Patent Application
20230203554
The present disclosure relates to a process for reducing unwanted culture byproducts in a glutamine-free cell culture medium, a culture process for producing a target protein of interest, and a culture process for producing a target protein.
Animal cell culture in the biotechnology field has been considered to be an important technology for producing high value-added substances, such as new antibody production and vaccine development and production. Studies on cell metabolism and regulation methods also play an important role in raising the economic value of such substances. Thus, intensive research has been conducted on the components of media needed for culturing cells, and much effort has been made to increase productivity with respect to a target protein by adding various nutrients to the media components.
To increase the production efficiency of proteins including antibodies, it is important to improve cell viability. However, there are factors that limit the improvement of protein productivity. Among these factors, the most important factor is waste products or by-products generated during cell culture. These substances, which are unnecessarily produced in a cell metabolism process, may be toxic to cells or inhibit cell growth and metabolism in many different ways. The most representative example of these by-products is ammonia. Generally, there are many reports of cytotoxicity of 2 mM to 10 mM ammonia in a cell culture medium. For example, it is known that, in Chinese hamster ovary (CHO) cells, 8 mM ammonia inhibited cell growth by 50% (Kurano N, Leist C, et al., 1990, J. Biotechnol. 15:113-128), and inhibits glycosylation of proteins by directly inhibiting the expression of major enzymes involved in glycosylation (Chen P, and Harcum S W., 2006, Metab. Eng., 8:123-132). Accordingly, ammonia may not only simply cause cytotoxicity, but also cause even structural and functional defects of a target protein to be produced. In addition, ammonia may also decrease the functions of other components involved in metabolism, and exhibit unnecessary functions, such as the release of essential metabolites from cells. However, it is difficult to easily remove ammonia from a cell culture medium, and thus the concentration of ammonia in a medium may be a more crucial factor in the production of a target protein.
Therefore, there is a need to develop a method of suppressing or reducing the generation of by-products, especially ammonia, in animal cell culture, while also maintaining or enhancing the productivity of a target protein.
Provided is a culture process for reducing unwanted culture by-products when a target protein is produced in a glutamine-free cell culture medium.
Provided is a culture process for producing a target protein in a glutamine-free cell culture medium.
According to an aspect of an embodiment, an improved culture process for reducing an unwanted culture by-product when a target protein is produced in a glutamine-free cell culture medium includes culturing mammalian cell in a glutamine-free cell culture medium under conditions allowing survival or proliferation of the cell, wherein the cell culture medium includes hypoxanthine at a concentration of about 20 μM to about 1,000 μM and thymidine at a concentration of about 2 μM to about 1,000 μM.
The term “glutamine (Gln or Q)” as used herein refers to the amino acid L-glutamine.
The term “cell culture medium” as used herein refers to a solution containing nutrients needed for culturing an animal eukaryotic cell. The term “cell culture medium” as used herein may be used interchangeably with the term “culture medium,” “medium,” or “growth medium.” The medium includes a commercialized or prepared medium used in culturing the animal cell.
The term “glutamine-free cell culture medium” as used herein refers to a cell culture medium not containing glutamine. The glutamine-free cell culture medium also includes a cell culture medium that does not substantially contain glutamine.
The cell culture medium includes hypoxanthine at a concentration of about 20 μM to about 1,000 μM and thymidine at a concentration of about 2 μM to about 1,000 μM. Hypoxanthine is a purine derivative and is a compound having the molecular formula C5H4N4O. The hypoxanthin may be natural or synthesized hypoxanthin. The thymidine is a compound of pyrimidine deoxynucleoside. Thymidine is also referred to as deoxythymidine, deoxyribosylthymine, or thymine deoxyriboside. The thymidine may be natural or synthesized thymidine.
The cell culture medium may include hypoxanthin at a concentration of about 50 μM to about 1,000 μM. For example, the cell culture medium may include hypoxanthin at a concentration of about 100 μM to about 1,000 μM, between greater than about 100 μM and about 1,000 μM or less, about 100 μM to about 900 μM, about 100 μM to about 800 μM, about 100 μM to about 700 μM, about 100 μM to about 600 μM, about 100 μM to about 500 μM, about 100 μM to about 400 μM, about 100 μM to about 300 μM, about 100 μM to about 200 μM, about 110 μM to about 950 μM, about 120 μM to about 900 μM, about 130 μM to about 850 μM, about 140 μM to about 800 μM, about 150 μM to about 750 μM, about 150 μM to about 700 μM, about 150 μM to about 650 μM, about 150 μM to about 600 μM, about 150 μM to about 550 μM, about 150 μM to about 500 μM, about 150 μM to about 450 μM, about 150 μM to about 350 μM, about 150 μM to about 300 μM, about 150 μM to about 250 μM, about 175 μM to about 225 μM, or about 200 μM.
