activated carbon in the carrier material is preferably set in the range of 30 to 70% by weight, more preferably 40 to 60% by weight. When the content of the activated carbon is less than 30% by weight, the above-mentioned effects provided by the activated carbon become insufficient, and it becomes difficult to exhibit satisfactory deodorizing performance. On the other hand, if the content of activated carbon exceeds 70% by weight, the amount of one component of the binder tends to be relatively short, and the physical strength of the carrier is reduced, causing problems such as breakage and powder peeling during use. Come.
活性炭を含む担体素材は、 所定量の活性炭粉末をシリカ -アルミ ナ、 シリカ、 アルミナ、 チタニア、 ゼォライ ト、 チタ二アーシリカ 複合酸化物等のセラミ ック系バインダーと共に均一に混合し、 ペレ ッ ト状、 板状、 ハニカム状など任意の形状に成形してから乾燥もし くは非酸化性雰囲気下で加熱焼成することによって得ることができ る。 For a carrier material containing activated carbon, a predetermined amount of activated carbon powder is uniformly mixed with a ceramic-based binder such as silica-alumina, silica, alumina, titania, zeolite, titania silica composite oxide, etc. , Plate, honeycomb, etc. Alternatively, it can be obtained by firing under heating in a non-oxidizing atmosphere.
本発明の脱臭材は、 後述する様な方法で上記担体に前述の 3成分 を必須的に含む脱臭成分を担持させることによって製造されるが、 脱臭効果をより効果的に発揮させるには、 脱臭材としての比表面積 が 2 5 0 m 2 Z g以上、 より好ましくは 3 5 0 m 2 Z g以上とする ことが望ましい。 しかして悪臭成分の脱臭は、 前述の如く まず悪臭 成分が脱臭材の吸着サイ 卜に吸着トラップされ、 該吸着サイ ト内で 脱臭成分の作用を受けて無臭成分に分解されると考えられるので、 脱臭効果を高めるには吸着サイ トをできるだけ多くすることが有効 であり、 そのためには、 脱臭材の比表面積を可及的に大きく するこ とが有効であるからである。 尚、 活性炭主体の担体を使用すれば、 活性炭の比表面積が非常に大きいので、 2 5 0 m 2 Z g以上の比表 面積を容易に確保することができる。 The deodorizing material of the present invention is produced by supporting a deodorizing component essentially containing the above-mentioned three components on the above-mentioned carrier by a method as described below. To make the deodorizing effect more effective, deodorizing material is used. It is desirable that the specific surface area of the material be at least 250 m 2 Zg, more preferably at least 350 m 2 Zg. As described above, it is considered that the deodorization of the offensive odor component is, first, that the offensive odor component is adsorbed and trapped on the adsorption site of the deodorant, and is decomposed into the odorless component by the action of the deodorant component in the adsorption site. In order to enhance the deodorizing effect, it is effective to increase the number of adsorption sites as much as possible. For that purpose, it is effective to increase the specific surface area of the deodorizing material as much as possible. In addition, if a carrier mainly composed of activated carbon is used, the specific surface area of activated carbon is very large, so that a specific surface area of 250 m 2 Zg or more can be easily secured.
脱臭材の製造方法としては、 酸化銅、 酸化マンガン及び硝酸銀ま たはそれらの前駆体を、 所定量の活性炭を含む担体素材と混練して 成形する方法、 あるいは担体素材を用いて前述の如くペレツ ト状ゃ ハニカム状等に成形した後、 脱臭活性成分あるいはその前駆体を担 持させる方法等を採用することができるが、 好ましいのは後者の方 法、 具体的には、 活性炭を含む担体素材を常法により任意の形状に 成形した後、 脱臭活性成分の前駆体を含む水溶性塩の混合溶液を塗 布もしくは含浸させ、 乾燥乃至焼成する方法である。  As a method for producing the deodorizing material, a method of kneading copper oxide, manganese oxide, silver nitrate, or a precursor thereof and a carrier material containing a predetermined amount of activated carbon to form the pellet, or using a carrier material to pelletize as described above. After forming into a honeycomb shape or the like, a method of supporting the deodorizing active component or a precursor thereof can be adopted, but the latter method is preferred, specifically, a carrier material containing activated carbon. Is formed into an arbitrary shape by a conventional method, and then coated or impregnated with a mixed solution of a water-soluble salt containing a precursor of a deodorizing active ingredient, and dried or fired.
