JPH10137524A - Anti-bacterial activated carbon and its production - Google Patents

Anti-bacterial activated carbon and its production

Info

Publication number
JPH10137524A
JPH10137524A JP8306221A JP30622196A JPH10137524A JP H10137524 A JPH10137524 A JP H10137524A JP 8306221 A JP8306221 A JP 8306221A JP 30622196 A JP30622196 A JP 30622196A JP H10137524 A JPH10137524 A JP H10137524A
Authority
JP
Japan
Prior art keywords
silver
activated carbon
water
antibacterial
sulfide
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
JP8306221A
Other languages
Japanese (ja)
Inventor
Yoshiaki Ikeda
美昭 池田
Tadao Nakatsuji
忠夫 仲辻
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.)
Sakai Chemical Industry Co Ltd
Original Assignee
Sakai Chemical Industry 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 Sakai Chemical Industry Co Ltd filed Critical Sakai Chemical Industry Co Ltd
Priority to JP8306221A priority Critical patent/JPH10137524A/en
Publication of JPH10137524A publication Critical patent/JPH10137524A/en
Pending legal-status Critical Current

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  • Filtering Materials (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an anti-bacterial activated carbon excellent in duration of antibacterial activity by eluting silver into water in a stable low concentration over a long period. SOLUTION: This anti-bacterial activated carbon is constituted so as to carry 0.1-15 pts.wt. total of silver, silver oxide and silver sulfide expressed in terms of silver to 100 pts.wt. of activated carbon. The anti-bacterial activated carbon is obtained by dipping the activated carbon in an aq. solution of a water soluble silver salt, drying to carry silver and silver oxide on the activated carbon and next treating with a sulfidizing agent to sulfidize a part of silver and silver oxide carried on the activated carbon.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、例えば、水に含ま
れる大腸菌やその他のバクテリア等の増殖を抑制する濾
材として水濾過器や浄水装置等に用いる抗菌性活性炭及
びその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an antibacterial activated carbon used for a water filter, a water purifier and the like as a filter medium for suppressing the growth of, for example, Escherichia coli and other bacteria contained in water, and a method for producing the same.

【0002】[0002]

【従来の技術】従来、例えば、一般の水道水に含まれる
有害なトリハロメタン類を除去するために、水道水を活
性炭で処理するようにした濾過器や浄水装置等が種々、
知られているが、これら装置に大腸菌等の雑菌が混入し
た場合、これらは装置内で増殖し、上記装置による処理
水を却って汚染することとなる。従って、従来の濾過器
や浄水装置等においては、止水後、24時間以上経過し
ておれば、数分間、装置に水を通して、所謂捨て水をす
ることが必要である。
2. Description of the Related Art Conventionally, for example, in order to remove harmful trihalomethanes contained in general tap water, there are various filters and water purifiers which treat tap water with activated carbon.
As is known, when bacteria such as Escherichia coli are mixed in these devices, they grow in the devices and contaminate the water treated by the devices. Therefore, in the case of a conventional filter, a water purifier, or the like, it is necessary to pass water through the device for a few minutes, so-called abandoned water, if 24 hours or more have passed after stopping water.

【0003】そこで、このような問題を解決するため
に、従来、活性炭に抗菌性の高い銀を担持させて、これ
を濾過器や浄水装置の濾材として用いることが多いが、
しかし、このように銀を担持させてなる活性炭を濾材と
して用いた場合、その初期には、水中への銀の溶出量が
過大であって、例えば、米国において基準値である50
ppbを越えるが、その後、溶出量が急激に低減して、
殺菌効果や菌の増殖を抑制する抗菌性が不十分となる。
即ち、従来の銀担持活性炭は、その抗菌効果の安定持続
性に欠ける。
Therefore, in order to solve such a problem, activated carbon is conventionally supported with silver having a high antibacterial property, and this is often used as a filter medium of a filter or a water purification device.
However, when activated carbon carrying silver as described above is used as a filter medium, the amount of silver eluted into water is excessive in the initial stage, and for example, the standard value in the United States of 50
ppb, but then the amount of elution sharply decreases,
The bactericidal effect and the antibacterial property of suppressing the growth of bacteria become insufficient.
That is, the conventional silver-carrying activated carbon lacks the stability and sustainability of its antibacterial effect.

