JP3655002B2 - Adsorbent and method for producing adsorbent - Google Patents
Adsorbent and method for producing adsorbent Download PDFInfo
- Publication number
- JP3655002B2 JP3655002B2 JP08940896A JP8940896A JP3655002B2 JP 3655002 B2 JP3655002 B2 JP 3655002B2 JP 08940896 A JP08940896 A JP 08940896A JP 8940896 A JP8940896 A JP 8940896A JP 3655002 B2 JP3655002 B2 JP 3655002B2
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- JP
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- Prior art keywords
- adsorbent
- wood
- heating
- hours
- charcoal
- 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.)
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Description
【0001】
【発明の属する技術分野】
本発明は、吸着剤に関し、特に環境保護のために、汚染物質が環境に放出されるのを防止したり、また汚染物質を環境から除去したりするのに用いるのに好適な吸着剤及びその吸着剤の製造方法に関する。
【0002】
【従来の技術】
今日の産業社会にあっては多種多様な汚染物質が環境に放出され、またその可能性を残している。それ故、限りある地球環境を維持して行くためには、汚染物質の特性や発生態様などに応じて、汚染物質の環境への放出を効果的に防止し、また環境に放出された汚染物質を環境から効果的に除去するための技術を確立することが早急な課題となっている。
【0003】
【発明が解決しようとする課題】
本発明は、上記のような課題に応える技術の一つとして汚染物質を吸着により処理するのに用いる吸着剤、特に間伐材などの木材資源を有効に利用でき、しかも比較的低コストでの製造を可能とする吸着剤とその吸着剤の製造方法の提供を目的としている。
【0004】
【課題を解決するための手段】
本発明による吸着剤は、木材を熱変換させて得る。より好ましくは、木材を一般的に用いられている木炭焼成条件で一旦木炭とした後、あらためてこの木炭を熱変換させて得る。具体的には、先ず木材を例えば600〜700℃で焼成して木炭とする。それからこの木炭をあらためて800〜2000℃で2〜5時間、例えば窒素ガスなどを不活性ガスの雰囲気下で加熱することにより熱変換させて得る。このように木材を一旦木炭とするのは、熱変換のための加熱条件の管理を行ない易くするためである。すなわちこのように木材を一旦木炭とすることにより、木材を直接に熱変換させる場合に生じる可能性のある暴走的な自己燃焼をなくすことができ、熱変換のための加熱条件の管理が行ない易くなる。そして加熱条件をより厳密に管理することにより、吸着能の安定性により優れた吸着剤とすることができる。
【0005】
このようにして得られる吸着剤は、木材が本来的に持つ多孔質性が上記のような特定の加熱条件により特異的に熱変換させられており、例えば洗浄剤などとして広く用いられているイソプロピルアルコールやメチルアルコールあるいはエチルアルコールなどのアルコール類に対し高い吸着能力を持つ。その吸着能力は、活性炭に比べれば劣るものの、通常の木炭との比較では、例えばイソプロピルアルコールを例にとると、加熱温度を800〜1000℃とするのが最も好ましく、初期濃度が10000ppmの場合に、通常の木炭の吸着濃度が4000ppm程度であるのに対し8000〜9000ppm程度と2倍乃至これを超えるようになり、実用的に求められる吸着能を十分に満足させることができる。
【0006】
このような特性は上記のような加熱条件において効率的に出現させることができる。すなわち加熱温度が800℃以下であったり、加熱時間が2時間以下であると、通常の木炭における吸着能力との相違はほとんどないが、800℃以上の加熱温度条件の下で2時間以上加熱することにより、後述のような各種の汚染物質に対し特異的に発揮される吸着能力を急激に高めることができる。一方、加熱温度を2000℃以上にしたり、加熱時間を5時間以上にしても吸着能の向上は実質的に見られない。したがって上記のような加熱条件とすることで、実用的な吸着能を十分に満足させる吸着剤を活性炭などに比べ低コストで得ることが可能となる。
【0007】
本発明による吸着剤で処理可能な汚染物質には、空気中への放出が問題になるものとして、例えば工業用の洗浄剤などとして広く用いられているアルコール類、それに排気ガスに含まれるNOxやSOx、また水中への放出が問題になるものとして、生体に有害な重金属類、それに農薬や洗剤などに含まれる難分解性の有機高分子などを主なものとして挙げることができる。
【0008】
【実施の形態】
本発明を好ましい形態で実施するには、木材を600〜700℃で焼成して得られる黒炭を原料とする。そしてこの黒炭を、例えば円筒状の加熱炉中を緩やかに下降させながら所定温度に保って所定時間加熱する。またこの加熱の際しては加熱炉に例えば窒素ガスなどの不活性ガスを供給するようにする。
【0009】
【実施例】
一つの実施例では、杉の黒炭を原料として、加熱温度を800℃、900℃、及び1000℃とし、それぞれについて3時間加熱した。これにより得られた吸着剤のイソプロピルアルコールに対する吸着能力は、初期濃度10000ppmの条件で、加熱温度800℃の吸着剤では、約8000ppmであり、加熱温度900℃の吸着剤では、約8500ppmであり、加熱温度1000℃の吸着剤では、約9000ppmであった。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to adsorbents, especially for environmental protection, or to prevent the contaminants are released into the environment, also suitable adsorbents for use contaminants to or removed from the environment and The present invention relates to a method for producing an adsorbent .
