JPS6229368B2 - - Google Patents
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- Publication number
- JPS6229368B2 JPS6229368B2 JP54080537A JP8053779A JPS6229368B2 JP S6229368 B2 JPS6229368 B2 JP S6229368B2 JP 54080537 A JP54080537 A JP 54080537A JP 8053779 A JP8053779 A JP 8053779A JP S6229368 B2 JPS6229368 B2 JP S6229368B2
- Authority
- JP
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- Prior art keywords
- activated carbon
- spherical activated
- spherical
- present
- temperature
- 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.)
- Expired
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Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K33/00—Medicinal preparations containing inorganic active ingredients
- A61K33/44—Elemental carbon, e.g. charcoal, carbon black
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P39/00—General protective or antinoxious agents
- A61P39/02—Antidotes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
- C01B32/33—Preparation characterised by the starting materials from distillation residues of coal or petroleum; from petroleum acid sludge
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
- C01B32/384—Granulation
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Epidemiology (AREA)
- Engineering & Computer Science (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Toxicology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Medicinal Preparation (AREA)
- External Artificial Organs (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Carbon And Carbon Compounds (AREA)
Description
本発明は、活性炭の少なくとも85%が真球であ
る球形活性炭から成る、消化器系から毒物あるい
は有害物質を除去、解毒するのに適した球形活性
炭およびその製造法に関する。
更に詳しくは、本発明は胃、腸のような消化器
系内に存在あるいは生成される有害物質を、活性
炭の服用によつて解毒する際に、従来から問題と
されていた便秘性副作用を示さない、活性炭の少
なくとも85%が真球である解毒剤に適した球形活
性炭およびその製造法に関する。
活性炭は、これを服用することにより腸疾患等
の治療に効果的であるということは古くから知ら
れており、多くの病気治療の目的に用いられてい
る。活性炭を服用することにより、赤痢、コレ
ラ、腸チフス、食中毒等の細菌性感染性、消化不
良、腸の張り、慢性胃炎、てんかん、めまい、萎
黄病及び炭疽病等に対して、特に優れた治療効果
を示すということが報告されている。また、薬
物、毒物の摂取に際して、救急的に活性炭を服用
することにより解毒効果が得られている。更に、
活性炭の服用は、その他各種の疾患に併なう代謝
異常により生成する消化器系内の有害物質の除去
に対しても効果的である。
これらの効果は、消化器系内の毒素、異常代謝
物又は毒素を生成する或いは代謝異常をひきおこ
す物質が生体に対して全く毒性のない活性炭に吸
着され、活性炭と共に体外に排出されるためと考
えられている。
従来、この解毒作用を目的としては全て粉末活
性炭が用いられており、この粉末活性炭を水とい
つしよに服用するか、適当な錠剤として服用され
ていた。
錠剤として服用しても体内で解錠され粉末状と
なり水といつしよに服用した場合と同等の吸着能
力を発現する。しかしながら、粉末活性炭の使用
は副作用として便秘現象を起せしめ、これが大き
な欠点でもあつた。特に活性炭は通常、各種疾患
に際して服用するものであるから、患者の体力が
消耗している場合が多く、この時、副作用として
起る便秘は患者にとつて著しい苦痛であるばかり
でなく、患者が充分な排泄力を有していない場合
には、機械的にこれを除去しなければ、生命に関
する場合も生じ得るという欠点を従来の活性炭は
有していた。
このような状況に鑑み、本発明者は、前述した
欠点を解決すべく、鋭意研究の結果、活性炭の少
なくとも85%、好ましくは90%が真球である特定
な球形活性炭が、優れた解毒作用を有しかつ便秘
性副作用を示さないことを見出し、本発明に到達
した。
本発明による解毒剤は、2工程からなる次の記
載の方法によつて高分子量炭化水素、例えばピツ
チから製造される。
第一工程では、ピツチを熔融状態で小粒球形と
し冷却の後、酸化して不融化し、その後不活性雰
囲気中800〜1000℃の温度で炭化し、次いで水蒸
気雰囲気中で900〜1000℃の温度で賦活して、直
径0.05〜2mm、表面積500〜2000m2/g、細孔半径
100〜75000Åの範囲での細孔容積0.05〜1.0ml/
g、PH=8〜10の微小球形活性炭を製造する。
第二工程では、これらの球形活性炭をNH3を1
〜1000ppm好ましくは5〜100ppm含有する希ア
ンモニア水溶液で接触処理し乾燥して、アンモニ
ア処理をおこなう前の球形活性炭と同一直径、表
面積及び細孔容積を有し、アンモニア処理する前
の球形活性炭に比較してPH=6〜8の微小球形活
性炭を製造する。
この生成物は、活性炭の少なくとも85%が真球
である微小球形活性炭からなつており、この活性
炭は、めだつたかどのない、なめらかな凸表面を
有しており、最大直径と最小直径の割合が1.0―
1.3である。
球形活性炭の粒径(直径)が0.05mm以下では解
毒作用はあつても便秘性副作用の除去には充分効
果的でない。また球形活性炭の粒径が2mm以上に
なると、服用し難いだけでなく、目的とする解毒
効果も迅速に発現しない。
活性炭の形状は本発明の満足すべき医薬上の効
果を得る上でのひとつの重要な因子であり、実質
に球形であることが必要である。更に、詳しく
は、活性炭の少なくとも85%が真球であることが
必要である。
形状と同様に、活性炭の表面積及び細孔容積
も、充分な解毒作用と便秘性副作用の除去という
効果を同時に発現させる上で重要な要因となる。
即ち、活性炭の表面積、細孔容積が小さすぎると
吸着力が弱くなり実用上充分な解毒効果は得られ
ず、また表面積、細孔容積が大きすぎると解毒作
用はあつても便秘現象を併なうことになる。また
活性炭の表面積、細孔容積が本発明の範囲より大
きくなると、強度が低下して服用時又は服用後に
形状が崩れ粉化を併なうことも便秘性副作用を生
ずる原因と考えられる。
本発明の微小球形活性炭の表面積は、市販の表
面積測定装置を用いて測定すると、500〜2000m2/
g、好ましくは700〜1500m2/gである。
細孔容積は、市販の水銀圧入ボロシメーターで
測定すると、細孔半径100〜75000Åの領域で0.05
〜1.0ml/g、好ましくは0.1〜0.8ml/gである。
このような特性を有する活性炭の製造に用いる
原料として、オガ屑、石炭、ヤシ殻、ピツチ類、
有機合成高分子等の公知の原料の何れでもよく、
これらの物質から球形活性炭を製造することがで
きる。
例えば、所期の球形活性炭を製造する方法とし
ては、粉末原料をピツチ等のバインダーを用いて
小粒球形に造粒し、次いで不活性雰囲気中で800
〜1000℃に加熱焼成して炭化し、水蒸気雰囲気中
で900〜1000℃で賦活する方法がある。
一方、例えば特公昭50―18879に開示されてい
る方法により、ピツチ類を熔融状態で小粒球形と
し次いで酸化により不融化した後、不活性雰囲気
中で800〜1000℃で加熱焼成して炭化し、水蒸気
雰囲気中で900〜1000℃で賦活する方法により球
形活性炭を製造することができる。特に、後者の
方法では真球度の高い、高強度の表面から滑らか
な球形活性炭が得られるので、本発明の活性炭の
製造方法として好適である。
本発明の微小球活性炭の製造方法の第二工程
は、特に重要なプロセスである。球形活性炭のPH
は、通常PH=8〜10であるが、これをPH=6〜8
に変える。この第二工程の処理をすることによつ
て球形活性炭は優れた性質をもつようになる。
