JPS60225639A - Activated carbon-inorganic sintered body molded adsorbent - Google Patents
Activated carbon-inorganic sintered body molded adsorbentInfo
- Publication number
- JPS60225639A JPS60225639A JP59083261A JP8326184A JPS60225639A JP S60225639 A JPS60225639 A JP S60225639A JP 59083261 A JP59083261 A JP 59083261A JP 8326184 A JP8326184 A JP 8326184A JP S60225639 A JPS60225639 A JP S60225639A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- powder
- sintered body
- water
- inorg
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は活性炭粉末に適当な無機質を混合し。[Detailed description of the invention] In the present invention, activated carbon powder is mixed with a suitable inorganic substance.
これを任意の形状に成形し乾燥したのら、これを120
0℃以下の温度で無機質を焼結してなる活性炭−無機質
焼結体吸着剤成形物に関する。After molding this into any shape and drying it,
The present invention relates to an activated carbon-inorganic sintered adsorbent molded product obtained by sintering an inorganic material at a temperature of 0° C. or lower.
活性炭は炭素系の代表的な吸着剤であり5有害ガスの吸
着除去、水中に溶存する有機物質の除去等に広く使用さ
れている。活性炭は本質的に非極性表面を保有すること
から、非極性物質、すなわちいわゆる有機物質の除去に
効果的である。Activated carbon is a typical carbon-based adsorbent and is widely used for the adsorption and removal of five harmful gases and the removal of organic substances dissolved in water. Activated carbon has an essentially non-polar surface and is therefore effective in removing non-polar substances, ie so-called organic substances.
一方、粘土鉱物シリカおよびシリカアルミナなどに代表
される無機質は極性表面を有し、極性物質すなわら水あ
るいは分子の末端に極性基を有する低級有機物質の除去
に有効である。しかしながらこれらの無機質の中には、
活性炭のように広い比表面積を有する物質が少なく、シ
リカゲル、シリカアルミナ、ゼオライト、および活性ア
ルミナなどを除くと、比表面積は小さい、ところがこれ
らの無機質に、活性炭を添加して混合、成形、乾燥およ
び焼結させて得られた焼結体は、無機質が焼結してしま
うことにより無機質自身の表面積はほとんど期待できな
いにもかかわらず、焼結体全体としての表面積は、それ
ほど小さくならない。On the other hand, inorganic substances such as clay minerals silica and silica alumina have polar surfaces and are effective in removing polar substances, such as water or lower organic substances having polar groups at the terminals of their molecules. However, some of these minerals are
There are few substances with a wide specific surface area like activated carbon, and with the exception of silica gel, silica alumina, zeolite, and activated alumina, the specific surface area is small. In the sintered body obtained by sintering, the surface area of the sintered body as a whole does not become so small, although the inorganic substance itself is hardly expected to have a surface area because the inorganic substance is sintered.
これは本発明の大きな特徴である。ずなわら、成形物の
構造体を形成させるために添加した無機質は、活性炭粒
子の表面極性とは反対の極性的性質を示すため、活性炭
粒子とは直接接合することなく1粒子との境界面を保ち
ながら焼結し、その結果、無機質単独の焼結体では得る
ことのできない比較的高い比表面積値を示すものと思わ
れる。This is a major feature of the present invention. However, since the inorganic substance added to form the structure of the molded product exhibits polarity opposite to the surface polarity of the activated carbon particles, it does not bond directly to the activated carbon particles but rather forms at the interface with one particle. As a result, it is thought that it exhibits a relatively high specific surface area value that cannot be obtained with a sintered body made of an inorganic substance alone.
吸着能力の観点からこの焼結体吸着剤を見れば。If we look at this sintered adsorbent from the perspective of adsorption capacity.
極性物質は無機質焼結部に、また非極性物質は活性炭部
に吸着されることになり、各々単独の吸着剤では得られ
ない特徴ある吸着能力を示す。Polar substances are adsorbed on the inorganic sintered part, and non-polar substances are adsorbed on the activated carbon part, each exhibiting a characteristic adsorption ability that cannot be obtained with a single adsorbent.
