JPH10226508A - Glucomannan activated carbon - Google Patents

Glucomannan activated carbon

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Publication number
JPH10226508A
JPH10226508A JP9030574A JP3057497A JPH10226508A JP H10226508 A JPH10226508 A JP H10226508A JP 9030574 A JP9030574 A JP 9030574A JP 3057497 A JP3057497 A JP 3057497A JP H10226508 A JPH10226508 A JP H10226508A
Authority
JP
Japan
Prior art keywords
glucomannan
activated carbon
mannan
carbon
hydrated gel
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
Application number
JP9030574A
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Japanese (ja)
Other versions
JP3012940B2 (en
Inventor
Nobuhisa Kawano
信久 川野
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Individual
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Individual
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Publication of JPH10226508A publication Critical patent/JPH10226508A/en
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  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a glucomannan activated carbon to supplement the lack of the source material for activated carbon which largely depends on import, by drying a hydrated gel prepared from glucomannan as the main source material, carbonizing the obtd. dry solid and then activating. SOLUTION: Glucomannan, a coagulating agent such as calcium hydroxide, and if necessary, a carbon-contg. material which can be used as a carbon having high porous structure (such as plant-based, natural and synthetic materials) are mixed, to which 5 to 10 pts.wt. of water is added to 1 pt.wt. of the glucomannan. The mixture is stirred and kneaded to obtain a hydrated gel essentially comprising glucomannan. The amt. of water is preferably as small as possible in such a range that the glucomannan particles and the coagulating agent are uniformly and sufficiently in contact with each other in the hydrated gel. The hydrated gel is dried to obtain a dry solid. The dry solid is heated at 600 to 800 deg.C to carbonize and then heated at 850 to 1150 deg.C to activate in an atmosphere containing water vapor, air and combustion gas.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、活性炭、より詳細
にはグルコマンナンを主原料として製造される活性炭に
関する。
[0001] The present invention relates to activated carbon, and more particularly to activated carbon produced using glucomannan as a main raw material.

【0002】[0002]

【従来の技術】サトイモ科の植物であるコンニャク芋
は、その球茎中に多糖類のグルコマンナン(狭義)その
他のマンナン類を含有しており、これらは総括してグル
コンマンナン(広義)と称されており、また市販のこん
にゃく原料であるところからコンニャクマンナン(こん
にゃく精粉)とも呼ばれている。
BACKGROUND OF THE INVENTION Konjac potato, a plant of the taro family, contains the polysaccharide glucomannan (in a narrow sense) and other mannans in its corm, and these are collectively referred to as glucon mannan (in a broad sense). It is also called konjac mannan (konjac fine powder) because it is a commercially available konjac raw material.

【0003】本発明の活性炭の製造方法において使用す
べきグルコマンナンは、必ずしも純品(狭義のグルコマ
ンナン)である必要はなく、コンニャクマンナン(広義
のグルコマンマンナン)を使用することのできることは
もちろんである。そこで、以下の説明では特に必要のな
い限り、狭義および広義のグルコマンナンを特に断らな
い限り一括して単に「マンナン」と略記することがあ
る。
[0003] Glucomannan to be used in the method for producing activated carbon of the present invention is not necessarily a pure product (glucomannan in a narrow sense), and konjac mannan (glucomannan in a broad sense) can of course be used. It is. Thus, in the following description, glucomannan in a narrow sense and a broad sense may be simply abbreviated as "mannan" unless otherwise specified, unless otherwise specified.

