JPH0422618B2 - - Google Patents

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Publication number
JPH0422618B2
JPH0422618B2 JP62210714A JP21071487A JPH0422618B2 JP H0422618 B2 JPH0422618 B2 JP H0422618B2 JP 62210714 A JP62210714 A JP 62210714A JP 21071487 A JP21071487 A JP 21071487A JP H0422618 B2 JPH0422618 B2 JP H0422618B2
Authority
JP
Japan
Prior art keywords
activated carbon
adsorbent
tio
mgo
composite
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 - Lifetime
Application number
JP62210714A
Other languages
Japanese (ja)
Other versions
JPS6456141A (en
Inventor
Susumu Okazaki
Hiroshi Endo
Kuniaki Hino
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
Application filed by Kureha Corp filed Critical Kureha Corp
Priority to JP62210714A priority Critical patent/JPS6456141A/en
Priority to ES88307827T priority patent/ES2054816T3/en
Priority to US07/235,415 priority patent/US4988569A/en
Priority to DE8888307827T priority patent/DE3881141T2/en
Priority to EP88307827A priority patent/EP0311244B1/en
Priority to CA000575490A priority patent/CA1324601C/en
Priority to KR1019880010842A priority patent/KR910004018B1/en
Publication of JPS6456141A publication Critical patent/JPS6456141A/en
Publication of JPH0422618B2 publication Critical patent/JPH0422618B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 [発明の技術分野] 本発明は、石油系又は石炭系ピツチ、有機合成
高分子類等から得られる球状あるいは粒状活性炭
若しくはヤシ殻炭、造粒炭等の活性炭に、MgO
−TiO2複合物を添着(担持)してなる吸着剤に
係る。 [発明の技術的背景] 腎臓や肝蔵に機能障害をもつ患者では、代謝老
廃物等の体外排泄能が不十分となり、これ等の物
質が体内に蓄積され、結果として種々の生理的障
害を生じている。従つて、これ等の機能障害者の
病態改善には、一般に代謝老廃物等を生体から取
り除くことが行なわれている。 例えば、腎機能障害者の典型として腎不全患者
が知られているが、この患者に対しては、現在、
透析膜を用いる血液浄化法或いは活性炭を用いる
血液潅流法等の治療法が施されている。 ところで腎不全患者では、尿中へのリン排泄機
能の低下に伴う高リン血症の併発が問題となつて
いるが、前記した従来の治療法では高リン血症の
病態を改善し得ないでいる。即ち、前者の透析膜
による血液浄化法は血中のリン濃度を十分に抑制
し得るものではなく、しかも高リン血症の最大要
因であるリンの腸管吸収に対しては全く無力であ
る。一方、後者の活性炭を用いる治療法ではリン
等の無機物質に対する吸着力が非常に劣るという
活性炭自身の特性上の問題を有している。 [発明の目的] 本発明者等は、前記実情に鑑み、活性炭の吸着
性能を損なうことなく、しかもリンの吸着特性に
優れる新規な吸着剤の提供を目的とし鋭意検討し
た結果、活性炭表面にMgO−TiO2複合物が添着
された吸着剤が極めて合目的であることを見い出
し、本発明の完成に至つた。 [発明の構成及び効果] 上記知見に基づく本発明は、活性炭にMgO−
TiO2複合物を添着してなる吸着剤(以下本発明
の吸着剤と称する)に係る。 本発明者等は、MgO−TiO2複合物リンに対し
て選択的な吸着特性を有することから、該複合物
を抗高リン血症剤として同日出願している。本発
明は前記同日出願の吸着剤を更に発展せしめたも
のである。即ち、本発明の吸着剤は活性炭の有す
る有機物除去能を保持し、しかもリン除去能を有
するものである。従つて、本発明の吸着剤は血液
潅流用として、あるいは経口的腎疾患治療剤とし
て極めて有効である。 [発明の開示] 以下、本発明を詳述する。 本発明に係る活性炭は、ヤシ殻炭あるいは粉末
炭をバインダー固めた造粒炭、あるいはピツチ類
及び/又は有機合成高分子類から作られる球状活
性炭等を使用し得る。 球状活性炭は、例えば、特公昭50−18879号、
特開昭56−69214号、特開昭54−105897号に開示
されている製造法によつて生成し得る。また、原
