JPS6168412A - Freeze-drying of medicine - Google Patents
Freeze-drying of medicineInfo
- Publication number
- JPS6168412A JPS6168412A JP19026084A JP19026084A JPS6168412A JP S6168412 A JPS6168412 A JP S6168412A JP 19026084 A JP19026084 A JP 19026084A JP 19026084 A JP19026084 A JP 19026084A JP S6168412 A JPS6168412 A JP S6168412A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- aqueous solution
- concentration
- freeze
- medicine
- 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
Landscapes
- Drying Of Solid Materials (AREA)
- Medicinal Preparation (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野:
この発明は、医薬品の凍結乾燥方法の改良に関するもの
であり、注射剤等の凍結乾燥製剤の製造に利用される。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application: The present invention relates to an improvement in a method for freeze-drying pharmaceuticals, and is used in the production of freeze-dried preparations such as injections.
従来技術:
医薬品の凍結乾燥製剤は、異物の混入を回避できる点に
おいて品質的に優れた製剤であり、特に注射剤の一剤型
として多用されている。そして、従来、この種の製剤は
、水との共晶体析出濃度より低い濃度の水溶液を凍結乾
燥することによシ製造されていた。Prior Art: Freeze-dried pharmaceutical preparations are excellent quality preparations in that they can avoid contamination with foreign substances, and are often used particularly as single-dose forms of injections. Conventionally, this type of preparation has been produced by freeze-drying an aqueous solution having a concentration lower than the concentration of the eutectic precipitated with water.
解決すべき問題点;
従来の凍結乾燥法では、水との共晶体析出濃度より低い
濃度の水溶液を冷却していたため、まず氷が析出して水
溶液中の医薬品の濃度が次第に高められていた。そして
、その濃度が水との共晶体析出濃度に達すれば該共晶体
が析出するものと考えられるが、実際には凍結条件が動
的な過程(非平衡過程)であるため共晶体が析出せず、
水溶液は高濃度化され、ついには高粘度化されて、医薬
品の結晶が析出しないで溶液状態のまま固化されて、い
わゆる工/トロピー凍結体が生成していた。Problems to be solved: In the conventional freeze-drying method, an aqueous solution with a concentration lower than the eutectic precipitation concentration with water was cooled, so ice first precipitated and the concentration of the drug in the aqueous solution gradually increased. It is thought that the eutectic will precipitate when its concentration reaches the eutectic precipitation concentration with water, but in reality, the eutectic does not precipitate because the freezing conditions are a dynamic process (non-equilibrium process). figure,
The aqueous solution becomes highly concentrated and finally becomes highly viscous, and the drug crystals do not precipitate and solidify in the solution state, resulting in the formation of a so-called chemical/tropic frozen product.
この凍結体中の水分は昇華し難いため、乾燥に長時間を
要し効率的でなかった。しかも、乾燥を完全ならしめる
ためには、通常の乾燥工程に比べてより高温でより低圧
の過酷な条件を必要とし、そのだめゴム栓中の昇華性物
質までが昇華されて医薬品に付着し、凍結乾燥製剤の品
質を1氏下させるという問題もあった。Since the water in this frozen body is difficult to sublimate, drying takes a long time and is not efficient. Furthermore, in order to ensure complete drying, harsh conditions such as higher temperatures and lower pressures are required compared to normal drying processes, and as a result, even the sublimable substances in the rubber stopper sublimate and adhere to the medicine. There was also the problem of lowering the quality of the freeze-dried preparation by one degree.
問題点を解決するための手段:
この発明の発明者らは、乾燥工程で昇華される品
水分が共晶体中の氷や医薬磨結晶中の結晶水であれば乾
燥が容易である点に着目し、鋭意研究の結果、この発明
を完成した。Means for Solving the Problem: The inventors of the present invention focused on the fact that drying is easy if the product water sublimated in the drying process is ice in the eutectic or crystal water in the pharmaceutical polishing crystal. As a result of intensive research, this invention was completed.
