RU2000113224A - METHOD FOR PRODUCING A HIGH DEGREE OF VIRUS-SAFE COMPONENTS FOR PRODUCING FIBRINE GLUE FROM A HUMAN PLASMA POOL - Google Patents
METHOD FOR PRODUCING A HIGH DEGREE OF VIRUS-SAFE COMPONENTS FOR PRODUCING FIBRINE GLUE FROM A HUMAN PLASMA POOLInfo
- Publication number
- RU2000113224A RU2000113224A RU2000113224/14A RU2000113224A RU2000113224A RU 2000113224 A RU2000113224 A RU 2000113224A RU 2000113224/14 A RU2000113224/14 A RU 2000113224/14A RU 2000113224 A RU2000113224 A RU 2000113224A RU 2000113224 A RU2000113224 A RU 2000113224A
- Authority
- RU
- Russia
- Prior art keywords
- solution
- thrombin
- stage
- prothrombin
- activated
- Prior art date
Links
- 210000002381 Plasma Anatomy 0.000 title claims 2
- 239000003292 glue Substances 0.000 title 1
- 238000004519 manufacturing process Methods 0.000 title 1
- NKCXQMYPWXSLIZ-PSRDDEIFSA-N (2S)-2-[[(2S)-1-[(2S)-5-amino-2-[[2-[[(2S)-6-amino-2-[[2-[[(2S)-2-[[(2S)-4-amino-2-[[(2S)-2-[[(2S,3R)-2-[[(2S)-2-[[(2S,3R)-2-amino-3-hydroxybutanoyl]amino]-3-(1H-indol-3-yl)propanoyl]amino]-3-hydroxybutanoyl]amino]propanoyl]amino]-4-oxobutanoyl]amino]-3-m Chemical compound O=C([C@H](CCC(N)=O)NC(=O)CNC(=O)[C@H](CCCCN)NC(=O)CNC(=O)[C@@H](NC(=O)[C@H](CC(N)=O)NC(=O)[C@H](C)NC(=O)[C@@H](NC(=O)[C@H](CC=1C2=CC=CC=C2NC=1)NC(=O)[C@@H](N)[C@@H](C)O)[C@@H](C)O)C(C)C)N1CCC[C@H]1C(=O)N[C@@H](CO)C(O)=O NKCXQMYPWXSLIZ-PSRDDEIFSA-N 0.000 claims 16
- 108090000190 Thrombin Proteins 0.000 claims 16
- 229960004072 thrombin Drugs 0.000 claims 16
- 239000000243 solution Substances 0.000 claims 12
- 239000011780 sodium chloride Substances 0.000 claims 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims 7
- 102100015239 F2 Human genes 0.000 claims 6
- 108010094028 Prothrombin Proteins 0.000 claims 6
- 229940039716 Prothrombin Drugs 0.000 claims 6
- 239000007853 buffer solution Substances 0.000 claims 6
- UXVMQQNJUSDDNG-UHFFFAOYSA-L cacl2 Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims 5
- 239000001110 calcium chloride Substances 0.000 claims 5
- 229910001628 calcium chloride Inorganic materials 0.000 claims 5
- 238000010438 heat treatment Methods 0.000 claims 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 5
- 210000002845 Virion Anatomy 0.000 claims 4
- 239000002244 precipitate Substances 0.000 claims 4
- 238000002360 preparation method Methods 0.000 claims 4
- 150000003839 salts Chemical class 0.000 claims 4
- 238000005341 cation exchange Methods 0.000 claims 3
- 239000003814 drug Substances 0.000 claims 3
- 229940079593 drugs Drugs 0.000 claims 3
- 238000004108 freeze drying Methods 0.000 claims 3
- 238000001556 precipitation Methods 0.000 claims 3
- 239000006228 supernatant Substances 0.000 claims 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 3
- 102000007562 Serum Albumin Human genes 0.000 claims 2
- 108010071390 Serum Albumin Proteins 0.000 claims 2
- HRXKRNGNAMMEHJ-UHFFFAOYSA-K Trisodium citrate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O HRXKRNGNAMMEHJ-UHFFFAOYSA-K 0.000 claims 2
- 239000007864 aqueous solution Substances 0.000 claims 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M buffer Substances [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims 2
- 239000001913 cellulose Substances 0.000 claims 2
- 229920002678 cellulose Polymers 0.000 claims 2
- 239000002131 composite material Substances 0.000 claims 2
- QKSIFUGZHOUETI-UHFFFAOYSA-N copper;azane Chemical compound N.N.N.N.[Cu+2] QKSIFUGZHOUETI-UHFFFAOYSA-N 0.000 claims 2
- 239000003599 detergent Substances 0.000 claims 2
- 238000011026 diafiltration Methods 0.000 claims 2
- 230000000694 effects Effects 0.000 claims 2
- 239000012510 hollow fiber Substances 0.000 claims 2
- 239000012528 membrane Substances 0.000 claims 2
- 239000002245 particle Substances 0.000 claims 2
