JPS62209146A - Porous base material - Google Patents

Porous base material

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Publication number
JPS62209146A
JPS62209146A JP61054334A JP5433486A JPS62209146A JP S62209146 A JPS62209146 A JP S62209146A JP 61054334 A JP61054334 A JP 61054334A JP 5433486 A JP5433486 A JP 5433486A JP S62209146 A JPS62209146 A JP S62209146A
Authority
JP
Japan
Prior art keywords
reaction
polylactide
polyglycolide
base material
porous base
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
JP61054334A
Other languages
Japanese (ja)
Other versions
JPH0323100B2 (en
Inventor
Takao Okada
隆雄 岡田
Hironobu Fukuzaki
裕延 福崎
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.)
Taki Chemical Co Ltd
Original Assignee
Taki Chemical Co Ltd
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 Taki Chemical Co Ltd filed Critical Taki Chemical Co Ltd
Priority to JP61054334A priority Critical patent/JPS62209146A/en
Publication of JPS62209146A publication Critical patent/JPS62209146A/en
Publication of JPH0323100B2 publication Critical patent/JPH0323100B2/ja
Granted legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Medicinal Preparation (AREA)
  • Cosmetics (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)
  • Fats And Perfumes (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)

Abstract

PURPOSE:To obtain a porous base material readily controllable in the pore size, outstanding in strength and slow-release characteristics, by reaction between polylactide, polyglycolide or copolycondensate therefrom and aluminum alcoholate. CONSTITUTION:(A) A solution prepared by dissolving, in an organic solvent (e.g. chloroform), polylactide, polyglycolide or copolycondensate therefrom with a number-average molecular weight 300-200,000 derived from direct dehydration polycondensation of, e.g. lactic acid and/or glycolic acid, under reduced pressure, with a polymer concentration 0.5-40wt% is incorporated with, while stirring, (B) a second solution prepared by dissolving, in an organic solvent, an aluminum alcoholate such as aluminum isopropoxide, with a concentration up to 10wt% to carry out reaction. Following completion of the reaction, the resulting gelled product is dried under reduced pressure, thus obtaining the objective porous base material. The pore size can be regulated by controlling the molecular weight and/or concentration of the polymer in the component A.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は多孔性基剤に関し、殊に薬剤等を基剤に含浸さ
せた際に薬剤の優れた徐放特性を付与する多孔性基剤の
91造方法に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a porous base material, and in particular to a porous base material that provides excellent sustained release properties of a drug when the base material is impregnated with a drug. Regarding the 91 construction method.

FL酸、グリコール酸等の重縮合体、即ちポリラクチド
、ポリグリコリドは生体内分解性のポリマーとして、近
年縫合糸1人工気管、人工血管等の医用インブラント材
料に応用されている。
Polycondensates of FL acid, glycolic acid, etc., ie, polylactide and polyglycolide, are biodegradable polymers that have recently been applied to medical implant materials such as suture threads, artificial tracheas, and artificial blood vessels.

また一方で、生理活性物質、農薬等の薬剤の徐放化基剤
としての応用もされつつある。
On the other hand, it is also being applied as a sustained release base for drugs such as physiologically active substances and agricultural chemicals.

これらの材料に所望される特性として、生体親和性、生
体内分解性等をイIすることだけでなく、薬剤等を斥浸
した材料については一定期間内に薬剤を基剤から放出す
るという徐放制御が課題となっている。
Desired properties for these materials include not only biocompatibility and biodegradability, but also, for materials impregnated with drugs, gradual release of drugs from the base within a certain period of time. Release control is an issue.

この新しい展開として、近年ポリラクチド等の徐放化、
即ち多孔質化が検討されている。
As a new development, in recent years, the sustained release of polylactide, etc.
That is, making it porous is being considered.

