WO1997041836A1 - Compositions pharmaceutiques pour la liberation prolongee de principes actifs insolubles - Google Patents
Compositions pharmaceutiques pour la liberation prolongee de principes actifs insolubles Download PDFInfo
- Publication number
- WO1997041836A1 WO1997041836A1 PCT/EP1997/002187 EP9702187W WO9741836A1 WO 1997041836 A1 WO1997041836 A1 WO 1997041836A1 EP 9702187 W EP9702187 W EP 9702187W WO 9741836 A1 WO9741836 A1 WO 9741836A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pharmaceutical composition
- composition according
- active principle
- lactic acid
- approximately
- Prior art date
Links
- 239000008194 pharmaceutical composition Substances 0.000 title claims abstract description 29
- 238000013268 sustained release Methods 0.000 title abstract description 3
- 239000012730 sustained-release form Substances 0.000 title abstract description 3
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical compound C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 claims abstract description 26
- 229920001519 homopolymer Polymers 0.000 claims abstract description 10
- 239000004480 active ingredient Substances 0.000 claims description 20
- 229920000642 polymer Polymers 0.000 claims description 18
- 239000007943 implant Substances 0.000 claims description 17
- 238000013270 controlled release Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000004005 microsphere Substances 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 5
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- 229940088597 hormone Drugs 0.000 description 2
- 239000005556 hormone Substances 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 230000001225 therapeutic effect Effects 0.000 description 2
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Polymers OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 description 1
- 108010051696 Growth Hormone Proteins 0.000 description 1
- 229920000954 Polyglycolide Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 102100038803 Somatotropin Human genes 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000011319 anticancer therapy Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005354 coacervation Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 229940124558 contraceptive agent Drugs 0.000 description 1
- 239000003433 contraceptive agent Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 206010013663 drug dependence Diseases 0.000 description 1
- 239000013583 drug formulation Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000122 growth hormone Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002657 hormone replacement therapy Methods 0.000 description 1
- 238000001794 hormone therapy Methods 0.000 description 1
- 239000012729 immediate-release (IR) formulation Substances 0.000 description 1
- 238000002513 implantation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 238000011866 long-term treatment Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229940127554 medical product Drugs 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000003094 microcapsule Substances 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 238000011328 necessary treatment Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 206010033675 panniculitis Diseases 0.000 description 1
- 238000007911 parenteral administration Methods 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 229940127557 pharmaceutical product Drugs 0.000 description 1
- 239000004626 polylactic acid Substances 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000003488 releasing hormone Substances 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229940075620 somatostatin analogue Drugs 0.000 description 1
- 210000004304 subcutaneous tissue Anatomy 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 208000011117 substance-related disease Diseases 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 239000003826 tablet Substances 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
- A61K9/1605—Excipients; Inactive ingredients
- A61K9/1629—Organic macromolecular compounds
- A61K9/1641—Organic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, poloxamers
- A61K9/1647—Polyesters, e.g. poly(lactide-co-glycolide)
Definitions
- the present invention relates to pharmaceutical compositions based on biodegradable polymers for the controlled release of active ingredients insoluble in water.
- Controlled release pharmaceutical compositions containing biodegradable polymers are extremely useful for dispensing medical and pharmaceutical products and find a wide variety of applications in which they offer many advantages over standard drug formulations.
- a simple administration of a controlled release formulation ensures a slow release of the active ingredient over an extended period.
- One of the first applications of this type of controlled release formulation was in the field of drug addiction.
- the treatment of patients who use drugs is made delicate and difficult since, with standard formulations, it is not always easy to obtain the patient's cooperation. Thus, with standard formulations, there is always the risk that the patient will refuse to take the necessary treatment at the right time.
- simple administration ensures effective treatment for a certain duration, greater than what can be obtained from a single dose.
- Controlled release formulations are also particularly useful in applications such as anti-cancer therapy where long-term treatments are often required.
- Controlled release pharmaceutical compositions can be provided in a variety of dosage formulations.
- implant formulations as well as formulations allowing oral or parenteral administration.
- Oral formulations are normally in the form of tablets or capsules that can be easily swallowed or ingested.
- parenteral formulations can be in particular in the form of microgranules, microspheres or microcapsules.
- implants may sometimes be preferred over parenteral formulations. This preference exists in particular in the case where a certain flexibility is desired with respect to the therapeutic protocol. Compared with parenteral formulations, the implants have the advantage of being able to be removed surgically, if need be, for any reason, to stop the treatment before the complete release of the active principle has taken place.
- compositions according to the present invention can be in particular in the form of implants, microgranules and / or microspheres.
