JPS6399009A - Production of sustained release formulation - Google Patents
Production of sustained release formulationInfo
- Publication number
- JPS6399009A JPS6399009A JP61271226A JP27122686A JPS6399009A JP S6399009 A JPS6399009 A JP S6399009A JP 61271226 A JP61271226 A JP 61271226A JP 27122686 A JP27122686 A JP 27122686A JP S6399009 A JPS6399009 A JP S6399009A
- Authority
- JP
- Japan
- Prior art keywords
- alcohol
- hydrophobic
- solid particles
- binder
- drug
- 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
Links
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- Medicinal Preparation (AREA)
Abstract
Description
【発明の詳細な説明】
11上五1」11
本発明は特効性製剤の製造法に関し、さらに詳しくは、
薬剤を含有する固体粒子を疎水性固体物質で被覆して持
効性製剤を製造するための簡便で効率のよい方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a specific drug, and more specifically,
The present invention relates to a simple and efficient method for producing sustained-release preparations by coating solid particles containing a drug with a hydrophobic solid substance.
従来の技術
従来から、薬剤含有固体粒子の表面を疎水性物質で被覆
することにより、薬剤の放出が遅延化された持効性製剤
は知られている。そのような持効性製剤の製造法として
は、疎水性固体物質を有機溶媒に溶解し、得られる溶液
を薬剤含有固体粒子の表面に噴霧し、乾燥することによ
り薬剤含有固体粒子を疎水性固体物質でコーティングす
る方法や、有機溶媒を用いずに、疎水性固体物質の加熱
溶融物を薬剤含有固体粒子の表面に直接噴霧して、該薬
剤含有固体粒子の表面に該疎水性固体物質のコーティン
グを形成する方法等が挙げられる。BACKGROUND ART Sustained-release preparations in which the release of a drug is delayed by coating the surface of drug-containing solid particles with a hydrophobic substance have been known. The manufacturing method for such sustained-release preparations involves dissolving a hydrophobic solid substance in an organic solvent, spraying the resulting solution onto the surface of drug-containing solid particles, and drying the drug-containing solid particles to form a hydrophobic solid. Coating the surface of the drug-containing solid particles with the hydrophobic solid substance by directly spraying a heated melt of the hydrophobic solid substance onto the surface of the drug-containing solid particles without using a coating method or an organic solvent. Examples include a method of forming a .
明が解決しようとする間 点
しかしながら、前者の方法では、通常有機溶媒として、
人体に有害な四塩化炭素、クロロホルム−等のハロゲン
化炭化水素;ヘキサン、ベンゼン等の灰化水素;メタノ
ール、プロパツール等の低級アルコール;およびアセト
ン等のケトン類が使用されているので、持効性製剤の製
造上、作業者等への安全性を確保し、また大気汚染の防
止を図るために多大の設備を必要とする。また、かかる
有機溶媒が比較的多量に使用きれるため、コーテイング
後の製剤中からこれらの溶媒を除去するのに多大の時間
たとえば8〜10時間もの時間を要して、製剤の製造効
率が極めて悪い等の問題点がある。However, in the former method, usually as an organic solvent,
Halogenated hydrocarbons such as carbon tetrachloride and chloroform, which are harmful to the human body; hydrogen ash such as hexane and benzene; lower alcohols such as methanol and propatool; and ketones such as acetone are used, so they have a long-lasting effect. In manufacturing sex preparations, a large amount of equipment is required to ensure safety for workers and to prevent air pollution. In addition, since a relatively large amount of such organic solvents can be used, it takes a long time, for example, 8 to 10 hours, to remove these solvents from the coated preparation, resulting in extremely poor preparation efficiency. There are other problems.
一方、これらの問題点を回避するために開発された上記
後者の方法は、疎水性物質を溶融するための溶融釜;及
び配管や噴霧ノズル中で溶融した疎水性物質が固化しな
いように該配管やノズルを高温度に保持するための設備
を必要とする。また、薬剤含有固体粒子表面を均一に疎
水性物質で被覆するためには、該疎水性物質の溶融物を
非常に細かくして噴霧する必要があり、そのためには高
圧で液滴をノズルから噴霧するための高圧装置を必要と
する等の問題点がある。さらに、この方法は、被覆作業
後の洗浄清掃が煩雑でかなり時間を要して、作業効果を
低下させる。On the other hand, the latter method, which was developed to avoid these problems, uses a melting pot for melting the hydrophobic substance; requires equipment to maintain the nozzle and nozzle at high temperatures. In addition, in order to uniformly coat the surface of drug-containing solid particles with a hydrophobic substance, it is necessary to spray the melted substance of the hydrophobic substance in extremely fine particles, and to do this, droplets must be sprayed from a nozzle under high pressure. There are problems such as the need for high-pressure equipment. Furthermore, in this method, cleaning after the coating operation is complicated and takes a considerable amount of time, reducing the efficiency of the operation.
本発明の目的は、従来法における上記のごとき問題点を
解消した特効性製剤の製造法を提供することである。An object of the present invention is to provide a method for producing a specific drug that eliminates the above-mentioned problems of conventional methods.
かくして、本発明の主たる目的は、疎水性固体物質を溶
解するための前記のごとき有害な有機溶媒の使用の必要
性を排し、また、疎水性物質を溶融するための溶融釜、
配管やノズルの保温のための設備、高圧ノズル等を必要
とすることなく、優れた薬剤の持続放出性を発揮する特
効性製剤を、簡便かつ容易に製造する方法を提供するこ
とである。Thus, a principal object of the present invention is to eliminate the need for the use of harmful organic solvents as described above for dissolving hydrophobic solid substances, and to provide a melt kettle for melting hydrophobic substances;
It is an object of the present invention to provide a simple and easy method for producing a specific drug that exhibits excellent sustained drug release properties without requiring equipment for keeping piping or nozzles warm, high-pressure nozzles, etc.
