WO2004024752A1 - タンパク質精製方法 - Google Patents
タンパク質精製方法 Download PDFInfo
- Publication number
- WO2004024752A1 WO2004024752A1 PCT/JP2003/011642 JP0311642W WO2004024752A1 WO 2004024752 A1 WO2004024752 A1 WO 2004024752A1 JP 0311642 W JP0311642 W JP 0311642W WO 2004024752 A1 WO2004024752 A1 WO 2004024752A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- antibody
- protein
- dna
- aqueous solution
- conductivity
- Prior art date
Links
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
-
- 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
-
- 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
- C07K1/16—Extraction; Separation; Purification by chromatography
- C07K1/22—Affinity chromatography or related techniques based upon selective absorption processes
-
- 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
- C07K1/34—Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
- C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
- C07K14/52—Cytokines; Lymphokines; Interferons
- C07K14/53—Colony-stimulating factor [CSF]
- C07K14/535—Granulocyte CSF; Granulocyte-macrophage CSF
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
- C07K16/18—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans
- C07K16/26—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against hormones ; against hormone releasing or inhibiting factors
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
- C07K16/18—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans
- C07K16/28—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants
- C07K16/2866—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants against receptors for cytokines, lymphokines, interferons
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
- C07K16/18—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans
- C07K16/28—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants
- C07K16/2896—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants against molecules with a "CD"-designation, not provided for elsewhere
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
- C07K16/18—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans
- C07K16/28—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants
- C07K16/30—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants from tumour cells
- C07K16/3061—Blood cells
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K2317/00—Immunoglobulins specific features
- C07K2317/20—Immunoglobulins specific features characterized by taxonomic origin
- C07K2317/24—Immunoglobulins specific features characterized by taxonomic origin containing regions, domains or residues from different species, e.g. chimeric, humanized or veneered
Definitions
- the present invention relates to a method for purifying a protein, and more particularly to a method for removing impurities such as 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 bioactive proteins obtained from host cells with anion exchange chromatography, hydroxyapatite chromatography, or a combination thereof. Has been removed.
- bioactive protein when the bioactive protein is an antibody obtained using a mammalian cell as a host, protein A or protein G can be used by utilizing the property that protein A or protein G binds to the Fc chain of IgG. After performing affinity column chromatography, the product is purified by various chromatography methods.
- an antibody obtained from a mammalian cell culture is applied to absorb the antibody onto a column, and then an acidic solution (about 0.1 M concentration of citric acid, PH The antibody is eluted using 3.0-3.5), and the resulting acidic eluate is applied to ion exchange column chromatography and size exclusion column chromatography in that order for purification.
- an acidic solution about 0.1 M concentration of citric acid, PH
- the antibody is eluted using 3.0-3.5
- the resulting acidic eluate is applied to ion exchange column chromatography and size exclusion column chromatography in that order for purification.
- An object of the present invention is to provide a method for purifying a physiologically active protein, particularly an antibody, which can reliably remove impurities such as DNA contaminants and viruses by a simpler method, has a low loss of the biologically active protein, and has a low implementation cost. It is to be. Disclosure of the invention
- the present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, surprisingly, a bioactive protein-containing sample was prepared using a low-conductivity aqueous solution at a pH lower than the isoelectric point of the bioactive protein.
- the present inventors have found that the resulting particles can be efficiently filtered to remove impurities such as DNA contaminants and viruses without performing a complicated chromatographic step by filtering.
- the present invention provides the following.
- bioactive protein-containing sample is converted to a low conductivity aqueous solution of PH below the isoelectric point of the bioactive protein
- a method for removing impurities in a sample containing a physiologically active protein is provided.
- the bioactive protein-containing sample is made into a low-conductivity acidic or alkaline aqueous solution, and a buffer is added to the obtained sample to adjust the pH to a value lower than the isoelectric point of the bioactive protein.
- the method of (1) is made into a low-conductivity acidic or alkaline aqueous solution, and a buffer is added to the obtained sample to adjust the pH to a value lower than the isoelectric point of the bioactive protein.
- the physiologically active protein is an antibody
- the antibody-containing sample is applied to protein A or protein G affinity chromatography, and is eluted with a low-conductivity acidic aqueous solution.
- 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-dicolon stimulating factor (GM-CSF), Hematopoietic factors such as erythropoietin (EPII) and thrombopoietin, interferon, cytokins such as IL-11 and IL-16, monoclonal antibodies, tissue plasminogen activator (TPA;), perokinase, serum albumin But not limited to, blood coagulation factor VIII, lebutin, insulin, stem cell growth factor (SCF) and the like.
- G-CSF granulocyte colony stimulating factor
- GM-CSF granulocyte macrophage-dicolon stimulating factor
- EPII erythropoietin
- thrombopoietin interferon
- cytokins such as IL-11 and IL-16
- TPA tissue
- antibodies such as G-CSF and monoclonal antibodies are preferred, and monoclonal antibodies are more preferred.
- a monoclonal antibody is preferable.
- Antibodies are classified into IgG, IgA, IgE, IgD, and IgM, with IgG antibodies being preferred.
- the bioactive protein is a protein having substantially the same biological activity as a mammal, particularly a human bioactive protein, and includes naturally-occurring proteins and those obtained by genetic recombination, but is preferred. This was obtained by the genetic recombination method. Genetically modified bioactive proteins are produced in bacteria such as Escherichia coli; yeast; cultured cells derived from animals such as Chinese hamster ovary (CHO) cells, C127 cells, and COS cells, and extracted by various methods. Separated and refined products are used. Proteins obtained by genetic recombination include those having the same amino acid sequence as the natural protein, or those having one or more of the amino acid sequences deleted, substituted, or added, and having the biological activity. Furthermore, the biologically active protein 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 Hams evening ovary cells (CHO cells), BHK cells, COS cells, and human-derived cells, among which CHO cells are the most preferred. No.
- EP ⁇ may be produced by any method, extracted from human urine by various methods, separated and purified, genetic engineering techniques (for example, It is produced in bacteria such as Escherichia coli, yeast, Chinese hamster ovary cells (CH B), BHK cells, COS cells, human-derived cells, etc. and extracted and separated by various methods. The purified product is used. Furthermore, EPO chemically modified with PEG or the like is also included (see International Patent Application Publication No. WO 90/12874). Furthermore, 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 at the N- or O-linked carbohydrate chain binding site in the amino acid sequence of EPO (eg, And 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 one produced by any method, such as one obtained by culturing a cell line of human tumor cells and extracting and separating and purifying it from various methods, or E. coli or the like by genetic engineering techniques. Bacteria; List bacteria; produced in animal-derived cultured cells such as Chinese hamster ovary (CHO) cells, C127 cells, and COS cells, and extracted and separated and purified by various methods are used. Preferably, it is produced by a gene recombination method using Escherichia coli, Listeria or CHO cells. Most preferably, it is produced by a CHO cell using a genetic recombination method. 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 immune cells are fused with a known parent cell by a usual cell fusion method to give a usual screen.
