JPH10263391A - Odor component-containing gas deodorant, deodorizing method using the same, and method for regenerating the deodorant - Google Patents
Odor component-containing gas deodorant, deodorizing method using the same, and method for regenerating the deodorantInfo
- Publication number
- JPH10263391A JPH10263391A JP9071884A JP7188497A JPH10263391A JP H10263391 A JPH10263391 A JP H10263391A JP 9071884 A JP9071884 A JP 9071884A JP 7188497 A JP7188497 A JP 7188497A JP H10263391 A JPH10263391 A JP H10263391A
- Authority
- JP
- Japan
- Prior art keywords
- deodorant
- clay mineral
- odor
- mol
- hydrothermal synthesis
- 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.)
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明はゴミ焼却場、下水処
理場、家畜飼育場、肥料製造工場、発酵食品製造加工工
場など一般に悪臭発生源となる施設における高濃度且つ
複合された臭気を含む空気や排ガスを脱臭するための脱
臭剤、該脱臭剤を用いる脱臭方法、及び該脱臭剤の再生
処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to air containing high concentration and combined odor in facilities that generally generate odors, such as garbage incineration plants, sewage treatment plants, livestock breeding plants, fertilizer production plants, and fermented food production processing plants. The present invention relates to a deodorant for deodorizing gas and exhaust gas, a deodorizing method using the deodorant, and a method for regenerating the deodorant.
【0002】[0002]
【従来の技術】下水処理場やゴミ焼却場における吸着剤
として従来使用されている活性炭や合成ゼオライトは、
複合臭気に対する吸着性能が未だ実用上満足すべきもの
ではない。例えば活性炭は、アンモニア、硫化水素、酪
酸、吉草酸などの臭気ガスの塩基性度や酸性度に応じ
て、それぞれ各種薬品を添着する必要があり、複合臭気
に対しては数種類の組合わせ使用を要する。また、ゼオ
ライトはガス中の水分含有量が多い場合には吸着性能が
劣化しやすい。2. Description of the Related Art Activated carbon and synthetic zeolites conventionally used as adsorbents in sewage treatment plants and garbage incineration plants are:
The adsorption performance for complex odor is not yet satisfactory in practical use. For example, activated carbon requires various chemicals to be impregnated according to the basicity and acidity of odor gas such as ammonia, hydrogen sulfide, butyric acid, and valeric acid. It costs. In addition, the adsorption performance of zeolite is apt to deteriorate when the water content in the gas is large.
【0003】[0003]
【発明が解決しようとする課題】本発明は、臭気含有ガ
ス中の臭気成分、特にアンモニア、メルカプタン、硫化
メチル、硫化水素、トリメチルアミン、酪酸、吉草酸な
ど塩基性から酸性に亘る複合臭気ガスに対して1種類で
実用的な効果を持つ複合臭気用脱臭剤の提供、この脱臭
剤を用いる脱臭方法、及びこの脱臭剤の使用後の再生処
理方法の提供を課題とする。DISCLOSURE OF THE INVENTION The present invention relates to an odor component in an odor-containing gas, particularly to a complex odor gas ranging from basic to acidic, such as ammonia, mercaptan, methyl sulfide, hydrogen sulfide, trimethylamine, butyric acid, and valeric acid. It is an object of the present invention to provide a deodorizing agent for a complex odor which has one kind of practical effect, a deodorizing method using the deodorizing agent, and a regeneration treatment method after using the deodorizing agent.
【0004】[0004]
【課題を解決するための手段】臭気成分を除去するため
の脱臭剤として、請求項1では組成比がシリカ(SiO
2 )20−70モル%、アルミナ(Al2 O3 )5−2
0モル%、三酸化二鉄(Fe2 O3 )0−10モル%、
マグネシア(MgO)0−15モル%、結晶水(H
2 O)5−20モル%である層構造粘土鉱物を50℃−
100℃の温度で、1−5時間第一段水熱合成した後、
さらに150℃−250℃で1−3時間第二段水熱合成
してなる粘土鉱物微結晶を主成分とする臭気含有ガス脱
臭剤を提供する。As a deodorant for removing odorous components, in claim 1, the composition ratio is silica (SiO 2).