間 、を 決するための手段
本発明によれば、薬剤を含有する固体粒子を転動許せな
がら、該固体粒子の表面に、結合剤の水又はアルコール
溶液を噴霧し、かつ胃及び腸で容易に溶解しない疎水性
固体物質の微粉末を散布し、それによって該固体粒子を
該結合剤及び該疎水性固体物質で被覆することを特徴と
する特効性製剤の製造方法が提供される。According to the present invention, a water or alcoholic solution of a binder is sprayed onto the surface of solid particles containing a drug while allowing them to tumble, and the solid particles are easily absorbed in the stomach and intestines. A method for producing a specific drug is provided, characterized in that a fine powder of an undissolved hydrophobic solid substance is dispersed, thereby coating the solid particles with the binder and the hydrophobic solid substance.
本発明の方法に従い特効性のコーティングが施される薬
剤を含有する固体粒子は、薬剤(薬理学的に活性のある
物質)の一種または二種以上を、固形製剤の製造に際し
て慣用の担体、例えばトウモロコシデンプン、バレイシ
ョデンブン、乳糖りηマンニット等の賦形製剤、メタケ
イ酸アルミン酸マグネシウム、軽質無水ケイ酸、タルク
等の滑沢剤、カルボキシメチルセルロースカルシウム置
度ヒドロキシプロピルセルロース、微結晶セルロース等
の崩壊剤、ヒドロキシプロピルセルロース、ヒドロキシ
プロピルメチルセルロース、ポリビニルピロリドン等の
結合剤と共に固体粒子状に形成することにより製造され
る。その際固体粒子は顆粒状、ミニベレット状、ピル状
綿任意の形態に形成することができ、その大きさは平均
粒径で表現して一般に250〜3000ミクロンの範囲
、好ましくは500〜1500ミクロンの範囲内にある
ことが適当である。また、この固体粒子は、類似の形態
を有するものであれば、薬剤自身の結晶であっても良い
。The drug-containing solid particles to which a specific coating is applied according to the method of the present invention can be prepared by transporting one or more drugs (pharmacologically active substances) to carriers customary for the production of solid preparations, such as Excipients such as corn starch, potato starch, lactose mannitol, etc., lubricants such as magnesium aluminate metasilicate, light anhydrous silicic acid, talc, carboxymethyl cellulose calcium, hydroxypropyl cellulose, microcrystalline cellulose, etc. It is produced by forming solid particles together with a disintegrant and a binder such as hydroxypropylcellulose, hydroxypropylmethylcellulose, or polyvinylpyrrolidone. In this case, the solid particles can be formed into any form such as granules, mini-vellets, or pill-like cotton, and their size, expressed as an average particle size, is generally in the range of 250 to 3000 microns, preferably 500 to 1500 microns. It is appropriate that the value be within the range of . Further, the solid particles may be crystals of the drug itself as long as they have a similar morphology.
また、かかる固体粒子に含ませうる薬剤としては、哺乳
動物の体内での徐放性を望まれるものである限り同等制
限はなく任意の薬剤であることができ、具体的には例え
ば、インドメタシン、イブプロフェン、アセトアミノフ
ェン等の鎮痛消炎剤;マレイン酸クロルフェニラミン等
の抗ヒスタミン剤;ニフェジピン、硝酸インソルビット
、プロプラノロール等の循環器用剤:フマル酸第−鉄等
の鉄剤;セファレキシン等の抗生物質;テオフィリン等
の抗喘息剤;塩化カリウム等のカリウム剤;塩酸チオリ
ダジン等の請神安定剤;カルバミン酸クロルフェネシン
等の筋弛緩剤;炭酸リチウム停の抗繰剤が挙げられる。Further, as the drug that can be contained in such solid particles, there is no equivalent restriction and any drug can be used as long as sustained release in the body of a mammal is desired.Specifically, for example, indomethacin, Analgesic and anti-inflammatory agents such as ibuprofen and acetaminophen; antihistamines such as chlorpheniramine maleate; cardiovascular agents such as nifedipine, insorbitol nitrate, and propranolol; iron preparations such as ferrous fumarate; antibiotics such as cephalexin; theophylline, etc. anti-asthmatic agents; potassium agents such as potassium chloride; tranquilizers such as thioridazine hydrochloride; muscle relaxants such as chlorphenesin carbamate; and anti-inflammatory agents such as lithium carbonate.
薬剤含有固体粒子の調製はそれ自体既知の転動造粒法を
用いて行なうことができる。例えば、40〜50メツシ
ユの砂糖結晶を舞動造粒機に仕込み、結合剤溶液の噴霧
と同時に、前記の薬剤及び担体を散布することによって
、薬物含有固体粒子を製造することができる。上記のご
とくして一旦調製した薬剤含有固体粒子に対して適当な
転動装置中で行なうのが好都合である。The drug-containing solid particles can be prepared using a rolling granulation method known per se. For example, drug-containing solid particles can be produced by charging 40 to 50 meshes of sugar crystals into a floating granulator and simultaneously spraying the binder solution and dispersing the drug and carrier. It is convenient to carry out the treatment in a suitable rolling device on the drug-containing solid particles once prepared as described above.