(従来の技術) 従来、ポリラクチドを多孔質化する方法として、クロロ
ホルム−エタノール等の特定混合溶媒にポリラクチドと
シュウ酸ナトリウムを溶解し、この溶媒を一定速度で蒸
発させた後、シュウ酸ナトリウムをエタノールで抽出す
ることにより得る方法が知られている。 (Panni
ngsら、C。
(Prior art) Conventionally, as a method of making polylactide porous, polylactide and sodium oxalate are dissolved in a specific mixed solvent such as chloroform-ethanol, and after this solvent is evaporated at a constant rate, the sodium oxalate is dissolved in ethanol. A known method is to extract (Panni
ngs et al., C.

11oid、 polyIl、 Sci、、工、477
(1983))しかしこの方法は、溶媒の蒸発速度の制
御が非常に難しく、所望する孔径のポリマーが得られな
い、また添加したシュウ酸ナトリウム等の塩がポリマー
中に残留し、生体系への用途が制約される。
11oid, polyIl, Sci,, engineering, 477
(1983)) However, with this method, it is very difficult to control the evaporation rate of the solvent, making it impossible to obtain a polymer with the desired pore size.Also, added salts such as sodium oxalate remain in the polymer, and are harmful to biological systems. Usage is restricted.

また別に、低分子量のポリラクチドとクロム、アルミニ
ウム等の塩化物、炭酸塩とを約260〜280°Cとい
う高温で反応させ、樹脂をIR遺する方法が知られてい
るが、この方法は反応に極めて長時間を要し、ポリラク
チドの分解を促進し、反応生成物中に分H物が多層に残
存する。
Separately, a method is known in which low molecular weight polylactide is reacted with chlorides or carbonates of chromium, aluminum, etc. at a high temperature of about 260 to 280°C, and the resin is left with IR. This process takes an extremely long time, accelerates the decomposition of polylactide, and leaves multiple layers of decomposition products in the reaction product.

そして、このものは低分子址、低強度であることから、
多孔性基剤として通常使用できないものである。
And since this material is low molecular weight and has low strength,
It cannot normally be used as a porous base.

このようにポリラクチド、ポリグリコリド等からなる多
孔性基剤として、未だ徐放性、基剤強度等に優れる基剤
を得る方法は見出されていないのが現状である。
As described above, as a porous base made of polylactide, polyglycolide, etc., no method has yet been found to obtain a base having excellent sustained release properties, base strength, etc.

(発明が解決しようとする問題点) そこで本発明者らは、前記の問題を解決すべく多孔性基
剤として孔径の制御が容易であり。
(Problems to be Solved by the Invention) In order to solve the above-mentioned problems, the present inventors have developed a porous base material that allows easy control of the pore diameter.

しかも基剤としての強度、徐放特性に優れるポリラクチ
ドまたはポリグリコリド等からなる多孔性基剤を得る方
法につき鋭意研究を進めた。
In addition, we have conducted extensive research into methods for obtaining porous bases made of polylactide, polyglycolide, etc., which have excellent strength and sustained release properties as bases.

(It!I 111点を解決するための手段)本発明者
らは種々の検討を行なった結果、ポリラクチド、ポリグ
リコリド又はそれらの共重縮合体と、アルミニウムイソ
プロポえシト等のアルミニウムアルコレートとを、有機
溶媒中で反応を行うか、若しくは溶融混合反応後にイf
a溶媒中で膨潤させることにより、ポリラクチド、ポリ
グリコリド又はそれらの共重縮合体を所望する孔径に多
孔質化でき、しかもこの反応は室温程度の温度で短時間
に行なえることを見い出し、その結果、初期のポリマー
分子量の低下刃「回避され、徐放性、強度特性共に優れ
る多孔性基剤を1)ることか可能になり、本発明を完成
させるに至ったものである。
(Means for solving It!I 111 points) As a result of various studies, the present inventors found that polylactide, polyglycolide, or their copolycondensates, and aluminum alcoholates such as aluminum isopropoester The reaction is carried out in an organic solvent or after the melt-mixing reaction.
We have discovered that polylactide, polyglycolide, or their copolycondensates can be made porous to a desired pore size by swelling them in a solvent, and that this reaction can be carried out in a short time at a temperature around room temperature. 1) It has now become possible to create a porous base that avoids the initial decrease in polymer molecular weight and has excellent sustained release properties and strength properties, leading to the completion of the present invention.

