ES2421736T3 - Procedimiento para la preparación de inmunoglobulinas para administración intravenosa y otros productos inmunoglobulínicos - Google Patents
Procedimiento para la preparación de inmunoglobulinas para administración intravenosa y otros productos inmunoglobulínicosInfo
- Publication number
- ES2421736T3 ES2421736T3 ES10184829T ES10184829T ES2421736T3 ES 2421736 T3 ES2421736 T3 ES 2421736T3 ES 10184829 T ES10184829 T ES 10184829T ES 10184829 T ES10184829 T ES 10184829T ES 2421736 T3 ES2421736 T3 ES 2421736T3
- Authority
- ES
- Spain
- Prior art keywords
- immunoglobulin
- resin
- buffer
- range
- elution
- 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.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
- C07K16/06—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies from serum
- C07K16/065—Purification, fragmentation
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K39/00—Medicinal preparations containing antigens or antibodies
- A61K39/395—Antibodies; Immunoglobulins; Immune serum, e.g. antilymphocytic serum
- A61K39/39591—Stabilisation, fragmentation
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
- A61P31/12—Antivirals
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P43/00—Drugs for specific purposes, not provided for in groups A61P1/00-A61P41/00
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Organic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Immunology (AREA)
- Pharmacology & Pharmacy (AREA)
- Animal Behavior & Ethology (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Chemical & Material Sciences (AREA)
- Molecular Biology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Epidemiology (AREA)
- Biochemistry (AREA)
- Biophysics (AREA)
- Genetics & Genomics (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Mycology (AREA)
- Microbiology (AREA)
- Virology (AREA)
- Communicable Diseases (AREA)
- Oncology (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Peptides Or Proteins (AREA)
Abstract
Un procedimiento para purificar inmunoglobulina G (IgG) a partir de una fracción proteica plasmática crudaque contiene inmunoglobulina, en donde el procedimiento comprende las etapas de: (a) preparar una suspensión acuosa de la fracción proteica plasmática cruda que contiene inmunoglobulina,de modo que la concentración de IgG en la suspensión acuosa sea de al menos aproximadamente 4 g/l, elpH de la suspensión que contiene inmunoglobulina está dentro del intervalo de 5,1 a 5,7 y la suspensiónque contiene inmunoglobulina se filtra adicionalmente mediante filtración en profundidad; (b) añadir un agente precipitante de proteína, sustancialmente no desnaturalizante, hidrosoluble a dichasuspensión filtrada de la etapa (a) en una cantidad suficiente para causar la precipitación de una elevadaproporción de proteínas no inmunoglobulinas G, inmunoglobulinas agregadas y partículas incluyendo partículaspotencialmente infecciosas tales como partículas víricas, sin causar una precipitación sustancial de lainmunoglobulina G monomérica, formando de esta manera una mezcla de precipitado sólido y material sobrenadantelíquido; en donde el agente precipitante es PEG 3350, PEG 4000 o PEG 6000 dentro del intervalode 4 a 10% en peso e incubar desde aproximadamente 2 horas hasta aproximadamente 12 horas atemperatura entre 2ºC y 8ºC; (c) clarificar y recuperar un material sobrenadante que contiene inmunoglobulina G a partir de la mezcla dela etapa (b); y filtrar en profundidad el material sobrenadante clarificado para eliminar las partículas y agregadosde gran tamaño; (d) aplicar el material sobrenadante clarificado que contiene inmunoglobulina G de la etapa (c) a una resinaDEAE Sepharose Fast Flow (DEAE) y posteriormente a una resina CM Sepharose Fast Flow (CM), en dondela resina DEAE y la resina CM están conectadas en serie y en donde el tampón utilizado para la cromatografíaDEAE y la CM es el mismo tampón, el pH de dicho tampón está en el intervalo de 5,4 a 5,9 y laconductividad está en el intervalo de 1,0 a 1,4 mS/cm, lavar con un volumen de columna de un tampón delavado y a continuación desconectar las columnas DEAE y CM; (e) eliminar por lavado los contaminantes proteicos y las proteínas precipitadas procedentes de la resinaCM de la etapa (d) con un tampón que tiene un pH y una fuerza iónica suficientes para eliminar los contaminantesde la resina sin causar una elución sustancial de la inmunoglobulina G, en donde el tampón tieneun pH entre 5,2 y 5,8; (f) eluir la inmunoglobulina G desde la resina CM de la etapa (e) con un tampón sustancialmente no desna30turalizante que tiene un pH y una fuerza iónica suficientes para causar una elución eficaz de la inmunoglobulinaG, recuperando de esta manera un eluido que contiene inmunoglobulina G; en donde la elución serealiza como una etapa con gradiente de elución desde aproximadamente 125 mM a aproximadamente 350mM de cloruro sódico y un pH en el intervalo de 5,2 a 5,8; (g) realizar una diafiltración/ultrafiltración con el eluido que contiene inmunoglobulina G de la etapa (f) paraconcentrar y/o dializar el eluido hasta que la conductividad de la solución ultrafiltrada se reduzca a un valorinferior a aproximadamente 1,3 mS/cm y en donde el pH se mantiene dentro del intervalo de 4,0 a 6,0, yopcionalmente añadir un agente estabilizante; (h) realizar una etapa de inactivación de virus, y (i) si se desea, someter la solución purificada que contiene IgG a tratamientos adicionales con el fin deadaptarla a una formulación como producto líquido.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP98201909 | 1998-06-09 | ||
US10205598P | 1998-09-28 | 1998-09-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2421736T3 true ES2421736T3 (es) | 2013-09-05 |
Family
ID=44193921
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES10011725.8T Expired - Lifetime ES2527915T3 (es) | 1998-06-09 | 1999-06-09 | Producto de inmunoglobulina G (IgG) líquido |
ES10184829T Expired - Lifetime ES2421736T3 (es) | 1998-06-09 | 1999-06-09 | Procedimiento para la preparación de inmunoglobulinas para administración intravenosa y otros productos inmunoglobulínicos |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES10011725.8T Expired - Lifetime ES2527915T3 (es) | 1998-06-09 | 1999-06-09 | Producto de inmunoglobulina G (IgG) líquido |
Country Status (4)
Country | Link |
---|---|
US (2) | US6281336B1 (es) |
JP (1) | JP4685238B2 (es) |
DK (2) | DK2270044T3 (es) |
ES (2) | ES2527915T3 (es) |
Families Citing this family (72)
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SE0001128D0 (sv) * | 2000-03-30 | 2000-03-30 | Amersham Pharm Biotech Ab | A method of producing IgG |
US6962700B1 (en) * | 2000-09-13 | 2005-11-08 | Atopix Pharmaceuticals Corporation | Method of manufacturing immune globulin |
ES2184594B1 (es) * | 2001-01-17 | 2004-01-01 | Probitas Pharma Sa | Procedimiento para la produccion de gammaglobulina g humana inactivada de virus. |
AU2002257620B2 (en) * | 2001-03-09 | 2007-09-13 | Diapharm Limited | Natural antibodie active against HIV virus |
US6957672B2 (en) * | 2001-07-25 | 2005-10-25 | Imperial Chemical Industries Plc | Method for ensuring that coating compositions have correct color |
WO2003049117A2 (en) * | 2001-12-05 | 2003-06-12 | Cangene Corporation | Immune globulin formulations for the treatment and prevention of an orthopoxvirus infection |