本発明の方法は、転動造粒機等の粒子転動装置中で、前
記のごとくして調製きれた薬剤含有固体粒子を転動させ
ながら、該固体粒子に結合剤の水又はアルコール溶液を
噴霧し、かつ胃及び腸で容易には溶解しない疎水性固体
物質微粉末を散布することにより実施きれる。その好適
な一方法においては、該固体粒子を転動させつつ、該固
体粒子に結合剤の溶液を噴霧し、その噴霧とほぼ同時的
に該疎水性固体物質微粉末を少しずつ散布するか、ある
いは所定量の結合剤溶液の噴霧が終わった直後に該疎水
性固体物質微粉末を散布し、この操作を繰り返し行なう
。これによって、結合剤溶液により湿潤された固体粒子
の表面に疎水性固体物質の微粉末が付着し、該疎水性固
体物質の微粉末が該固体粒子の表面を被覆するようにな
る。The method of the present invention involves rolling the drug-containing solid particles prepared as described above in a particle rolling device such as a rolling granulator, while adding a water or alcohol solution of a binder to the solid particles. It can be carried out by spraying and dispersing a fine powder of a hydrophobic solid substance that does not easily dissolve in the stomach and intestines. In one preferred method, a solution of the binder is sprayed onto the solid particles while rolling the solid particles, and almost simultaneously with the spraying, the fine powder of the hydrophobic solid substance is gradually dispersed; Alternatively, immediately after spraying a predetermined amount of the binder solution, the fine powder of the hydrophobic solid substance is sprinkled, and this operation is repeated. As a result, the fine powder of the hydrophobic solid substance adheres to the surface of the solid particles wetted with the binder solution, and the fine powder of the hydrophobic solid substance coats the surface of the solid particle.
このようにして、疎水性固体物質の微粉末で被覆きれた
固体粒子は乾燥することにより、該結合剤溶液に使用し
た溶媒を除去する。乾燥温度は該溶媒の種類により一般
に約40〜約70’C,好ましくは60〜70℃の範囲
内であり、また、乾燥時間としては通常0.5〜1時間
時間色することができる。The solid particles coated with the fine powder of the hydrophobic solid substance in this manner are dried to remove the solvent used in the binder solution. The drying temperature is generally in the range of about 40 to about 70'C, preferably 60 to 70'C, depending on the type of solvent, and the drying time is usually 0.5 to 1 hour.
上記本発明の方法において使用されうる結合剤には、水
又はアルコールに可溶性の薬学的に許容される高分子物
質が包含きれ、例えばメチルセルロース、エチルセルロ
ース、ヒドロキシメチルセルロース、ヒドロキシエチル
セルロース、ヒドロキシプロピルセルロース、ヒドロキ
シプロピルメチルセルロース等のセルロース誘導体;ポ
リビニルピロリドン、ポリビニルアルコール等の水溶性
合成高分子物質が挙げられる。これらはそれぞれ単独で
使用することができ、あるいは二種又はそれ以上併用し
てもよい。これらの中、特にメチルセルロースおよびエ
チルセルロースが好適である。Binders that can be used in the method of the present invention include pharmaceutically acceptable polymeric substances that are soluble in water or alcohol, such as methylcellulose, ethylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxypropylcellulose, etc. Examples include cellulose derivatives such as methylcellulose; water-soluble synthetic polymer substances such as polyvinylpyrrolidone and polyvinyl alcohol. Each of these can be used alone, or two or more kinds can be used in combination. Among these, methylcellulose and ethylcellulose are particularly preferred.
一方、上記結合剤を溶解するための溶媒としては、水の
他に、エタノールのごとき無毒性のアルコールもまた使
用することができる。On the other hand, as a solvent for dissolving the binder, in addition to water, non-toxic alcohol such as ethanol can also be used.
これらの溶媒中における結合剤の含量は厳密に制限され
るものではなく、薬剤含有固体粒子の種類や形態、疎水
性固体物質の種類、結合剤の種類等に応じて変えること
ができる。The content of the binder in these solvents is not strictly limited, and can be changed depending on the type and form of the drug-containing solid particles, the type of hydrophobic solid substance, the type of binder, etc.
上記結合剤溶液の薬剤含有固体粒子への噴霧は、例えば
噴霧ノズルを用いて行なうことができる。The binder solution can be sprayed onto the drug-containing solid particles using, for example, a spray nozzle.
また、本発明の方法において使用する疎水性固体物質は
、胃及び腸では容易に溶解しないが、該物質と上記結合
剤とから形成きれる被覆を通して薬剤含有固体粒子から
薬剤を徐々に放出することが可能な常温で固体の物質が
包含きれ、特に融点が50〜90°Cの範囲内にある疎
水性固体物質が適している。そのような疎水性固体物質
は、常温で固体の、高級アルコール、高級脂肪酸、高級
脂肪酸グリセリンエステル、油脂類、ワックス類及び高
級炭化水素等の中から選ぶことができる。Furthermore, although the hydrophobic solid substance used in the method of the present invention does not easily dissolve in the stomach and intestines, it is possible to gradually release the drug from the drug-containing solid particles through the coating formed from the substance and the binder. Substances that are solid at possible normal temperatures can be included, and hydrophobic solid substances having a melting point within the range of 50 to 90°C are particularly suitable. Such hydrophobic solid substances can be selected from higher alcohols, higher fatty acids, glycerin esters of higher fatty acids, oils and fats, waxes, higher hydrocarbons, etc. that are solid at room temperature.
前記高級アルコールとしては、たとえば、セチルアルコ
ール
1、ステアリルアルコール、16−メチルオクタデカノ
ール−1、エイコサノール−1、18−メチルノナデカ
ノール−1、18−メチルエイコサノール22−メチル
テトラコサノール−1,24−メチルペンタコサノール
−1,24−メチルヘキサフサノール−1、オクタコサ
ノール−1、ノナコサノール−1、ミリシルアルフーJ
L−、コレスチ尋ロール等が挙げられ、これら高級アル
コールの中でも炭素原子数16〜26個のもの、殊にス
テアリルアルコールが好ましい。Examples of the higher alcohol include cetyl alcohol 1, stearyl alcohol, 16-methyloctadecanol-1, eicosanol-1, 18-methylnonadecanol-1, 18-methyleicosanol 22-methyltetracosanol- 1,24-methylpentacosanol-1,24-methylhexafsanol-1, octacosanol-1, nonacosanol-1, myricylalfu J
Among these higher alcohols, those having 16 to 26 carbon atoms, particularly stearyl alcohol, are preferred.