【0004】さて、マンナンの水溶液は、Ca(OH)
2などのアルカリ性化合物(凝固剤)に接触するとゲル
化し、その生成した水和ゲルを加温すると不可逆的弾性
ゲルとなり、日本の伝統的な食品である「こんにゃく」
ができることは周知の通りである。より詳しくは、こん
にゃくは、例えば、マンナンを水中攪拌の後、マンナン
粒子を完全に溶解させる(膨潤または粒子の目開きとも
いう)ために凡そ60〜120分間程度放置し、次に凝
固剤を添加して十分に混練してマンナン水和物のゲルと
し、その後成形し、加熱して不可逆的ゲルを得るという
一連の必須工程を経て製造される。マンナンの特性は、
このようにして、例えばこんにゃくを通して食材に活用
されている。
Now, the aqueous solution of mannan is Ca (OH)
When it comes into contact with alkaline compounds (coagulants) such as 2, it gels, and when the resulting hydrated gel is heated, it becomes an irreversible elastic gel, a traditional Japanese food "konjac"
Is well known. More specifically, for example, after stirring mannan in water, konjac is left for about 60 to 120 minutes to completely dissolve the mannan particles (also referred to as swelling or particle opening), and then a coagulant is added. Then, the mixture is thoroughly kneaded to form a gel of mannan hydrate, then molded and heated to obtain an irreversible gel. The characteristics of mannan are:
In this way, konjac is used for foodstuffs.

【0005】しかして、このようなこんにゃくの製造法
においては、マンナンの完全溶解(完全膨潤)および凝
固剤添加後十分に混練するために、マンナンの水溶液の
調製に際して十分量の水を使用しなければならない。す
なわち、マンナン1重量部に対し、使用水は35〜45
重量部が良好な作業域であり、たとえば30重量部以下
では、強力な水和ゲル生成のため、膨潤後にアルカリ剤
を添加して十分に混練することは不可能であり、また他
の食材に添加して均質化することも不可能である。この
ように、凝固剤のマンナン接触が不均質、不十分では、
マンナンの食材利用は、ぬめりやネトをもたらし、更に
強い嫌忌臭が増幅して食用に耐え得るものではない結果
を来すのである。したがって、マンナンの食材利用は今
日においてもなをこんにゃくを超える進展が阻まれてい
る。
However, in such a method for producing konjac, a sufficient amount of water must be used in preparing an aqueous solution of mannan in order to completely dissolve (completely swell) mannan and to knead it sufficiently after adding a coagulant. Must. That is, for 1 part by weight of mannan, the water used is 35-45.
Parts by weight are good working areas. For example, below 30 parts by weight, it is impossible to add an alkali agent and sufficiently knead after swelling due to the formation of a strong hydrated gel. It is not possible to add and homogenize. Thus, if the coagulant mannan contact is heterogeneous or insufficient,
Mannan's use of foodstuffs can result in sliminess and neto, as well as exacerbation of a strong aversion to non-edible products. Therefore, the use of foodstuffs by mannan has been hampered today even more than konjac.

【0006】因みに、マンナンの水和ゲルを、先に説明
したようにこんにゃくの製造時に見られる完全溶解とそ
れに続く凝固剤を添加して十分混練する工程を解消して
製造できるマンナンとしては、本発明者の発明に係わる
即溶解性グルコマンナン組成物(特開平5−3826
3)を好適なものとして挙げることができる。
[0006] Incidentally, as described above, mannan which can be produced by eliminating the complete dissolution seen during the production of konjac and the subsequent step of adding a coagulant and sufficiently kneading the hydrated mannan gel as described above, Rapidly soluble glucomannan composition according to the invention of the inventor (JP-A-5-3826)
3) can be mentioned as a preferable example.

【0007】わが国では、コンニャク芋は畑作農産物と
して栽培されており、それから得られるマンナンは、従
来、唯一こんにゃくの原料として使用され、その優れた
特性を有効活用するには至っていない。その主な原因
は、マンナン1重量部に対し、水40重量部前後もの使
用が、こんにゃく製造の標準プロセスであり、然も、製
品のこんにゃくは強アルカリ性(pH11.0〜13.
0)水溶液中に存在し、食用には特別の手間を必要とす
るなどの弾性に富む凝固物のため、その原料であるマン
ナンは、他の食品や工業用原材料使用への進展が阻まれ
今日に至っている。
[0007] In Japan, konjac potatoes are cultivated as upland agricultural products, and mannan obtained therefrom has conventionally been used only as a raw material for konjac, and its excellent properties have not been effectively utilized. The main reason is that the use of about 40 parts by weight of water with respect to 1 part by weight of mannan is a standard process for the production of konjac, and the konjac of the product is strongly alkaline (pH 11.0-13.
0) Mannan, the raw material, is present in an aqueous solution and has a high elasticity, such as requiring special labor for edible use. Has been reached.