- 102000004169 proteins and genes Human genes 0.000 claims 2
- 108090000623 proteins and genes Proteins 0.000 claims 2
- 239000000377 silicon dioxide Substances 0.000 claims 2
- 235000012239 silicon dioxide Nutrition 0.000 claims 2
- 239000001509 sodium citrate Substances 0.000 claims 2
- 239000002904 solvent Substances 0.000 claims 2
- 239000011778 trisodium citrate Substances 0.000 claims 2
- 230000003253 viricidal Effects 0.000 claims 2
- LENZDBCJOHFCAS-UHFFFAOYSA-N 2-amino-2-(hydroxymethyl)propane-1,3-diol Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-K 2qpq Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 claims 1
- SLXKOJJOQWFEFD-UHFFFAOYSA-N Aminocaproic acid Chemical compound NCCCCCC(O)=O SLXKOJJOQWFEFD-UHFFFAOYSA-N 0.000 claims 1
- 229920002307 Dextran Polymers 0.000 claims 1
- 102100008658 FN1 Human genes 0.000 claims 1
- 108010071289 Factor XIII Proteins 0.000 claims 1
- 108010049003 Fibrinogen Proteins 0.000 claims 1
- 229940012952 Fibrinogen Drugs 0.000 claims 1
- 102000008946 Fibrinogen Human genes 0.000 claims 1
- 229940019698 Fibrinogen containing hemostatics Drugs 0.000 claims 1
- 108010067306 Fibronectins Proteins 0.000 claims 1
- 229960003766 Thrombin (Human) Drugs 0.000 claims 1
- 241000700605 Viruses Species 0.000 claims 1
- 239000002253 acid Substances 0.000 claims 1
- 238000003916 acid precipitation Methods 0.000 claims 1
- 239000008366 buffered solution Substances 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000004587 chromatography analysis Methods 0.000 claims 1
- 230000036425 denaturation Effects 0.000 claims 1
- 238000004925 denaturation Methods 0.000 claims 1
- 238000007865 diluting Methods 0.000 claims 1
- 229940012444 factor XIII Drugs 0.000 claims 1
- 230000037320 fibronectin Effects 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 150000004676 glycans Polymers 0.000 claims 1
- 238000004255 ion exchange chromatography Methods 0.000 claims 1
- 150000002632 lipids Chemical class 0.000 claims 1
- 238000000034 method Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 230000001264 neutralization Effects 0.000 claims 1
- 229920001282 polysaccharide Polymers 0.000 claims 1
- 239000005017 polysaccharide Substances 0.000 claims 1
- 150000004804 polysaccharides Polymers 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 239000000047 product Substances 0.000 claims 1
- 238000000746 purification Methods 0.000 claims 1
- 239000012266 salt solution Substances 0.000 claims 1
- 238000005185 salting out Methods 0.000 claims 1
- 230000003381 solubilizing Effects 0.000 claims 1
- 230000000087 stabilizing Effects 0.000 claims 1
- 150000003568 thioethers Chemical class 0.000 claims 1
Claims (16)
а) преципитации белков цельной плазмы путем добавления первой соли в количестве, достаточном для достижения эффекта высаливания и для доведения рН до значения от около 7,5 до около 8,5 при температуре, составляющей от около 0oС до около 4oС, или путем добавления второй соли в количестве, достаточном для достижения кислотной преципитации и для доведения рН до значения от около 4,5 до около 5,5 при температуре, составляющей от около 4oС до около 20oС, в результате чего осаждаются фибриноген, фактор XIII и фибронектин, причем указанную преципитацию проводят в присутствии амино-6-гексановой кислоты в концентрации, составляющей, по крайней мере, 50 мМ; и выделения супернатанта, содержащего протромбин;
б) диафильтрации указанного супернатанта вплоть до получения раствора протромбина, который имеет осмолярность около 100 мОсмоль/кг массы или менее;
в) разбавления указанного протромбинового раствора водой, которую добавляют в отношении примерно 4 объема воды на 1 объем протромбинового раствора;
г) преципитации протромбина путем добавления кислотного раствора до получения значения рН примерно 5,2;