前記高級脂肪酸としては、たとえば、ミリスチン酸、バ
ルミチン酸、ステアリン酸、ベヘン酸、12−ヒドロキ
システアリン酸等が挙げられ、これら高級脂肪酸の中で
も、炭素原子数14〜22個のもの、殊にステアリン酸
が好ましい。Examples of the higher fatty acids include myristic acid, balmitic acid, stearic acid, behenic acid, 12-hydroxystearic acid, etc. Among these higher fatty acids, those having 14 to 22 carbon atoms, especially stearic acid. is preferred.
前記高級脂肪酸グリセリンエステルとしては、たとえば
、前記高級脂肪酸とグリセリンとのモノグリセリド、ジ
グリセリド、トリグリセリド等が挙げられる。Examples of the higher fatty acid glycerin ester include monoglycerides, diglycerides, and triglycerides of the higher fatty acids and glycerin.
油脂類としては、たとえば、硬化大豆油、硬化ヒマシ油
、モクロウ、硬化生還、硬化豚脂等が挙げられ、これら
油脂類の中でも特に硬化ヒマシ油が好ましい。Examples of the fats and oils include hydrogenated soybean oil, hydrogenated castor oil, Japanese wax, hardened lard, and hardened lard, and among these fats and oils, hydrogenated castor oil is particularly preferred.
前記ロウ類としては、たとえば、カルナウバロウ、硬質
ラノリン、カンデリラロウ、ミツロウ等が挙げられ、こ
れらロウ類の中でも、カルナウバロウが特に好ましい。Examples of the waxes include carnauba wax, hard lanolin, candelilla wax, and beeswax, and among these waxes, carnauba wax is particularly preferred.
前記高級炭化水素としては、たとえば、パラフィン、セ
レシン、マイクロクリスタリンワックス等の好ましくは
炭素原子数16〜70個の炭化水素が挙げられ、特にパ
ラフィンが好ましい。Examples of the higher hydrocarbons include hydrocarbons preferably having 16 to 70 carbon atoms, such as paraffin, ceresin, and microcrystalline wax, with paraffin being particularly preferred.
上記の疎水性固体物質は微粉末状で使用される。その粒
径は、芯となる薬剤含有固体粒子の粒径よりも十分に小
さくなければならない。その粒υ
径甲一般に100ミクロン以下、好ましくは10〜30
ミクロンの範囲内であることが望ましい。該疎水性固体
物質の粒径及び付itを適当に選択することにより、被
覆された薬剤含有固体粒子からの薬剤の放出をコントロ
ールすることができる。The hydrophobic solid substances mentioned above are used in fine powder form. The particle size must be sufficiently smaller than the particle size of the core drug-containing solid particles. The particle size υ is generally less than 100 microns, preferably 10 to 30 microns.
Preferably, it is in the micron range. By appropriately selecting the particle size and adhesion of the hydrophobic solid material, the release of the drug from the coated drug-containing solid particles can be controlled.
以上述べた結合剤及び疎水性固体物質微粉末の使用量は
厳密に制限きれるものではなく、薬剤の種類、該薬剤を
含む固体粒子の形状や大きさ、結合剤の種類、疎水性固
体物質微粉末の種類や粒径等に応じて変えることができ
るが、一般には、結合剤は該疎水性固体物質100重量
部当り1〜30重量部、好ましくは5〜15重量部の範
囲内の量で使用する。また、疎水性固体物質は、前記薬
剤含有固体粒子100重量部肖り5〜60重量部、好ま
しくは10〜40重量部の範囲内の量で使用し、該薬剤
含有固体粒子の表面が疎水性固体物質の微粉末により均
一に被覆されるようにするのが望ましい。The amount of the binder and the hydrophobic solid substance fine powder described above is not strictly limited, but may be affected by the type of drug, the shape and size of the solid particles containing the drug, the type of binder, the hydrophobic solid substance fine powder, etc. Although it can be varied depending on the type and particle size of the powder, generally the amount of the binder is within the range of 1 to 30 parts by weight, preferably 5 to 15 parts by weight, per 100 parts by weight of the hydrophobic solid material. use. The hydrophobic solid substance is used in an amount of 5 to 60 parts by weight, preferably 10 to 40 parts by weight, based on 100 parts by weight of the drug-containing solid particles, so that the surface of the drug-containing solid particles is hydrophobic. It is desirable to have a uniform coating with a fine powder of solid material.
前記の結合剤及び疎水性固体物質の微粒子が被覆された
薬剤含有固体粒子は、前記の条件下で乾燥することによ
り、目的とす、る持効性製剤を得ることができる。By drying the drug-containing solid particles coated with the binder and fine particles of the hydrophobic solid substance under the conditions described above, the desired sustained-release preparation can be obtained.
さらに、本発明に従えば、このようにして製造された特
効性製剤を、該疎水性固体物質の溶融温度以上の温度で
且つ望ましくは、該溶融温度プラス30°Cまでの範囲
内の温度で加熱処理することにより、結合剤及び疎水性
固体物質からなる持効性のコーティングをより緻密なも
のとすることができる。該加熱処理の条件は、上記の温
度範囲、好ましくは70〜90℃の範囲の温度及び約0
.5〜10時間、好ましくは1〜3時間とすることがで
きる。Furthermore, according to the invention, the specific-effect formulation thus produced is prepared at a temperature above the melting temperature of the hydrophobic solid substance and preferably at a temperature within the range of the melting temperature plus 30°C. Heat treatment can make the long-acting coating of binder and hydrophobic solid material more dense. The conditions for the heat treatment include the above-mentioned temperature range, preferably a temperature in the range of 70 to 90°C, and a temperature of about 0.
