JPH061674A - Production of porous carbon material - Google Patents
Production of porous carbon materialInfo
- Publication number
- JPH061674A JPH061674A JP4166160A JP16616092A JPH061674A JP H061674 A JPH061674 A JP H061674A JP 4166160 A JP4166160 A JP 4166160A JP 16616092 A JP16616092 A JP 16616092A JP H061674 A JPH061674 A JP H061674A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- treated
- porous carbon
- carbon material
- heat
- 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
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は多孔質炭素材料の製造方
法に関するものである。さらに詳しくはガス、液体の吸
着炭素材料、電池用炭素材料等に使用される多孔質炭素
材料の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a porous carbon material. More specifically, the present invention relates to a method for producing a porous carbon material used as a gas or liquid adsorbing carbon material, a carbon material for a battery, or the like.
【0002】[0002]
【従来の技術】近年、水質汚染、大気汚染等の環境問題
がクローズアップされ、活性炭等の多孔質炭素材料が益
々注目されてきた。特に飲料水に使用する水質の悪化の
ために細菌、臭気物質、またさらには発癌性を示すとい
われる塩素化合物の除去、また大気汚染の一つであるオ
キシダントの原因、地球環境のオゾン層の破壊の一因で
あると言われている自動車排気ガス中の有機成分の除去
等の公害防止対策の一つとして多孔質炭素材料が使用さ
れている。2. Description of the Related Art In recent years, environmental problems such as water pollution and air pollution have been highlighted, and porous carbon materials such as activated carbon have attracted more and more attention. Removal of bacteria, odorous substances and chlorine compounds, which are said to be carcinogenic due to deterioration of water quality used for drinking water, cause of oxidant which is one of air pollution, and destruction of ozone layer of global environment A porous carbon material is used as one of pollution prevention measures such as removal of organic components in automobile exhaust gas, which is said to be one of the causes.
【0003】従来水質、大気ガス中の汚染物質の吸着除
去に使用される多孔質炭素材料はヤシ殻等の植物の繊維
や石炭等を仮焼後、空気、水蒸気等のガスの存在下で賦
活処理を施して、表面積、気孔量の増加を図り、多孔質
炭素材料の特性を調整しているのが現状である。また、
石油価格の高騰、深夜電力の利用、通信システムの発達
により、一次及び二次電池が急速に見直され、拡大を続
けており、それに応じて電池に使用される炭素材料も注
目されるようになっており、種々の炭素材料、特に多孔
質炭素材料が注目されている。従来電池用炭素材料とし
てはタール系重質油等を熱分解して製造されるカーボン
ブラック等が使用されている。Porous carbon materials conventionally used for adsorption and removal of pollutants in water quality and atmospheric gas are activated in the presence of gas such as air and water vapor after calcination of plant fibers such as coconut shells and coal. Under the present circumstances, treatment is performed to increase the surface area and the amount of pores, and the characteristics of the porous carbon material are adjusted. Also,
With the rise in oil prices, the use of late-night power, and the development of communication systems, primary and secondary batteries have been rapidly reviewed and expanded, and the carbon materials used in batteries have come to attract attention accordingly. Therefore, various carbon materials, especially porous carbon materials, are attracting attention. Conventionally, as a carbon material for a battery, carbon black produced by thermally decomposing tar-based heavy oil or the like has been used.
【0004】[0004]
【発明が解決しようとする課題】しかし、これらの多孔
質高表面積の炭素質粉末はいずれも高温で処理しなけれ
ばならず、場合によっては空気、水蒸気等のガスで賦活
処理をする必要があり、製造コストが高いのが現状であ
った。又空気、水蒸気等のガス中、高温で処理するため
に炭素が燃焼し、歩留りが低い、物性の調整が困難であ
る等の問題があった。また、自動車等に積載するために
小さくて軽く効率の良いものが望まれている。However, all of these porous high surface area carbonaceous powders must be treated at high temperature, and in some cases, activation treatment with a gas such as air or steam is required. The current situation is that the manufacturing cost is high. Further, since carbon is burned in a gas such as air or water vapor at a high temperature, there are problems such as low yield and difficulty in adjusting physical properties. There is also a demand for a small, light and efficient one for loading on an automobile or the like.
【0005】[0005]
【課題を解決するための手段】かかる状況に鑑み、本発
明者等は鋭意検討した結果、ピッチ類又は生コークス類
に特定の無機化合物を添加後、この混合物を熱処理し、
該熱処理生成物を酸で処理すると容易に多孔質炭素材料
が生成することを見出し、本発明の完成に至った。すな
わち、本発明の要旨はピッチ類又は生コークス類に酸に
可溶な無機化合物を添加後、該混合物を熱処理し、次い
で、得られる該熱処理生成物を酸で処理することを特徴
とする多孔質炭素材料の製造方法にある。In view of the above situation, the present inventors have made diligent studies, and as a result, after adding a specific inorganic compound to pitches or raw coke, heat treating this mixture,
It was found that when the heat-treated product is treated with an acid, a porous carbon material is easily produced, and the present invention has been completed. That is, the gist of the present invention is that, after adding an acid-soluble inorganic compound to pitches or raw cokes, heat treating the mixture, and then treating the resulting heat-treated product with an acid. There is a method for producing a high quality carbon material.