- the Polylactide and polyglycolide copolymers and homopolymers are particularly preferred in controlled release formulations because they are easily degradable, decompose in harmless products such as carbon dioxide and water, and therefore leave no residue over time. release of the active ingredient.
- US Patent 3,773,919 describes polymer formulations of drugs, based on polylactides. It is mentioned therein that the invention is of particular interest for drugs which require prolonged administration or sustained slow release, for example for certain fertility regulation drugs or the hormones used in hormone replacement therapy. It should be noted that the implants, as well as the microgranules, can be prepared according to a "dry process", which avoids the use of solvents for the prior dissolu ⁇ tion of the active principles and / or polymers. This avoids the disadvantage of methods such as micro-encapsulation, where there is always the problem of traces of residual solvent which can compromise the use of the compositions for therapeutic purposes. The company Demand has developed this "dry process" for the preparation of microgranules and implants. This process is described in Swiss patent 679 207 which the Applicant Company owns. Microgranules resulting from this process allow a regular release of the active substance over a period of approximately 1 month.
- compositions allowing a prolonged release of active ingredients insoluble in water over a longer period, such as two, even three or four or four months.
- the Applicant Company has been able to develop a new type of pharmaceutical composition allowing a controlled release of active principles which are insoluble in water, on a period longer than one month, and in particular two to three months, or even beyond.
- compositions according to the present invention are characterized in that they comprise a homopolymer of low molecular weight lactic acid.
- the polymer can be a homopolymer of D, L-lactic acid or L-lactic acid.
- the polymer used in the present case is a polymer having a low molecular weight. Indeed, one could think that the lower the molecular weight of the polymer, the faster its degradation rate would be important. The Applicant Company discovered that this was not the case for the homopolymers of D, L-lactic acid and L-lactic acid.
- the molecular weight of the homopolymer of L-lactic acid is advantageously chosen between approximately 1,000 and 30,000, preferably between approximately 3,000 and 15,000, and more preferably still being approximately 4,000.
- the molecular weight of one homopolymer of D, L-lactic acid is advantageously chosen between approximately 1,000 and 30,000, preferably between approximately 2,000 and 20,000, and more preferably still between approximately 2,000 and 6,000.
- the percentage of polymer in the pharmaceutical composition according to the invention is between 98 and 70%, preferably between 95 and 75%, and even more preferably between 85 and 75%.
- active ingredients insoluble in water means active ingredients which may themselves be soluble in aqueous solution, but which are made insoluble by conversion to an insoluble salt of the active ingredient.
- insoluble in water means a solubility in water which does not exceed 100 ⁇ g / ml (definition of USP,
- the active principle made insoluble in water according to the present invention can be chosen from proteins, polypeptides, hormones. More particularly, the active principle can be chosen from the pharmaceutically acceptable salts of oxytocin, vasopressin, ACTH, calcitonin, LH-RH or its analogs, epidermal growth factor, prolactin, inhibin, interferon, somatostatin or its analogs such as vapeotide pamoate, insulin, glucagon, atrial natriuretic factor, endorphin, a renin peptide inhibitor, release releasing factor growth hormone, T-peptide and their synthetic analogs.
- the active principle can be chosen from the pharmaceutically acceptable salts of oxytocin, vasopressin, ACTH, calcitonin, LH-RH or its analogs, epidermal growth factor, prolactin, inhibin, interferon, somatostatin or its analogs such as vapeotide pamoate, insulin, glu
- the pharmaceutically acceptable insoluble salts of the active principle can be advantageously chosen from pamoate, tannate, stearate or palmitate.
- the present invention therefore relates to a pharmaceutical composition for the controlled release of at least one active ingredient insoluble in water, comprising a homopoly ⁇ mother of D, L-lactic acid or L-lactic acid having a low molecular weight and being intimately associated with said active ingredient.
- compositions according to the invention can be in the form of implants, microgranules or microspheres.
- the implants and the microgranules according to the invention can be prepared according to known methods, in particular that described in Swiss Patent 679,207.
- the active ingredient and the polymer are dry mixed in a suitable device, such as a ball mill, at room temperature (about 25 ° C) or even at a lower temperature, for example 5 at 10 ° C.
- the mixture is duly homogenized, it is subjected to progressive compression and, simultaneously, to progressive heating before being extruded.
- the mixture thus precompressed and preheated is then subjected to an extrusion, at a temperature most generally between approximately 80 and 100 ° C.
- the extrusion can take place under a pressure varying between 50 and 500 kg / cm 2 .
- the wires thus extruded are cooled and then cut into sticks or other shapes with regard to the implants.
