JPS62223125A - Antidote for oral administration - Google Patents

Antidote for oral administration

Info

Publication number
JPS62223125A
JPS62223125A JP62012799A JP1279987A JPS62223125A JP S62223125 A JPS62223125 A JP S62223125A JP 62012799 A JP62012799 A JP 62012799A JP 1279987 A JP1279987 A JP 1279987A JP S62223125 A JPS62223125 A JP S62223125A
Authority
JP
Japan
Prior art keywords
activated carbon
spherical
spherical activated
diameter
surface area
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
JP62012799A
Other languages
Japanese (ja)
Other versions
JPS6360009B2 (en
Inventor
Yasushi Nishimura
西村 寧
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kureha Corp
Original Assignee
Kureha Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from JP8053779A external-priority patent/JPS565313A/en
Application filed by Kureha Corp filed Critical Kureha Corp
Priority to JP62012799A priority Critical patent/JPS62223125A/en
Publication of JPS62223125A publication Critical patent/JPS62223125A/en
Publication of JPS6360009B2 publication Critical patent/JPS6360009B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To provide a peroral antidote containing an NH3-treated spherical activated carbon having specific particle diameter, surface area, pore volume and pH as an active component, free from side effect of constipation and exhibiting excellent antidotal effect. CONSTITUTION:An activated carbon of minute spherical form having a diameter of 0.05-2mm, a surface area of 500-2,000m<2>/g a pore volume of 0.05-1ml/g corresponding to pore radius of 100-75,000Angstrom and pH of 8-10 is produced e.g. by forming small spheres of pitch in molten state, oxidizing and infusibilizing the spherical pitch, carbonizing in an inert atmosphere at 800-1,000 deg.C and activating in steam atmosphere at 900-1,000 deg.C. The produced activated carbon is made to contact with an aqueous solution of NH3 and dried to obtain activated carbon having 6-8pH and the same shape as above. >=85% of the obtained activated carbon has true spherical form wherein the ratio of the maximum diameter and the minimum diameter is 1-1.3. A particular surface can be obtained by the NH3-treatment to acquire excellent adsorptivity compared with a conventional activated carbon.

Description

【発明の詳細な説明】 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3:系から汚物あるいは付言物′
a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。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for removing waste from the system, comprising spherical activated carbon in which at least 85% of the activated carbon is true spheres.
The present invention relates to spherical activated carbon suitable for removing and detoxifying a and its production method.

更に訂しく(ま、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
って解毒する際に、従来から問題とされていた便泌性副
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
More precisely (well, the present invention eliminates the fecal secretion side effects that have traditionally been a problem when taking activated charcoal to detoxify harmful substances that exist or are produced within the digestive system such as the stomach and intestines). 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.

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、萎黄病及び炭痕病等に対して、特に優れた治療
効果を丞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伴う代謝異常により生成する消化器
系内の有毒物質の除去に対しても効果的である。
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, you can prevent dysentery, cholera, typhoid fever, bacterial infections such as food poisoning, indigestion, intestinal tension, chronic gastritis, epilepsy,
It has been reported that it has particularly excellent therapeutic effects on dizziness, yellowing disease, charcoal scar disease, etc. Also, drugs,
When ingesting poisonous substances, activated charcoal is taken as an emergency measure to have a detoxifying effect. Furthermore, taking activated charcoal,
It is also effective in removing toxic substances in the digestive system that are produced due to metabolic abnormalities associated with various other diseases.

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
対して全く重性のない活性炭に吸着され、活性炭と共に
体外に刊出されるためと考えられている。
These effects are due to the fact that toxins, abnormal metabolites, or substances that produce toxins or cause metabolic abnormalities in the digestive system are adsorbed to activated carbon, which has no weight to living organisms, and are released outside the body along with activated carbon. It is believed that.

