JP2003252751A5 - - Google Patents

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JP2003252751A5
JP2003252751A5 JP2002374330A JP2002374330A JP2003252751A5 JP 2003252751 A5 JP2003252751 A5 JP 2003252751A5 JP 2002374330 A JP2002374330 A JP 2002374330A JP 2002374330 A JP2002374330 A JP 2002374330A JP 2003252751 A5 JP2003252751 A5 JP 2003252751A5
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production method
salt
osmotic pressure
polymer
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JP2002374330A
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JP2003252751A (en
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Claims (28)

水中乾燥法によるマイクロスフェアの製造時に、外水相に浸透圧調節剤を添加することを特徴とする、分散性が改善されたマイクロスフェアの製造法。A method for producing a microsphere with improved dispersibility, comprising adding an osmotic pressure regulator to an outer aqueous phase when producing the microsphere by an underwater drying method. 改善された分散性が、約400から約700mgのマイクロスフェアを1.5mLの注射用分散媒に2分未満で分散できる程度である、請求項1記載の製造法。The process according to claim 1, wherein the improved dispersibility is such that about 400 to about 700 mg of microspheres can be dispersed in 1.5 mL of injectable dispersion medium in less than 2 minutes. 水中乾燥法にW/O/W型乳化物を用いる請求項1記載の製造法。The production method according to claim 1, wherein a W / O / W emulsion is used for the underwater drying method. 内水相にさらに薬物保持物質を含ませる請求項3記載の製造法。The production method according to claim 3, further comprising a drug-retaining substance in the inner aqueous phase. 水中乾燥法にO/W型乳化物を用いる請求項1記載の製造法。The production method according to claim 1, wherein an O / W emulsion is used for the underwater drying method. 水中乾燥法にS/O/W型乳化物を用いる請求項1記載の製造法。The process according to claim 1, wherein an S / O / W emulsion is used for the underwater drying method. 生理活性物質またはその塩を含む液を内水相とし、重量平均分子量15000〜50000の乳酸重合体またはその塩を含む溶液を油相とするW/O型乳化物を、浸透圧調節剤を含有した外水相に分散させて水中乾燥法に付することを特徴とするマイクロスフェアの製造法。Contains an osmotic pressure regulator, a W / O emulsion containing a liquid containing a physiologically active substance or a salt thereof as an inner aqueous phase and a lactic acid polymer having a weight average molecular weight of 15,000 to 50,000 or a salt thereof as an oil phase. A method for producing microspheres, characterized by being dispersed in an outer aqueous phase and subjected to an underwater drying method. 乳酸重合体またはその塩における重量平均分子量5000以下の重合体含有量が約10重量%以下である、請求項7記載の製造法。The production method according to claim 7, wherein the content of the polymer having a weight average molecular weight of 5000 or less in the lactic acid polymer or a salt thereof is about 10% by weight or less. 乳酸重合体またはその塩における重量平均分子量5000以下の重合体含有量が約5重量%以下である、請求項7記載の製造法。The production method according to claim 7, wherein the content of the polymer having a weight average molecular weight of 5000 or less in the lactic acid polymer or a salt thereof is about 5% by weight or less. 乳酸重合体またはその塩における重量平均分子量3000以下の重合体含有量が約1.5重量%以下である、請求項7記載の製造法。The production method according to claim 7, wherein the content of the polymer having a weight average molecular weight of 3000 or less in the lactic acid polymer or a salt thereof is about 1.5% by weight or less. 乳酸重合体またはその塩における重量平均分子量1000以下の重合体含有量が約0.1重量%以下である、請求項7記載の製造法。The production method according to claim 7, wherein the content of the polymer having a weight average molecular weight of 1000 or less in the lactic acid polymer or a salt thereof is about 0.1% by weight or less. 乳酸重合体またはその塩の重量平均分子量が15000〜40000のものである、請求項7記載の製造法。The process according to claim 7, wherein the lactic acid polymer or a salt thereof has a weight average molecular weight of 15,000 to 40,000. 乳酸重合体またはその塩の重量平均分子量が17000〜26000のものである、請求項7記載の製造法。The production method according to claim 7, wherein the lactic acid polymer or a salt thereof has a weight average molecular weight of 17000 to 26000. 浸透圧調節剤が、アルコール類、糖類、アミノ酸類、ペプチド類、タンパク質類、水溶性アミノ酸の塩、もしくはその誘導体またはこれらの混合物である、請求項1または7記載の製造法。The production method according to claim 1 or 7, wherein the osmotic pressure regulator is an alcohol, a saccharide, an amino acid, a peptide, a protein, a salt of a water-soluble amino acid, a derivative thereof, or a mixture thereof. 浸透圧調節剤がマンニトールである、請求項1または7記載の製造法。The production method according to claim 1 or 7, wherein the osmotic pressure regulator is mannitol. 浸透圧調節剤の外水相中の濃度が、外水相の浸透圧が生理食塩水の浸透圧の約1/50〜約5倍となる濃度である請求項1または7記載の製造法。The method according to claim 1 or 7, wherein the concentration of the osmotic pressure regulator in the outer aqueous phase is such that the osmotic pressure of the outer aqueous phase is about 1/50 to about 5 times the osmotic pressure of physiological saline. 生理活性物質が水溶性の生理活性物質である請求項7記載の製造法。The production method according to claim 7, wherein the physiologically active substance is a water-soluble physiologically active substance. 生理活性物質が生理活性ペプチドである請求項7記載の製造法。The method according to claim 7, wherein the physiologically active substance is a physiologically active peptide. 生理活性物質がLH-RH誘導体である請求項7記載の製造法。The method according to claim 7, wherein the physiologically active substance is an LH-RH derivative. LH-RH誘導体が式
5-oxo-Pro-His-Trp-Ser-Tyr-Y-Leu-Arg-Pro-Z
[式中、YはDLeu、DAla、DTrp、DSer(tBu)、D2NalまたはDHis(ImBzl)を示し、ZはNH-C2H5またはGly-NH2を示す。]で表されるペプチドまたはその塩である請求項7記載の製造法。
LH-RH derivative is formula
5-oxo-Pro-His-Trp-Ser-Tyr-Y-Leu-Arg-Pro-Z
[Wherein Y represents DLeu, DAla, DTrp, DSer (tBu), D2Nal or DHis (ImBzl), and Z represents NH—C 2 H 5 or Gly-NH 2 . The production method according to claim 7, which is a peptide represented by the formula:
請求項1または7記載の製造法によって得られるマイクロスフェア。A microsphere obtained by the production method according to claim 1 or 7. 請求項21記載のマイクロスフェアを含有してなる徐放性組成物。A sustained release composition comprising the microsphere according to claim 21. 前立腺癌、前立腺肥大症、子宮内膜症、子宮筋腫、子宮線維腫、思春期早発症、月経困難症もしくは乳癌の予防、治療用または避妊用である請求項22の徐放性組成物。The sustained-release composition according to claim 22, which is used for the prevention, treatment or contraception of prostate cancer, benign prostatic hyperplasia, endometriosis, uterine fibroids, uterine fibroma, precocious puberty, dysmenorrhea or breast cancer. 注射用である請求項22記載の徐放性組成物。The sustained release composition according to claim 22, which is for injection. さらにマンニトールを含有する請求項22記載の徐放性組成物。The sustained-release composition according to claim 22, further comprising mannitol. 組成物全体に対してマイクロスフェアを約70重量%以上含有する請求項22記載の徐放性組成物。The sustained-release composition according to claim 22, comprising about 70% by weight or more of microspheres based on the whole composition. 分散性が改善されたマイクロスフェアを製造するために、生理活性物質またはその塩と高分子重合物を含む乳化物を水中乾燥する際に、外水相に浸透圧調節剤を存在させることを特徴とする方法。In order to produce microspheres with improved dispersibility, an osmotic pressure regulator is present in the outer aqueous phase when an emulsion containing a physiologically active substance or a salt thereof and a polymer is dried in water. And how to. 分散性が改善されたマイクロスフェアの製造するための、生理活性物質またはその塩と高分子重合物を含む乳化物を水中乾燥する際の外水相における、浸透圧調節剤の使用。Use of an osmotic pressure regulator in an outer aqueous phase when an emulsion containing a physiologically active substance or a salt thereof and a polymer is dried in water to produce microspheres with improved dispersibility.
JP2002374330A 2001-12-26 2002-12-25 New microsphere and method for producing the same Withdrawn JP2003252751A (en)