US20030201229A1 (en) * | 2002-02-04 | 2003-10-30 | Martin Siwak | Process for prefiltration of a protein solution |
WO2003066669A2 (en) * | 2002-02-04 | 2003-08-14 | Millipore Corporation | Process for removing protein aggregates and virus from a protein solution |
US20040033228A1 (en) | 2002-08-16 | 2004-02-19 | Hans-Juergen Krause | Formulation of human antibodies for treating TNF-alpha associated disorders |
JPWO2004087761A1 (ja) * | 2003-03-31 | 2006-07-27 | 麒麟麦酒株式会社 | ヒトモノクローナル抗体およびヒトポリクローナル抗体の精製 |
DK1648940T3 (en) | 2003-07-28 | 2016-08-15 | Genentech Inc | Reduction of leaching of protein A during protein A affinity chromatography |
ES2687671T3 (es) | 2004-01-30 | 2018-10-26 | Shire Pharmaceuticals Ireland Limited | Arilsulfatasa A recombinante para reducir los niveles de galatosil sulfátidos en un sujeto |
WO2005072772A1 (en) * | 2004-01-30 | 2005-08-11 | Suomen Punainen Risti Veripalvelu | Pharmaceutical compositions |
US7553938B2 (en) * | 2004-02-27 | 2009-06-30 | Octapharma Ag | Method of providing a purified, virus safe antibody preparation |
WO2005086698A2 (en) * | 2004-03-04 | 2005-09-22 | Mayo Foundation For Medical Education And Research | Methods for altering t cell diversity |
WO2006024497A1 (en) * | 2004-08-30 | 2006-03-09 | Lonza Biologics Plc. | Affinity- plus ion exchange- chromatography for purifying antibodies |
TWI320788B (en) | 2005-05-25 | 2010-02-21 | Hoffmann La Roche | Method for the purification of antibodies |
CA2610839C (en) | 2005-06-14 | 2019-06-25 | Amgen Inc. | Self-buffering protein formulations |
US20070049732A1 (en) * | 2005-09-01 | 2007-03-01 | Zurlo Eugene J | Ultra-high yield intravenous immune globulin preparation |
US8293242B2 (en) * | 2005-09-01 | 2012-10-23 | Plasma Technologies, Llc | Ultra-high yield of alpha-1-anti-trypsin |
US7879332B2 (en) * | 2005-09-01 | 2011-02-01 | Plasma Technologies, Llc | Ultra-high yield intravenous immune globulin preparation |
US7662930B2 (en) * | 2005-12-06 | 2010-02-16 | Amgen Inc. | Polishing steps used in multi-step protein purification processes |
FR2899111B1 (fr) * | 2006-03-31 | 2010-09-03 | Lab Francais Du Fractionnement | Concentre d'immunoglobulines specifiques du chikungunya en tant que medicament. |
CA2644642C (en) * | 2006-04-04 | 2016-01-26 | Zymenex A/S | A process for concentration of a polypeptide |
WO2007146188A2 (en) | 2006-06-07 | 2007-12-21 | The Board Of Trustees Of The Leland Stanford Junior University | Anti-leukocyte recruitment therapy for the treatment of seizures and epilepsy |
US20080031903A1 (en) * | 2006-07-27 | 2008-02-07 | Andrea Gambotto | Method of treating ocular infections |
US7714111B2 (en) * | 2006-09-08 | 2010-05-11 | Wyeth Llc | Arginine derivative wash in protein purification using affinity chromatography |
EP2076287A2 (en) * | 2006-10-12 | 2009-07-08 | Wyeth | Methods and compositions with reduced opalescence |
DE102007001521A1 (de) * | 2007-01-10 | 2008-07-17 | Matthias, Torsten, Dr. | Verwendung von Cohn-Oncley-Fraktionen II und II/III zur Behandlung des systemischen Lupus erythematodes |
AU2013204044B2 (en) * | 2007-11-30 | 2017-08-31 | Abbvie Biotechnology Ltd. | Protein formulations and methods of making same |
US8883146B2 (en) | 2007-11-30 | 2014-11-11 | Abbvie Inc. | Protein formulations and methods of making same |
KR20150080038A (ko) * | 2007-11-30 | 2015-07-08 | 애브비 바이오테크놀로지 리미티드 | 단백질 제형 및 이의 제조방법 |
CA2716521A1 (en) * | 2008-02-29 | 2009-09-11 | Baxter Healthcare S.A. | Anti-amyloid .beta. activity of intravenous immunoglobulin (ivig) in vitro |
MY157239A (en) | 2009-05-27 | 2016-05-13 | Baxalta Inc | A method to produce a highly concentrated immunoglobulin preparation for subcutaneous use |