従来、この解ff1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一緒に服用す
るか、適当な錠剤として服用されていた。
Conventionally, powdered activated carbon has been used for the purpose of this eff1 effect, and this powdered activated carbon has been taken with water or in the form of a suitable tablet.

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
一緒に服用した場合と同等の吸着能力を発現でる。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った。1.1に活
性炭は通常、各種疾患に際して服用づるものであるから
、患菖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とにとって著しい苦痛であるばか
りでなく、患名が充分な1ノ[胆力を有していない場合
には、)1械的にこれを除去しなければ、生命に関づる
場合も生じ11するという欠点を従来の活性炭は有して
い lこ 。
Even when taken as a tablet, it is unlocked within the body and turns into powder, which exhibits the same adsorption capacity as when taken with water. However, the use of powdered activated carbon causes constipation as a side effect, which is a major drawback. 1.1 Since activated charcoal is usually taken for various diseases, the physical strength of the patient is often exhausted, and constipation that occurs as a side effect is not only extremely painful for the patient. Conventional activated charcoal has the disadvantage that if the patient does not have enough courage to remove it mechanically, it may become life-threatening. lko.

このような状況に鑑み、本発明化は、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、
(傷れた解毒作用をイボ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。
In view of this situation, in order to solve the above-mentioned drawbacks, the present invention has been developed as a result of intensive research, and has been developed to solve the above-mentioned drawbacks.
A particular spherical activated carbon, preferably 90% true spheres,
(The present invention was achieved by discovering that the detoxifying effect of the detoxifying agent can be reversed and that it does not cause constipation side effects.

本発明による解毒剤は、2工程からなる次に記載の方法
によって高分子量炭化水素、例えばピッチから製造され
る。
The antidote according to the invention is prepared from high molecular weight hydrocarbons, such as pitch, by the following two-step process.

第一工程では、ピッ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、次いで水魚゛気雰囲気中で
900〜1000℃の温度で賦活して、直径0.05〜
2H,表面積500〜2000m / !7 、細孔半
径10(1−75000人の範囲テノ細孔容積0.05
〜1.0ml/ g 、 pH=8〜10の微小球形活
性炭を製造する。
In the first step, the pitch is made into small spherical shapes in a molten state, cooled, oxidized to make it infusible, and then heated to 800~
Carbonized at a temperature of 1000°C, then activated at a temperature of 900-1000°C in an aquatic atmosphere to form a diameter of 0.05-1000°C.
2H, surface area 500-2000m/! 7, pore radius 10 (1-75000 people range teno pore volume 0.05
Produce microspherical activated carbon with ~1.0 ml/g, pH=8-10.

第二工Pdでは、これらの球形活性炭をN +−13を
1〜1000 ppm好ましくは5〜100 ppm含
右する希アンモニア水溶液で接触処理し乾燥して、アン
モニア処理を行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[ニア処理する前の球形活性
炭に比較してp 11 = 6〜8の微小球形活性炭を
製造づる。
In Dainiku Pd, these spherical activated carbons are contacted with a dilute ammonia aqueous solution containing 1 to 1000 ppm of N+-13, preferably 5 to 100 ppm, and dried to form the same spherical activated carbon as before ammonia treatment. Microspherical activated carbon having a diameter, surface area and pore volume of p 11 = 6 to 8 compared to the spherical activated carbon before annealing is produced.

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っており、この活性炭は、めだっ
たかどのない、滑らかな凸表面を有してJ5す、最大直
径と7,1小直径の割合が1,0〜13である。
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, a maximum diameter of J5, and a maximum diameter of 7.1. The proportion of small diameter is 1.0-13.

球形活性炭の粒径(直径)が0.05+m以下では解毒
作用はあっ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2厘以上になると、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。
If the particle size (diameter) of the spherical activated carbon is 0.05+m or less, even if it has a detoxifying effect, it is not sufficiently effective in eliminating constipation side effects. Furthermore, if the particle size of the spherical activated carbon exceeds 2 centimeters, it will not only be difficult to take, but also the desired detoxifying effect will not be achieved quickly.

