HK1002017B - Lyospheres comprising gonadotropin - Google Patents
Lyospheres comprising gonadotropin Download PDFInfo
- Publication number
- HK1002017B HK1002017B HK98101026.9A HK98101026A HK1002017B HK 1002017 B HK1002017 B HK 1002017B HK 98101026 A HK98101026 A HK 98101026A HK 1002017 B HK1002017 B HK 1002017B
- Authority
- HK
- Hong Kong
- Prior art keywords
- gonadotropin
- lyospheres
- freeze
- lyosphere
- dried
- Prior art date
Links
Description
The invention relates to lyospheres comprising gonadotropin, the preparation thereof, as well as pharmaceutical preparations comprising the same.
Lyospheres are freeze-dried droplets. Spherical freeze-dried particles are known from Price et al. (US 3,655,838). These spherical beads, contain material for immunological reactions. Lyospheres comprising biological active materials are known, for instance from USP 3,932,943, and also from many other patents. Known advantages of lyospheres are the uniformity of the particles, the easy to handle products, the faster freeze-dry process, less degradation during the freeze-dry process, and the improved dissolution properties.
Surprisingly, it has now been found that lyospheres comprising gonadotropin have an improved shelf-life in comparison to conventionally freeze-dried gonadotropins. Moreover, as additional advantages it has been found that the recovery of the gonadotropin after freeze-drying of the lyospheres is better than the recovery after conventional freeze-drying, and that the analysis properties are improved.
The invention therefore, relates to a lyosphere which comprise a gonadotropin. Preferably said gonadotropin is HCG (human chorionic gonadotropin), FSH (follicle stimulating hormone), or LH (luteinizing hormone), or a combination thereof. Said gonadotropins may may obtained by isolation from natural sources or by recombinant techniques. With most preference, said gonadotropin is rec-FSH.
The lyospheres may also comprise pharmaceutically acceptable auxiliaries, such as fillers, stabilizers, and surfactants. Usual auxiliaries are for example sucrose, mannose, trehalose, dextran, Tween, polyvinyl pyrrolidone, sodium citrate and the like.
The lyospheres can be prepared by freeze-drying droplets of an aqueous gonadotropin solution, which optionally also comprises the auxiliaries. To obtain droplets of the required size, the solution can be sprayed into a cold bath (for example as disclosed in DT 2,140,747, EP 81913, or US 3,928,566), into liquid nitrogen (for example as disclosed in J5 9169,504), or onto a refrigerated drum (for example as disclosed in USP 3892876) or a refrigerated plate (for example as disclosed in US 4,501,719). Various other methods are well-known in the art.
The lyospheres of the invention can be processed into a pharmaceutical preparation. The term pharmaceutical preparation means a vial or syringe, or any other means in which the lyospheres can be introduced, and as such can be used by physicians. When the lyosphere comprises FSH or rec-FSH as the gonadotropin, pharmaceutical preparations comprise 75, 100, 150, 300, and preferably 50 IU of the FSH. Preferably each lyosphere comprises a fixed amount of gonadotropin, for instance 50 IU. Determination of the amount of IU's present in the pharmaceutical preparation can then simply achieved by counting the number of lyospheres. When the lyosphere contains hCG or rec-CG as the gonadotropin, pharmaceutical preparations comprise preferably 1, 2.5, 5, 10, or 5000 IU of the gonadotropin.
The lyospsheres of the invention may be used for medical applications where gonadotropins are required. The lyospheres containing FSH or rec-FSH are particularly useful for application in IVF (in vitro fertilisation).
The invention is further illustrated by the following examples.
Lyospheres were prepared as follows. The ingredients (gonadotropin and the expedients sucrose or trehalose, polysorbate 20, and possibly sodium citrate) were dissolved in water and diluted to the desired final concentration. The pH was adjusted to 7 using hydrochloric acid and/or sodium hydroxide. After filtration through a disposable 0.2 µm Durapore membrane filter, 100 µl droplets were formed and frozen, for instance in liquid nitrogen. The frozen droplets were collected and freeze-dried at -50 °C in a manner known per se. The freeze-dried droplets (lyospheres) were transferred into an ampoule or vial.