料の有機合成高分子類としては、フエノール樹
脂、エポキシ樹脂の如き熱硬化性樹脂、またはス
チレン樹脂、塩化ビニリデン樹脂及びこれらの共
重合樹脂の如き熱可塑性樹脂が使用し得る。 本発明に使用する活性炭は、耐久性、保形性の
面から形状は球状であり、平均粒径0.1〜1mm、
比表面積500〜2000m2/g、半径100〜75000Åの
細孔容積0.1〜1.0cm3/gの特性を有する球状活性
炭が好ましい。 本発明における活性炭に添着されているMgO
−TiO2複合物は、リン吸着性能の点で下記特性
を有するものが好ましい。 (i) 組成比(モル比):MgO/TiO2=99.99/
0.01〜80/20好ましくは99.9/0.1〜90/10 (ii) 結晶構造:粉末X線回折法において、MgO
の結晶回折パターンを示す。 本発明の吸着剤は次の様にして製造される。マ
グネシウム及びチタンのアルコキシドを硝酸等の
酸溶液中で混合水溶化し、活性炭を浸漬した後、
アンモニア水等のアルカリ又は尿素で加水分解す
ることにより吸着前駆体を得る。該吸着前駆体を
焼成し本発明の吸着剤を得る。 焼成条件は、調製法、調製条件、配合割合等に
よつて多少異なるが、通常200〜1000℃、好まし
くは300〜700℃、更に好ましくは350〜500℃の温
度が好適である。本発明の吸着剤はMgO−TiO2
複合物が1〜10重量%添着していることが好まし
い。添着量が1重量%以下ではリンに対する吸着
量の効果は小さく、また10重量%以上では添着量
の増加に伴なうリン吸着量の大幅な向上はない。 尚、前駆体の製造は次の方法でも行ない得る。
即ち、マグネシウム及びチタンそれぞれの塩の混
合水溶液中に前記活性炭を浸漬処理し、次いでア
ンモニア水等のアルカリで加水分解する方法、あ
るいはアンモニア水の代りに尿素を用いる均一共
沈澱法、あるいは一方の金属塩の水溶液中に前記
活性炭を浸漬し、次いで他方の金属塩の水溶液に
浸漬させた後、アンモニア水等で加水分解する方
法である。 金属複合物の添着に際し、前記活性炭をあらか
じめ硝酸あるいは空気等によつて表面処理して用
いることもできる。焼成工程は、前記前駆体の複
合物化とともに表面化学特性を調整するものであ
る。 本発明の吸着剤を構成するMgO−TiO2複合物
は、TiO2の比率が高くなるに従つて結晶性が乱
れ、MgO固有のX線回折パターンが消滅し、同
時にリン吸着性能も低下する。TiO2の比率が低
い場合、酸化マグネシウム単独のものとX線回折
的に区別がつき難いものとなる。しかしながら、
酸化マグネシウム吸着剤では大気中の炭酸ガスの
影響を受け経時的な吸着性能の低下がみられるの
に対し、本発明の吸着剤は大気中においても長期
間安定な吸着性能を維持する。 本発明の吸着剤は、リン酸イオン等のリン成分
を吸着する優れた能力を有しているとともに、活
性炭の吸着特性、例えばクレアチニン等の有機物
の除去能力を併せ有するものである。即ち、リン
成分の吸着による高リン血症の治療に有用である
とともに、クレアチニン等の尿毒症性代謝物を吸
着除去する能力を有するため、血液潅流用吸着剤
としても有用なものである。 さらに使用方法として、本発明の吸着剤はゼラ
チン、アルブミン、ポリ−2−ヒドロキシエチル
メタクリレート等の高分子を被膜して使用するこ
ともできる。また他の吸着剤と混合して用いた
り、過等の他の透析療法との併用で使用するこ
ともできる。 さらに経口的に投与して消化器内でリンを除去
する目的で、単独であるいは薬剤組成物の形態で
経口吸着剤として使用することもできる。この
際、本発明の吸着剤は、医薬上許容される担体及
び/又は補助剤との組成物とし、錠剤、舌下錠
剤、カプセル剤、トローチ或いは水性もしくは油
性溶剤、懸濁液剤、乳剤、シロツプ剤、ゲル化剤
等の各種形態で使用し得る。錠剤、カプセル剤等
においては、腸溶性の剤形も本発明に包含され得
るものである。さらに上記製剤化に際して、必要
に応じ、甘味料、香味料、着色剤、保存剤、浸透
圧調整用塩、緩衝剤等の製薬補助剤を用いること
も可能である。 活性炭に、MgO−TiO2複合物を8.9重量%添着
してなる本発明の吸着剤はJcl−SDラツトに
15000mg/Kgを経口投与した場合に急性毒性とし
て何ら異常は認められなかつた。 本発明の吸着剤の製剤組成中における含有率は
適宜変化し得るが1重量%〜99重量%、好ましく
は70重量%〜99重量%含有させることが出来る。 服用量は、疾患の程度等によつても異なるが、
通常MgO−TiO2複合物を添着した活性炭として
0.5〜10g/回、1日3回程度が適度である。ま
た緊急を要する場合は勿論この限りでない。また
服用時期は透析前の保存期或いは透析期等特に限
定されない。 以下、実施例をもつて本発明を詳述する。 活性炭製造例 石油熱分解によつて得られるピツチと該ピツチ
に相溶性のある有機溶剤を混合し、懸濁液を含む
水を分散媒として、該ピツチ−有機溶剤混合物を
熔融分散せしめ、得られた球形粒子を脱溶剤し、
次いで不融化炭化し、900℃で賦活することによ
つて、平均粒径0.4mm、比表面積(メタノール吸
着法)1200m2/g、半径100〜75000Åの細孔容積
(水銀圧入法)0.3cm3/gの球状活性炭を得た。 実施例 1 攪拌した水中に0.22gのチタンテトライソプロ
ポキシド[(CH32CHO]4Tiを加え、生成した沈
澱を過し、十分に水洗した後、水2mlに分散
し、硝酸(61重量%)0.52gを加えて溶解した。
次いでこの溶液に、20gの硝酸マグネシウムMg
(NO32・6H2Oを水9mlに溶かした溶液を加え
て、マグネシウム/チタン混合溶液を調製した。 活性炭製造例で生成した球状活性炭10gを前記