【0004】[0004]

【発明が解決しようとする課題】本発明は、従来、濾材
として用いられている銀担持活性炭における上述したよ
うな問題を解決するためになされたものであって、銀を
長期間にわたって安定して低い濃度で水中に溶出させ、
かくして、抗菌作用の持続性にすぐれた抗菌性活性炭及
びその製造方法を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention has been made to solve the above-mentioned problems in the silver-supported activated carbon conventionally used as a filter medium, and is intended to stabilize silver for a long period of time. Eluted in water at low concentration,
Thus, an object of the present invention is to provide an antibacterial activated carbon having excellent antibacterial activity and a method for producing the same.

【0005】[0005]

【課題を解決するための手段】本発明による抗菌性活性
炭は、活性炭100重量部に対して、銀、酸化銀及び硫
化銀を合計量にて銀換算にて0.1〜15重量部の割合に
て担持させてなることを特徴とする。以下、活性炭に担
持させた銀、酸化銀及び硫化銀の銀換算による合計量を
全銀担持量という。
The antibacterial activated carbon according to the present invention comprises silver, silver oxide and silver sulfide in a total amount of 0.1 to 15 parts by weight in terms of silver based on 100 parts by weight of activated carbon. It is characterized by being carried by. Hereinafter, the total amount of silver, silver oxide, and silver sulfide carried on activated carbon in terms of silver is referred to as total silver carried amount.

【0006】本発明によれば、この全銀担持量のうち、
硫化銀の割合が銀換算にて5〜80重量%であることが
好ましい。以下、全銀担持量のうち、銀換算による硫化
銀の割合を単に硫化銀担持比率という。また、本発明に
よる抗菌性活性炭の製造方法は、活性炭を水溶性銀塩の
水溶液に浸漬した後、乾燥させて、活性炭に銀及び酸化
銀を担持させ、次いで、この活性炭を硫化剤にて処理
し、活性炭に担持させた上記銀及び酸化銀の一部を硫化
することを特徴とする。
According to the present invention, of the total silver carrying amount,
The proportion of silver sulfide is preferably from 5 to 80% by weight in terms of silver. Hereinafter, the ratio of silver sulfide in terms of silver in the total silver carried amount is simply referred to as silver sulfide carried ratio. In addition, the method for producing an antibacterial activated carbon according to the present invention comprises immersing activated carbon in an aqueous solution of a water-soluble silver salt, drying the activated carbon, supporting silver and silver oxide on the activated carbon, and then treating the activated carbon with a sulfurizing agent. In addition, a part of the silver and the silver oxide supported on the activated carbon is sulfurized.

【0007】[0007]

【発明の実施の形態】本発明において用いる活性炭は、
その種類や形状や大きさは、特に、限定されるものでは
ないが、例えば、椰子がら活性炭の顆粒状物、繊維状
物、ハニカム成形体等を好ましく用いることができる。
本発明による抗菌性活性炭は、このような活性炭を水溶
性銀塩の水溶液に浸漬した後、乾燥させて、銀及び酸化
銀を担持させ、次いで、このような活性炭を硫化剤にて
処理して、上記銀及び酸化銀の一部を硫化銀に変換す
る。
BEST MODE FOR CARRYING OUT THE INVENTION The activated carbon used in the present invention is:
The type, shape and size are not particularly limited, but, for example, coconut palm, activated carbon granules, fibrous materials, honeycomb molded bodies, and the like can be preferably used.
The antibacterial activated carbon according to the present invention is obtained by immersing such activated carbon in an aqueous solution of a water-soluble silver salt, drying it, supporting silver and silver oxide, and then treating such activated carbon with a sulfurizing agent. The silver and part of the silver oxide are converted to silver sulfide.

【0008】上記水溶性銀塩としては、例えば、炭酸塩
や硝酸塩が好ましく用いられる。これらの活性炭への担
持量は、活性炭100重量部に対して、銀換算で0.1〜
15重量部、好ましくは、0.5〜10重量部の範囲であ
る。このようにして、活性炭に銀を担持させた後、必要
に応じて、活性炭を100〜300℃程度の比較的低い
温度で焼成してもよい。特に、200℃以上の温度で焼
成することによって、酸化銀の担持割合を増加させるこ
とができる。また、必要に応じて、還元性雰囲気中で焼
成してもよく、これによれば、銀の担持割合を増加させ
ることができる。
As the water-soluble silver salt, for example, a carbonate or a nitrate is preferably used. The amount supported on these activated carbons is 0.1 to 100 parts by weight of activated carbon in terms of silver.
It is in the range of 15 parts by weight, preferably 0.5 to 10 parts by weight. After silver is thus supported on the activated carbon, the activated carbon may be fired at a relatively low temperature of about 100 to 300 ° C., if necessary. In particular, by firing at a temperature of 200 ° C. or higher, the loading ratio of silver oxide can be increased. Further, if necessary, sintering may be performed in a reducing atmosphere, whereby the loading ratio of silver can be increased.