The recovery of freeze-drying of lyospheres and conventional freeze-drying was compared by EIA (enzyme immuno assay) using aqueous formulations containing 10 U of rec-HCG.
| formulation | content of HCG in U after freeze-drying | |
| lyospheres | conventional | |
| A | 10 | 7.4 |
| B | 9.9 | 7.2 |
| Formulations per ml: A: 50 mg of sucrose, 0.04 mg of Tween 20, 0.92 mg of sodium citrate, 10 U of rec HCG. B: 50 mg of sucrose, 0.20 mg of Tween 20, 0.92 mg of sodium citrate, 10 U of rec HCG. | ||
A 500 µl solution containing 75 IU of rec-FSH, 25 mg of sucrose, 7.35 mg of sodium citrate and 0.1 mg of polysorbate 20 was conventionally freeze-dried and compared with a 100 µl solution containing 75 IU of rec-FSH, 25 mg of sucrose, 7.35 mg of sodium citrate and 0.02 mg of polysorbate 20 which was freeze-dried as a lyosphere. Both freeze-dried products were stored for 6 months at 4, 25, 30, 40, and 50 °C, and for 12 months at 4, 25 and 30 °C. After 6 and 12 months the in vitro activity was determined according to the method of Mannaerts et al. in Roland et al. (ed.): Neuroendocrinology of reproduction, 1987, p.49-58, and expressed as percentage of the activity of the sample stored at 4 °C:
| temp in °C | lyosphere | conventional | ||
| activity in % | ||||
| 6 | 12 | 6 | 12 months | |
| 4 | 100 | 100 | 100 | 100 |
| 25 | - | 96 | 102 | 73 |
| 30 | 118 | 85 | 97 | 77 |
| 40 | 118 | - | 76 | - |
| 50 | 100 | - | 50 | - |
A 500 µl solution containing 5 IU of rec-HCG, 25 mg of sucrose, 0.46 mg of sodium citrate and 0.1 mg of polysorbate 20 was conventionally freeze-dried and compared with a 100 µl solution containing 5 IU of HCG, 25 mg of sucrose, 0.46 mg of sodium citrate and 0.02 mg of polysorbate 20 which was freeze-dried as a lyosphere. Both freeze-dried products were stored for 2 months at -18 and 50 °C. After 2 months the activity was determined by EIA and expressed as percentage of the activity of the sample stored at -18 °C:
| temp in °C | lyosphere | conventional |
| activity in % | ||
| -18 | 100 | 100 |
| 50 | 84 | 59 |
A 500 µl solution containing 5 IU of urinary HCG, 25 mg of sucrose, 0.46 mg of sodium citrate and 0.1 mg of polysorbate 20 was conventionally freeze-dried and compared with a 100 µl solution containing 5 IU of urinary HCG, 25 mg of sucrose, 0.46 mg of sodium citrate and 0.02 mg of polysorbate 20 which was freeze-dried as a lyosphere. Both freeze-dried products were stored for 2 or 6 months at -18, 8, 30, and 50 °C. After 2 or 6 months the activity was determined by EIA and expressed as percentage of the activity of the sample stored at - 18 °C:
| temp in °C | lyosphere | conventional | |
| month 2 | 6 | 2 | |
| activity in % | |||
| -18 | 100 | 100 | 100 |
| 8 | 100 | 100 | - |
| 30 | 100 | 93 | 82 |
| 50 | 82 | 78 | 25 |
Claims (7)
- A lyosphere, characterized in that the lyosphere comprises a gonadotropin.
- The lyosphere of claim 1, wherein the gonadotropin is HCG, FSH, or LH, or a combination thereof.
- The lyosphere of claim 1 or 2, wherein the gonadotropin is mixed with pharmaceutically acceptable auxiliaries.
- The lyosphere of any one of claims 1-3 for use in IVF.
- The preparation of the lyosphere of any one of claims 1-3, characterized in that the gonadotropin is freeze-dried as a droplet.
- A pharmaceutical preparation comprising the lyospheres of any one of claims 1-3.
