US20020034809A1 - Process for producing a plasma protein-containing medicament - Google Patents

Process for producing a plasma protein-containing medicament Download PDF

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Publication number
US20020034809A1
US20020034809A1 US09/254,288 US25428899A US2002034809A1 US 20020034809 A1 US20020034809 A1 US 20020034809A1 US 25428899 A US25428899 A US 25428899A US 2002034809 A1 US2002034809 A1 US 2002034809A1
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US
United States
Prior art keywords
plasma
protein
citrate
medicament
exchanging
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.)
Abandoned
Application number
US09/254,288
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English (en)
Inventor
Wolfgang Teschner
Yendra Linnau
Sonja Svatos
Herwig Igel
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Oesterreichisches Institut fuer Haemoderivate
Original Assignee
Immuno AG
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Publication date
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Application filed by Immuno AG filed Critical Immuno AG
Assigned to IMMUNO AKTIENGESELLSCHAFT reassignment IMMUNO AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: IGEL, HERWIG, LINNAU, YENDRA, SVATOS, SONJA, TESCHNER, WOLFGANG
Publication of US20020034809A1 publication Critical patent/US20020034809A1/en
Priority to US11/151,295 priority Critical patent/US8709492B2/en
Priority to US14/264,369 priority patent/US20140234292A1/en
Abandoned legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K35/00Medicinal preparations containing materials or reaction products thereof with undetermined constitution
    • A61K35/12Materials from mammals; Compositions comprising non-specified tissues or cells; Compositions comprising non-embryonic stem cells; Genetically modified cells
    • A61K35/14Blood; Artificial blood
    • A61K35/16Blood plasma; Blood serum
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00Medicinal preparations containing peptides
    • A61K38/16Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • A61K38/17Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • A61K38/1703Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from vertebrates
    • A61K38/1709Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from vertebrates from mammals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/76Albumins
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K16/00Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
    • C07K16/06Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies from serum