本発明に用いる活性炭ば、市販の扮未炭あるいは粒状炭
の微細なカスなら、いずれを用いても良い。また無機質
としてはカオリンやモンモリロナイト鉱物に代表される
粘土鉱物、ガラス粉、無定形シリカ、シリカアルミナ粉
などのほか、金属粉や金属酸化物のうら、1200℃以
下で焼結可能な物質を用いれば良い。モンモリロナイト
系の粘土は、800℃以上の加熱処理を行うと焼結構造
物ができないので注意が必要である。1200℃以上の
加熱処理を行うと、活性炭の細孔構造が変化し、比表面
積が低下する。理想的には活性炭の細孔構造に変化を来
さない1100℃以下が望ましく、この場合においても
、長時間の保持は避けた方が良い。すなわち無機物が焼
結し得る温度と時間を、各々の無機質に応じて選定する
ことが必要である。The activated carbon used in the present invention may be any fine dregs of commercially available uncharcoal or granular carbon. In addition, inorganic materials include clay minerals such as kaolin and montmorillonite minerals, glass powder, amorphous silica, silica-alumina powder, metal powders, metal oxides, and substances that can be sintered at temperatures below 1200℃. good. If montmorillonite clay is heated to 800° C. or higher, a sintered structure will not be formed, so care must be taken. When heat treatment is performed at 1200° C. or higher, the pore structure of activated carbon changes and the specific surface area decreases. Ideally, the temperature is preferably 1100° C. or lower, which does not cause any change in the pore structure of the activated carbon, and even in this case, it is better to avoid holding it for a long time. In other words, it is necessary to select the temperature and time at which the inorganic substance can be sintered, depending on each inorganic substance.
粘土鉱物やシリカあるいはシリカアルミナゾルを無機質
として用いる場合は、それ自均の粘着性によって成形物
を作ることが可能であるが、その他の粘着力のない無機
質を用いる場合は、成形物の形を保つために接着剤を添
加する必要がある。接着剤としては、水溶性のデキスト
リン、メチルセルロース、カルボキシメチルセルロース
、などのセルロース系の接着剤、ポリビニルアルコール
などのビニル系接着剤、あるいは酢酸ビニル樹脂あるい
はその誘導体や、ポリビニリデンクロライドあるいはそ
の誘導体などの水とのエマルジョンを用いることができ
る。これらの接着剤は、ポリビニリデンクロライドを除
いてその大半は、加熱処理過程で熱分解、ガス化して焼
結体内部に残留しない。ポリビニリデンクロライドは加
熱処理によって焼結体内に一部残留するが、この残留物
はそれ自体が活性炭と同様に炭素系多孔質材料となるの
で問題ない。When clay minerals, silica, or silica alumina sol are used as the inorganic material, it is possible to make molded products due to their own adhesive properties, but when using other non-adhesive minerals, the shape of the molded product can be maintained. It is necessary to add adhesive for this purpose. Adhesives include water-soluble dextrin, cellulose adhesives such as methyl cellulose and carboxymethyl cellulose, vinyl adhesives such as polyvinyl alcohol, water-soluble adhesives such as vinyl acetate resin or its derivatives, and polyvinylidene chloride or its derivatives. An emulsion can be used. Most of these adhesives, except for polyvinylidene chloride, are thermally decomposed and gasified during the heat treatment process and do not remain inside the sintered body. Although some polyvinylidene chloride remains in the sintered body due to the heat treatment, this residue itself becomes a carbon-based porous material similar to activated carbon, so there is no problem.
このようにして得られた焼結体は、活性炭と同じように
有機物質の吸着除去に効果があるばかりか活性炭のめで
は吸着除去できない極性無機物質あるいは低級の極性有
機物質の除去に効果がある。The sintered body obtained in this way is not only effective in adsorbing and removing organic substances like activated carbon, but also effective in removing polar inorganic substances and lower polar organic substances that cannot be adsorbed and removed by activated carbon. .