- Example 1 An alternative method for preparing the implants according to the invention is described in Example 1.
- the extrusion product is cooled and then sprayed at low temperature, between 0 and -30 ° C.
- the microgranules can then be sorted according to their dimensions.
- the size of the microgranules is advantageously around 15 ⁇ m.
- the microspheres according to the present invention can be prepared according to the method described in the US patent
- the active principle is dispersed in a solution of polymer in an organic solvent.
- An agent incompatible with the solvent polymer system is added, where the temperature and pressure are varied. This causes a phenomenon which is called “coacervation”, that is to say the precipitation of the polymer with the active ingredient dispersed, which gives microspheres which consist of a polymer matrix in which the molecules of the active ingredient are dispersed. .
- the microspheres thus obtained are separated by filtration and then dried.
- the size of the microspheres according to the invention is advantageously around 40 ⁇ m.
- the percentage of the active principle relative to the total weight is between approximately 1 and 45%, preferably between approximately 5 and 10% when it is a question of microgranules or microspheres, and between about 2 and 30%, preferably between about 5 and 25%, and more preferably still between about 15 and 25% when it comes to implants.
- an effective amount of the active principle is released over a period of at least 1 month, preferably at least 2 months, and even more preferably more than 3 months.
- the release profiles according to the invention can show a "burst effect", that is to say a significant immediate release, followed by a slow and steady release over a long period.
- Figures 1, 2 and 3 show release profiles obtained from the implants according to the invention with different percentages of active ingredient.
- L104 which is an L-polylactic acid having a molecular mass of approximately 4,000, and which is marketed by the company BOEHRINGER INGELHEIM, is mixed, using a three-dimensional mixer.
- Vaprotide pamoate (a Somatostatin analogue sold by NOVA BIOCHEM in Switzerland).
- the mixture is homogenized in an agate mortar and then it is deionized.
- the mixture obtained is extruded at a temperature of about 80 ° C on a piston extruder.
- the filament thus obtained is then cut into cylindrical implants 15 mm in length using a scalpel.
- Example 2 The procedure is as in Example 1 until filaments are obtained which are cooled to room temperature. Then, they are cut into small portions and finally ground at -30 ° C. After sieving, the microgranules with an average size of 15 ⁇ or less are collected.
- EXAMPLE 3 Implantation in Animals and Liberation Curve Implants are prepared as in Example 1 using percentages of active principle of 15, 20 and 25%.
- Each implant is sterilized by gamma radiation, at a dose of 2.5 M rads.
- Each type of implant is then injected into the subcutaneous tissue of the skin of the neck of a male albino rat of the Spragne Dawleu strain, the rats being 8 to 9 weeks old and having an average weight between 330 and 340 g.
- the injection is made using a trocar, the prototype of which is supplied by S.F.M. in Germany.
- Blood samples are then taken to determine, by RIA assay, the release of the active ingredient.
- Figures 1, 2 and 3 show the release curves for the different percentages of active ingredient (15, 20 and 25% respectively). It should be noted that a prolonged release is noted beyond 4 months (120 days).
Landscapes
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Epidemiology (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Medicinal Preparation (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9539493A JP2000509403A (ja) | 1996-05-06 | 1997-04-28 | 不溶性活性成分の持続放出のための製薬組成物 |
EP97921812A EP0896527A1 (fr) | 1996-05-06 | 1997-04-28 | Compositions pharmaceutiques pour la liberation prolongee de principes actifs insolubles |
IL12689297A IL126892A (en) | 1996-05-06 | 1997-04-28 | Pharmaceutical compositions for the sustained release of at least one water-insoluble active principle |