The cell culture medium may include thymidine at a concentration of about 2 μM to about 500 μM. For example, the cell culture medium may include thymidine at a concentration of about 6 μM to about 500 μM, about 9 μM to about 500 μM, about 12 μM to about 500 μM, about 16 μM to about 500 μM, between greater than 16 μM and about 500 μM or less, about 18 μM to about 450 μM, about 18 μM to about 400 μM, about 18 μM to about 350 μM, about 18 μM to about 300 μM, about 20 μM to about 300 μM, about 20 μM to about 250 μM, about 20 μM to about 200 μM, about 20 μM to about 150 μM, about 25 μM to about 200 μM, about 25 μM to about 150 μM, about 25 μM to about 100 μM, about 25 μM to about 75 μM, about 25 μM to about 50 μM, about 25 μM to about 40 μM, about 30 μM to about 40 μM, about 30 μM to about 35 μM, or about 32 μM.
The term “culture by-product” as used herein refers to a substance that is produced in the cell and secreted to a medium when the animal cell is cultured. The culture by-product may adversely affect protein expression, survival, proliferation, growth, differentiation, or function of cultured cell. The term “culture by-product” may be used interchangeably with the term “waste product.”
The unwanted culture by-product may be ammonia. The amount of ammonia may be reduced by about 10% or more, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. For example, the amount of ammonia may be reduced by about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 99% or more, about 100%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 20% to about 60%, about 20% to about 50%, about 20% to about 40%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The process may include culturing a mammalian cell in a glutamine-free cell culture medium under conditions allowing survival or proliferation of the cell.
The mammalian cell refers to a cell derived from mouse, rat, rabbit, dog, cat, sheep, cow, horse, monkey, chimpanzee, or human. The cell may be a cell line.
The cell is, for example, a cell selected from the group consisting of Chinese hamster ovary (CHO) cell, DG44 cell, human embryonic kidney (HEK) cell, NS0 cell, PER.C6 cell, HeLa cell, and Madin-Darby Canine Kidney (MDCK) cell. The CHO cell may be CHO K1 or CHO DUKK cell. The HEK cell may be HEK 293 cell.
The conditions allowing survival or proliferation of the cell may vary according to the type of a cell. For example, the cell may be cultured in the presence of a medium containing nutrients needed for proliferating the cell. The cell may be cultured at a temperature of about 25° C. to about 42° C., about 25° C. to about 40° C., about 30° C. to about 40° C., about 30° C. to about 37° C., or about 37° C. The cell may be cultured in the presence of air containing about 1% CO2 to about 10% CO2, or about 5% CO2 to about 10% CO2.
The culture may vary according to the type of a cell. The culture may be performed using a known method. The culture may be performed in a plate, a flask, or the like. The culture may be performed by adhering the cell to a substrate or floating the cell in a culture solution. The culture may be performed by subculture. The culture may be batch culture. The batch culture may be fed-batch culture. When the culture is performed, the cell culture medium may be periodically replaced with a fresh medium. The cell may be cultured for about 1 day or more, about 2 days or more, about 3 days or more, about 4 days or more, about 5 days or more, about 6 days or more, about 1 week or more, about 10 days or more, about 2 weeks or more, about 3 weeks or more, about 1 month or more, about 1 day to about 1 month, about 1 day to about 3 weeks, about 1 day to about 2 weeks, about 2 days to about 2 weeks, about 3 days to about 2 weeks, about 4 days to about 2 weeks, about 5 days to about 2 weeks, about 6 days to about 2 weeks, or about 1 week to about 2 weeks.