2 ) 20-70 mol%, alumina (Al 2 O 3 ) 5-2
0 mol%, diiron trioxide (Fe 2 O 3 ) 0-10 mol%,
Magnesia (MgO) 0-15 mol%, water of crystallization (H
2 O) 5-20 the layer structure clay mineral is a mol% 50 ° C. -
After the first-stage hydrothermal synthesis at a temperature of 100 ° C. for 1-5 hours,
Further, the present invention provides an odor-containing gas deodorizing agent mainly composed of clay mineral microcrystals obtained by hydrothermal synthesis at 150 ° C. to 250 ° C. for 1-3 hours.
【0005】請求項2の発明では、水熱合成後の上記粘
土鉱物をさらに酸処理することにより、酸強度関数(H
0 )で表示した固体酸性度を−3.0≦H0 ≦−0.5
の範囲に調整してなる粘土鉱物微結晶を主成分とする脱
臭剤を提供する。According to the second aspect of the present invention, the clay mineral after the hydrothermal synthesis is further subjected to an acid treatment to obtain an acid strength function (H
0 ) is -3.0 ≦ H 0 ≦ −0.5
The present invention provides a deodorant containing clay mineral microcrystals as a main component and adjusted to the range described above.
【0006】請求項3の発明では、上記請求項1または
2記載の粘土鉱物微結晶に長周期型周期律表第4周期の
7A族、8族、及び1B族、または白金族元素よりなる
群(即ち、Mn、Fe、Co、Ni、Cu、またはP
d、Pt等)よりなる群から選ばれる少なくとも1種類
以上の金属もしくは金属酸化物を担持してなる粘土鉱物
微結晶を主成分とする脱臭剤を提供する。In a third aspect of the present invention, there is provided the clay mineral microcrystal according to the first or second aspect, wherein the group comprises a 7A group, a 8 group, a 1B group, or a platinum group element of the fourth period of the long period type periodic table. (Ie, Mn, Fe, Co, Ni, Cu, or P
d, Pt, etc.) The present invention provides a deodorant mainly composed of clay mineral microcrystals supporting at least one metal or metal oxide selected from the group consisting of:
【0007】請求項4の発明では、臭気含有ガスを上記
請求項1、2または3記載の脱臭剤と−40℃−100
℃の温度においてガス圧力が1−10kg/cm2 、G
HSVが1,000−95,000h- 1 の条件下で接
触させることを特徴とする臭気含有ガスの脱臭方法を提
供する。According to a fourth aspect of the present invention, the odor-containing gas is mixed with the deodorant of the first, second or third aspect at -40.degree.
At a gas pressure of 1-10 kg / cm 2 ,
Provided is a method for deodorizing an odor-containing gas, wherein the contact is performed under the conditions of an HSV of 1,000 to 95,000 h -1 .
【0008】さらに請求項5の発明では、脱臭処理に使
用後の請求項3記載の脱臭剤を温度100℃−500℃
加熱処理することを特徴とする脱臭剤の再生処理方法を
提供する。Further, in the invention according to claim 5, the deodorant according to claim 3 used in the deodorizing treatment is used at a temperature of 100 ° C. to 500 ° C.
Provided is a method for regenerating a deodorant, which comprises performing a heat treatment.
【0009】[0009]
【発明の実施の形態】本発明に使用する原料鉱物は、組
成比がSiO2 :20−70モル%、Al2O3 :5−
20モル%、Fe2 O3 :0−10モル%、 MgO:
0−10モル%、H2 O:5−20モル%である粘土鉱
物であって、基本骨格構造として層構造を有し、微結晶
の粒子形態を有する粘土鉱物である。具体的には天然の
モンモリロナイト、ベントナイト、或いはこれらの精製
物、上記組成比を有する合成物等を例示できる。請求項
1の発明では、この原料鉱物を2段階の水熱合成処理し
て脱臭性能を強化する。即ち、公知の方法を用いて前記
層構造粘土鉱物を温度50℃−100℃にて1−5時間
第一段水熱合成を行い、その後さらに150℃−250
℃で1−3時間第二段水熱合成を行って得た粘土鉱物微
結晶を本発明の脱臭剤の主成分として使用する。通常上
記主成分と多孔質性付与鉱物との混合物を押出成形等の
常法により造粒し、焼成して脱臭剤とする。BEST MODE FOR CARRYING OUT THE INVENTION The raw material mineral used in the present invention has a composition ratio of SiO 2 : 20-70 mol%, Al 2 O 3 : 5-
20 mol%, Fe 2 O 3: 0-10 mol%, MgO:
A clay mineral having 0 to 10 mol% and H 2 O: 5 to 20 mol%. The clay mineral has a layer structure as a basic skeleton structure and has a microcrystalline particle form. Specific examples include natural montmorillonite and bentonite, purified products thereof, and synthetic products having the above composition ratios. In the invention of claim 1, the raw material mineral is subjected to a two-stage hydrothermal synthesis treatment to enhance the deodorizing performance. That is, the layered clay mineral is subjected to the first-stage hydrothermal synthesis at a temperature of 50 ° C. to 100 ° C. for 1 to 5 hours by using a known method, and then further at 150 ° C. to 250 ° C.