【0009】このようにして銀と酸化銀とを担持させた
活性炭を硫化処理するには、通常、この活性炭を硫化剤
の水溶液に浸漬すればよい。この硫化剤としては、通
常、硫化ナトリウムや硫化アンモニウムが好ましく用い
られる。しかし、場合によっては、活性炭を水に分散さ
せ、これに硫化水素を吹き込むことによっても、活性炭
に担持させた銀と酸化銀を硫化することもできる。この
ように、水中にて活性炭に担持させた銀及び酸化銀を硫
化した後、これを濾過し、乾燥して、銀及び酸化銀を担
持させた活性炭を得る。
In order to carry out the sulfurizing treatment of the activated carbon carrying silver and silver oxide in this manner, it is usually sufficient to immerse the activated carbon in an aqueous solution of a sulfurizing agent. Normally, sodium sulfide and ammonium sulfide are preferably used as the sulfurizing agent. However, in some cases, silver and silver oxide supported on the activated carbon can be sulfided by dispersing the activated carbon in water and blowing hydrogen sulfide into the water. After sulfided silver and silver oxide supported on activated carbon in water in this way, the resultant is filtered and dried to obtain activated carbon supporting silver and silver oxide.

【0010】必要に応じて、このようにして硫化処理し
た活性炭を還元性雰囲気中、100〜200℃程度の比
較的低い温度で焼成してもよく、これによれば、銀の担
持割合を増加させることができる。このようにして、活
性炭に担持させた銀、酸化銀及び硫化銀を硫化物とする
ことによって、水中への銀の溶出量を長期間にわたって
低く抑えて、抗菌性を持続させることができる。このよ
うに、銀及び酸化銀の硫化処理によって、水中への銀の
溶出を抑えることができるのは、硫化処理が銀及び酸化
銀の表面に溶出量が極めて低い硫化銀の被膜を形成し
て、銀及び酸化銀の溶出を制御するためでけあるとみら
れる。しかし、本発明は、何ら理論によって限定される
ものではない。
[0010] If necessary, the activated carbon thus sulfurized may be calcined in a reducing atmosphere at a relatively low temperature of about 100 to 200 ° C. Can be done. In this way, by using silver, silver oxide and silver sulfide carried on activated carbon as sulfide, the amount of silver eluted into water can be kept low for a long period of time, and the antibacterial property can be maintained. Thus, silver can be suppressed from elution into water by the sulfurizing treatment of silver and silver oxide because the sulfurating treatment forms a silver sulfide coating with a very low elution amount on the surface of silver and silver oxide. To control the dissolution of silver, silver and silver oxide. However, the present invention is not limited by any theory.

【0011】本発明によれば、このようにして、活性炭
における全銀担持量は、主として、経済性の点から、活
性炭100重量部に対して、0.1〜15重量部、好まし
くは、0.5〜10重量部の範囲であり、しかも、この全
銀担持量のうち、硫化銀担持比率は、5〜80重量%の
範囲であることが好ましく、特に、30〜50重量%の
範囲であることが好ましい。本発明によれば、活性炭に
銀、酸化銀及び硫化銀をこのような割合で担持させるこ
とによって、銀を低いレベルで、長期間にわたって安定
に水中に溶出させることができる。即ち、本発明による
抗菌性活性炭は、通常、1000mLあたり、数十トン
乃至100トンの水を濾過処理した後も、滞留水中に、
通常、5〜100ppbの範囲、好ましくは、10〜5
0ppbの範囲で銀を水中に溶出させることができる。
According to the present invention, the total silver loading on the activated carbon is 0.1 to 15 parts by weight, preferably 0 to 15 parts by weight, based on 100 parts by weight of the activated carbon, mainly from the viewpoint of economy. The amount of silver sulfide carried is preferably in the range of 5 to 80% by weight, and more preferably in the range of 30 to 50% by weight. Preferably, there is. According to the present invention, silver, silver oxide and silver sulfide are supported on activated carbon at such a ratio, whereby silver can be stably eluted in water at a low level for a long period of time. That is, the antibacterial activated carbon according to the present invention is usually, after filtering treatment of several tens tons to 100 tons of water per 1000 mL, in the retained water,
Usually, in the range of 5-100 ppb, preferably 10-5
Silver can be eluted in water in the range of 0 ppb.