すなわち、この発明の方法では従来技術とは逆に、凍結
されるべき水溶液の濃度が共晶体析出濃度よりも高いた
め、これを冷却するとまず医薬品の結晶が析出して水溶
液の濃度が従来法とは逆に順次低下し、共晶体析出濃度
に達したところで共晶体が確実に析出する。したがって
、凍結体の乾燥が極めて容易となり、従来法に比べてよ
り短時間に、かつより緩和な条件下に乾燥することがで
きる。That is, in the method of this invention, contrary to the prior art, the concentration of the aqueous solution to be frozen is higher than the eutectic precipitation concentration, so when it is cooled, the pharmaceutical crystals first precipitate, and the concentration of the aqueous solution is lower than that of the conventional method. On the contrary, it gradually decreases, and when the eutectic precipitation concentration is reached, the eutectic is reliably precipitated. Therefore, it becomes extremely easy to dry the frozen body, and it can be dried in a shorter time and under milder conditions than in conventional methods.
この発明の方法は、まず医薬品の水溶液を調製すること
により行われる。The method of this invention is carried out by first preparing an aqueous solution of the drug.
この発明の方法において用いられる医薬品は、温度差に
より水溶液から析出する性質を有するものであればよく
、特に限定されないが、この発明の方法により渇られる
のが凍結乾燥製剤であるという点を考慮すれば注射用医
薬品であるのが通例 ′であり、殊に注射用抗生
物質にこの発明の方法を適用するのが最も効果的である
。このような注射用抗生物質としては、例えばセファゾ
リンナトリウム、セファゾリンナトリウム等が挙げられ
る。The pharmaceutical used in the method of this invention is not particularly limited as long as it has the property of being precipitated from an aqueous solution due to a temperature difference, but it should be taken into consideration that it is a freeze-dried drug that is quenched by the method of this invention. Generally, injectable drugs are used, and it is most effective to apply the method of the present invention to injectable antibiotics. Examples of such injectable antibiotics include cefazolin sodium and cefazolin sodium.
これらの医薬品を溶解すべき水としては、この発明の方
法により得られる凍結乾燥製剤が注射剤である場合には
、注射用蒸留水が用いられる。Distilled water for injection is used as the water in which these pharmaceuticals are to be dissolved, when the freeze-dried preparation obtained by the method of the present invention is an injection.
そして、水溶液中の医薬品の濃度の上限は、室温で該医
薬品が析出する濃度より低いことが必要である。なぜな
らば、水溶液中の医薬品の濃度がこの上限値を越えると
、水溶液ではなくて懸濁液となシ、個々のバイアル中へ
の医薬品の充填量にバラツキが生ずるからである。The upper limit of the concentration of the drug in the aqueous solution needs to be lower than the concentration at which the drug precipitates at room temperature. This is because if the concentration of the drug in the aqueous solution exceeds this upper limit, the solution becomes a suspension rather than an aqueous solution, and the amount of the drug filled into each vial will vary.
まだ、水溶液中の医薬品の濃度の下限は、該医薬品と水
との共晶体の析出濃度よシ高いことが必要であり、その
理由は前述したところより明らかである。Still, the lower limit of the concentration of the drug in an aqueous solution needs to be higher than the concentration of the precipitated eutectic of the drug and water, and the reason for this is clear from the above.
この発明の方法で用いられる医薬品の水溶液の濃度は、
上記の上限値と下限値の範囲内であればよいが、上限値
に近い方が、凍結体から昇華させる水分量が少ないため
、より好ましい。なお、上記の上限濃度および下限濃度
は個々の医薬品について常法によりそれぞれ求めること
ができる。The concentration of the aqueous solution of the drug used in the method of this invention is:
It may be within the range of the above upper limit and lower limit, but it is more preferable to be closer to the upper limit because the amount of water sublimated from the frozen body is smaller. In addition, the above-mentioned upper limit concentration and lower limit concentration can be determined for each drug by a conventional method.