この方法を採用すれば、 活性炭主体の担体の吸着サイ 卜壁面に前 述の脱臭活性成分が担持されることになり、 脱臭処理工程では該吸 着サイ 卜に吸着トラッブされた悪臭成分に脱臭活性成分が速やかに 作用するからである。  If this method is adopted, the aforementioned deodorizing active component will be carried on the adsorption site wall surface of the activated carbon-based carrier. In the deodorizing treatment step, the deodorizing active component will be deodorized to the malodor component adsorbed and trapped on the adsorption site. This is because the components act quickly.
上記の製法を実施するに当たっては、 脱臭活性成分のうち特に硝 酸銀の活性を有効に引き出すため、 硝酸銀を含めて前記 3成分もし く はそれらの前駆体を含む溶液を担体に塗布もしく は含浸させた 後焼成する際に、 処理雰囲気を窒素などの非酸化性雰囲気とする と共に、 焼成温度を硝酸銀の分解温度未満、 好ましく は 2 0 0〜 4 0 0 * の範囲に制御する必要がある。 In carrying out the above-mentioned production method, among the deodorizing active ingredients, In order to effectively extract the activity of silver acid, when the carrier is coated with or impregnated with a solution containing the above three components or their precursors including silver nitrate and then calcined, the treatment atmosphere is changed to a non-nitrogen atmosphere. In addition to the oxidizing atmosphere, it is necessary to control the sintering temperature below the decomposition temperature of silver nitrate, preferably in the range of 200 to 400 *.
しかして、 焼成を酸化性雰囲気で行ない、 あるいは焼成温度が 4 0 0 を越えて硝酸銀の分解温度以上になると、 硝酸銀の酸化若 しく は分解が起こって本発明の効果が有効に発揮されなく なるから である。 尚焼成温度の下限は特に規定しないが、 硝酸銀を含めた脱 臭活性成分の活性化と担持をより確実に行なう意味から、 焼成温度 は 2 0 O 'C以上に設定することが望ましい。  If the firing is performed in an oxidizing atmosphere, or the firing temperature exceeds 400 and exceeds the decomposition temperature of silver nitrate, the oxidation or decomposition of silver nitrate occurs and the effect of the present invention cannot be exhibited effectively. From. Although the lower limit of the firing temperature is not particularly defined, the firing temperature is desirably set to 20 O'C or more from the viewpoint of more securely activating and supporting the deodorizing active component including silver nitrate.
ところで硝酸銀は酸化性の高い化合物であり、 還元され易い物質 の共存下で通元され易く、 硝酸銀を含む溶液に活性炭を含む担体を 含浸すると、 担体の表面に金属銀の析出が見られる。 こう した現象 が本発明にとって好ましくないことは、 前述の説明から容易に理解 されるところであるが、 前記 3成分を含む溶液に、 硝酸銀に対して 1 Z 3〜 1 Z 2モル量のクェン酸を含有させると、 金属銀の析出が 著しく抑えられ、 硝酸銀としての担持がより確実に行なわれること が確認された。 その理由は必ずしも明確にされた訳ではないが、 ク ェン酸は担体に白金族金属を担持させるときの競争吸着剤として有 効に作用することが確認されており、 同様の作用によって活性炭の 硝酸銀との反応サイ トを保護する役割を果たしているものと考えて いる。 rnm  By the way, silver nitrate is a compound having a high oxidizing property, and is easily passed in the presence of a substance that is easily reduced. When a solution containing silver nitrate is impregnated with a carrier containing activated carbon, precipitation of metallic silver is observed on the surface of the carrier. It is easily understood from the above description that such a phenomenon is not preferable for the present invention.However, the solution containing the three components is mixed with citric acid in an amount of 1Z3 to 1Z2 mol based on silver nitrate. It was confirmed that when contained, the precipitation of metallic silver was remarkably suppressed, and loading as silver nitrate was more reliably performed. Although the reason has not been clearly clarified, it has been confirmed that citric acid effectively acts as a competitive adsorbent when the platinum group metal is supported on the carrier. We believe it plays a role in protecting the reaction site with silver nitrate. rnm
