JPS58110412A - Manufacture of granular activated carbon from waste powdered activated carbon as starting material - Google Patents
Manufacture of granular activated carbon from waste powdered activated carbon as starting materialInfo
- Publication number
- JPS58110412A JPS58110412A JP56214830A JP21483081A JPS58110412A JP S58110412 A JPS58110412 A JP S58110412A JP 56214830 A JP56214830 A JP 56214830A JP 21483081 A JP21483081 A JP 21483081A JP S58110412 A JPS58110412 A JP S58110412A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- adhesive
- bentonite
- inorg
- granular activated
- 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
Links
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
現在、粉末活性炭素は食品工業を中心に年間5万トン前
後使用されている。使用済みの廃粉末活性炭素は廃校状
活性炭素と興なり再生することが難しく、大部分は埋立
処分されている。最近では埋立地の確保が次第に困難に
なっており、廃粉末活性炭素の後処理が問題になってき
ている。DETAILED DESCRIPTION OF THE INVENTION Currently, approximately 50,000 tons of powdered activated carbon is used annually, mainly in the food industry. Used waste activated carbon powder becomes waste activated carbon and is difficult to recycle, so most of it is disposed of in landfills. Recently, it has become increasingly difficult to secure land for landfills, and post-treatment of waste activated carbon powder has become an issue.
廃粉末活性炭素の吸着力は表1に示すようにかなり残っ
ており、吸着力を回復させる再生自体は比較的容易であ
るが、通常高活性炭素には水分が50%以上含まれてお
り、加熱再生を行う時、装置の水蒸気が発生し、このた
め活性炭素の微粉が飛散するので、商業ベースの太μの
再生は困難である。As shown in Table 1, the adsorption power of the waste activated carbon powder remains considerable, and regeneration itself to restore the adsorption power is relatively easy. However, highly activated carbon usually contains more than 50% water. When thermal regeneration is performed, water vapor is generated in the equipment, which scatters fine activated carbon powder, making it difficult to regenerate large μ on a commercial basis.
そこで廃粉末活性炭素の再生時の問題廂である加熱時の
飛散を防ぐため、廃粉末活性炭素を粒状化して再生作業
を容易にし、合わせて安価な粒状活性炭素の製造方法を
検討した。Therefore, in order to prevent the scattering during heating, which is a problem when recycling waste activated carbon powder, we granulated waste activated carbon powder to make the recycling process easier, and at the same time, we investigated an inexpensive method for producing granular activated carbon.
種々の接着剤を廃粉末活性炭素に添加して粒状化し、焼
成を行い、得られた粒状活性炭素の性能を測定して、高
性能で安価な粒状活性炭素を製造 \出来る接着剤を探
索した。We added various adhesives to waste powdered activated carbon, granulated it, fired it, measured the performance of the resulting granular activated carbon, and searched for adhesives that can produce high-performance, inexpensive granular activated carbon. .
有機物質系接着剤では、得られた粒状活性炭素を加熱再
生すると粒子の硬度が著しく小さくなる、あるいは吸着
力の回復が不充分であるなどの問題があることがわかっ
た。It has been found that organic adhesives have problems, such as when the obtained granular activated carbon is heated and regenerated, the hardness of the particles is significantly reduced, or the recovery of adsorption power is insufficient.
無機物質系#着剤では、有機物質系接着剤で生じた上記
の問題点はないが、成型が難しい、あるいは接着剤を多
く添加しないと成型が出来ないなど検討課暉がある。Although inorganic adhesives do not have the above-mentioned problems encountered with organic adhesives, there are still issues to consider, such as difficulty in molding or the inability to mold without adding a large amount of adhesive.
本研究では成型性を改善するための添加物質を探索して
、無機物質系接着剤による廃粉末活性炭素の成型を検討
した。In this study, we searched for additives to improve moldability and investigated the molding of waste activated carbon powder using an inorganic adhesive.
その結果、添加物質としてはベントナイト、無機物質系
接着剤としていわゆるセメント系のケイ酸塩化合物を用
いて廃粉末活性炭素を成型することが出来た。As a result, it was possible to mold waste activated carbon powder using bentonite as an additive and a so-called cement-based silicate compound as an inorganic adhesive.
また成型品を種々の温度で焼成し、焼成品の吸着力を測
定した。その結果500℃以上の温度で焼成すれば吸着
力は大部分回復することがわかった。In addition, the molded products were fired at various temperatures and the adsorption force of the fired products was measured. As a result, it was found that most of the adsorption force can be recovered by firing at a temperature of 500°C or higher.