- the antibody can be prepared by screening monoclonal antibody-producing cells by the screening method.
- a recombinant antibody produced by using an antibody gene cloned from a hybridoma, inserted into an appropriate vector, introduced into a host, and produced using a genetic recombination technique can be used (see, for example, Carl, AK Borrebaeck, James, W. Larrick, THERAPEUTIC MONOCLONAL ANTIBODIES, Published in the United Kingdom by MACMILLAN PUBLISHERS LTD, 1990).
- cDNA for the variable region (V region) of the antibody is synthesized from the hybridoma mRNA using reverse transcriptase.
- DNA encoding the V region of the desired antibody is obtained, it is ligated to DNA encoding the desired antibody constant region (C region) and incorporated into an expression vector.
- DNA encoding the V region of the antibody may be incorporated into an expression vector containing the DNA of the human C region.
- An expression control region for example, an enhancer, is incorporated into an expression vector so that expression is performed under the control of a promoter.
- host cells can be transformed with this expression vector to express the antibody.
- a recombinant antibody artificially modified for the purpose of, for example, reducing the antigenicity to humans such as a chimeric antibody and a humanized antibody
- modified antibodies can be produced using known methods.
- a chimeric antibody is an antibody consisting of a heavy chain and light chain variable region of a mouse antibody and a heavy chain and light chain constant region of a human antibody, and encodes the variable region of a mouse antibody.
- the DNA can be obtained by ligating the DNA to be ligated to the DNA encoding the constant region of a human antibody, incorporating the DNA into an expression vector, introducing it into a host, and producing it.
- the humanized antibody is also called a reshaped human antibody.
- the complementarity determining region (CDR) of a non-human mammal, such as a mouse antibody, is transplanted into the complementarity determining region of a human antibody.
- the general method of gene recombination is also known. Specifically, a DNA sequence designed to link the CDR of a mouse antibody and the framework region (FR) of a human antibody was constructed so as to have an overlapping portion at the end. Oligonu It is synthesized from nucleotides by the PGR method. The obtained DNA is ligated to DNA encoding the constant region of a human antibody, then inserted into an expression vector, and introduced into a host to produce it (European Patent Application Publication No.
- a preferred example of such a reshaped humanized antibody is a humanized anti-IL-16 receptor antibody (hPM-1) (see International Patent Application Publication No. W ⁇ 92-19795). ). Also, a humanized anti-HM1.24 antigen monoclonal antibody (see International Patent Application Publication No. WO98-145580), a humanized anti-parathyroid hormone-related peptide antibody (anti-PTH rP antibody) (see International Patent Application Publication No. WO98-133388), humanized anti-tissue factor antibody (see International Patent Application Publication No. WO99-51734), etc. Are also preferred antibodies for use in the present invention.
- a method for obtaining a human antibody is known.
- human lymphocytes are sensitized in vitro with a desired antigen or cells expressing the desired antigen, and the sensitized lymphocytes are fused with human myeloma cells, for example, U266, to obtain a desired human antibody having antigen-binding activity.
- a desired human antibody can be obtained by immunizing a transgenic animal having the entire repertoire of human antibody genes with an antigen (International Patent Application Publication Nos. WO 93/12227, WO 92/03918, WO 94 / 02602, WO 94/25585, WO 96/34096, WO 96/33735).
- a technique for obtaining human antibodies by panning using a human antibody library is also known.
- a phage that binds to an antigen can be selected by expressing the variable region of a human antibody as a single-chain antibody (scFv) on the surface of a phage by the phage display method.
- scFv single-chain antibody
- the DNA sequence encoding the variable region of the human antibody that binds to the antigen can be determined.
- a suitable expression vector can be prepared based on the sequence to obtain a human antibody.
- antibodies produced by transgenic animals or the like are also preferred.
- antibodies include antibody fragments such as Fab, (Fab ') 2 , Fc, Fc', and Fd, and reconstituted antibodies such as monovalent or bivalent or more single-chain antibodies (scFV).
- the bioactive protein-containing sample or the antibody-containing sample is preferably a culture medium for mammalian cells such as CH ⁇ cells containing a bioactive protein or antibody obtained by culturing, or a partial culture medium thereof. It is one that has undergone a certain process such as purification.
- bioactive protein-containing sample is converted into a low-conductivity aqueous solution of PH below the isoelectric point of the bioactive protein
- the impurity removed by the method of the present invention may be any substance other than the target protein.
- impurities include DNA contaminants, viruses, protein A (eluted from ram), endotoxin, HCP (cell-derived protein), medium components Hy-Fish (FL), and IGF.
- it is a DNA contaminant or virus.
- the DNA contaminants are DNAs in a sample containing a physiologically active protein, and include DNAs from a host and DNAs from a contaminated virus.
- the virus removed by the method of the present invention is not particularly limited, and any virus may be removed, and includes a DNA virus and an RNA virus.
- the RNA virus include a retrovirus such as X-MuLV, a reovirus such as Reo3, and a parabovirus such as MVM.
- viruses removed by the method of the present invention include, for example, X-MuLV, PRV, Reo3, MVM, VSV, Herpes Simplex, CHV, Sindbis, Mumps, Wax Chair, Measle, Rubella, Flu, Hells Zos Yuichi, Cytomegalo, Para Influenza, EB, HIV, HA, HB, NANB, ATL, ECHO, Valpo, etc.
- the low-conductivity aqueous solution is generally an aqueous solution having a molar concentration of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 3 OmM, or an ionic strength of 0 to 0.2, preferably 0 to 0 mM. 0.12 or an aqueous solution having a conductivity of 0 to 300 mS / m, preferably 0 to 200 mS / m, and more preferably 0 to 150 mS / m.
- the isoelectric point of a bioactive protein is a value of pH at which the charge of the bioactive protein disappears in an aqueous solution.
- the isoelectric point can be measured by a method known to those skilled in the art.For example, the isoelectric point is obtained by performing electrophoresis in a solution having various pH values and determining the pH at which the physiologically active protein does not move. It can be measured by such means.
- the pH below the isoelectric point of the bioactive protein is preferably a pH below the isoelectric point of the bioactive protein.
- the impurity is DNA
- the bioactive protein is positively charged by setting the pH to be equal to or lower than the isoelectric point of the bioactive protein, and that the DNA is further negatively charged.