【0012】また、前述したようにして、銀及び酸化銀
を担持させた活性炭を得た後、これを還元剤にて還元処
理し、次いで、この活性炭を硫化剤にて処理し、活性炭
に担持させた銀及び酸化銀の一部を硫化することによっ
ても、本発明による抗菌性活性炭を得ることができる。
銀及び酸化銀を担持させた活性炭を還元剤にて還元処理
することによって、上記銀/酸化銀の割合を高くするこ
とができ、硫化処理後も、銀/酸化銀の割合を高く維持
するすることができ、ここに、水中への銀の溶出速度が
酸化銀よりも遅いので、かくして、このようにして得ら
れる抗菌性活性炭は、水中への初期の銀の溶出量が低い
と共に、低い濃度での溶出を一層長期間にわたって持続
することができる。
As described above, after obtaining activated carbon carrying silver and silver oxide, the activated carbon is reduced with a reducing agent, and then the activated carbon is treated with a sulphidating agent to carry the activated carbon on activated carbon. The antibacterial activated carbon according to the present invention can also be obtained by sulfurizing a part of the silver and silver oxide.
By reducing the activated carbon carrying silver and silver oxide with a reducing agent, the ratio of silver / silver oxide can be increased, and the ratio of silver / silver oxide is maintained high even after the sulfurating treatment. Here, since the elution rate of silver into water is lower than that of silver oxide, the thus obtained antibacterial activated carbon has a low initial silver elution rate in water and a low concentration. Can be continued for a longer period of time.

【0013】本発明による抗菌性活性炭を従来の浄水装
置に濾材として組み込むことによって、浄水装置に衛生
機能を付加して高機能化することができる。また、本発
明による抗菌性活性炭を濾材とする濾過装置を従来の浄
水装置と組合わせて用いてもよい。更に、本発明による
抗菌性活性炭は、高層建築物における貯水槽の処理に用
いてもよい。このようにして、本発明による抗菌性活性
炭を用いれば、安全な飲料水等の生活用水や動植物の飼
育用の水等を容易に且つ低廉に得ることができる。
By incorporating the antibacterial activated carbon according to the present invention into a conventional water purification device as a filter medium, the water purification device can be provided with a hygienic function to be highly functional. Further, a filtration device using the antibacterial activated carbon according to the present invention as a filter medium may be used in combination with a conventional water purification device. Further, the antibacterial activated carbon according to the present invention may be used for treating water tanks in high-rise buildings. In this way, the use of the antibacterial activated carbon according to the present invention makes it possible to easily and inexpensively obtain safe living water such as drinking water and water for breeding animals and plants.

【0014】[0014]

【発明の効果】以上のように、本発明による抗菌性活性
炭は、活性炭に銀と酸化銀とを担持させた後、これらの
一部を硫化処理してなるものであるので、長期間にわた
って安定して低いレベルで水中に銀を溶出させることが
でき、かくして、水中の大腸菌やその他のバクテリア等
の増殖を抑制する濾材として好適に用いることができ
る。
As described above, the antibacterial activated carbon according to the present invention is obtained by carrying silver and silver oxide on activated carbon and subjecting a part of them to sulfuration treatment, so that they are stable for a long period of time. Thus, silver can be eluted into water at a low level, and thus can be suitably used as a filter medium for suppressing the growth of Escherichia coli and other bacteria in water.

【0015】[0015]

【実施例】以下に実施例を挙げて本発明を説明するが、
本発明はこれら実施例により何ら限定されるものではな
い。
EXAMPLES The present invention will be described below with reference to examples.
The present invention is not limited by these examples.