Definitions

  • the invention relates to a method of preparing a plasma-protein-containing medicament from citrated plasma or from a citrate-containing plasma fraction, the medicament being substantially free from undesired metals.
  • albumin is the main component in plasma. Its therapeutic use has been known for a long time, an administration of albumin being indicated, e.g., in case of an acute loss of blood or plasma or in case of failure of the vasomotoric regulation. Since the osmotic pressure of a 20% (25%) albumin solution is approximately 4 times (5 times) that of normal human serum, the effect of albumin is mainly based on its ability to maintain the osmotic pressure.
  • Human albumin preparations are prepared from human plasma by multiple fractionation, e.g. by a fractionation according to Cohn, or they are prepared by means of recombinant methods. On account of various materials used during its preparation or when the albumin solution is stored in glass containers, aluminum gets into the albumin preparation so that the final content of aluminum in the respective preparations may be quite substantial.
  • Aluminum which constitutes one of the most frequently occurring elements in nature, has recently been increasingly associated with various diseases of the human body, primarily with diseases of the nervous and bone systems. Although the lungs and the gastro-intestinal tract form an efficient barrier for the uptake of aluminum, this barrier is no longer effective in patients receiving intravenous preparations, and the aluminum possibly present in the administered preparations may be taken up without hindrance. Thus, e.g., D. S. Milliner et al. (N. Engl. J. Med. (1985), 312, pp. 165-167) report that some albumin products comprising large amounts of aluminum have lead to diseases of the bones or to encephalitis. Aluminum is also increasingly associated with Alzheimer's disease.
  • the present invention has as its object to provide a novel and simple method of avoiding or reducing, respectively, undesired metals in plasma-protein-containing medicaments, in which both, the undesired metals are removed in the course of the preparation method and a contamination of the finished preparations during storage in metal-containing containers is prevented or reduced, respectively.
  • citrate ion-containing preparations are precipitated and subsequently taken up in a citrate ion free buffer, the new solution may still contain considerable portions of citrate ions. Since most of the fractionation methods in the recovery of pharmaceutical preparations from plasma—to which nearly always citrate is added during the extraction—comprise one or several precipiation steps, the inventive exchange method for citrate ions thus constitutes an interesting possibility for a simple, low-cost and efficient removal of citrate ions which can easily be incorporated into already established procedures.
  • the plasma fraction e.g. a fraction obtained according to the Cohn fractionation
  • albumin e.g., an albumin-containing precipitate from the Cohn fractionation is used.
  • the exchange step thus must be carried out under non-precipitating conditions, since otherwise—as has been mentioned—there will be a risk that the citrate can be removed only insufficiently because of its high affinity to the precipitated protein.
  • the exchange of the citrate will take place at an early time in the preparation method.
  • a medicament comprising one or several factors of coagulation and fibrinolysis, immunoglobulins, glycoproteins and/or albumin, is prepared.
  • fibrinogen, prothrombin, the factors V, VII, VIII, IX, X, XI, XII and XIII optionally in their activated form, von Willebrand factor, but also anticoagulants, such as heparin, heparinoids or cumarin derivatives, or fibrinolytic agents, such as streptokinase, urokinase, pro-urokinase, t-PA or plasmin, can be considered as the coagulation and fibrinolysis factors.
  • the immunoglobulins various preparations comprising immunoglobulins of the classes IgG, IgA, IgM and mixtures thereof, optionally in high titers, may be prepared.
  • glycoprotein orosomucoid may, e.g., be used.
  • a salt of an organic carboxylic acid having 2 to 20 carbon atoms is used for the exchange of the citrate, a caprylate or a tartrate or mixtures thereof being particularly preferred.
  • an organic mono- or dicarboxylic acid is to be understood as a mono- or dicarboxylate, since in any case the exchange of the citrate in solution will always be for the anion of the acid.
  • an organic mono- or dicarboxylic acid having 2 to 4 carbon atoms is used for exchanging the citrate.
  • the method according to the invention has proved particularly suitable for the preparation of plasma-protein-containing medicaments that exhibit excellent properties particularly in respect of their aluminum contamination by being substantially free from any detectable aluminum.
  • exchanging of the citrate must be effected under non-precipitating conditions.
  • the exchange step is effected during a diafiltration, ultrafiltration or during a chromatographic process, since these steps have proved particularly suitable for a simple, low-cost and effecient exchange.
  • the conditions during the exchange step depend on the method used and in particular will be chosen such that the exchange of the citrate and optionally also of citrate-bound metals will be as complete as possible. Therefore, the respective parameter which determine the method, in particular the temperature, the duration of the exchange step and the concentration of the respective mono- or dicarboxylate or mono- or dicarboxylic acid, respectively, have to be optimized.
  • the temperature will preferably be in a range of between 0 and 50° C., more preferred in a range of between 10 and 30° C., most preferred approximately at room temperature.