また焼結体自身がある程度の4電性を示すことがら、こ
の成形焼結体の両端に一定の電圧をかけることにより、
焼結体が自己発熱し、吸着した分子が脱離し、再生が可
能である。ガス吸着用に用いた場合は、はぼ100%の
再生が可能で、水溶液系の吸着に用いた場合でも、電圧
を制御するごとにより、かなりの比率で再生が可能であ
る。ただし電圧をかけすぎると、焼結体の発熱度が過度
になり、活性炭自体が酸化燃焼し、無機質のみしか残留
しないので1両側にかける電圧は焼結体温度が400°
Cを越えない程度が好ましい。もちろん通常の活性炭の
再生に用いられる方法でも再生可能である。Furthermore, since the sintered body itself exhibits a certain degree of tetraelectricity, by applying a constant voltage to both ends of this shaped sintered body,
The sintered body self-heats, the adsorbed molecules are desorbed, and regeneration is possible. When used for gas adsorption, almost 100% regeneration is possible, and even when used for adsorption of an aqueous solution, regeneration is possible at a considerable rate each time the voltage is controlled. However, if too much voltage is applied, the heat generation of the sintered body becomes excessive, and the activated carbon itself oxidizes and burns, leaving only inorganic matter.
It is preferable that it does not exceed C. Of course, it is also possible to regenerate by the method used for regenerating normal activated carbon.
以下に実施例を示す。Examples are shown below.
実施例1
沼田粘土 40重量部
活性炭粉末(ダイアホープ、100メソ60〃シユ バ
ス)三菱化成工業■
ポリエチレングリコール IO〃
上記配合物に50重量部の水を添加し、ニーダ−8三段
ロールにて混練後、水分量30%で室温で3璽璽φ10
0鶴長の円柱状に成形した。これを100℃で1日乾燥
したのち、1100℃の不活性雰囲気で焼成した。得ら
れた焼結体の比表面積(S、A、)は900イ/gで、
相対圧0.1における25℃でのベンゼン吸着量は30
重量%であった。Example 1 Numata clay 40 parts by weight Activated carbon powder (Diahope, 100 Meso 60〃Bas) Mitsubishi Chemical Corporation■ Polyethylene glycol IO〃 50 parts by weight of water was added to the above mixture and kneaded with a kneader 8 three-stage roll. After that, 3 seals φ10 at room temperature with a moisture content of 30%.
It was molded into a cylindrical shape with a length of 0. After drying this at 100°C for one day, it was fired at 1100°C in an inert atmosphere. The specific surface area (S, A,) of the obtained sintered body was 900 i/g,
The amount of benzene adsorbed at 25°C at a relative pressure of 0.1 is 30
% by weight.
実施例2
ガラス粉 30重量部
活性炭粉末(シラサギ 成田薬品)70〃125° F
パラフィンワックス 20〃カルボキシメチルセルロー
ス 3 〃
上記配合物に50M量部の水を添加し、ニーダ−2三段
ロールで混練後、水分量30%で50℃で2.5鶴φ1
00mm長に押出成形した。得られた成形物を】00°
Cで2日乾燥したのち600°Cの不活性雰囲気で焼成
した。得られた焼結体のS、A、は950m/g、25
°C相対圧0.1におけるベンゼン吸着量は35重量%
であった。Example 2 Glass powder 30 parts by weight Activated carbon powder (Shirasagi Narita Pharmaceutical) 70〃125°F
Paraffin wax 20〃Carboxymethylcellulose 3〃 50M parts of water was added to the above mixture, and after kneading with a kneader 2 three-stage roll, 2.5 cranes φ1 were heated at 50°C with a water content of 30%.
It was extruded to a length of 00 mm. The obtained molded product is 】00°
After drying at C for 2 days, it was fired at 600°C in an inert atmosphere. S and A of the obtained sintered body are 950 m/g, 25
The amount of benzene adsorbed at °C relative pressure of 0.1 is 35% by weight.
Met.
実施例3
シリカゾル(触媒化成工業(41) 100重量部(シ
リカ分30%)
活性炭粉末 60重情部
(ダイアソーブ 三菱化成工業(掬)
酢酸ビニル樹脂エマルジョン 10〃
125° Fパラフィンワックス 10〃上記配合物に
50重量部の水を加えニーダ−1三段ロールで混練後1
分子量3wt%で100℃にて3鶴の四角柱状に100
nの長さで成形した。Example 3 Silica sol (Catalyst Kasei Kogyo (41)) 100 parts by weight (silica content 30%) Activated carbon powder 60 parts by weight (Diasorb Mitsubishi Chemical Industries (Kikki)) Vinyl acetate resin emulsion 10〃 125°F Paraffin wax 10〃The above formulation Add 50 parts by weight of water and knead with three rolls of kneader 1.