【0016】実施例1 硝酸銀32gを蒸留水10Lに溶解させ、得られた溶液
に粒子径0.1〜0.3mm相当の椰子がら活性炭2kgを
1時間浸漬した後、これを濾過し、水洗し、乾燥させ
た。次いで、このようにして、銀と酸化銀とを担持させ
た活性炭を硫化ナトリウム9水和物の5重量%水溶液1
0Lに1時間浸漬した後、濾過し、十分に水洗し、その
後、110℃で24時間、乾燥させて、本発明による抗
菌性活性炭を得た。
Example 1 32 g of silver nitrate was dissolved in 10 L of distilled water, and 2 kg of coconut palm with a particle size of 0.1 to 0.3 mm was immersed in the obtained solution for 1 hour, followed by filtration and washing with water. And dried. Then, the activated carbon carrying silver and silver oxide was mixed with a 5% by weight aqueous solution of sodium sulfide nonahydrate 1 in this manner.
After being immersed in 0 L for 1 hour, the solution was filtered, sufficiently washed with water, and then dried at 110 ° C. for 24 hours to obtain an antibacterial activated carbon according to the present invention.

【0017】このようにして得られた抗菌性活性炭にお
ける銀、酸化銀及び硫化銀の合計の担持量(全銀担持
量)は、蛍光X線分析装置(理学電機(株)製3270
型)を用いる検量線による銀の定量分析から求めた。そ
の結果、全銀担持量は、活性炭100重量部に対して、
0.98重量部であった。同様にして、抗菌性活性炭にお
けるイオウ量を蛍光X線分析装置(理学電機(株)製3
270型)を用いる検量線による定量分析から求め、こ
れに基づいて銀換算による硫化銀担持量を求めたとこ
ろ、活性炭100重量部に対して、0.45重量部であっ
た。これより、抗菌性活性が有持する全銀担持量のう
ち、硫化銀比率は、45.9重量%であった。
The total supported amount of silver, silver oxide and silver sulfide (total silver supported amount) in the thus obtained antibacterial activated carbon was determined by a fluorescent X-ray analyzer (3270 manufactured by Rigaku Corporation).
) Was determined from a quantitative analysis of silver by a calibration curve using As a result, the total silver carried amount was 100 parts by weight of activated carbon,
0.98 parts by weight. Similarly, the amount of sulfur in the antibacterial activated carbon was measured using a fluorescent X-ray analyzer (Rigaku Denki Co., Ltd. 3
The amount of silver sulfide carried was calculated in terms of silver based on the quantitative analysis using a calibration curve using Model 270), and it was 0.45 part by weight based on 100 parts by weight of activated carbon. As a result, the ratio of silver sulfide to the total amount of silver supported by the antibacterial activity was 45.9% by weight.

【0018】また、抗菌性活性炭における銀/酸化銀
(銀換算による重量比)は、X線光電子分光分析装置
((株)島津製作所製ESCA−850)を用いて測定
した結果、61/39であった。次に、抗菌性活性炭2
00mLを塩化ビニル樹脂製カラムに充填し、水道水を
3L/分の割合で100トン通水し、その間、所定の間
隔でカラムに水道水を8時間滞留させて、水中への銀の
溶出量を測定した。水中の銀の溶出量は、セイコー電子
(株)製SPS−1200Aを用いるプラズマ発光分析
法(ICP)にて検量線による定量分析を行なった。そ
の結果を表1に示すように、銀の溶出量は20〜50p
pbの範囲であった。
The silver / silver oxide (weight ratio in terms of silver) of the antibacterial activated carbon was measured using an X-ray photoelectron spectrometer (ESCA-850, manufactured by Shimadzu Corporation). there were. Next, antibacterial activated carbon 2
100 mL was packed in a vinyl chloride resin column, and 100 tons of tap water was passed through at a rate of 3 L / min. During that time, tap water was retained in the column at predetermined intervals for 8 hours to elute silver into the water. Was measured. The amount of silver eluted in water was quantitatively analyzed by a calibration curve by plasma emission spectrometry (ICP) using SPS-1200A manufactured by Seiko Denshi Co., Ltd. As shown in Table 1, the elution amount of silver was 20 to 50 p.
pb range.

【0019】実施例2 硝酸銀16gを蒸留水10Lに溶解させ、得られた溶液
に粒子径0.1〜0.3mm相当の椰子がら活性炭2kgを
1時間浸漬した後、これを濾過し、水洗した。このよう
にして銀と酸化銀とを担持させた活性炭を再度、水10
Lに分散させ、これにヒドラジン1容量%を加え、発泡
が終わって、30分後に濾過、水洗し、乾燥させた。次
いで、このようにして酸化銀を還元した活性炭を硫化ナ
トリウム9水和物の5重量%水溶液10Lに1時間浸漬
した後、濾過し、十分に水洗し、その後、110℃で2
4時間、乾燥させて、本発明による抗菌性活性炭を得
た。
Example 2 16 g of silver nitrate was dissolved in 10 L of distilled water, and 2 kg of coconut palm with a particle size of 0.1 to 0.3 mm was immersed in the obtained solution for 1 hour, followed by filtration and washing with water. . The activated carbon carrying silver and silver oxide in this way is again
L, and 1% by volume of hydrazine was added thereto. After the foaming was completed, the mixture was filtered, washed with water and dried after 30 minutes. Then, the activated carbon thus reduced in silver oxide was immersed in 10 L of a 5% by weight aqueous solution of sodium sulfide nonahydrate for 1 hour, filtered, washed thoroughly with water, and then dried at 110 ° C. for 2 hours.
After drying for 4 hours, an antibacterial activated carbon according to the present invention was obtained.