混合溶液に加え、50℃で2時間攪拌した。 球状活性炭を別し、80℃で4時間乾燥した
後、20%アンモニア水50ml中に投入し6時間攪拌
した。次いで球状活性炭を別し、十分水洗した
後、窒素気流中200℃/hrで400℃まで昇温し、
400℃で1時間保持した後、冷却し、活性炭に
MgO−TiO2複合物(モル比99/1)を添着して
なる吸着剤10.89g(添着量8.9%)を得た。 実施例 2 実施例1で調製したマグネシウム/チタン混合
溶液に水8mlを加えた後、活性炭製造例で生成し
た球状活性炭10gを加え、50℃で2時間攪拌し
た。球状活性炭を別し80℃で4時間乾燥した
後、20%アンモニア水50mlに投入し6時間攪拌し
た。次いで球状活性炭を別し、十分水洗した
後、窒素気流中200℃/hrで400℃まで昇温し、
400℃で1時間保持した後、冷却し、活性炭に
MgO−TiO2複合物(モル比99/1)を添着して
なる吸着剤10.66g(添着量6.6%)を得た。 実施例 3 実施例1で調製したマグネシウム/チタン混合
溶液に水23mlを加えた後、活性炭製造例で生成し
た球状活性炭10gを加え、50℃で2時間攪拌し
た。球状活性炭を別し80℃で4時間乾燥した
後、20%アンモニア水50mlに投入し6時間攪拌し
た。次いで球状活性炭を別し、十分水洗した
後、窒素気流中200℃/hrで400℃まで昇温し、
400℃で1時間保持した後、冷却し、活性炭に
MgO−TiO2複合物(モル比99/1)を添着して
なる吸着剤10.47g(添着量4.7%)を得た。 実施例 4 ヒト血清にNaH2PO4・2H2Oを加えてリン濃
度10.1mg/dlに調整し、更にクレアチニンを加え
てクレアチニン濃度9.8mg/dlに調整した。該血
清10mlを各々共栓三角フラスコにとり、実施例1
〜3で得られた吸着剤及び活性炭製造例で生成し
た球状活性炭0.5gを加え、37℃で2時間振盪し
た後、上澄血清を採取し、リン濃度はRaBA−
Mark(京都第一科学製)により、クリアチニ
ン濃度はベツクマンクレアチニン分析計(ベツク
マン製)により測定した。結果を第1表に示す。 【表】
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention provides activated carbon such as spherical or granular activated carbon, coconut shell carbon, granulated carbon, etc. obtained from petroleum-based or coal-based pitch, organic synthetic polymers, etc. MgO
-Relates to an adsorbent impregnated with (supported by) a TiO 2 composite. [Technical background of the invention] In patients with kidney or liver dysfunction, the ability to excrete metabolic waste products from the body is insufficient, and these substances accumulate in the body, resulting in various physiological disorders. It is occurring. Therefore, in order to improve the pathological conditions of these functionally impaired individuals, metabolic waste products and the like are generally removed from the living body. For example, patients with renal failure are known to be typical of patients with renal dysfunction;
Treatment methods include blood purification using a dialysis membrane and blood perfusion using activated carbon. Incidentally, patients with renal failure have a problem of hyperphosphatemia due to a decline in the ability to excrete phosphorus into the urine, but the conventional treatment methods described above cannot improve the pathology of hyperphosphatemia. There is. That is, the former blood purification method using a dialysis membrane cannot sufficiently suppress the phosphorus concentration in the blood, and is completely powerless against intestinal absorption of phosphorus, which is the most important factor in