SI2459291T1 (en) | 2009-07-30 | 2018-06-29 | F. Hoffmann-La Roche Ag | Portable separator for chromatographic columns |
WO2011035282A1 (en) * | 2009-09-21 | 2011-03-24 | Ge Healthcare Bio-Sciences Ab | Dual capture separation |
EP2480561B1 (en) * | 2009-09-23 | 2016-07-13 | E. R. Squibb & Sons, L.L.C. | Cation exchange chromatography |
US8304248B2 (en) | 2009-11-16 | 2012-11-06 | Torres Anthony R | Protein separation via ion-exchange chromatography and associated methods, systems, and devices |
IT1397061B1 (it) | 2009-12-28 | 2012-12-28 | Kedrion Spa | Nuovo processo di purificazione su scala industriale di gammaglobuline da plasma umano per uso industriale. |
RU2467783C2 (ru) * | 2010-07-30 | 2012-11-27 | Закрытое акционерное общество "БиоХимМак СТ" | Способ хроматографического выделения иммуноглобулина |
CA2814781A1 (en) * | 2010-11-01 | 2012-05-10 | Diderik Reinder Kremer | Single unit ion exchange chromatography antibody purification |
EP2671074A1 (en) | 2011-02-02 | 2013-12-11 | F. Hoffmann-La Roche AG | Chromatography column support |
SI3318571T1 (sl) * | 2011-03-16 | 2021-08-31 | F. Hoffmann-La Roche Ag | Ionska izmenjevalna kromatografija z izboljšano selektivnostjo za ločevanje polipeptidnih monomerov, agregatov in fragmentov s spremembo mobilne faze |
FR2974301B1 (fr) | 2011-04-20 | 2013-08-23 | Lab Francais Du Fractionnement | Procede de preparation d'un produit plasmatique deplete en un ou plusieurs facteurs thrombogenes |
IL212911A0 (en) | 2011-05-16 | 2011-07-31 | Omrix Biopharmaceuticals Ltd | Immunoglobulin reduced in thrombogenic contaminants and preparation thereof |
BR112013031906A2 (pt) * | 2011-06-16 | 2016-12-13 | Dsm Ip Assets Bv | unidade única de cromatografia de purificação de anticorpo |
US10336992B2 (en) | 2011-07-08 | 2019-07-02 | Shire Human Genetic Therapies, Inc. | Methods for purification of arylsulfatase A |
WO2013023362A1 (zh) * | 2011-08-16 | 2013-02-21 | 深圳市卫武光明生物制品有限公司 | 静注巨细胞病毒人免疫球蛋白及其制备方法 |
BR112014004445B1 (pt) * | 2011-08-26 | 2022-11-22 | Takeda Pharmaceutical Company Limited | Método para reduzir conteúdo de fator xi e/ou fator xia em uma composição de imunoglobulina |
ES2381828B1 (es) * | 2012-03-20 | 2012-11-16 | Grifols, S.A. | PROCEDIMIENTO PARA OBTENER UNA COMPOSICION DE IgG MEDIANTE TRATAMIENTO TERMICO |
EP2682168A1 (en) | 2012-07-02 | 2014-01-08 | Millipore Corporation | Purification of biological molecules |
WO2014039903A2 (en) | 2012-09-07 | 2014-03-13 | Coherus Biosciences, Inc. | Stable aqueous formulations of adalimumab |
JP6427502B2 (ja) | 2013-01-09 | 2018-11-21 | シャイアー ヒューマン ジェネティック セラピーズ インコーポレイテッド | アリールスルファターゼaの精製方法 |
AU2013203043B2 (en) * | 2013-03-15 | 2016-10-06 | Takeda Pharmaceutical Company Limited | Methods to produce a human plasma-derived igg preparation enriched in brain disease-related natural iggs |
JP6474798B2 (ja) * | 2013-07-01 | 2019-02-27 | ツェー・エス・エル・ベーリング・アクチエンゲゼルシャフト | 方法 |
US20160257754A1 (en) | 2013-10-16 | 2016-09-08 | Momenta Pharmaceuticals Inc. | Sialylated glycoproteins |
US9663553B2 (en) | 2014-01-29 | 2017-05-30 | Hemarus Therapeutics Limited | Integrated process for the production of therapeutics (human albumin, immunoglobulins, clotting factor VIII and clotting factor IX) from human plasma |
FR3018450B1 (fr) * | 2014-03-11 | 2016-04-15 | Lab Francais Du Fractionnement | Procede de preparation de proteines plasmatiques humaines |
CN106414476B (zh) * | 2014-03-11 | 2019-12-31 | 株式会社绿十字控股 | 用于纯化免疫球蛋白的方法 |
US9556253B2 (en) | 2014-12-02 | 2017-01-31 | Hemarus Therapeutics Limited | Process for increased yield of immunoglobulin from human plasma |
KR101657690B1 (ko) * | 2015-06-05 | 2016-09-19 | 주식회사 녹십자홀딩스 | 혈장 유래 b형 간염 사람 면역글로불린 제제의 제조방법 |