Clay mineral microcrystals obtained by performing the second stage hydrothermal synthesis at 1-3 ° C. for 1-3 hours are used as the main component of the deodorant of the present invention. Usually, a mixture of the above-mentioned main component and the porosity imparting mineral is granulated by a conventional method such as extrusion molding and the like, and calcined to obtain a deodorant.
【0010】請求項2の発明では、前記粘土鉱物微結晶
を硫酸、塩酸等の強酸性鉱酸を用いて酸処理して、先ず
該鉱物の固体酸としての酸性度を−4.0≦H0 ≦−
2.0の範囲に調整する。酸処理の例として、例えば濃
度40%の濃硫酸を原料である粘土鉱物に重量比で60
%加え、80−100℃で2−4時間撹拌した後、よく
水洗し乾燥する。或いは濃度15−20%の塩酸を原料
粘土に重量比2−3倍量加え、沸騰還流させつつ3−5
時間撹拌した後、よく水洗し乾燥する。次いで酸性度を
例えば n−ブチルアミン滴定法により測定しつつ、撹
拌時間を調節して酸性度を−3.0≦H0 ≦−0.5の
範囲に調整する。このように調製した組成物として、例
えば合成フライポンタイト(水沢化学工業社製、商品名
ミズカナイト)を例示できる。According to the second aspect of the present invention, the clay mineral microcrystals are acid-treated using a strong acid mineral acid such as sulfuric acid or hydrochloric acid, and the acidity of the mineral as a solid acid is firstly -4.0 ≦ H 0 ≦ −
Adjust to the range of 2.0. As an example of the acid treatment, for example, concentrated sulfuric acid having a concentration of 40% is added to a clay mineral as a raw material in a weight ratio of 60%.
%, Stirred at 80-100 ° C for 2-4 hours, washed well with water and dried. Alternatively, hydrochloric acid having a concentration of 15-20% is added to the raw clay in an amount 2-3 times by weight, and the mixture is boiled and refluxed for 3-5 times.
After stirring for an hour, wash well with water and dry. Then, while measuring the acidity by, for example, an n-butylamine titration method, the stirring time is adjusted to adjust the acidity to a range of −3.0 ≦ H 0 ≦ −0.5. An example of the composition thus prepared is synthetic frypontite (Mizukanite, manufactured by Mizusawa Chemical Industry Co., Ltd.).
【0011】請求項3の発明では、Mn、Cu、または
Pt等よりなる特定のいわゆる主遷移金属群のうち1種
類、または2種類以上の元素を前記請求項1または2記
載の粘土鉱物微結晶上に金属もしくは金属酸化物の状態
となるように担持して脱臭剤とする。担持する元素とし
ては、Mn、Fe、Co、Ni、Cu、Pd、Ptが好
ましく、中でもPtが特に好ましい。担持の方法は、例
えば請求項1または2記載の粘土鉱物微結晶に前記金属
の水溶性塩類の水溶液を混合し、成形し、自然乾燥また
は120℃程度で加熱乾燥したのち焼成する方法、或い
は上記粘土鉱物微結晶に粘結剤を加え適当なサイズに造
粒し焼成したペレットを前記水溶液に浸漬し、乾燥し、
焼成する方法等、当業界で常用される方法が用いられ
る。このように製造した本発明の脱臭剤は、高温加熱に
より臭気成分を酸化分解する作用を有する。According to the third aspect of the present invention, one or more elements of a specific group of so-called main transition metals, such as Mn, Cu, and Pt, are added to the clay mineral microcrystal according to the first or second aspect. A metal or metal oxide is supported thereon to form a deodorant. As the element to be supported, Mn, Fe, Co, Ni, Cu, Pd, and Pt are preferable, and Pt is particularly preferable. The supporting method is, for example, a method in which an aqueous solution of a water-soluble salt of the metal is mixed with the clay mineral microcrystal according to claim 1 or 2, and the mixture is molded, dried naturally or dried by heating at about 120 ° C., and then calcined. The binder obtained by adding a binder to the clay mineral microcrystals, granulating to an appropriate size, and sintering the pellets is immersed in the aqueous solution, and dried.