即ち本発明は、ポリラクチド、ポリグリコリド又はそれ
らの共重縮合体とアルミニウムアルコレートとを反応さ
せてなる多孔性基剤に関する。
That is, the present invention relates to a porous base material formed by reacting polylactide, polyglycolide, or a copolycondensate thereof with aluminum alcoholate.

(作 用) 本発明の多孔性基剤の製造に用いる原料として、先ずポ
リラクチド、ポリグリコリド又はそれらの共重縮合体に
ついては、これらは一般的な方法により製造されるもの
であれば何れのものであってもよい。
(Function) As raw materials for producing the porous base of the present invention, polylactide, polyglycolide, or their copolycondensates may be any polylactide, polyglycolide, or copolycondensate thereof, as long as they are produced by a general method. It may be.

例えば、乳酸、グリコール酸を減圧下で直接脱水重縮合
を行なうことによりポリラクチド、ポリグリコリドが得
られる。(湯原ら、王化、L2(6)、955(196
4)) また、乳酸、グリコール酸を酸化亜鉛等の触媒存在下で
縮合を行ない、ラクチド、グリコリドを得た後、これを
テトラフェニルスズ、塩化第1スズ等の触媒存在下で重
合反応を行なうことによっても製造できる。 (Kul
karni、J、Biomed、Mater、Res、
、J、169(1971))更に、これらの場合に使用
する乳酸のモノマーは、D一体、L一体、及びDL一体
の各れのものであってもよい。
For example, polylactide and polyglycolide can be obtained by directly dehydrating and polycondensing lactic acid and glycolic acid under reduced pressure. (Yubara et al., Wangka, L2(6), 955 (196
4)) In addition, lactic acid and glycolic acid are condensed in the presence of a catalyst such as zinc oxide to obtain lactide and glycolide, which are then subjected to a polymerization reaction in the presence of a catalyst such as tetraphenyltin or stannous chloride. It can also be manufactured by (Kul
karni, J., Biomed, Mater, Res.
, J, 169 (1971)) Furthermore, the lactic acid monomer used in these cases may be any one of D monomer, L monomer, and DL monomer.

本発明ではこの様にして得られるポリラクチド、ポリグ
リコリド又はそれらの共重縮合体の数平均分子量が通常
300〜200000のものを使用する。
In the present invention, the polylactide, polyglycolide, or copolycondensate thereof obtained in this manner usually has a number average molecular weight of 300 to 200,000.

次に、本発明で用いるアルミニウムアルコレートに関し
て云えば、アルミニウムアルコレートとしては、アルミ
ニウムイソプロポキシド、アルミニウムメトキシド、ア
ルミニウムエトキシド、アルミニウムーn−ブトキシド
、フェニルメトキシド、フェニルエトキシド等が使用で
きる。
Next, regarding the aluminum alcoholate used in the present invention, aluminum isopropoxide, aluminum methoxide, aluminum ethoxide, aluminum-n-butoxide, phenyl methoxide, phenylethoxide, etc. can be used as the aluminum alcoholate. .

またアルミニウムアルコレート以外の他のアルミニウム
塩の使用では、本発明の反応が起こらず、または反応し
ても多孔質体が生起せず、以って本発明の多孔質体を得
ることができない。
Furthermore, when aluminum salts other than aluminum alcoholate are used, the reaction of the present invention does not occur, or even if the reaction occurs, no porous body is formed, and therefore the porous body of the present invention cannot be obtained.

更に、本発明では有機溶媒を使用するが、この有機溶媒
に関しては、前記のポリラクチド、ポリグリコリド又は
それらの共重縮合体を溶解する有機溶媒であれば何であ
ってもよく、クロロホルム、四塩化炭素、ベンゼン、ト
ルエン、ジオキサン等、更にはイソプロパツール、ブタ
ノール等のアルコール類、及びアセトン等が使用できる
Further, in the present invention, an organic solvent is used, and any organic solvent may be used as long as it dissolves the polylactide, polyglycolide, or copolycondensate thereof, including chloroform, carbon tetrachloride, etc. , benzene, toluene, dioxane, alcohols such as isopropanol, butanol, acetone, etc. can be used.