The cell maintained in the above-described process conditions may exhibit increased glucose consumption, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. Since a cell uses glucose as an energy source, an increase in glucose consumption of cell may mean an increase in metabolic activity of cell. The glucose consumption may be increased by about 10% or more as compared to glucose consumption in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. For example, the glucose consumption may be increased by about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 99% or more, about 100%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 10% to about 30%, about 15% to about 60%, about 15% to about 50%, about 15% to about 40%, about 15% to about 30%, about 15% to about 20%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell maintained in the above-described process conditions may exhibit increased cell viability, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. The cell viability refers to the ability of cultured cell to survive, grow, or proliferate in a cultured environment, and the cell viability (%) may be calculated as a relative ratio of viable cell density in an experimental group to that in a negative control. The cell viability may be increased by about 3% or more, as compared to cell viability in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. For example, the cell viability may be increased by about 5% or more, about 8% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 3% to about 50%, about 3% to about 40%, about 3% to about 30%, about 3% to about 20%, about 3% to about 10%, about 3% to about 5%, about 5% to about 50%, about 5% to about 40%, about 5% to about 30%, about 5% to about 20%, about 5% to about 10%, about 10% to about 15%, about 15% to about 20%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell maintained under the above-described process conditions may exhibit an increased expression level (titer) of a polypeptide, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. The term “expression level” as used herein may be used interchangeably with the term “titer.” The expression level of a polypeptide of the cell may be represented as the concentration (g/L) of a protein in a cell culture medium obtained through the process. The expression level of a polypeptide of the cell may be increased by about 10% or more, as compared to an expression level of a polypeptide in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthin and thymidine. For example, the expression level of a polypeptide of the cell may be increased by about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 99% or more, about 100%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 15% to about 60%, about 15% to about 50%, about 15% to about 40%, about 15% to about 30%, about 15% to about 20%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The target protein refers to a protein to be obtained by culturing cell. The target protein may be a cytoplasmic polypeptide, a membranous polypeptide, or a secretable polypeptide. The target protein may be a recombinant protein. The recombinant protein may be selected from the group consisting of, for example, an antibody or an antigen-binding fragment thereof, immunoadhesin, transforming growth factor (TGF)-β superfamily signaling molecule, blood coagulation factor, anti-tumor necrosis factor receptor (TNFR) antibody, anti-human epidermal growth factor receptor 2 (HER2) antibody, and TNFR:Fc. The term “antibody” as used herein is used interchangeably with the term “immunoglobulin (Ig).” A complete antibody has a structure including two full-length light chains and two full-length heavy chains, wherein each light chain is linked to the heavy chain by disulfide bonds (SS-bond). The antibody may be, for example, IgA, IgD, IgE, IgG, or IgM. The antibody may be a monoclonal antibody or a polyclonal antibody. The antibody may be an animal-derived antibody, a mouse-human chimeric antibody, a humanized antibody, or a human antibody. The term “antigen-binding fragment” refers to a fragment of the whole immunoglobulin structure and a portion of a polypeptide containing an antigen-binding portion. For example, the antigen-binding fragment may be scFv, (scFv)2, Fv, Fab, Fab′, Fv F(ab′)2, or a combination thereof. The immunoadhesin refers to an antibody-like protein and a fusion protein of the Fc region of an immunoglobulin and the functional domain of a binding protein (e.g., receptors, ligand cell-adhesion molecules). The TGF-β superfamily signaling molecules may be, for example, TGF-β 1, TGF-β 2, or TGF-β 3. The blood coagulation factor refers to a factor involved in blood coagulation. The blood coagulation factor may be, for example, fibrinogen, prothrombin, tissue tromboplastin, factor V, factor VII, factor VIII, factor IX, factor X, factor XI, factor XII, factor XIII, a von Willebrand factor, prekallikrein, high-molecular-weight kininogen, fibronectin, antithrombin III, heparin cofactor II, protein C, protein S, protein Z, a protein Z-linked protease inhibitor, plasminogen, alpha 2-antiplasmin, a tissue plasminogen activator, urokinase, plasminogen activator inhibitor-1, plasminogen activator inhibitor-2, or a cancer procoagulant. The anti-TNFR antibody may be an antibody specifically binding to TNFR or an antigen-binding fragment thereof. The anti-HER2 antibody may be an antibody specifically binding to HER2 or an antigen-binding fragment thereof. The TNFR:Fc refers to a fusion protein of TNFR and an Fc region.