- the pH for negatively charging is not particularly limited, and a preferable pH below the isoelectric point of the bioactive protein can be used. Since the preferable pH below the isoelectric point of the bioactive protein is considered to be different for each bioactive protein, those skilled in the art will be familiar with known methods (for example, as described in the Examples, a plurality of samples having different pHs). , And measuring the DNA removal rate, protein recovery rate, etc.), it is possible to select a preferable pH below the isoelectric point of the bioactive protein. Such pH is usually pH 2.0 or higher, preferably pH 3.0 or higher, and particularly preferably pH 4.0 or higher.
- ETC electrophoresis titration curve
- a sample containing a physiologically active protein is acidified with low conductivity.
- a buffer is added to the obtained sample to adjust the pH to a value below the isoelectric point of the bioactive protein
- the impurities removed by the method of the present invention are as described above.
- the acidic aqueous solution having a low conductivity refers to an aqueous solution having a molar concentration of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 3 O mM, or an ionic strength of 0 to 0 mM. 2, preferably 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 2.0 to 3.9, Preferably, it refers to an aqueous solution having 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 H of the low-conductivity acidic aqueous solution to be used vary depending on the type of the biologically active protein and the antibody to be purified, and those skilled in the art may carry out preliminary tests according to the method described in this specification. By doing so, these optimum conditions can be easily set.
- the low-conductivity alkaline aqueous solution used in the method of the present invention may be a water solution having a molar concentration of 0 to 100 mM, preferably 0 to 50 mM, more preferably 0 to 30 mM, or an ion solution.
- a bioactive protein-containing sample is converted into a low-conductivity acidic or alkaline aqueous solution, and a buffer is added to the obtained sample to adjust the pH to the isoelectricity of the bioactive protein. Adjust the pH below the point.
- the buffer include Tris-HCl, phosphate, Tris, Na 2 HPO 4 , and NaOH.
- an antibody-containing sample is applied to an affinity mouth chromatography of protein A or protein G and eluted with a low-conductivity acidic aqueous solution. Then, it is possible to adjust the pH to a preferable value below the isoelectric point of the physiologically active protein by adding a buffer to the obtained eluate.
- a buffer is added to the obtained eluate to adjust the pH to a value below the isoelectric point of the physiologically active protein
- the impurities removed by the method of the present invention are as described above.
- Acidic aqueous solution of low conductivity for use in this process Ki is permitted to use those mentioned above, also as a buffer, for example Tris-HCl, phosphate, Tris, and the like Na 2 HP0 4, NaOH it can.
- a solution having a pH below the isoelectric point of the physiologically active protein in the above-described step produces particles (cloudy).
- impurities such as DNA contaminants can be efficiently removed.
- the filter used for the filtration for example, a 1.0-0.2 m Cellulose Acetate Filter System (manufactured by Coming) 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 the method is not limited to filter filtration.
- the present inventors presume that when the impurity is DNA, the particle is a complex formed by a bioactive protein and DNA.
- a protein is positively charged when it has a pH lower than its isoelectric point, while a negatively charged DNA forms a complex of DNA and protein. It is estimated that it will be formed.
- the use of a low-conductivity aqueous solution makes it easier to form complexes. The removal of the particles by filtration removes a small amount of the bioactive protein contained in the DNA-bioactive protein complex, but it is a few percent of the total bioactive protein, and is described in Examples described later. Thus, about 90% of the bioactive protein could be recovered.
- the bioactive protein purified by the method of the present invention can be further purified by cation exchange chromatography, anion exchange chromatography, hydroxyapatite chromatography, or a combination thereof, and used in a pharmaceutical preparation.
- 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.
- TCID 50 tissue culture infective dose (50%); 50% cultivated cell infection amount) using the virus infectivity to detected cells as an index, and RT / Q that can quantify the amount of virus in fractions -Measured by PCR and Q-PCR, but not limited to these.
- Example 1 Investigation of buffer composition of protein A affinity chromatography in purification of hPM-1 (humanized anti-IL-16 receptor antibody)
- h PM-1 antibody humanized anti-IL-6 receptor antibody production CHO cell culture supernatant (hereinafter abbreviated as CM) (Cell centrifugation removed: stored at -80 ° C) It was filtered using Cellulose Acetate (abbreviated as CA) Filter System (CORNING) and used for purification studies.
- CM Cell culture supernatant
- CA Cellulose Acetate
- CORNING Cellulose Acetate
- HPLC L-6200 Intelligent Pump (HITACHI)
- hPM-1 quantification method Quantification is performed by reverse-phase HPLC using a PLRP-S column (Polymer Laboratories) by a linear concentration gradient method.
- DNA content measurement method Threshold total DNA measurement method. Perform a DNA extraction procedure (such as a DNA extractor kit ⁇ Wako Pure Chemicals>) prior to measurement. For the measurement, use a threshold total DNA quantification kit (Molecular Devices). Turbidity measurement method: A spectrophotometer is used to measure the sample to monitor the state of particle formation.
- the sample is subjected to U-2000 (HITACHI), and the absorption at 660 nm is measured.
- NaCl was added to the eluate hydrochloric acid in Elution Method 2, and the correlation between the added NaCl concentration (0 mM, 50 mM, 100 mM) and various factors was determined.
- the Protein A eluted fraction with each NaCl addition was adjusted to pH 7.0 with a 300 mM Tris solution before filtering, and after adjusting the pH, the sample was added to a 0.22 m CA Filter. The filtered sample was taken after filtration. The hPM-1 recovery rate (after filtration only) of the sample before and after filtration was measured using the above measurement method, and the remaining The amount of DNA was measured.
- Table 2 shows the results of examining the correlation between the added NaCl concentration in the eluate hydrochloric acid and various factors.
- the hPM-1 recovery 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 sample before and after filtration showed a low value in the sample with OmM NaCl, and the sample with OmM NaCl after filtration showed a very low value of llpg DNA / mg h PM-1.
- a 0.45 + 0.2 m CA SARTOBRAN P filter (sartorius) was purified by a method using protein A affinity single column chromatography under the following conditions.
- the PTHrP antibody was obtained from International Patent Application Publication No.
- CA filter to remove DNA by filtration (conditions are examined in (1) below).
- 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 single 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. WO 98/14580 (isoelectric point: pH 9.0).
- hPM-1 antibody humanized IL-16 receptor antibody
- CH ⁇ cell culture supernatant (CM) Cell centrifuged: stored at 80 ° C
- X-MuLV Reo 3 MVM was added to each sample. After the addition, each CM was filtered using a 0.45 m filter (pottle top filter: CORNING) and used for purification studies.
- the hPM-1 antibody was prepared in the same manner as in Example 1. Each virus used was obtained from ATCC (American Type Culture Collection).
- the virus-added sample prepared in 5.1 was purified by rProtein Column Chromatography.
- the specific conditions are as follows.