hyperphosphatemia. On the other hand, the latter treatment method using activated carbon has a problem due to the characteristics of activated carbon itself, that is, its adsorption power for inorganic substances such as phosphorus is extremely poor. [Purpose of the Invention] In view of the above-mentioned circumstances, the inventors of the present invention have conducted extensive studies with the aim of providing a new adsorbent that has excellent phosphorus adsorption properties without impairing the adsorption performance of activated carbon. It has been discovered that an adsorbent impregnated with a -TiO 2 composite is extremely suitable for this purpose, leading to the completion of the present invention. [Structure and Effects of the Invention] Based on the above knowledge, the present invention provides activated carbon with MgO-
The present invention relates to an adsorbent impregnated with a TiO 2 composite (hereinafter referred to as the adsorbent of the present invention). The present inventors filed an application on the same day to use the MgO-TiO 2 composite as an antihyperphosphatemia agent because it has selective adsorption properties for phosphorus. The present invention is a further development of the adsorbent filed on the same day. That is, the adsorbent of the present invention retains the organic matter removal ability of activated carbon and also has phosphorus removal ability. Therefore, the adsorbent of the present invention is extremely effective for blood perfusion or as an oral drug for treating renal diseases. [Disclosure of the Invention] The present invention will be described in detail below. The activated carbon according to the present invention may be granulated carbon obtained by hardening coconut shell carbon or powdered carbon with a binder, or spherical activated carbon made from pitch and/or organic synthetic polymers. Spherical activated carbon is disclosed in, for example, Japanese Patent Publication No. 50-18879,
It can be produced by the production method disclosed in JP-A-56-69214 and JP-A-54-105897. Further, as the raw organic synthetic polymers, thermosetting resins such as phenol resins and epoxy resins, or thermoplastic resins such as styrene resins, vinylidene chloride resins, and copolymer resins thereof can be used. The activated carbon used in the present invention has a spherical shape in terms of durability and shape retention, and has an average particle size of 0.1 to 1 mm.