アンモニア水溶液による処理の条件は、水蒸気
処理をした球形活性炭の状態に依つて異なるが、
通常は、アンモニア水溶液のNH3の濃度は1〜
1000ppm好ましくは5〜100ppm、アンモニア水
溶液と球形活性炭の容量割合は1〜50、好ましく
は2〜10で、処理温度は10〜50℃で、処理時間は
0.5〜5時間である。アンモニア水溶液中のNH3
の濃度が上述した範囲よりも高くなると生成物の
PHも高くなつて、アルカリ領域となり、またNH3
の濃度が低くなると生成物のPHはアルカリ領域に
残る。
アルカリ性を示す球形活性炭が、アルカリ試
薬、すなわち、アンモニア水溶液と接触させるこ
とによつて酸性―中性の球形活性炭に変わる理由
は明らかではなく、更にこのようなPHの変化は全
く予期せぬことであつた。次に、このようにアン
モニア水溶液によつて処理された球形活性炭を通
常100〜150℃の温度で乾燥し、服用に適するサイ
ズにふるいわけをする。一様なサイズの生成物に
調整すること、すなわち一定の範囲のサイズに篩
分けすることは服用する際に好ましいことであ
る。ふるいわけは、最大粒子と最小粒子の直径の
比が1〜1.3であるような球形活性炭を得るため
に、アンモニア水溶液処理をおこなう前に、おこ
なわれる。
何れの場合においても球形活性炭は服用するも
のであるから、安全上充分な純度のものでなけれ
ばならないのは勿論であつて例えば、日本薬局法
第九改正、“薬用炭”の項に示されている純度試
験に適合するものでなければならない。
本発明による球形活性炭の服用方法は、通常の
活性炭と同様の公知の方法でよい。飲料水に本発
明による微小球形活性炭を懸濁させて服用するの
が最も簡単であるが、常法に従い球形活性炭を適
当な形の錠剤として服用してもよい。但し、この
場合は勿論本発明の球形活性炭としての効果を示
す様、体内で元の球形活性炭粒子に解錠される必
要がある。
又常法に従い通常の円筒形カプセルに包含させ
て服用してもよい。
球形活性炭の服用量は、疾患の程度、緊急解毒
の必要性等によつても異なるが通常1回0.5〜10
g、1日3回程度である。又、食間服用が好まし
いが、緊急を要する場合は勿論この限りでない。
本発明の球形活性炭が解毒作用を維持しかつ便
秘性副作用の除去に著しい効果を示すことは全く
予期し得なかつたことで、未だその原因は明らか
でないが、本発明の球形活性炭はアンモニア処理
によつて表面が特殊な状態になつているため、外
因性及び内因性有害物質の吸着能力を保有してい
る。即ち、本発明の球形活性炭は摂取した食物、
消化した食物やその消化物の存在下においても、
従来の粉末活性炭、或いは単に粉末活性炭から球
形あるいは塊状化した活性炭と比較して、優れた
吸着能力を有する。従来の粉末炭又は、該粉末炭
の球状化あるいは塊状化物は腸運動の刺激物質も
吸着し、腸の運動を弱めると同時に便によく混合
して便の凝集力を増して便秘をきたすのに対し、
本発明の球形活性炭は表面性質の異なる滑らかな
球体であるため、便の凝集力上昇効果をもたらさ
ないと同時に、腸運動の刺激物質の吸着が少な
く、又、球形活性炭が腸に適度な刺激を与える等
の複合効果により便秘をきたさないとも推定され
る。
以下、実施例によつて本発明の効果を説明する
が、何等本発明の範囲を限定するものではない。
実施例1 (球形活性炭の製造)
原油の高温分解により得られたピツチ(軟化点
175℃、ニトロベンゼン不溶分25%、H/C元素比
0.63)750部、ナフタレン250部を撹拌機付ステン
レス製オートクレープに仕込み、170℃で混合溶
解し、これに「ゴーセノールGH―17」(日本合成
社製ポリビニルアルコール系懸濁剤)0.5%水溶
液3000部を加えて130℃で60分間激しく撹拌した
後、撹拌下に室温まで冷却し、真球状の球形粒子
を得た。大部分の水を別した後、粒子重量の5
倍量のメタノールに浸漬、振盪してナフタレンを
抽出除去した後通風乾燥し、次いで、小型ロータ
リー・キルン中で空気を送入しながら25℃/Hr
で300℃まで昇温して不触性の球形粒子を得た。
次いで空気送入を停止し、代りに水蒸気を送入し
ながら900℃まで昇温することによつて炭化し、
更にこの温度に保つことによつて賦活を進めて、
粒径0.1〜1.5mmの真球性の高い球形活性炭を得
た。
賦活時間を変えることによつて賦活の程度が異
なつた2種の球形活性炭を、製造した。
比較試料No.1は賦活度の低いものであり、比較
試料No.2は賦活度の高いものであり、共に球形サ
イズをふるいわけにて整えてものである。
次に、比較試料No.1及び比較試料No.2の球形活
性炭のそれぞれ一部を、NH3の濃度が10ppmであ
るアンモニア水溶液に、アンモニア水溶液と球形
活性炭の容積/重量比が10ml/1gで、室温下3
時間浸した。続いて、溶液から球形活性炭を取り
出し、110℃の温度で16時間乾燥して、球形活性
炭を生成した。
賦活度の低い度合の活性炭からの生成物を試料
No.1とし、賦活度の高い度合の活性炭からの生成
物を試料No.2とする。
これら4つの活性炭の特性を表―1に示す。
尚、吸着能力は試験管内試験によつて、クレア
チニン及び尿酸に対する吸着能力をそれぞれ測定
した。前述の2つの物質は、腎疾患等の代謝異常
で体内に生成する有害物質としてよく知られてい
るものである。
The present invention relates to spherical activated carbon, which is made of spherical activated carbon in which at least 85% of the activated carbon is true spheres, and is suitable for removing and detoxifying poisons or harmful substances from the digestive system, and a method for producing the same. More specifically, the present invention shows that when activated charcoal is taken to detoxify harmful substances that exist or are produced within the digestive system such as the stomach and intestines, the constipation side effect that has been a problem in the past has been demonstrated. The present invention relates to a spherical activated carbon suitable for an antidote, in which at least 85% of the activated carbon is true spheres, and a method for producing the same. Activated charcoal has long been known to be effective in treating intestinal diseases and the like when ingested, and is used to treat many diseases. By taking activated charcoal, it has a particularly excellent therapeutic effect on dysentery, cholera, typhoid fever, bacterial infections such as food poisoning, indigestion, intestinal tension, chronic gastritis, epilepsy, dizziness, yellowing disease, anthrax, etc. It has been reported that it shows. In addition, detoxifying effects have been obtained by taking activated charcoal as an emergency when ingesting drugs or poisonous substances. Furthermore,
