WO2002072615A1 - Methode de purification de proteines - Google Patents
Methode de purification de proteines Download PDFInfo
- Publication number
- WO2002072615A1 WO2002072615A1 PCT/JP2002/002248 JP0202248W WO02072615A1 WO 2002072615 A1 WO2002072615 A1 WO 2002072615A1 JP 0202248 W JP0202248 W JP 0202248W WO 02072615 A1 WO02072615 A1 WO 02072615A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- antibody
- aqueous solution
- protein
- dna
- conductivity
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/30—Extraction; Separation; Purification by precipitation
-
- 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
Definitions
- the present invention relates to a method for purifying a protein, and more particularly to a method for removing DNA as a contaminant from a sample containing a physiologically active protein such as an antibody.
- DNA is generally obtained by treating an aqueous medium containing a bioactive protein obtained from a host cell with anion exchange chromatography, hydroxyapatite chromatography, or a combination thereof. Has been removed.
- bioactive protein when the bioactive protein is an antibody obtained by using a mammalian cell as a host, protein A or protein G can be used by utilizing the property of protein A or protein G to bind to the Fc chain of IgG. After performing the affinity column chromatography, it is purified by various chromatography methods.
- an antibody-containing aqueous medium obtained from mammalian cell culture is applied to protein A or protein G column chromatography to absorb the antibody into the column,
- the antibody is eluted using a solution (concentration of about 0.1 M, citric acid, pH 3.0-3.5), and the resulting acidic eluate is subjected to ion exchange column chromatography and size exclusion column chromatography. It is applied and refined sequentially.
- these various chromatography steps and their combinations are time-consuming, labor-intensive, costly, complicated, and their effects are not stable.
- the present inventors have conducted intensive studies to solve the above-mentioned problems.As a result, surprisingly, the physiologically active protein-containing sample was made into a low-conductivity acidic aqueous solution, and a buffer was added to adjust the pH to a neutral range.
- the present invention was completed by finding that DNA contaminants can be efficiently removed without performing a complicated one-step chromatography step by raising the concentration and filtering the resulting particles through a filter.
- the present invention provides the following.
- bioactive protein-containing sample is brought into a low-conductivity aqueous solution in a neutral pH range, and 2) The resulting particles are removed.
- a method for removing DNA contaminants in a bioactive protein-containing sample comprising:
- a method for removing DNA contaminants in a sample containing a physiologically active protein comprising:
- a method for removing DNA contaminants in an antibody-containing sample comprising: (4) The method according to the above (2) or (3), wherein the conductivity of the low-conductivity acidic aqueous solution is a molar concentration of 0 to 100 mM.
- the acidic aqueous solution is selected from aqueous solutions of hydrochloric acid, citric acid, and acetic acid;
- the bioactive protein contained in the bioactive protein-containing sample purified by the method of the present invention includes, for example, granulocyte colony stimulating factor (G—CSF), granulocyte macrophage colony stimulating factor (GM—CSF), erythropoietin (EPO ), Hematopoietic factors such as thrombopoietin, interferon ', cytokinin such as IL-1 and IL-6, monoclonal antibodies, tissue plasminogen activator (TPA :), perokinase, serum albumin, blood coagulation Including but not limited to factor VIII, leptin ', insulin, stem cell growth factor (SCF), and the like.
- G—CSF granulocyte colony stimulating factor
- GM—CSF granulocyte macrophage colony stimulating factor
- EPO erythropoietin
- Hematopoietic factors such as thrombopoietin, interferon ', cytokinin such
- a bioactive protein is a protein having substantially the same biological activity as that of a mammal, particularly a human bioactive protein, and includes those derived from nature and those obtained by genetic recombination. Preferred are those obtained by genetic recombination. Proteins obtained by the genetic recombination method have the same amino acid sequence as the natural protein, or have one or more of the amino acid sequences deleted, replaced, or added, and have the biological activity described above. including. Furthermore, the biologically active protein also includes those chemically modified with PEG or the like.
- the origin of the sugar chain is not particularly limited, but a sugar chain added to mammalian cells is preferable.
- Mammalian cells include, for example, Chinese hamster ovary cells (CHO cells), BHK cells, COS cells, human-derived cells, etc. Among them, CHO cells are most preferred.
- EPO may be produced by any method, extracted from human urine by various methods, separated and purified, or obtained by genetic engineering techniques (for example, 6 1- 1 2 2 8 8) to produce Chinese hamster ovary cells (CHO), BHK cells, COS cells, and human-derived cells. For this purpose, those extracted and separated and purified by various methods are used.
- EPO chemically modified with PEG or the like see International Patent Application Publication No. WO 90/12874.