- the eluted fraction obtained in 5.2 was adjusted to pH 3.2 ⁇ 0.1 with lmol / L hydrochloric acid and kept at room temperature 15 ⁇ 5 for 30 minutes or more. Thereafter, each eluted fraction was adjusted to pH 7.2 ⁇ 0.1 with a 300 mmol / LTris solution. 40.0 mL of this was placed in a glass fiber filter (Millipore) (0.2 m PALL) on the primary side, and Bio-inert (0.2 m, PALL) in a PALL filter holder with a diameter of 15 mm. (Attached to an Asystar)) and filtered under a pressure of 0.03 ⁇ 0.01 MPa using a filter unit connected to the secondary side. 5.4 Virus Detection
- TCID 5 o All the collected samples were measured at TCID 5 o.
- RT / Q-PCR and Q-PCR which can quantify the amount of virus in fractions, can be used in addition to TCID 50 , which measures virus infectivity to detected cells. r seven.
- Table 8 virus titer (TCID 5 o method: Logio / mL)
- impurities such as DNA contaminants and viruses can be efficiently removed by an extremely simple method, and the purification of bioactive proteins, particularly antibodies, has become much more effective.
- impurities are D NA is the very low concentrations of D NA concentration (eg 22.5 pg / ml)
- the Huy Ruska value very low values (e.g. TCID 5 o Method 1.0 3 (by the notation of Logio / mL)).
- the cost can be reduced by the method of the present invention, which has a special technical significance.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Biophysics (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Medicinal Chemistry (AREA)
- Molecular Biology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Immunology (AREA)
- Analytical Chemistry (AREA)
- Cell Biology (AREA)
- Endocrinology (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Hematology (AREA)
- Toxicology (AREA)
- Zoology (AREA)
- Gastroenterology & Hepatology (AREA)
- Peptides Or Proteins (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
Abstract
Description
Claims
Priority Applications (14)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/527,455 US8420789B2 (en) | 2002-09-11 | 2003-09-11 | Method for removing DNA contaminants from a protein-containing sample |
JP2004535948A JP5525118B2 (ja) | 2002-09-11 | 2003-09-11 | タンパク質精製方法 |
SI200332458T SI1561756T1 (sl) | 2002-09-11 | 2003-09-11 | Postopek čiščenja proteinov |
EP03795400.5A EP1561756B1 (en) | 2002-09-11 | 2003-09-11 | Method of purifying protein |
ES03795400.5T ES2558303T3 (es) | 2002-09-11 | 2003-09-11 | Método de purificación de proteínas |
KR1020057004158A KR101119448B1 (ko) | 2002-09-11 | 2003-09-11 | 단백질 정제 방법 |
CA2497364A CA2497364C (en) | 2002-09-11 | 2003-09-11 | Protein purification method |
DK03795400.5T DK1561756T3 (en) | 2002-09-11 | 2003-09-11 | PROCEDURE FOR CLEANING PROTEIN. |
AU2003262087A AU2003262087B2 (en) | 2002-09-11 | 2003-09-11 | Protein purification method |
HK06100461.4A HK1077836A1 (en) | 2002-09-11 | 2006-01-11 | Method of purifying protein |
US13/847,691 US8809509B2 (en) | 2002-09-11 | 2013-03-20 | Protein purification method |
US14/329,487 US10654888B2 (en) | 2002-09-11 | 2014-07-11 | Method for removing viruses in a physiologically-active protein-containing sample |
US16/844,063 US20200231624A1 (en) | 2002-09-11 | 2020-04-09 | Protein purification method |
US17/562,536 US20220185843A1 (en) | 2002-09-11 | 2021-12-27 | Protein purification method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002-265609 | 2002-09-11 | ||
JP2002265609 | 2002-09-11 |
Related Child Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10527455 A-371-Of-International | 2003-09-11 | ||
US10/527,455 A-371-Of-International US8420789B2 (en) | 2002-09-11 | 2003-09-11 | Method for removing DNA contaminants from a protein-containing sample |
US13/847,691 Division US8809509B2 (en) | 2002-09-11 | 2013-03-20 | Protein purification method |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004024752A1 true WO2004024752A1 (ja) | 2004-03-25 |
Family
ID=31986593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2003/011642 WO2004024752A1 (ja) | 2002-09-11 | 2003-09-11 | タンパク質精製方法 |
Country Status (13)
Country | Link |
---|---|
US (5) | US8420789B2 (ja) |
EP (3) | EP1561756B1 (ja) |
JP (2) | JP5525118B2 (ja) |
KR (1) | KR101119448B1 (ja) |
CN (1) | CN100522989C (ja) |
AU (1) | AU2003262087B2 (ja) |
CA (1) | CA2497364C (ja) |
DK (2) | DK2261230T3 (ja) |
ES (2) | ES2626268T3 (ja) |
HK (1) | HK1077836A1 (ja) |
HU (1) | HUE027134T2 (ja) |
SI (2) | SI1561756T1 (ja) |
WO (1) | WO2004024752A1 (ja) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011006489A (ja) * | 2002-09-11 | 2011-01-13 | Chugai Pharmaceut Co Ltd | タンパク質精製方法 |
JP2013521323A (ja) * | 2010-03-10 | 2013-06-10 | エフ.ホフマン−ラ ロシュ アーゲー | 免疫グロブリン溶液を精製するための方法 |
US8883146B2 (en) | 2007-11-30 | 2014-11-11 | Abbvie Inc. | Protein formulations and methods of making same |
US8940873B2 (en) | 2007-03-29 | 2015-01-27 | Abbvie Inc. | Crystalline anti-human IL-12 antibodies |
CN105358571A (zh) * | 2013-07-01 | 2016-02-24 | 瑞士杰特贝林生物制品有限公司 | 方法 |
CN105837667A (zh) * | 2016-05-18 | 2016-08-10 | 北京天坛生物制品股份有限公司 | 去除重组汉逊酵母乙肝表面抗原中宿主细胞残留dna的方法 |