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′dに球形である
ことが必要である。更に、詳しくは、h古性炭の少なく
とも85%が真課であることが必要である。
The shape of the activated carbon is one important factor in obtaining the satisfactory pharmaceutical effects of the present invention, and in fact it is necessary that it be spherical. More specifically, it is necessary that at least 85% of the aged coal be true grains.

形状と同様に、活性炭の表面積及び細孔容1?4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、細孔容積が小さずぎると吸着力が弱くなり実用」−
充分な解毒効果は1!7られず、また表面積、細孔容積
が大きすぎると解1作用はあっても便秘現象を伴うこと
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
形状が崩れ粉化を伴うことも便秘性副作用を生ずる原因
と考えられる。
Similar to the shape, the surface area and pore volume of activated carbon (1-4) 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, making it difficult to put into practical use.
A sufficient detoxification effect cannot be achieved, and if the surface area and pore volume are too large, constipation will occur even if the detoxification effect is achieved. Furthermore, when the surface area and pore volume of the activated carbon are larger than the ranges 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.

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、500〜200074/3.
好ましくは700〜1500況、/gである。細孔容積
は、市販の水銀圧入ポロシメーターで測定すると、細孔
半径100〜75000人の領域でO,OS〜1.0m
/41?、好ましくは0.1〜0.8 d/びである。
The surface area of the microspherical activated carbon of the present invention is 500 to 200074/3 when measured using a commercially available surface area measuring device.
Preferably it is 700-1500 g. When measured with a commercially available mercury intrusion porosimeter, the pore volume is O, OS ~ 1.0 m in the pore radius range of 100 to 75,000 m.
/41? , preferably 0.1 to 0.8 d/d/d.

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、ピッチ類、有機合成高分子
等の公知の原料のいずれでもよく、これらの物71から
球形活性炭を製造することができる。
As raw materials used for producing activated carbon having such characteristics, any known raw materials such as sawdust, coal, coconut shells, pitches, organic synthetic polymers, etc. may be used, and spherical activated carbon can be produced from these materials 71. I can do it.

例えば、初期の球形活性炭を製造する方法としては、粉
末原料をピッ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。
For example, the initial method for manufacturing spherical activated carbon was to granulate powdered raw materials into small spherical shapes using a binder such as pitch, then heat and sinter them at 800 to 1000°C in an inert atmosphere to carbonize them, and then carbonize them in a steam atmosphere. Inside 900-・1000
There is a method of activating at °C.

一方、例えば特公昭50−18879に開示されている
方法ににす、ピッチ類を熔融状態で小粒球形とし次いで
酸化により不融化だ後、不活性雰囲気中で800〜10
00℃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。
On the other hand, for example, by the method disclosed in Japanese Patent Publication No. 50-18879, pitches are made into small spherical shapes in a molten state, and after being made infusible by oxidation, they are
Carbonized by heating and firing at 00°C and heated to 900°C in a steam atmosphere.
Spherical activated carbon can be produced by a method of activation at ~1000°C.

特に、少者の方法では真球度の高い、高強度の表面の滑
らかな球形活性炭が得られるので、本発明の活性炭の製
jTXi方法として好適である。
In particular, the method of the present invention is suitable as the jTXi method for producing activated carbon of the present invention, since it yields spherical activated carbon with high sphericity, high strength, and a smooth surface.

本発明の微小球形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1】11は、通常
n11=8〜10であるが、これをpl+=6〜8に変
える。この第二工程の処理をすることによって球形活性
炭はを1れた性質をもつようになる。
The second step of the method for producing microspherical activated carbon of the present invention is a particularly important process. 1]11 of spherical activated carbon is normally n11=8 to 10, but this is changed to pl+=6 to 8. By performing this second step, the spherical activated carbon has improved properties.