- EPO without sugar chain is also chemically modified with PEG or the like.
- EP ⁇ analogs that have been modified to increase the number of one or more glycosylation sites in the N-linked carbohydrate chain binding site or the 0-linked carbohydrate chain binding site in the amino acid sequence of EPO ( For example, see JP-A-8-151398 and JP-T-8-506023.
- the amount of sugar chains may be increased by increasing the content of sialic acid or the like without changing the number of sugar chain binding sites.
- any G-CSF can be used as long as it is highly purified G-CSF.
- the G-CSF in the present invention may be produced by any method, such as those obtained by culturing a cell line of human tumor cells and extracting and separating and purifying it from various methods, or E. coli by genetic engineering techniques. Bacteria such as yeast, yeast, Chinese hamster ovary (CHO) cells, C127 cells, and cultured cells derived from animals such as COS cells, etc., which are extracted and separated and purified by various methods are used. Preferably, it is produced by a gene recombination method using Escherichia coli, yeast or CH C cells. Most preferably, they are produced by genetic recombination using CHO cells. Furthermore, G-CSF chemically modified with PEG or the like is also included (see International Patent Application Publication No. WO 90/12874). '
- the monoclonal antibody may be produced by any method.
- a monoclonal antibody is basically immunized with a sensitizing antigen according to a usual immunization method using a known technique, and the obtained immunocytes are fused with a known parent cell by a usual cell fusion method, followed by usual screening. It can be prepared by screening monoclonal antibody-producing cells by the method.
- the monoclonal antibody is not limited to the monoclonal antibody produced by the hybridoma, and includes a chimeric antibody artificially modified for the purpose of, for example, reducing the antigenicity against humans. Alternatively, reshaped humanized antibodies can be used in the present invention.
- a reshaped humanized antibody is a humanized anti-IL-16 receptor antibody (hPM-1) (see International Patent Application Publication No. WO92-19759).
- hPM-1 humanized anti-IL-16 receptor antibody
- a humanized anti-HM1.24 antigen monoclonal antibody see International Patent Application Publication No. WO 98-14580
- a humanized antiparathyroid hormone-related peptide antibody anti-PTH1-P antibody
- WO 98-13388 International Patent Application Publication No. WO 98-13388
- humanized anti-tissue factor antibody see International Patent Application Publication No. WO 99-51743 are also preferred antibodies used in the present invention.
- a human antibody produced by a transgenic animal such as a phage display, is also preferable.
- the bioactive protein-containing sample or the antibody-containing sample is preferably a culture medium of a mammalian cell such as a CHO cell containing a bioactive protein or an antibody obtained by culturing, or a part thereof. It is one that has been subjected to certain processing such as purification.
- bioactive protein-containing sample is brought into a low-conductivity aqueous solution in a neutral pH range
- the low-conductivity aqueous solution having a neutral pH range generally means an aqueous solution having a molar concentration of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 30 mM, or an ionic strength of 0 to 30 mM.
- bioactive protein is an antibody, comprising the following steps:
- the DNA contaminants in the antibody-containing sample are removed by a method comprising:
- the sample containing a physiologically active protein is placed in a low-conductivity acidic aqueous solution state, and the low-conductivity is preferably obtained by eluting protein A or protein G affinity chromatography with a low-conductivity acidic aqueous solution.
- Acid aqueous solution The acidic aqueous solution having low conductivity in the present invention is generally an aqueous solution having a molarity of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 30 mM, or an ionic strength of 0 to 0 mM.
- an aqueous solution of 0 to 0.12 or an aqueous solution having a conductivity of 0 to 300 mS / m, preferably 0 to 200 mS / m, more preferably 0 to 150 mS / m, pH 1.5 to 3.9 It preferably refers to an aqueous solution having a pH of 2.0 to 3.9, more preferably a pH of 2.0 to 3.0.
- the acidic aqueous solution may be selected from aqueous solutions of hydrochloric acid, citric acid, acetic acid and the like.
- the type, conductivity, and pH of the low-conductivity acidic aqueous solution to be used vary depending on the type of biologically active protein and antibody to be purified, and those skilled in the art carry out preliminary tests according to the method described in this specification. By doing so, these optimal conditions can be set easily.
- the physiologically active protein-containing sample is brought into a low-conductivity acidic aqueous solution state, and then a buffer is added to the obtained sample to raise the pH to a neutral range.
- a buffer is added to the obtained sample to raise the pH to a neutral range.
- the antibody-containing sample to protein A or protein G affinity chromatography, elute with a low-conductivity acidic aqueous solution, and buffer the resulting eluate.