ベントナイトおよびケイ酸塩化合物は安価な物質であり
、また再生処理も500℃以上での短時間焼成であるの
で以上の製造方法で作られる粒状活性炭素は経済的であ
る。Bentonite and silicate compounds are inexpensive substances, and the regeneration treatment involves short-time firing at 500° C. or higher, so the granular activated carbon produced by the above production method is economical.
実施例
廃粉末活性炭素、ベントナイトおよびケイ酸塩化合物を
60:/3:23 (乾燥重量)の割合でよく混合し、
これに70の比で水を加え、混合した。混合物を直径/
wryの球状に成型した。球状物を乾燥後700’C,
30分間加熱して球状活性炭素を得た。この球状活性炭
素の諸性能は次の通りであった。Example Waste powder activated carbon, bentonite and silicate compound were mixed well in a ratio of 60:/3:23 (dry weight),
Water was added to this in a ratio of 70 and mixed. Diameter of the mixture/
It was molded into a spherical shape. After drying the spheres at 700'C,
Spherical activated carbon was obtained by heating for 30 minutes. The various performances of this spherical activated carbon were as follows.
かさ比重 0.55
比表面積 750♂t
カラメル脱色力 7q
硬度 9.20g
カラメル脱色力はJIS K l 470−1967に
従って測定した。また硬度は粒子7個が破壊される圧力
で20粒子の平均値である。Bulk specific gravity 0.55 Specific surface area 750♂t Caramel decolorizing power 7q Hardness 9.20g Caramel decolorizing power was measured according to JIS Kl 470-1967. Moreover, the hardness is the average value of 20 particles at the pressure at which 7 particles are destroyed.
第1表は廃粉末活性炭素の物性を表したもので項目につ
いてはJISKI470−1967に従って測定した。
また項目中の灰分は固形分を100とした残分である。
手続補正齋
昭和57年S月70日
1、事件の表示 昭和56年特許第214830号2
、発朗の名称
:3.補正をする者
事件との関係 特許出願人
4、補正命令の日付
昭和57年を月9日
5、補正の対象
図面および明細書
6、補正の内容
明細書
1、発明の名称
廃粉末活性炭素を原料とした粒状活性炭素の製造法。
2、特許請求の範囲
廃粉末活性炭素、ベントナイトおよび無機系接着剤をI
IO〜70:5〜30:10〜50の割合によく混合し
たものを成型し、次いて焼成(温度= s o o”c
以上)することにより粒状活性炭素を製造する製法。
3、発明の詳細な説明
現在、粉末活性炭素は食品工業を中心に年間5万トン前
後使用されている。使用済みの廃粉末活性炭素は廃粒状
活性炭素と異なり再生することが難しく、大部分は埋立
処分されている。最近では埋立地の確保が次第に困難に
なっており、廃粉末活性炭素の後処理が問題になってき
ている。
廃粉末活性炭素の吸着力は表1に示すようにかなり残っ
ており、吸着力を回復させる再生自体は比較的容易であ
るが、通常開活性炭素には水分が50%以上含まれてお
り、袈熱再生を行う時、多量の水蒸気が発生し、このた
め活性炭素の微粉が飛散するので、商業ベースの大量の
再生は困難である。
表1 廃粉末活性炭素の物性
1) JIS K 1470−1967に従って
測定した。
2) 固形分を/DOとした残分。
そこで廃粉末活性炭素の再生時の問題点である加熱時の
飛散を防ぐため、廃粉末活性炭素を粒状化して再生作業
を容易にし、合わせて安価な粒状活性炭素の製造方法を
検討した。
種々の接着剤を廃粉末活性炭素に添加して粒状化し、焼
成を行い、得られた粒状活性炭素の性能を測定して、高
性能で安価な粒状活性炭素を製造出来る接着剤を探索し
た。
有機物質系接着剤では、得られた粒状活性炭素を加熱再
生すると粒子の硬度が著しく小さくなる、あるいは吸着
力の回復が不充分であるなとの問題があることがわかっ
た。
無機物質系接着剤では、何機物質系接着剤で生じた上記
の問題点はないが、成型が難しい、あるいは接着剤を多
く添加しないと成型が出来ないなと検討課題がある。
本研究では成型性を改善するた1めの添加物質を探索し
て、無機物質系接着剤による廃粉末活性炭素の成型を検
討した。
その結果、添加物質としてはベントナイト、無機物質系
接着剤としていわゆるセメント系のケイ酸塩化合物を用
いて廃粉末活性炭素を成型することが出来た。
また成型品を種々の温度で焼成し、焼成品の吸着力を測
定した。その結果300°C以ヒの温度で焼成すれば吸
着力は大部分回復することがわかった。
ベントナイトおよびケイ酸塩化合物は安価な物質であり
、また再生処理も、5−00”C以上での短時間焼成で
あるので以上の製造方法で作られる粒状活性炭素は経済
的である。
実施例
廃粉末活性炭素、ベントナイトおよびケイ酸塩化合物を
乙0:/S:25(乾燥重量)の割合でよく混合し、こ
れに70の比で水を加え、混合した。混合物を直径/m
mの球状に成型した。球状物を乾燥後700’C,30
分間加熱して球状活性炭素を得た。この球状活性炭素の
諸性能は表2の通りであった。
表2 球状活性炭素の諸性能
カラメル脱色力はJIS K 1470−1967
に従って測定した。また硬度は粒子7個が破壊される圧
力で20粒子の平均値である。
特許出願人 中島化学産業株式会社
中 島 俊 之Table 1 shows the physical properties of the waste activated carbon powder, and the items were measured according to JISKI470-1967. In addition, the ash content in the item is the residue when the solid content is taken as 100. Procedural amendments S. 70, 1982 1, Case description 1982 Patent No. 214830 2
, Hatsuro's name: 3. Relationship with the case of the person making the amendment Patent applicant 4, date of amendment order 9, 1980 5, drawings and specification subject to amendment 6, statement of contents of amendment 1, name of invention: waste powder activated carbon A method for producing granular activated carbon as a raw material. 2. Claims Waste powder activated carbon, bentonite and inorganic adhesive
The mixture was well mixed in the ratio of IO~70:5~30:10~50 and then fired (temperature = s o o”c