以下、 実施例を挙げて本発明をより具体的に説明するが、 本発明 はもとより下記実施例によって制限を受けるものではなく、 前 · 後 記の趣旨に適合し得る範囲で適当に変更を加えて実施することも可 能であり、 それらはいずれも本発明の技術的範囲に包含される。 実施例 1 Hereinafter, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to the following examples. It is also possible to implement the present invention with appropriate modifications within a range that can conform to the gist of the description, and all of them are included in the technical scope of the present invention. Example 1
椰子殻活性炭粉末 (比表面積 1 5 0 0 m 2 / g ) を粘土鉱物系 無機バイ ンダー (組成 : A 1 2 0 a 4 0重量% , S i 0 2 6 0重 量%) 及びセルロース系有機バインダーと混練し、 押出し成形した 後乾燥 · 焼成して活性炭含有率が 4 5重量%のハニカム状担体を製 造した。 得られたハニカム状担体を、 硝酸銅、 硝酸マンガン、 硝酸 銀をそれぞれ表 1 に示す C u O : M n 0 2 : A g N 0 3 換算比率で 含有すると共に、 硝酸銀に対して 0 . 4倍モル量のクェン酸を溶解 した混合水溶液に含浸し、 余剰液をエアーブローにより除去してか ら 1 0 0でで通風乾燥した後、 窒素雰囲気中 3 0 0 *0で 2時間焼成 して脱臭材を得た。 得られた脱臭材の組成を表 1 に示した。 Coconut shell activated carbon powder (specific surface area 1 5 0 0 m 2 / g ) of the clay mineral-based inorganic by Nda (composition: A 1 2 0 a 4 0 wt%, S i 0 2 6 0 by weight%) and cellulose based organic It was kneaded with a binder, extruded, dried and fired to produce a honeycomb-shaped carrier having an activated carbon content of 45% by weight. The resulting honeycomb carrier, copper nitrate, C u O shown manganese nitrate, silver in Tables 1: M n 0 2:. While contained in A g N 0 3 conversion ratio, 0 for silver nitrate 4 Impregnated with a mixed aqueous solution in which double molar amount of citric acid was dissolved, the excess liquid was removed by air blow, then dried by ventilation at 100, and calcined in nitrogen atmosphere at 300 * 0 for 2 hours. A deodorant was obtained. Table 1 shows the composition of the obtained deodorizing material.
実施例 2〜 5 , 参考例 1  Examples 2 to 5, Reference example 1
実施例 1 において、 活性炭の配合量および脱臭活性成分の含有比 率を表 1 に示す様に変更した以外は実施例 1 と同様にして脱臭材を 製造した。  A deodorizing material was produced in the same manner as in Example 1 except that the blended amount of the activated carbon and the content ratio of the deodorizing active component were changed as shown in Table 1.
(比較例 1 〜 3 )  (Comparative Examples 1 to 3)
実施例 1 において、 表 1 に示す如く必須成分の一部を省略した以 外は実施例 1 と同様にして比較脱臭材を製造した。  A comparative deodorizing material was produced in the same manner as in Example 1 except that some of the essential components were omitted as shown in Table 1.
(比較例 4 )  (Comparative Example 4)
活性アルミナを用いて製造した八二カム状担体を、 硝酸マンガン 及び硝酸銀の混合水溶液に含浸して乾燥した後、 空気中で 5 0 0 C で 2時間焼成して比較脱臭材を得た。 得られた脱臭材の組成は表 1 に示した。  The 82 cam-shaped carrier produced using activated alumina was impregnated with a mixed aqueous solution of manganese nitrate and silver nitrate, dried, and calcined at 500 C for 2 hours in the air to obtain a comparative deodorizing material. Table 1 shows the composition of the obtained deodorant.
(参考例 2 )  (Reference example 2)
実施例 1 において、 クェン酸を添加しなかった以外は実施例 1 と 同様にして参考脱臭材を得た。 Example 1 was the same as Example 1 except that citrate was not added. Similarly, a reference deodorant was obtained.