- The pharmaceutical preparation of claim 6, wherein the lyospheres comprises 50 IU of FSH or rec-FSH.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP93201215 | 1993-04-28 | ||
| EP93201215 | 1993-04-28 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| HK1002017B true HK1002017B (en) | 1998-07-24 |
| HK1002017A1 HK1002017A1 (en) | 1998-07-24 |
Family
ID=8213798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HK98101026A HK1002017A1 (en) | 1993-04-28 | 1998-02-11 | Lyospheres comprising gonadotropin |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US5656597A (en) |
| EP (1) | EP0695171B1 (en) |
| JP (1) | JPH08509483A (en) |
| KR (1) | KR100334856B1 (en) |
| AT (1) | ATE146360T1 (en) |
| AU (1) | AU679986B2 (en) |
| CA (1) | CA2150251C (en) |
| DE (1) | DE69401204T2 (en) |
| DK (1) | DK0695171T3 (en) |
| ES (1) | ES2098140T3 (en) |
| FI (1) | FI112324B (en) |
| GR (1) | GR3022510T3 (en) |
| HK (1) | HK1002017A1 (en) |
| NO (1) | NO311168B1 (en) |
| NZ (1) | NZ265956A (en) |
| WO (1) | WO1994025005A1 (en) |
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|---|---|---|---|---|
| IL120202A (en) * | 1996-03-07 | 2001-03-19 | Akzo Nobel Nv | Container with freeze-dried vaccine components |
| GB2329124B (en) * | 1997-09-12 | 2002-05-08 | Hiran Asoka Malinga Ratwatte | Method of forming dose units of active agents |
| EP1658840A1 (en) * | 1999-04-05 | 2006-05-24 | Mannkind Corporation | Methods for fine powder formation |
| DE60026982T2 (en) | 1999-04-05 | 2006-11-16 | Mannkind Corp., Danbury | PROCESS FOR FORMING FINE POWDER |
| US9006175B2 (en) | 1999-06-29 | 2015-04-14 | Mannkind Corporation | Potentiation of glucose elimination |
| WO2003080149A2 (en) | 2002-03-20 | 2003-10-02 | Mannkind Corporation | Inhalation apparatus |
| US20040248784A1 (en) * | 2003-06-03 | 2004-12-09 | Marco Filicori | Unitary combinations of FSH and hCG |
| JP2007522085A (en) * | 2003-06-27 | 2007-08-09 | スミスクライン・ビーチャム・コーポレイション | Stabilized topotecan liposome compositions and methods |
| PL1786784T3 (en) | 2004-08-20 | 2011-04-29 | Mannkind Corp | Catalysis of diketopiperazine synthesis |
| KR101644250B1 (en) | 2004-08-23 | 2016-07-29 | 맨카인드 코포레이션 | Diketopiperazine salts, diketomorpholine salts or diketodioxane salts for drug delivery |
| CN104324362B (en) | 2005-09-14 | 2018-04-24 | 曼金德公司 | Method for preparation of drug based on improving affinity of the active agent to crystalline microparticle surfaces |
| IN2015DN00888A (en) | 2006-02-22 | 2015-07-10 | Mannkind Corp | |
| TWI436789B (en) | 2008-01-21 | 2014-05-11 | Intervet Int Bv | Method for lyophilising particles having a pharmaceutical compound contained therein and a pharmaceutical pack containing such particles |
| CN101959527B (en) | 2008-03-05 | 2016-04-20 | 赛诺菲巴斯德有限公司 | A method of stabilizing an adjuvanted vaccine composition |
| CN101269215B (en) * | 2008-05-15 | 2011-03-23 | 上海天伟生物制药有限公司 | Glucoprotein incretion composition |
| US8485180B2 (en) | 2008-06-13 | 2013-07-16 | Mannkind Corporation | Dry powder drug delivery system |
| ES2929343T3 (en) | 2008-06-13 | 2022-11-28 | Mannkind Corp | Suction Actuated Dry Powder Inhaler for Drug Delivery |
| KR101628410B1 (en) | 2008-06-20 | 2016-06-08 | 맨카인드 코포레이션 | An interactive apparatus and method for real-time profiling of inhalation efforts |
| TWI614024B (en) | 2008-08-11 | 2018-02-11 | 曼凱公司 | Ultra-fast use of insulin |
| US8314106B2 (en) | 2008-12-29 | 2012-11-20 | Mannkind Corporation | Substituted diketopiperazine analogs for use as drug delivery agents |
| DK2405963T3 (en) | 2009-03-11 | 2013-12-16 | Mannkind Corp | DEVICE, SYSTEM AND PROCEDURE FOR MEASURING RESISTANCE IN AN INHALATOR |