Preferably, spherical activated carbon has a specific surface area of 500 to 2000 m 2 /g, a radius of 100 to 75000 Å, and a pore volume of 0.1 to 1.0 cm 3 /g. MgO impregnated on activated carbon in the present invention
-TiO 2 composites preferably have the following properties in terms of phosphorus adsorption performance. (i) Composition ratio (molar ratio): MgO/TiO 2 =99.99/
0.01 to 80/20 preferably 99.9/0.1 to 90/10 (ii) Crystal structure: In powder X-ray diffraction, MgO
The crystal diffraction pattern of The adsorbent of the present invention is manufactured as follows. After mixing and water-solubilizing magnesium and titanium alkoxides in an acid solution such as nitric acid, and soaking activated carbon,
An adsorption precursor is obtained by hydrolysis with an alkali such as aqueous ammonia or urea. The adsorption precursor is calcined to obtain the adsorbent of the present invention. Although the firing conditions vary somewhat depending on the preparation method, preparation conditions, blending ratio, etc., a temperature of usually 200 to 1000°C, preferably 300 to 700°C, and more preferably 350 to 500°C is suitable. The adsorbent of the present invention is MgO−TiO 2
Preferably, 1 to 10% by weight of the composite is attached. When the amount of impregnation is less than 1% by weight, the effect of adsorption on phosphorus is small, and when it is more than 10% by weight, there is no significant improvement in the amount of phosphorus adsorbed as the amount of impregnation increases. Note that the precursor can also be produced by the following method.
That is, a method in which the activated carbon is immersed in a mixed aqueous solution of salts of magnesium and titanium, and then hydrolyzed with an alkali such as aqueous ammonia, a homogeneous co-precipitation method using urea in place of aqueous ammonia, or a method in which one of the metals is This is a method in which the activated carbon is immersed in an aqueous solution of a salt, then immersed in an aqueous solution of the other metal salt, and then hydrolyzed with aqueous ammonia or the like. When impregnating the metal composite, the activated carbon may be surface-treated with nitric acid or air beforehand. The firing process converts the precursor into a composite and adjusts the surface chemical properties. In the MgO-TiO 2 composite constituting the adsorbent of the present invention, as the ratio of TiO 2 increases, the crystallinity becomes disordered, the X-ray diffraction pattern unique to MgO disappears, and at the same time, the phosphorus adsorption performance decreases. When the ratio of TiO 2 is low, it becomes difficult to distinguish from magnesium oxide alone in terms of X-ray diffraction. however,
In contrast to magnesium oxide adsorbents whose adsorption performance deteriorates over time due to the influence of carbon dioxide in the atmosphere, the adsorbent of the present invention maintains stable adsorption performance over a long period of time even in the air. The adsorbent of the present invention has an excellent ability to adsorb phosphorus components such as phosphate ions, and also has the adsorption properties of activated carbon, such as the ability to remove organic substances such as creatinine. That is, it is useful for treating hyperphosphatemia by adsorbing phosphorus components, and is also useful as an adsorbent for blood perfusion because it has the ability to adsorb and remove uremic metabolites such as creatinine. Further, as a method of use, the adsorbent of the present invention can be used by coating it with a polymer such as gelatin, albumin, or poly-2-hydroxyethyl methacrylate. It can also be used in combination with other adsorbents or in combination with other dialysis treatments. Furthermore, it can be used alone or in the form of a pharmaceutical composition as an oral adsorbent for the purpose of orally administering and removing phosphorus in the digestive tract. In this case, the adsorbent of the present invention is a composition with a pharmaceutically acceptable carrier and/or auxiliary agent, and is prepared in the form of a tablet, sublingual tablet, capsule, troche, or aqueous or oily solvent, suspension, emulsion, or syrup. It can be used in various forms such as agents and gelling agents. For tablets, capsules, etc., enteric-coated dosage forms may also be included in the present invention. Furthermore, when preparing the above formulation, pharmaceutical auxiliaries such as sweeteners, flavorants, coloring agents, preservatives, salts for adjusting osmotic pressure, and buffering agents can be used as necessary. The adsorbent of the present invention, which is made by impregnating activated carbon with 8.9% by weight of MgO-TiO 2 composite, was used in Jcl-SD rats.
No abnormalities were observed in acute toxicity when 15,000 mg/Kg was orally administered. Although the content of the adsorbent of the present invention in the formulation composition may vary as appropriate, it can be contained in the range of 1% to 99% by weight, preferably 70% to 99% by weight. The dosage varies depending on the severity of the disease, etc.