.. The time can be 5 to 10 hours, preferably 1 to 3 hours.
上記の加熱処理は例えば、流動層乾燥機等により行なう
ことができる。The above heat treatment can be performed using, for example, a fluidized bed dryer.
しかして、疎水性固体物質の使用量及び粒径並びに加熱
処理条件を適宜選択することにより、薬剤含有固体粒子
上の持効性のコーティングの厚さと緻密度を調節し、そ
れによって該固体粒子からの薬剤の放出を自由にコント
ロールできる。Therefore, by appropriately selecting the amount and particle size of the hydrophobic solid substance used and the heat treatment conditions, the thickness and density of the long-lasting coating on the drug-containing solid particles can be adjusted, thereby allowing the solid particles to be separated from the solid particles. drug release can be freely controlled.
以上述べた本発明の方法によれば、何ら特別の装置を用
いることなく、経済的に簡便かつ容易に薬剤を持続的に
放出きせる製剤を製造することができる。According to the method of the present invention described above, it is possible to economically, simply and easily produce a preparation that can continuously release a drug without using any special equipment.
火」1倒
次にこの発明の実施例および試験例を示してこの発明を
更に具体的に説明する。Next, the present invention will be explained in more detail by showing examples and test examples of the present invention.
実施例1
転動造粒法により、40〜50メツシユの砂IM結晶2
00gに対し、結合剤としてヒドロキシブ口ピルセルロ
ース5%水溶液290gを徐々に噴霧すると同時に、無
水カフェイン300gとトウモロコシデンプン500g
を混合した粉末を徐々に散布し、散布終了後、造粒物を
60°Cで1時間乾燥し、篩を用い、16〜32メツシ
ユの粒子径のカフェインを含む球形顆粒を調製した。Example 1 Sand IM crystals 2 of 40 to 50 meshes were produced by rolling granulation method.
00g, gradually sprayed 290g of a 5% aqueous solution of hydroxybupil cellulose as a binder, and at the same time added 300g of anhydrous caffeine and 500g of corn starch.
After the spraying was completed, the granules were dried at 60° C. for 1 hour, and using a sieve, spherical granules containing caffeine with a particle size of 16 to 32 mesh were prepared.
直径36cmの転動造粒機を用い、毎分150回転で回
転させ、この中に前記のカフェインを含む球形顆粒50
0gを仕込み、転動させ、この顆粒表面に結合剤として
エチルセルロース8gをエチルアルコール192gに溶
かした溶液を毎分20m1lの速度で噴霧しながら、そ
れと同時に平均粒子径30ミクロンの硬化ヒマシ油10
0gを徐々に散布し、その被覆を終了した。A rolling granulator with a diameter of 36 cm was used and rotated at 150 revolutions per minute to form 50 spherical granules containing the above-mentioned caffeine.
A solution of 8 g of ethyl cellulose dissolved in 192 g of ethyl alcohol as a binder was sprayed on the surface of the granules at a rate of 20 ml/min, while at the same time hydrogenated castor oil 10
0g was gradually spread and the coating was completed.
この顆粒物を70″Cで1時間乾燥して持効性製剤(製
剤1)を得た。The granules were dried at 70''C for 1 hour to obtain a sustained-release preparation (Formulation 1).
実施例2
エチルセルロース15g1エチルアルフール360g1
球形顆粒(カフェイン含有量H300ng/g−実施例
1で用いたものと同じもの) 500g%および平均粒
子径30ミクロンの硬化ヒマシ油200gを使用して前
記実施例1と同様にして持効性製剤(製剤2)を得た。Example 2 Ethylcellulose 15g1 Ethyl alfur 360g1
Spherical granules (caffeine content H 300 ng/g - same as used in Example 1) Long-acting as in Example 1 above using 200 g of hydrogenated castor oil with 500 g% and average particle size of 30 microns A formulation (Formulation 2) was obtained.
実施例3
エチルセルロース22g1エチルアルコール528g、
球形顆粒(カフェイン含有量; 300+yg/g−実
施例1で用いたものと同じもの) 500g、および平
均粒子径30ミクロンの硬化ヒマシ油300gを使用し
て前記実施例1と同様にして持効性製剤(製剤3)を得
た。Example 3 22 g of ethyl cellulose 528 g of ethyl alcohol,
A sustained effect was obtained in the same manner as in Example 1 using 500 g of spherical granules (caffeine content; 300+yg/g - the same as used in Example 1) and 300 g of hydrogenated castor oil with an average particle size of 30 microns. A sex preparation (Formulation 3) was obtained.
実施例4
平均粒子径30ミクロンの硬化ヒマシ油100gの代わ
りに平均粒子径15ミクロンのカルナウバロウ100g
を使用する外は前記実施例1と同様にして特効性製剤(
製剤4)を得た。Example 4 100 g of carnauba wax with an average particle size of 15 microns instead of 100 g of hydrogenated castor oil with an average particle size of 30 microns
A specific drug (
Formulation 4) was obtained.
実施例5
平均粒子径30ミクロンの硬化ヒマシ油200gの代わ
りに平均粒子径15ミクロンのカルナウバロウ200g
を使用するほかは前記実施例2と同様にして特効性製剤
(製剤5)を得た。Example 5 200 g of carnauba wax with an average particle size of 15 microns instead of 200 g of hydrogenated castor oil with an average particle size of 30 microns
A specific-effect formulation (Formulation 5) was obtained in the same manner as in Example 2 except that .