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って異なるが、通常は、アンモ
ニア水溶液のNH3の濃度は1〜10001)l)m、
好ましくは5〜100 ppm 、アンモニア水溶液と
球形活性炭の各船割合は1〜50.好ましくば2へ・1
0で、処理温度は10〜50°Cで、処理時間は0.5
〜5時間である。アンモニア水溶液中のN i−13の
濃度が上述した範囲、」;り高くなると生成物のpl+
も高くなって、アルカリ領域となり、またN[13の濃
度が低くなると生成物のpHはアルカリ領域に残る。
The conditions for treatment with an ammonia aqueous solution vary depending on the state of the steam-treated spherical activated carbon, but usually the NH3 concentration of the ammonia aqueous solution is 1 to 10,001) l)m,
Preferably, it is 5 to 100 ppm, and the proportion of ammonia aqueous solution and spherical activated carbon is 1 to 50 ppm. Preferably go to 2/1
0, the processing temperature is 10-50°C, and the processing time is 0.5
~5 hours. When the concentration of N i-13 in the aqueous ammonia solution increases within the above-mentioned range, the pl+ of the product increases.
As the concentration of N[13 increases, the pH of the product remains in the alkaline region, and as the concentration of N[13 decreases.

アルカリ性を示す球形活性炭が、アルカリ試薬、すなわ
ら、アンモニア水溶液と接触させることによって酸性−
中性の球形活性炭に変わる理由は明らかではナク、更に
このようなpl+の変化は全く予期ぜぬことであった。
Spherical activated carbon that exhibits alkalinity becomes acidic by contacting it with an alkaline reagent, such as an aqueous ammonia solution.
The reason for the change to neutral spherical activated carbon is not clear, and furthermore, such a change in pl+ was completely unexpected.

次に、このようにアンモニア水溶液によって処理された
球形活性炭を通常100・〜・150℃の温度で乾燥し
、服用に適する4ノ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。
Next, the spherical activated carbon thus treated with the ammonia aqueous solution is dried at a temperature of usually 100 to 150°C, and sieved into four sizes suitable for administration. Adjusting the product to a uniform size, ie sieving to a range of sizes, is preferred for dosing.

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19るために、アンモニア
水溶液処理を行う前に、行われる。
For sieving, the ratio of the diameter of the largest particle to the smallest particle is 1 to 1.
In order to obtain spherical activated carbon as shown in Example 3, it is carried out before the ammonia aqueous solution treatment.

何れの場合においてb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
勿論であって例えば、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。
In any case, since the spherical activated carbon is to be taken, it must of course be of sufficient purity for safety.
It must pass the purity test specified in section .

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筒中であるが、
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どし
ての効果を示づ様、体内で元の球形活性炭粒子に解錠さ
れる必要がある。
The method for taking the spherical activated carbon according to the present invention may be the same known method as for ordinary activated carbon. The most convenient method is to suspend the microspherical activated carbon according to the present invention in drinking water.
Spherical activated carbon may be taken as a suitably shaped tablet in a conventional manner. However, in this case, of course, the spherical activated carbon of the present invention needs to be unlocked into the original spherical activated carbon particles within the body in order to exhibit its effects.

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bよい。
It may also be taken in a conventional cylindrical capsule in a conventional manner.

球形活性炭の服用mは、疾患の程度、緊急解毒の必要性
等によっても異なるが通常1回、0.5〜109.1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。
The dosage m of spherical activated carbon varies depending on the severity of the disease, the need for emergency detoxification, etc., but is usually once, about 0.5 to 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.