【0008】本発明者は、前記した「即溶解性グルコマ
ンナン組成物」に見るごとく、マンナンの微粉体に副原
料(でんぷん、凝固剤、その他)を粉体混合し、これを
水和撹拌するときは、凝固剤はマンナン水和物中におい
てマンナン粒子と容易に均質かつ十分に接触して平衡状
態に達するので、たとえばマンナン粉体原料1重量部に
対し、必要に応じては水5〜10重量部という少量でも
マンナンの均質な凝固を達することのできるところか
ら、マンナンの特性である水和溶解と水和物の粘度、さ
らに不可逆的凝固は、広範囲の用途利用が可能であると
する知見を得、たとえば、増粘性、乳化性、付着性、粘
着性、被覆性など多目的に利用しようとする研究から、
食品フィルム、冷凍食品、畜肉食品、製菓類、その他食
品補助剤として、また塗料、肥料、農薬、土壌の調整改
良などの工業用に、さらに医療関係のX線透視用のカプ
セル剤の皮殻や薬剤のバインダーなどへの用途開発に鋭
意研究を進めたが、マンナンのさらなる用途開発が望ま
れる。
The inventor of the present invention, as seen in the aforementioned “quickly dissolving glucomannan composition”, mixes powdered auxiliary materials (starch, coagulant, etc.) with fine powder of mannan, and hydrates and mixes these. Sometimes, the coagulant easily and homogeneously and sufficiently contacts the mannan particles in the mannan hydrate to reach an equilibrium state. For example, 1 part by weight of the mannan powder raw material and, if necessary, 5-10 parts of water. The fact that mannan can be homogeneously coagulated even in a small amount of parts by weight means that the hydration dissolution and hydrate viscosity, which are the characteristics of mannan, and the irreversible coagulation can be used in a wide range of applications. From, for example, from research to be used for multipurpose such as thickening, emulsifying, adhesive, sticky, coating,
Food film, frozen food, animal meat food, confectionery, and other food supplements, paints, fertilizers, pesticides, industrial adjustment and improvement of soil, etc., as well as capsule shells for medical X-ray fluoroscopy Despite extensive research into the development of applications for drug binders and the like, further application development of mannan is desired.

【0009】[0009]

【発明が解決しようとする課題】前項記載の従来技術の
背景下に、本発明の目的は、グルコマンナンのさらなる
用途を開発提供することにある。
SUMMARY OF THE INVENTION Under the background of the prior art described in the preceding paragraph, an object of the present invention is to develop and provide further uses of glucomannan.

【0010】[0010]

【課題を解決するための手段】本発明者は、前記記載の
課題を解決すべく鋭意研究の結果、グルコマンナンは、
前記の用途の他にも、活性炭の良好な原料になり得ると
の知見を得、このような知見に基づいて、本発明を完成
した。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, glucomannan
In addition to the above-mentioned uses, the present inventors have found that they can be a good raw material for activated carbon, and have completed the present invention based on such findings.

【0011】すなわち、本発明は、グルコマンナンを主
原料とする水和ゲルを乾燥し、得られた乾燥固形物を炭
化処理し、次いで賦活処理して製造することができるこ
とを特徴とするグルコマンナン活性炭に関する。
[0011] That is, the present invention is characterized in that it can be produced by drying a hydrated gel containing glucomannan as a main raw material, carbonizing the resulting dried solid, and then activating. Regarding activated carbon.

【0012】因みに、本発明の活性炭をグルコマンナン
活性炭と称するのは、その主原料がこのようにグルコマ
ンナンであることによる。
The activated carbon of the present invention is referred to as glucomannan activated carbon because its main raw material is glucomannan.

【0013】[0013]

【発明の実施の形態】以下、本発明を詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.