  • the respective period of time for the exchange is particularly dependent on the ratio of the volume to be exchanged to the membrane surface and on the temperature and preferably is at least 30 minutes, in particular the period of time will be in a range of between 30 minutes and several hours.
  • a parameter like the period of time will just as well depend on the respective exchange volume of the material in question.
  • the exchange volume will be at least 5 times, most preferred at least 30 times that of the starting solution, and the period of time for the exchange will be chosen accordingly.
  • the concentration of mono- or dicarboxylate or of mono- or dicarboxylic acid preferably is in a range of between 0.001 and 10 mol/l, most preferred in a range of between 0.001 and 1 mol/l.
  • Sodium caprylate e.g., is added at a concentration of between 1.0 mmol/l and 1.5 mol/l, preferably in a range of between 1.0 mmol/l and 25 mmol/l.
  • Sodium acetate e.g., is added at a concentration of between 1 mmol/l and 5.5 mol/l, preferably between 50 mmol/l and 1.0 mol/l.
  • the sodium salt of the hexanoic acid e.g., is added at a concentration of between 1.0 mmol/l and 1.0 mol/l, preferably in a range of between 5.0 mmol/l and 0.1 mol/l.
  • Sodium tartrate may be added at a concentration of between 1.0 mmol/l and 1.2 mol/l, preferably between 10.0 mmol/l and 0.2 mol/l.
  • salts of higher acids thus the efficient amounts can already be found in a range of from 0.001 to 0.1 mol/l, while salts of lower acids preferably are added at somewhat higher concentrations.
  • a further parameter which is decisive for the method is the pH of the solution.
  • it is at pH 6 to 8, most preferred at pH 6.5 to 7.5.
  • Beside carboxylate or carboxylic acid may be contained in the solution for increasing the ionic strength thereof.
  • inorganic salts such as, e.g., sodium or potassium salts
  • an at least 4% sodium chloride solution is contained.
  • various buffer salts may be contained.
  • materials for the respective exchange method in particular commercially available materials, such as, e.g., diafiltration membranes, ultrafiltration units, various chromatographic gels, molecular sieves and others may be used. All these materials may be based on organic or inorganic materials; they may be of synthetic of biological origin.
  • a preferred embodiment of the method according to the invention thus relates to a method in which the plasma-protein-containing solution is treated, preferably heat-treated, before and/or after the exchange so as to inactivate possibly present viruses.
  • Common virus inactivation treatments which may be used within the scope of the present method have been described in EP-0 159 311, EP-0 519 901 or in EP-0 674 531.
  • the plasma protein recovered is further subjected to a dialyses against a medium with a low salt content, e.g. water. This may provide an additional stabilizing effect for the plasma protein because of the presence of the mono- or dicarboxylate.
  • the recovery of the plama protein or plasma proteins and the finishing of the medicament preferably should be effected exclusively with citrate-free components so as to avoid the renewed contamination of the preparation with citrate ions which are responsible for a renewed contamination with metal ions in case of longer storage.
  • the method according to the invention has proved quite particularly suitable for removing aluminum ions or for preventing a renewed contamination with aluminum ions, respectively, during storage of the medicament.
  • metal ions from which it is known that they may contaminate plasma-protein-containing medicaments, such as aluminum-like metals, cadmium, zink, lead, iron and others, may efficiently be reduced.
  • an object of the present invention is also a plasma-protein-containing medicament which is obtainable according to the method of the invention and has a content of undesired metal of less than 100 ⁇ g/l, preferably less than 10 ⁇ g/l, in particular less than 200 ng/l, determined, e.g., by atomic absorption spectroscopy, this maximum content not being exceeded even after extended storage, even when stored for more than 5 years.
  • the plasma-protein-containing medicament of the invention may be stored in the most varying containers of the prior art.
  • Such containers may consist of glass, synthetic material, metals or combinations thereof.
  • the containers may also be specially pre-treated; thus, the surface may have been siliconized, e.g.
  • As the glasses both hard glasses and soft glasses (cf. e.g. glasses of the classification USP 23, p. 1781) may be used.
  • the plasma-protein-containing medicament of the invention has a low content of undesired metals when stored in hard glasses; particularly preferred the latter is less than 100 ⁇ g/l, more preferred less than 10 ⁇ g/l, most preferred less than 200 ng/l.
  • a precipitate of Cohn fractionation comprising albumin in a purity of >95% is dissolved 1+2 (w/v; 1kg in 2) in 50 g/l NaCl solution at a neutral pH.
  • the solution is continuously diafiltered with a regenerated cellulose membrane at +4° C. against water. At this, 0.1 mmol caprylate is added per g of protein.
  • Table 1 b) shows the aluminum decrease and the citrate decrease after diafiltration with the addition of 0.1 mmol caprylate. 1 b) with the addition of caprylate Aluminum content Citrate content ⁇ g/g ⁇ mol/g Sample Protein in % Protein in % Before 2.999 100.0 139.5 100.0 diafiltration Diaconcentrate 0.096 3.2 1.1 0.8
  • a precipitate of Cohn fractionation comprising albumin in a purity of >95% is dissolved 1+2 (w/v; 1 kg in 2 l) in 50 g/l NaCl solution at a neutral pH.
  • the solution is continuously diafiltered with a regenerated cellulose membrane at +4° C. against water. At this, 5 mmol acetate is added per g of protein.