The target protein may be selected from the group consisting of abagovomab, abciximab, adalimumab, adecatumumab, alemtuzumab, altumomab, altumomab pentetate, anatumomab, anatumomab mafenatox, arcitumomab, atlizumab, basiliximab, bectumomab, ectumomab, belimumab, benralizumab, bevacizumab, brentuximab, canakinumab, capromab, capromab pendetide, catumaxomab, certolizumab, clivatuzumab tetraxetan, daclizumab, denosumab, eculizumab, edrecolomab, efalizumab, etaracizumab, ertumaxomab, fanolesomab, fontolizumab, gemtuzumab, girentuximab, golimumab, ibritumomab, igovomab, infliximab, ipilimumab, labetuzumab, mepolizumab, muromonab, muromonab-CD3, natalizumab, necitumumab, nimotuzumab, ofatumumab, omalizumab, oregovomab, palivizumab, panitumumab, ranibizumab, rituximab, satumomab, sulesomab, ibritumomab, ibritumomab tiuxetan, tocilizumab, tositumomab, trastuzumab, ustekinumab, visilizumab, votumumab, zalutumumab, brodalumab, anrukinzumab, bapineuzumab, dalotuzumab, demcizumab, ganitumab, inotuzumab, mavrilimumab, moxetumomab pasudotox, rilotumumab, sifalimumab, tanezumab, tralokinumab, tremelimumab, urelumab, adornase alfa, Rebif, becaplermin, alteplase, laronidase, alefacept, aflibercept, Raxibacumab, darbepoetin alfa, Becaplermin Concentrate, interferon beta-1b, Botulinum Toxin Type A, rasburicase, asparaginase, epoetin alfa, etanercept, agalsidase beta, interferon alfacon-1, interferon alfa-2a, anakinra, Botulinum Toxin Type B, pegfilgrastim, oprelvekin, filgrastim, denileukin diftitox, peginterferon alfa-2a, aldesleukin, dornase alfa, interferon beta-1a, becaplermin, reteplase, interferon alfa-2, tenecteplase, drotrecogin alfa, rilonacept, romiplostim, methoxypolyethylene glycol-epoetin beta, a C1 esterase inhibitor, idursulfase, alglucosidase alfa, abatacept, galsulfase, palifermin, and interferon gamma-1b.
The polypeptide may be a target protein.
According to an aspect of another embodiment, an improved culture process for reducing an unwanted culture by-product when a target protein is produced in a glutamine-free cell culture medium includes culturing mammalian cell in the glutamine-free cell culture medium under conditions allowing survival or proliferation of the cell, wherein the cell culture medium includes hypoxanthine at a concentration of about 150 μM to about 300 μM and thymidine at a concentration of about 25 μM to about 150 μM, and cell maintained under the above-described process conditions exhibit at least one of a decrease in the amount of ammonia, which is an unwanted culture by-product, an increase in glucose consumption of the cell, an increase in cell viability, and an increase in an expression level of a polypeptide of the cell, as compared to those in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine.
The cell, the cell culture medium, the glutamine-free cell culture medium, the culture by-product, the unwanted culture by-product, the conditions allowing survival or proliferation of the cell, the culturing, the hypoxanthine, the thymidine, the ammonia, the glucose consumption, the cell viability, the polypeptide, and the expression level of a polypeptide of the cell are the same as described above.
The cell maintained under the above-described process conditions may exhibit at least one of a decrease in the amount of ammonia, which is an unwanted culture by-product, an increase in glucose consumption of the cell, an increase in cell viability, and an increase in an expression level of a polypeptide of the cell, as compared to those in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine. For example, the cell may exhibit an about 10% or more decrease in the amount of ammonia, an about 10% or more increase in glucose consumption of the cell, an about 3% or more increase in the cell viability, an about 10% or more increase in an expression level of a polypeptide of the cell, or a combination thereof.
The process according to an embodiment and the process according to another embodiment may further include supplementing the cell culture medium with uridine. The uridine is a compound of pyrimidine nucleoside. The uridine may be natural or synthesized uridine. The amount of uridine in the cell culture medium may range from about 0.01 mM to about 100 mM, about 0.05 mM to about 95 mM, about 0.1 mM to about 90 mM, about 0.1 mM to about 85 mM, about 0.5 mM to about 80 mM, about 1 mM to about 80 mM, about 1 mM to about 75 mM, about 1 mM to about 70 mM, about 1 mM to about 65 mM, about 1 mM to about 60 mM, about 1 mM to about 55 mM, about 1 mM to about 50 mM, about 1 mM to about 45 mM, about 1 mM to about 40 mM, about 1 mM to about 35 mM, about 1 mM to about 30 mM, about 1 mM to about 25 mM, about 1 mM to about 20 mM, about 1.5 mM to about 20 mM, about 2 mM to about 20 mM, about 2 mM to about 15 mM, about 2 mM to about 10 mM, about 2.5 mM to about 10 mM, about 2.5 mM to about 9 mM, about 2.5 mM to about 8 mM, about 3 mM to about 8 mM, about 3 mM to about 7 mM, about 3.5 mM to about 7 mM, about 3.5 mM to about 6 mM, about 3.5 mM to about 5 mM, or about 4 mM. The supplementation may be performed by adding uridine to the cell culture medium at the initial stage of the culture or during the culture.