実施例6
平均粒子径30ミクロンの硬化ヒマシ油300gの代わ
りに平均粒子径15ミクロンのカルナウバロウ300g
を使用するほかは前記実施例3と同様にして持効性製剤
(製剤6)を得た。Example 6 300 g of carnauba wax with an average particle size of 15 microns instead of 300 g of hydrogenated castor oil with an average particle size of 30 microns
A sustained-release preparation (Formulation 6) was obtained in the same manner as in Example 3 except that .
実施例7
平均粒子径30ミクロンの硬化ヒマシ油100gの代わ
りに平均粒子径20ミクロンのステアリン酸100gを
使用するほかは前記実施例1と同様にして特効性製剤(
製剤7)を得た。Example 7 A specific-effect preparation (
Formulation 7) was obtained.
実施例8
平均粒子径30ミクロンの硬化ヒマシ油200gの代わ
りに平均粒子径20ミクロンのステアリン酸200gを
使用するほかは前記実施例2と同様にして持効性製剤(
製剤8)を得た。Example 8 A sustained-release preparation (
Formulation 8) was obtained.
実施例9
平均粒子径30ミクロンの硬化ヒマシ油300gの代わ
りに平均粒子径20ミクロンのステアリン9300gを
使用する外は前記実施例3と同様にして特効性製剤(製
剤9)を得た。Example 9 A specific-effect formulation (Formulation 9) was obtained in the same manner as in Example 3 except that 9300 g of stearin with an average particle size of 20 microns was used instead of 300 g of hydrogenated castor oil with an average particle size of 30 microns.
実施例10
平均粒子径30ミクロンの硬化ヒマシ油100gの代わ
りに平均粒子径25ミクロンのステアリルアルコール1
00gを使用する外は前記実施例1と同様にして持効性
製剤(製剤10)を得た。Example 10 1 stearyl alcohol with an average particle size of 25 microns instead of 100 g of hydrogenated castor oil with an average particle size of 30 microns
A sustained-release preparation (Formulation 10) was obtained in the same manner as in Example 1 except that 00g was used.
実施例11
平均粒子径30ミクロンの硬化ヒマシ油200gの代わ
りに平均粒子径25ミクロンのステアリルアルコール2
00gを使用する外は前記実施例2と同様にして特効性
製剤(製剤11)を得た。Example 11 Stearyl alcohol 2 with an average particle size of 25 microns instead of 200 g of hydrogenated castor oil with an average particle size of 30 microns
A specific-effect formulation (Formulation 11) was obtained in the same manner as in Example 2 except that 00g was used.
実施例12
平均粒子径30ミクロンの硬化ヒマシ油300gの代わ
りに平均粒子径25ミクロンのステアリルアルコール3
00gを使用するほかは前記実施例3と同様にして特効
性製剤(製剤12)を得た。Example 12 Stearyl alcohol 3 with an average particle size of 25 microns instead of 300 g of hydrogenated castor oil with an average particle size of 30 microns
A specific-effect formulation (Formulation 12) was obtained in the same manner as in Example 3 except that 00g was used.
実施例13
平均粒子径30ミクロンの硬化ヒマシ油100gの代わ
りに平均粒子径30ミクロンのパラフィン1oogを使
用するほかは前記実施例1と同様にして特効性製剤(製
剤13)を得た。Example 13 A specific-effect formulation (Formulation 13) was obtained in the same manner as in Example 1 except that 100 g of hydrogenated castor oil with an average particle size of 30 microns was replaced with 100 g of paraffin with an average particle size of 30 microns.
実施例14
平均粒子径30ミクロンの硬化ヒマシ油200gの代わ
りに平均粒子径30ミクロンのパラフィン200gを使
用するほかは前記実施例2と同様にして特効性製剤(製
剤14)を得た。Example 14 A specific-effect formulation (Formulation 14) was obtained in the same manner as in Example 2 except that 200 g of paraffin with an average particle diameter of 30 microns was used instead of 200 g of hydrogenated castor oil with an average particle diameter of 30 microns.
実施例15
平均粒子径30ミクロンの硬化ヒマシ油300gの代わ
りに平均粒子径30ミクロンのパラフィン300gを使
用するほかは前記実施例3と同様にして持効性製剤(製
剤15)を得た。Example 15 A sustained-release preparation (Formulation 15) was obtained in the same manner as in Example 3 except that 300 g of paraffin with an average particle size of 30 microns was used instead of 300 g of hydrogenated castor oil with an average particle size of 30 microns.
試験例1
前記実施例1で使用の球形顆粒を対照剤1とし、前記実
施例1〜3でそれぞれ調製した製剤1〜3と対照剤1と
について、第十改正日本薬局方、溶出試験法第2法(試
験液として精製水を使用し、適時試料を採取してカフェ
インの溶出量を測定)により、カフェインの溶出性を調
べた。Test Example 1 The spherical granules used in Example 1 were used as Control Agent 1, and preparations 1 to 3 prepared in Examples 1 to 3 and Control Agent 1 were tested according to the Japanese Pharmacopoeia, 10th Edition, Dissolution Test Method No. The elution property of caffeine was investigated by method 2 (purified water was used as the test liquid, samples were taken at appropriate times and the amount of elution of caffeine was measured).
その結果を第1図に示す。The results are shown in FIG.
試験例2
前記実施例4〜6でそれぞれ調製した製剤4〜6と対照
剤1とについて、上記試験例1におけると同様にして、
カフェインの溶出性を調べた。Test Example 2 For formulations 4 to 6 and control agent 1 prepared in Examples 4 to 6, respectively, in the same manner as in Test Example 1,
The dissolution properties of caffeine were investigated.
その結果を第2図に示す。The results are shown in FIG.