本発明の球形活性炭が解毒作用を維持しかつ伊那性副作
用の除去に著しい効果を示すことは全く予期しくqなか
ったことで、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って表面が4S7殊な
状態になっているため、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
取した植物、消化した植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!i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、擾れた吸着
能力を右する。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1.j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ぎたざないとも推定される。
It was completely unexpected that the spherical activated carbon of the present invention maintains its detoxification effect and shows a remarkable effect on eliminating side effects of inertia, and although the cause is still not clear, the spherical activated carbon of the present invention can be effectively treated with ammonia. Since the surface is in a special state, it has the ability to adsorb exogenous and endogenous harmful substances. That is, the spherical activated carbon of the present invention can be used in the presence of ingested plants, digested plants, and their digested products, as well as conventional powdered activated carbon or! The adsorption capacity of powdered activated carbon is reduced compared to that of spherical or lumped activated carbon. 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, the spherical activated carbon of the present invention has different surface properties. Because it is a smooth sphere, it does not have the effect of increasing the cohesive force of stool, and at the same time, it does not adsorb substances that stimulate intestinal motility, and the spherical activated carbon provides moderate stimulation to the intestines, which has the combined effect of preventing constipation. It is also estimated that there is no gap.

以下、実施例によって本発明の詳細な説明するが、同等
本発明の節回を限定するものではない。
Hereinafter, the present invention will be explained in detail with reference to examples, but the scope of the present invention is not limited to the equivalent examples.

実施例−1(球形活性炭の製゛″I 原油の0′f:A分解により19られたピッチ(軟化点
175℃、ニトロベンゼン不溶分25%、l−1/C元
索比0.133)  750部、ナフタレン250部を
撹拌1 (qステンレス製オートクレーブに仕込み、1
70℃で混喬溶解し、これに「ゴーセノールGH−17
J(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、撹拌下に空温まで冷却し、真球状の球
形粒子を19た。大部分の水を戸別した後、粒子重量の
518最のメタノールに浸漬、振盪してブフクレンを抽
出除去した後通風乾燥し、次いで、小型に1−タリー・
キルン中で空気を送入しながら25℃/11rで300
℃まで7i+温して不触性の球形粒子を1[また。次い
で空気送入を停止し、代りに水蒸気を送入しながら90
0℃まで胃温することによって炭化し、更にこの温度に
保つことによって賦活を進めて、粒径0,1〜15mの
真球性の高い球形活性炭を (!7 Iこ 。
Example-1 (Production of spherical activated carbon "I" Pitch obtained by 0'f:A decomposition of crude oil (softening point 175°C, nitrobenzene insoluble content 25%, l-1/C ratio 0.133) 750 Stir 1 part and 250 parts of naphthalene in a stainless steel autoclave.
Mix and dissolve at 70°C, and add "GOHSENOL GH-17" to this.
J (polyvinyl alcohol suspending agent manufactured by Nippon Gohsei) 0.
After adding 3,000 parts of a 5% aqueous solution and stirring vigorously at 130° C. for 60 minutes, the mixture was cooled to air temperature while stirring to obtain 19 true spherical particles. After most of the water was removed, the particles were immersed in 518 particles of methanol, shaken to extract and remove Bufculen, and then dried with ventilation.
300 at 25℃/11r while blowing air in the kiln
Warm to 7i+°C to form inaccessible spherical particles at 1 [Also. Then, the air supply was stopped and steam was supplied instead for 90 minutes.
It is carbonized by warming the stomach to 0℃, and further activated by keeping it at this temperature, producing highly spherical activated carbon with a particle size of 0.1 to 15 m (!7 I).

賦活時間を変えることにJ:って賦活の程度が異なった
2種の球形活性炭を%J JMした。
By changing the activation time, two types of spherical activated carbon with different degrees of activation were analyzed.

比較試jThlNo、1は賦活度の低いものであり、比
較試料N002は賦活度の高いものであり、共に球形リ
イズをふるいわけにて整えたものである。
Comparative sample j ThlNo. 1 has a low activation degree, and comparative sample No. 002 has a high activation degree, and both have spherical beads prepared by sieving.