[0002]
[Prior art]
In today's industrial society, a wide variety of pollutants are released into the environment and remain possible. Therefore, in order to maintain a limited global environment, it is possible to effectively prevent the release of pollutants into the environment, and the pollutants released to the environment, depending on the characteristics and generation mode of the pollutants. It is an urgent issue to establish a technology for effectively removing the odor from the environment.
[0003]
[Problems to be solved by the invention]
The present invention can effectively use wood resources such as adsorbents, particularly thinned wood, which are used to treat pollutants by adsorption as one of the technologies that meet the above-mentioned problems, and can be manufactured at a relatively low cost. It is an object of the present invention to provide an adsorbent that can be used and a method for producing the adsorbent .
[0004]
[Means for Solving the Problems]
The adsorbent according to the present invention is obtained by thermally converting wood. More preferably, wood is once converted into charcoal under generally used charcoal firing conditions, and then this charcoal is again thermally converted. Specifically, first, wood is fired at, for example, 600 to 700 ° C. to obtain charcoal. Then, the charcoal is reheated at 800 to 2000 ° C. for 2 to 5 hours, for example, by heating nitrogen gas or the like in an inert gas atmosphere. The reason why wood is once used as charcoal is to facilitate management of heating conditions for heat conversion. In other words, once the wood is made into charcoal, runaway self-combustion that may occur when wood is directly converted to heat can be eliminated, and the heating conditions for heat conversion can be easily managed. Become. And it can be set as the adsorbent which was more excellent by stability of adsorption capacity by managing heating conditions more strictly.
[0005]
The adsorbent obtained in this way has the inherent porosity of wood that is specifically heat-converted under the specific heating conditions as described above. For example, isopropyl is widely used as a cleaning agent. High adsorption capacity for alcohols such as alcohol, methyl alcohol and ethyl alcohol. Although its adsorption capacity is inferior to activated carbon, in comparison with ordinary charcoal, for example, taking isopropyl alcohol as an example, the heating temperature is most preferably 800 to 1000 ° C., and the initial concentration is 10,000 ppm. The adsorption concentration of ordinary charcoal is about 4000 ppm, and is about 8000 to 9000 ppm, which is twice or more, and can sufficiently satisfy the practically required adsorption capacity.
[0006]
Such characteristics can be efficiently exhibited under the above heating conditions. That is, when the heating temperature is 800 ° C. or less or the heating time is 2 hours or less, there is almost no difference from the adsorption ability in normal charcoal, but heating is performed for 2 hours or more under a heating temperature condition of 800 ° C. or more. As a result, the adsorption ability that is specifically exhibited for various contaminants as described later can be rapidly increased. On the other hand, even if the heating temperature is set to 2000 ° C. or higher, or the heating time is set to 5 hours or longer, substantially no improvement in adsorption capacity is observed. Therefore, by using the heating conditions as described above, it is possible to obtain an adsorbent that sufficiently satisfies the practical adsorption ability at a lower cost than activated carbon or the like.
[0007]
Contaminants that can be treated with the adsorbent according to the present invention are subject to release into the air, such as alcohols widely used as industrial cleaners, NOx contained in exhaust gas, Examples of SOx and substances that cause release into water are heavy metals that are harmful to living organisms, and persistent organic polymers contained in agricultural chemicals and detergents.
[0008]
Embodiment
In order to implement the present invention in a preferred form, black coal obtained by firing wood at 600 to 700 ° C. is used as a raw material. The black charcoal is heated for a predetermined time while maintaining a predetermined temperature while slowly descending, for example, in a cylindrical heating furnace. In this heating, an inert gas such as nitrogen gas is supplied to the heating furnace.
[0009]
【Example】
In one example, cedar black charcoal was used as a raw material, and the heating temperatures were 800 ° C., 900 ° C., and 1000 ° C., and each was heated for 3 hours. The adsorption capacity of the adsorbent thus obtained for isopropyl alcohol is about 8000 ppm for an adsorbent with a heating temperature of 800 ° C. and about 8500 ppm for an adsorbent with a heating temperature of 900 ° C. For an adsorbent with a heating temperature of 1000 ° C., it was about 9000 ppm.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP08940896A JP3655002B2 (en) | 1996-04-11 | 1996-04-11 | Adsorbent and method for producing adsorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP08940896A JP3655002B2 (en) | 1996-04-11 | 1996-04-11 | Adsorbent and method for producing adsorbent |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09276693A JPH09276693A (en) | 1997-10-28 |
JP3655002B2 true JP3655002B2 (en) | 2005-06-02 |
Family
ID=13969827
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP08940896A Expired - Fee Related JP3655002B2 (en) | 1996-04-11 | 1996-04-11 | Adsorbent and method for producing adsorbent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3655002B2 (en) |
-
1996
- 1996-04-11 JP JP08940896A patent/JP3655002B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH09276693A (en) | 1997-10-28 |
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