JPS58153537A - Adsorbent - Google Patents
AdsorbentInfo
- Publication number
- JPS58153537A JPS58153537A JP57037651A JP3765182A JPS58153537A JP S58153537 A JPS58153537 A JP S58153537A JP 57037651 A JP57037651 A JP 57037651A JP 3765182 A JP3765182 A JP 3765182A JP S58153537 A JPS58153537 A JP S58153537A
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- parts
- furnace slag
- alkali metal
- binder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、活性炭を成型する際に、微粉末の高炉水砕ス
ラグとアルカリ金属水酸化物を結合材として用いた吸着
剤に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an adsorbent using finely powdered granulated blast furnace slag and an alkali metal hydroxide as a binder when molding activated carbon.
従来より、ポリエステル、エポキシなどの有機系あるい
はポルトランドセメント、アルミナセメントなどの無機
系の結合材を用い、活性体を所望形状に成型してなる吸
着剤は、脱臭剤などの用途として周く賞月されている。Traditionally, adsorbents made by molding active materials into desired shapes using organic binders such as polyester and epoxy or inorganic binders such as Portland cement and alumina cement have been widely used as deodorizing agents. has been done.
しかし、これらの結合材を用いたものは、吸着能に悪影
響を及ぼしたり、6oo〜1000′cで再生処理する
時に形がくずれたり、強度が減少したりして再使用する
ことが難しいなどの問題があった。However, products using these binders have a negative effect on adsorption capacity, lose their shape when recycled at 6oo~1000'c, and lose strength, making them difficult to reuse. There was a problem.
すなわち、有機系の結合材を用いると、吸着剤表面から
活性炭粉末がはげ落ちるという仕上り状態をよくするこ
とができるが、活性炭の表面を覆ってしまうため、吸着
能が低下し、かつ耐熱性が小さい。一方、無機系の結合
材は、吸着能に大きな悪影響を与えないが、仕上り状態
は悪く耐熱性も小さい。In other words, using an organic binder can improve the finish of the activated carbon powder by flaking off from the adsorbent surface, but since it covers the surface of the activated carbon, the adsorption capacity decreases and the heat resistance decreases. small. On the other hand, inorganic binders do not have a large negative effect on the adsorption capacity, but the finish is poor and the heat resistance is low.
本発明者は、これらの欠点を解決するために種々検討し
た結果、結合材として、高炉水砕スラグ粉末とアルカリ
金属水酸化物を使用すればよいことを見い出し、本発明
を完成したものである。As a result of various studies to solve these drawbacks, the present inventor found that granulated blast furnace slag powder and alkali metal hydroxide could be used as the binder, and completed the present invention. .
すなわち、本発明は、活性炭を高炉水砕スラグ粉末とア
ルカリ土類金属水酸化物からなる結合材、を用いて所望
形状に成型してなる吸着剤である。That is, the present invention is an adsorbent formed by molding activated carbon into a desired shape using a binder made of granulated blast furnace slag powder and an alkaline earth metal hydroxide.
以下、詳しく本発明を説明、すると、活性炭は、粉末活
性炭、造粒活性炭の区別なく使用できる。The present invention will be described in detail below. Activated carbon can be used regardless of whether it is powdered activated carbon or granulated activated carbon.