Families Citing this family (45)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2382488T3 (es) | 1997-03-21 | 2012-06-08 | Chugai Seiyaku Kabushiki Kaisha | Un agente preventivo o terapéutico para enfermedades mediadas por células t sensibilizadas que comprende un antagonista de il-6 como ingrediente activo |
UA80091C2 (en) | 2001-04-02 | 2007-08-27 | Chugai Pharmaceutical Co Ltd | Remedies for infant chronic arthritis-relating diseases and still's disease which contain an interleukin-6 (il-6) antagonist |
US20050118163A1 (en) * | 2002-02-14 | 2005-06-02 | Hidefumi Mizushima | Antibody-containing solution pharmaceuticals |
GB2401040A (en) * | 2003-04-28 | 2004-11-03 | Chugai Pharmaceutical Co Ltd | Method for treating interleukin-6 related diseases |
EP3736295A1 (en) * | 2004-03-24 | 2020-11-11 | Chugai Seiyaku Kabushiki Kaisha | Subtypes of humanized antibody against interleukin-6 receptor |
WO2007113188A1 (en) * | 2006-03-30 | 2007-10-11 | Novo Nordisk A/S | Two-phase precipitation of proteins |
CA2661872A1 (en) * | 2006-08-28 | 2008-03-06 | Ares Trading S.A. | Process for the purification of fc-fusion proteins |
FI2061803T4 (fi) | 2006-08-28 | 2023-03-14 | Process for the purification of fc-containing proteins | |
CA2660795C (en) | 2006-09-18 | 2014-11-18 | Xencor, Inc. | Optimized antibodies that target hm1.24 |
US20080071067A1 (en) * | 2006-09-20 | 2008-03-20 | Avigenics, Inc. | Methods of purifying proteins from egg white |
KR20190140090A (ko) | 2007-07-09 | 2019-12-18 | 제넨테크, 인크. | 폴리펩티드의 재조합 생산 동안의 디술피드 결합 환원의 방지 |
AU2016213727A1 (en) * | 2007-07-09 | 2016-08-25 | Genentech, Inc. | Prevention of disulfide bond reduction during recombinant production of polypeptides |
NZ602498A (en) * | 2007-11-30 | 2014-08-29 | Abbvie Inc | Protein formulations and methods of making same |
PE20091174A1 (es) | 2007-12-27 | 2009-08-03 | Chugai Pharmaceutical Co Ltd | Formulacion liquida con contenido de alta concentracion de anticuerpo |
EP3604324B1 (en) * | 2008-08-14 | 2024-02-28 | Genentech, Inc. | Methods for removing a contaminant using indigenous protein displacement ion exchange membrane chromatography |
GB0818228D0 (en) * | 2008-10-06 | 2008-11-12 | Avecia Biolog Ltd | Purification process |
WO2010109920A1 (ja) * | 2009-03-27 | 2010-09-30 | 旭化成メディカル株式会社 | 高濃度モノクローナル抗体溶液中のウイルス除去方法 |
SG177577A1 (en) * | 2009-08-07 | 2012-03-29 | Emd Millipore Corp | Methods for purifying a target protein from one or more impurities in a sample |
PL2493922T3 (pl) | 2009-10-26 | 2017-07-31 | F.Hoffmann-La Roche Ag | Sposób wytwarzania glikozylowanych immunoglobulin |
SG10201408384PA (en) | 2009-12-18 | 2015-01-29 | Novartis Ag | Wash solution and method for affinity chromatography |
EP4029881A1 (en) | 2010-11-08 | 2022-07-20 | F. Hoffmann-La Roche AG | Subcutaneously administered anti-il-6 receptor antibody |
EP2682168A1 (en) | 2012-07-02 | 2014-01-08 | Millipore Corporation | Purification of biological molecules |
JP6067889B2 (ja) * | 2013-02-26 | 2017-01-25 | イー・エム・デイー・ミリポア・コーポレイシヨン | 溶液条件を調整することによる活性化炭素を使用したタンパク質混合物からの1種のタンパク質の選択的除去 |
BR112015032960B1 (pt) | 2013-07-04 | 2021-01-05 | F. Hoffmann-La Roche Ag | imunoensaio suprimido por interferência para detectar anticorpos anti-fármaco em amostras de soro |
JP2016533172A (ja) | 2013-10-03 | 2016-10-27 | タケダ ワクチン,インコーポレイテッド | 細胞株からラブドウイルスを検出および除去する方法 |
EP2986307A4 (en) | 2014-01-03 | 2017-04-12 | Bio-rad Laboratories, Inc. | Removal of impurities from protein a eluates |
JP6521351B2 (ja) | 2014-10-14 | 2019-05-29 | テックプロジェクトサービス株式会社 | ウィルス不活化およびサンプリング装置 |
WO2016121701A1 (ja) | 2015-01-26 | 2016-08-04 | 株式会社カネカ | 免疫グロブリンκ鎖可変領域含有タンパク質精製用アフィニティー分離マトリックス |
JP6663360B2 (ja) | 2015-01-26 | 2020-03-11 | 株式会社カネカ | 変異型免疫グロブリンκ鎖可変領域結合性ペプチド |
EP3337818A1 (en) * | 2015-08-21 | 2018-06-27 | H. Hoffnabb-La Roche Ag | Affinity chromatography purification with low conductivity wash buffer |
JP7073253B2 (ja) * | 2015-08-21 | 2022-05-23 | エフ.ホフマン-ラ ロシュ アーゲー | アフィニティークロマトグラフィーにおける宿主細胞タンパク質の低減方法 |
EP3337812B1 (en) | 2015-08-21 | 2021-04-28 | F. Hoffmann-La Roche AG | Method for the reduction of host cell proteins in affinity chromatography |
CN106496302B (zh) * | 2015-09-08 | 2021-12-10 | 三生国健药业(上海)股份有限公司 | 一种用离子交换层析纯化蛋白质的方法 |
CN108367245A (zh) * | 2015-12-09 | 2018-08-03 | 巴斯夫欧洲公司 | 在解吸条件下从发酵固体纯化蛋白质的方法 |
PL3373739T3 (pl) * | 2016-02-19 | 2019-06-28 | Coöperatie Avebe U.A. | Skoagulowane białko w żywności dla ludzi |
US11484591B2 (en) | 2016-02-22 | 2022-11-01 | Ohio State Innovation Foundation | Chemoprevention using controlled-release formulations of anti-interleukin 6 agents, synthetic vitamin A analogues or metabolites, and estradiol metabolites |
WO2017195638A1 (ja) | 2016-05-09 | 2017-11-16 | 株式会社カネカ | 抗体またはκ鎖可変領域含有抗体断片の精製方法 |
US11033496B2 (en) | 2017-03-17 | 2021-06-15 | The Regents Of The University Of Michigan | Nanoparticles for delivery of chemopreventive agents |
EP3727629A1 (en) * | 2017-12-22 | 2020-10-28 | Regeneron Pharmaceuticals, Inc. | System and method for characterizing drug product impurities |
CN107937425A (zh) * | 2017-12-27 | 2018-04-20 | 北京四环生物制药有限公司 | 长效重组人促红素的生产方法 |