- the solution is added to raise the pH to a neutral range. Buffer added at this stage, for example, Tris-HCl buffer, and the like phosphate buffer, further Tris solution, Na 2 HP0 4 aqueous solution, but also including aqueous NaOH.
- the neutral region differs depending on the type of physiologically active protein and antibody to be purified, and is generally pH 4 to 8, preferably pH 4.3 to 7.5, and more preferably pH 4.5. ⁇ 7.5.
- the type of buffer solution used and the pH in the neutral region those skilled in the art can easily set the optimal conditions by conducting a preliminary test according to the method described herein.
- the low-conductivity alkaline aqueous solution used in the method of the present invention is usually an aqueous solution having a molar concentration of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 30 mM.
- the pH is 7.5 to 13 (pH varies depending on the bioactive protein to be purified and the type of antibody).
- the solution that has reached the neutral region in the above step produces particles (white turbidity).
- particles white turbidity
- DNA contaminants can be efficiently removed.
- the filter used for filtration for example, a 1.0-0.2 ⁇ Cellulose Acetate Filter System (manufactured by Corning) or TFF can be used, but the filter is not limited thereto.
- a centrifugal separation operation or the like can be considered, and any method capable of efficiently removing the particles may be used, and is not limited to filter filtration.
- this particle is a complex formed by a bioactive protein and DNA. Filtering out the particles results in a small loss of bioactive protein contained in the DNA-bioactive protein complex, but it is a few percent of the total bioactive protein, and is described in the Examples below. Thus, about 90% of the bioactive protein could be recovered.
- the bioactive protein purified by the method of the present invention may be further purified by cation exchange chromatography, anion exchange chromatography, hydroxyapatite chromatography, or a combination thereof, and used in a pharmaceutical preparation. Can be.
- a DNA quantification method measurement is performed by a threshold total DNA quantification method, and a DNA extraction operation is performed prior to the measurement, but is not limited thereto.
- DNA contaminants can be efficiently removed at extremely low DNA concentrations (for example, 22.5 pg / ml) by an extremely simple method, and purification of bioactive proteins, particularly antibodies, can be performed. Became much more effective.
- the cost can be reduced by the method of the present invention, which has a special technical significance.
- Example 1 Investigation of the buffer composition of porcine tin Affinity take mouth chromatography for purification of hPM-1 (humanized anti-IL-16 receptor antibody).
- CM Humanized anti-IL-6 receptor antibody
- CA Cellulose Acetate
- HPLC L-6200 Intelligent Pump (HITACHI) L-4200 UV-VIS Detector (HITACHI)
- h PM-1 quantification method Quantification is performed by reverse-phase HPLC using a PLRP-S column (Polymer Laboratories) by a linear concentration gradient method.
- Threshold total DNA is measured by a DNA quantification method. Perform a DNA extraction procedure (such as DNA extractor kit Kuwako Pure Chemicals) prior to measurement. For the measurement, use a threshold total DNA determination kit (Molecular Devices).
- Turbidity measurement method A measurement sample is supplied to a spectrophotometer U-2000 (HITACHI) to monitor the state of particle formation, and the absorption at 660 nm is measured.
- HITACHI spectrophotometer U-2000
- NaCl was added to the eluate hydrochloric acid in Elution Method 2, and the correlation between the added NaCl concentrations (0 mM, 50 mM, 100 mM) and various factors was determined.
- the Protein A eluted fraction with each addition of NaCl was adjusted to pH 7.0 with a 300 mM Tris solution before filtering, and after adjusting the pH, the sample was 0.22 ⁇ m.
- the sample filtered by m CA Filter was called after filtration. Before and after filtration, the sample after filtration was measured for the recovery of hPM-1 (after filtration only) by the above-described method to determine the amount of residual DNA.
- the hPM-1 recovery rate under each elution condition was measured. As a result, the recovery in elution method 1 was 98.6 ° /. And was good. The recovery rate in the elution method 2 varied from 83.8% to 97.1%, and the recovery rate in the elution method 2 varied from 83.5% to 93.7%. It was presumed to be variation. Therefore, a study with an improved purification scale (elution method 2) confirmed that hPM-1 yield was 90% or more stably. Therefore, even when hydrochloric acid is eluted, h PM The recovery rate of 11 was found to be good.
- Table 2 shows the results of examining the correlation between the added NaCl concentration in the eluate hydrochloric acid and various factors. [Table 2]
- the hPM-1 recovery rate after filtration was 88% for the lOOmM NaCl-added sample, and was 86% for the 50mM NaCl addition and 81% for the OmM NaCl addition in that order.