At 100℃ with a molecular weight of 3 wt%, it is
It was molded with a length of n.
得られた成形物を90℃、2日加熱処理後1000℃の
不活性雰囲気で焼成した。得られた焼結体のS、A、は
1000rrr/g、25℃相対圧0゜1におけるベン
ゼン吸着量は38%であった。The obtained molded product was heat treated at 90°C for 2 days and then fired at 1000°C in an inert atmosphere. The S and A of the obtained sintered body were 1000 rrr/g, and the amount of benzene adsorbed at 25° C. and a relative pressure of 0°1 was 38%.
実施例4
シリカアルミナ粉(天然ゼオライト粉)40重量部活性
炭粉末 60〃
(ダイアホープ 三菱化成工業@)
デキストリン 10〃
ポリエチレングリコール 10〃
上記配合物に50重量部の水を加え、実施例1と同様に
混合、成形、乾燥し、焼結体を得た。Example 4 Silica alumina powder (natural zeolite powder) 40 parts by weight Activated carbon powder 60〃 (Diahope Mitsubishi Chemical Industries @) Dextrin 10〃 Polyethylene glycol 10〃 50 parts by weight of water was added to the above mixture, and the same procedure as in Example 1 was carried out. The mixture was mixed, molded, and dried to obtain a sintered body.
得られた焼結体のS、A、は900r//g、ベンセン
吸着量は35重量%であった。The S and A of the obtained sintered body were 900 r//g, and the benzene adsorption amount was 35% by weight.
実施例5
銅粉末(100メソシユ、パス) 30M量部活性炭粉
末 70〃
(ダイアホープ 三菱化成工業0瀞)
メチルセルロース 5 〃
125° Fパラフィンワックス 20〃上記配合物を
実施例2と同様に調製し焼結体を得た。得られた焼結体
のS、A、は850m/gヘンゼン吸着量は30重量%
、水中におけるメチレンブルー吸着能力は、20重量%
であった。Example 5 Copper powder (100 mesoyu, pass) 30M parts Activated carbon powder 70〃 (Diahope, Mitsubishi Chemical Industries, Ltd. 0) Methyl cellulose 5〃 125°F paraffin wax 20〃The above mixture was prepared in the same manner as in Example 2 and sintered. I got a body. The S, A, of the obtained sintered body was 850 m/g, and the Hensen adsorption amount was 30% by weight.
, methylene blue adsorption capacity in water is 20% by weight
Met.
特許出願人 株式会社トンボ鉛筆 代表者 小川浩平patent applicant Tombow Pencil Co., Ltd. Representative Kohei Ogawa
Claims (1)
のうち1200℃以下で焼結可能な無機質を添加し、必
要に応じて成形物の可塑性および接着性を持たせ1作業
性を向上させる目的でデキストリン、メチルセルロース
、カルボキシメチルセフL10−ス、ポリビニルアルコ
ールなどの水溶性接着剤、或いはビニル樹脂およびそれ
らの誘導体5ビニリデンクロライド樹脂およびそれらの
誘導体の水とのエマルジョンなどを添加して、混合、成
形、乾燥および不活性雰囲気で焼成焼結してなる活性炭
−無機質焼結体吸着剤成形物。[Claims] Activated carbon powder, clay, glass powder, and amorphous silica. Inorganic materials such as silica alumina powder, clay, metal powder, or metal oxides that can be sintered at temperatures below 1200℃ are added to give plasticity and adhesiveness to the molded product as necessary, and to improve workability. By adding a water-soluble adhesive such as dextrin, methylcellulose, carboxymethylcephalic acid, polyvinyl alcohol, or an emulsion of vinylidene chloride resin and their derivatives with water, mixing, molding, An activated carbon-inorganic sintered adsorbent molded product obtained by drying and firing and sintering in an inert atmosphere.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59083261A JPS60225639A (en) | 1984-04-25 | 1984-04-25 | Activated carbon-inorganic sintered body molded adsorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59083261A JPS60225639A (en) | 1984-04-25 | 1984-04-25 | Activated carbon-inorganic sintered body molded adsorbent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60225639A true JPS60225639A (en) | 1985-11-09 |
Family
ID=13797401
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59083261A Pending JPS60225639A (en) | 1984-04-25 | 1984-04-25 | Activated carbon-inorganic sintered body molded adsorbent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60225639A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02142437U (en) * | 1989-04-28 | 1990-12-03 | ||