(参考例 3 )  (Reference example 3)
実施例 1 において、 窒素雰囲気での焼成温度を 1 5 0 で 2時間 に変更した以外は実施例 1 と同様にして参考脱臭材を得た。  A reference deodorant was obtained in the same manner as in Example 1 except that the firing temperature in a nitrogen atmosphere was changed to 150 at 2 hours.
(参考例 4 )  (Reference example 4)
実施例 1 において、 窒素雰囲気での焼成温度を 5 0 0 °Cで 2時間 に変更した以外は実施例 1 と同様にして参考脱臭材を得た。  A reference deodorizing material was obtained in the same manner as in Example 1, except that the firing temperature in a nitrogen atmosphere was changed to 500 ° C. for 2 hours.
[脱臭材としての評価]  [Evaluation as a deodorant]
脱臭性能は流通系の反応装置を使用し、 各脱臭材を充填した充填 層の入口側及び出口側のガスを採取してガスクロマトグラフィ一に よ り各悪臭成分ガスの澳度を測定し、 悪臭成分の除去効率を求め た。 悪臭ガスと してはメチルメルカブタン、 硫化メチル、 ト リ メチ ルアミンの 3種類を選定し、 入口濃度を l O p p mとし 2 5 °C, 湿 度 5 0 % R Hで空間速度を 5 0, 0 0 0 H r の条件で評価した。 尚.メチルメルカブタンについては、 充填層出口部で検出されるニ硫 化メチルのガス溏度も測定した。 実施例、 比較例、 参考例の各脱臭 材について、 ガスの流通開始から 2時間経過後に測定した結果を表 2に示した。 The deodorization performance was measured using a flow-through reactor, collecting gas at the inlet and outlet of the packed bed filled with each deodorant, measuring the odor of each odorous component gas by gas chromatography, and The removal efficiency of the components was determined. Three types of malodorous gases were selected: methyl mercaptan, methyl sulfide, and trimethylamine, with an inlet concentration of lO ppm and a space velocity of 50, 0 at 25 ° C, 50% humidity and 50% RH. Evaluation was made under the condition of 0 0 H r. For methyl mercaptan, the gas concentration of methyl disulfide detected at the outlet of the packed bed was also measured. Table 2 shows the measurement results of the deodorizing materials of Examples, Comparative Examples, and Reference Examples 2 hours after the start of gas flow.
脱 オ中の脱臭活賊分含有率 脱臭材の 担体基材の材質 (w t%) 比表面積 Deodorizing pirate content during deodorization Deodorizing material carrier base material (wt%) Specific surface area
CuO Μηθ2 A NOa 讓列 1 活髓 (含有率 45%) 2 10 4 380 CuO Μηθ2 A NOa Substring 1 Active marrow (content 45%) 2 10 4 380
2 同 上 4 8 4 3752 Same as above 4 8 4 375
3 同 上 8 4 4 3803 Same as above 8 4 4 380
Λ 2 4 2 uUU o c 2 4 8 lU 参考例 1 活搬 (含有率 10%) 2 4 6 150 比較例 1 活髓 (含有率 45%) 12 0 4 380Λ 2 4 2 uUU o c 2 4 8 lU Reference example 1 Active (content 10%) 2 4 6 150 Comparative example 1 Active marrow (content 45%) 12 0 4 380
2 同 上 0 12 4 3702 Same as above 0 12 4 370
3 同 上 10 2 0 3753 Same as above 10 2 0 375
4 活性アルミナ 0 12 4 160 4 Activated alumina 0 12 4 160
メチルメルカブタン winし,キノ し 卜 リ メ手 レア- 、ノ Methyl mercaptan win and win
脱臭効率 脱臭効率 出口二硫化メチ  Deodorization efficiency Deodorization efficiency Outlet disulfide
ノ Jlレ iM f¾tf innUmU) (%) (%) 卖 ^^施Hli例l 1 9 8 0. 0 5以下 9 6 98  No Jll iM f¾tf innUmU) (%) (%) 卖 ^^ Hli example l 1 9 8 0.