A manufacturing method for producing granular activated carbon by the above). 3. Detailed Description of the Invention Currently, around 50,000 tons of powdered activated carbon is used annually, mainly in the food industry. Unlike waste granular activated carbon, used waste activated carbon powder is difficult to regenerate, and most of it is disposed of in landfills. Recently, it has become increasingly difficult to secure land for landfills, and post-treatment of waste activated carbon powder has become an issue. As shown in Table 1, the adsorption power of the waste activated carbon powder remains considerable, and the regeneration itself to restore the adsorption power is relatively easy, but normally open activated carbon contains more than 50% water. When performing heat regeneration, a large amount of water vapor is generated, which scatters fine activated carbon powder, making it difficult to regenerate large quantities on a commercial basis. Table 1 Physical properties of waste activated carbon powder 1) Measured according to JIS K 1470-1967. 2) Residue with solids content as /DO. Therefore, in order to prevent the scattering during heating, which is a problem when recycling waste activated carbon powder, we granulated waste activated carbon powder to make the recycling process easier, and we also investigated a method for manufacturing inexpensive granular activated carbon. Various adhesives were added to waste powdered activated carbon, granulated, and fired, and the performance of the resulting granular activated carbon was measured to search for an adhesive that can produce high-performance, inexpensive granular activated carbon. It has been found that organic adhesives have problems in that when the obtained granular activated carbon is heated and regenerated, the hardness of the particles becomes extremely small, or the recovery of adsorption power is insufficient. Inorganic adhesives do not have the above-mentioned problems that occur with organic adhesives, but there are issues to consider such as difficulty in molding or the inability to mold without adding a large amount of adhesive. In this study, we searched for additives to improve moldability and investigated the molding of waste activated carbon powder using an inorganic adhesive. As a result, it was possible to mold waste activated carbon powder using bentonite as an additive and a so-called cement-based silicate compound as an inorganic adhesive. In addition, the molded products were fired at various temperatures and the adsorption force of the fired products was measured. As a result, it was found that most of the adsorption power was recovered by firing at a temperature of 300°C or higher. Bentonite and silicate compounds are inexpensive materials, and the regeneration process involves short-time firing at temperatures above 5-00"C, so the granular activated carbon produced by the above production method is economical. Examples Waste powder activated carbon, bentonite and silicate compound were mixed well in a ratio of 0:/S:25 (dry weight), and water was added and mixed in a ratio of 70.The mixture was mixed in a diameter/m
It was molded into a spherical shape of m. After drying the spheres, 700'C, 30
After heating for a minute, spherical activated carbon was obtained. The various performances of this spherical activated carbon were as shown in Table 2. Table 2 Performance of spherical activated carbon Caramel decolorizing power is JIS K 1470-1967
Measured according to Moreover, the hardness is the average value of 20 particles at the pressure at which 7 particles are destroyed. Patent applicant: Toshiyuki Nakajima, Nakajima Chemical Industry Co., Ltd.