- the value of OmM NaCl-added kamuna sampnore showed a low value, and in particular, the OmM NaCl-added sample after filtration had an extremely low value of llpg DNA / mg h PM-1.
- Elution fraction adjustment Adjust the pH to various values with a 1M Tris aqueous solution, and remove the DNA by filtration with a 0.2 im Cellulose Acetate (hereinafter abbreviated as CA) filter (examine the conditions in (1) below).
- CA Cellulose Acetate
- the antibody-containing CM was loaded. Subsequently, unbound impurities were washed with 150 mM NaCl in citrate-phosphate buffer pH 7.5, and further washed with citrate-phosphate buffer pH 7.5 in order to lower the conductivity. Elution was performed with an aqueous solution. The elution profile was monitored at A280nm and protein peaks were collected. The following conditions were examined using the protein A elution fraction.
- a sample containing a humanized anti-HM1.24 antigen monoclonal antibody (culture supernatant cultured in CHO cells) was purified by a method using protein A affinity column chromatography under the conditions shown in Table 4 below. .
- the HM1.24 antigen monoclonal antibody was prepared by the method described in International Patent Application Publication No. WO9814580.
- EPO-containing sample composition (1 mM phosphate buffer);
- G-CSF-containing sample cultivated in CHO cells: manufactured by Chugai Pharmaceutical
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- Biochemistry (AREA)
- Biophysics (AREA)
- Genetics & Genomics (AREA)
- Molecular Biology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Pharmacology & Pharmacy (AREA)
- Animal Behavior & Ethology (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Peptides Or Proteins (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP02703958A EP1380589A4 (en) | 2001-03-09 | 2002-03-11 | PROTEIN CLEANING METHOD |
US10/471,374 US7332289B2 (en) | 2001-03-09 | 2002-03-11 | Method of purifying protein |
JP2002571528A JP4391086B2 (ja) | 2001-03-09 | 2002-03-11 | タンパク質精製方法 |
EP16170137.0A EP3088412B1 (en) | 2001-03-09 | 2002-03-11 | Protein purification method |
US12/018,688 US7927815B2 (en) | 2001-03-09 | 2008-01-23 | Protein purification method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001067111 | 2001-03-09 | ||
JP2001-067111 | 2001-03-09 |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10471374 A-371-Of-International | 2002-03-11 | ||
US12/018,688 Division US7927815B2 (en) | 2001-03-09 | 2008-01-23 | Protein purification method |
Publications (1)
Publication Number | Publication Date |
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WO2002072615A1 true WO2002072615A1 (fr) | 2002-09-19 |
Family
ID=18925508
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2002/002248 WO2002072615A1 (fr) | 2001-03-09 | 2002-03-11 | Methode de purification de proteines |
Country Status (5)
Country | Link |
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US (2) | US7332289B2 (ja) |
EP (3) | EP3088412B1 (ja) |
JP (2) | JP4391086B2 (ja) |
ES (1) | ES2869895T3 (ja) |
WO (1) | WO2002072615A1 (ja) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2261230A1 (en) | 2002-09-11 | 2010-12-15 | Chugai Seiyaku Kabushiki Kaisha | Protein purification method |
JP2013534143A (ja) * | 2010-08-20 | 2013-09-02 | ベーリンガー インゲルハイム インターナショナル ゲゼルシャフト ミット ベシュレンクテル ハフツング | 細胞培養物から得られた液体のpH変化によってプロテアーゼを不活性化するための方法 |
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AU2003211991B2 (en) * | 2002-02-14 | 2008-08-21 | Chugai Seiyaku Kabushiki Kaisha | Antibody-containing solution formulations |
GB2401040A (en) * | 2003-04-28 | 2004-11-03 | Chugai Pharmaceutical Co Ltd | Method for treating interleukin-6 related diseases |
US7318925B2 (en) * | 2003-08-08 | 2008-01-15 | Amgen Fremont, Inc. | Methods of use for antibodies against parathyroid hormone |
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WO2007133495A1 (en) * | 2006-05-10 | 2007-11-22 | Human Genome Sciences, Inc. | Mixture for decreasing protein interference |