2 9 9 0. 05以下 9 5 9 7 r> Q A Q C O 9 9 0. 08  2 9 9 0.05 or less 9 5 9 7 r> Q A Q C O 9 9 0.08
4 99 0. 0 5以下 95 98 4 99 0.05 or less 95 98
5 9 7 0. 0 5以下 97 98 参考例 1 9 6 0. 1 2 88 9 0 比較例 1 y y U . O Z 90 8 5 5 9 7 0. 0 5 or less 97 98 Reference example 1 9 6 0.12 88 9 0 Comparative example 1 y y U. O Z 90 8 5
2 8 2 0. 0 5以下 9 3 94 2 8 2 0. 0 5 or less 9 3 94
3 9 9 0. 09 65 7 33 9 9 0.09 65 7 3
4 78 1 . 60 3 1 4 9 参考例 2 98 0. 34 68 7 2 4 78 1 .60 3 1 4 9 Reference example 2 98 0.34 68 7 2
3 7 5 0. 2 2 70 6 3 3 7 5 0.2 2 70 6 3
4 9 5 0. 4 5 78 7 5 4 9 5 0. 4 5 78 7 5
表 1 , 2からも明らかである様に、 本発明の規定要件を全て満足 する実施例の脱臭材は、 比較例の脱臭材に比べて各種悪臭ガスに対 して高い脱臭性能を有しており、 担体素材や脱臭活性成分の配合比 の最適化によって卓越した脱臭性能を示すことを確認できる。 また 参考例は、 本発明で好ましい条件として推奨する要件を外れる製法 を採用したものであり、 得られる脱臭材の脱臭活性は、 担体素材中 に占める活性炭の含有率や製造条件によっても変わってく ることを 確認することができる。 発明の効果 As is clear from Tables 1 and 2, the deodorizing materials of Examples that satisfy all the requirements of the present invention have higher deodorizing performance against various odorous gases than the deodorizing materials of Comparative Examples. It can be confirmed that excellent deodorizing performance is exhibited by optimizing the mixing ratio of the carrier material and the deodorizing active ingredient. Further, the reference example adopts a production method which deviates from the requirements recommended as preferable conditions in the present invention, and the deodorizing activity of the obtained deodorizing material varies depending on the content of activated carbon in the carrier material and the production conditions. Can be confirmed. The invention's effect
本発明は以上の様に構成されており、 硫化水素ゃメチルメルカブ タン等の如く反応性の高い悪臭成分はもとより、 硫化メチル、 アン モニァ、 アミ ン類等の如く反応性の低い悪臭成分に対しても優れた 脱臭作用を示し、 またメチルメルカブ夕ンから他の悪臭成分である 二硫化メチルを副生することもなく、 悪臭成分を効率よく分解除去 できるので、 冷蔵庫、 トイ レ、 動物飼育舎、 汚水処理場その他の脱 臭に広く活用することができる。  The present invention is constituted as described above, and is used not only for malodorous components having high reactivity such as hydrogen sulfide / methyl mercaptan, but also for malodorous components having low reactivity such as methyl sulfide, ammonia and amines. Also has an excellent deodorizing effect, and can efficiently decompose and remove malodorous components without producing by-products other methyl sulfide, methyl disulfide, from methyl mercaptan, so refrigerators, toilets, animal breeding houses, and sewage It can be widely used for deodorization in treatment plants and others.

Claims

請 求 の 範 囲 The scope of the claims
1 . 活性炭を含む担体素材に、 酸化銅、 酸化マンガンおよび硝酸 銀からなる脱臭成分が担持されたものであることを特徴とする脱臭 材。  1. A deodorizing material characterized in that a carrier material containing activated carbon is loaded with a deodorizing component comprising copper oxide, manganese oxide and silver nitrate.
2. 脱臭材中における酸化銅、 酸化マンガンおよび硝酸銀の組成 比が、 酸化銅 : C υ 0換算で 0. 5〜 1 0重量部、 酸化マンガン : Μ η 02 換算で 1〜 2 0重量部、 硝酸銀 : A g N 03 換算で 1〜 20重量部である請求項 1に記載の脱臭材。 2. copper oxide in the deodorizer, the composition ratio of manganese oxide and silver nitrate, copper oxide: 0.5 to 1 0 weight parts C upsilon 0 terms, manganese oxide: Micromax eta 0 2 terms at 1-2 0 parts by weight , silver nitrate: a g N 0 3 deodorizing material according to 1 to claim 1 which is 20 parts by weight basis.