д) солюбилизации преципитата стадии (г) в растворе, имеющем около нейтральный рН и
е) превращения протромбина стадии (д) в тромбин в присутствии хлорида кальция до достижения концентрации хлорида кальция от около 20 до около 32 мМ.1. The method of obtaining thrombin, comprising the following stages
a) precipitation of whole plasma proteins by adding the first salt in an amount sufficient to achieve the salting-out effect and to bring the pH to a value of from about 7.5 to about 8.5 at a temperature of from about 0 o C to about 4 o C, or by adding a second salt in an amount sufficient to achieve acid precipitation and to bring the pH to a value of from about 4.5 to about 5.5 at a temperature of about 4 ° C. to about 20 ° C. , whereby fibrinogen precipitates, a factor XIII and fibronectin, moreover, the specified precipitation pr bred in the presence of amino-6-hexanoic acid in a concentration of at least 50 mm; and isolating a prothrombin-containing supernatant;
b) diafiltration of the indicated supernatant until a prothrombin solution is obtained that has an osmolality of about 100 mOsmol / kg or less;
c) diluting said prothrombin solution with water, which is added in relation to about 4 volumes of water per 1 volume of prothrombin solution;
d) prothrombin precipitation by adding an acid solution until a pH of about 5.2 is obtained;
e) solubilizing the precipitate of step (d) in a solution having about a neutral pH and
e) the conversion of prothrombin stage (d) to thrombin in the presence of calcium chloride to achieve a concentration of calcium chloride from about 20 to about 32 mm.
ж) инкубирования указанного тромбина с вирицидным раствором растворителя/детергента в количестве, достаточном для инактивации липид-содержащих вирусов;
з) очистки инкубированного тробина путем последующей ионообменной хроматографии с использованием одной катионо-обменной среды с сульфалкил-активированным полисахаридом, выбранной из группы, состоящей из активированной сульфалкилом полиагарозы, активированного сульфалкилом полидекстрана и несжимаемой композиционной среды, состоящей из активированного сульфалкилом декстрана и частиц двуокиси кремния, обладающей высокой степенью селективности по отношению к тромбину, и с использованием в качестве элюирующего агента водного солевого раствора, по крайней мере, в трех возрастающих концентрациях и
и) выделения элюата тромбинового пика при проведении хроматографии (з) и замену соли элюата физиологически приемлемым стабилизирующим буфером препарата в целях стабилизации выделенного тромбина, и получения препарата буферного раствора тромбина.2. The method according to p. 1, which, in addition, includes the following stages
g) incubating said thrombin with a viricidal solution of solvent / detergent in an amount sufficient to inactivate lipid-containing viruses;
h) purification of incubated trobin by subsequent ion-exchange chromatography using one cation-exchange medium with a sulfalkyl-activated polysaccharide selected from the group consisting of sulfagyl-activated polyagarose, sulfide-activated polydextran and an incompressible composition medium consisting of sulfonyl-activated dextran and particles of silicon dioxide, having a high degree of selectivity with respect to thrombin, and using an aqueous salt solution as an eluting agent of a solution of at least three and increasing concentrations
i) isolating the thrombin peak eluate during chromatography (h) and replacing the eluate salt with a physiologically acceptable stabilizing buffer of the preparation in order to stabilize the thrombin isolated, and preparing the thrombin buffered solution.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/960,660 US5981254A (en) | 1997-10-30 | 1997-10-30 | Process for producing thrombin from plasma |