次に、比較試rANo、 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10 p
pm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/重聞比が10d/1びで、室温下3時
間浸漬した。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。
Next, a portion of each of the spherical activated carbons of Comparative Sample rA No. 1 and Comparative Sample No. 2 was added at a concentration of NH3 of 10 p.
The spherical activated carbon was immersed in an ammonia aqueous solution with a volume/weight ratio of 10 d/1 at room temperature for 3 hours. Next, take out the spherical activated carbon from the solution,
Drying at a temperature of 110° C. for 16 hours produced spherical activated carbon.

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おl
No、2とする。
The product from activated carbon with a low degree of activation was sample No. 1.
Try products from activated carbon with a high degree of activation.
No, set as 2.

これら4つの活性炭の特性を表−1に示す。Table 1 shows the properties of these four activated carbons.

尚、吸着能力は試験管内試験によって、クレアチニン及
び尿酸に対する吸着能力をてれでれ測定した。前述の2
つの物質は、腎疾患等の代謝責常で体内に生成する有害
物質としてよく知られているしのである。
In addition, the adsorption ability was measured by an in vitro test for adsorption ability for creatinine and uric acid. 2 mentioned above
These substances are well known as harmful substances that are produced in the body due to metabolic disorders such as kidney disease.

第1 表  球形活性炭試v1の特性 (注)4=1   細孔半径ioo〜75000人の範
囲の細孔容積を水銀圧入ポロシメーター ”Porosimetro Model 70” (イ
タリア、 Carlo Erba社製)により測定。
Table 1 Characteristics of spherical activated carbon test v1 (Note) 4 = 1 The pore volume in the range of pore radius ioo to 75,000 pores was measured using a mercury intrusion porosimeter "Porosimetro Model 70" (manufactured by Carlo Erba, Italy).

*2  リン酸塩緩衝液においてpH7,4で基質の5
■/(1ρの濃度で測定。
*2 5 of the substrate at pH 7.4 in phosphate buffer
■/(Measured at a concentration of 1ρ.

*3  球形活性炭のpllは、日本薬局法(第九改正
)「薬用炭」に記載されてい る7J法に従って測定した。
*3 The pll of the spherical activated carbon was measured according to the 7J method described in the Japanese Pharmacopoeia Law (9th revision) "Medicinal Charcoal".

試v+、 3びを60dの蒸留水に浸し、5分間沸騰し
、次いで冷fJI後、蒸発によって減少した伍の蒸留水
を加え、 口別復、液相のpllを測定した。
Samples V+ and 3 were immersed in 60 d of distilled water, boiled for 5 minutes, and then after cold fJI, 50 ml of distilled water, which had been reduced by evaporation, was added, and the pll of the liquid phase was measured.

測定されたpllの値を試IIのpll値として使用す
る。
The measured pll value is used as the pll value of Trial II.

尚、何れの試料も日本薬局法(第九改正)「薬用炭」の
純度試験、乾燥域T、強熱残分の各基準に適合した。
All samples met the standards for purity test, drying range T, and ignition residue of "medicinal charcoal" under the Japanese Pharmacopoeia Act (9th revision).

(急性毒性試験〕 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りしても極めて安全性の高いも
のであることを確認した。
(Acute toxicity test) An acute toxicity test was conducted using mice for the samples shown in Table 1.The results are shown below, and the spherical activated carbon of the present invention is extremely safe even when thrown in large quantities. It was confirmed that the value was high.

実験動物として、市販I CR、、−J CL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、Litcl+ricld−14tlcoxo
n法からLDsoを求めた。結果を第2表に示づ一01
週間後、解則したが、外観的及び内臓!IQ察において
も特記づべき異常所見を認めず又特記すべき中m症状も
認められなかった。
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 probe. Litcl+ricld-14tlcoxo was determined by the determination of life and death after one week.
LDso was determined using the n method. The results are shown in Table 2.
After a week, it was resolved, but the appearance and internal organs were fixed! No noteworthy abnormal findings were found in the IQ test, nor were there any noteworthy symptoms of mediocrity.