これらの原料を使用し、本発明の多孔性基剤を製造する
方法は次のように行なう。
The method for producing the porous base of the present invention using these raw materials is as follows.

先ず、ポリラクチド、ポリグリコリド又はそれらの共重
縮合体を前記の有機溶媒に溶解するこの時の、これらポ
リマーの′a度は、その分子量、所望する基剤の孔径等
によって異なるが、大略0.5〜40重鼠%の範囲で使
用する。
First, when polylactide, polyglycolide, or a copolycondensate thereof is dissolved in the above-mentioned organic solvent, the a degree of the polymer varies depending on its molecular weight, the desired pore size of the base material, etc., but is approximately 0. It is used in a range of 5 to 40%.

即ち、この時のポリマー分子量及びポリマー濃度の選択
により、本発明では自由に多孔性基剤の孔径を調整する
ことができる。即ちポリマーの濃度を高く、または分子
量が大きいものを使用するほど基剤孔径は小さくなり、
また反対にポリマー濃度を低くまたは分子量が小さいも
のを使用する程基剤の孔径は大きくなる。
That is, by selecting the polymer molecular weight and polymer concentration at this time, the pore diameter of the porous base material can be freely adjusted in the present invention. In other words, the higher the polymer concentration or the larger the molecular weight used, the smaller the base pore diameter.
Conversely, the lower the polymer concentration or the lower the molecular weight used, the larger the pore size of the base material.

またこの時のポリマー濃度が0.5〜40 重量%の範
囲を逸脱し、0.5重量%を下回る場合には。
Further, if the polymer concentration at this time deviates from the range of 0.5 to 40% by weight and is less than 0.5% by weight.

反応に著しく長時間を要するばかりか、基剤の孔径が過
大となり過ぎ、基剤の強度が低下し好ましくなく、逆に
40瓜量%を上回る場合には後述するポリマーとアルミ
ニウムアルコレートとの反応が局部的となると共に、基
剤の孔径が過小となり、本発明の多孔性基剤を得ること
が困難となる。
Not only does the reaction take an extremely long time, but the pore size of the base material becomes too large and the strength of the base material decreases, which is undesirable.On the other hand, if the amount exceeds 40%, the reaction between the polymer and aluminum alcoholate described below The porous base material becomes localized and the pore size of the base material becomes too small, making it difficult to obtain the porous base material of the present invention.

次に前記に掲示したアルミニウムアルコレートを、同様
に有機溶媒に溶解または懸濁させる。
Next, the aluminum alcoholate listed above is similarly dissolved or suspended in an organic solvent.

この場合に、これらアルミニウムアルコレートは、概ね
10重廿%までの範囲で溶解又は分散懸濁させる。
In this case, these aluminum alcoholates are dissolved or dispersed and suspended in an amount of up to about 10% by weight.

イア0溶媒に溶解したポリラクチド、ポリグリコリド、
又はそれらの共重縮合体と前記のアルミニウムアルコレ
ートとの反応は、先ず前記のポリマーの溶液を反応容器
に入れ、次にアルミニウムアルコレートの溶液を攪はん
しながら添加する。
Polylactide, polyglycolide dissolved in Ia0 solvent,
In the reaction of a copolycondensate thereof and the aluminum alcoholate, first, a solution of the polymer is placed in a reaction vessel, and then a solution of the aluminum alcoholate is added while stirring.

この場合に、添加順序については別設限定はなく、アル
ミニウムアルコレートを先に、又はポリマーとアルコレ
ートを同時に添加する方法によってもよい。
In this case, there is no particular limitation on the order of addition, and the aluminum alcoholate may be added first, or the polymer and alcoholate may be added simultaneously.