【0014】活性炭の製法については、「木の粉に塩化
亜鉛溶液を加え浸透させた後、無酸素下で600〜70
0℃に加熱して炭化する。または、木炭や石炭に水蒸気
を吹き込みながら800〜1,200℃で加熱する。」
(日本食品工業学会編「新版食品工業総合事典」P.2
58、(株)光琳平成5年発行)といわれ、また「木
炭、ヤシがら、石炭チャーその他の原料を十分に炭化し
たのち、水蒸気による高温処理あるいは塩化亜鉛などの
水溶液の含浸と高温焼成などの方法で賦活し、製造され
る。」(「化学辞典」P.275、(株)東京化学同人
1994年発行)といわれている。
Regarding the method for producing activated carbon, "a zinc chloride solution is added to wood flour and impregnated, and then 600-70 under anoxic condition.
Heat to 0 ° C and carbonize. Alternatively, heating is performed at 800 to 1,200 ° C. while blowing steam into charcoal or coal. "
(Japanese Society of Food Industry, “New Edition of the Food Industry General Encyclopedia” P.2
58, published by Korin Co., Ltd. in 1993), and "After sufficiently carbonizing charcoal, coconut palm, coal char, and other raw materials, high-temperature treatment with steam or impregnation with an aqueous solution such as zinc chloride and high-temperature sintering, etc. It is activated by a method and is manufactured. "(" Chemistry Dictionary "P. 275, published by Tokyo Chemical Industry Co., Ltd., 1994).

【0015】活性炭は、活性炭の使用目的に従って、そ
の形状から粉末活性炭、粒状活性炭、繊維状活性炭など
に分類され、さらに粒状活性炭は破砕炭と球状、円柱状
などの成形炭とに区別することができる。本発明の活性
炭は、その形状を粒状活性炭、なかでも破砕炭の形状と
することが容易である。
Activated carbon is classified into powdered activated carbon, granular activated carbon, fibrous activated carbon, and the like according to the shape of the activated carbon according to the purpose of use. Further, granular activated carbon can be classified into crushed carbon and spherical or cylindrical shaped carbon. it can. The activated carbon of the present invention can be easily made into granular activated carbon, especially crushed carbon.

【0016】わが国では、粒状活性炭の製造に際しての
賦活処理は、ガス賦活及び薬品賦活の両者が採用され、
このような賦活処理を経て製造された活性炭は、それぞ
れの特性が生かされながら使用されている。しかしなが
ら、粒状活性炭は、激しい国際競争の中で、なお新製
品、新技術の開発が課題となっている。すなわち、良質
な原料の安定確保、および代替原料の探索、その原料に
よる新製品の開発(使途目的に沿う需要の定着を図
る)、さらには、再生処理に安定な製品、その他をその
ような課題として挙げることができる。
In Japan, the activation treatment for producing granular activated carbon employs both gas activation and chemical activation.
Activated carbon produced through such activation treatment is used while making the most of each characteristic. However, in the case of granular activated carbon, the development of new products and new technologies is still an issue in fierce international competition. In other words, we need to ensure stable supply of high-quality raw materials, search for alternative raw materials, develop new products using those raw materials (establish demand that meets the purpose of use), and provide products that are stable for reprocessing and other issues. It can be mentioned as.

【0017】活性炭は吸着機能をもつ多孔質炭材で、原
料は、例えば、それを焼成(炭化)して得る炭材が水蒸
気などの活性化ガスと高温下で反応して多孔質炭材にな
る、あるいはそれを塩化亜鉛のような賦活剤と混合した
後、焼成(炭化、賦活)すると多孔質炭材になる、よう
な含炭素物質であるところから、本発明者は、さらに研
究を続けた。
Activated carbon is a porous carbon material having an adsorbing function. The raw material is, for example, a carbon material obtained by calcining (carbonizing) the material and reacting with an activating gas such as steam at a high temperature to form a porous carbon material. The present inventor has continued his research, since it is a carbon-containing substance that becomes a porous carbon material when it is mixed with an activator such as zinc chloride and then calcined (carbonized, activated). Was.