A method commonly used in the art, such as a firing method, is used. The deodorant of the present invention thus produced has an action of oxidatively decomposing odor components by heating at a high temperature.
【0012】請求項4記載の脱臭方法では、例えば加熱
手段を有する流通系充填層反応器に前記本発明の除去剤
を充填し、所要温度に予熱し、臭気含有ガスを冬季大気
温度例えば−40℃からゴミ焼却処理場の排ガス放出温
度例えば100℃の範囲、ガス圧力1−10kg/cm
2 の範囲、ガス流速をGHSV1,000−95,00
0h- 1 の範囲の一定条件下で流通させることにより、
前記脱臭剤と接触させる。接触する際の温度が低い程脱
臭には有利であるが、排ガスを冬季の大気温度より低温
に冷却するのは脱臭処理工程全体としては実用的でな
く、また高い温度では脱臭率が低下し、例えば悪臭発生
源の排出ガス温度より高い温度特にゴミ焼却処理場の飽
和水蒸気を含む排煙温度より高い場合は実用的ではな
い。According to a fourth aspect of the present invention, for example, the removing agent of the present invention is filled in a flow-type packed bed reactor having a heating means, preheated to a required temperature, and the odor-containing gas is cooled to a winter atmospheric temperature of, for example, -40. Temperature range of exhaust gas from garbage incineration plant to 100 ° C., gas pressure 1-10 kg / cm
GHSV 1,000-95,000, gas flow rate in the range of 2
By distributing under certain conditions in the range of 0h -1 ,
Contact with the deodorant. The lower the temperature at the time of contact, the better the deodorization, but it is not practical for the entire deodorization process to cool the exhaust gas to a temperature lower than the atmospheric temperature in winter, and the deodorization rate decreases at high temperatures, For example, it is not practical when the temperature is higher than the exhaust gas temperature of the offensive odor source, especially when the temperature is higher than the temperature of the exhaust gas containing saturated steam in the garbage incineration plant.
【0013】次に、ガス流速についてはGHSVが1,
000h- 1 より低い場合は単位時間当りの脱臭処理能
率が低く、またGHSVが95,000h- 1 より高い
場合には、臭気成分と脱臭剤との接触が不充分となるた
めに脱臭率が低下し、いずれも好ましくない。Next, regarding the gas flow rate, GHSV is 1,
When it is lower than 000 h -1 , the deodorizing efficiency per unit time is low, and when GHSV is higher than 95,000 h -1 , the contact between the odor component and the deodorant becomes insufficient, so that the deodorization rate decreases. However, neither is preferred.
【0014】本発明における臭気成分の例として、通常
下水処理場やゴミ焼却処理場の臭気含有ガス中に複合臭
気として含有される成分、特にアンモニア、メルカプタ
ン、硫化メチル、硫化水素、トリメチルアミン、酪酸、
吉草酸など塩基性から酸性に亘る成分が挙げられ、その
他、都市ガスの付臭剤として添加されるt−ブチルメル
カプタン等のチオール類或いはジメチルスルフィド等の
チオエーテル類、硫化カルボニル(COS)、チオフェ
ン等の硫黄化合物等が挙げられる。Examples of the odor components in the present invention include components normally contained as complex odors in odor-containing gases of sewage treatment plants and garbage incineration plants, particularly ammonia, mercaptan, methyl sulfide, hydrogen sulfide, trimethylamine, butyric acid, and the like.
Components ranging from basic to acidic, such as valeric acid, are mentioned. In addition, thiols such as t-butyl mercaptan, thioethers such as dimethyl sulfide, carbonyl sulfide (COS), thiophene and the like are added as odorants for city gas. And the like.
【0015】[0015]
【実施例】本発明を更に詳しく説明するため実施例を示
すが、本発明はこれに限定されるものではない。ここで
「%」は特に断らない限り重量%を意味する。また脱臭
率は、各種悪臭成分を含有するガスを固定層流通式反応
器に流通させ、反応器出口ガスを官能試験し、強度1に
なる迄に脱臭剤に補集された各成分の重量を元の脱臭剤
重量で割った値を%に換算したものである。EXAMPLES The present invention will be described in more detail with reference to Examples, but it should not be construed that the invention is limited thereto. Here, "%" means% by weight unless otherwise specified. The deodorization rate was determined by flowing a gas containing various malodorous components through a fixed-bed flow reactor, performing a sensory test on the gas at the outlet of the reactor, and measuring the weight of each component collected by the deodorant until the strength reached 1. The value obtained by dividing by the weight of the original deodorant was converted to%.
