WO2004038010A1 - Método para la obtención de líneas celulares en medio libre de proteína y líneas celulares obtenidas por este método - Google Patents
Método para la obtención de líneas celulares en medio libre de proteína y líneas celulares obtenidas por este método Download PDFInfo
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- WO2004038010A1 WO2004038010A1 PCT/CU2003/000012 CU0300012W WO2004038010A1 WO 2004038010 A1 WO2004038010 A1 WO 2004038010A1 CU 0300012 W CU0300012 W CU 0300012W WO 2004038010 A1 WO2004038010 A1 WO 2004038010A1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
-
- 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
- C07K16/2803—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants against the immunoglobulin superfamily
- C07K16/2809—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against receptors, cell surface antigens or cell surface determinants against the immunoglobulin superfamily against the T-cell receptor (TcR)-CD3 complex
-
- 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
- C07K16/2863—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 growth factors, growth regulators
-
- 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
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/06—Animal cells or tissues; Human cells or tissues
- C12N5/0602—Vertebrate cells
- C12N5/0693—Tumour cells; Cancer cells
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/06—Animal cells or tissues; Human cells or tissues
- C12N5/0602—Vertebrate cells
- C12N5/0693—Tumour cells; Cancer cells
- C12N5/0694—Cells of blood, e.g. leukemia cells, myeloma cells
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P21/00—Preparation of peptides or proteins
-
- 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
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N2500/00—Specific components of cell culture medium
- C12N2500/90—Serum-free medium, which may still contain naturally-sourced components
- C12N2500/95—Protein-free medium and culture conditions
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N2510/00—Genetically modified cells
- C12N2510/02—Cells for production
Definitions
- the present invention relates to biotechnology, specifically with a method to obtain stable cell lines adapted to grow in serum-free and protein-free medium, by a two-stage adaptation process.
- a protein-free medium For culture conditions in a protein-free medium, several techniques have been developed. Thus, specifically defined protein free media have been developed, which allow cell growth under these conditions.
- WO 97/05240 describes the expression of recombinant proteins under conditions of a protein-free medium.
- JP 2696001 describes the use of a protein-free medium for the production of HIV factor in CHO cells by adding a nonionic active tensing agent or cyclodextrin to increase the productivity of host cells. To increase the effectiveness of these additives, the addition of, for example, butyrate and lithium is recommended.
- WO 96/26266 describes the culture of cells in a medium with protein hydrolyzate containing glutamine, whose free amino acid content is less than 15% of the total weight of the protein, and whose peptides have a molecular weight of less than 44 kD.
- a synthetic minimum medium is used as the culture medium for the cells, as the basic medium to which are added in addition to the protein hydrolyzate, bovine fetal serum, gentamicin and mercapto-ethanol. The use of serum containing medium for the production of recombinant blood factors has not been mentioned.
- US 5,393,668 A describes cell growth under conditions of protein-free medium of cells adhered to special synthetic surfaces. To stimulate cell proliferation, CHO cells that overexpress human insulin proliferate on an artificial substrate to which insulin has covalently bound (Ito et al. 1996 PNAS USA. 93: 3598-3601).
- Reiter et al. (1992, Cytotechnology 9: 247-253) describe the immobilization of the first high-density r-CHO cells on carriers in serum-containing medium, and the subsequent perfusion of immobilized cells in the protein-free medium during the production phase , finding a continuous release of the protein in the culture supernatant. There, the cells were maintained for less than 10 generations in the medium without protein.
- the culture of the fermenter consists of a larger population of non-producing cells or cells that have a low expression.
- the present invention provides a strategy for developing stable cell lines adapted to grow in serum and protein free medium. Following the proposed strategy, different clones adapted to grow in a protein-free medium have been obtained.
- Two-stage adaptation of cell lines to growth in a protein-free medium Two-stage adaptation of cell lines to growth in a protein-free medium.
- This procedure encompasses the mammalian cell lines, for which it is not possible to perform a direct procedure of adaptation of the medium supplemented with serum to the medium free of serum and protein.
- the method of the invention includes two steps in adapting the line to the protein-free medium (MLP).
- MLP protein-free medium
- the first stage considered noncritical, the reduction of the protein content of the medium occurs without the loss of cell viability and there is no significant decrease in the doubling time of the population at each step during the reduction of the protein concentration.
- the non-critical stage is generally observed between 5 and 0.5 mg / mL of total protein in the culture medium and this almost shows the same growth rate as in the initial culture medium.
- the previous concentration where there is still cell growth considered as a pre-critical concentration, and from it the protein concentration is slowly decreased until the cells recover viability and The original dubbing time.
- the cells are seeded in at least 3 replicates a density of 1-5 x ios cells / ml in culture medium containing serum and proteins, after
- the entire culture medium is replaced every 48 hours with the fresh medium with 50% of the initial protein concentration; iii.
- the cells are allowed to grow in the medium with 50% of the initial protein concentration until the culture reaches the confluence; iv.