AU27735/97A AU710539B2 (en) | 1996-05-06 | 1997-04-28 | Pharmaceutical compositions for the sustained release of insoluble active principles |
US09/180,451 US6245346B1 (en) | 1996-05-06 | 1997-04-28 | Pharmaceutical compositions for the sustained release of insoluble active principles |
NO985145A NO985145D0 (no) | 1996-05-06 | 1998-11-04 | Farmas°ytiske preparater for forsinket frigj°ring av uoppl°selige, aktive bestanddeler |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR96/05630 | 1996-05-06 | ||
FR9605630A FR2748205A1 (fr) | 1996-05-06 | 1996-05-06 | Compositions pharmaceutiques pour la liberation controlee de principes actifs insolubles |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997041836A1 true WO1997041836A1 (fr) | 1997-11-13 |
Family
ID=9491862
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1997/002187 WO1997041836A1 (fr) | 1996-05-06 | 1997-04-28 | Compositions pharmaceutiques pour la liberation prolongee de principes actifs insolubles |
Country Status (9)
Country | Link |
---|---|
US (1) | US6245346B1 (fr) |
EP (1) | EP0896527A1 (fr) |
JP (1) | JP2000509403A (fr) |
AU (1) | AU710539B2 (fr) |
CA (1) | CA2253377A1 (fr) |
FR (1) | FR2748205A1 (fr) |
IL (1) | IL126892A (fr) |
NO (1) | NO985145D0 (fr) |
WO (1) | WO1997041836A1 (fr) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001087265A3 (fr) * | 2000-05-18 | 2002-04-18 | Zentaris Ag | Forme d'administration pharmaceutique pour des peptides, son procede de production et son utilisation |
WO2006063848A1 (fr) | 2004-12-17 | 2006-06-22 | Devgen N.V. | Compositions nematicides |
WO2011117308A1 (fr) | 2010-03-24 | 2011-09-29 | Basf Se | Procédé de production de dispersions aqueuses de polyesters thermoplastiques |
WO2013041649A1 (fr) | 2011-09-23 | 2013-03-28 | Basf Se | Utilisation d'une dispersion aqueuse de polyesters biodégradables |
US8604101B2 (en) | 2010-03-24 | 2013-12-10 | Basf Se | Process for producing aqueous dispersions of thermoplastic polyesters |
US8889174B1 (en) | 2001-06-22 | 2014-11-18 | Durect Corporation | Zero-order prolonged release coaxial implants |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002058671A1 (fr) * | 2001-01-26 | 2002-08-01 | Debio Recherche Pharmaceutique S.A. | Microparticules pharmaceutiques exemptes d"eclatement |
GB0122113D0 (en) * | 2001-09-11 | 2001-10-31 | Astrazeneca Ab | Composition |
US6987111B2 (en) * | 2003-08-06 | 2006-01-17 | Alkermes Controlled Therapeutics, Ii | Aripiprazole, olanzapine and haloperidol pamoate salts |
US8541028B2 (en) | 2004-08-04 | 2013-09-24 | Evonik Corporation | Methods for manufacturing delivery devices and devices thereof |
US20070106271A1 (en) * | 2005-11-09 | 2007-05-10 | Searete Llc, A Limited Liability Corporation | Remote control of substance delivery system |
CA2709712C (fr) | 2007-12-20 | 2016-05-10 | Surmodics Pharmaceuticals, Inc. | Procede pour preparer des microparticules ayant un faible volume de solvant residuel |
ES2581837T3 (es) * | 2010-07-26 | 2016-09-07 | Université De Genève | Composiciones que comprenden polímeros preparados a partir de ácidos 2-hidroxi alquil |
WO2015158823A1 (fr) | 2014-04-16 | 2015-10-22 | Veyx-Pharma Gmbh | Composition pharmaceutique vétérinaire et utilisation de ladite composition pharmaceutique vétérinaire |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4622244A (en) * | 1979-09-04 | 1986-11-11 | The Washington University | Process for preparation of microcapsules |
FR2620621A1 (fr) * | 1987-09-21 | 1989-03-24 | Bpd Biopharm Dev Ltd | Composition pharmaceutique pour la liberation soutenue et controlee de polypeptides insolubles dans l'eau |
GB2246514A (en) * | 1990-08-01 | 1992-02-05 | Scras | Sustained release particles preparation |
EP0474098A1 (fr) * | 1990-08-30 | 1992-03-11 | Senju Pharmaceutical Co., Ltd. | Composition pour la libération contrôlée de médicaments |
EP0669128A1 (fr) * | 1992-11-17 | 1995-08-30 | Yoshitomi Pharmaceutical Industries, Ltd. | Microsphere a liberation prolongee contenant un antipshychotique et procede de production |
WO1996010397A1 (fr) * | 1994-09-30 | 1996-04-11 | Takeda Chemical Industries, Ltd. | Preparation buvable a liberation lente |