【0016】[脱臭剤製造実施例1]固体酸性度を調整
した粘土鉱物微結晶である水沢化学工業社製のミズカナ
イトに常用の塩類水溶液含浸法によりPtを0.2%担
持させて、本発明の遷移金属担持型脱臭剤を得た。[Deodorizing Agent Production Example 1] 0.2% of Pt was supported on a mizucanite manufactured by Mizusawa Chemical Industry Co., Ltd., which is a clay mineral microcrystal having an adjusted solid acidity, by a conventional salt solution impregnation method. Was obtained.
【0017】[脱臭処理実施例1]管型反応器に上記脱
臭剤100gを充填し、アンモニア50ppmと硫化水
素30ppmを含み、露点30℃である空気をGHSV
10,000h-1にて流通させ、出口ガスを官能試験
し、強度1になる迄に脱臭剤に補集された各成分の重量
を測定した。元の脱臭剤の重量100gに対する重量%
を求めた結果、アンモニアの補集量7%、硫化水素の補
集量20%であった。[Deodorizing Treatment Example 1] A tubular reactor was charged with 100 g of the above deodorizing agent, and air containing 50 ppm of ammonia and 30 ppm of hydrogen sulfide and having a dew point of 30 ° C. was purified by GHSV.
The mixture was circulated at 10,000 h -1 , and the outlet gas was subjected to a sensory test. The weight of each component collected by the deodorant until the strength reached 1 was measured. % By weight based on 100 g of the original deodorant
As a result, the collection amount of ammonia was 7% and the collection amount of hydrogen sulfide was 20%.
【0018】[比較例1]上記管型反応器に通常用いら
れる活性炭脱臭剤(商品名、粒状白鷺)100gを充填
し、実施例1と同一のガスを同一条件で流通させた結
果、アンモニアの補集量3%、硫化水素の補集量10%
であった。Comparative Example 1 The above tubular reactor was charged with 100 g of a commonly used activated carbon deodorant (trade name, granular Shirasagi), and the same gas as in Example 1 was allowed to flow under the same conditions. Collection amount 3%, hydrogen sulfide collection amount 10%
Met.
【0019】[再生処理実施例1]上記実施例1で使用
した後の本発明の脱臭剤を上記反応器に充填したまま、
空気をGHSV10,000の速度で流通させつつ35
0℃で加熱し、臭気成分をH2 O、N2 、CO2 等に酸
化分解させた。こうして再生した脱臭剤で再び実施例1
の通り脱臭処理を行った。これを繰り返し、10回再生
処理を行った後の脱臭剤についての脱臭結果は、アンモ
ニアの補集量5%、硫化水素の補集量17%であった。[Regeneration Treatment Example 1] The deodorant of the present invention after being used in Example 1 was charged into the reactor,
While flowing air at a speed of 10,000 GHSV, 35
By heating at 0 ° C., the odor component was oxidized and decomposed into H 2 O, N 2 , CO 2 and the like. Example 1 again with the regenerated deodorant
The deodorization treatment was performed as described above. This was repeated, and the deodorizing result of the deodorizing agent after the regeneration treatment was performed 10 times was 5% for the collection amount of ammonia and 17% for the collection amount of hydrogen sulfide.
【0020】[0020]
【発明の効果】本発明の脱臭剤は、臭気含有ガス中の臭
気成分、特にアンモニア、メルカプタン、硫化メチル、
硫化水素、トリメチルアミン、酪酸、吉草酸など塩基性
から酸性に亘る成分を含有する複合臭気ガスに対して、
1種類の脱臭剤で有効な脱臭効果を持つので、複合臭気
に対して実用的価値が高い。The deodorant of the present invention is characterized by the fact that the odor components in the odor-containing gas, particularly ammonia, mercaptan, methyl sulfide,
For complex odor gas containing components ranging from basic to acidic such as hydrogen sulfide, trimethylamine, butyric acid, valeric acid,
Since one type of deodorant has an effective deodorizing effect, it has high practical value against complex odors.
【0021】本発明の脱臭方法は、大気温度または従来
技術に比べて相当低い温度で行うので、脱臭剤の活性点
が微量成分の分解物により被覆される等の性能低下が長
期間起こらず、また何度も再生可能であるため更に長期
の使用に耐え得る。Since the deodorizing method of the present invention is carried out at the atmospheric temperature or at a temperature considerably lower than that of the prior art, the deteriorating agent does not deteriorate for a long time, for example, the active sites of the deodorizing agent are covered by the decomposed products of trace components. In addition, since it can be reproduced many times, it can withstand long-term use.
【0022】本発明の脱臭方法は、従来技術のように使
用前に賦活操作を行う必要が無いので簡便であり、脱臭
設備の再起動が容易である。The deodorizing method of the present invention does not require an activation operation before use as in the prior art, so that it is simple and the deodorizing equipment can be easily restarted.
Claims (5)
モル%、アルミナ(Al2 O3 )5−20モル%、三酸
化二鉄(Fe2 O3 )0−10モル%、マグネシア(M
gO)0−15モル%、H2 O が5−20モル%であ
る層構造粘土鉱物を50℃−100℃の温度で1−5時
間第一段水熱合成した後、150℃−250℃で1−3
時間第二段水熱合成してなる粘土鉱物微結晶を主成分と
する臭気含有ガス脱臭剤。1. A composition ratio of silica (SiO 2 ) 20-70.
Mol%, of alumina (Al 2 O 3) 5-20 mol%, diiron trioxide (Fe 2 O 3) 0-10 mol%, magnesia (M
gO) The first-stage hydrothermal synthesis of a layered clay mineral having 0 to 15 mol% and H 2 O of 5 to 20 mol% at a temperature of 50 ° C. to 100 ° C. for 1 to 5 hours, and then at 150 ° C. to 250 ° C. 1-3
An odor-containing gas deodorant composed mainly of clay mineral microcrystals obtained by second-stage hydrothermal synthesis.
ることにより酸強度関数(H0 )で表示した固体酸性度
を−3.0≦H0 ≦−0.5の範囲に調整した粘土鉱物
微結晶を主成分とする請求項1記載の脱臭剤。2. The clay mineral after hydrothermal synthesis is further treated with an acid to adjust the solid acidity expressed by an acid strength function (H 0 ) to a range of −3.0 ≦ H 0 ≦ −0.5. 2. The deodorant according to claim 1, comprising a clay mineral microcrystal as a main component.
に長周期型周期律表第4周期の7A族、8族、及び1B
族、または白金族元素よりなる群から選ばれる少なくと
も1種類以上の金属もしくは金属酸化物を担持してなる
粘土鉱物微結晶を主成分とする脱臭剤。3. The clay mineral microcrystal according to claim 1 or 2, wherein the fourth period of the long period type periodic table has a 7A group, a 8 group, and a 1B group.
A deodorant containing, as a main component, clay mineral microcrystals carrying at least one or more metals or metal oxides selected from the group consisting of group III or platinum group elements.
載の脱臭剤と−40℃−100℃の温度においてガス圧
力が1−10kg/cm2 、GHSVが1,000−9
5,000h- 1 の条件下で接触させることを特徴とす
る臭気含有ガスの脱臭方法。4. An odor-containing gas comprising the deodorant according to claim 1, 2 or 3, and a gas pressure of 1-10 kg / cm 2 and a GHSV of 1,000-9 at a temperature of -40 ° C.-100 ° C.
A method for deodorizing an odor-containing gas, wherein the odor-containing gas is contacted under a condition of 5,000 h -1 .
剤を100℃−500℃の温度で加熱処理することを特
徴とする脱臭剤の再生処理方法。5. A method for regenerating a deodorant according to claim 3, wherein the deodorant is heated at a temperature of 100 ° C. to 500 ° C. after use in the deodorizing treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9071884A JPH10263391A (en) | 1997-03-25 | 1997-03-25 | Odor component-containing gas deodorant, deodorizing method using the same, and method for regenerating the deodorant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9071884A JPH10263391A (en) | 1997-03-25 | 1997-03-25 | Odor component-containing gas deodorant, deodorizing method using the same, and method for regenerating the deodorant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10263391A true JPH10263391A (en) | 1998-10-06 |
Family
ID=13473413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9071884A Pending JPH10263391A (en) | 1997-03-25 | 1997-03-25 | Odor component-containing gas deodorant, deodorizing method using the same, and method for regenerating the deodorant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10263391A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013040066A (en) * | 2011-08-12 | 2013-02-28 | Osaka Prefecture Univ | Method for manufacturing lamellar silicate compound |
-
1997
- 1997-03-25 JP JP9071884A patent/JPH10263391A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013040066A (en) * | 2011-08-12 | 2013-02-28 | Osaka Prefecture Univ | Method for manufacturing lamellar silicate compound |
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