Usually as activated carbon impregnated with MgO-TiO 2 composite
0.5-10g/time, about 3 times a day, is appropriate. Of course, this does not apply in cases of emergency. Moreover, the timing of administration is not particularly limited, such as the storage period before dialysis or the dialysis period. Hereinafter, the present invention will be explained in detail with reference to Examples. Activated carbon production example Pitch obtained by thermal decomposition of petroleum and an organic solvent compatible with the pitch are mixed, and the pitch-organic solvent mixture is melted and dispersed using water containing a suspension as a dispersion medium. Remove the solvent from the spherical particles,
Then, by infusible carbonization and activation at 900°C, the particles have an average particle diameter of 0.4 mm, a specific surface area (methanol adsorption method) of 1200 m 2 /g, and a pore volume of 100 to 75000 Å in radius (mercury intrusion method) 0.3 cm 3 /g of spherical activated carbon was obtained. Example 1 0.22 g of titanium tetraisopropoxide [(CH 3 ) 2 CHO] 4 Ti was added to stirred water, the resulting precipitate was filtered, thoroughly washed with water, dispersed in 2 ml of water, and diluted with nitric acid (61 % by weight) was added and dissolved.
This solution was then added with 20 g of magnesium nitrate, Mg
A solution of (NO 3 ) 2 ·6H 2 O dissolved in 9 ml of water was added to prepare a magnesium/titanium mixed solution. 10 g of the spherical activated carbon produced in the activated carbon production example was added to the mixed solution and stirred at 50° C. for 2 hours. The spherical activated carbon was separated and dried at 80° C. for 4 hours, then poured into 50 ml of 20% ammonia water and stirred for 6 hours. Next, the spherical activated carbon was separated, thoroughly washed with water, and then heated to 400°C at a rate of 200°C/hr in a nitrogen stream.
After holding at 400℃ for 1 hour, cool it and turn it into activated carbon.
10.89 g (impregnated amount: 8.9%) of an adsorbent impregnated with a MgO-TiO 2 composite (molar ratio 99/1) was obtained. Example 2 After adding 8 ml of water to the magnesium/titanium mixed solution prepared in Example 1, 10 g of the spherical activated carbon produced in the activated carbon production example was added and stirred at 50°C for 2 hours. After separating the spherical activated carbon and drying it at 80°C for 4 hours, it was poured into 50 ml of 20% aqueous ammonia and stirred for 6 hours. Next, the spherical activated carbon was separated, thoroughly washed with water, and then heated to 400°C at a rate of 200°C/hr in a nitrogen stream.
After holding at 400℃ for 1 hour, cool it and turn it into activated carbon.
10.66 g (impregnated amount: 6.6%) of an adsorbent impregnated with a MgO-TiO 2 composite (molar ratio 99/1) was obtained. Example 3 After adding 23 ml of water to the magnesium/titanium mixed solution prepared in Example 1, 10 g of the spherical activated carbon produced in the activated carbon production example was added and stirred at 50°C for 2 hours. After separating the spherical activated carbon and drying it at 80°C for 4 hours, it was poured into 50 ml of 20% aqueous ammonia and stirred for 6 hours. Next, the spherical activated carbon was separated, thoroughly washed with water, and then heated to 400°C at a rate of 200°C/hr in a nitrogen stream.
After holding at 400℃ for 1 hour, cool it and turn it into activated carbon.
10.47 g (impregnated amount: 4.7%) of an adsorbent impregnated with a MgO-TiO 2 composite (molar ratio 99/1) was obtained. Example 4 NaH 2 PO 4 .2H 2 O was added to human serum to adjust the phosphorus concentration to 10.1 mg/dl, and creatinine was further added to adjust the creatinine concentration to 9.8 mg/dl. Example 1: Take 10 ml of the serum into each stoppered Erlenmeyer flask.