更にこの時の添加量は、反応に用いるポリラクチド、ポ
リグリコリド、又はそれらの共fL重縮合体濃度、分子
量により異なるが、概ねA I /C0OHモル比(但
し、AIは前記アルミニウムアルコレートに由来する^
l、またC00)Iはポリラクチド、ポリグリコリド、
又はそれらの共重縮合体に由来する重縮合体の反応性の
C0OHを示す、)が0.2以上で行なう。
Furthermore, the amount added at this time varies depending on the concentration and molecular weight of the polylactide, polyglycolide, or their co-fL polycondensate used in the reaction, but is generally based on the A I /C0OH molar ratio (however, AI is derived from the aluminum alcoholate). ^
l, and C00) I is polylactide, polyglycolide,
or the reactive COOH of a polycondensate derived from a copolycondensate thereof) is 0.2 or more.

即ち0.2を下回る場合には、生成物の強度が著しく低
下し、本発明の多孔性基剤を得ることが困難となる。
That is, if it is less than 0.2, the strength of the product decreases significantly, making it difficult to obtain the porous base of the present invention.

また、前記のポリラクチド、ポリグリコリド、又はそれ
らの共Yil縮合体由来する重縮合体の反応性C00H
JIは、次の方法により求める。
In addition, the reactivity C00H of the polylactide, polyglycolide, or a polycondensate derived from their co-Yil condensate
JI is determined by the following method.

< C0OH定量方法〉 ポリラクチド、ポリグリコリド、又はそれらの共重縮合
体の約1gを20m1のベンジルアルコールに加熱溶解
し、冷却後フェノールフタレインを指示薬に用い、 0
.025Nの水酸化カリウムのベンジルアルコール溶液
で滴定する0滴定に際しては空気中の二酸化炭素等の妨
害を除去するため、N2ガスを導入しながら窒素雰囲気
下で行う。
<C0OH quantification method> Approximately 1 g of polylactide, polyglycolide, or their copolycondensates was heated and dissolved in 20 ml of benzyl alcohol, and after cooling, phenolphthalein was used as an indicator.
.. The zero titration, in which titration is performed with a benzyl alcohol solution of 025N potassium hydroxide, is carried out under a nitrogen atmosphere while introducing N2 gas in order to remove interference such as carbon dioxide in the air.

滴定値より次式により重縮合体の反応性C00H盪を求
める。
The reactivity C00H of the polycondensate is determined from the titration value using the following formula.

0.025  x  10−”  f(S−B)X= 
                 (mol/g)但
し簀:gL縮合体ffi量(g) f :0.025)l水酸化カリウム溶液の7アクター
S :                    滴定
量(フン71ル)B :              
       滴定量(79ランク)X:l縮合体の反
応性C00H1i (aol/g)反応時の溶液の温度
は、通常、室温で行なえばよいが、適度な加温を行って
もよい。
0.025 x 10-” f(S-B)X=
(mol/g) However, gL Amount of condensate ffi (g) f: 0.025)l 7 actors of potassium hydroxide solution S: Titration amount (71 l) B:
Titration amount (79 rank)

反応の進行と共に反応液はゲル化するが、反応開始時よ
り通常、2時間までに反応は終了する。
As the reaction progresses, the reaction solution turns into a gel, but the reaction usually ends within 2 hours from the start of the reaction.

反応の終了後、得られるゲル状物をメタノール、エタノ
ール、エーテル等の溶媒で溶媒析出処理し、乾燥を行な
うか、あるいはゲル状物を直接減圧乾燥することにより
1本発明の多孔性基剤を得ることが出来る。
After the reaction is completed, the porous base of the present invention can be prepared by subjecting the resulting gel to a solvent precipitation treatment with a solvent such as methanol, ethanol, or ether, and drying, or by directly drying the gel under reduced pressure. You can get it.