- the cells obtained in the previous step (iii) are seeded in at least 3 replicates at a density of 1-5 x ios cells / ml in the medium containing 50% of the initial protein concentration and after 48 hours of growth, half of the culture supernatant is replaced with fresh protein-free medium, leaving the final protein concentration at
- the entire medium is replaced every 48 hours with fresh medium containing 75% of the pre-critical concentration; x.
- the cells are allowed to grow in the medium containing 75% of the pre-critical protein concentration until the culture reaches the confluence; xi.
- the cell line derived from the previous step is seeded in at least 3 replicates at a density of 2-6 x ios cells / ml in the medium containing 75% of the pre-critical protein concentration and after 48 hours of growth, replaces 25% of the culture supernatant by means fresh protein-free, leaving the final protein concentration at 75% of the previous concentration; xii.
- the entire medium is replaced every 48 hours with fresh medium containing 75% of the previous concentration; xiii.
- the cells are allowed to grow in the medium containing 75% of the previous protein concentration until the culture reaches the confluence; xiv.
- the procedure (xi) is repeated to (xiii) reducing in each cycle the concentration of the protein contained in the medium to 75% of that used in the previous cycle, until reaching a protein concentration such that when the cells are transferred to lower concentrations grow with a similar viability and with the original doubling time, so that the subsequent decrease in protein concentration does not affect the viability or the doubling time.
- the culture medium in which the cells are initially planted comprises between 5% and 10% bovine fetal serum.
- the mammalian cell line that adapts to grow in a protein-free medium is a myeloma, particularly NSO.
- the invention can also be applied for the adaptation of NSO transfected with a sequence encoding a recombinant protein or polypeptide, particularly when the sequence encodes a recombinant antibody or its fragments, so it also includes mammalian cell lines adapted to grow in protein free medium.
- mammalian cell lines that express any of the humanized or chimeric antibodies to EGF receptor I1R3, anti-CD6 TlhT, anti-CD3 T3Q or fragments thereof, adapted to grow by the method of invention in a protein-free medium, as well as the aforementioned antibodies obtained from said lines.
- the lines adapted by the method of the invention grow steadily under conditions of serum and protein free medium for at least 40 generations. Examples of realization: Example i: Adaptation of the I1R3 recombinant cell line to protein-free medium.
- the recombinant I1R3 cell line was obtained by transfecting the NSO myeloma cell line with the vector constructs for the expression of the light and heavy chains of the humanized I1R3 monoclonal antibody that recognizes the human EGF receptor.
- the adaptation of this cell line to a protein-free medium was carried out following the procedure described previously, by means of a reduction of the protein content in two stages.
- the cells were initially cultured in RPMI-1640 medium supplemented with 10% fetal bovine serum (SFB) and then from a protein concentration of 0.15 mg / mL the fetal serum was replaced by the protein-rich supplement, Nutridoma NS (Boheringer Manheinn) added to the basal medium RPMI-1640 (serum free medium).
- the reduction in protein content was made by successive dilutions in PFHM-II medium (Gibco) of the protein content present in the initial medium.
- Example 2 Adaptation of the recombinant TlhT cell line to protein-free medium.
- the recombinant TlhT cell line was obtained by transfecting the NSO myeloma cell line with the constructs of the vectors for the expression of the light and heavy chains of the humanized TlhT monoclonal antibody by the T epitope suppression method and that recognizes the receptor CD6 of human T lymphocytes.
- Example 3 Adaptation of the T3Q recombinant cell line to protein-free medium.
- the T3Q recombinant cell line was obtained by transfection of the NSO myeloma cell line with the constructs of the vectors for the expression of the light and heavy chains of the T3Q monoclonal antibody humanized by the T epitope suppression method and that recognizes the receptor CD3 of human T lymphocytes.
- the adaptation of this cell line to a protein-free medium was carried out following the procedure described in point 2, by means of a two-stage protein content reduction.
- the cells were initially cultured in RPMI-1640 medium supplemented with 10% SFB.
- the reduction in protein content was made by successive dilutions in PFHM-II medium (Gibco) of the protein content present in the initial medium.
- Figure 1 Correlation of the time needed to adapt the I1R3 line to each protein concentration (until viability and doubling time is recovered) with the natural logarithm of the inverse of the protein concentration.
- Critical protein concentration values for the I1R3 cell line are: - 0.32 and 0.11 mg / mL of the total protein concentration.
- Figure 2 Correlation of the total time elapsed since the beginning of the adaptation procedure with the natural logarithm of the inverse of the protein concentration for the I1-R3 cell line. Value of the adaptation speed of this line in the critical phase: - 0.0053 mg / d.
- Figure 3 Correlation of the time needed to adapt the TlhT line to each protein concentration (until viability and doubling time is recovered) with the natural logarithm of the inverse protein concentration.
- the Critical protein concentration values for the TlhT cell line are: - 0.12 and 0.01 mg / mL of the total protein concentration.