The process according to an embodiment and the process according to another embodiment may further include supplementing the cell culture medium with magnesium (Mg). The Mg may be a Mg ion or a Mg salt. The amount of Mg in the cell culture medium may range from about 0.01 mM to about 100 mM, about 0.01 mM to about 95 mM, about 0.01 mM to about 90 mM, about 0.01 mM to about 85 mM, about 0.01 mM to about 50 mM, about 0.05 mM to about 85 mM, about 0.05 mM to about 80 mM, about 0.1 mM to about 80 mM, about 0.1 mM to about 75 mM, about 0.1 mM to about 70 mM, about 0.1 mM to about 65 mM, about 0.1 mM to about 60 mM, about 0.1 mM to about 55 mM, about 0.1 mM to about 50 mM, about 0.2 mM to about 50 mM, about 0.2 mM about 45 mM, about 0.2 mM about 40 mM, about 0.2 mM to about 35 mM, about 0.4 mM to about 35 mM, about 0.4 mM to about 30 mM, about 0.4 mM to about 25 mM, about 0.4 mM to about 20 mM, about 0.5 mM to about 25 mM, about 0.6 mM to about 20 mM, about 0.6 mM to about 15 mM, about 0.6 mM to about 10 mM, about 0.6 mM to about 9 mM, about 0.6 mM to about 8 mM, about 0.6 mM to about 7 mM, about 0.6 mM to about 6 mM, about 0.6 mM to about 5 mM, about 0.8 mM to about 5 mM, about 0.8 mM to about 4 mM, about 0.8 mM to about 3 mM, about 0.8 mM to about 2 mM, about 0.8 mM to about 1.5 mM, about 0.8 mM to about 1.2 mM, or about 1 mM. The supplementation may be performed by adding magnesium to the cell culture medium at the initial stage of the culture or during the culture.
According to an aspect of another embodiment, an improved culture process for producing a target protein in a glutamine-free cell culture medium includes culturing mammalian cell in a glutamine-free cell culture medium under conditions allowing survival or proliferation of the cell, wherein the cell culture medium includes uridine at a concentration of about 0.01 mM to about 100 mM.
The cell, the cell culture medium, the glutamine-free cell culture medium, the target protein, the conditions allowing survival or proliferation of the cell, and the uridine are the same as described above.
The cell maintained in the cell culture medium may exhibit increased cell viability, as compared to that in a glutamine-free cell culture medium that does not contain uridine. The cell viability may be increased by about 3% or more, as compared to cell viability in the glutamine-free cell culture medium that does not contain uridine. For example, the cell viability may be increased by about 5% or more, about 8% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 3% to about 50%, about 3% to about 40%, about 3% to about 30%, about 3% to about 20%, about 3% to about 10%, about 3% to about 5%, about 5% to about 50%, about 5% to about 40%, about 5% to about 30%, about 5% to about 20%, about 5% to about 10%, about 10% to about 15%, about 15% to about 20%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell maintained in the cell culture medium may exhibit an increased viable cell density (VCD), as compared to that in a glutamine-free culture medium that does not contain uridine. The VCD may be increased by about 5% or more, as compared to VCD in a glutamine-free culture medium that does not contain uridine. For example, the VCD may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 3% to about 5%, about 5% to about 10%, about 5% to about 60%, about 5% to about 50%, about 5% to about 40%, about 5% to about 30%, about 5% to about 20%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 10% to about 30%, about 10% to about 20%, about 10% to about 15%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell culture medium may further include hypoxanthine at a concentration of about 20 μM to about 1,000 μM and thymidine at a concentration of about 2 μM to about 1,000 μM. The cell maintained in the cell culture medium may exhibit a reduced amount of ammonia as an unwanted culture by-product of the cell culture medium, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine. The amount of ammonia may be reduced by about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 99% or more, about 100%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 20% to about 60%, about 20% to about 50%, about 20% to about 40%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine.