Claims (1)
O〜70:5〜30 : 70〜50の割合によく混合
したものを成型し、次いで焼成(温度=500℃以上)
することにより粒状活性炭素を製造する製法。A mixture of waste activated carbon powder, bentonite, and inorganic adhesive in a ratio of 70:5 to 30:70 to 50 is molded and then fired (temperature = 500°C or higher).
A manufacturing method for producing granular activated carbon by
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56214830A JPS58110412A (en) | 1981-12-24 | 1981-12-24 | Manufacture of granular activated carbon from waste powdered activated carbon as starting material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56214830A JPS58110412A (en) | 1981-12-24 | 1981-12-24 | Manufacture of granular activated carbon from waste powdered activated carbon as starting material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58110412A true JPS58110412A (en) | 1983-07-01 |
Family
ID=16662239
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56214830A Pending JPS58110412A (en) | 1981-12-24 | 1981-12-24 | Manufacture of granular activated carbon from waste powdered activated carbon as starting material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58110412A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0278061A2 (en) * | 1987-02-11 | 1988-08-17 | Degussa Aktiengesellschaft | Active carbon granulates and process for their preparation |
KR20030055354A (en) * | 2001-12-21 | 2003-07-04 | 전보술 | Manufacturing method of multifunctional carbon molding |
US8329035B2 (en) * | 2007-12-19 | 2012-12-11 | Saudi Arabian Oil Company | Suspended media granular activated carbon membrane biological reactor system and process |
US8440074B2 (en) | 2009-07-08 | 2013-05-14 | Saudi Arabian Oil Company | Wastewater treatment system including irradiation of primary solids |
US8551341B2 (en) | 2009-06-15 | 2013-10-08 | Saudi Arabian Oil Company | Suspended media membrane biological reactor system including suspension system and multiple biological reactor zones |
US8557111B2 (en) | 2009-07-08 | 2013-10-15 | Saudi Arabian Oil Company | Low concentration wastewater treatment system |
CN108479699A (en) * | 2018-04-11 | 2018-09-04 | 承德鑫永晟炭业有限公司 | A kind of preparation method of absorption oil gas complex spherical activated carbon |
CN108584953A (en) * | 2018-06-07 | 2018-09-28 | 李子臻 | A kind of method and apparatus that the regeneration of Industry Waste carbon dust prepares activated carbon |
-
1981
- 1981-12-24 JP JP56214830A patent/JPS58110412A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0278061A2 (en) * | 1987-02-11 | 1988-08-17 | Degussa Aktiengesellschaft | Active carbon granulates and process for their preparation |
KR20030055354A (en) * | 2001-12-21 | 2003-07-04 | 전보술 | Manufacturing method of multifunctional carbon molding |
US8329035B2 (en) * | 2007-12-19 | 2012-12-11 | Saudi Arabian Oil Company | Suspended media granular activated carbon membrane biological reactor system and process |
US8551341B2 (en) | 2009-06-15 | 2013-10-08 | Saudi Arabian Oil Company | Suspended media membrane biological reactor system including suspension system and multiple biological reactor zones |
US8440074B2 (en) | 2009-07-08 | 2013-05-14 | Saudi Arabian Oil Company | Wastewater treatment system including irradiation of primary solids |
US8557111B2 (en) | 2009-07-08 | 2013-10-15 | Saudi Arabian Oil Company | Low concentration wastewater treatment system |
US8721889B2 (en) | 2009-07-08 | 2014-05-13 | Saudi Arabian Oil Company | Wastewater treatment process including irradiation of primary solids |
US9073764B2 (en) | 2009-07-08 | 2015-07-07 | Saudi Arabian Oil Company | Low concentration wastewater treatment system and process |
US9290399B2 (en) | 2009-07-08 | 2016-03-22 | Saudi Arabian Oil Company | Wastewater treatment process including irradiation of primary solids |
US9340441B2 (en) | 2009-07-08 | 2016-05-17 | Saudi Arabian Oil Company | Wastewater treatment system including irradiation of primary solids |
CN108479699A (en) * | 2018-04-11 | 2018-09-04 | 承德鑫永晟炭业有限公司 | A kind of preparation method of absorption oil gas complex spherical activated carbon |
CN108584953A (en) * | 2018-06-07 | 2018-09-28 | 李子臻 | A kind of method and apparatus that the regeneration of Industry Waste carbon dust prepares activated carbon |
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