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JP2001394663 2001-12-26
JP2001-394663 2001-12-26
JP2002374330A JP2003252751A (en) 2001-12-26 2002-12-25 New microsphere and method for producing the same

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JP2003252751A JP2003252751A (en) 2003-09-10
JP2003252751A5 true JP2003252751A5 (en) 2005-09-08

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1532985B1 (en) * 2002-06-25 2016-10-12 Takeda Pharmaceutical Company Limited Process for producing a sustained-release composition
JP4659510B2 (en) * 2005-04-28 2011-03-30 サンスター株式会社 W / O / W type emulsion composition
JP5092369B2 (en) * 2006-05-09 2012-12-05 東レ株式会社 Method for producing spherical particles
JP5419704B2 (en) * 2007-11-07 2014-02-19 株式会社カネカ Method for producing microcapsules using solid fat
JP5733551B2 (en) * 2010-03-02 2015-06-10 学校法人東京理科大学 Nanocomposite particles and method for producing the same

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DE69316101T2 (en) * 1992-08-07 1998-10-22 Takeda Chemical Industries Ltd Manufacture of microcapsules containing water-soluble drugs
JP3790567B2 (en) * 1994-09-30 2006-06-28 武田薬品工業株式会社 Sustained release agent
JPH08259460A (en) * 1995-01-23 1996-10-08 Takeda Chem Ind Ltd Production of sustained release pharmaceutical preparation
JPH09208488A (en) * 1995-11-30 1997-08-12 Takeda Chem Ind Ltd Treating agent for cerebrovascular dementia
JPH09221420A (en) * 1995-12-15 1997-08-26 Takeda Chem Ind Ltd Sustained release agent of hydroxamic acid compound
JPH09241178A (en) * 1996-03-07 1997-09-16 Takeda Chem Ind Ltd Production of sustained release pharmaceutical preparation of adenocorticotropic hormone derivative
JPH10273447A (en) * 1997-01-29 1998-10-13 Takeda Chem Ind Ltd Delayed-release microsphere and its production and use
JPH11269094A (en) * 1998-01-16 1999-10-05 Takeda Chem Ind Ltd Sustained release composition, its production and use
AU2002358831B2 (en) * 2001-10-10 2007-09-06 Pierre Fabre Medicament Prolonged release biodegradable microspheres and method for preparing same

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