高炉水砕スラグ粉末は、鉄鋼製造時の副産物として排出
されるごく普通のもので十分であり、その粉末度は、活
性炭の粉末度に応じて細かくすることが望ましいことで
あるが、強度発現を考慮して、ブレーン比表面積3 、
000 cm5/lもあれば十分である0アルカリ金属
水酸化物は、高炉水砕スラグ粉末の水和活性を刺激して
、短時間に吸着剤を成型するのに必要な成分であり、そ
の使用量は、高炉水砕スラグ100重量部に対し0.5
〜15重景部程度が好ましい。0.5重量部よりも著し
く少量では強度発現は小さく、また、15重量部よりも
多量であっても強度発現の伸びはなく、却ってアルカリ
が溶出する危険がある。好適には3〜10重量部である
。アルカリ金属水−化物は、活性炭を賦活する効果もあ
り、吸着能によい影響を与える。アルカリ金属水酸化物
としては、LiOH、NaOH、KOHなどがあげられ
るが、工業的にはNaOHが好ましい。As for the granulated blast furnace slag powder, it is sufficient to use a very ordinary one discharged as a by-product during steel manufacturing, and it is desirable to make the powder fine according to the fineness of the activated carbon, but it is important to reduce the strength development. Considering the Blaine specific surface area 3,
000 cm5/l is sufficient.0 Alkali metal hydroxide is a necessary component to stimulate the hydration activity of granulated blast furnace slag powder and form an adsorbent in a short time, and its use is The amount is 0.5 per 100 parts by weight of granulated blast furnace slag.
It is preferable to have a depth of about 15 to 15. If the amount is significantly less than 0.5 parts by weight, the strength development will be small, and if the amount is more than 15 parts by weight, there will be no increase in the strength development, and there is a risk that the alkali will elute. It is preferably 3 to 10 parts by weight. Alkali metal hydrates also have the effect of activating activated carbon and have a positive effect on adsorption capacity. Examples of the alkali metal hydroxide include LiOH, NaOH, and KOH, but NaOH is industrially preferred.
また、アルカリ金属水酸化物は、例えば、Na2CO3
゜NaHCO3,K2Co、 、 IG(Co、などの
アルカリ金属炭酸塩やアルカリ金属炭酸水素塩と併用す
ることにより、さらに大きな強度を有する吸着剤とする
ことができる。その添加量は、高炉水砕□スラグ100
重量部に対し、10重量部以下、とくに5〜8重量部が
るいは粉末状などのいずれであってもよい。Further, the alkali metal hydroxide is, for example, Na2CO3
By using it in combination with an alkali metal carbonate or alkali metal hydrogen carbonate such as NaHCO3, K2Co, or IG(Co), an adsorbent with even greater strength can be obtained. slag 100
The amount may be 10 parts by weight or less, particularly 5 to 8 parts by weight, or it may be in powder form.
以上の活性炭と結合材とを水で混練し、所望形状に賦形
後硬化させれば、本発明の吸着剤が得られる。これらの
配合割合の一例を示せば、重量で高炉水砕スラグ100
部、結合材5〜50部、水50〜200部である。The adsorbent of the present invention can be obtained by kneading the above activated carbon and binder with water, shaping it into a desired shape, and then curing it. An example of these blending ratios is: 100% granulated blast furnace slag by weight
part, 5 to 50 parts of binder, and 50 to 200 parts of water.
その際、より少ない使用水で適切な成型性を付与し、か
つ、強度の大きな吸着剤を得るために、セメント系減水
剤や成型助剤を添加することは望ましいことである。At that time, it is desirable to add a cement-based water reducing agent or a molding aid in order to provide appropriate moldability with less water usage and to obtain a strong adsorbent.
セメント系減水剤としては、例えば、アルキルアリルス
ルホン酸塩系、芳香族多環縮合物スルホン酸塩系、水溶
性メラミンホルマリンスルホン酸塩系、リグニンスルホ
ラ酸塩系、オキシ有機酸塩系、ポリオール系、ポリオキ
シエチレンアルキルエーテル系、高級多価ア)レコール
系などから選ばれた1種または2種・以上が使用される
。これらのうち、分子内にスルホン基を有する化合物や
オキシ有機酸塩系が特に好ましい。これらの使用量は結
合材100重量部に対し0.01〜3重量部程度である
。Examples of cement water reducing agents include alkylaryl sulfonate, aromatic polycyclic condensate sulfonate, water-soluble melamine formalin sulfonate, lignin sulforate, oxyorganic acid salt, and polyol. One or two or more selected from the group consisting of polyoxyethylene alkyl ether, higher polyhydric a)lecole, etc. are used. Among these, compounds having a sulfone group in the molecule and oxyorganic acid salts are particularly preferred. The amount of these used is about 0.01 to 3 parts by weight per 100 parts by weight of the binder.