【0018】活性炭の原料としては、一般に、木材系、
果実殻系、果実種子系、その他を含む植物系原料;海
藻、その他を含む天然素材;再生繊維、その他を含む合
成素材;に及び、さらに粉末活性炭では、鋸屑などの植
物系原料、ピート炭、褐炭などの鉱物系原料の他、パル
プ廃液等の特殊な原料も挙げられ、一方、粒状活性炭で
は、木炭、やし殻炭、低灰分のピート炭、褐炭、レキ青
炭および無煙炭も挙げられる。そして、汎用活性炭の原
料は殆ど海外からの輸入に依存しており、質的及び量的
に安定確保が必要となっている。
As a raw material of activated carbon, wood-based,
Plant raw materials including fruit husks, fruit seeds, and others; natural materials including seaweeds and others; synthetic materials including regenerated fibers and others; and, in the case of powdered activated carbon, plant raw materials such as sawdust, peat charcoal, In addition to mineral raw materials such as lignite, special raw materials such as pulp waste liquor are also included. On the other hand, granular activated carbon includes charcoal, coconut shell, low-ash peat coal, lignite, lime blue coal, and anthracite. Most of the raw materials for general-purpose activated carbon depend on imports from overseas, and it is necessary to ensure qualitative and quantitative stability.

【0019】次に、従来法による活性炭の製造について
例を挙げて説明する。
Next, the production of activated carbon by a conventional method will be described with reference to examples.

【0020】1つの例は、炭化装置を用い、製材鋸屑を
乾留炭化し(空気を遮断して鋸屑固体を強く熱し、熱分
解によりできた揮発分や油状物質などを回収)、つぎに
炭化物を賦活炉内で水蒸気、空気および燃焼ガスなどを
適宜混合したガスと、850〜1150℃の温度条件下
で接触させて活性化反応をすすめる。この場合、得られ
る中間原料の炭化物は炭化処理で粒子の変形、ひび割
れ、融着などがおこらないよう徐々に600〜800℃
まで加熱する。炭化処理については、原料の炭化操作が
容易に制御でき、均質な炭化物を連続して生産できるも
のが望ましく、賦活処理も、やし殻活性炭の場合と同様
に、用途に応じて活性化反応をすすめるが、所望の活性
炭の種類および性状、活性化反応速度によって賦活炉の
形式および規模が選定される。
One example is the use of a carbonizer to dry distill and carbonize sawdust (the air is cut off to strongly heat the sawdust solids and recover volatiles and oily substances produced by thermal decomposition), and then to remove the carbides. The activation reaction is promoted by bringing the mixture into contact with a gas in which steam, air, a combustion gas or the like is appropriately mixed in an activation furnace at a temperature of 850 to 1150 ° C. In this case, the obtained carbide of the intermediate raw material is gradually heated to 600 to 800 ° C. so as not to cause the deformation, cracking, fusion, etc. of the particles in the carbonization treatment.
Heat until As for the carbonization treatment, it is desirable that the carbonization operation of the raw material can be easily controlled and that a homogeneous carbide can be continuously produced, and the activation treatment can also be performed according to the application, as in the case of coconut shell activated carbon. It is recommended that the type and size of the activation furnace be selected depending on the type and properties of the desired activated carbon and the activation reaction rate.

