EP0343596A2 - Récipient pour lyophilisation sous conditions stériles - Google Patents
Récipient pour lyophilisation sous conditions stériles Download PDFInfo
- Publication number
- EP0343596A2 EP0343596A2 EP89109246A EP89109246A EP0343596A2 EP 0343596 A2 EP0343596 A2 EP 0343596A2 EP 89109246 A EP89109246 A EP 89109246A EP 89109246 A EP89109246 A EP 89109246A EP 0343596 A2 EP0343596 A2 EP 0343596A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- membrane
- container
- dried
- drying
- freeze
- 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
- 238000004108 freeze drying Methods 0.000 title claims abstract description 13
- 239000012528 membrane Substances 0.000 claims abstract description 33
- 239000000463 material Substances 0.000 claims abstract description 24
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 24
- 239000011148 porous material Substances 0.000 claims description 5
- 239000001913 cellulose Substances 0.000 claims description 4
- 229920002678 cellulose Polymers 0.000 claims description 4
- -1 polytetrafluoroethylene Polymers 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 2
- 229920002301 cellulose acetate Polymers 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 229920001155 polypropylene Polymers 0.000 claims description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 2
- 239000003708 ampul Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 238000001035 drying Methods 0.000 description 18
- 239000000243 solution Substances 0.000 description 9
- 238000012360 testing method Methods 0.000 description 8
- 239000000126 substance Substances 0.000 description 5
- 244000052616 bacterial pathogen Species 0.000 description 4
- 229920001817 Agar Polymers 0.000 description 3
- 239000008272 agar Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 238000000859 sublimation Methods 0.000 description 3
- 230000008022 sublimation Effects 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000008223 sterile water Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229920000544 Gore-Tex Polymers 0.000 description 1
- 239000007836 KH2PO4 Substances 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 238000006887 Ullmann reaction Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000006161 blood agar Substances 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 230000036512 infertility Effects 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 229940091925 mediplast Drugs 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 1
- 235000019796 monopotassium phosphate Nutrition 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000008174 sterile solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/06—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum the process involving freezing
Definitions
- the invention relates to a method for freeze drying under sterile conditions and a container for carrying out the method.
- the invention particularly relates to the drying of biological and / or pharmaceutical material.
- Freeze-drying of biological and pharmaceutical substances is generally known (see also Ullmanns Enzyklopadie der Technischen Chemie, 3rd edition, Vol. I, p. 556 ff.). In order to avoid contamination of the dried goods with germs and other impurities, complex equipment and process engineering measures are taken.
- the procedure is such that vials containing the frozen good are provided with a bacterial filter and the good in the vial is dried in a first drying step until sublimation of the frozen solvent is complete is.
- the so-called post-drying or residual drying the goods remaining moisture removed. Since this second drying step is usually carried out in a special apparatus, the ampoules or vials must be removed from the first drying apparatus in a further contamination-sensitive operation and introduced into the second drying apparatus.
- the bacterial filter is removed and replaced by an aluminum cap with a rubber diaphragm and a hollow needle.
- the drying room is filled with an inert gas and with a slight overpressure and the diaphragm opening is sealed as vapor-tight as possible by a sealing compound.
- freeze-drying of biological and pharmaceutical material is also carried out on plates under sterile conditions.
- a solution of the material to be dried is first sterilized, for example by filtration through a sterile filter, then poured onto plates under sterile conditions and freeze-dried using known methods.
- this method presupposes that the entire freeze dryer can be sterilized. It is also necessary to keep the area around the drying plant germ-free.
- the aim of the invention is to overcome the disadvantages indicated above and to provide a simple method by means of which a sterile, freeze-dried material can be obtained without the complex sterility requirements for the drying system and the space surrounding it.
- the material to be dried is introduced under sterile conditions into a germ-tight sealable container, the boundary wall surfaces of which at least partially consist of a germ-tight, porous, water-vapor-permeable hydrophobic membrane, that the container is sealed germ-tight and pressure-tight, in particular glued or welded, and the material is freeze-dried directly in the closed container under usual conditions.