| CN104721825B (en) | 2009-06-12 | 2019-04-12 | 曼金德公司 | With the diketopiperazine particle for determining specific surface area |
| WO2011056889A1 (en) | 2009-11-03 | 2011-05-12 | Mannkind Corporation | An apparatus and method for simulating inhalation efforts |
| IL223742A (en) | 2010-06-21 | 2016-06-30 | Mannkind Corp | Dry powder inhaler and composition therefor |
| AU2012236150B2 (en) | 2011-04-01 | 2016-03-31 | Mannkind Corporation | Blister package for pharmaceutical cartridges |
| WO2012174472A1 (en) | 2011-06-17 | 2012-12-20 | Mannkind Corporation | High capacity diketopiperazine microparticles |
| BR112014009686A2 (en) | 2011-10-24 | 2018-08-07 | Mannkind Corp | Inhalable analgesic composition, dry powder and method for treating pain |
| CN104619369B (en) | 2012-07-12 | 2018-01-30 | 曼金德公司 | Dry powder drug delivery systems and methods |
| US10159644B2 (en) | 2012-10-26 | 2018-12-25 | Mannkind Corporation | Inhalable vaccine compositions and methods |
| AU2014228415B2 (en) | 2013-03-15 | 2018-08-09 | Mannkind Corporation | Microcrystalline diketopiperazine compositions and methods |
| US11446127B2 (en) | 2013-08-05 | 2022-09-20 | Mannkind Corporation | Insufflation apparatus and methods |
| US10307464B2 (en) | 2014-03-28 | 2019-06-04 | Mannkind Corporation | Use of ultrarapid acting insulin |
| US10561806B2 (en) | 2014-10-02 | 2020-02-18 | Mannkind Corporation | Mouthpiece cover for an inhaler |
| WO2017066134A1 (en) * | 2015-10-16 | 2017-04-20 | Merck Sharp & Dohme Corp. | Processes for preparing formulations for gastrointestinal-targeted therapies |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3932943A (en) * | 1970-08-14 | 1976-01-20 | E. I. Du Pont De Nemours And Company | Method of preparation of lyophilized biological products |
| ATE14047T1 (en) * | 1981-12-11 | 1985-07-15 | Wyeth John & Brother Ltd | METHOD AND DEVICE FOR FREEZING A LIQUID. |
| JPS60258125A (en) * | 1984-06-06 | 1985-12-20 | Hayashibara Biochem Lab Inc | Water-soluble dried material containing proteinic physiologically active substance |
| ES2062530T3 (en) * | 1989-05-01 | 1994-12-16 | Alkermes Inc | PROCEDURE FOR PRODUCING SMALL PARTICLES OF BIOLOGICALLY ACTIVE MOLECULES. |
| IE64738B1 (en) * | 1990-03-20 | 1995-09-06 | Akzo Nv | Stabilized gonadotropin containing preparations |
-
1994
- 1994-04-25 WO PCT/EP1994/001303 patent/WO1994025005A1/en not_active Ceased
- 1994-04-25 US US08/454,333 patent/US5656597A/en not_active Expired - Lifetime
- 1994-04-25 ES ES94915121T patent/ES2098140T3/en not_active Expired - Lifetime
- 1994-04-25 DE DE69401204T patent/DE69401204T2/en not_active Expired - Lifetime
- 1994-04-25 DK DK94915121.1T patent/DK0695171T3/en active
- 1994-04-25 JP JP6523868A patent/JPH08509483A/en active Pending
- 1994-04-25 AT AT94915121T patent/ATE146360T1/en active
- 1994-04-25 CA CA002150251A patent/CA2150251C/en not_active Expired - Fee Related
- 1994-04-25 EP EP94915121A patent/EP0695171B1/en not_active Expired - Lifetime
- 1994-04-25 AU AU66488/94A patent/AU679986B2/en not_active Ceased
- 1994-04-25 NZ NZ265956A patent/NZ265956A/en not_active IP Right Cessation
- 1994-04-25 KR KR1019950702180A patent/KR100334856B1/en not_active Expired - Fee Related
-
1995
- 1995-07-14 FI FI953442A patent/FI112324B/en not_active IP Right Cessation
- 1995-10-27 NO NO19954320A patent/NO311168B1/en not_active IP Right Cessation
-
1997
- 1997-02-11 GR GR970400207T patent/GR3022510T3/en unknown
-
1998
- 1998-02-11 HK HK98101026A patent/HK1002017A1/en not_active IP Right Cessation
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