【0021】他の例として造粒活性炭の製造について説
明する。原料は、例えば木炭、やし殻炭、石炭、コーク
スなどから最適な原料が選ばれ、それらを200メッシ
ュ以下に微粉砕し、これにコールタール、ピッチ、デン
プン、糖蜜など種々の結着剤を加え、また活性化反応に
有効な触媒や、そのほか、酸、塩基を適宜配合する。結
着剤の使用割合は、原料1重量部に対し、0.4〜0.
55とし、当該混合物を加温しながら均等に混練し、一
定粒度に成形し、ついで乾燥して、燃焼ガス気流中で4
50℃程度まで加熱して表面を硬化してから炭化する
か、あるいは乾燥物を徐々に600〜800℃まで加熱
炭化して、緻密な硬い炭化物とする。賦活処理は、炭化
物を750〜1050℃の温度で水蒸気、二酸化炭素で
活性化反応をすすめ、さらに賦活炭の製品化は炭素中の
無機質(灰分)を希塩酸などで洗い脱灰し、さらに水洗
いを繰り返して精製後、乾燥して完成する。
The production of granulated activated carbon will be described as another example. For the raw material, for example, the most suitable raw material is selected from charcoal, coconut shell charcoal, coal, coke, and the like. In addition, a catalyst effective for the activation reaction, an acid and a base are appropriately added. The binder is used in an amount of 0.4 to 0.
The mixture was uniformly kneaded while being heated, formed into a uniform particle size, dried, and dried in a combustion gas stream.
It is heated to about 50 ° C. to harden the surface and then carbonized, or the dried product is gradually heated to 600 to 800 ° C. and carbonized to form a dense hard carbide. The activation treatment promotes the activation reaction of the carbide with steam and carbon dioxide at a temperature of 750 to 1050 ° C. Further, the commercialization of the activated carbon involves washing the inorganic matter (ash) in the carbon with dilute hydrochloric acid or the like, deashing it, and further washing with water. After repeated purification, dry and complete.

【0022】本発明の活性炭は、原料にグルコマンナン
を使用する以外は、適宜このような従来の活性炭の製法
に依拠して製造することができる。すなわち、いずれの
活性炭の製法にも、マンナンは良好な原料となるのであ
る。
The activated carbon of the present invention can be produced by appropriately relying on such a conventional method for producing activated carbon, except that glucomannan is used as a raw material. That is, mannan is a good raw material in any of the methods for producing activated carbon.

【0023】これを詳述すると、本発明の活性炭は、グ
ルコマンナンを主原料とする水和ゲルを乾燥し、得られ
た乾燥固形物を炭化処理し、次いで賦活処理して製造す
ることができるものであり、例えば、グルコマンナンを
主原料とする水和ゲル(糊)を成形して乾燥し、得られ
た乾燥固形物を炭化処理に付し、次いで賦活処理するこ
とで製造することができる。
More specifically, the activated carbon of the present invention can be produced by drying a hydrated gel containing glucomannan as a main raw material, carbonizing the obtained dried solid, and then activating. It can be produced, for example, by molding and drying a hydrated gel (glue) containing glucomannan as a main raw material, subjecting the obtained dried solid to a carbonization treatment, and then performing an activation treatment. .

【0024】ここに、グルコマンナンを主原料とする水
和ゲル(糊)は、例えば、グルコマンナンと水酸化カル
シウムなどの凝固剤および必要に応じて孔隙構造が発達
した炭素とする見地から使用することのできる含炭素物
質(植物系や天然素材、合成素材等)などの原料を粉体
混合し、これに水を加えて攪拌混練することで調製する
ことができる。水の使用量は、水和ゲルを成形して乾燥
する見地からは、グルコマンナン粒子と凝固剤とが水和
ゲル中において均一かつ十分に接触できるかぎり可及的
少量であることが好ましく、これは、このように、グル
コマンナンと凝固剤を粉体混合し、これに水を加えて攪
拌することで達成することができる。具体的には、水の
使用量は、グルコマンナン1重量部当たり、例えば5〜
10重量部とすることができる。
Here, the hydrated gel (glue) containing glucomannan as a main material is used from the viewpoint of, for example, glucomannan and a coagulant such as calcium hydroxide and, if necessary, carbon having a developed pore structure. It can be prepared by mixing powders of raw materials such as carbon-containing substances (vegetables, natural materials, synthetic materials, etc.), adding water thereto, and stirring and kneading. From the viewpoint of forming and drying the hydrated gel, the amount of water used is preferably as small as possible as long as the glucomannan particles and the coagulant can be uniformly and sufficiently contacted in the hydrated gel. Can be achieved by mixing powder of glucomannan and a coagulant, adding water thereto, and stirring. Specifically, the amount of water used is, for example, 5 to 5 parts by weight of glucomannan.
It can be 10 parts by weight.