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Zoology (AREA)
  • Immunology (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Molecular Biology (AREA)
  • Genetics & Genomics (AREA)
  • Biophysics (AREA)
  • Biochemistry (AREA)
  • Animal Behavior & Ethology (AREA)
  • Engineering & Computer Science (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Epidemiology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Toxicology (AREA)
  • Hematology (AREA)
  • Cell Biology (AREA)
  • Marine Sciences & Fisheries (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Developmental Biology & Embryology (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Virology (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Peptides Or Proteins (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
US09/254,288 1996-09-16 1997-09-10 Process for producing a plasma protein-containing medicament Abandoned US20020034809A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US11/151,295 US8709492B2 (en) 1996-09-16 2005-06-14 Process for producing a plasma protein-containing medicament with reduced concentration of citrate and metals
US14/264,369 US20140234292A1 (en) 1996-09-16 2014-04-29 Process for Producing a Plasma Protein-Containing Medicament

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AT0163396A AT403989B (de) 1996-09-16 1996-09-16 Verfahren zur herstellung eines plasmaprotein-hältigen arzneimittels
ATA1633/96 1996-09-16

Related Parent Applications (1)

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PCT/AT1997/000197 A-371-Of-International WO1998012225A2 (de) 1996-09-16 1997-09-10 Verfarhen zur herstellung eines plasmaprotein-hältigen arzneimittels

Related Child Applications (1)

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US11/151,295 Continuation US8709492B2 (en) 1996-09-16 2005-06-14 Process for producing a plasma protein-containing medicament with reduced concentration of citrate and metals

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US20020034809A1 true US20020034809A1 (en) 2002-03-21

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US09/254,288 Abandoned US20020034809A1 (en) 1996-09-16 1997-09-10 Process for producing a plasma protein-containing medicament
US11/151,295 Expired - Lifetime US8709492B2 (en) 1996-09-16 2005-06-14 Process for producing a plasma protein-containing medicament with reduced concentration of citrate and metals
US14/264,369 Abandoned US20140234292A1 (en) 1996-09-16 2014-04-29 Process for Producing a Plasma Protein-Containing Medicament

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US11/151,295 Expired - Lifetime US8709492B2 (en) 1996-09-16 2005-06-14 Process for producing a plasma protein-containing medicament with reduced concentration of citrate and metals
US14/264,369 Abandoned US20140234292A1 (en) 1996-09-16 2014-04-29 Process for Producing a Plasma Protein-Containing Medicament

Country Status (24)

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US (3) US20020034809A1 (de)
EP (1) EP0927195B1 (de)
JP (1) JP2001500867A (de)
KR (1) KR20000036002A (de)
CN (1) CN1230967A (de)
AR (1) AR009582A1 (de)
AT (2) AT403989B (de)
AU (1) AU732519B2 (de)
BR (1) BR9712044A (de)
CA (1) CA2265936C (de)
CZ (1) CZ91199A3 (de)
DE (1) DE59710700D1 (de)
DK (1) DK0927195T3 (de)
ES (1) ES2206701T3 (de)
HU (1) HUP0002265A3 (de)
ID (1) ID21224A (de)
IL (1) IL128770A0 (de)
IN (1) IN187314B (de)
MX (1) MXPA99002144A (de)
NO (1) NO991198L (de)
PL (1) PL332159A1 (de)
PT (1) PT927195E (de)
SK (1) SK32899A3 (de)
WO (1) WO1998012225A2 (de)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040191231A1 (en) * 1997-11-12 2004-09-30 Friedrich Braun Medicinal product for the promotion of wound healing
WO2004054607A3 (de) * 2002-12-18 2004-10-07 Bio Prod & Bio Eng Ag Stabile therapeutische proteine
US20060160720A1 (en) * 2003-05-23 2006-07-20 Novo Nordisk A/S Protein stabilization in solution

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2103236B1 (es) * 1996-01-30 1998-04-16 Grifols Grupo Sa Albumina humana terapeutica con baja capacidad para la fijacion de aluminio.
AT408946B (de) * 1999-02-18 2002-04-25 Immuno Ag Verwendung von orosomucoid zur herstellung einer pharmazeutischen präparation
JP2003040798A (ja) * 2001-07-26 2003-02-13 Nihon Pharmaceutical Co Ltd 低アルミニウム含有アルブミン製剤およびその製造法
IL162239A0 (en) 2001-12-21 2005-11-20 Novo Nordisk Healthcare Ag Liquid composition of factor vii polypeptides
US7897734B2 (en) 2003-03-26 2011-03-01 Novo Nordisk Healthcare Ag Method for the production of proteins
ES2574581T3 (es) 2003-08-14 2016-06-20 Novo Nordisk Health Care Ag Composición farmacéutica líquida acuosa de polipéptidos de tipo Factor VII
ES2294976B1 (es) * 2007-11-12 2008-12-16 Grifols, S.A. "procedimiento de obtencion de albumina humana de alta eficacia para su uso en terapia de detoxificacion".
RU2624139C2 (ru) 2011-12-05 2017-06-30 Фэктор Байосайенс Инк. Способы и препараты для трансфекции клеток
ES2381828B1 (es) * 2012-03-20 2012-11-16 Grifols, S.A. PROCEDIMIENTO PARA OBTENER UNA COMPOSICION DE IgG MEDIANTE TRATAMIENTO TERMICO
CA3067735A1 (en) 2017-08-17 2019-02-21 Just Biotherapeutics, Inc. Method of purifying glycosylated protein from host cell galectins and other contaminants