このようにして調製された医薬品の水溶液は、医薬品の
水溶液を充填したバイアルを、次いで凍結乾燥機内に収
容して氷点下まで冷却する。この工程はいわゆる医薬品
の晶析過程であり、医薬品の結晶が析出すると共に、水
の一部が氷結する。The aqueous pharmaceutical solution prepared in this manner is cooled to below freezing by placing the vial filled with the aqueous pharmaceutical solution in a freeze dryer. This process is a so-called pharmaceutical crystallization process, in which pharmaceutical crystals are precipitated and a portion of the water freezes.
冷却温度は医薬品の種類によっても異なるが、通常、約
−10℃前後で充分である。Although the cooling temperature varies depending on the type of medicine, a temperature around -10°C is usually sufficient.
冷却者1度が目標点に達したならば、次いで氷がM’U
解し、かつ、結晶の一部が残存する温度すなわち20℃
付近まで昇温させ、その温度で維持する。Once the cooler 1 degree reaches the target point, then the ice reaches M'U
The temperature at which the crystals dissolve and some of the crystals remain, that is, 20°C
Raise the temperature to around the same temperature and maintain it at that temperature.
結晶の一部がバイアル底部に沈積したら、常法により一
30℃付近まで冷却してバイアル中の内容物を完全に凍
結固化させる。この工程は、いわゆる結晶成長と共晶体
生成過程であり、最終的には医薬品の結晶と氷から成る
混合物が凍結体として潟られる。Once a portion of the crystals have settled at the bottom of the vial, the contents in the vial are completely frozen and solidified by cooling to around -30° C. by a conventional method. This process is a so-called crystal growth and eutectic formation process, and the final result is a mixture of pharmaceutical crystals and ice as a frozen solid.
このようにして得られる凍結体を次いで常法により加温
、減圧下に乾燥する。この工程はいわゆる乾燥過程であ
り、共晶体中の氷が昇華させられると共に、医薬品の結
晶中に結晶水が含まれている場合にはその結晶水も同時
に昇華させられる。The frozen product thus obtained is then heated and dried under reduced pressure in a conventional manner. This process is a so-called drying process, in which the ice in the eutectic is sublimated, and if crystal water of the drug is included, the crystal water is also sublimed at the same time.
乾燥工程が終了したならば、必要に応じてバイアル中の
空気を窒素置換したのち密栓して、凍結乾燥製剤が得ら
れる。When the drying process is completed, the air in the vial is replaced with nitrogen if necessary, and the vial is tightly capped to obtain a lyophilized preparation.
発明の作用効果:
この発明の方法によれば、昇華させられるべき水分は、
共晶体中の氷および医薬品の結晶中の結晶水のみであり
、従来法に比して容易に昇華させ得るため、短時間で乾
燥工程を終了することができ、効率的である。Effects of the invention: According to the method of the invention, the water to be sublimed is
Since only the ice in the eutectic and the water of crystallization in the pharmaceutical crystal can be sublimated more easily than in conventional methods, the drying process can be completed in a short time and is efficient.
その上、加温条件および減圧条件が従来法に比べて緩和
であるため、ゴム栓中の昇華性物質が昇華して医薬品に
付着するという品質面での欠陥も克服される。Furthermore, since the heating conditions and depressurization conditions are milder than in conventional methods, the quality defect of sublimable substances in the rubber stopper sublimating and adhering to medicines can also be overcome.
実施例゛
次に、この発明の方法を実施例により具体的に説明する
。なお、実施例中の温度は凍結乾燥機内の棚の温度を意
味する。EXAMPLES Next, the method of the present invention will be specifically explained using examples. In addition, the temperature in Examples means the temperature of the shelf in a freeze dryer.