【0020】実施例1と同様にして、この抗菌性活性炭
を分析した結果、全銀担持量は、活性炭100重量部に
対して、銀換算にて、0.99重量部であり、また、硫化
銀担持量は、銀換算にて、活性炭100重量部に対し
て、0.42重量部であった。従って、抗菌性活性が有持
する全銀担持量のうち、硫化銀担持比率は、42.4重量
%であった。
As a result of analyzing this antibacterial activated carbon in the same manner as in Example 1, the total amount of silver carried was 0.99 parts by weight in terms of silver with respect to 100 parts by weight of activated carbon. The amount of silver carried was 0.42 parts by weight in terms of silver based on 100 parts by weight of activated carbon. Therefore, the silver sulfide loading ratio was 42.4% by weight of the total silver loading having the antibacterial activity.

【0021】また、抗菌性活性炭における銀/酸化銀
(銀換算による重量比)は93/7であった。この抗菌
性活性炭について、実施例1と同様に試験して、水中へ
の銀の溶出量を測定した。結果を表1に示すように、銀
の溶出量は10〜40ppbの範囲であった。
The ratio of silver / silver oxide (weight ratio in terms of silver) of the antibacterial activated carbon was 93/7. This antibacterial activated carbon was tested in the same manner as in Example 1, and the amount of silver eluted into water was measured. As shown in Table 1, the elution amount of silver was in the range of 10 to 40 ppb.

【0022】比較例1 椰子がら活性炭100重量部に対して、銀1重量部を担
持させてなる市販品を用いて、実施例1と同様に試験し
て、水中への銀の溶出量を測定した。結果を表1に示す
ように、通水初期の水中への銀溶出量が非常に高い反
面、溶出量は経時的に急激に減少した。
COMPARATIVE EXAMPLE 1 Using a commercial product having 1 part by weight of silver supported on 100 parts by weight of activated carbon from coconut palm, a test was conducted in the same manner as in Example 1, and the amount of silver eluted into water was measured. did. As shown in Table 1, the amount of silver eluted into water in the initial stage of water passage was extremely high, but the amount of elution rapidly decreased with time.

【0023】[0023]

【表1】 [Table 1]

【0024】比較例2 実施例1において、活性炭に担持させた銀と酸化銀とを
硫化するに際して、硫化ナトリウム9水和物の30重量
%水溶液を用いた以外は、実施例1と同様にして、抗菌
性活性炭を得た。実施例1と同様にして、この抗菌性活
性炭を分析した結果、全銀担持量は、活性炭100重量
部に対して、0.99重量部であり、硫化銀担持量は、活
性炭100重量部に対して、銀換算にて、0.93重量部
であった。従って、抗菌性活性が有持する全銀担持量の
うち、硫化銀担持比率は、94.9重量%であった。この
抗菌性活性炭200mLを塩化ビニル樹脂製カラムに充
填し、水道水を3L/分の割合で5トン通水した後、カ
ラムに水道水を8時間滞留させて、水中への銀の溶出量
を実施例1と同様にして測定したところ、5ppbを下
回るものであった。
Comparative Example 2 The procedure of Example 1 was repeated, except that a 30% by weight aqueous solution of sodium sulfide nonahydrate was used to sulfide silver and silver oxide supported on activated carbon. , An antibacterial activated carbon was obtained. As a result of analyzing this antibacterial activated carbon in the same manner as in Example 1, the total amount of silver carried was 0.99 parts by weight with respect to 100 parts by weight of activated carbon, and the amount of silver sulfide carried was 100 parts by weight of activated carbon. On the other hand, it was 0.93 parts by weight in terms of silver. Therefore, the silver sulfide loading ratio was 94.9% by weight of the total silver loading having the antibacterial activity. After filling 200 mL of this antibacterial activated carbon into a vinyl chloride resin column and passing 5 tons of tap water at a rate of 3 L / min, the tap water was retained in the column for 8 hours to reduce the amount of silver eluted into the water. It was less than 5 ppb when measured in the same manner as in Example 1.