【0006】以下本発明を詳細に説明する。まず本発明
に使用されるピッチ類又は生コークス類(以下、「炭素
質原料」という。)としては、コールタールの蒸留、熱
処理により生成するタールピッチ、石油系重質油、およ
びその接触分解油または蒸留残油、それらの水素添加分
解油等の熱処理生成物、またナフタリン等の低分子化合
物を触媒の存在下重縮合したピッチおよび溶剤処理をし
た生成物(以下、これらを「ピッチ類」と総称する)、
及びそれらを原料としてオートクレーブ、ディレードコ
ーカー等で300〜500℃、1〜48時間程度熱処理
して得られる生コークス等が用いられる。The present invention will be described in detail below. First, as pitches or raw cokes (hereinafter referred to as "carbonaceous raw material") used in the present invention, tar pitch produced by distillation of coal tar and heat treatment, petroleum heavy oil, and catalytic cracking oil thereof are used. Or distillation residual oils, heat-treated products such as hydrogenated cracked oils, pitches obtained by polycondensation of low molecular weight compounds such as naphthalene in the presence of a catalyst, and products subjected to solvent treatment (hereinafter, these are referred to as “pitches”). (Collectively),
Also, raw coke or the like obtained by heat-treating them at 300 to 500 ° C. for 1 to 48 hours in an autoclave, a delayed coker or the like is used as a raw material.
【0007】本発明で使用する炭素質原料は、通常30
0℃以下留分が10%以下、好ましくは、360℃以下
留分が10%以下、最も好ましくは360℃以下留分が
1〜5%のものが好適である。酸に可溶な無機化合物と
しては、アルカリ土類金属の化合物が好ましく、たとえ
ば、カルシウム(Ca)、バリウム(Ba)、マグネシ
ウム(Mg)等の塩化物、硫酸塩、炭酸塩、酸化物等が
利用できるが、炭酸塩、酸化物が処理し易く好ましい。
特に酸化物が好ましく、マグネシウム、カルシウムの酸
化物が最も好ましい。The carbonaceous raw material used in the present invention is usually 30
It is suitable that the fraction at 0 ° C or lower is 10% or less, preferably the fraction at 360 ° C or lower is 10% or less, and most preferably the fraction at 360 ° C or lower is 1 to 5%. The acid-soluble inorganic compound is preferably an alkaline earth metal compound, and examples thereof include chlorides such as calcium (Ca), barium (Ba), and magnesium (Mg), sulfates, carbonates, and oxides. Although it can be used, carbonates and oxides are preferable because they are easily treated.
Oxides are particularly preferable, and oxides of magnesium and calcium are most preferable.
【0008】添加量は炭素質原料に対して重量割合で1
/1以上(=無機化合物/炭素質原料)が好ましく、さ
らに好ましくは55/45〜95/5であり、最も好ま
しくは60/40〜90/10である。添加方法として
は炭素質原料と酸に可溶な無機化合物を好ましくは粉体
でブレンドする。また、ピッチ類の場合は、それを加熱
溶融して液体状態にし、それに無機化合物をブレンドす
ることもできる。[0008] The addition amount is 1 by weight ratio to the carbonaceous raw material.
/ 1 or more (= inorganic compound / carbonaceous raw material) is preferable, 55/45 to 95/5 is more preferable, and 60/40 to 90/10 is most preferable. As a method of addition, a carbonaceous raw material and an acid-soluble inorganic compound are preferably blended in the form of powder. Further, in the case of pitches, it is also possible to heat and melt it into a liquid state and blend the inorganic compound with it.
【0009】さらには、炭素質原料を溶媒に分散、また
は溶解して溶媒中で混合することもできるし、生コーク
スを溶媒に分散して混合することもできる。該混合物の
熱処理は150℃以上で0.5〜24時間行うのが好ま
しく、さらには180〜350℃で0.5〜10時間が
好ましく、最も好ましくは200〜300℃で0.5〜
5時間行うのがよい。Further, the carbonaceous raw material may be dispersed or dissolved in a solvent and mixed in the solvent, or raw coke may be dispersed in the solvent and mixed. The heat treatment of the mixture is preferably carried out at 150 ° C. or higher for 0.5 to 24 hours, more preferably at 180 to 350 ° C. for 0.5 to 10 hours, and most preferably at 200 to 300 ° C. for 0.5 to
It is good to do it for 5 hours.
【0010】また、該熱処理物はさらに高温(350〜
1000℃)で焼成することもでき、必要に応じて揮発
分を除去できる。熱処理の際の圧力は、大気圧で通常行
なわれるが、高圧下でも可能である。雰囲気は不活性ガ
ス中、酸素存在下、コークスブリーズ中でも処理できる
が、酸素が存在した方が好ましく、酸素の濃度を5〜5
0%に調整して処理することも可能である。Further, the heat-treated product has a higher temperature (350 to
It can also be baked at 1000 ° C., and the volatile matter can be removed if necessary. The pressure during the heat treatment is usually atmospheric pressure, but it can be performed under high pressure. The atmosphere can be treated in an inert gas, in the presence of oxygen, or in coke breeze, but it is preferable that oxygen is present, and the oxygen concentration is 5 to 5
It is also possible to adjust and process to 0%.