PL3135687T3 (pl) * | 2015-08-31 | 2019-09-30 | Instituto Grifols, S.A. | Sposób wytwarzania immunoglobulin |
CN108495860A (zh) * | 2015-09-29 | 2018-09-04 | K·黄 | 一种从组分iii制备静脉注射免疫球蛋白的方法 |
US11229702B1 (en) | 2015-10-28 | 2022-01-25 | Coherus Biosciences, Inc. | High concentration formulations of adalimumab |
WO2017184880A1 (en) | 2016-04-20 | 2017-10-26 | Coherus Biosciences, Inc. | A method of filling a container with no headspace |
EP3275897A1 (en) * | 2016-07-27 | 2018-01-31 | Biotest AG | Process for preparing immunoglobulin compositions |
TWI712612B (zh) * | 2016-09-26 | 2020-12-11 | 西班牙商格里佛機構有限公司 | 製備免疫球蛋白溶液的方法 |
MX2019004580A (es) | 2016-10-21 | 2019-08-12 | Amgen Inc | Formulaciones farmaceuticas y metodos para prepararlas. |
US10259865B2 (en) | 2017-03-15 | 2019-04-16 | Adma Biologics, Inc. | Anti-pneumococcal hyperimmune globulin for the treatment and prevention of pneumococcal infection |
KR20190047376A (ko) * | 2017-10-27 | 2019-05-08 | 주식회사 녹십자 | 개선된 면역글로불린의 정제방법 |
WO2021198220A1 (en) | 2020-03-30 | 2021-10-07 | Allero Therapeutics B.V. | Treatment and prevention of secondary inflammation in patients suffering from a viral infection |
EP4188429A1 (en) * | 2020-07-27 | 2023-06-07 | Martin H. Bluth | Immunoglobulin mediated vaccinations against viral diseases |
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US3869436A (en) * | 1971-06-01 | 1975-03-04 | Statens Bakteriologiska Lab | Method for fractionating plasma proteins using peg and ion-exchangers |
DE2364792A1 (de) * | 1973-01-15 | 1974-07-18 | South African Inventions | Verfahren zum reinigen von gammaglobulin |
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JPS6042336A (ja) | 1983-08-18 | 1985-03-06 | Nippon Seiyaku Kk | 免疫グロブリンの製造方法 |
NZ216094A (en) | 1985-05-15 | 1989-06-28 | Commw Serum Lab Commission | Method for purification of an immunoglobulin |
DE3641115A1 (de) * | 1986-12-02 | 1988-06-16 | Lentia Gmbh | Verfahren zur herstellung eines intravenoes anwendbaren und in fluessiger form stabilen immunglobulins |
JP2547556B2 (ja) * | 1987-02-06 | 1996-10-23 | 株式会社 ミドリ十字 | r−グロブリンの液状製剤 |
US5177194A (en) * | 1990-02-01 | 1993-01-05 | Baxter International, Inc. | Process for purifying immune serum globulins |
DE59009020D1 (de) * | 1990-03-22 | 1995-06-08 | Biotest Pharma Gmbh | Verfahren zur Herstellung eines intravenös verträglichen Immunglobulin-G-Präparates. |
DE4118912C1 (es) * | 1991-06-08 | 1992-07-02 | Biotest Pharma Gmbh, 6072 Dreieich, De | |
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DE59309332D1 (de) * | 1993-12-27 | 1999-03-04 | Rotkreuzstiftung Zentratrallab | Verfahren zur Herstellung eines Konzentrates von Anti-D-Immunoglobulin G und pharmazeutische Zusammensetzung, die dieses enthält |
TW491855B (en) | 1996-08-07 | 2002-06-21 | Csl Ltd | Purification of immunoglobulins |
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-
1999
- 1999-06-09 DK DK10011725.8T patent/DK2270044T3/en active
- 1999-06-09 DK DK10184829.9T patent/DK2272870T3/da active
- 1999-06-09 US US09/328,497 patent/US6281336B1/en not_active Expired - Lifetime
- 1999-06-09 JP JP2000553468A patent/JP4685238B2/ja not_active Expired - Lifetime
- 1999-06-09 ES ES10011725.8T patent/ES2527915T3/es not_active Expired - Lifetime
- 1999-06-09 ES ES10184829T patent/ES2421736T3/es not_active Expired - Lifetime
-
2001
- 2001-07-10 US US09/902,174 patent/US7138120B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP4685238B2 (ja) | 2011-05-18 |
JP2002517516A (ja) | 2002-06-18 |
DK2270044T3 (en) | 2015-01-26 |
DK2272870T3 (da) | 2013-08-05 |
ES2527915T3 (es) | 2015-02-02 |
US20010051708A1 (en) | 2001-12-13 |
US7138120B2 (en) | 2006-11-21 |
US6281336B1 (en) | 2001-08-28 |
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