US08/960,660 | 1997-10-30 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2000113224A true RU2000113224A (en) | 2002-05-20 |
RU2236237C2 RU2236237C2 (en) | 2004-09-20 |
Family
ID=25503448
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2000113224/15A RU2236237C2 (en) | 1997-10-30 | 1998-10-29 | Method for producing highly virus-safety components for preparing fibrin glue from human plasma blood pool |
Country Status (16)
Country | Link |
---|---|
US (1) | US5981254A (en) |
EP (1) | EP1027371B1 (en) |
JP (1) | JP4278861B2 (en) |
AT (1) | ATE305011T1 (en) |
AU (1) | AU759145B2 (en) |
CA (1) | CA2307380A1 (en) |
DE (1) | DE69831684T2 (en) |
DK (1) | DK1027371T3 (en) |
ES (1) | ES2249843T3 (en) |
IL (1) | IL135812A (en) |
IN (1) | IN185759B (en) |
NO (1) | NO323299B1 (en) |
NZ (1) | NZ504246A (en) |
PL (1) | PL194589B1 (en) |
RU (1) | RU2236237C2 (en) |
WO (1) | WO1999023111A1 (en) |
Families Citing this family (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT407484B (en) * | 1997-11-12 | 2001-03-26 | Bio Prod & Bio Eng Ag | MEDICINES FOR PROMOTING Wound Healing |
EP1250929A4 (en) * | 1999-12-20 | 2004-12-29 | Mitsubishi Pharma Corp | Virus-free plasma protein compositions treated with porous membrane and process for producing the same |
AU779126B2 (en) * | 1999-12-23 | 2005-01-06 | Csl Limited | Separation of fibrinogen from plasma proteases |
WO2001048016A1 (en) * | 1999-12-23 | 2001-07-05 | Csl Limited | Separation of fibrinogen from plasma proteases |
JP2002114799A (en) * | 2000-08-01 | 2002-04-16 | Nihon Pharmaceutical Co Ltd | Method for removing virus |
US7411006B2 (en) * | 2000-10-23 | 2008-08-12 | Shanbrom Technologies, Llc | Enhanced production of blood clotting factors and fibrin fabric |
US7365173B2 (en) * | 2002-02-04 | 2008-04-29 | American National Red Cross | Method for the production of pure virally inactivated butyrylcholinesterase |
DE10211632A1 (en) | 2002-03-15 | 2003-10-09 | Aventis Behring Gmbh | Process for the separation of viruses from a protein solution by nanofiltration |
US20070015230A1 (en) * | 2002-04-15 | 2007-01-18 | Hammond David J | Identification and characterization of analytes from whole blood |
US20060275753A1 (en) * | 2002-04-15 | 2006-12-07 | Hammond David J | Recovery of analytes using combinatorial libraries |
US20060275829A1 (en) * | 2002-04-15 | 2006-12-07 | Hammond David J | Combinatorial library for proteomic investigations |
WO2003088990A1 (en) * | 2002-04-15 | 2003-10-30 | American National Red Cross | Plasma protein-binding ligands |
GB0216001D0 (en) | 2002-07-10 | 2002-08-21 | Nat Blood Authority | Process and composition |
ATE428440T1 (en) * | 2002-07-23 | 2009-05-15 | Bio & Bio Licensing Sa | THROMB-GENERATING AND THROMB-CONTAINING PHARMACEUTICAL ACTIVE PREPARATIONS AND MEDICINAL PRODUCTS |
ES2214967B1 (en) * | 2003-03-06 | 2005-06-16 | Probitas Pharma, S.A | PROCEDURE FOR THE ELIMINATION OF VIRUSES IN FIBRINOGEN AND FIBRINOGEN SOLUTIONS OBTAINED BY SUCH PROCEDURE. |
JP4874806B2 (en) | 2003-12-01 | 2012-02-15 | ノボ ノルディスク ヘルス ケア アクチェンゲゼルシャフト | Virus filtration of liquid factor VII compositions |
JP4767253B2 (en) * | 2004-06-22 | 2011-09-07 | ザイモジェネティクス, インコーポレイテッド | Thrombin composition |
DE102004044429B4 (en) * | 2004-09-14 | 2009-04-30 | Biotest Ag | Process for the preparation of a composition containing von Willebrand factor |
ES2226587B1 (en) * | 2004-10-22 | 2005-12-16 | Probitas Pharma, S.A. | STABLE THROMBINE COMPOSITION. |
US20060270015A1 (en) * | 2005-05-26 | 2006-11-30 | Dan Pawlak | Thrombin purification |
FR2887883B1 (en) | 2005-06-29 | 2007-08-31 | Lab Francais Du Fractionnement | PROCESS FOR SEPARATING FIBRINOGEN PROTEINS, FACTOR XIII AND BIOLOGICAL GLUE OF SOLUBILIZED PLASMA FRONTION AND PREPARATION OF LYOPHILIZED CONCENTRATES OF SAID PROTEINS |