HUE037633T2 (hu) | 2007-07-09 | 2018-09-28 | Genentech Inc | Diszulfidkötés redukciójának megelõzése polipeptidek rekombináns elõállítása során |
AU2016213727A1 (en) * | 2007-07-09 | 2016-08-25 | Genentech, Inc. | Prevention of disulfide bond reduction during recombinant production of polypeptides |
US7887821B2 (en) * | 2007-12-20 | 2011-02-15 | Alk-Abello A/S | Process for producing an allergen extract |
WO2009080781A1 (en) * | 2007-12-21 | 2009-07-02 | Cytos Biotechnology Ag | Process for clarifying cell homogenates |
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JP2013541594A (ja) | 2010-11-08 | 2013-11-14 | ジェネンテック, インコーポレイテッド | 皮下投与される抗il−6受容体抗体 |
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WO2017147169A1 (en) | 2016-02-22 | 2017-08-31 | Ohio State Innovation Foundation | Chemoprevention using controlled-release formulations of anti-interleukin 6 agents, synthetic vitamin a analogues or metabolites, and estradiol metabolites |
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JP2022527972A (ja) | 2019-04-02 | 2022-06-07 | アンスティチュ ナショナル ドゥ ラ サンテ エ ドゥ ラ ルシェルシュ メディカル | 前悪性病変を有する患者において癌を予測及び予防する方法 |
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2002
- 2002-03-11 ES ES16170137T patent/ES2869895T3/es not_active Expired - Lifetime
- 2002-03-11 EP EP16170137.0A patent/EP3088412B1/en not_active Expired - Lifetime
- 2002-03-11 US US10/471,374 patent/US7332289B2/en not_active Expired - Lifetime
- 2002-03-11 EP EP02703958A patent/EP1380589A4/en not_active Withdrawn
- 2002-03-11 WO PCT/JP2002/002248 patent/WO2002072615A1/ja active Application Filing
- 2002-03-11 JP JP2002571528A patent/JP4391086B2/ja not_active Expired - Lifetime
- 2002-03-11 EP EP10011215A patent/EP2336149A1/en not_active Withdrawn
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2008
- 2008-01-23 US US12/018,688 patent/US7927815B2/en not_active Expired - Fee Related
- 2008-10-06 JP JP2008260150A patent/JP5036679B2/ja not_active Expired - Lifetime
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EP0089218A2 (en) * | 1982-03-15 | 1983-09-21 | NIHON CHEMICAL RESEARCH KABUSHIKI KAISHA also known as JAPAN CHEMICAL RESEARCH CO., LTD | A process for purifying human chorionic gonadotropin |
EP0168506A1 (en) * | 1984-07-07 | 1986-01-22 | Armour Pharma GmbH | Process for preparing gamma globulin suitable for intravenous administration |
WO1991018919A1 (en) * | 1990-05-31 | 1991-12-12 | Schering Corporation | Purification of human interleukin-4 from a secreted escherichia coli mutant |
WO1992007084A1 (en) * | 1990-10-17 | 1992-04-30 | The Wellcome Foundation Limited | Purified cdw52-specific antibodies |
JPH1198997A (ja) * | 1997-08-01 | 1999-04-13 | Toray Ind Inc | インターフェロン−γの製造方法 |
Non-Patent Citations (1)
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See also references of EP1380589A4 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2261230A1 (en) | 2002-09-11 | 2010-12-15 | Chugai Seiyaku Kabushiki Kaisha | Protein purification method |
EP1561756B1 (en) | 2002-09-11 | 2015-12-23 | Chugai Seiyaku Kabushiki Kaisha | Method of purifying protein |
EP2261230B1 (en) * | 2002-09-11 | 2017-05-10 | Chugai Seiyaku Kabushiki Kaisha | Protein purification method |
US10654888B2 (en) | 2002-09-11 | 2020-05-19 | Chugai Seiyaku Kabushiki Kaisha | Method for removing viruses in a physiologically-active protein-containing sample |
JP2013534143A (ja) * | 2010-08-20 | 2013-09-02 | ベーリンガー インゲルハイム インターナショナル ゲゼルシャフト ミット ベシュレンクテル ハフツング | 細胞培養物から得られた液体のpH変化によってプロテアーゼを不活性化するための方法 |
Also Published As
Publication number | Publication date |
---|---|
US20080255342A1 (en) | 2008-10-16 |
US7332289B2 (en) | 2008-02-19 |
EP1380589A1 (en) | 2004-01-14 |
EP3088412A1 (en) | 2016-11-02 |
US7927815B2 (en) | 2011-04-19 |
JP2009062380A (ja) | 2009-03-26 |
ES2869895T3 (es) | 2021-10-26 |
JP5036679B2 (ja) | 2012-09-26 |
EP1380589A4 (en) | 2004-09-01 |
JP4391086B2 (ja) | 2009-12-24 |
US20040138424A1 (en) | 2004-07-15 |
EP2336149A1 (en) | 2011-06-22 |
JPWO2002072615A1 (ja) | 2004-07-02 |
EP3088412B1 (en) | 2021-05-05 |
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