3. 脱臭材中に占める酸化銅、 酸化マンガンおよび硝酸銀の総含 有率が 3~30重量%である請求項 1 または 2に記載の脱臭材。  3. The deodorizing material according to claim 1, wherein the total content of copper oxide, manganese oxide, and silver nitrate in the deodorizing material is 3 to 30% by weight.
4. 担体素材が、 活性炭を 30〜70重量%含有するものである 請求項 1 ~ 3のいずれかに記載の脱臭材。  4. The deodorizing material according to any one of claims 1 to 3, wherein the carrier material contains 30 to 70% by weight of activated carbon.
5. 脱臭材の比表面積が 2 50 m2 g以上である請求項 1〜4 のいずれかに記載の脱臭材。 5. deodorizing material according to any one of claims 1 to 4 specific surface area of the deodorizing material is 2 50 m 2 g or more.
6. 活性炭を含む担体素材を所定形状に成形した後、 これに、 酸 化銅、 酸化マンガン及び硝酸銀またはそれらの前駆体を含む溶液を 塗布または含浸させ、 非酸化性雰囲気下に硝酸銀の分解温度よ り低 い温度で焼成することを特徴とする脱臭材の製法。  6. After shaping the carrier material containing activated carbon into a prescribed shape, apply or impregnate a solution containing copper oxide, manganese oxide, silver nitrate or their precursors, and decompose the silver nitrate under a non-oxidizing atmosphere. A method for producing deodorants characterized by firing at lower temperatures.
7. 酸化銅、 酸化マンガン及び硝酸銀またはそれらの前駆体を含 む溶液に、 硝酸銀に対し 1 Z3〜 1 Z2モル量のクェン酸を加えた ものを使用する請求項 6に記載の製法。  7. The method according to claim 6, wherein a solution containing copper oxide, manganese oxide, silver nitrate or a precursor thereof and citrate in an amount of 1 Z3 to 1 Z2 mol based on silver nitrate is used.
8. 請求項 1〜5のいずれかに記載の脱臭材を用いて臭気成分含 有ガスを処理することを特徴とする脱臭方法。  8. A deodorizing method comprising treating an odorous component-containing gas using the deodorizing material according to any one of claims 1 to 5.
PCT/JP1996/000140 1995-01-27 1996-01-24 Deodorant material, process for producing the same, and method of deodorization WO1996022827A1 (en)

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JP2005279631A (en) * 2004-03-02 2005-10-13 Idemitsu Kosan Co Ltd Method for manufacturing sulfur compound removing adsorbent, sulfur compound removing adsorbent and method for removing sulfur compound

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CN100444950C (en) * 2006-03-03 2008-12-24 中国人民解放军63971部队 Immesion active carbon and its preparation method
CN104096255A (en) * 2013-04-09 2014-10-15 潘运平 Adsorbable deodorant and preparation method thereof
CN108837800A (en) * 2018-06-16 2018-11-20 高士雄 A kind of peculiar smell adsorption agent and preparation method thereof for refrigerator taste removal
CN110860204A (en) * 2019-12-01 2020-03-06 陈洁琼 Solid deodorant and preparation method thereof
US20230040547A1 (en) * 2019-12-25 2023-02-09 Nikki-Universal Co., Ltd. Deodorizing catalyst, slurry for forming deodorizing catalyst, deodorizing catalyst structure, method for producing deodorizing catalyst structure and deodorization method
CN114632540A (en) * 2020-12-15 2022-06-17 青岛品森环保科技有限公司 Preparation method of composite oxide modified ZSM-5 molecular sieve catalysis odor-removal module
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KR100457699B1 (en) * 2001-10-09 2004-11-18 (주)대동 에이씨 Deodorant and method for making the same using multiporous adsorbent
JP2005279631A (en) * 2004-03-02 2005-10-13 Idemitsu Kosan Co Ltd Method for manufacturing sulfur compound removing adsorbent, sulfur compound removing adsorbent and method for removing sulfur compound

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KR970701583A (en) 1997-04-12
TW278042B (en) 1996-06-11

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