【0025】実施例3及び比較例3及び4 実施例2と同様にして、種々の担持量にて銀を担持さ
せ、ヒドラジン還元した後、銀を硫化処理して、本発明
による抗菌性活性炭を得た。この抗菌性活性炭における
全銀担持量、硫化及びヒドラジン還元処理の条件、抗菌
性活性炭における銀/酸化銀/硫化銀の銀換算による重
量比を表2に示す。更に、実施例1と同様にして、それ
ぞれの抗菌性活性炭200mLを塩化ビニル樹脂製カラ
ムに充填し、水道水を3L/分の割合で5トン及び50
トン通水した後、カラムに水道水を12時間滞留させ
て、水中への銀の溶出量を実施例1と同様にして測定し
た。結果を表2及び表3に示す。
Example 3 and Comparative Examples 3 and 4 In the same manner as in Example 2, silver was supported in various amounts and hydrazine was reduced, and then the silver was sulfurized to obtain the antibacterial activated carbon according to the present invention. Obtained. Table 2 shows the total amount of silver carried in the antibacterial activated carbon, the conditions of the sulfurization and hydrazine reduction treatment, and the weight ratio of silver / silver oxide / silver sulfide in the antibacterial activated carbon in terms of silver. Further, in the same manner as in Example 1, 200 mL of each antibacterial activated carbon was packed in a vinyl chloride resin column, and tap water was supplied at a rate of 3 L / min for 5 tons and 50 tons.
After passing water through the column, tap water was retained in the column for 12 hours, and the amount of silver eluted into the water was measured in the same manner as in Example 1. The results are shown in Tables 2 and 3.

【0026】表2及び3に示すように、本発明の抗菌性
活性炭によれば、銀の溶出量は、10〜100ppbの
範囲であり、好ましい場合には、10〜50ppbの範
囲で安定している。これに対して、比較例3による抗菌
性活性炭は、全銀担持量が過大であって、硫化処理にか
かわらずに、水中への銀の溶出量が過大である。他方、
比較例4による抗菌性活性炭は、全銀担持量は、本発明
の範囲にあるが、硫化処理をしていないので、初期の銀
溶出量が過大であると共に、経時的に銀溶出量が急激に
減少し、銀溶出の持続性に欠ける。
As shown in Tables 2 and 3, according to the antibacterial activated carbon of the present invention, the amount of silver eluted is in the range of 10 to 100 ppb, and preferably, in the range of 10 to 50 ppb. I have. On the other hand, the antibacterial activated carbon according to Comparative Example 3 has an excessive amount of total silver and an excessive amount of silver eluted into water regardless of the sulfidation treatment. On the other hand,
The antibacterial activated carbon according to Comparative Example 4 has a total silver loading within the range of the present invention, but has not been subjected to sulfidation, so that the initial silver elution is excessive and the silver elution is abrupt over time. And the persistence of silver elution is lacking.

【0027】表2及び表3において、硫化ナトリウム濃
度とは、その水溶液10Lの硫化ナトリウム濃度(重量
%)であり、ヒドラジン濃度とは、10Lに対する容量
%である。また、抗菌性活性炭における銀(金属)、酸
化銀及び硫化銀のそれぞれの割合は、銀換算による割合
(重量%)である。
In Tables 2 and 3, the sodium sulfide concentration is the sodium sulfide concentration (% by weight) of 10 L of the aqueous solution, and the hydrazine concentration is the volume% with respect to 10 L. The ratio of silver (metal), silver oxide and silver sulfide in the antibacterial activated carbon is a ratio (% by weight) in terms of silver.