According to an aspect of another embodiment, an improved culture process for producing a target protein in a glutamine-free cell culture medium includes culturing mammalian cell in the glutamine-free cell culture medium under conditions allowing survival or proliferation of the cell, wherein the cell culture medium includes magnesium at a concentration of about 0.01 mM to about 100 mM.
The cell, the cell culture medium, the glutamine-free cell culture medium, the target protein, the conditions allowing survival or proliferation of the cell, and the magnesium are the same as described above.
The cell maintained in the cell culture medium may exhibit increased cell viability, as compared to that in a glutamine-free culture medium that does not contain magnesium. The cell viability may be increased by about 1% or more when compared to cell viability in a glutamine-free culture medium that does not contain magnesium. For example, the cell viability may be increased by about 1.5% or more, about 2% or more, about 3% or more, about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 1% to about 5%, about 1% to about 10%, about 1% to about 20%, about 1% to about 30%, about 1.5% to about 5%, about 1.5% to about 10%, about 1.5% to about 20%, about 1.5% to about 30%, about 3% to about 5%, about 5% to about 10%, about 5% to about 15%, about 10% to about 15%, about 15% to about 20%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell maintained in the cell culture medium may exhibit increased cell viable density, as compared to that in a glutamine-free culture medium that does not contain magnesium. The cell viable density may be increased by about 5% or more, as compared to cell viable density in a glutamine-free culture medium. For example, the cell viable density may be increased by about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 5% to about 60%, about 5% to about 50%, about 5% to about 40%, about 5% to about 30%, about 5% to about 20%, about 5% to about 10%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 10% to about 30%, about 10% to about 20%, about 10% to about 15%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%.
The cell culture medium may further include hypoxanthine at a concentration of about 20 μM to about 1,000 μM and thymidine at a concentration of about 2 μM to about 1,000 μM. The cell maintained in the cell culture medium may exhibit a reduced amount of ammonia as an unwanted culture by-product of the cell culture medium, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine. The amount of ammonia may be reduced by about 15% or more, about 20% or more, about 30% or more, about 40% or more, about 50% or more, about 60% or more, about 70% or more, about 80% or more, about 90% or more, about 99% or more, about 100%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 20% to about 60%, about 20% to about 50%, about 20% to about 40%, about 20% to about 30%, about 30% to about 40%, about 40% to about 50%, about 50% to about 60%, about 60% to about 70%, about 70% to about 80%, about 80% to about 90%, or about 90% to about 100%, as compared to that in a glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine.
The glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine may contain hypoxanthine at a concentration of less than 100 μM, 90 μM or less, 80 μM or less, 70 μM or less, 60 μM or less, 50 μM or less, 40 μM or less, 30 μM or less, 20 μM or less, 10 μM or less, 5 μM or less, or 1 μM or less, or may be a hypoxanthine-free medium. The glutamine-free culture medium that does not substantially contain at least one of hypoxanthine and thymidine may contain thymidine at a concentration of less than 16 μM, 15 μM or less, 14 μM or less, 13 μM or less, 12 μM or less, 11 μM or less, 10 μM or less, 9 μM or less, 8 μM or less, 7 μM or less, 6 μM or less, 5 μM or less, 4 μM or less, 3 μM or less, 2 μM or less, or 1 μM or less, or may be a thymidine-free medium.
In the embodiment or the other embodiment, the culturing process may include conditions of at least one temperature change, conditions of at least one pH change, or a combination thereof.
The conditions of at least one temperature change are as follows: the cell may be grown in a medium at a first temperature for 3 days or more, the temperature may be changed to a second temperature, which is about 1° C. to about 8° C. lower than the first temperature, and the cell may be maintained at the second temperature for about 2 days or more. The cell may be grown in a medium at a first temperature for about 3 days or more, about 4 days or more, about 1 week or more, about 2 days to about 1 week, or about 2 days to about 4 days. The cell may be maintained in a medium at a second pH value for about 2 days or more, about 3 days or more, about 4 days or more, about 1 week or more, about 2 weeks or more, about 3 weeks or more, about 1 month or more, about 1 day to about 1 month, about 1 week to about 3 weeks, about 1 day to about 2 weeks, about 1 day to about 1 week, or about 1 day to about 4 days. The first temperature may range from about 30° C. to about 42° C., about 32° C. to about 42° C., about 32° C. to about 40° C., about 34□ to about 40□, about 36° C. to about 40□, or about 37□. The second temperature may range from about 25° C. to about 41□, about 27□ to about 41□, about 27° C. to about 40□, about 30□ to about 40□, about 30□ to about 37□, about 30□ to about 35□, about 30□ to about 33□, or about 31□ to about 33□. A difference between the first and second temperatures may range from about 1° C. to about 7□, about 1□ to about 6□, about 1□ to about 5□, about 1° C. to about 4° C., about 1□ to about 3□, or about 1□ to about 2° C.