- the invention is based on the surprising finding that, contrary to expectations, the steam flow resulting from the sublimation of solvent molecules, in particular water molecules, which flows from the material to be dried to the condenser, is only hindered to a small extent by the membrane used in the process according to the invention.
- the freeze-drying of material that is enclosed by the membrane takes place almost as quickly as the freeze-drying of the same open, non-packaged material.
- the membranes used according to the invention are hydrophobic membranes, the pores contain, on the one hand permeable to water vapor, but on the other hand are so small that they can no longer be passed by microorganisms. Such pores preferably have a size of ⁇ 0.5 ⁇ m, in particular of ⁇ 0.2 ⁇ m.
- membranes are preferably used which are still tear-resistant even under the respective process conditions when wet.
- the method according to the invention can also be carried out with less stable membranes, provided that these are reinforced with a carrier material or are not subjected to excessive mechanical stress.
- the proportion of the membrane on the wall surface of the container used in the method according to the invention depends on the respectively selected conditions and the drying time and can easily be found out by a person skilled in the art by simply trying it out.
- the entire wall surface consists of the membrane film, in a further preferred embodiment approximately half.
- the method according to the invention can also advantageously be carried out even if the wall surface consists of only 10% of the membrane film.
- cellulose and conventional cellulose derivatives are particularly suitable.
- membranes made of films of polymer compounds, such as polytetrafluoroethylene or polypropylene, are also preferably used.
- Goretex and similar membranes are also available Usual film tubes used, such as those sold by Vihuri OY, Wipack, Finland, under the name "Mediplast".
- any film membrane can be used regardless of its constituents, provided that it fulfills the requirements specified in DIN standard 58 953 with regard to germ density, air permeability and, in particular, strength.
- the method according to the invention is carried out with a bag or tube, which preferably consists of two walls which are tightly and pressure-tightly connected at their edges, of which one wall consists of liquid-tight material and the other wall is formed by the membrane.
- the membrane is preferably welded or glued to the vessel.
- Troughs are particularly suitable as vessels according to the invention.
- the trough consists of liquid-tight plastic and preferably has a wall thickness of 0.5 to 1 mm.
- drying conditions such as pressure, temperature and quantity, depend on the material to be dried, the thickness of the membrane as well as the size and number of its pores and have to be determined for the respective material and the packaging by usual and simple trials.
- the test of the germ density of a membrane was carried out in accordance with DIN 58 953 in such a way that microorganisms in water drops were placed on the test pieces and after the water drops had dried on it was examined whether microorganisms had passed through on the underside of the test pieces.
- the membrane film to be tested was cut into squares with an edge length of approximately 50 mm.
- the test pieces were sterilized and dried. Each test piece of the sterilized membrane was placed with the side that can be contaminated during use upwards on a sterilized surface and inoculated with 5 drops of 0.1 ml (corresponding to 107 to 107 germs).
- the test pieces were stored at room temperature from 20 to 25 ° C under a relative humidity of 40 to 60%. The drops must be completely dry within 6 hours.
- Each specimen was placed with the inoculated area up on the surface of a blood agar plate (1.5% agar) so that the entire film area came into contact with the agar. After 5 to 6 seconds the paper was removed.
- the plates were incubated at 37 ° C for 16 to 25 h. If the agar plates treated with such film samples show no growth, the film is considered to be sufficiently germ-tight. Further information on testing the germ tightness of membranes, in particular the production of test microbial suspensions, can be found in part 6 of DIN standard 58 953.
- a nutrient solution was prepared which consisted of 10 g peptone, 5 g glucose, 5 g NaCl, 0.084 g KH2PO4, 0.187 g Na2-HPO4x2H2O and pyrogen-free water ad 1.0 l existed and which was adjusted to pH 7.0. It was then sterilized in a closed vial.
- a transparent sterile bag consisting of a transparent film and a suitable paper was prepared to hold the sterile nutrient solution to be lyophilized.