第2表 急性毒性試験 (注)  15,0OOfn9/に9以上の投与は実験
上、非常に困難であったので、本投与最で試 験を打切った。1500011tg/ KFIの投与で
、マウスの死亡例はなかった。
Table 2 Acute Toxicity Test (Note) As it was experimentally extremely difficult to administer doses of 9 or more to 15,0OOfn9/, the test was discontinued at the end of this administration. There were no deaths of mice after administration of 1500011 tg/KFI.

実流例−2(動物実験) 体ffl 130〜140 t)のウィスター(Wis
tar)系IIラッ1−を用い、ベントパルビタールー
Naを2oIyJ/に9体重になるように水溶液として
経口投与した。
Actual flow example-2 (animal experiment) Wistar (body ffl 130-140t)
Bentoparvital-Na was orally administered in the form of an aqueous solution to 2 oIyJ/9 body weight using a series II rat 1-.

次いで直ちに第1表に示した試料を水懸濁液どして20
0#l!J/句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石に10匹ずつ使用した。
Immediately, the samples shown in Table 1 were suspended in water for 20 minutes.
0#l! The animals were orally administered to achieve a body weight of J/kg. 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.

次いで血中のベンドパルビタール1’J aの最大潤度
の平均[直を求め比較試験群での濃度に対する割合を除
去率として口出した結果は第3表の通りである。
Next, the average maximum moisture content of bendoparbital 1'Ja in the blood was determined, and the ratio to the concentration in the comparison test group was expressed as the removal rate.The results are shown in Table 3.

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N02(アンしニア処理したしの)は
、比較試ilo、1及びNo、2 (アンモニア処理を
しないもの)に比較して特に顕署イヱ解毒効果を右して
いた。
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 (treated with ammonia) have particularly high detoxification effects compared to comparative samples Ilo, 1 and No. 2 (not treated with ammonia). Ta.

次いで、活性炭の投与から90分後にこれ等の検体I!
Yを麻酔化ざt!演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、鳴門から直腸末端までの仝艮に
対J゛る活性炭到達部までの移送距ρR1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8Yでは、イの移
送率が大きく、伊那作用の少ないことが示された。
Then, 90 minutes after administration of activated charcoal, these specimens I!
Anesthetize Y! The enzymatic tube was removed and the degree of intestinal transport of activated charcoal was compared. That is, the ratio of the transfer distance ρR1 from Naruto to the terminal end of the rectum to the activated carbon reach point was determined as the transfer rate. As shown in Table 4, the results show that in sample 8Y using the activated carbon sample of the present invention shown in Table 1, the transfer rate of A was large and the Ina effect was small.

第4表 活性炭試料の腸内移送率 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った。
Table 4: Intestinal transport rate of activated carbon sample 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 the activated carbon from adsorbing harmful substances in the intestine.

ステアリン酸ナトリウムをpl+ 7.4のリン酸緩衝
液中に、腸内のステアリン酸ナトリウムのII C3j
2度である2%の濃度に分散さけ、更にクレアチニンを
前述の溶液に15ate/dρ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。
II C3j of sodium stearate in the intestine in phosphate buffer of pl+ 7.4
Creatinine was further dissolved in the above solution to a concentration of 15 ate/dρ. Each sample from Table 1 was then added to the above solution and shaken for 3 hours, after which the mixture was divided into 5 ml portions.

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3W4混合物に加えた侵、表層のクレアチニ
ンの濃度を比色窓4法によって測定した。
10 of aluminum sulfate to precipitate the stearic acid.
% aqueous solution was added to the 3W4 mixture, and the concentration of creatinine in the surface layer was measured by the colorimetric window 4 method.

比色足間法による測定工程以外はすべて37℃の温度に
て実験をおこなった。
All experiments were conducted at a temperature of 37° C. except for the measurement step using the colorimetric interleaving method.