US11603527B2 (en) * | 2017-12-27 | 2023-03-14 | Global Life Sciences Solutions Usa Llc | Method and kit for viral vector isolation |
CN110272491B (zh) * | 2018-03-13 | 2023-01-24 | 江苏恒瑞医药股份有限公司 | 一种抗pd-1抗体的纯化工艺 |
CN111902720A (zh) | 2018-03-21 | 2020-11-06 | 沃特世科技公司 | 基于非抗体高亲和力的样品制备、吸附剂、装置和方法 |
US20220177978A1 (en) | 2019-04-02 | 2022-06-09 | INSERM (Institut National de la Santé et de la Recherche Médicale) | Methods of predicting and preventing cancer in patients having premalignant lesions |
WO2022155142A1 (en) * | 2021-01-12 | 2022-07-21 | Repligen Corporation | Offline and inline determination of concentration of metabolites in cell culture fluid |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0610729A1 (de) * | 1993-01-27 | 1994-08-17 | Dr. Karl Thomae GmbH | Verfahren zur Reinigung von Proteinen und Peptiden aus lipidhaltigen Lösungen |
WO1994020525A1 (en) * | 1993-03-05 | 1994-09-15 | Schering Corporation | Purification of human interleukin-10 |
WO1996035710A1 (en) * | 1995-05-08 | 1996-11-14 | Suomen Punainen Risti Veripalvelu | Preparation of immunoglobulin |
WO1997003706A1 (fr) * | 1995-07-14 | 1997-02-06 | Croix-Rouge De Belgique | Procede et installation d'inactivation de contaminants presents dans des produits sanguins |
WO1999019343A1 (en) * | 1997-10-14 | 1999-04-22 | Ortho Diagnostic Systems, Inc. | Viral clearance process |
JP2000319294A (ja) * | 1999-05-11 | 2000-11-21 | Asahi Chem Ind Co Ltd | 生物由来高分子溶液精製方法 |
JP2000351799A (ja) * | 1999-06-08 | 2000-12-19 | Jcr Pharmaceuticals Co Ltd | フィブロネクチン溶液の製造方法 |
EP1225180A2 (en) * | 2001-01-17 | 2002-07-24 | Probitas Pharma, S.A. | Process for the production of virus-inactivated human gammaglobulin G |
EP1247818A2 (en) * | 2001-04-02 | 2002-10-09 | Ortho-Clinical Diagnostics, Inc. | Prion and viral clearance process of immunoglobulin preparations |
Family Cites Families (64)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4124576A (en) | 1976-12-03 | 1978-11-07 | Coval M L | Method of producing intravenously injectable gamma globulin |
JPS58201994A (ja) | 1982-05-21 | 1983-11-25 | Hideaki Hagiwara | 抗原特異的ヒト免疫グロブリンの生産方法 |
JP2648301B2 (ja) | 1983-12-27 | 1997-08-27 | ジエネテイツクス・インスチチユ−ト・インコ−ポレ−テツド | 真核細胞の形質転換のための補助dnaを含むベクター |
FI852545L (fi) | 1984-06-29 | 1985-12-30 | Ortho Diagnostic Systems Inc | Sandwichanalys av antikroppslektin. |
GB8607679D0 (en) | 1986-03-27 | 1986-04-30 | Winter G P | Recombinant dna product |
DE3640513A1 (de) | 1986-11-27 | 1988-06-09 | Biotest Pharma Gmbh | Verfahren zur herstellung eines virussicheren, lagerstabilen und intravenoes vertraeglichen immunglobulin-g-praeparates |
DE3641115A1 (de) | 1986-12-02 | 1988-06-16 | Lentia Gmbh | Verfahren zur herstellung eines intravenoes anwendbaren und in fluessiger form stabilen immunglobulins |
DE3876273T2 (de) * | 1987-04-11 | 1993-05-27 | Ciba Geigy Ag | Isoelektrisches fokussierverfahren sowie einrichtung zur durchfuehrung dieses verfahrens. |
ATE121418T1 (de) * | 1987-10-23 | 1995-05-15 | Schering Corp | Verfahren zur proteinreinigung. |
ES2063783T3 (es) | 1988-06-03 | 1995-01-16 | Chugai Pharmaceutical Co Ltd | Factor de cristalino humano de estimulacion de colonias de granulocitos y procedimiento para su preparacion. |
US5166322A (en) | 1989-04-21 | 1992-11-24 | Genetics Institute | Cysteine added variants of interleukin-3 and chemical modifications thereof |
WO1991005867A1 (en) | 1989-10-13 | 1991-05-02 | Amgen Inc. | Erythropoietin isoforms |
US5177194A (en) | 1990-02-01 | 1993-01-05 | Baxter International, Inc. | Process for purifying immune serum globulins |
GB9015198D0 (en) | 1990-07-10 | 1990-08-29 | Brien Caroline J O | Binding substance |
DK0585287T3 (da) | 1990-07-10 | 2000-04-17 | Cambridge Antibody Tech | Fremgangsmåde til fremstilling af specifikke bindingsparelementer |
KR100272077B1 (ko) | 1990-08-29 | 2000-11-15 | 젠팜인터내셔날,인코포레이티드 | 이종 항체를 생산할 수 있는 전이유전자를 가진 인간이외의 동물 |
GB9022547D0 (en) | 1990-10-17 | 1990-11-28 | Wellcome Found | Purified immunoglobulin |
US5110910A (en) | 1991-03-25 | 1992-05-05 | Miles Inc. | Virucidal euglobulin precipitation |
AU668349B2 (en) * | 1991-04-25 | 1996-05-02 | Chugai Seiyaku Kabushiki Kaisha | Reconstituted human antibody against human interleukin 6 receptor |
WO1993006213A1 (en) | 1991-09-23 | 1993-04-01 | Medical Research Council | Production of chimeric antibodies - a combinatorial approach |
ES2341666T3 (es) | 1991-12-02 | 2010-06-24 | Medimmune Limited | Produccion de autoanticuerpos de repertorios de segmentos de anticue rpos expresados en la superficie de fagos. |
CA2124967C (en) | 1991-12-17 | 2008-04-08 | Nils Lonberg | Transgenic non-human animals capable of producing heterologous antibodies |
CA2131151A1 (en) | 1992-03-24 | 1994-09-30 | Kevin S. Johnson | Methods for producing members of specific binding pairs |
JPH07509137A (ja) | 1992-07-24 | 1995-10-12 | セル ジェネシス,インク. | 異種抗体の生産 |
US5840297A (en) | 1993-03-19 | 1998-11-24 | Johns Hopkins University | Vaccine comprising anti-idiotypic antibody to chlamydia GLXA and process |
EP0754225A4 (en) | 1993-04-26 | 2001-01-31 | Genpharm Int | HETEROLOGIC ANTIBODY-PRODUCING TRANSGENIC NON-HUMAN ANIMALS |