また、これ以外の方法としてポリラクチド、ポリグリコ
リド、又はそれらの共重縮合体とアルミニウムアルコレ
ートとを、90〜230℃の温度で溶融混合した後、前
記の有機溶媒中で膨潤させることによっても本発明の多
孔性基剤を(得ることができる。
Alternatively, polylactide, polyglycolide, or a copolycondensate thereof and aluminum alcoholate may be melt-mixed at a temperature of 90 to 230°C, and then swelled in the above-mentioned organic solvent. A porous base of the invention can be obtained.

この様にして得られた本発明の基剤は、多孔質であり、
基剤としての強度特性に優れ、またポリラクチド、ポリ
グリコリド、又はそれらの共重縮合体を基剤の主体とす
るため、基剤自体の徐放性との共同作用により徐放性が
著しく増加し、徐放性基剤としてA有すべき優れた徐放
特性を有するものである。
The base of the present invention obtained in this way is porous,
It has excellent strength properties as a base, and since the base is mainly polylactide, polyglycolide, or their copolycondensates, the sustained release properties are significantly increased due to the synergistic effect with the sustained release properties of the base itself. , has the excellent sustained release properties that A should have as a sustained release base.

従って本発明品は、薬剤等のマトリックス、インブラン
ト材t1のみならず、菌体、微生物の保持剤、マイクロ
カプセルとしての担体、土壌改良剤、崩壊性農業用フィ
ルム、果実の品質向上剤、気体分離透過膜、芳香剤等、
幅広い用途に用いることができる。
Therefore, the product of the present invention is suitable not only for use as a matrix for drugs, as an implant material t1, but also for bacterial cells, microorganism retention agents, carriers as microcapsules, soil conditioners, disintegrating agricultural films, fruit quality improvers, gaseous Separation permeable membranes, fragrances, etc.
It can be used for a wide range of purposes.

(実施例) 以下に本へ明の実施例を掲げ説明を行なうが、本発明は
これらに限定されるものではない。
(Examples) Specific examples will be described below, but the present invention is not limited thereto.

尚、%は特にことわらない限り全て重量%を示す。It should be noted that all percentages are by weight unless otherwise specified.

実施例I TJA度計、コンデンサー、攪はん機を備えた300m
1容のセパラブルフラスコに、第1表に示したアルミニ
ウムアルコレートの所定量と、クロロホルム45gを入
れ、攪はんを行った。
Example I 300m with TJA meter, condenser and stirrer
A predetermined amount of aluminum alcoholate shown in Table 1 and 45 g of chloroform were placed in a 1-volume separable flask and stirred.

これに数平均分子i 2590のポIJ−L−ラクチド
9.51gをクロロホルムに溶解し75gとした液を添
加し 反応を行った。(^l/C0OHモル比1.0)
ポリ−し一ラクチドの添加後数分で反応系がゲル化する
が、これに更にQJのクロロホルムを添加し、開始後3
0分で攪はんを止め、生成物をフラスコから取り出した
A solution obtained by dissolving 9.51 g of polyJ-L-lactide with a number average molecular weight i of 2590 in chloroform to make 75 g was added to the solution, and a reaction was carried out. (^l/C0OH molar ratio 1.0)
The reaction system gels within a few minutes after adding poly-lactide, but QJ's chloroform is further added to this and 3 minutes after the start.
Stirring was stopped at 0 minutes and the product was removed from the flask.

反応生成物を30℃5mmHgで減圧乾燥し、本発明の
多孔性基剤を得た。
The reaction product was dried under reduced pressure at 30° C. and 5 mmHg to obtain a porous base of the present invention.

また比較のために、アルミニウムアルコレート以外の他
のアルミニウム塩について、前記と同様に反応及び減圧
乾燥を行った。
For comparison, aluminum salts other than aluminum alcoholate were reacted and dried under reduced pressure in the same manner as described above.

これらを走査型電子顕微鏡で観察し、生成物の多孔性状
態を調べた。 その結果を第1表に示した。
These were observed with a scanning electron microscope to examine the porous state of the product. The results are shown in Table 1.

またアルミニウムイソプロポキシドを使用して得た本発
明の多孔性基Mの電子a微鏡写真を第1図に示した。
Further, an electron-a micrograph of the porous group M of the present invention obtained using aluminum isopropoxide is shown in FIG.