- the commercially available transparent sterilization pouch film from Wipak Medical, type Steri-King R 47, which is tubular, i.e. welded on both sides, otherwise open, located on a roll (width of the roll 400 mm), cut off a piece with a length of 800 mm. This tube was sealed on the two open sides to a bag with a commercially available film device.
- This bag was then sterilized in an autoclave with a filter program at 123 ° C and 2 bar steam pressure, the sterile bag with the transparent film facing downwards for better handling in an unsterile sheet tray (VA sheet, dimensions: length 800 mm, width 400 mm, height 30 mm) and opened in a laminar flow box under sterile conditions with disinfected scissors by cutting off a corner. Through this opening of approximately 30 mm between the film and paper, 1.5 l of the sterile nutrient solution were introduced via a sterile tube pushed into the opening. The bag filled in this way was sealed in the laminar flow box under sterile conditions by means of a commercially available film sealing device by corner sealing.
- the entire arrangement (sheet tray, bag and sterile solution) was placed on a plate pre-cooled to -45 ° C in a commercially available, non-sterilizable freeze drying system from Edwards + Kniese a total floor space of 1.5 m2 and the solution frozen.
- freeze-drying was carried out at a pressure of 10 ⁇ 1 torr and a plate temperature of 22 ° C and the product was dried at 10 ⁇ 3 torr, also under non-sterile conditions.
- the total drying time was approx. 72 h.
- the freeze-dried material thus obtained which was present as a light brown powder in the transparent sterilization bag, was placed in a laminar flow box including the bag and dissolved in 1.5 l of sterile water.
- the intended puncture site on the paper side was disinfected with alcohol, a total of 1.5 l of sterile water was added to the bag using a sterile cannula and a suitable sterile syringe, the dried material was dissolved and the solution was transferred to a sterile bottle. This solution was incubated for 4 days at 37 ° C. and the germ count of the incubated solution was then determined using the membrane filter method.
Landscapes
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
- Drying Of Solid Materials (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT89109246T ATE73226T1 (de) | 1988-05-26 | 1989-05-23 | Behaelter zum gefriertrocknen unter sterilen bedingungen. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3817906 | 1988-05-26 | ||
DE3817906A DE3817906A1 (de) | 1988-05-26 | 1988-05-26 | Verfahren und behaeltnis zum gefriertrocknen unter sterilen bedingungen |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0343596A2 true EP0343596A2 (fr) | 1989-11-29 |
EP0343596A3 EP0343596A3 (en) | 1990-02-28 |
EP0343596B1 EP0343596B1 (fr) | 1992-03-04 |
Family
ID=6355171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89109246A Expired - Lifetime EP0343596B1 (fr) | 1988-05-26 | 1989-05-23 | Récipient pour lyophilisation sous conditions stériles |
Country Status (13)
Country | Link |
---|---|
EP (1) | EP0343596B1 (fr) |
JP (1) | JPH0229256A (fr) |
AT (1) | ATE73226T1 (fr) |
CA (1) | CA1337974C (fr) |
DD (1) | DD283864A5 (fr) |
DE (2) | DE3817906A1 (fr) |
DK (1) | DK173643B1 (fr) |
ES (1) | ES2030556T3 (fr) |
FI (1) | FI91442C (fr) |
GR (1) | GR3004584T3 (fr) |
HU (1) | HU204126B (fr) |
IE (1) | IE61012B1 (fr) |
PL (1) | PL159938B1 (fr) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5257983A (en) * | 1991-04-12 | 1993-11-02 | Cryopharm Corporation | Blood bag for lyophilization |
US5340592A (en) * | 1988-05-18 | 1994-08-23 | Cobe Laboratories, Inc. | Lyophilization of erythrocytes |
US5425951A (en) * | 1988-05-18 | 1995-06-20 | Cryopharm Corporation | Method of reconstituting lyophilized cells |
WO1995027180A1 (fr) * | 1994-04-04 | 1995-10-12 | W.L. Gore & Associates, Inc. | Procede ameliore pour minimiser la contamination de produits lyophilises |
US5596814A (en) * | 1995-11-06 | 1997-01-28 | W. L. Gore & Associates, Inc. | Vented vial stopper for processing freeze-dried products |
FR2738057A1 (fr) * | 1995-08-22 | 1997-02-28 | Lab Francais Du Fractionnement | Emballage etanche pour sechage, notamment lyophilisation, et procede de sechage, notamment de lyophilisation, a l'aide d'un tel emballage |
WO1997008503A1 (fr) * | 1995-08-22 | 1997-03-06 | Laboratoire Français Du Fractionnement Et Des Biotechnologies | Emballage etanche pour sechage, notamment lyophilisation, et procede de sechage, notamment de lyophilisation, a l'aide d'un tel emballage |
WO1997020181A1 (fr) | 1995-11-29 | 1997-06-05 | Immuno Aktiengesellschaft | Procede et dispositif de lyophilisation, conteneurs et systeme de remplissage |
US5732837A (en) * | 1994-08-19 | 1998-03-31 | W. L. Gore & Associates, Inc. | Vented vial closure member for freeze-drying which minimizes contamination of freeze-dried products |
US5958778A (en) * | 1995-09-22 | 1999-09-28 | The United States Of America As Represented By The Department Of Health And Human Services | Container for drying biological samples, method of making such container, and method of using same |
US6312648B1 (en) | 1998-01-12 | 2001-11-06 | The United States Of America As Represented By The Department Of Health And Human Services | Applicator system |
EP1958618A1 (fr) * | 2007-02-15 | 2008-08-20 | Octapharma AG | Procédé destiné à la lyophilisation par reconstitution optimisée de biopolymères |
EP2386399B1 (fr) * | 2010-04-23 | 2015-06-10 | MC Beteiligungs-GmbH | Procédé pour faire des trous dans un revêtement étanche et corps de base avec un tel revêtement |
WO2015162273A1 (fr) | 2014-04-25 | 2015-10-29 | Merck Sharp & Dohme Bv | Procédé pour assécher de multiples corps individuels congelés et système permettant d'appliquer ce procédé |
US11609043B2 (en) | 2019-03-14 | 2023-03-21 | Terumo Bct Biotechnologies, Llc | Lyophilization container fill fixture, system and method of use |
US11634257B2 (en) | 2017-10-09 | 2023-04-25 | Terumo Bct Biotechnologies, Llc | Lyophilization container and method of using same |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19751031A1 (de) | 1997-11-19 | 1999-06-24 | Ingo Dipl Ing Heschel | Verfahren zur Herstellung poröser Strukturen |
DE19815993C2 (de) * | 1998-04-09 | 2003-03-06 | Schott Glas | Behälter zur Gefriertrocknung und Aufbewahrung medizinischer Produkte |
JP2010124931A (ja) * | 2008-11-26 | 2010-06-10 | Kanae Co Ltd | 凍結乾燥製剤の包装体の製造方法 |
JP2019090596A (ja) * | 2017-11-10 | 2019-06-13 | エイブル株式会社 | 凍結乾燥生成物の製造方法、及び、凍結乾燥用袋、並びに、凍結乾燥装置 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB995930A (en) * | 1961-11-28 | 1965-06-23 | Leybold Hochvakuum Anlagen | Method of freeze drying |
CH394945A (de) * | 1961-07-17 | 1965-06-30 | Hermorion Ltd | Verpackung für sterilisierte Milch |
US3391466A (en) * | 1965-09-24 | 1968-07-09 | Unilever Nv | Freeze-drying |
FR2284842A1 (fr) * | 1974-09-11 | 1976-04-09 | Nestle Sa | Perfectionnement apporte la lyophilisation des produits solides, liquides ou pateux |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60168464A (ja) * | 1983-11-18 | 1985-08-31 | 新技術事業団 | 血液保存方法及びその保存用容器 |
JPS6136942A (ja) * | 1984-07-28 | 1986-02-21 | Sony Corp | 電子部品装置 |
-
1988
- 1988-05-26 DE DE3817906A patent/DE3817906A1/de not_active Withdrawn
-
1989
- 1989-05-11 IE IE154189A patent/IE61012B1/en not_active IP Right Cessation
- 1989-05-19 CA CA000600212A patent/CA1337974C/fr not_active Expired - Lifetime
- 1989-05-23 EP EP89109246A patent/EP0343596B1/fr not_active Expired - Lifetime
- 1989-05-23 DE DE8989109246T patent/DE58900902D1/de not_active Expired - Lifetime
- 1989-05-23 AT AT89109246T patent/ATE73226T1/de not_active IP Right Cessation
- 1989-05-23 ES ES198989109246T patent/ES2030556T3/es not_active Expired - Lifetime
- 1989-05-24 DD DD89328870A patent/DD283864A5/de not_active IP Right Cessation
- 1989-05-24 DK DK198902525A patent/DK173643B1/da not_active IP Right Cessation
- 1989-05-24 PL PL1989279609A patent/PL159938B1/pl unknown
- 1989-05-25 HU HU892683A patent/HU204126B/hu unknown
- 1989-05-25 FI FI892563A patent/FI91442C/fi not_active IP Right Cessation
- 1989-05-26 JP JP1131693A patent/JPH0229256A/ja active Granted
-
1992
- 1992-05-13 GR GR920400224T patent/GR3004584T3/el unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH394945A (de) * | 1961-07-17 | 1965-06-30 | Hermorion Ltd | Verpackung für sterilisierte Milch |
GB995930A (en) * | 1961-11-28 | 1965-06-23 | Leybold Hochvakuum Anlagen | Method of freeze drying |
US3391466A (en) * | 1965-09-24 | 1968-07-09 | Unilever Nv | Freeze-drying |
FR2284842A1 (fr) * | 1974-09-11 | 1976-04-09 | Nestle Sa | Perfectionnement apporte la lyophilisation des produits solides, liquides ou pateux |
Non-Patent Citations (1)
Title |
---|
KUNSTSTOFFE, Band 71, Nr. 5, Mai 1981, Seiten 287-293, M}nchen, DE; H. RODER: "Kunststoffe in der Verpackung. Kunststoff-Verpackungsfolien" * |
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5340592A (en) * | 1988-05-18 | 1994-08-23 | Cobe Laboratories, Inc. | Lyophilization of erythrocytes |
US5425951A (en) * | 1988-05-18 | 1995-06-20 | Cryopharm Corporation | Method of reconstituting lyophilized cells |
US5257983A (en) * | 1991-04-12 | 1993-11-02 | Cryopharm Corporation | Blood bag for lyophilization |
WO1995027180A1 (fr) * | 1994-04-04 | 1995-10-12 | W.L. Gore & Associates, Inc. | Procede ameliore pour minimiser la contamination de produits lyophilises |
US5732837A (en) * | 1994-08-19 | 1998-03-31 | W. L. Gore & Associates, Inc. | Vented vial closure member for freeze-drying which minimizes contamination of freeze-dried products |
FR2738057A1 (fr) * | 1995-08-22 | 1997-02-28 | Lab Francais Du Fractionnement | Emballage etanche pour sechage, notamment lyophilisation, et procede de sechage, notamment de lyophilisation, a l'aide d'un tel emballage |
WO1997008503A1 (fr) * | 1995-08-22 | 1997-03-06 | Laboratoire Français Du Fractionnement Et Des Biotechnologies | Emballage etanche pour sechage, notamment lyophilisation, et procede de sechage, notamment de lyophilisation, a l'aide d'un tel emballage |
FR2740108A1 (fr) * | 1995-08-22 | 1997-04-25 | Lab Francais Du Fractionnement | Emballage etanche pour sechage, notamment lyophilisation, et procede de sechage, notamment de lyophilisation, a l'aide d'un tel emballage |
US6503455B1 (en) | 1995-09-22 | 2003-01-07 | The United States Of America As Represented By The Department Of Health And Human Services | Container for dying biological samples, method of making such container, and method of using same |
US5958778A (en) * | 1995-09-22 | 1999-09-28 | The United States Of America As Represented By The Department Of Health And Human Services | Container for drying biological samples, method of making such container, and method of using same |
US5596814A (en) * | 1995-11-06 | 1997-01-28 | W. L. Gore & Associates, Inc. | Vented vial stopper for processing freeze-dried products |
WO1997020181A1 (fr) | 1995-11-29 | 1997-06-05 | Immuno Aktiengesellschaft | Procede et dispositif de lyophilisation, conteneurs et systeme de remplissage |
US6312648B1 (en) | 1998-01-12 | 2001-11-06 | The United States Of America As Represented By The Department Of Health And Human Services | Applicator system |
US8518452B2 (en) | 2007-02-15 | 2013-08-27 | Octapharma Ag | Method for stabilizing blood plasma components in a lyophilizate using carbon dioxide and phosphoric acid |
EP2431024A1 (fr) | 2007-02-15 | 2012-03-21 | Octapharma AG | Procédé de stabilisation de composants de plasma sanguin dans un lyophilisat |
EP1958618A1 (fr) * | 2007-02-15 | 2008-08-20 | Octapharma AG | Procédé destiné à la lyophilisation par reconstitution optimisée de biopolymères |
EP2386399B1 (fr) * | 2010-04-23 | 2015-06-10 | MC Beteiligungs-GmbH | Procédé pour faire des trous dans un revêtement étanche et corps de base avec un tel revêtement |
WO2015162273A1 (fr) | 2014-04-25 | 2015-10-29 | Merck Sharp & Dohme Bv | Procédé pour assécher de multiples corps individuels congelés et système permettant d'appliquer ce procédé |
US11634257B2 (en) | 2017-10-09 | 2023-04-25 | Terumo Bct Biotechnologies, Llc | Lyophilization container and method of using same |
US11609043B2 (en) | 2019-03-14 | 2023-03-21 | Terumo Bct Biotechnologies, Llc | Lyophilization container fill fixture, system and method of use |
US11740019B2 (en) | 2019-03-14 | 2023-08-29 | Terumo Bct Biotechnologies, Llc | Lyophilization loading tray assembly and system |
US11747082B2 (en) | 2019-03-14 | 2023-09-05 | Terumo Bct Biotechnologies, Llc | Multi-part lyophilization container and method of use |
US11815311B2 (en) | 2019-03-14 | 2023-11-14 | Terumo Bct Biotechnologies, Llc | Lyophilization container fill fixture, system and method of use |
US11994343B2 (en) | 2019-03-14 | 2024-05-28 | Terumo Bct Biotechnologies, Llc | Multi-part lyophilization container and method of use |
Also Published As
Publication number | Publication date |
---|---|
DK173643B1 (da) | 2001-05-14 |
DE3817906A1 (de) | 1989-11-30 |
JPH0229256A (ja) | 1990-01-31 |
ATE73226T1 (de) | 1992-03-15 |
IE891541L (en) | 1989-11-26 |
EP0343596A3 (en) | 1990-02-28 |
HUT52617A (en) | 1990-07-28 |
DD283864A5 (de) | 1990-10-24 |
DK252589A (da) | 1989-11-27 |
FI91442C (fi) | 1994-06-27 |
PL159938B1 (pl) | 1993-01-29 |
EP0343596B1 (fr) | 1992-03-04 |
DK252589D0 (da) | 1989-05-24 |
FI892563A (fi) | 1989-11-27 |
JPH0450830B2 (fr) | 1992-08-17 |
DE58900902D1 (de) | 1992-04-09 |
CA1337974C (fr) | 1996-01-23 |
FI892563A0 (fi) | 1989-05-25 |
PL279609A1 (en) | 1990-01-22 |
ES2030556T3 (es) | 1992-11-01 |
FI91442B (fi) | 1994-03-15 |
GR3004584T3 (fr) | 1993-04-28 |
HU204126B (en) | 1991-11-28 |
IE61012B1 (en) | 1994-09-07 |
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