After adding the adsorbent obtained in 3 to 3 and 0.5 g of spherical activated carbon produced in the activated carbon production example and shaking at 37°C for 2 hours, the supernatant serum was collected, and the phosphorus concentration was determined to be RaBA-
Mark (manufactured by Kyoto Daiichi Kagaku), and the creatinine concentration was measured by a Beckman creatinine analyzer (manufactured by Beckman). The results are shown in Table 1. 【table】

Claims (1)

【特許請求の範囲】 1 活性炭にMgO−TiO2複合物を添着してなる
腎疾患治療用吸着剤。 2 活性炭は球状活性炭である特許請求の範囲第
1項記載の吸着剤。 3 MgO−TiO2複合物のMgO/TiO2比はモル
比で99.99/0.01〜80/20である特許請求の範囲
第1項記載の吸着剤。 4 MgO−TiO2複合物を活性炭に1重量%〜10
重量%添着してなる特許請求の範囲第1項記載の
吸着剤。 5 球状活性炭は平均粒径0.1〜1mm、比表面積
500〜2000m2/g、半径100〜75000Åの細孔容積
0.1〜1.0cm3/gの特性を有する特許請求の範囲第
2項記載の吸着剤。 6 抗高リン血症剤である特許請求の範囲第1項
記載の吸着剤。 7 血液潅流用吸着剤である特許請求の範囲第1
項記載の吸着剤。
[Claims] 1. An adsorbent for the treatment of renal diseases, which is made by impregnating activated carbon with a MgO-TiO 2 composite. 2. The adsorbent according to claim 1, wherein the activated carbon is spherical activated carbon. 3. The adsorbent according to claim 1, wherein the MgO/TiO 2 ratio of the MgO-TiO 2 composite is 99.99/0.01 to 80/20 in molar ratio. 4 MgO-TiO 2 composite to activated carbon 1% to 10% by weight
% by weight of the adsorbent according to claim 1. 5 Spherical activated carbon has an average particle size of 0.1 to 1 mm and a specific surface area.
Pore volume of 500-2000m 2 /g, radius 100-75000Å
The adsorbent according to claim 2, which has a characteristic of 0.1 to 1.0 cm 3 /g. 6. The adsorbent according to claim 1, which is an antihyperphosphatemic agent. 7 Claim 1 which is an adsorbent for blood perfusion
Adsorbent as described in section.
JP62210714A 1987-08-25 1987-08-25 Novel adsorbent Granted JPS6456141A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP62210714A JPS6456141A (en) 1987-08-25 1987-08-25 Novel adsorbent
ES88307827T ES2054816T3 (en) 1987-08-25 1988-08-24 COMPLEX OF MAGNESIUM OXIDE AND TITANIUM DIOXIDE AS A PHOSPHATE ADSORBENT.
US07/235,415 US4988569A (en) 1987-08-25 1988-08-24 Complex phosphate adsorbent of MgO-TiO2
DE8888307827T DE3881141T2 (en) 1987-08-25 1988-08-24 COMPOSITION OF MAGNESIUM OXYD AND TITANDIOXYD AS A PHOSPHATE SORBENT.
EP88307827A EP0311244B1 (en) 1987-08-25 1988-08-24 Complex of magnesium oxide and titanium dioxide as a phosphate adsorbent
CA000575490A CA1324601C (en) 1987-08-25 1988-08-24 Complex phosphate adsorbent
KR1019880010842A KR910004018B1 (en) 1987-08-25 1988-08-25 Phosphate adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62210714A JPS6456141A (en) 1987-08-25 1987-08-25 Novel adsorbent

Publications (2)

Publication Number Publication Date
JPS6456141A JPS6456141A (en) 1989-03-03
JPH0422618B2 true JPH0422618B2 (en) 1992-04-20

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP62210714A Granted JPS6456141A (en) 1987-08-25 1987-08-25 Novel adsorbent

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Country Link
JP (1) JPS6456141A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4910261A (en) * 1988-06-17 1990-03-20 Edison Polymer Innovation Corp. (Epic) Thermoplastic elastomers having isobutylene block and cyclized diene blocks
JP2746292B2 (en) * 1990-08-31 1998-05-06 インターナショナル・ビジネス・マシーンズ・コーポレイション Sputtering equipment
US7651974B2 (en) 2002-11-01 2010-01-26 Kureha Chemical Industry Co., Ltd. Adsorbent for oral administration
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
WO2011125758A1 (en) * 2010-03-31 2011-10-13 富田製薬株式会社 Dialysis composition, hemodialysis system, and hemodialyzer
CN108348673B (en) * 2015-11-11 2022-02-18 旭化成医疗株式会社 Phosphorus adsorbent for blood treatment, blood treatment system, and blood treatment method
EP3626281A4 (en) * 2017-05-17 2020-06-03 Asahi Kasei Medical Co., Ltd. Phosphorus adsorbent for blood treatment, blood treatment system, and blood treatment method

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