GB9313509D0 (en) | 1993-06-30 | 1993-08-11 | Medical Res Council | Chemisynthetic libraries |
IL110669A (en) | 1993-08-17 | 2008-11-26 | Kirin Amgen Inc | Erythropoietin analogs |
JPH09506508A (ja) | 1993-12-03 | 1997-06-30 | メディカル リサーチ カウンシル | 組換え結合タンパク質およびペプチド |
US5429746A (en) * | 1994-02-22 | 1995-07-04 | Smith Kline Beecham Corporation | Antibody purification |
US8017121B2 (en) | 1994-06-30 | 2011-09-13 | Chugai Seiyaku Kabushika Kaisha | Chronic rheumatoid arthritis therapy containing IL-6 antagonist as effective component |
JPH089902A (ja) | 1994-07-04 | 1996-01-16 | Shiseido Co Ltd | 低アレルギー加工食品 |
WO1996002576A1 (fr) | 1994-07-13 | 1996-02-01 | Chugai Seiyaku Kabushiki Kaisha | Anticorps humain reconstitue contre l'interleukine-8 humaine |
JP3630453B2 (ja) | 1994-09-30 | 2005-03-16 | 中外製薬株式会社 | Il−6レセプター抗体を有効成分とする未熟型骨髄腫細胞治療剤 |
KR20050085971A (ko) | 1995-04-27 | 2005-08-29 | 아브게닉스, 인크. | 면역화된 제노마우스 유래의 인간 항체 |
AU2466895A (en) | 1995-04-28 | 1996-11-18 | Abgenix, Inc. | Human antibodies derived from immunized xenomice |
JP3471195B2 (ja) | 1996-06-27 | 2003-11-25 | 中外製薬株式会社 | ナイトロジェンマスタード系抗癌剤と組合わせて使用するための骨髄腫治療剤 |
TW491855B (en) | 1996-08-07 | 2002-06-21 | Csl Ltd | Purification of immunoglobulins |
EP0962467A4 (en) | 1996-09-26 | 2002-10-30 | Chugai Pharmaceutical Co Ltd | ANTIBODIES AGAINST HUMAN PARATHORMON RELATED PEPTIDES |
UA76934C2 (en) | 1996-10-04 | 2006-10-16 | Chugai Pharmaceutical Co Ltd | Reconstructed human anti-hm 1.24 antibody, coding dna, vector, host cell, method for production of reconstructed human antibody, pharmaceutical composition and drug for treating myeloma containing reconstructed human anti-hm 1.24 antibody |
DE69739673D1 (de) | 1996-11-27 | 2009-12-31 | Genentech Inc | Affinitätsreinigung von Polypeptid-Proteinen auf einer Protein A Matrix |
US5886154A (en) * | 1997-06-20 | 1999-03-23 | Lebing; Wytold R. | Chromatographic method for high yield purification and viral inactivation of antibodies |
US5972613A (en) * | 1997-12-09 | 1999-10-26 | The Perkin-Elmer Corporation | Methods of nucleic acid isolation |
UA64742C2 (uk) | 1997-12-24 | 2004-03-15 | Альфа Терапевтик Корпорейшн | СПОСІБ ОДЕРЖАННЯ РОЗЧИНУ <font face="Symbol">g</font>-ГЛОБУЛІНУ, ПРИЗНАЧЕНОГО ДЛЯ ВНУТРІШНЬОВЕННОГО ВВЕДЕННЯ, І ПРОДУКТ, ЩО ОДЕРЖУЄТЬСЯ У ЦЕЙ СПОСІБ (ВАРІАНТИ) |
IL138801A0 (en) | 1998-04-03 | 2001-10-31 | Chugai Pharmaceutical Co Ltd | Humanized antibody against human tissue factor and process for the preparation thereof |
KR100501263B1 (ko) | 1998-06-09 | 2005-07-18 | 스태튼스 세룸 인스티튜트 | 정맥 주사용 면역글로불린의 제조 방법 및 그 외의 면역글로불린 제품 |
CA2362533A1 (en) | 1999-02-22 | 2000-08-31 | Variagenics, Inc. | Gene sequence variations with utility in determining the treatment of disease |
US6355243B1 (en) | 1999-11-13 | 2002-03-12 | Bayer Corporation | Method of thrombolysis by local delivery of active plasmin |
ES2477996T3 (es) | 2000-08-11 | 2014-07-18 | Chugai Seiyaku Kabushiki Kaisha | Preparaciones estabilizadas que contienen un anticuerpo |
JP2002265909A (ja) | 2001-03-07 | 2002-09-18 | Nippon Synthetic Chem Ind Co Ltd:The | 非水分散系感圧接着剤 |
EP3088412B1 (en) | 2001-03-09 | 2021-05-05 | Chugai Seiyaku Kabushiki Kaisha | Protein purification method |
JP4187941B2 (ja) | 2001-03-14 | 2008-11-26 | リンテック株式会社 | ホウ素含有ポリオルガノシルセスキオキサン及び接着剤組成物 |
ATE464068T1 (de) | 2001-06-26 | 2010-04-15 | Amgen Fremont Inc | Antikörper gegen opgl |
US7122641B2 (en) * | 2001-12-21 | 2006-10-17 | Immunex Corporation | Methods for purifying protein |
US20050118163A1 (en) | 2002-02-14 | 2005-06-02 | Hidefumi Mizushima | Antibody-containing solution pharmaceuticals |
ES2626268T3 (es) | 2002-09-11 | 2017-07-24 | Chugai Seiyaku Kabushiki Kaisha | Método de purificación de proteínas |
WO2006029385A2 (en) | 2004-09-08 | 2006-03-16 | Chelsea Therapeutics, Inc. | Quinazoline derivatives as metabolically inert antifolate compounds. |
JP2010524479A (ja) | 2007-05-02 | 2010-07-22 | エフ.ホフマン−ラ ロシュ アーゲー | タンパク質を安定化する方法 |
JP5504579B2 (ja) | 2008-05-12 | 2014-05-28 | 積水ハウス株式会社 | 住宅の床着脱構造及び住宅の改装方法 |
US8992920B2 (en) | 2008-11-25 | 2015-03-31 | Alderbio Holdings Llc | Anti-IL-6 antibodies for the treatment of arthritis |
NZ599456A (en) | 2009-10-26 | 2014-06-27 | Nestec Sa | Assays for the detection of anti-tnf drugs and autoantibodies |
US8623377B2 (en) | 2011-06-29 | 2014-01-07 | University Of Maryland, Baltimore | Joint-homing peptides and uses thereof |
CN110074968B (zh) | 2013-03-11 | 2021-12-21 | Sio2医药产品公司 | 涂布包装材料 |
CA2922732A1 (en) | 2013-09-03 | 2015-03-12 | L. Douglas GRAHAM | Treatment methods for rheumatoid arthritis |
-
2003
- 2003-09-11 ES ES10180577.8T patent/ES2626268T3/es not_active Expired - Lifetime
- 2003-09-11 CA CA2497364A patent/CA2497364C/en not_active Expired - Lifetime
- 2003-09-11 KR KR1020057004158A patent/KR101119448B1/ko active Protection Beyond IP Right Term
- 2003-09-11 US US10/527,455 patent/US8420789B2/en not_active Expired - Lifetime
- 2003-09-11 CN CNB038216825A patent/CN100522989C/zh not_active Expired - Lifetime
- 2003-09-11 EP EP03795400.5A patent/EP1561756B1/en not_active Revoked
- 2003-09-11 WO PCT/JP2003/011642 patent/WO2004024752A1/ja active Application Filing