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US3773919A (en) | 1969-10-23 | 1973-11-20 | Du Pont | Polylactide-drug mixtures |
CH679207A5 (fr) | 1989-07-28 | 1992-01-15 | Debiopharm Sa | |
US5869079A (en) * | 1995-06-02 | 1999-02-09 | Oculex Pharmaceuticals, Inc. | Formulation for controlled release of drugs by combining hydrophilic and hydrophobic agents |
-
1996
- 1996-05-06 FR FR9605630A patent/FR2748205A1/fr active Pending
-
1997
- 1997-04-28 JP JP9539493A patent/JP2000509403A/ja active Pending
- 1997-04-28 IL IL12689297A patent/IL126892A/en not_active IP Right Cessation
- 1997-04-28 US US09/180,451 patent/US6245346B1/en not_active Expired - Fee Related
- 1997-04-28 AU AU27735/97A patent/AU710539B2/en not_active Ceased
- 1997-04-28 WO PCT/EP1997/002187 patent/WO1997041836A1/fr not_active Application Discontinuation
- 1997-04-28 CA CA002253377A patent/CA2253377A1/fr not_active Abandoned
- 1997-04-28 EP EP97921812A patent/EP0896527A1/fr not_active Withdrawn
-
1998
- 1998-11-04 NO NO985145A patent/NO985145D0/no not_active Application Discontinuation
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US4622244A (en) * | 1979-09-04 | 1986-11-11 | The Washington University | Process for preparation of microcapsules |
FR2620621A1 (fr) * | 1987-09-21 | 1989-03-24 | Bpd Biopharm Dev Ltd | Composition pharmaceutique pour la liberation soutenue et controlee de polypeptides insolubles dans l'eau |
GB2246514A (en) * | 1990-08-01 | 1992-02-05 | Scras | Sustained release particles preparation |
EP0474098A1 (fr) * | 1990-08-30 | 1992-03-11 | Senju Pharmaceutical Co., Ltd. | Composition pour la libération contrôlée de médicaments |
EP0669128A1 (fr) * | 1992-11-17 | 1995-08-30 | Yoshitomi Pharmaceutical Industries, Ltd. | Microsphere a liberation prolongee contenant un antipshychotique et procede de production |
WO1996010397A1 (fr) * | 1994-09-30 | 1996-04-11 | Takeda Chemical Industries, Ltd. | Preparation buvable a liberation lente |
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Title |
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ASO Y ET AL: "EFFECT OF TEMPERATURE ON MECHANISMS OF DRUG RELEASE AND MATRIX DEGRADATION OF POLY(D,L-LACTIDE) MICROSPHERES", JOURNAL OF CONTROLLED RELEASE, vol. 31, no. 1, 1 August 1994 (1994-08-01), pages 33 - 39, XP000456578 * |
YASUHIKO TABATA: "A FORMULATION METHOD USING D,L-LACTIC ACID OLIGOMER FOR PROTEIN RELEASE WITH REDUCED INITIAL BURST", JOURNAL OF CONTROLLED RELEASE, vol. 23, no. 1, 1 January 1993 (1993-01-01), pages 55 - 63, XP000332068 * |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001087265A3 (fr) * | 2000-05-18 | 2002-04-18 | Zentaris Ag | Forme d'administration pharmaceutique pour des peptides, son procede de production et son utilisation |
US7718599B2 (en) | 2000-05-18 | 2010-05-18 | Aeterna Zentaris Gmbh | Pharmaceutical administration form for peptides, process for its preparation, and use |
US8889174B1 (en) | 2001-06-22 | 2014-11-18 | Durect Corporation | Zero-order prolonged release coaxial implants |
WO2006063848A1 (fr) | 2004-12-17 | 2006-06-22 | Devgen N.V. | Compositions nematicides |
EP1941799A2 (fr) | 2004-12-17 | 2008-07-09 | Devgen NV | Compositions nematicides |
EP1941798A2 (fr) | 2004-12-17 | 2008-07-09 | Devgen NV | Compositions nematicides |
EP2460408A1 (fr) | 2004-12-17 | 2012-06-06 | deVGen N.V. | Compositions nematicides |
WO2011117308A1 (fr) | 2010-03-24 | 2011-09-29 | Basf Se | Procédé de production de dispersions aqueuses de polyesters thermoplastiques |
US8604101B2 (en) | 2010-03-24 | 2013-12-10 | Basf Se | Process for producing aqueous dispersions of thermoplastic polyesters |
WO2013041649A1 (fr) | 2011-09-23 | 2013-03-28 | Basf Se | Utilisation d'une dispersion aqueuse de polyesters biodégradables |
Also Published As
Publication number | Publication date |
---|---|
NO985145L (no) | 1998-11-04 |
AU2773597A (en) | 1997-11-26 |
EP0896527A1 (fr) | 1999-02-17 |
IL126892A (en) | 2004-07-25 |
FR2748205A1 (fr) | 1997-11-07 |
NO985145D0 (no) | 1998-11-04 |
CA2253377A1 (fr) | 1997-11-13 |
US6245346B1 (en) | 2001-06-12 |
IL126892A0 (en) | 1999-09-22 |
JP2000509403A (ja) | 2000-07-25 |
AU710539B2 (en) | 1999-09-23 |
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