測定の結果を第5表に示づ。The measurement results are shown in Table 5.

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)に比べて模れた
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ら、ク
レアチニンのような有害物質に対する吸収能力が1・9
れていることが明らかである。
As is clear from Table 5, the spherical activated carbon of the present invention has a similar adsorption capacity compared to the comparative sample (not treated with ammonia). As a result, the spherical activated carbon of the present invention has an absorption capacity of 1.9% for harmful substances such as creatinine in the presence of substances such as sodium stearate that prevent activated carbon from adsorbing harmful substances in the intestine.
It is clear that

Claims (1)

【特許請求の範囲】[Claims] (1)球形活性炭の少なくとも85%が真球であって、
粒子の最大径と最小径の比が1.0〜1.3、直径0.
05〜2.0mm、表面積500〜2000m^2/g
、細孔半径100〜75000Åにおける細孔容積0.
05〜1.0ml/g、pH=6〜8の特性を有する、
アンモニア処理された経口解毒剤。
(1) At least 85% of the spherical activated carbon is a true sphere,
The ratio of the maximum diameter to the minimum diameter of the particles is 1.0 to 1.3, and the diameter is 0.
05~2.0mm, surface area 500~2000m^2/g
, the pore volume at a pore radius of 100 to 75,000 Å is 0.
05-1.0ml/g, pH=6-8,
Ammoniated oral antidote.
JP62012799A 1979-06-26 1987-01-22 Antidote for oral administration Granted JPS62223125A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62012799A JPS62223125A (en) 1979-06-26 1987-01-22 Antidote for oral administration

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP8053779A JPS565313A (en) 1979-06-26 1979-06-26 Detoxificating spherical active carbon and preparing the same
JP62012799A JPS62223125A (en) 1979-06-26 1987-01-22 Antidote for oral administration

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP8053779A Division JPS565313A (en) 1977-12-27 1979-06-26 Detoxificating spherical active carbon and preparing the same

Publications (2)

Publication Number Publication Date
JPS62223125A true JPS62223125A (en) 1987-10-01
JPS6360009B2 JPS6360009B2 (en) 1988-11-22

Family

ID=26348471

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62012799A Granted JPS62223125A (en) 1979-06-26 1987-01-22 Antidote for oral administration

Country Status (1)

Country Link
JP (1) JPS62223125A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
JP2002308785A (en) * 2001-04-11 2002-10-23 Kureha Chem Ind Co Ltd Oral administration adsorbent
EP1748031A1 (en) * 2004-04-02 2007-01-31 Kureha Corporation Method for producing spherical activated carbon
WO2010018855A1 (en) * 2008-08-14 2010-02-18 ソニー株式会社 Drug sustained release agent, adsorbent, functional food, mask, and adsorptive sheet

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI370012B (en) * 2004-04-02 2012-08-11 Kureha Corp Adsorbent for oral administration, and agent for treating or preventing renal or liver disease
JP5781164B2 (en) 2011-10-07 2015-09-16 帝人ファーマ株式会社 Adsorbent for oral administration

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
JP2002308785A (en) * 2001-04-11 2002-10-23 Kureha Chem Ind Co Ltd Oral administration adsorbent
EP1748031A1 (en) * 2004-04-02 2007-01-31 Kureha Corporation Method for producing spherical activated carbon
EP1748031A4 (en) * 2004-04-02 2011-03-09 Kureha Corp Method for producing spherical activated carbon
WO2010018855A1 (en) * 2008-08-14 2010-02-18 ソニー株式会社 Drug sustained release agent, adsorbent, functional food, mask, and adsorptive sheet
JP2010106007A (en) * 2008-08-14 2010-05-13 Sony Corp Drug sustained-release agent, adsorbent, functional food, mask and adhesive sheet

Also Published As

Publication number Publication date
JPS6360009B2 (en) 1988-11-22

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