試験例3
前記実施例7〜9でそれぞれ調製した製剤7〜9と対照
剤1とについて、上記試験例1におけると同様にして、
カフェインの溶出性を調べた。Test Example 3 For formulations 7 to 9 and control agent 1 prepared in Examples 7 to 9, respectively, in the same manner as in Test Example 1,
The dissolution properties of caffeine were investigated.
その結果を第3図に示す。The results are shown in FIG.
試験例4
前記実施例10〜12でそれぞれ調製した製剤10〜1
1と対照剤1とについて、上記試験例1におけると同様
にして、カフェインの溶出性を調べた。Test Example 4 Preparations 10 to 1 prepared in Examples 10 to 12, respectively
1 and Comparative Agent 1, the elution properties of caffeine were investigated in the same manner as in Test Example 1 above.
その結果を第4図に示す。The results are shown in FIG.
試験例5
前記実施例13〜15でそれぞれ調製した製剤13〜1
5と対照剤1とについて、上記試験例1におけると同様
にして、カフェインの溶出性を調べた。Test Example 5 Preparations 13 to 1 prepared in Examples 13 to 15 respectively
5 and Comparative Agent 1, the elution properties of caffeine were investigated in the same manner as in Test Example 1 above.
その結果を第5図に示す。The results are shown in FIG.
実施例16
(1)エチルセルロース8g巳エチルアルコール192
gに溶解して結合剤溶液200gを調製した。Example 16 (1) Ethyl cellulose 8g Ethyl alcohol 192g
200 g of binder solution was prepared by dissolving in
被覆装置の中で転動している16〜32メツシユの球形
顆粒(カフェイン含有量;300■/g−実施例1で用
いたものと同じ) 500gの表面に前記結合剤溶液を
噴霧しながら、平均粒子径30ミクロンの硬化ヒマシ油
100gを徐々に散布し、これを60℃で1時間乾燥し
て顆粒(A)を得た。While spraying the binder solution onto the surface of 500 g of 16-32 mesh spherical granules (caffeine content: 300 μ/g - same as used in Example 1) rolling in a coating device. , 100 g of hydrogenated castor oil having an average particle size of 30 microns was gradually sprinkled on the mixture, and this was dried at 60° C. for 1 hour to obtain granules (A).
(2)前記<1)で得た顆粒(A>を転動させなから8
0°Cで1時間加熱処理して持効性製剤(製剤16を得
た。(2) Roll the granules (A> obtained in <1) above to 8
A sustained-release preparation (Formulation 16) was obtained by heat treatment at 0°C for 1 hour.
実施例17
実施例16(1)で得た顆粒(A)を実施例16(2)
に準じて80°Cで3時間加熱処理して持効性製剤(製
剤17)を得た。Example 17 The granules (A) obtained in Example 16 (1) were converted into Example 16 (2).
A sustained-release formulation (Formulation 17) was obtained by heat treatment at 80°C for 3 hours according to the same procedure.
実施例18
実施例16(1)で得た顆粒(A)を実施例16(2)
に準じて90°Cで1時間加熱処理して特効性製剤(製
剤18)を得た。Example 18 The granules (A) obtained in Example 16 (1) were converted into Example 16 (2).
A specific-effect formulation (Formulation 18) was obtained by heat treatment at 90°C for 1 hour.
実施例19
実施例16(1)で得た顆粒(A)を実施例16(2)
に準じて90℃で3時間加熱処理して持効性製剤(製剤
19)を得た。Example 19 The granules (A) obtained in Example 16 (1) were converted into Example 16 (2).
A sustained-release preparation (Formulation 19) was obtained by heat treatment at 90° C. for 3 hours according to the same procedure.
実施例20
(1)平均粒子径30ミクロンの硬化ヒマシ油100g
の代わりに平均粒子径15ミクロンのカルナバロウ10
0gを使用するほかは実施例16(1)と同様にして顆
粒(B)を得た。Example 20 (1) 100 g of hydrogenated castor oil with an average particle size of 30 microns
Carnauba wax 10 with an average particle size of 15 microns instead of
Granules (B) were obtained in the same manner as in Example 16 (1) except that 0 g was used.
<2)前項(1)で得た顆粒(B)を実施例16(2)
に準じて80°Cで1時間加熱処理して持効性製剤(製
剤20)を得た。<2) The granules (B) obtained in the previous section (1) were added to Example 16 (2)
A sustained-release preparation (Formulation 20) was obtained by heat treatment at 80° C. for 1 hour according to .
実施例21
実施例20(1)で得た顆粒(B)を実施例20(2)
に準じて80°Cで3時間加熱処理して持効性製剤(製
剤21)を得た。Example 21 The granules (B) obtained in Example 20(1) were converted into Example 20(2).
A sustained-release preparation (Formulation 21) was obtained by heat treatment at 80° C. for 3 hours.
実施例22
実施例20(1)で得た顆粒(B)を実施例20(2)
に準じて90°Cで1時間加熱処理して持効性製剤(製
剤22)を得た。Example 22 The granules (B) obtained in Example 20(1) were converted into Example 20(2).
A sustained-release formulation (Formulation 22) was obtained by heat treatment at 90°C for 1 hour according to .
実施例23
実施例20(1)で得た顆粒(B)を実施例20(2)
に準じて90°Cで3時間加熱処理して持効性製剤(製
剤23)を得た。Example 23 The granules (B) obtained in Example 20(1) were converted into Example 20(2).
A sustained-release preparation (Formulation 23) was obtained by heat treatment at 90° C. for 3 hours according to .
試験例6
実施例16(1)で使用の球形顆粒を対照剤1、実施例
16(1)で調製した顆粒(A)を製剤24とし、実施
例16〜19でそれぞれ調製した製剤16〜19と対照
剤1および製剤24とについて、前記試験例1における
と同様にして、カフェインの溶出性を調べた。Test Example 6 The spherical granules used in Example 16 (1) were used as control agent 1, the granules (A) prepared in Example 16 (1) were used as formulation 24, and formulations 16 to 19 were prepared in Examples 16 to 19, respectively. For Comparative Agent 1 and Formulation 24, the elution properties of caffeine were examined in the same manner as in Test Example 1 above.