Taking activated charcoal is also effective in removing harmful substances in the digestive system that are produced due to metabolic abnormalities associated with various other diseases. These effects are thought to be due to the fact that toxins, abnormal metabolites, or substances that produce toxins or cause metabolic abnormalities in the digestive system are adsorbed by activated carbon, which is completely non-toxic to living organisms, and are excreted from the body along with the activated carbon. It is being Conventionally, powdered activated carbon has been used for the purpose of detoxification, and this powdered activated carbon has been taken with water or in the form of a suitable tablet. Even when taken as a tablet, it is unlocked within the body and turns into a powder, which exhibits the same adsorption capacity as when taken with water. However, the use of powdered activated carbon caused constipation as a side effect, which was a major drawback. In particular, since activated charcoal is usually taken to treat various diseases, patients' physical strength is often exhausted, and the constipation that occurs as a side effect is not only extremely painful for the patient, but also Conventional activated carbon has the disadvantage that if it does not have sufficient excretion power, it may be life-threatening unless it is removed mechanically. In view of this situation, in order to solve the above-mentioned drawbacks, the inventor of the present invention has conducted extensive research and found that a specific spherical activated carbon in which at least 85%, preferably 90% of the activated carbon is true spheres has an excellent detoxifying effect. The present invention was achieved based on the discovery that the present invention has the following properties and does not exhibit constipation side effects. The antidote according to the invention is prepared from a high molecular weight hydrocarbon, such as pitch, by the following described process consisting of two steps. In the first step, pitch is made into small spherical particles in a molten state, cooled, oxidized to make it infusible, then carbonized at a temperature of 800 to 1000°C in an inert atmosphere, and then carbonized at a temperature of 900 to 1000°C in a steam atmosphere. Activated with 0.05~2mm diameter, surface area 500~ 2000m2 /g, pore radius
Pore volume 0.05-1.0ml/ in the range 100-75000Å
g, to produce microspherical activated carbon with pH=8-10. In the second step, these spherical activated carbons are heated with 1 NH 3
~1000ppm, preferably by contact treatment with a dilute ammonia aqueous solution containing 5 to 100ppm and drying, to have the same diameter, surface area and pore volume as the spherical activated carbon before the ammonia treatment, compared to the spherical activated carbon before the ammonia treatment. Microspherical activated carbon with a pH of 6 to 8 is produced. The product consists of microspherical activated carbon in which at least 85% of the activated carbon is true spheres, the activated carbon has a smooth convex surface with no noticeable edges, and the ratio of maximum diameter to minimum diameter is 1.0―
It is 1.3. If the particle size (diameter) of spherical activated carbon is 0.05 mm or less, it will not be sufficiently effective in eliminating constipation side effects, even if it has a detoxifying effect. Furthermore, if the particle size of the spherical activated carbon exceeds 2 mm, it will not only be difficult to take, but also the desired detoxifying effect will not be achieved quickly. The shape of the activated carbon is one important factor in obtaining the satisfactory pharmaceutical effects of the present invention, and it is necessary that it be substantially spherical. More specifically, at least 85% of the activated carbon needs to be true spheres. Similar to the shape, the surface area and pore volume of activated carbon are also important factors in achieving sufficient detoxification and eliminating constipation side effects at the same time.
In other words, if the surface area and pore volume of activated carbon are too small, the adsorption power will be weak and a practically sufficient detoxification effect will not be obtained, and if the surface area and pore volume are too large, even if the activated carbon has a detoxifying effect, it may also cause constipation. That's what happens. Furthermore, when the surface area and pore volume of activated carbon are larger than the range of the present invention, the strength decreases, the shape collapses during or after ingestion, and powdering occurs, which is also considered to be a cause of constipation side effects. The surface area of the microspherical activated carbon of the present invention is 500 to 2000 m 2 /
