St2 antigen binding proteins
US-2024368292-A1 · Nov 7, 2024 · US
US2020157230A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020157230-A1 |
| Application number | US-202016779336-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 31, 2020 |
| Priority date | May 27, 2011 |
| Publication date | May 21, 2020 |
| Grant date | — |
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The present disclosure relates to compositions of daclizumab suitable for subcutaneous administration and methods of manufacturing thereof.
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What is claimed is: 1 . A modified NS0 cell that has been adapted to grow in serum- and cholesterol-free media and that is engineered to express a recombinant protein, said cell being capable of achieving a volumetric productivity exceeding 100 mg/L/day recombinant protein in a culture of 100 L in a 10-day fed-batch process when grown in serum- and cholesterol-free media. 2 . The modified NS0 cell of claim 1 which is capable of achieving a volumetric productivity exceeding: (a) 100 mg/L/day recombinant protein in a culture of 1,000 L in a 10-day fed-batch process when grown in media free of cholesterol and animal-derived components; (b) 100 mg/L/day recombinant protein in a culture of 16,000 L in a 10-day fed-batch process when grown in media free of cholesterol and animal-derived components; (c) 200 mg/L/day recombinant protein in a culture of at least 100 L in a 13-day fed-batch process; (d) 200 mg/L/day recombinant protein in a culture of 1,000 L in a 13-day fed-batch process when grown in cholesterol-free media; or (e) 100 mg/L/day recombinant protein in a culture of 16,000 L in a 10-day fed-batch process when grown in serum- and cholesterol-free media. 3 . The modified NS0 cell of claim 1 , wherein said fed-batch process comprises adding a feed medium is added according to the following schedule, where the volume added represents the percentage of the initial cell culture volume: Day Volume added 0 0 1 0 2 4 3 7.8 4 7.8 5 7.8 6 11 7 13 8 15 9 15 10 0 4 . The modified NS0 cell of claim 1 which is stably transfected with a nucleic acid useful for expressing an anti-CD25 monoclonal antibody, optionally in which the anti-CD25 monoclonal antibody comprises a V L chain corresponding in sequence to positions 21-233 of SEQ ID NO:2 and a V H chain corresponding in sequence to positions 20 to 465 of SEQ ID NO:4. 5 . A method of producing a recombinant protein, comprising culturing the modified NS0 cell of claim 1 : (a) under conditions that result in the production of at least 100 mg/L/day recombinant protein in a 100 L, 1,000 L or 16,000 L culture in a 10-day fed-batch process, or at least 200 mg/L/day recombinant protein in a 100 L, 1,000 L or 16,000 L culture in a 13-day fed-batch process; (b) in the absence of serum and cholesterol, and optionally in the absence of tropolone and hydrocortisone; (c) in a basal and/or feed medium containing 10-35 g/L glucose; or (d) in a basal medium containing 15 g/L glucose and/or a feed medium containing 28 g/L glucose, optionally wherein the basal medium is composed of the components of PFBM2±10% or PFFM3±10% and wherein the cell is cultured in basal medium for 1-3 days, and then in feed medium for 10-13 days. 6 . A vector useful for recombinantly expressing a protein of interest, comprising a weak promoter driving expression of a selectable marker operable in mammalian cells and a strong promoter driving expression of a protein of interest, optionally wherein the vector is pAbX.gpt or pHAT.IgG1.rg.dE and/or the protein of interest is (a) a therapeutic antibody; (b) an anti-CD25 antibody; (c) an anti-CD25 antibody which comprises the CDRs of daclizumab; or (d) daclizumab. 7 . A method for obtaining a mammalian host cell that has a high volumetric productivity of a protein of interest, comprising transfecting the cell with the vector of claim 6 , and selecting a cell that is capable of producing at least 100 mg/L/day protein of interest in a 100 L, 1,000 L or 16,000 L culture in a 10-day fed-batch process or at least 200 mg/L/day recombinant protein in a 100 L, 1,000 L or 16,000 L culture in a 13-day fed-batch process. 8 . A composition comprising daclizumab, wherein the daclizumab is characterized by the presence of a pE/Q heavy chain N-linked isoform and/or a Q/VHS heavy chain N-terminal isoform, optionally wherein the pE/Q heavy chain N-terminal isoform constitutes approximately 3-17%, approximately 3-15%, approximately 6-15%, approximately 5-15%, approximately 5-12%, or approximately 7-12% of the daclizumab, and, optionally wherein the Q/VHS heavy chain N-terminal isoform constitutes approximately 1-15% or approximately 3-12% of the daclizumab. 9 . The composition of claim 8 in which the heavy chain of daclizumab exists in the following N-terminal isoforms: Isoform Prevalence (a) pE/pE 25%-50% pE/Q 3%-15% pE/VHS 25%-48% Q/VHS 1%-15% VHS/VHS 0.5%-25% or (b) pE/pE 31-46% pE/Q 5%-12% pE/VHS 31%-42% Q/VHS 3%-12% VHS/VHS 1%-17%
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