更に、友応、乾燥後に得られた本発明品及び比較調高に
ついて、ジオキサン吸収量を測定し、基剤の多孔質化度
をみた。 M果を第1表に示した。
Furthermore, the dioxane absorption amount was measured for the products of the present invention and comparative preparations obtained after drying, and the degree of porosity of the base was determined. M fruits are shown in Table 1.

くジオキサン吸収量の測定法〉 基剤試f1の2gを300m1容のビーカーに入れ、こ
れに200gのジオキサンを添加し、24時間浸漬させ
た。  浸i)を後、余分のジオキサンを除去した後、
ろ紙上で1時間風乾し、これの重量を測定し、次式によ
りジオキサン吸収量を算出した。
Method for Measuring Absorption of Dioxane> 2 g of base sample f1 was placed in a 300 ml beaker, 200 g of dioxane was added thereto, and the mixture was immersed for 24 hours. After soaking i) and removing excess dioxane,
It was air-dried on a filter paper for 1 hour, its weight was measured, and the amount of dioxane absorbed was calculated using the following formula.

但し、xニジオキサン吸収量(g#) W、:試料採取1(g) 112;ジオキサン吸収後の試料型Nk (g)第1表 実施例2 実施例1と同じ反応器を用い、第2表に示した各分子量
のボII−DL−ラクチドとアルミニウムイソプロポキ
シドの所2量をクロロホルムに溶解し、攪f、i/、下
400Cテ反応を行ツタ、 (AI/C0OHモル比0
.5) 1時間反応後に得られたゲル化生成物を、石油エーテル
に浸漬し、クロロホルムを除去した後、室温で乾燥させ
、本発明の多孔性基剤を得た。
However, x Nidioxane absorption amount (g #) W,: Sample collection 1 (g) 112; Sample type after dioxane absorption Nk (g) Table 1 Example 2 Using the same reactor as Example 1, the second Two amounts of Bo II-DL-lactide and aluminum isopropoxide of each molecular weight shown in the table were dissolved in chloroform, and the reaction was carried out under stirring at 400 C. (Al/C0OH molar ratio 0
.. 5) The gelled product obtained after 1 hour of reaction was immersed in petroleum ether to remove chloroform and then dried at room temperature to obtain the porous base of the present invention.

得られた多孔性基剤の走査型電子顕微g観察、及びジオ
キサン吸収量を測定し、結果を第2表に示した。
The obtained porous base material was observed using a scanning electron microscope and the amount of dioxane absorbed was measured, and the results are shown in Table 2.

実施例3 攪はん損を備えた300m1容のビーカーに、アルミニ
ウムイソプロポキシド0.6gとキシレン50区を入れ
、攪はんを行った。
Example 3 In a 300 ml beaker equipped with a stirring loss, 0.6 g of aluminum isopropoxide and 50 sections of xylene were placed and stirred.

遣 攪は□んを続けながら数平均分子量1300のし一うク
チ1°−グリコリド共!縮合体(りゝリフリビーし一う
クチビモル比2.33)3.82gをキシレン150g
に溶解した溶液を添加し、55℃で加温、1.7時間の
反応を行った・ 反応終了後、得られたゲル化生成物をメタノール中にP
i潰しキシレンを除去した後、40℃3mmHg−C−
減圧乾燥し、本発明の多孔性基剤を得た。   !この
基剤の電子顕微鏡観察の結果、ち密な多孔質体となって
おり、またジオキサン吸収量は45g/gであった。 
更に、基剤は指触によっても脆化しない強度を有してい
た。
While continuing to stir, add 1°-glycolide with a number average molecular weight of 1300! 3.82 g of condensate (relily-free-bis-one-cut mole ratio 2.33) was added to 150 g of xylene.
After the reaction was completed, the resulting gelled product was dissolved in methanol and reacted for 1.7 hours.
i After removing crushed xylene, 40°C 3mmHg-C-
It was dried under reduced pressure to obtain a porous base of the present invention. ! As a result of electron microscopic observation of this base, it was found to be a dense porous body, and the amount of dioxane absorbed was 45 g/g.
Furthermore, the base had a strength that did not become brittle even when touched with a finger.