The conditions of at least one pH change are as follows: the cell may be grown in a medium at a first pH value for about 2 days or more, the pH may be changed to a second pH value, which is about 0.05 to about 1 lower than the first pH value, and the cell may be grown at the second pH value for about 1 day or more. The cell may be grown in a medium at a first pH value for about 2 days or more, about 3 days or more, about 4 days or more, about 1 week or more, about 2 days to about 1 week, or about 2 days to about 4 days. The cell may be maintained in a medium at a second pH value for about 1 day or more, about 2 days or more, about 3 days or more, about 4 days or more, about 1 week or more, about 2 weeks or more, about 3 weeks or more, about 1 month or more, about 1 day to about 1 month, about 1 day to about 3 weeks, about 1 day to about 2 weeks, about 1 day to about 1 week, or about 1 day to about 4 days. The first pH value may range from about pH 6.8 to about pH 7.5, about pH 6.8 to about pH 7.2, about pH 6.8 to about pH 7.0, or about pH 7.0 to about pH 7.2. The second pH value may range from about pH 6.0 to about pH 7.1, about pH 6.0 to about pH 7.0, about pH 6.0 to about pH 6.8, about pH 6.0 to about pH 6.6, about pH 6.0 to about pH 6.4, or about pH 6.0 to about pH 6.2. A difference between the first and second pH values may range from, for example, about pH 0.05 to about pH 0.9, about pH 0.05 to about pH 0.8, about pH 0.05 to about pH 0.7, about pH 0.05 to about pH 0.6, about pH 0.05 to about pH 0.5, about pH 0.05 to about pH 0.4, about pH 0.05 to about pH 0.3, about pH 0.05 to about pH 0.2, about pH 0.05 to about pH 0.1, or about pH 0.05 to about pH 0.08.
In the embodiment or the other embodiment, the process may further include adding glucose to the glutamine-free cell culture medium such that the concentration of the glucose is maintained at about 2 g/L or more.
The concentration of the glucose in the cell culture medium may be maintained at about 2 g/L or more, about 2.5 g/L or more, about 3.0 g/L or more, about 3.5 g/L or more, about 4 g/L or more, about 4.5 g/L or more, about 5 g/L or more, about 5.5 g/L or more, about 6 g/L or more, about 7 g/L or less, about 2 g/L to about 7 g/L, about 2 g/L to about 6 g/L, about 2.5 g/L to about 5.5 g/L, about 3 g/L to about 5 g/L, about 3.5 g/L to about 5 g/L, or about 3.5 g/L to about 4.5 g/L. The glucose may be added to the cell culture medium during cell culture.
According to an embodiment or another embodiment, the cell may be cultured in a medium prepared by adding hypoxanthine, thymidine, uridine, magnesium, or a combination thereof to a glutamine-free medium, thereby reducing the production of ammonia due to the cell, increasing an expression level of a polypeptide of the cell, increasing a viable cell density, and increasing cell viability, and accordingly, the production of a target protein from the cell may be significantly increased.
0 mM glutamine+2×HT,
: 0 mM glutamine+1×HT).
Hereinafter, the present disclosure will be described in further detail with reference to the following examples. However, these examples are provided for illustrative purposes only and are not intended to limit the scope of the present disclosure.
When cells are cultured, the concentration of ammonia in a cell culture medium is increased, and ammonia has cytotoxicity. In addition, during cell culture, as the number of cells increases, the amount of glucose consumed by the cells increases, and the content of glucose in the cell culture medium decreases. It was examined whether the amount of ammonia produced by cells during cell culture was decreased and the consumption of glucose of the cells was increased, in a case in which 2×HT was added to a cell culture medium.