また、成型助剤としては、)殿粉、カルボキシメチルセ
ルロース、メチルセルロース、アビセル、ポリビニール
アルコール、リグニン等の水溶性高分子物質系のもの、
ベントナイト、カオリン、活性白土、酸性白土、ケイソ
ウ土のようなりレー系のもの、コロイダルシリカ、アル
ミナゾル、リン酸アルミニウム、珪酸アルカリ、珪弗化
物などの無機系のもの、エチルシリケール、オルベンよ
うなシリ□力やベントナイトに有機基をグラフトしたも
の、有機ポリマーラテックス等があげられるが、これら
のうち、とくにクレー系と無機系のものが好ましい。そ
の使用量は、活性炭100重景重量対し200重量部以
下である。In addition, molding aids include water-soluble polymer substances such as starch, carboxymethyl cellulose, methyl cellulose, Avicel, polyvinyl alcohol, and lignin;
Ray-based materials such as bentonite, kaolin, activated clay, acid clay, and diatomaceous earth; inorganic materials such as colloidal silica, alumina sol, aluminum phosphate, alkali silicate, and silicate fluorides; Examples include □bentonite grafted with an organic group, organic polymer latex, etc. Among these, clay-based and inorganic-based materials are particularly preferred. The amount used is 200 parts by weight or less per 100 parts by weight of activated carbon.
以上のように、本発明の吸着剤は、活性炭を高炉水砕ス
ラグ粉末とアルカリ金属水酸化物を結合材として成型し
たものであり、それによって、粉末活性炭のはげ落ちが
なく(仕上り状態がよく)、吸着能に全く影響せず、耐
熱性は高く、600〜1000 Cの再生処理をしても
強度低下がほとんどないなど、すぐれた性能を有する吸
着剤とすることができる。As described above, the adsorbent of the present invention is made by molding activated carbon with granulated blast furnace slag powder and alkali metal hydroxide as a binder, and as a result, the powdered activated carbon does not flake off (it has a good finish). ), it does not affect the adsorption capacity at all, has high heat resistance, and shows almost no decrease in strength even after regeneration treatment at 600 to 1000 C, making it possible to create an adsorbent with excellent performance.
以下、実施例をあげてさらに説明する。The present invention will be further explained below with reference to Examples.
実施例1 次に示す工程により粒状冶性炭を製造した。Example 1 Granular metallurgical coal was manufactured by the following steps.
先ず、重量基準で、粉末活性炭(ヤシ殻炭を水蒸気賦活
したもの)100部に対して、ブレーン比表面積6 、
000 cm”/lの高炉水砕スラグ粉末65部、Na
OH2部、グルコン酸ソーダ0.03部、ペン・トナイ
ト15部、活性白土1ち部、アルミナゾルよびポリビニ
ルアルコール2部を混合しながら、水170部を徐々に
添加し、捏和した湿式混練物をペレタイザーに投入し、
円柱状顆粒化した。なお、混線機としてはモルタルミキ
サーを用いた。次G)で、この湿ペレット化したものを
転勤式造粒機であるマルメライザーにより球形化し、そ
れを100Cで乾燥した。得られた成型物の1〜5wm
のものを選別し、本発明の吸着剤とした。比較品として
普通ポルトランドセメントとポリエステル系の結合材を
使用し、同様な工程で吸着剤を製造した。First, on a weight basis, Blaine specific surface area 6 for 100 parts of powdered activated carbon (coconut shell charcoal activated with steam),
000 cm”/l 65 parts of granulated blast furnace slag powder, Na
While mixing 2 parts of OH, 0.03 parts of sodium gluconate, 15 parts of pen tonite, 1 part of activated clay, 2 parts of alumina sol and polyvinyl alcohol, 170 parts of water was gradually added, and the resulting wet kneaded product was mixed. Pour into pelletizer,
It was formed into cylindrical granules. Note that a mortar mixer was used as the mixer. In the next step G), the wet pellets were spheroidized using a Marumerizer, which is a rotating granulator, and dried at 100C. 1 to 5 wm of the obtained molded product
These were selected and used as the adsorbent of the present invention. As a comparative product, an adsorbent was manufactured in the same process using ordinary Portland cement and a polyester-based binder.