【0025】このようにして得られた水和ゲルは、乾燥
し易いように適宜成形してから乾燥し、次いで得られた
乾燥固形物を、順次、炭化処理及び賦活処理に付する。
炭化処理及び賦活処理は、先に述べたように、適宜従来
法によることができ、また賦活処理後必要に応じて精製
処理するが、この精製処理も適宜従来法によることがで
きる。
The hydrated gel thus obtained is appropriately shaped so as to be easily dried, and then dried. Then, the obtained dried solid is subjected to a carbonizing treatment and an activation treatment sequentially.
As described above, the carbonization treatment and the activation treatment can be appropriately performed by a conventional method. Further, after the activation treatment, a purification treatment is performed as necessary. The purification treatment can also be appropriately performed by a conventional method.

【0026】本発明の活性炭は、もちろん、上に例示説
明した方法により製造された活性炭に限られるものでは
なく、グルコマンナンを主原料とする水和ゲルから製造
される活性炭であって、このような方法により得られる
ものと同様の活性炭特性を有するものであれば、これら
は全て本発明のグルコマンナン活性炭に含まれる。
The activated carbon of the present invention is, of course, not limited to the activated carbon produced by the method described above, but is activated carbon produced from a hydrated gel containing glucomannan as a main raw material. These are all included in the glucomannan activated carbon of the present invention as long as they have the same activated carbon properties as those obtained by the various methods.

【0027】[0027]

【実施例】以下、実施例をもって本発明をさらに詳細に
説明する。
The present invention will be described in more detail with reference to the following examples.

【0028】実施例1 マンナン(こんにゃく精粉)40g、「アビセル」(旭
化成(株)製結晶セルローズ粉体)19.8gおよびC
a(OH)21.2g(計60g)を粉体混合し、これ
を水(20℃)480g中に投入してハンドミキサーで
撹拌し、粘度が上昇した約5分後に撹拌を中止し、樹脂
ヘラで約1分間押さえ延ばしして練り、マンナンの水和
ゲル(糊)540gを得、これをバットに入れて延ば
し、そのまま約2時間放置して安定を図った後、ほぼ均
等の6本に切り分け(4cm×15cm×3.3c
m)、60℃の乾燥機で2時間加熱乾燥した後、50℃
に設定した恒温機でさらに72時間乾燥し、320g
(6本)の木片のような乾燥固形物を得た。次に、この
固形物を焼釜で、450℃までに温度上昇する約30分
加熱して乾留炭化し、ついで、この炭化物を900〜1
000℃で水蒸気および二酸化炭素の適宜混合ガスと接
触させて賦活(活性化)をはかった後冷却し、次に希塩
酸で洗い脱灰し、これを水洗いして乾燥し、活性炭6本
(120g)を収得した。マンナンの硬質な凝固物の活
性炭原料の乾留炭化物は、活性化反応がすすみ、良好な
活性炭となった。
Example 1 40 g of mannan (konjac fine powder), 19.8 g of "Avicel" (crystalline cellulose powder manufactured by Asahi Kasei Corporation) and C
a (OH) 2 1.2 g (total 60 g) was powder mixed, and the mixture was poured into 480 g of water (20 ° C.) and stirred with a hand mixer. After about 5 minutes when the viscosity increased, the stirring was stopped. Press and extend with a resin spatula for about 1 minute and knead to obtain 540 g of mannan hydrated gel (glue), put it in a vat and spread it, leave it for about 2 hours to stabilize, (4cm × 15cm × 3.3c
m), after drying by heating in a dryer at 60 ° C for 2 hours,
Dry for another 72 hours in a thermostat set at
A dry solid like (6) wood chips was obtained. Next, the solid is heated in a baking oven for about 30 minutes to raise the temperature to 450 ° C., and carbonized by dry distillation.
After activation (activation) by contacting with an appropriate mixed gas of steam and carbon dioxide at 000 ° C., cooling, then washing with dilute hydrochloric acid and decalcification, washing with water and drying, 6 activated carbons (120 g) Was obtained. The activated carbonized carbonized raw material as a raw material of activated carbon, which is a hard coagulate of mannan, progressed to an activated carbon.