JPH02307527A (en) * | 1989-05-19 | 1990-12-20 | Kobe Steel Ltd | Solvent adsorbing material and solvent recovery apparatus |
JPH05168916A (en) * | 1991-05-08 | 1993-07-02 | Air Prod And Chem Inc | Oxygen and carbon dioxide selective composite drting agent, preparation thereof, and method for adsorptive separation of nitrogen from oxygen |
US5310593A (en) * | 1990-10-31 | 1994-05-10 | Osaka Gas Company Limited | Adsorbent |
KR20030055354A (en) * | 2001-12-21 | 2003-07-04 | 전보술 | Manufacturing method of multifunctional carbon molding |
US6682667B1 (en) | 2002-02-05 | 2004-01-27 | Calgon Carbon Corporation | Method for producing self-supporting activated carbon structures |
KR100895867B1 (en) * | 2007-11-28 | 2009-04-30 | (주)동화라이징 | Method for preparing of porous sintered bodies |
US8691722B2 (en) | 2008-07-03 | 2014-04-08 | Corning Incorporated | Sorbent comprising activated carbon particles, sulfur and metal catalyst |
CN104692377A (en) * | 2015-02-09 | 2015-06-10 | 江西能欣生物科技有限公司 | Production technique of novel wood columnar activated carbon |
WO2017075425A1 (en) * | 2015-10-28 | 2017-05-04 | Rennovia Inc. | Porous shaped metal-carbon products |
US11253839B2 (en) | 2014-04-29 | 2022-02-22 | Archer-Daniels-Midland Company | Shaped porous carbon products |
WO2023092842A1 (en) * | 2021-11-24 | 2023-06-01 | 清华大学 | Molded activated carbon, preparation method therefor and use thereof |
-
1984
- 1984-04-25 JP JP59083261A patent/JPS60225639A/en active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02142437U (en) * | 1989-04-28 | 1990-12-03 | ||
JPH02307527A (en) * | 1989-05-19 | 1990-12-20 | Kobe Steel Ltd | Solvent adsorbing material and solvent recovery apparatus |
US5310593A (en) * | 1990-10-31 | 1994-05-10 | Osaka Gas Company Limited | Adsorbent |
JPH05168916A (en) * | 1991-05-08 | 1993-07-02 | Air Prod And Chem Inc | Oxygen and carbon dioxide selective composite drting agent, preparation thereof, and method for adsorptive separation of nitrogen from oxygen |
KR20030055354A (en) * | 2001-12-21 | 2003-07-04 | 전보술 | Manufacturing method of multifunctional carbon molding |
US6682667B1 (en) | 2002-02-05 | 2004-01-27 | Calgon Carbon Corporation | Method for producing self-supporting activated carbon structures |
KR100895867B1 (en) * | 2007-11-28 | 2009-04-30 | (주)동화라이징 | Method for preparing of porous sintered bodies |
US8691722B2 (en) | 2008-07-03 | 2014-04-08 | Corning Incorporated | Sorbent comprising activated carbon particles, sulfur and metal catalyst |
US11253839B2 (en) | 2014-04-29 | 2022-02-22 | Archer-Daniels-Midland Company | Shaped porous carbon products |
CN104692377A (en) * | 2015-02-09 | 2015-06-10 | 江西能欣生物科技有限公司 | Production technique of novel wood columnar activated carbon |
WO2017075425A1 (en) * | 2015-10-28 | 2017-05-04 | Rennovia Inc. | Porous shaped metal-carbon products |
US10722869B2 (en) | 2015-10-28 | 2020-07-28 | Archer-Daniels-Midland Company | Porous shaped metal-carbon products |
EP3862079A1 (en) * | 2015-10-28 | 2021-08-11 | Archer-Daniels-Midland Company | Porous shaped metal-carbon products |
WO2023092842A1 (en) * | 2021-11-24 | 2023-06-01 | 清华大学 | Molded activated carbon, preparation method therefor and use thereof |
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