これらの吸着剤の性能を評価するため、100C乾燥後
と700C再生処理後における強さ及びフェノール吸着
量を測定した。それらの結果を第1表に示す。In order to evaluate the performance of these adsorbents, the strength and adsorption amount of phenol were measured after drying at 100C and after regeneration treatment at 700C. The results are shown in Table 1.
なお、強さは台ばかりに1粒の粒状活性炭をおき、その
上に平板をのせ、力を加えて割れたときの目盛(?数)
を読んで測定した。また、吸着量はフェノール溶液1p
に1?の粒状活性炭を入れて口過し、0液中のフェノー
ル炙存量を定量して吸着量を求めた。The strength is measured by placing a grain of activated carbon on the stand, placing a flat plate on top of it, and applying force to it to break it.
was read and measured. In addition, the amount of adsorption is 1 p of phenol solution.
1? granulated activated carbon was added and passed through the mouth, and the amount of phenol remaining in the liquid was determined to determine the amount of adsorption.
以下余白
第 1 表
実施例2
実施例1と同様の方法で製造した湿式混線物を加圧成型
(圧′j:J30に#f/m”) シて得た角柱状(−
2儒X 2 cm X 8 m)の吸着量につき試験を
した。その結果を第2表に示す。The following is a margin: Table 1 Example 2 A prismatic (-
A test was conducted on an adsorption amount of 2 cm x 2 cm x 8 m). The results are shown in Table 2.
なお、圧縮強度は、JISR52(11に準じて測定し
た0
第 2 表The compressive strength was measured according to JISR52 (11) Table 2
Claims (1)
らなる結合材を用いて所望形状に成型してなる吸着剤。An adsorbent made by molding activated carbon into a desired shape using a binder consisting of granulated blast furnace slag powder and an alkali metal hydroxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57037651A JPS58153537A (en) | 1982-03-10 | 1982-03-10 | Adsorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57037651A JPS58153537A (en) | 1982-03-10 | 1982-03-10 | Adsorbent |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58153537A true JPS58153537A (en) | 1983-09-12 |
JPH0314497B2 JPH0314497B2 (en) | 1991-02-26 |
Family
ID=12503541
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57037651A Granted JPS58153537A (en) | 1982-03-10 | 1982-03-10 | Adsorbent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58153537A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4855276A (en) * | 1987-09-02 | 1989-08-08 | Purafil, Inc. | Solid filtration medium incorporating alumina and carbon |
US4946663A (en) * | 1987-10-15 | 1990-08-07 | The British Petroleum Company, P.L.C. | Production of high surface area carbon fibres |
JP2012250904A (en) * | 2011-05-06 | 2012-12-20 | National Institute Of Advanced Industrial Science & Technology | Composite containing metal complex, and radiocesium adsorbent using the same |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5468833A (en) * | 1977-11-10 | 1979-06-02 | Mitsubishi Mining & Cement Co | Method of making cured gypsum base body |
-
1982
- 1982-03-10 JP JP57037651A patent/JPS58153537A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5468833A (en) * | 1977-11-10 | 1979-06-02 | Mitsubishi Mining & Cement Co | Method of making cured gypsum base body |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4855276A (en) * | 1987-09-02 | 1989-08-08 | Purafil, Inc. | Solid filtration medium incorporating alumina and carbon |
US4946663A (en) * | 1987-10-15 | 1990-08-07 | The British Petroleum Company, P.L.C. | Production of high surface area carbon fibres |
JP2012250904A (en) * | 2011-05-06 | 2012-12-20 | National Institute Of Advanced Industrial Science & Technology | Composite containing metal complex, and radiocesium adsorbent using the same |
Also Published As
Publication number | Publication date |
---|---|
JPH0314497B2 (en) | 1991-02-26 |
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