g, preferably 700 to 1500 m 2 /g. The pore volume is 0.05 in the pore radius region of 100 to 75000 Å when measured with a commercially available mercury intrusion borosimeter.
-1.0ml/g, preferably 0.1-0.8ml/g. Raw materials used to produce activated carbon with such characteristics include sawdust, coal, coconut shells, pithus,
Any known raw materials such as organic synthetic polymers may be used,
Spherical activated carbon can be produced from these materials. For example, to produce the desired spherical activated carbon, powder raw materials are granulated into small spherical shapes using a binder such as pitch, and then 800 g
There is a method of carbonizing by heating to ~1000°C and activating at 900~1000°C in a steam atmosphere. On the other hand, for example, according to the method disclosed in Japanese Patent Publication No. 50-18879, pitches are made into small spherical shapes in a molten state, and then made infusible by oxidation, and then carbonized by heating at 800 to 1000°C in an inert atmosphere. Spherical activated carbon can be produced by a method of activation at 900 to 1000°C in a steam atmosphere. In particular, the latter method is suitable as the method for producing activated carbon of the present invention, since smooth spherical activated carbon with a high sphericity and high strength surface can be obtained. The second step of the method for producing activated carbon microspheres of the present invention is a particularly important process. PH of spherical activated carbon
is usually PH=8~10, but this is PH=6~8
Change to By performing this second step, the spherical activated carbon has excellent properties. The conditions for treatment with aqueous ammonia solution vary depending on the state of the spherical activated carbon that has been treated with steam, but
Usually, the concentration of NH 3 in ammonia aqueous solution is 1 to
1000ppm, preferably 5-100ppm, the volume ratio of ammonia aqueous solution and spherical activated carbon is 1-50, preferably 2-10, the treatment temperature is 10-50℃, and the treatment time is
It is 0.5 to 5 hours. NH3 in aqueous ammonia solution
When the concentration of is higher than the range mentioned above, the product
PH also increases and becomes alkaline, and NH 3
When the concentration of is low, the PH of the product remains in the alkaline region. It is not clear why spherical activated carbon, which exhibits alkalinity, changes to acidic-neutral spherical activated carbon when it comes into contact with an alkaline reagent, that is, an aqueous ammonia solution, and furthermore, such a change in PH is completely unexpected. It was hot. Next, the spherical activated carbon thus treated with the aqueous ammonia solution is dried at a temperature of usually 100 to 150°C and sieved into sizes suitable for administration. Adjusting the product to a uniform size, ie sieving to a range of sizes, is preferred for dosing. Sieving is carried out before the ammonia aqueous solution treatment in order to obtain spherical activated carbon with a diameter ratio of the largest particles to the smallest particles of 1 to 1.3. In any case, since the spherical activated carbon is to be taken, it must of course be of sufficient purity for safety. The purity test must be passed. The method for taking the spherical activated carbon according to the present invention may be the same known method as for ordinary activated carbon. Although it is easiest to take the microspherical activated carbon according to the present invention by suspending it in drinking water, it is also possible to take the spherical activated carbon in the form of an appropriately shaped tablet according to a conventional method. However, in this case, of course, it is necessary to unlock the original spherical activated carbon particles within the body so that the spherical activated carbon of the present invention can exhibit its effects. It may also be taken in a conventional cylindrical capsule according to a conventional method. The dose of spherical activated charcoal varies depending on the severity of the disease, the need for emergency detoxification, etc., but it is usually 0.5 to 10 g per dose.
g, about 3 times a day. Also, it is preferable to take the drug between meals, but of course this does not apply if there is an emergency. It was completely unexpected that the spherical activated carbon of the present invention would maintain the detoxification effect and show a remarkable effect on eliminating constipation side effects, and although the cause is still unclear, the spherical activated carbon of the present invention does not require ammonia treatment. Because of its special surface condition, it has the ability to adsorb exogenous and endogenous harmful substances. That is, the spherical activated carbon of the present invention can be used for ingested food,
Even in the presence of digested food and its digested products,
It has superior adsorption ability compared to conventional powdered activated carbon or activated carbon made from powdered activated carbon into spheres or agglomerates. Conventional powdered charcoal or spheroidized or agglomerated powdered charcoal also adsorbs substances that stimulate intestinal motility, weakening intestinal motility, and at the same time mix well with stool, increasing the cohesive force of stool and causing constipation. On the other hand,
Since the spherical activated carbon of the present invention is a smooth sphere with different surface properties, it does not have the effect of increasing the cohesive force of stool, and at the same time adsorbs few substances that stimulate intestinal motility, and the spherical activated carbon provides moderate stimulation to the intestines. It is also presumed that constipation will not occur due to the combined effect of feeding. EXAMPLES Hereinafter, the effects of the present invention will be explained with reference to Examples, but the scope of the present invention is not limited in any way. Example 1 (Production of spherical activated carbon) Pitch obtained by high-temperature decomposition of crude oil (softening point
175℃, nitrobenzene insoluble content 25%, H/C element ratio
0.63) 750 parts of naphthalene and 250 parts of naphthalene were placed in a stainless steel autoclave equipped with a stirrer, mixed and dissolved at 170°C, and added with 3000 g of a 0.5% aqueous solution of "GOHSENOL GH-17" (polyvinyl alcohol suspension agent made by Nippon Gohsei). After stirring vigorously at 130° C. for 60 minutes, the mixture was cooled to room temperature while stirring to obtain true spherical particles. After separating most of the water, 5 of the particle weight
After being immersed in twice the amount of methanol and shaking to extract and remove naphthalene, it was dried with ventilation, and then 25°C/Hr while blowing air in a small rotary kiln.
The temperature was raised to 300°C to obtain inaccessible spherical particles.
Next, the air supply is stopped, and steam is supplied instead to raise the temperature to 900℃, thereby carbonizing.
Furthermore, activation is promoted by keeping it at this temperature,
Highly spherical activated carbon with a particle size of 0.1 to 1.5 mm was obtained. Two types of spherical activated carbon with different degrees of activation were produced by changing the activation time. Comparative sample No. 1 has a low degree of activation, and comparative sample No. 2 has a high degree of activation, and both have spherical sizes adjusted by sieving. Next, a portion of each of the spherical activated carbons of Comparative Sample No. 1 and Comparative Sample No. 2 was added to an ammonia aqueous solution with an NH 3 concentration of 10 ppm at a volume/weight ratio of the ammonia aqueous solution and the spherical activated carbon of 10 ml/1 g. , at room temperature 3
Soaked for an hour. Subsequently, the spherical activated carbon was taken out from the solution and dried at a temperature of 110° C. for 16 hours to produce spherical activated carbon. Sample product from activated carbon with low degree of activation
Sample No. 1 and the product from activated carbon with a high degree of activation are Sample No. 2. Table 1 shows the properties of these four activated carbons. The adsorption capacity was determined by an in vitro test to measure the adsorption capacity for creatinine and uric acid. The two substances mentioned above are well known as harmful substances that are produced in the body due to metabolic abnormalities such as renal disease.
【表】【table】
第1表に示した試料について、マウスを用いた
急性毒性試験を実施した。結果は以下に示す通り
であり、本発明の球形活性炭を多量に投与しても
極めて安全性の高いものであることを確認した。
実験動物として、市販ICR―JCL系雌マウス
(体重22±1g)を用い、第1表の4つの試料を
胃ゾンデを用いて強制経口投与した。1週間後の
生死の判定により、Litchfield―Wilcoxon法から
LD50を求めた。結果を第2表に示す。1週間
後、解剖したが、外観的及び内臓観察においても
特記すべき異常所見を認めず又特記すべき中毒症
状も認められなかつた。
An acute toxicity test using mice was conducted on the samples shown in Table 1. The results are shown below, and it was confirmed that the spherical activated carbon of the present invention is extremely safe even when administered in large amounts. Commercially available ICR-JCL female mice (body weight 22±1 g) were used as experimental animals, and the four samples shown in Table 1 were orally administered by force using a gastric tube. After one week, the Litchfield-Wilcoxon method was used to determine whether the animal was alive or dead.
Asked for LD50 . The results are shown in Table 2. One week later, the animal was dissected, but no notable abnormal findings were found in the external appearance or internal organ observation, nor were any notable toxic symptoms observed.