実施例1
セファゾリンナトリウム(400g力価)を注射用蒸留
水(1040m/)に溶解して、セファゾリンナトリウ
ムの28%水溶液を調製する。この水出液を3.3 m
l容量のバイアル400本に分注し、凍結乾燥機内に収
容する。次いで約1時間を要して一10℃付近まで冷却
したのち、約1時間を要して20′C付近まで昇温させ
、同温度で約1時間保持する。次いで約2時間を要して
一30℃付近寸で冷却し、内容物を凍結させたのち、約
150mJo r rの減圧下に約3時間を要して13
℃付近まで昇温させる。同温、同圧下に約14時間乾燥
を続けたのち、各バイアルを密栓して、セファゾリンナ
トリウム1g力価を含有する凍結乾燥製剤を肖る。Example 1 A 28% aqueous solution of cefazolin sodium is prepared by dissolving cefazolin sodium (400 g strength) in distilled water for injection (1040 m/). 3.3 m of this water
Dispense into 400 vials of 1 volume and store in a freeze dryer. Next, it takes about 1 hour to cool down to around -10°C, and then it takes about 1 hour to raise the temperature to around 20'C, and is maintained at the same temperature for about 1 hour. Next, the contents were cooled to around -30°C over a period of about 2 hours and frozen, and then heated under a reduced pressure of about 150 mJo r r over a period of about 3 hours to 130°C.
Raise the temperature to around ℃. After continuing drying at the same temperature and pressure for about 14 hours, each vial was tightly stoppered and a lyophilized preparation containing 1 g of cefazolin sodium was added.
Claims (1)
において、該医薬品を、その室温晶析濃度より低くかつ
水との共晶体析出濃度より高い濃度範囲の水溶液とし、
該水溶液を氷点下まで冷却して医薬品を晶析させ、次い
で氷が融解しかつ析出結晶が溶解しない温度範囲まで昇
温させ、同温度を維持したのち再び冷却して医薬品の結
晶を成長させると共に系全体を完全に凍結させたのち、
再び昇温させて減圧下に乾燥することを特徴とする医薬
品の凍結乾燥方法。In a freeze-drying method for a pharmaceutical product that is crystallized from an aqueous solution by a temperature difference, the pharmaceutical product is made into an aqueous solution with a concentration range lower than the room temperature crystallization concentration and higher than the eutectic precipitation concentration with water;
The aqueous solution is cooled to below freezing point to crystallize the drug, then heated to a temperature range where the ice melts and the precipitated crystals do not dissolve, and after maintaining the same temperature, the solution is cooled again to grow drug crystals and the system. After completely freezing the entire
A method for freeze-drying pharmaceuticals, which is characterized by raising the temperature again and drying under reduced pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19026084A JPS6168412A (en) | 1984-09-10 | 1984-09-10 | Freeze-drying of medicine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19026084A JPS6168412A (en) | 1984-09-10 | 1984-09-10 | Freeze-drying of medicine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6168412A true JPS6168412A (en) | 1986-04-08 |
JPH0466202B2 JPH0466202B2 (en) | 1992-10-22 |
Family
ID=16255181
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19026084A Granted JPS6168412A (en) | 1984-09-10 | 1984-09-10 | Freeze-drying of medicine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6168412A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0394050A2 (en) * | 1989-04-18 | 1990-10-24 | Sankyo Company Limited | A method of preparing a freeze-dried formulation containing a drug |
US6197349B1 (en) | 1993-08-12 | 2001-03-06 | Knoll Aktiengesellschaft | Particles with modified physicochemical properties, their preparation and uses |
WO2002005787A1 (en) * | 2000-07-17 | 2002-01-24 | Takeda Chemical Industries, Ltd. | Production method for freeze-dried products |
-
1984
- 1984-09-10 JP JP19026084A patent/JPS6168412A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0394050A2 (en) * | 1989-04-18 | 1990-10-24 | Sankyo Company Limited | A method of preparing a freeze-dried formulation containing a drug |
US5044091A (en) * | 1989-04-18 | 1991-09-03 | Sankyo Company, Limited | Method of preparing a freeze-dried formulation containing a drug |
US6197349B1 (en) | 1993-08-12 | 2001-03-06 | Knoll Aktiengesellschaft | Particles with modified physicochemical properties, their preparation and uses |
WO2002005787A1 (en) * | 2000-07-17 | 2002-01-24 | Takeda Chemical Industries, Ltd. | Production method for freeze-dried products |
Also Published As
Publication number | Publication date |
---|---|
JPH0466202B2 (en) | 1992-10-22 |
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