US20120195953A1 (en) * | 2007-09-19 | 2012-08-02 | Kieu Hoang | Fibrin sealant (FIBRINGLURAAS) consisting of a kit of lyophilized high concentrate fribinogen intentionally enriched and preserved with fibronolysis inhibitor A1AT |
GB0814570D0 (en) | 2008-08-08 | 2008-09-17 | Diagnostics For The Real World | Isolation of nucleic acid |
US9011846B2 (en) | 2011-05-02 | 2015-04-21 | Biomet Biologics, Llc | Thrombin isolated from blood and blood fractions |
NO2900247T3 (en) * | 2012-09-26 | 2018-06-16 | ||
RU2583931C2 (en) * | 2014-06-11 | 2016-05-10 | Федеральное государственное бюджетное учреждение Гематологический научный центр Министерства здравоохранения РФ | Method of producing thrombin concentrate |
US9932388B2 (en) | 2014-11-13 | 2018-04-03 | Hemarus Therapeutics Limited | Chromatographic process for producing high purity fibrinogen and thrombin |
JP6666757B2 (en) * | 2016-03-10 | 2020-03-18 | 日本メジフィジックス株式会社 | Method for quantifying polyoxyethylene nonionic surfactant and method for producing radiopharmaceutical preparation |
BR112020016727A2 (en) * | 2018-02-19 | 2020-12-15 | Bayer Healthcare Llc | MODIFIED FILTERING MEMBRANE AND METHOD |
WO2020229521A1 (en) | 2019-05-14 | 2020-11-19 | INSERM (Institut National de la Santé et de la Recherche Médicale) | Methods for inhibiting or reducing bacterial biofilms on a surface |
CN113754757B (en) * | 2021-07-01 | 2024-06-14 | 华兰生物工程股份有限公司 | Preparation method of human fibrinogen |
WO2023020914A1 (en) | 2021-08-18 | 2023-02-23 | Biotest Ag | Dry heat treatment of plasma-derived factor viii |
KR20230121373A (en) * | 2022-02-11 | 2023-08-18 | 주식회사 녹십자 | Method for Purifying Factor XIII |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3843126C3 (en) * | 1988-12-22 | 1994-10-06 | Octapharma Ag | Process for the production of a high-purity thrombin concentrate |
FR2679251B1 (en) * | 1991-07-18 | 1993-11-12 | Nord Assoc Essor Transfusion San | PROCESS FOR THE PREPARATION OF A HUMAN THROMBIN CONCENTRATE FOR THERAPEUTIC USE. |
US5395923A (en) * | 1993-02-23 | 1995-03-07 | Haemacure-Biotech, Inc. | Process for the obtention of a biological adhesive made of concentrated coagulation factors by "salting-out" |
US5290918A (en) * | 1993-02-23 | 1994-03-01 | Haemacure Biotech Inc. | Process for the obtention of a biological adhesive made of concentrated coagulation factors by acidic precipitation |
US5506127A (en) * | 1994-09-21 | 1996-04-09 | Proba; Zbigniew | Therapeutic grade thrombin produced by chromatography |
-
1997
- 1997-10-30 US US08/960,660 patent/US5981254A/en not_active Expired - Fee Related
-
1998
- 1998-10-29 CA CA002307380A patent/CA2307380A1/en not_active Abandoned
- 1998-10-29 IN IN1927CA1998 patent/IN185759B/en unknown
- 1998-10-29 AT AT98951133T patent/ATE305011T1/en not_active IP Right Cessation
- 1998-10-29 PL PL98340300A patent/PL194589B1/en not_active IP Right Cessation
- 1998-10-29 DK DK98951133T patent/DK1027371T3/en active
- 1998-10-29 WO PCT/CA1998/001008 patent/WO1999023111A1/en active IP Right Grant
- 1998-10-29 IL IL135812A patent/IL135812A/en not_active IP Right Cessation
- 1998-10-29 ES ES98951133T patent/ES2249843T3/en not_active Expired - Lifetime
- 1998-10-29 DE DE69831684T patent/DE69831684T2/en not_active Expired - Lifetime
- 1998-10-29 EP EP98951133A patent/EP1027371B1/en not_active Expired - Lifetime
- 1998-10-29 NZ NZ504246A patent/NZ504246A/en unknown
- 1998-10-29 JP JP2000518981A patent/JP4278861B2/en not_active Expired - Fee Related
- 1998-10-29 RU RU2000113224/15A patent/RU2236237C2/en not_active IP Right Cessation
- 1998-10-29 AU AU97316/98A patent/AU759145B2/en not_active Ceased
-
2000
- 2000-04-28 NO NO20002293A patent/NO323299B1/en not_active IP Right Cessation
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