その結果を第6図に示す。The results are shown in FIG.
試験例7
実施例20(1)で調製した顆粒(B)を製剤25とし
、実施例20〜23でそれぞれ調製した製剤20〜23
と対照剤1および製剤25とについて、前記試験例1に
おけると同様にして、カフェインの溶出性を調べた。Test Example 7 Granules (B) prepared in Example 20 (1) were used as Formulation 25, and Formulation 20 to 23 prepared in Examples 20 to 23, respectively.
For Comparative Agent 1 and Formulation 25, the elution properties of caffeine were examined in the same manner as in Test Example 1 above.
その結果を第7図に示す。The results are shown in FIG.
第1図〜第7図は、実施例で調製した製剤および対照剤
についての溶出試験結果を示す溶出率一時間特性図であ
る。FIG. 1 to FIG. 7 are dissolution rate one-hour characteristic diagrams showing the dissolution test results for the preparations prepared in the examples and the control agent.
Claims (9)
体粒子の表面に、結合剤の水又はアルコール溶液を噴霧
し、かつ胃及び腸で容易に溶解しない疎水性固体物質の
微粒子を散布し、それによって該固体粒子を該結合剤及
び該疎水性固体物質で被覆することを特徴とする持効性
製剤の製造方法。(1) While rolling the solid particles containing the drug, spray a water or alcohol solution of the binder onto the surface of the solid particles, and scatter fine particles of a hydrophobic solid substance that does not easily dissolve in the stomach and intestines. and thereby coating the solid particles with the binder and the hydrophobic solid substance.
容される高分子物質である特許請求の範囲第1項記載の
方法。(2) The method according to claim 1, wherein the binder is a pharmaceutically acceptable polymeric substance soluble in water or alcohol.
ルロースである特許請求の範囲第2項記載の方法。(3) The method according to claim 2, wherein the polymeric substance is methylcellulose or ethylcellulose.
範囲第1項記載の方法。(4) The method according to claim 1, wherein the alcohol is ethyl alcohol.
ール、高級脂肪酸、高級脂肪酸グリセリンエステル、油
脂、ワックス類及び高級炭化水素から選ばれる特許請求
の範囲第1項記載の方法。(5) The method according to claim 1, wherein the hydrophobic biosolid substance is selected from higher alcohols, higher fatty acids, higher fatty acid glycerin esters, oils and fats, waxes, and higher hydrocarbons that are solid at room temperature.
アリン酸、硬化ヒマシ油、カルナウバロウ及びパラフィ
ンから選ばれる特許請求の範囲第5項記載の方法。6. The method of claim 5, wherein the hydrophobic solid material is selected from stearyl alcohol, stearic acid, hydrogenated castor oil, carnauba wax, and paraffin.
求の範囲第1項記載の方法。(7) The method according to claim 1, wherein the coated solid particles are further heat-treated.
温度プラス30℃までの温度で行なう特許請求の範囲第
7項記載の方法。(8) The method according to claim 7, wherein the heat treatment is performed at a temperature from the melting temperature of the hydrophobic solid substance to the melting temperature plus 30°C.
状である特許請求の範囲第1項記載の方法。(9) The method according to claim 1, wherein the solid particles are in the form of granules, mini-pellets, or pills.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61271226A JPH0764726B2 (en) | 1985-11-15 | 1986-11-14 | Method for manufacturing sustained-release preparations |
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25730285 | 1985-11-15 | ||
| JP60-257302 | 1985-11-15 | ||
| JP12415886 | 1986-05-29 | ||
| JP61-124158 | 1986-05-29 | ||
| JP61271226A JPH0764726B2 (en) | 1985-11-15 | 1986-11-14 | Method for manufacturing sustained-release preparations |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6399009A true JPS6399009A (en) | 1988-04-30 |
| JPH0764726B2 JPH0764726B2 (en) | 1995-07-12 |
Family
ID=27314873
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61271226A Expired - Fee Related JPH0764726B2 (en) | 1985-11-15 | 1986-11-14 | Method for manufacturing sustained-release preparations |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0764726B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH037220A (en) * | 1989-03-30 | 1991-01-14 | Yoshitomi Pharmaceut Ind Ltd | Stable tablet containing alkylcysteine or acid addition salt thereof |
| EP0508653A1 (en) | 1991-04-08 | 1992-10-14 | Tanabe Seiyaku Co., Ltd. | Sustained-release pharmaceutical preparation and process for preparing the same |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005005566A2 (en) * | 2003-07-14 | 2005-01-20 | Superseal Ltd. | Hydrophobic composites and particulates and applications thereof |
| JP7482645B2 (en) * | 2020-02-18 | 2024-05-14 | 沢井製薬株式会社 | Method for producing granules containing core particles |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5138413A (en) * | 1974-09-25 | 1976-03-31 | Freunt Ind Co Ltd | JOZAISEIZOHO |
-
1986
- 1986-11-14 JP JP61271226A patent/JPH0764726B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5138413A (en) * | 1974-09-25 | 1976-03-31 | Freunt Ind Co Ltd | JOZAISEIZOHO |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH037220A (en) * | 1989-03-30 | 1991-01-14 | Yoshitomi Pharmaceut Ind Ltd | Stable tablet containing alkylcysteine or acid addition salt thereof |
| EP0508653A1 (en) | 1991-04-08 | 1992-10-14 | Tanabe Seiyaku Co., Ltd. | Sustained-release pharmaceutical preparation and process for preparing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0764726B2 (en) | 1995-07-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |