JPH04349934A - Inorganic adsorbent - Google Patents

Inorganic adsorbent

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Publication number
JPH04349934A
JPH04349934A JP3041380A JP4138091A JPH04349934A JP H04349934 A JPH04349934 A JP H04349934A JP 3041380 A JP3041380 A JP 3041380A JP 4138091 A JP4138091 A JP 4138091A JP H04349934 A JPH04349934 A JP H04349934A
Authority
JP
Japan
Prior art keywords
silicate
activated carbon
zinc compound
adsorbent
particles
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.)
Pending
Application number
JP3041380A
Other languages
Japanese (ja)
Inventor
Eiji Tanaka
栄治 田中
Tetsuya Tsushima
津島 哲也
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kuraray Chemical Co Ltd
Original Assignee
Kuraray Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kuraray Chemical Co Ltd filed Critical Kuraray Chemical Co Ltd
Priority to JP3041380A priority Critical patent/JPH04349934A/en
Publication of JPH04349934A publication Critical patent/JPH04349934A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To improve the safety of an inorganic adsorbent comprising silicate, zinc compound, and active carbon in which the active carbon particles are dispersed uniformly, by preparing the adsorbent in the form of powder or spherical particles. CONSTITUTION:An adsorbent comprizing silicate, zinc compound, and active carbon is characterized not only by an excellent power of deodorizing various gasses with offsensive odor existing in a daily life environment such as hydrogen sulfide, ammonia, mercaptan, amine, and aldehyde but also by a high level safety due to its harmless composition of silicate, zinc compound, and active carbon. Since the adsorbent can be prepared in the form of fine powder, it is mixed easily into paper and sheets. Its thermal stability at up to about 500 deg.C enables mixing into plastic and affords a good processability. The adsorbent of spherical particles is easy in handling and can be used in wide applications.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は吸着剤に関するものであ
り、更に詳しく述べるならば、硫化水素、アンモニア、
メルカプタン、アミン及びアルデヒド等の悪臭成分の吸
着除去に優れた性質を有するものである。
[Field of Industrial Application] The present invention relates to an adsorbent, and more specifically, it relates to an adsorbent for hydrogen sulfide, ammonia,
It has excellent properties for adsorption and removal of malodorous components such as mercaptans, amines, and aldehydes.

【0002】0002

【従来の技術】近年、日常の生活空間に存在する硫化水
素、アンモニア、メルカプタン、アミン、及びアルデヒ
ド等の各種悪臭ガスが問題となっている。このため快適
な生活環境を維持するために、これらの悪臭ガスを除去
する機能を有する脱臭剤について社会的関心が高まり、
様々な種類の脱臭剤が使用されている。
BACKGROUND OF THE INVENTION In recent years, various malodorous gases such as hydrogen sulfide, ammonia, mercaptans, amines, and aldehydes that exist in daily living spaces have become a problem. For this reason, in order to maintain a comfortable living environment, there is growing social interest in deodorizers that have the ability to remove these foul-smelling gases.
Various types of deodorizers are used.

【0003】これらの脱臭剤は日常生活で使用されてい
るものであるため、少なくとも次のような条件を満たす
ものであることが要求される。
[0003] Since these deodorizing agents are used in daily life, they are required to satisfy at least the following conditions.

【『004】(1)日常の生活空間に存在する各種悪臭
ガスに対して良好な脱臭性能を有するものであること。 (2)安全性の高いものであること。(3)取扱が容易
なものであること。(4)安価なものであること。
[004] (1) It must have good deodorizing performance against various malodorous gases present in everyday living spaces. (2) It must be highly safe. (3) It must be easy to handle. (4) It must be inexpensive.

【0005】しかしながら従来、上記のすべての条件を
充分に満足する脱臭剤は存在しなかった。活性炭はメル
カプタン及びアミン等の悪臭ガスの脱臭効果は優れてい
るが、日常の生活空間に存在する代表的な悪臭ガスであ
る硫化水素やアンモニアに対する脱臭効果はあまり高く
ない。この点を改良する目的で活性炭に酸、アルカリあ
るいはある種のハロゲン化合物を担持させた添着炭と呼
ばれる製品もつくられている。しかし、そのような処理
を行った製品は酸或いはアルカリそのものと同様に一種
の危険物としての取扱が必要となるため、日常生活での
使用には適さない場合も多い。
[0005] Conventionally, however, there has been no deodorizing agent that fully satisfies all of the above conditions. Although activated carbon has an excellent deodorizing effect on malodorous gases such as mercaptans and amines, it is not very effective in deodorizing hydrogen sulfide and ammonia, which are typical malodorous gases present in everyday living spaces. In order to improve this point, a product called impregnated carbon, in which activated carbon is loaded with acid, alkali, or some kind of halogen compound, is also produced. However, products that have undergone such treatment must be treated as a type of dangerous substance, similar to acids or alkalis themselves, and are therefore often unsuitable for use in daily life.

【0006】また、硫酸鉄にアスコルビン酸を加えた製
品も市販されている。この種のものは、アンモニア、ア
ミン等の塩基性の悪臭ガスに対する脱臭効果は良好であ
るが、硫化水素、メルカプタン及びアルデヒド等に対す
る脱臭効果は殆どなく、また水に濡れると溶解するため
、湿潤ガスの脱臭には使用できないという欠点がある。
[0006] Products containing iron sulfate and ascorbic acid are also commercially available. This type of product has a good deodorizing effect on basic foul-smelling gases such as ammonia and amines, but it has almost no deodorizing effect on hydrogen sulfide, mercaptans, aldehydes, etc., and it dissolves when wet with water, so it is a wet gas. The disadvantage is that it cannot be used for deodorizing.

【0007】その他の化学脱臭剤も多数開示されている
が、酸性やアルカリ性の強いものが多く、また脱臭でき
るガスの種類も限られており、吸湿または乾燥の影響を
受け易いといった欠点がある。
Although many other chemical deodorizing agents have been disclosed, many of them are strongly acidic or alkaline, the types of gases that can be deodorized are limited, and they have drawbacks such as being susceptible to moisture absorption or drying.

【0008】ほかに有機系脱臭剤もあるが耐熱性が低く
、加工も困難でまた高価である。
There are other organic deodorizing agents, but they have low heat resistance, are difficult to process, and are expensive.

【0009】[0009]

【発明が解決しようとする課題】本発明は日常の生活空
間に存在する悪臭成分の除去を目的としたもので、特に
問題となる硫化水素、アンモニア、メルカプタン、アミ
ン及びアルデヒド等の悪臭ガスに対して良好な脱臭効果
を有し、安全性が高く且つ取扱の容易な、全く新しい組
成の脱臭剤を提供することにある。
[Problems to be Solved by the Invention] The present invention is aimed at removing malodorous components present in daily living spaces, and is particularly aimed at removing malodorous gases such as hydrogen sulfide, ammonia, mercaptans, amines, and aldehydes. The object of the present invention is to provide a deodorizing agent having a completely new composition, which has a good deodorizing effect, is highly safe, and is easy to handle.

【0010】0010

【課題を解決するための手段】本発明等は、上記目的を
達成するため、珪酸塩、亜鉛化合物及び活性炭の3成分
系組成物について鋭意研究を重ねた結果、硫化水素、ア
ンモニア、メルカプタン、アミン及びアルデヒド等の悪
臭ガスに対して優れた脱臭性能を有する組成物が存在す
ることを見出し、それに基づいて本発明に到達した。
[Means for Solving the Problems] In order to achieve the above-mentioned objects, the present invention has conducted intensive research on three-component compositions of silicates, zinc compounds, and activated carbon. The inventors have discovered that there are compositions that have excellent deodorizing performance against malodorous gases such as aldehydes and aldehydes, and have arrived at the present invention based on this finding.

【0011】すなわち、珪酸塩、亜鉛化合物、及び活性
炭からなる粒子で、活性炭粒子をその内部に均一に分散
せしめてなる無機質吸着剤、及び珪酸塩と亜鉛化合物を
混合した水溶液の比重を1.5 〜2.5 に調整し、
活性炭粒子を加えて混合した後、該混合液を上部が疎水
性の液体、下部が凝固液の2層からなる凝固浴に滴下し
て珪酸塩、亜鉛化合物、及び活性炭からなる球状粒子を
凝固、生成させることを特徴とする珪酸塩、亜鉛化合物
、及び活性炭からなる無機質吸着剤の製法である。
That is, the specific gravity of an inorganic adsorbent made of particles made of a silicate, a zinc compound, and activated carbon, with the activated carbon particles uniformly dispersed therein, and an aqueous solution containing a mixture of the silicate and the zinc compound is 1.5. Adjust to ~2.5,
After adding activated carbon particles and mixing, the mixed liquid is dropped into a coagulation bath consisting of two layers: a hydrophobic liquid at the top and a coagulation liquid at the bottom to coagulate spherical particles consisting of silicate, zinc compound, and activated carbon. This is a method for producing an inorganic adsorbent comprising a silicate, a zinc compound, and activated carbon.

【0012】以下本発明について詳しく説明する。The present invention will be explained in detail below.

【0013】本発明の吸着剤は珪酸塩、亜鉛化合物及び
活性炭からなる粒子である。本発明に使用する珪酸塩は
特に限定せず広範囲の珪酸塩を使用できるが、水ガラス
、水酸化珪素、シリカゾル、シリカゲル等が好ましい。 また亜鉛化合物も特に限定しないが、例えば、硫酸亜鉛
、塩化亜鉛、硝酸亜鉛、酢酸亜鉛等が好ましい。
The adsorbent of the present invention is a particle consisting of a silicate, a zinc compound and activated carbon. The silicate used in the present invention is not particularly limited and a wide range of silicates can be used, but water glass, silicon hydroxide, silica sol, silica gel and the like are preferred. The zinc compound is also not particularly limited, but preferred examples include zinc sulfate, zinc chloride, zinc nitrate, and zinc acetate.

【0014】活性炭としては椰子殻系、石炭系、フェノ
ール系、PAN(ポリアクリロニトリル)系、ピッチ系
ら各種の活性炭が使用出来、また形状は粒状、繊維状、
粉末状の活性炭を使用することも出来るが、組成物の内
部に均一に分散させるためには微粒子が最も好ましい。
Various activated carbons such as coconut shell, coal, phenol, PAN (polyacrylonitrile), and pitch can be used as the activated carbon, and they can be in the form of granules, fibers, or
Powdered activated carbon can also be used, but fine particles are most preferred for uniform dispersion within the composition.

【0015】本発明の吸着剤粒子の内部における珪酸塩
、亜鉛化合物の性状はとくに限定しないが、珪酸塩がゲ
ル状となっている状態が最も高い吸着性を示す。活性炭
はこのゲル状粒子の内部において均一に分散している必
要がある。活性炭が偏在していると、活性炭と珪酸塩、
亜鉛化合物のゲルが別個に存在する状態と同様な吸着性
を示し、両者の相乗効果は認められない。従って、本発
明の吸着剤の吸着性を高めるためには、活性炭は可及的
に微粒子を使用し、ゲル状粒子内部に均一に分散させる
必要がある。
The properties of the silicate and zinc compound inside the adsorbent particles of the present invention are not particularly limited, but the state in which the silicate is in the form of a gel exhibits the highest adsorptivity. Activated carbon must be uniformly dispersed inside the gel particles. If activated carbon is unevenly distributed, activated carbon and silicates,
The adsorption properties are similar to those in the state where the zinc compound gel exists separately, and no synergistic effect between the two is observed. Therefore, in order to enhance the adsorption properties of the adsorbent of the present invention, it is necessary to use as fine particles of activated carbon as possible and to uniformly disperse them inside the gel particles.

【0016】本発明の吸着剤を調製するには、珪酸塩と
、亜鉛化合物をPH10付近の水溶液とし、活性炭を加
え、攪拌しながら、酸によってPH2〜7、好ましくは
2〜5にすると、該水溶液中の珪酸塩と、亜鉛化合物は
凝固して、ゲル状の珪酸質の内部に亜鉛と活性炭が分散
された沈澱物を生成する。次にこの沈澱物を液から分離
した後、乾燥することにより、微粉末状の本発明の吸着
剤が得られる。ここで溶液のPHの調製にはアルカリ及
び酸が使用されるが、アルカリ化合物としては水酸化ナ
トリウム、水酸化カルシウム、水酸化バリウム、アンモ
ニア等が、一方酸としては塩酸、硫酸、硝酸、酢酸など
を使用することが出来る。但し、亜鉛化合物が硫酸塩の
場合には、PH調整のアルカリ化合物として水酸化カル
シウムや水酸化バリウムを使用すると水に不溶性の塩を
生じるため、不溶性の塩が生成しないアルカリ化合物を
選択する必要がある。
To prepare the adsorbent of the present invention, a silicate and a zinc compound are made into an aqueous solution with a pH around 10, activated carbon is added, and the pH is adjusted to 2 to 7, preferably 2 to 5, with an acid while stirring. The silicate and zinc compound in the aqueous solution coagulate to form a precipitate in which zinc and activated carbon are dispersed inside the gel-like silicic acid. Next, this precipitate is separated from the liquid and then dried to obtain a finely powdered adsorbent of the present invention. Alkali and acids are used to adjust the pH of the solution. Alkaline compounds include sodium hydroxide, calcium hydroxide, barium hydroxide, ammonia, etc., while acids include hydrochloric acid, sulfuric acid, nitric acid, acetic acid, etc. can be used. However, if the zinc compound is a sulfate, using calcium hydroxide or barium hydroxide as an alkaline compound for pH adjustment will produce water-insoluble salts, so it is necessary to select an alkaline compound that does not produce insoluble salts. be.

【0017】同様にPH調整のアルカリ化合物として水
酸化カルシウムや水酸化バリウムを使用した場合は、P
H調整の酸として硫酸を使用すると水に不溶な塩が生成
するので好ましくない。不溶性の塩を生じないアルカリ
化合物を選択する必要がある。
Similarly, when calcium hydroxide or barium hydroxide is used as an alkaline compound for pH adjustment, P
Use of sulfuric acid as the acid for H adjustment is undesirable because a water-insoluble salt is produced. It is necessary to choose an alkaline compound that does not form insoluble salts.

【0018】更に本発明の吸着剤を球状粒子とする製法
として、珪酸塩と亜鉛化合物をPH9〜11で水溶液と
し、活性炭を加え、攪拌しながら酸によってPH6〜9
好ましくは7〜8にした後、上層に疎水性の液体が存在
し、下層にPH6〜8に調整した凝固液が存在する2層
からなる凝固浴に滴下し、上層に疎水性の液体中で滴下
液の表面張力により球形粒子が生成され、次に下層の凝
固液中で凝固して球状の吸着剤粒子が得られる。
Furthermore, as a method for manufacturing the adsorbent of the present invention into spherical particles, a silicate and a zinc compound are made into an aqueous solution at pH 9 to 11, activated carbon is added, and the pH is adjusted to pH 6 to 9 with acid while stirring.
Preferably, after adjusting the pH to 7 to 8, it is dropped into a coagulation bath consisting of two layers, in which a hydrophobic liquid is present in the upper layer and a coagulating liquid adjusted to pH 6 to 8 is present in the lower layer, and the upper layer is in a hydrophobic liquid. Spherical particles are generated by the surface tension of the dropped liquid, which is then coagulated in the underlying coagulation liquid to obtain spherical adsorbent particles.

【0019】ここで、疎水性の液体とは、水に不溶性な
液状化合物で例えば、高級炭化水素、エステル、ベンゼ
ン、高級アルコール、灯油等である。また、凝固液とは
PH6〜8に調製した水溶液で、珪酸塩溶液を滴下した
時容易に凝固してゲル化するような液である。
Here, the hydrophobic liquid is a liquid compound insoluble in water, such as higher hydrocarbons, esters, benzene, higher alcohols, and kerosene. Further, the coagulating liquid is an aqueous solution prepared to have a pH of 6 to 8, and is a liquid that easily coagulates and gels when the silicate solution is dropped.

【0020】この際、珪酸塩と亜鉛化合物の水溶液の比
重は1.5 〜2.5 、好ましくは1.5 〜2.2
 、より好ましくは、1.8〜2.0 に調製する必要
がある。これは珪酸塩及び、亜鉛化合物の水溶液に活性
炭を添加すると、その比重差により分離が起こる場合が
あるためで、溶液の比重が1.8 より低下すると活性
炭が沈降し、また、比重が2.5 より高い場合は浮遊
する。従って、活性炭粒子が吸着剤の内部で均一に分散
されず、偏在して吸着性能や粒子の強度が低下するから
である。
At this time, the specific gravity of the aqueous solution of the silicate and zinc compound is 1.5 to 2.5, preferably 1.5 to 2.2.
, more preferably 1.8 to 2.0. This is because when activated carbon is added to an aqueous solution of silicate and zinc compounds, separation may occur due to the difference in specific gravity.If the specific gravity of the solution decreases below 1.8, the activated carbon will settle, and if the specific gravity decreases to 2. If it is higher than 5, it will float. Therefore, the activated carbon particles are not uniformly dispersed inside the adsorbent and are unevenly distributed, resulting in a decrease in adsorption performance and particle strength.

【0021】更に、均一な吸着剤粒子を得るためには、
凝固浴の温度は好ましくは50〜70℃、より好ましく
は55〜65℃である。
Furthermore, in order to obtain uniform adsorbent particles,
The temperature of the coagulation bath is preferably 50-70°C, more preferably 55-65°C.

【0022】本発明の吸着剤の珪酸塩、亜鉛化合物及び
活性炭の組成はどのような比率でも相当高い吸着性能を
有するが、珪酸塩5重量部に対して、亜鉛化合物及び活
性炭の比率がそれぞれ1〜4の範囲内の組成がより好ま
しい。すなわち亜鉛化合物対活性炭の重量比が4対1よ
り亜鉛化合物が多い領域、或いは1対4より活性炭が多
い組成領域で生成した沈澱を乾燥して得られる粒子は、
各々単体成分である亜鉛化合物あるいは活性炭とほぼ同
様な吸着性を示し、これらの吸着性は本発明の組成領域
で得られる球形粒子の吸着特性に比べて相乗効果が乏し
くなることが認められる。
The composition of the silicate, zinc compound and activated carbon in the adsorbent of the present invention has a considerably high adsorption performance at any ratio, but when the ratio of the zinc compound and activated carbon is 1 to 5 parts by weight of the silicate, respectively. A composition within the range of ˜4 is more preferable. That is, the particles obtained by drying the precipitate produced in a region where the weight ratio of zinc compound to activated carbon is more than 4:1, or a composition region where the ratio of activated carbon is more than 1:4, are:
Each exhibits almost the same adsorption properties as the single component zinc compound or activated carbon, and it is recognized that these adsorption properties have a poor synergistic effect compared to the adsorption properties of spherical particles obtained in the composition range of the present invention.

【0023】[0023]

【実施例】以下に実施例を挙げて本発明を更に具体的に
説明する。
[Examples] The present invention will be explained in more detail with reference to Examples below.

【0024】(実施例1)2リットルビーカーに純水1
リットルと水ガラス60g、Zn(OH)224gを加
えNaOHでPHを10にして攪拌し、均一な溶液とし
、さらに活性炭粉末6gを加え再度攪拌しながら40%
H2SO4 を加えてPHを7.3 に調製し、室温に
て4時間放置した。
(Example 1) Pure water 1 in a 2 liter beaker
Add 60 g of water glass and 224 g of Zn(OH), adjust the pH to 10 with NaOH, stir to make a homogeneous solution, then add 6 g of activated carbon powder and stir again until the solution reaches 40%
The pH was adjusted to 7.3 by adding H2SO4, and the mixture was left at room temperature for 4 hours.

【0025】生成物を濾過洗浄後、200 ℃で3時間
乾燥し、本発明の珪酸塩、亜鉛化合物、活性炭系の吸着
剤を調製した。この脱臭剤のBET比表面積は、610
 m2 /gであり、化学分析により、構成比率は重量
比で珪酸塩対亜鉛化合物対活性炭は5対4対1であった
After filtering and washing the product, it was dried at 200° C. for 3 hours to prepare the silicate, zinc compound, and activated carbon-based adsorbent of the present invention. The BET specific surface area of this deodorizer is 610
m2/g, and chemical analysis revealed that the weight ratio of silicate to zinc compound to activated carbon was 5:4:1.

【0026】この吸着剤の硫化水素、アンモニア、メル
カプタン、アミン及びアルデヒド等の悪臭ガスに対する
吸着特性を次のようにして測定した。
The adsorption properties of this adsorbent for malodorous gases such as hydrogen sulfide, ammonia, mercaptans, amines and aldehydes were measured as follows.

【0027】吸着剤100mg を内容積120ml 
の硝子製バイアル瓶に入れ、ゴム栓をした後、マイクロ
シリンジを使って所定量の悪臭ガス成分をバイアル瓶内
に注入する。 ガスを注入してから2時間後、バイアル瓶内の空気をマ
イクロシリジンで取り出し、ガスクロマトグラフを使用
してガス濃度を分析する。
[0027] 100mg of adsorbent with an internal volume of 120ml
After placing the sample in a glass vial and sealing it with a rubber stopper, a predetermined amount of the malodorous gas component is injected into the vial using a microsyringe. Two hours after injecting the gas, the air inside the vial is extracted using microsilidine, and the gas concentration is analyzed using a gas chromatograph.

【0028】結果を表1に示した。The results are shown in Table 1.

【0029】(実施例2〜4)亜鉛化合物と活性炭の量
的割合を種々変化させた以外は実施例1と全く同様にし
て吸着剤を得た。これらの吸着剤の化学分析による珪酸
塩と亜鉛化合物と活性炭の重量比、及び各種悪臭ガスに
対する吸着特性を表1に示した。
(Examples 2 to 4) Adsorbents were obtained in exactly the same manner as in Example 1, except that the quantitative ratios of the zinc compound and activated carbon were varied. Table 1 shows the weight ratio of silicate, zinc compound, and activated carbon, as well as the adsorption characteristics for various malodorous gases, as determined by chemical analysis of these adsorbents.

【0030】(比較例1〜3)珪酸塩と亜鉛化合物と活
性炭の比率を種々変化させた以外は、実施例1と全く同
様にして吸着剤を得た。比較例1、2、3のBRT比表
面積はそれぞれ、470、800 、580 m2 /
gであった。 各種悪臭ガスに対する吸着特性を表1に示した。
(Comparative Examples 1 to 3) Adsorbents were obtained in exactly the same manner as in Example 1, except that the ratios of silicate, zinc compound, and activated carbon were varied. The BRT specific surface areas of Comparative Examples 1, 2, and 3 are 470, 800, and 580 m2/
It was g. Table 1 shows the adsorption characteristics for various malodorous gases.

【0031】(比較例4)市販活性炭について各種悪臭
ガスに対する吸着特性を表1に示した。
(Comparative Example 4) Table 1 shows the adsorption properties of commercially available activated carbon for various malodorous gases.

【0032】(実施例1)2リットルビーカーに純水1
リットルと水ガラス60g、Zn(OH)224gを加
えNaOHでPHを10にして攪拌し均一な溶液としさ
らに活性炭粉末12g を加え再度攪拌しながら40%
H2SO4 を加えてPHを7.3 に調製した後、上
層は灯油、下層はPH6.8 の希硫酸溶液の凝固液の
2層からなる凝固浴に滴下して、上層の灯油中で球形粒
子を生成させ、下層の凝固液中で球形粒子を凝固せしめ
た。
(Example 1) 1 liter of pure water in a 2 liter beaker
Add 60 g of water glass and 224 g of Zn(OH), adjust the pH to 10 with NaOH, stir to make a homogeneous solution, then add 12 g of activated carbon powder and stir again until the solution reaches 40%
After adjusting the pH to 7.3 by adding H2SO4, the spherical particles were added dropwise to a coagulation bath consisting of two layers: kerosene in the upper layer and coagulation liquid of a dilute sulfuric acid solution with a pH of 6.8 in the lower layer. The spherical particles were coagulated in the coagulation liquid in the lower layer.

【0033】生成物を濾過洗浄後、200 ℃で3時間
乾燥し、本発明の珪酸塩、亜鉛化合物、活性炭系の吸着
剤を調製した。この脱臭剤のBET比表面積は580 
m2 /gであり、化学分析により、構成比率は重量比
で珪酸塩対亜鉛化合物対活性炭は5対4対2であった。
After filtering and washing the product, it was dried at 200° C. for 3 hours to prepare the silicate, zinc compound, and activated carbon-based adsorbent of the present invention. The BET specific surface area of this deodorizer is 580
m2/g, and chemical analysis revealed that the weight ratio of silicate to zinc compound to activated carbon was 5:4:2.

【0034】この吸着剤の硫化水素、アンモニア、メル
カプタン、アミン及びアルデヒド等の悪臭ガスに対する
吸着特性を測定しその結果を表1に示した。
The adsorption properties of this adsorbent for malodorous gases such as hydrogen sulfide, ammonia, mercaptans, amines and aldehydes were measured and the results are shown in Table 1.

【0035】[0035]

【表1】[Table 1]

【0036】[0036]

【発明の効果】本発明の珪酸塩、亜鉛化合物、及び活性
炭系吸着剤は、日常の生活環境に存在する硫化水素、ア
ンモニア、メルカプタン、アミン及びアルデヒド等の各
種悪臭ガスの脱臭に優れた性能を有するのみならず、毒
性がない珪酸塩、亜鉛化合物及び活性炭から構成されて
いるため安全性が高い特徴がある。
Effects of the Invention: The silicate, zinc compound, and activated carbon-based adsorbent of the present invention exhibits excellent deodorizing performance of various malodorous gases such as hydrogen sulfide, ammonia, mercaptans, amines, and aldehydes that exist in the daily living environment. Not only that, but it is also highly safe because it is composed of non-toxic silicates, zinc compounds, and activated carbon.

【0037】本吸着剤は微粉末状にすることが出来るた
め、紙及びシート等に容易に担持でき、熱的にも500
 ℃程度まで安定な為、プラスチックへの練り込みも可
能であることなど、加工性にも優れている。
Since the present adsorbent can be made into a fine powder, it can be easily supported on paper, sheets, etc., and has a thermal resistance of 500%.
It also has excellent processability, as it is stable up to temperatures around ℃ and can be kneaded into plastics.

【0038】また、球状粒子とすることも出来、取扱も
容易で広範囲な用途に使用することが出来る。
[0038] Furthermore, it can be made into spherical particles, which are easy to handle and can be used in a wide range of applications.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】  珪酸塩、亜鉛化合物、及び活性炭から
なる粒子で、活性炭粒子をその内部に均一に分散せしめ
てなる無機質吸着剤。
1. An inorganic adsorbent comprising particles consisting of a silicate, a zinc compound, and activated carbon, with activated carbon particles uniformly dispersed therein.
【請求項2】  脱臭剤粒子が球状である請求項1の無
機質吸着剤。
2. The inorganic adsorbent according to claim 1, wherein the deodorant particles are spherical.
【請求項3】  珪酸塩5重量部に対し、亜鉛化合物及
び活性炭がそれぞれ1〜4重量部である請求項1の無機
質吸着剤。
3. The inorganic adsorbent according to claim 1, wherein the zinc compound and activated carbon are each contained in an amount of 1 to 4 parts by weight based on 5 parts by weight of the silicate.
【請求項4】  珪酸塩と亜鉛化合物を混合した水溶液
の比重を1.5 〜2.5 に調整し、活性炭粒子を加
えて混合した後、該混合液を上部が疎水性の液体、下部
が凝固液の2層からなる凝固浴に滴下して珪酸塩、亜鉛
化合物、及び活性炭からなる球状粒子を生成させること
を特徴とする珪酸塩、亜鉛化合物、及び活性炭からなる
無機質吸着剤の製法。
4. Adjust the specific gravity of an aqueous solution containing a mixture of silicate and zinc compound to 1.5 to 2.5, add activated carbon particles, and mix. A method for producing an inorganic adsorbent consisting of a silicate, a zinc compound, and activated carbon, which comprises dropping the coagulating liquid dropwise into a coagulation bath consisting of two layers to produce spherical particles consisting of a silicate, a zinc compound, and activated carbon.
JP3041380A 1991-01-15 1991-01-15 Inorganic adsorbent Pending JPH04349934A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3041380A JPH04349934A (en) 1991-01-15 1991-01-15 Inorganic adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3041380A JPH04349934A (en) 1991-01-15 1991-01-15 Inorganic adsorbent

Publications (1)

Publication Number Publication Date
JPH04349934A true JPH04349934A (en) 1992-12-04

Family

ID=12606793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3041380A Pending JPH04349934A (en) 1991-01-15 1991-01-15 Inorganic adsorbent

Country Status (1)

Country Link
JP (1) JPH04349934A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336697A (en) * 2001-05-14 2002-11-26 Gl Sciences Inc Method for producing adsorbent for separation and adsorbent
JPWO2005041658A1 (en) * 2003-10-31 2007-11-29 アース製薬株式会社 Gel material
WO2026037982A1 (en) * 2024-08-13 2026-02-19 Kemira Oyj Silicate adsorbent material and use of silicate adsorbent material in water treatment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336697A (en) * 2001-05-14 2002-11-26 Gl Sciences Inc Method for producing adsorbent for separation and adsorbent
JPWO2005041658A1 (en) * 2003-10-31 2007-11-29 アース製薬株式会社 Gel material
WO2026037982A1 (en) * 2024-08-13 2026-02-19 Kemira Oyj Silicate adsorbent material and use of silicate adsorbent material in water treatment

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