First, a cell line expressing a fusion protein (CHO cell line) was prepared (the cell line was prepared by transfecting a CHO cell line with a vector expressing the fusion protein), and the cells were cultured in a glutamine-free medium. Cells at a density of 9×105 cells/ml were inoculated in a cell culture dish, and a glutamine-free medium was added thereto. The medium was supplemented with a 100× stock (catalog number: 11067030, Gibco) of 10 mM sodium hypoxanthine and 1.6 mM thymidine so that the final concentrations of hypoxanthine and thymidine in the medium reached 100 μM and 16 μM, respectively (hereinafter, referred to as “1×HT”), or 200 μM and 32 μM, respectively (hereinafter, referred to as “2×HT”). The cells were cultured at 37° C. and 5% CO2, and the medium was replaced with a fresh medium every two days.
While the cells were cultured for about 15 days, the concentrations of ammonia (mM) and glucose (g/L) in the medium according to culture time (day) were measured using an ammonium ion-selective electrode and a glucose membrane kit (catalog No.: 24458, Nova Biomedical) of a Bioprofile analyzer (Model No.: BioProfile 400, Nova Biomedical). The results thereof are illustrated in
As illustrated in
In addition, as illustrated in
Thus, it was confirmed that, when cells were cultured in a glutamine-free and 2×HT-containing medium, the production of ammonia by the cells was reduced, and cytotoxicity due to the produced ammonia was reduced, and accordingly, glucose consumption of the cells was increased, as compared to a case in which cells were cultured in a glutamine-free and 1×HT-containing medium.
It was examined whether there were differences in cell viability and polypeptide expression level (titer) of the cultured cells when the cells were cultured in a glutamine-free and 2×HT-containing medium, as compared to when the cells were cultured in a glutamine-free and 1×HT-containing medium.
The cells were cultured in a glutamine-free and 2×HT-containing medium or a glutamine-free and 1×HT-containing medium using the same method as that used in Example 1. Cells cultured in a glutamine-free medium were used as a negative control.
The relative cell viability (%) and polypeptide expression level (g/L) of the cells with respect to the negative control were measured using a Cedex HiRes analyzer (Model No.: 05650216001, Roche) and HPLC (Model No.: 720000370EN, Waters), respectively through a Trypan blue exclusion method and a UV280 measurement method. The results thereof are illustrated in
As illustrated in
It was examined whether the addition of uridine affected viable cell density (VCD) and cell viability, when cells were cultured in a medium prepared by adding uridine to 2×HT.
Cells were prepared using the same method as that used in Example 1, and a glutamine-free and 2×HT-containing medium was added to the prepared cells. 4 mM of uridine (catalog No.: U3003, Sigma) or 8 mM of galactose (Catalog No.: G0750, Sigma) was added to the medium. The cells were cultured at 37° C. and 5% CO2, and the medium was replaced with a fresh medium every two days. Cells cultured in a glutamine-free medium were used as a negative control.
After about 14 days, viable cell density and cell viability were measured using a Cedex HiRes analyzer (Model No.: 05650216001, Roche) through a scanner-based imaging method and a Trypan blue exclusion method. The viable cell density (CHO cells/ml) of cells cultured in the presence of uridine and in the presence of galactose is illustrated in
As illustrated in
In contrast, as illustrated in
As illustrated in
In contrast, as illustrated in
Thus, it was confirmed that, when cells were cultured in a 2×HT- and uridine-containing medium, viable cell density and cell viability were significantly increased.
Similar to Example 3, it was examined whether the addition of magnesium affected viable cell density and cell viability, when cells were cultured in a medium prepared by adding magnesium to 2×HT.
Cells were prepared using the same method as that used in Example 1, and a glutamine-free and 2×HT-containing medium was added to the prepared cells. 1 mM of magnesium (Catalog No.: M4880, Sigma) was added to the medium. The cells were cultured at 37° C. and 5% CO2, and the medium was replaced with a fresh medium every two days. Cells cultured in a glutamine-free medium were used as a negative control.
After about 14 days, viable cell density and cell viability were measured using a Cedex HiRes analyzer (Model No.: 05650216001, Roche) through a scanner-based imaging method and a Trypan blue exclusion method, respectively. The viable cell density (CHO cells/ml) and cell viability of the cells cultured in the presence of magnesium are illustrated in
As illustrated in
Thus, it was confirmed that the viable cell density and the cell viability were significantly increased in a case in which cells were cultured in a 2×HT- and magnesium-containing medium.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2016-0143427 | Oct 2016 | KR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2017/011872 | 10/26/2017 | WO |