【0029】このものの吸着性能(液相)をテストする
ため、その破砕物20gを0.2%カラメル水溶液20
0mlに約30分浸した(10分ごとに2回かき回し)
結果、0.03%のカラメル水溶液と同程度の着色度に
まで脱色されたことを確認した(85%脱色)。
To test the adsorption performance (liquid phase) of this product, 20 g of the crushed product
Soaked in 0ml for about 30 minutes (twice every 10 minutes)
As a result, it was confirmed that the color was decolorized to the same degree of coloring as the 0.03% aqueous caramel solution (85% decolorization).

【0030】[0030]

【発明の効果】今日、活性炭の用途が飛躍的にひろが
り、その需要が顕著に増大した。活性炭は、形状や機能
がますます多種多様化し、用途も複雑であり、然も高度
化しているが、今後さらに用途開発が進められ、社会機
構での必須要項となる重要な役割を担っているが、その
原料を殆ど外国からの輸入に依存するため、原料価格は
もちろん、質、量ともに極めて不安定で、しかも不足し
ている。この現状において、本発明の活性炭の原料であ
るグルコマンナンは、わが国の農産物として食品原料に
使用されてきた安全な永年の実績を持ち、現状において
も数倍の計画生産が可能(財団法人「日本こんにゃく協
会」平成7年・年次畑作栽培実績調査報告書)とされて
いる。
The use of activated carbon has been dramatically expanded today, and the demand for the activated carbon has increased remarkably. Activated carbon has an ever-increasing variety of shapes and functions, and its use is complicated, and it is becoming more sophisticated.However, the use of activated carbon will be further developed in the future, and it will play an important role as an essential element in social organizations However, since its raw materials mostly depend on imports from foreign countries, raw materials prices, quality and quantity are extremely unstable, and they are in short supply. Under the present circumstances, glucomannan, which is a raw material of the activated carbon of the present invention, has a long and safe track record of being used as a food product in Japan as an agricultural product, and even under the present circumstances, several times the planned production is possible (Japan Konjac Association, 1995, annual field cultivation results survey report).

【0031】本発明によれば、グルコマンナンの活用に
より前記のような活性炭原料の不足が補われ、延いては
グルコマンナンの活性炭の原料としての新規需要が実現
するに至り、農産振興に寄与すると共に、本発明による
活性炭の及ぼす経済効果は極めて大である。
According to the present invention, the above-mentioned shortage of activated carbon raw material is compensated for by utilizing glucomannan, and new demand for glucomannan as a raw material for activated carbon is realized, contributing to the promotion of agricultural production. In addition, the economic effect of the activated carbon according to the present invention is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 グルコマンナンを主原料とする水和ゲル
を乾燥し、得られた乾燥固形物を炭化処理し、次いで賦
活処理して製造することができることを特徴とするグル
コマンナン活性炭。
1. A glucomannan activated carbon characterized in that it can be produced by drying a hydrated gel containing glucomannan as a main raw material, carbonizing the resulting dried solid, and then activating it.
JP9030574A 1997-02-14 1997-02-14 Glucomannan activated carbon Expired - Fee Related JP3012940B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9030574A JP3012940B2 (en) 1997-02-14 1997-02-14 Glucomannan activated carbon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9030574A JP3012940B2 (en) 1997-02-14 1997-02-14 Glucomannan activated carbon

Publications (2)

Publication Number Publication Date
JPH10226508A true JPH10226508A (en) 1998-08-25
JP3012940B2 JP3012940B2 (en) 2000-02-28

Family

ID=12307629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9030574A Expired - Fee Related JP3012940B2 (en) 1997-02-14 1997-02-14 Glucomannan activated carbon

Country Status (1)

Country Link
JP (1) JP3012940B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006169300A (en) * 2004-12-14 2006-06-29 Shimizu Kagaku Kk Method for producing glucomannan gel particle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006169300A (en) * 2004-12-14 2006-06-29 Shimizu Kagaku Kk Method for producing glucomannan gel particle

Also Published As

Publication number Publication date
JP3012940B2 (en) 2000-02-28

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