実施Ij44 実施例1で得た本発明の多孔性基剤、及び比較調高を粉
砕し、250〜420μ瓢となるように漬分した粉末4
.5gに0.5gのブタンベン(p−7ミノ安息香酸n
−7’fルエステル)を各粉末の溶媒吸収限度量の範囲
内となるようにクロロホルムに展開した溶液を全量吸収
させた。  これを乾燥5中で20°03時間乾燥させ
、クロロホルムを揮散除去した。
Implementation Ij44 Powder 4 obtained by pulverizing the porous base of the present invention obtained in Example 1 and comparative toner powder and dividing it into 250 to 420μ gourds.
.. 0.5g of butamben (p-7 minobenzoic acid n) in 5g
-7'f ester) developed in chloroform so that the amount was within the solvent absorption limit of each powder, and the entire amount of the solution was absorbed. This was dried in Drying 5 for 20°03 hours to volatilize and remove chloroform.

このブタンベン吸収後の基剤0.15gを300m1の
37℃PH7,4のりん酸緩衝液に浸漬し、300rp
mで攪はんを行いながら所定時間毎に、ブタンベンの水
への溶出量を吸光光度計で測定した。
After absorbing this butaneben, 0.15 g of the base was immersed in 300 ml of phosphate buffer solution at 37°C, pH 7.4, and heated at 300 rpm.
While stirring at m, the amount of butaneben eluted into water was measured at predetermined intervals using an absorptiometer.

結果を第3表に示した。The results are shown in Table 3.

II3表 手続補正I(方式) 昭和61年6J18日 1、事件の表示 昭和61年特許願第54334号。II3 table Procedural amendment I (method) 6J18, 1985 1.Display of the incident Patent Application No. 54334 of 1985.

2、発明の名称 多孔性基剤 3、補正をする者 事件との関係 特許出願人 4、補正命令の(」付は 昭和61年 5月 7日 5、補正の対象 明細丼及び図面 6、補正の内容 (1)明細書第13頁第4〜6行に「またアルミニウム
イソプロポキシドを・・・・・・・・第1図に示した。
2. Name of the invention Porous base 3. Relationship with the case of the person making the amendment Patent applicant 4. The amendment order was dated May 7, 1986. 5. Specification to be amended and drawings 6. Amendment Contents (1) Page 13 of the specification, lines 4 to 6: ``Aluminum isopropoxide is also shown in Figure 1.

」とあるを全文削除する。'' is deleted in its entirety.

(2)同ff1lQ頁第1〜4行の図面の簡単な説明の
欄を全文削除する。
(2) Delete the entire text of the brief description of the drawing column in lines 1 to 4 of the same page ff1lQ.

(3)図面の第1図を削除する。(3) Delete Figure 1 of the drawings.

Claims (1)

【特許請求の範囲】[Claims] ポリラクチド、ポリグリコリド、又はそれらの共重縮合
体とアルミニウムアルコレートとを反応させてなる多孔
性基剤
A porous base obtained by reacting polylactide, polyglycolide, or a copolycondensate thereof with aluminum alcoholate.
JP61054334A 1986-03-11 1986-03-11 Porous base material Granted JPS62209146A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61054334A JPS62209146A (en) 1986-03-11 1986-03-11 Porous base material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61054334A JPS62209146A (en) 1986-03-11 1986-03-11 Porous base material

Publications (2)

Publication Number Publication Date
JPS62209146A true JPS62209146A (en) 1987-09-14
JPH0323100B2 JPH0323100B2 (en) 1991-03-28

Family

ID=12967702

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61054334A Granted JPS62209146A (en) 1986-03-11 1986-03-11 Porous base material

Country Status (1)

Country Link
JP (1) JPS62209146A (en)

Also Published As

Publication number Publication date
JPH0323100B2 (en) 1991-03-28

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