- 2003-09-11 HU HUE03795400A patent/HUE027134T2/en unknown
- 2003-09-11 ES ES03795400.5T patent/ES2558303T3/es not_active Expired - Lifetime
- 2003-09-11 SI SI200332458T patent/SI1561756T1/sl unknown
- 2003-09-11 SI SI200332529T patent/SI2261230T1/sl unknown
- 2003-09-11 EP EP17164053.5A patent/EP3225625A1/en active Pending
- 2003-09-11 DK DK10180577.8T patent/DK2261230T3/en active
- 2003-09-11 JP JP2004535948A patent/JP5525118B2/ja not_active Expired - Lifetime
- 2003-09-11 AU AU2003262087A patent/AU2003262087B2/en not_active Expired
- 2003-09-11 DK DK03795400.5T patent/DK1561756T3/en active
- 2003-09-11 EP EP10180577.8A patent/EP2261230B1/en not_active Revoked
-
2006
- 2006-01-11 HK HK06100461.4A patent/HK1077836A1/xx not_active IP Right Cessation
-
2010
- 2010-10-14 JP JP2010231719A patent/JP5687469B2/ja not_active Expired - Lifetime
-
2013
- 2013-03-20 US US13/847,691 patent/US8809509B2/en not_active Expired - Lifetime
-
2014
- 2014-07-11 US US14/329,487 patent/US10654888B2/en not_active Expired - Fee Related
-
2020
- 2020-04-09 US US16/844,063 patent/US20200231624A1/en not_active Abandoned
-
2021
- 2021-12-27 US US17/562,536 patent/US20220185843A1/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0610729A1 (de) * | 1993-01-27 | 1994-08-17 | Dr. Karl Thomae GmbH | Verfahren zur Reinigung von Proteinen und Peptiden aus lipidhaltigen Lösungen |
WO1994020525A1 (en) * | 1993-03-05 | 1994-09-15 | Schering Corporation | Purification of human interleukin-10 |
WO1996035710A1 (en) * | 1995-05-08 | 1996-11-14 | Suomen Punainen Risti Veripalvelu | Preparation of immunoglobulin |
WO1997003706A1 (fr) * | 1995-07-14 | 1997-02-06 | Croix-Rouge De Belgique | Procede et installation d'inactivation de contaminants presents dans des produits sanguins |
WO1999019343A1 (en) * | 1997-10-14 | 1999-04-22 | Ortho Diagnostic Systems, Inc. | Viral clearance process |
JP2000319294A (ja) * | 1999-05-11 | 2000-11-21 | Asahi Chem Ind Co Ltd | 生物由来高分子溶液精製方法 |
JP2000351799A (ja) * | 1999-06-08 | 2000-12-19 | Jcr Pharmaceuticals Co Ltd | フィブロネクチン溶液の製造方法 |
EP1225180A2 (en) * | 2001-01-17 | 2002-07-24 | Probitas Pharma, S.A. | Process for the production of virus-inactivated human gammaglobulin G |
EP1247818A2 (en) * | 2001-04-02 | 2002-10-09 | Ortho-Clinical Diagnostics, Inc. | Prion and viral clearance process of immunoglobulin preparations |
Non-Patent Citations (1)
Title |
---|
See also references of EP1561756A1 * |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2261230B1 (en) | 2002-09-11 | 2017-05-10 | Chugai Seiyaku Kabushiki Kaisha | Protein purification method |
JP2011006489A (ja) * | 2002-09-11 | 2011-01-13 | Chugai Pharmaceut Co Ltd | タンパク質精製方法 |
EP1561756B1 (en) | 2002-09-11 | 2015-12-23 | Chugai Seiyaku Kabushiki Kaisha | Method of purifying protein |
US8940873B2 (en) | 2007-03-29 | 2015-01-27 | Abbvie Inc. | Crystalline anti-human IL-12 antibodies |
US11191834B2 (en) | 2007-11-30 | 2021-12-07 | 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 |
US9085619B2 (en) | 2007-11-30 | 2015-07-21 | Abbvie Biotechnology Ltd. | Anti-TNF antibody formulations |
US11167030B2 (en) | 2007-11-30 | 2021-11-09 | Abbvie Biotechnology Ltd | Protein formulations and methods of making same |
JP2015213511A (ja) * | 2010-03-10 | 2015-12-03 | エフ.ホフマン−ラ ロシュ アーゲーF. Hoffmann−La Roche Aktiengesellschaft | 免疫グロブリン溶液を精製するための方法 |
KR101555740B1 (ko) | 2010-03-10 | 2015-09-25 | 에프. 호프만-라 로슈 아게 | 면역글로불린 용액 정제 방법 |
JP2013521323A (ja) * | 2010-03-10 | 2013-06-10 | エフ.ホフマン−ラ ロシュ アーゲー | 免疫グロブリン溶液を精製するための方法 |
CN105358571A (zh) * | 2013-07-01 | 2016-02-24 | 瑞士杰特贝林生物制品有限公司 | 方法 |
CN105358571B (zh) * | 2013-07-01 | 2019-03-05 | 瑞士杰特贝林生物制品有限公司 | 方法 |
CN105837667A (zh) * | 2016-05-18 | 2016-08-10 | 北京天坛生物制品股份有限公司 | 去除重组汉逊酵母乙肝表面抗原中宿主细胞残留dna的方法 |
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2004024752A1 (ja) | タンパク質精製方法 | |
JP5036679B2 (ja) | タンパク質精製方法 | |
JP6722455B2 (ja) | 等電点の低い抗体の精製方法 | |
US20240158437A1 (en) | Process of purification of protein | |
JP2017507132A (ja) | 抗体プロセス | |
CN111704670B (zh) | 重组抗RANKL抗体IgG2型的二硫键异构体及其纯化方法 | |
US20240239838A1 (en) | Process of purification of protein | |
US20240092883A1 (en) | Methods of purifying ranibizumab or a ranibizumab variant |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2004535948 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003262087 Country of ref document: AU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2497364 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020057004158 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 20038216825 Country of ref document: CN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003795400 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1020057004158 Country of ref document: KR |
|
WWP | Wipo information: published in national office |
Ref document number: 2003795400 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2006142549 Country of ref document: US Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10527455 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 10527455 Country of ref document: US |