【0028】[0028]

【表2】 [Table 2]

【0029】[0029]

【表3】 [Table 3]

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】活性炭100重量部に対して、銀、酸化銀
及び硫化銀を合計量にて銀換算にて0.1〜15重量部の
割合にて担持させてなることを特徴とする抗菌性活性
炭。
1. An antibacterial agent comprising silver, silver oxide and silver sulfide in a total amount of 0.1 to 15 parts by weight of silver based on 100 parts by weight of activated carbon. Activated carbon.
【請求項2】活性炭に担持させた銀、酸化銀及び硫化銀
のうち、硫化銀の割合が銀換算にて5〜80重量%であ
る請求項1に記載の抗菌性活性炭。
2. The antibacterial activated carbon according to claim 1, wherein the ratio of silver sulfide to silver, silver oxide and silver sulfide carried on the activated carbon is 5 to 80% by weight in terms of silver.
【請求項3】活性炭を水溶性銀塩の水溶液に浸漬した
後、乾燥させて、活性炭に銀及び酸化銀を担持させ、次
いで、この活性炭を硫化剤にて処理し、活性炭に担持さ
せた上記銀及び酸化銀の一部を硫化することを特徴とす
る抗菌性活性炭の製造方法。
3. The activated carbon is immersed in an aqueous solution of a water-soluble silver salt, and then dried to deposit silver and silver oxide on the activated carbon. Then, the activated carbon is treated with a sulphidating agent to be activated on the activated carbon. A method for producing an antibacterial activated carbon, characterized in that a part of silver and silver oxide is sulfurized.
【請求項4】硫化剤が硫化ナトリウム又は硫化アンモニ
ウムである請求項3に記載の抗菌性活性炭の製造方法。
4. The method according to claim 3, wherein the sulfurizing agent is sodium sulfide or ammonium sulfide.
【請求項5】活性炭を水溶性銀塩の水溶液に浸漬した
後、乾燥させて、活性炭に銀及び酸化銀を担持させ、こ
のように銀及び酸化銀を担持させた活性炭を還元剤にて
還元処理し、次いで、この活性炭を硫化剤にて処理し、
活性炭に担持させた銀及び酸化銀の一部を硫化すること
を特徴とする抗菌性活性炭の製造方法。
5. The activated carbon is immersed in an aqueous solution of a water-soluble silver salt and then dried to carry silver and silver oxide on the activated carbon. The activated carbon thus carrying silver and silver oxide is reduced with a reducing agent. Treatment, and then the activated carbon is treated with a sulfurizing agent,
A method for producing an antibacterial activated carbon, characterized in that a part of silver and silver oxide carried on the activated carbon is sulfurized.
【請求項6】硫化剤が硫化ナトリウム又は硫化アンモニ
ウムである請求項5に記載の抗菌性活性炭の製造方法。
6. The method according to claim 5, wherein the sulfurizing agent is sodium sulfide or ammonium sulfide.
【請求項7】還元剤がヒドラジンである請求項5に記載
の抗菌性活性炭の製造方法。
7. The method according to claim 5, wherein the reducing agent is hydrazine.
JP8306221A 1996-11-18 1996-11-18 Anti-bacterial activated carbon and its production Pending JPH10137524A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8306221A JPH10137524A (en) 1996-11-18 1996-11-18 Anti-bacterial activated carbon and its production

Publications (1)

Publication Number Publication Date
JPH10137524A true JPH10137524A (en) 1998-05-26

Family

ID=17954459

Family Applications (1)

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Country Status (1)

Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000027202A1 (en) * 1998-11-06 2000-05-18 'mid-West' Aktivkohle Gmbh Method for producing bactericidal charcoal
CN1308231C (en) * 2004-07-12 2007-04-04 深圳市清华源兴生物医药科技有限公司 Active carbon loading silver and its preparing method and use
JP2008184718A (en) * 2007-01-31 2008-08-14 Fuji Electric Holdings Co Ltd Activated carbon sheet and method for producing the same
WO2007144057A3 (en) * 2006-06-16 2008-11-06 Merck Patent Gmbh Antimicrobial carbon
KR101093524B1 (en) 2007-04-20 2011-12-14 (주)삼천리카보텍 Preparation method of antibacterial activated carbon

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000027202A1 (en) * 1998-11-06 2000-05-18 'mid-West' Aktivkohle Gmbh Method for producing bactericidal charcoal
CN1308231C (en) * 2004-07-12 2007-04-04 深圳市清华源兴生物医药科技有限公司 Active carbon loading silver and its preparing method and use
WO2007144057A3 (en) * 2006-06-16 2008-11-06 Merck Patent Gmbh Antimicrobial carbon
JP2008184718A (en) * 2007-01-31 2008-08-14 Fuji Electric Holdings Co Ltd Activated carbon sheet and method for producing the same
KR101093524B1 (en) 2007-04-20 2011-12-14 (주)삼천리카보텍 Preparation method of antibacterial activated carbon

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