Citations (1)

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Publication number Priority date Publication date Assignee Title
US5846930A (en) * 1996-01-30 1998-12-08 Grupo Grifols, S.A. Therapeutic human albumin having a low aluminium binding capacity

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DE384134C (de) * 1921-05-07 1923-10-25 Chemisch Pharmazeutische Werke Verfahren zur Herstellung eines Kamillenextraktes
DE2331854A1 (de) * 1973-06-22 1975-01-16 Greither Salus Haus Dr Otto Verfahren zur herstellung standardisierter arzneimittel aus kamillenblueten
FR2630115B1 (fr) * 1988-04-14 1994-10-28 Merieux Inst Procede de stabilisation des solutions d'albumine humaine et solution obtenue
SE500110C2 (sv) * 1989-06-27 1994-04-18 Kabi Pharmacia Ab Sätt att rena ett protein från därtill bundna flervärda metalljoner
US5250663A (en) * 1990-04-19 1993-10-05 Miles Inc. Preparing essentially monomeric normal human serum albumin
JP2949846B2 (ja) * 1990-11-30 1999-09-20 吉富製薬株式会社 アルブミン製剤の保存方法
US5561115A (en) * 1994-08-10 1996-10-01 Bayer Corporation Low temperature albumin fractionation using sodium caprylate as a partitioning agent
US5744586A (en) * 1996-06-26 1998-04-28 Alpha Therapeutic Corporation Manufacturing process for the production of purified transferrin
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Patent Citations (1)

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US5846930A (en) * 1996-01-30 1998-12-08 Grupo Grifols, S.A. Therapeutic human albumin having a low aluminium binding capacity

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040191231A1 (en) * 1997-11-12 2004-09-30 Friedrich Braun Medicinal product for the promotion of wound healing
US8268362B2 (en) 1997-11-12 2012-09-18 Bio-Products & Bio-Engineering Aktiengesellschaft Medicinal product for the promotion of wound healing
WO2004054607A3 (de) * 2002-12-18 2004-10-07 Bio Prod & Bio Eng Ag Stabile therapeutische proteine
US20060009376A1 (en) * 2002-12-18 2006-01-12 Johann Eibl Stable therapeutic proteins
US20110009324A1 (en) * 2002-12-18 2011-01-13 Johann Eibl Stable Therapeutic Proteins
US20060160720A1 (en) * 2003-05-23 2006-07-20 Novo Nordisk A/S Protein stabilization in solution
US8536127B2 (en) 2003-05-23 2013-09-17 Novo Nordisk Healthcare Ag Protein stabilization in solution

Also Published As

Publication number Publication date
CA2265936C (en) 2008-04-22
AR009582A1 (es) 2000-04-26
IN187314B (de) 2002-03-23
EP0927195A2 (de) 1999-07-07
EP0927195B1 (de) 2003-09-03
WO1998012225A3 (de) 1998-04-23
WO1998012225A2 (de) 1998-03-26
ID21224A (id) 1999-05-06
KR20000036002A (ko) 2000-06-26
US20050249815A1 (en) 2005-11-10
ATA163396A (de) 1997-12-15
BR9712044A (pt) 1999-08-24
NO991198D0 (no) 1999-03-11
AU732519B2 (en) 2001-04-26
CZ91199A3 (cs) 1999-06-16
SK32899A3 (en) 1999-08-06
ES2206701T3 (es) 2004-05-16
CN1230967A (zh) 1999-10-06
ATE248857T1 (de) 2003-09-15
DE59710700D1 (de) 2003-10-09
PT927195E (pt) 2004-01-30
AT403989B (de) 1998-07-27
IL128770A0 (en) 2000-01-31
JP2001500867A (ja) 2001-01-23
CA2265936A1 (en) 1998-03-26
PL332159A1 (en) 1999-08-30
US20140234292A1 (en) 2014-08-21
US8709492B2 (en) 2014-04-29
HUP0002265A3 (en) 2003-01-28
HUP0002265A2 (hu) 2000-11-28
NO991198L (no) 1999-05-14
AU4289997A (en) 1998-04-14
DK0927195T3 (da) 2003-11-24
MXPA99002144A (es) 2005-04-28

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