- Figure 4 Correlation of the total time elapsed since the start of the adaptation procedure with the natural logarithm of the inverse protein concentration for the TlhT cell line. Value of the speed of adaptation of this line in the critical phase: - 0.0014 mg / d.
- Figure 5 Correlation of the time needed to adapt the T3Q line to each protein concentration (until viability and doubling time is recovered) with the natural logarithm of the inverse protein concentration.
- the critical protein concentration value for the T3Q cell line is: - 0.63 mg / mL of the total protein concentration.
- Figure 6 Correlation of the total time elapsed since the beginning of the adaptation procedure with the natural logarithm of the inverse protein concentration for the T3Q cell line. Value of the adaptation speed of this line in the critical phase: - 0.0172 mg / d.
Abstract
Description
Claims
Priority Applications (17)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2003273727A AU2003273727B2 (en) | 2002-10-23 | 2003-10-22 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
DE60336415T DE60336415D1 (de) | 2002-10-23 | 2003-10-22 | Verfahren zur gewinnung einer rekombinanten säuger- myeloma zelllinie adaptiert an wachstum in serum- und proteinfreien medien |
JP2004545689A JP4674087B2 (ja) | 2002-10-23 | 2003-10-22 | 蛋白質非含有培地中での細胞株の取得方法およびこうして取得された細胞株 |
DK03757654.3T DK1564285T3 (da) | 2002-10-23 | 2003-10-22 | Fremgangsmåde til opnåelse af en rekombinant pattedyr myelomacellelinje tilpasset at gro i serum- og proteinfri medier |
CN2003801036918A CN1714147B (zh) | 2002-10-23 | 2003-10-22 | 无蛋白培养基中获得细胞系的方法以及用此方法获得的细胞系 |
CA2503315A CA2503315C (en) | 2002-10-23 | 2003-10-22 | Procedure for obtaining cell lines in a protein-free media and cell line obtained by the method |
EA200500695A EA007465B1 (ru) | 2002-10-23 | 2003-10-22 | Процедура получения клеточных линий в безбелковых средах и клеточные линии, полученные этим способом |
AT03757654T ATE502103T1 (de) | 2002-10-23 | 2003-10-22 | Verfahren zur gewinnung einer rekombinanten säuger- myeloma zelllinie adaptiert an wachstum in serum- und proteinfreien medien |
BRPI0315565-0A BRPI0315565B1 (pt) | 2002-10-23 | 2003-10-22 | Método para se obter uma linhagem celular de mieloma nso que contém uma sequência que codifica um polipeptídeo recombinante ou uma proteína recombinante adaptada para crescer em meio livre de soro e proteína, e, uso do método |
EP03757654A EP1564285B1 (en) | 2002-10-23 | 2003-10-22 | Method of obtaining a recombinant mammalian myeloma cell lines adapted to growth in serum- and protein-free media |
KR1020057006995A KR101186048B1 (ko) | 2002-10-23 | 2003-10-22 | 무단백질 배지에서 세포주의 수득 방법 및 수득된 세포주 |
US10/532,269 US20060036082A1 (en) | 2002-10-23 | 2003-10-22 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
NZ540171A NZ540171A (en) | 2002-10-23 | 2003-10-22 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
TNP2005000116A TNSN05116A1 (en) | 2002-10-23 | 2005-04-22 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
HR20050760A HRP20050760A2 (en) | 2002-10-23 | 2005-09-02 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
HK06104515.2A HK1084414A1 (en) | 2002-10-23 | 2006-04-13 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
US12/759,208 US20100197011A1 (en) | 2002-10-23 | 2010-04-13 | Method of obtaining cell lines in a protein-free medium and cell lines thus obtained |
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CU20020239A CU23097A1 (es) | 2002-10-23 | 2002-10-23 | Método para la obtención de líneas celulares en medio libre de proteína y líneas celulares obtenidas por este método |
CU239/2002 | 2002-10-23 |
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PCT/CU2003/000012 WO2004038010A1 (es) | 2002-10-23 | 2003-10-22 | Método para la obtención de líneas celulares en medio libre de proteína y líneas celulares obtenidas por este método |
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EP (2) | EP2363418B1 (es) |
JP (1) | JP4674087B2 (es) |
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CN (1) | CN1714147B (es) |
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CA (1) | CA2503315C (es) |
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DK (1) | DK1564285T3 (es) |
EA (1) | EA007465B1 (es) |
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US3886616A (en) * | 1972-12-06 | 1975-06-03 | Fay A Hayes | Hand propelled swimming pool cleaner |
US4275474A (en) * | 1979-04-30 | 1981-06-30 | Woodard Randle C | Vacuum head for swimming pool cleaning system |
US4240174A (en) * | 1979-07-30 | 1980-12-23 | Scott Jeffrey L | Self-contained mobile pool cleaning apparatus |
US4430214A (en) * | 1982-09-15 | 1984-02-07 | Baker Marvin E | Strainer mill for swimming pool pump intake |
US4558479A (en) * | 1984-01-26 | 1985-12-17 | Alopex Industries, Inc. | Pool cleaner |
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