【表】
実施例2 (動物実験)
体重130〜140gのウイスター(Wistar)系雌
ラツトを用い、ベントバルビタール―Naを20mg/
Kg体重になるように水溶液として経口投与した。
次いで直ちに第1表に示した試料を水懸濁液とし
て200mg/Kg体重になるように経口投与した。同時
に活性炭を投与しない比較試験を実施した。検体
は、各活性炭試料投与群及び非投与群毎に10匹ず
つ使用した。次いで血中のベントバルビータール
―Naの最大濃度の平均値を求め比較試験群での
濃度に対する割合を除去率として算出した結果は
第3表の通りである。
第3表から明らかなとうり、何れの球形活性炭
試料投与群においても解毒効果が観察された。し
かしながら、試料No.1及びNo.2(アンモニア処理
したもの)は、比較試料No.1及びNo.2(アンモニ
ア処理をしないもの)に比較して特に顕著な解毒
効果を有していた。[Table] Example 2 (Animal experiment) Using female Wistar rats weighing 130 to 140 g, bentobarbital-Na was administered at 20 mg/day.
It was orally administered as an aqueous solution to a body weight of Kg.
Immediately thereafter, the samples shown in Table 1 were orally administered as an aqueous suspension at a concentration of 200 mg/Kg body weight. At the same time, a comparative test was conducted in which activated charcoal was not administered. Ten specimens were used for each activated carbon sample administration group and non-administration group. Next, the average value of the maximum concentration of bentobarbital-Na in the blood was determined, and the ratio to the concentration in the comparative test group was calculated as the removal rate. The results are shown in Table 3. As is clear from Table 3, detoxification effects were observed in all groups administered with the spherical activated carbon samples. However, Samples No. 1 and No. 2 (those treated with ammonia) had particularly remarkable detoxifying effects compared to Comparative Samples No. 1 and No. 2 (those not treated with ammonia).
【表】
次いで、活性炭の投与から90分後にこれ等の検
体群を痲酔死させ消化管を摘出して活性炭の腸内
移送の程度を比較した。即ち、噴門から直腸末端
までの全長に対する活性炭到達部までの移送距離
の割合を移送率として判定した。結果は第4表に
示す様に、第1表に示す本発明の活性炭試料を用
いた検体群では、その移送率が大きく、便秘作用
の少ないことが示された。[Table] Next, 90 minutes after the administration of activated charcoal, these sample groups were killed by anesthesia, the gastrointestinal tract was removed, and the degree of intestinal transport of activated charcoal was compared. That is, the ratio of the transfer distance to the activated carbon reaching part to the total length from the cardia to the end of the rectum was determined as the transfer rate. As shown in Table 4, the results show that in the sample group using the activated carbon samples of the present invention shown in Table 1, the transport rate was high and the constipation effect was small.
【表】
実施例3 (吸着能)
本発明の球形活性炭の実際の吸着能力をみるた
めに、腸内で活性炭による有害物質の吸着を妨げ
るステアリン酸ナトリウムの存在下で次の実験を
おこなつた。
ステアリン酸ナトリウムをPH7.4のリン酸緩衝
液中に、腸内のステアリン酸ナトリウムの概算濃
度である2%の濃度に分散させ、更にクレアチニ
ンを前述の溶液に15ml/dlの濃度になるように溶
解した。次いで第1表の各試料を前述の溶液に加
え、3時間振り、その後混合物を5ml毎に分け
た。ステアリン酸を沈澱させる為に硫酸アルミニ
ウムの10%水溶液を3滴混合物に加えた後、表層
のクレアチニンの濃度を比色定量法によつて測定
した。比色定量法による測定工程以外はすべて37
℃の温度にて実験をおこなつた。
測定の結果を第5表に示す。
第5表から明らかな如く、本発明の球形活性炭
は比較試料(アンモニア処理をしていないもの)
に比べて優れた吸着能力を有している。この結
果、本発明の球形活性炭は、腸内で活性炭による
有害物質の吸着を妨げるステアリン酸ナトリウム
のような物質の存在下においても、クレアチニン
のような有害物質に対する吸収能力が優れている
ことが明らかである。[Table] Example 3 (Adsorption capacity) In order to examine the actual adsorption capacity of the spherical activated carbon of the present invention, the following experiment was conducted in the presence of sodium stearate, which prevents activated carbon from adsorbing harmful substances in the intestines. . Sodium stearate was dispersed in a phosphate buffer solution with a pH of 7.4 to a concentration of 2%, which is the approximate concentration of sodium stearate in the intestine, and creatinine was further added to the above solution at a concentration of 15 ml/dl. Dissolved. Each sample from Table 1 was then added to the above solution and shaken for 3 hours, after which time the mixture was divided into 5 ml portions. After adding 3 drops of a 10% aqueous solution of aluminum sulfate to the mixture to precipitate the stearic acid, the concentration of creatinine in the surface layer was determined by colorimetric method. All except the measurement process using colorimetric method are 37
The experiment was conducted at a temperature of ℃. The results of the measurements are shown in Table 5. As is clear from Table 5, the spherical activated carbon of the present invention is a comparative sample (not subjected to ammonia treatment).
It has superior adsorption ability compared to As a result, it is clear that the spherical activated carbon of the present invention has an excellent ability to absorb harmful substances such as creatinine even in the presence of substances such as sodium stearate that prevent activated carbon from adsorbing harmful substances in the intestine. It is.
【表】
チニンのmgの量
[Table] Amount of tinine in mg
Claims (1)
いで冷却した後、酸化して不融化し、次いで不活
性気体中で加熱炭化した後、水蒸気中で加熱して
賦活することによつて、少なくとも全量の85%が
真球である球形活性炭を製造する方法において、
該球形活性炭を1〜1000ppmのNH3を含有するア
ンモニア水溶液で、アンモニア水溶液と球形活性
炭の容積比を2〜10となし、10〜50℃の温度で
0.5〜5時間処理し、次いで100〜150℃の温度で
乾燥し、篩分けをすることによつて粒子間の最大
直径と最小直径の比が1〜1.3である球形活性炭
とすることを特徴とする経口解毒剤の製造方法。1. By molding pitches in a molten state into small spherical shapes, cooling them, oxidizing them to make them infusible, heating them in an inert gas to carbonize them, and then heating them in steam to activate them. In a method for producing spherical activated carbon in which 85% of the total amount is true spheres,
The spherical activated carbon was treated with an ammonia aqueous solution containing 1 to 1000 ppm of NH 3 at a volume ratio of 2 to 10 at a temperature of 10 to 50°C.
Treated for 0.5 to 5 hours, then dried at a temperature of 100 to 150°C, and sieved to obtain spherical activated carbon having a ratio of maximum diameter to minimum diameter between particles of 1 to 1.3. A method for producing an oral antidote.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8053779A JPS565313A (en) | 1979-06-26 | 1979-06-26 | Detoxificating spherical active carbon and preparing the same |
| CA000354378A CA1139673A (en) | 1979-06-26 | 1980-06-19 | Spherical particles of activated carbon suitable for use as an antidotal pharmaceutical composition |
| FR8014129A FR2459660A1 (en) | 1979-06-26 | 1980-06-25 | ACTIVE CARBON SPHERICAL PARTICLES USEFUL AS ANTIDOTE, PROCESS FOR THEIR PREPARATION AND PHARMACEUTICAL COMPOSITION CONTAINING THEM |
| GB8020864A GB2053176B (en) | 1979-06-26 | 1980-06-25 | Spherical particles of activated carbon suitable for use in a pharmaceutical composition |
| DE3023848A DE3023848C2 (en) | 1979-06-26 | 1980-06-25 | Pharmaceutical agent |
| IT23051/80A IT1131386B (en) | 1979-06-26 | 1980-06-26 | ACTIVATED CARBON SPHERICAL PARTICLES SUITABLE FOR USE IN PHARMACEUTICAL COMPOSITIONS AGAINST INTOXICATIONS |
| US06/759,933 US4761284A (en) | 1977-12-27 | 1985-07-29 | Antidote including activated carbon particles |
| JP62012799A JPS62223125A (en) | 1979-06-26 | 1987-01-22 | Antidote for oral administration |
| US07/047,291 US4822765A (en) | 1977-12-27 | 1987-05-08 | Process for treating activated carbon with aqueous ammonia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8053779A JPS565313A (en) | 1979-06-26 | 1979-06-26 | Detoxificating spherical active carbon and preparing the same |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62012799A Division JPS62223125A (en) | 1979-06-26 | 1987-01-22 | Antidote for oral administration |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS565313A JPS565313A (en) | 1981-01-20 |
| JPS6229368B2 true JPS6229368B2 (en) | 1987-06-25 |
Family
ID=13721096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8053779A Granted JPS565313A (en) | 1977-12-27 | 1979-06-26 | Detoxificating spherical active carbon and preparing the same |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JPS565313A (en) |
| CA (1) | CA1139673A (en) |
| DE (1) | DE3023848C2 (en) |
| FR (1) | FR2459660A1 (en) |
| GB (1) | GB2053176B (en) |
| IT (1) | IT1131386B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013051680A1 (en) | 2011-10-07 | 2013-04-11 | 帝人ファーマ株式会社 | Orally administered adsorbent |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3801457A1 (en) * | 1988-01-20 | 1989-08-03 | Hasso Von Bluecher | Activated carbon having high abrasion resistance and low moisture sensitivity |
| SU1706690A1 (en) * | 1988-04-19 | 1992-01-23 | Всесоюзный Научно-Исследовательский Институт Технического Углерода | Porous carbon material |
| DE3819000A1 (en) * | 1988-06-03 | 1989-12-14 | Hasso Von Bluecher | Bag of a teabag type for eliminating pollutants |
| JPH01309984A (en) * | 1988-06-08 | 1989-12-14 | Sanyo Electric Co Ltd | Method for preventing rusting of heat exchanger |
| IT1273678B (en) * | 1993-08-12 | 1997-07-09 | Bluecher Hasso Von | ACTIVATED CARBON PRODUCTION PROCESS |
| NL1000078C2 (en) * | 1994-04-19 | 1996-04-22 | Bluecher Hasso Von | Odor filter for vacuum cleaners. |
| SE509743C2 (en) * | 1994-06-17 | 1999-03-01 | Bluecher Hasso Von | Adsorptionsfilterskikt |
| SE515506C2 (en) * | 1994-06-17 | 2001-08-20 | Mhb Filtration Gmbh & Co Kg | Odor filter for ventilation outlet hoods |
| JPH10316578A (en) * | 1997-05-13 | 1998-12-02 | Kureha Chem Ind Co Ltd | Medicine for improving blood lipoprotein lipase activity-lowering disease |
| JPH1129485A (en) * | 1997-07-10 | 1999-02-02 | Kureha Chem Ind Co Ltd | Antiobestic medicine |
| JP3522708B2 (en) * | 2001-04-11 | 2004-04-26 | 呉羽化学工業株式会社 | Adsorbent for oral administration |
| US6830753B2 (en) | 2001-04-11 | 2004-12-14 | Kureha Chemical Industry Co., Ltd. | Adsorbent for oral administration |
| JP2003267715A (en) * | 2002-03-15 | 2003-09-25 | Osaka Gas Co Ltd | Activated carbon and its producing method |
| JP4311923B2 (en) * | 2002-10-07 | 2009-08-12 | 株式会社クレハ | Treatment or prevention agent for liver disease for oral administration |
| EP1407772B9 (en) * | 2002-10-09 | 2007-02-21 | Kureha Corporation | Pharmaceutical composition comprising porous spherical carbonaceous substance and its use for the treatment of renal and liver diseases |
| CA2504514C (en) * | 2002-11-01 | 2008-08-12 | Kureha Corporation | Adsorbent for oral administration |
| ES2285203T3 (en) * | 2002-11-01 | 2007-11-16 | Kureha Corporation | ADSORBENTS FOR ORAL, CURATIVE OR PREVENTIVE ADMINISTRATION FOR RENAL AND CURATIVE OR PREVENTIVE DISEASES FOR HEPATIC DISEASES. |
| US7651974B2 (en) | 2002-11-01 | 2010-01-26 | Kureha Chemical Industry Co., Ltd. | Adsorbent for oral administration |
| JP3585043B2 (en) * | 2003-01-22 | 2004-11-04 | メルク・ホエイ株式会社 | Pharmaceutical adsorbent and its production method |
| KR101135260B1 (en) | 2003-10-22 | 2012-04-12 | 가부시키가이샤 쿠레하 | Adsorbent for oral administration, and agent for treating or preventing renal or liver disease |
| JP2005162683A (en) * | 2003-12-03 | 2005-06-23 | Kureha Chem Ind Co Ltd | Therapeutic or prophylactic agent for hyperuricemia |
| TWI370013B (en) | 2004-04-02 | 2012-08-11 | Kureha Corp | Adsorbent for oral administration, and agent for treating or preventing renal or liver disease |
| TWI370012B (en) | 2004-04-02 | 2012-08-11 | Kureha Corp | Adsorbent for oral administration, and agent for treating or preventing renal or liver disease |
| JP2005015482A (en) * | 2004-06-07 | 2005-01-20 | Koki Bussan Kk | Adsorbent removal agent for harmful substances |
| DE102005062160A1 (en) * | 2005-12-19 | 2007-06-21 | BLüCHER GMBH | Activated charcoal for medical use |
| US8247072B2 (en) | 2006-02-14 | 2012-08-21 | Eastman Chemical Company | Resol beads, methods of making them and methods of using them |
| US20080041643A1 (en) * | 2006-08-17 | 2008-02-21 | Khalife Tony N | Wind-power vehicle aka WPV |
| JP5984352B2 (en) * | 2010-10-12 | 2016-09-06 | フタムラ化学株式会社 | Method for producing pharmaceutical adsorbent for oral administration |
| JP5985027B2 (en) * | 2010-10-12 | 2016-09-06 | フタムラ化学株式会社 | Method for producing pharmaceutical adsorbent for oral administration |
| WO2018116947A1 (en) * | 2016-12-21 | 2018-06-28 | 株式会社クレハ | Spherical activated carbon and method for producing same |
| JP6637573B2 (en) * | 2017-12-18 | 2020-01-29 | フタムラ化学株式会社 | Adsorbent production method |
| CN111511466B (en) * | 2017-12-28 | 2022-06-24 | 株式会社可乐丽 | Adsorption filter |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5018879A (en) * | 1973-06-20 | 1975-02-27 | ||
| US3917821A (en) * | 1973-10-23 | 1975-11-04 | Milton Manes | Palatable activated carbon |
| JPS53113193A (en) * | 1977-03-14 | 1978-10-03 | Asahi Chemical Ind | Activated charcoal for artificial viscera |
| JPS5489010A (en) * | 1977-12-27 | 1979-07-14 | Kureha Chem Ind Co Ltd | Spherical activated charcoal antidote |
-
1979
- 1979-06-26 JP JP8053779A patent/JPS565313A/en active Granted
-
1980
- 1980-06-19 CA CA000354378A patent/CA1139673A/en not_active Expired
- 1980-06-25 FR FR8014129A patent/FR2459660A1/en active Granted
- 1980-06-25 DE DE3023848A patent/DE3023848C2/en not_active Expired
- 1980-06-25 GB GB8020864A patent/GB2053176B/en not_active Expired
- 1980-06-26 IT IT23051/80A patent/IT1131386B/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013051680A1 (en) | 2011-10-07 | 2013-04-11 | 帝人ファーマ株式会社 | Orally administered adsorbent |
Also Published As
| Publication number | Publication date |
|---|---|
| IT1131386B (en) | 1986-06-18 |
| JPS565313A (en) | 1981-01-20 |
| IT8023051A0 (en) | 1980-06-26 |
| FR2459660B1 (en) | 1983-11-25 |
| GB2053176B (en) | 1983-03-09 |
| GB2053176A (en) | 1981-02-04 |
| FR2459660A1 (en) | 1981-01-16 |
| CA1139673A (en) | 1983-01-18 |
| DE3023848A1 (en) | 1981-01-08 |
| DE3023848C2 (en) | 1985-10-24 |
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