【0011】そのようにして得た処理物は、必要に応じ
て粉砕した後に、塩酸、硫酸等の5〜35%の無機酸、
または酢酸等の5〜50%の有機酸で処理して、該無機
化合物を溶解除去し、生成物を得ることができるが、酸
としては無機酸が溶解力が強く有利である。溶解は室温
下で行っても良いが溶解を促進するために高温(50〜
100℃)で行っても良い。The treated product thus obtained is, if necessary, pulverized and then treated with 5 to 35% of an inorganic acid such as hydrochloric acid or sulfuric acid.
Alternatively, the product can be obtained by treating with 5 to 50% of an organic acid such as acetic acid to dissolve and remove the inorganic compound, but as the acid, the inorganic acid has a strong dissolving power and is advantageous. The dissolution may be carried out at room temperature, but in order to accelerate the dissolution, high temperature (50-
You may perform it at 100 degreeC.
【0012】また、熱処理物と酸を混合してバッチで処
理してもよいが、酸を流通させながら連続的に処理する
こともできる。酸処理して得られる生成物は必要に応じ
て更に焼成、黒鉛化することもできる。このようにして
得られた炭素質材料は、通常粒子の平均粒度が50μm
以下、好ましくは0.1〜30μmであり、表面積が1
00m2/g以上である多孔質炭素粉末、さらには50
0〜2000m2/g以上である多孔質炭素粉末とな
り、水質の浄化、大気ガス中の有害物質の処理等に使用
されるものである。以下、実施例によりさらに本発明を
詳細に説明する。Further, the heat-treated product and the acid may be mixed and treated in a batch, but it is also possible to perform the treatment continuously while circulating the acid. The product obtained by the acid treatment can be further calcined and graphitized if necessary. The carbonaceous material thus obtained usually has an average particle size of 50 μm.
The following is preferably 0.1 to 30 μm and has a surface area of 1
Porous carbon powder having a particle size of 00 m 2 / g or more, and further 50
It becomes a porous carbon powder of 0 to 2000 m 2 / g or more and is used for purification of water quality, treatment of harmful substances in atmospheric gas, and the like. Hereinafter, the present invention will be described in more detail with reference to Examples.
【0013】[0013]
実施例−1 市販の含浸ピッチと市販のマグネシア(MgO)粉末3
0/70(重量比)を粉体の状態で混合後、250℃で
空気中で熱処理を行った。該熱処理物を室温下、濃塩酸
を10倍に希釈した塩酸に1昼夜浸し、その後さらに塩
酸で洗浄後乾燥し生成物を得た。該生成物の平均粒子径
は20μmであり、表面積は700m2/gであった。
生成多孔質炭素質粉末を走査型電子顕微鏡で観察したと
ころ孔の形状はハニカム構造であった。Example-1 Commercial Impregnated Pitch and Commercial Magnesia (MgO) Powder 3
After mixing 0/70 (weight ratio) in a powder state, heat treatment was performed in air at 250 ° C. The heat-treated product was immersed in hydrochloric acid diluted with concentrated hydrochloric acid 10 times at room temperature for one day and then washed with hydrochloric acid and dried to obtain a product. The average particle size of the product was 20 μm and the surface area was 700 m 2 / g.
When the produced porous carbonaceous powder was observed with a scanning electron microscope, the shape of the holes was a honeycomb structure.
【0014】[0014]
【発明の効果】本発明によれば、多孔質高表面積の炭素
質材料を比較的低温で容易に製造でき、物性の調整が容
易で高歩留りとなる。According to the present invention, a porous high surface area carbonaceous material can be easily produced at a relatively low temperature, physical properties can be easily adjusted, and a high yield can be obtained.
Claims (1)
な無機化合物を添加後、この混合物を熱処理し、次い
で、得られる熱処理生成物を酸で処理することを特徴と
する多孔質炭素質材料の製造方法。1. A porous carbonaceous material characterized in that an inorganic compound soluble in an acid is added to pitches or raw coke, and then this mixture is heat-treated, and then the heat-treated product obtained is treated with an acid. Material manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4166160A JPH061674A (en) | 1992-06-24 | 1992-06-24 | Production of porous carbon material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4166160A JPH061674A (en) | 1992-06-24 | 1992-06-24 | Production of porous carbon material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH061674A true JPH061674A (en) | 1994-01-11 |
Family
ID=15826187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4166160A Pending JPH061674A (en) | 1992-06-24 | 1992-06-24 | Production of porous carbon material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH061674A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014122158A (en) * | 2004-07-30 | 2014-07-03 | Toyo Tanso Kk | Activated carbon |
-
1992
- 1992-06-24 JP JP4166160A patent/JPH061674A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014122158A (en) * | 2004-07-30 | 2014-07-03 | Toyo Tanso Kk | Activated carbon |
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