Method for producing monomeric and multimeric molecules and uses thereof
US-2015218250-A1 · Aug 6, 2015 · US
US12134633B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12134633-B2 |
| Application number | US-202318298857-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 11, 2023 |
| Priority date | May 11, 2016 |
| Publication date | Nov 5, 2024 |
| Grant date | Nov 5, 2024 |
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The invention relates to a separation matrix comprising at least 11 mg/ml Fc-binding ligands covalently coupled to a porous support, wherein: a) the ligands comprise multimers of alkali-stabilized Protein A domains, and b) the porous support comprises cross-linked polymer particles having a volume-weighted median diameter (d50,v) of 56-70 micrometers and a dry solids weight of 55-80 mg/ml.
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The invention claimed is: 1. A separation matrix comprising at least 15 mg/ml Fc-binding ligands covalently coupled to a porous support, wherein: the ligands comprise multimers of alkali-stabilized Protein A domains; the porous support comprises cross-linked polymer particles having a volume-weighted median diameter (d50,v) of from 56 μm to 70 μm; the separation matrix has a max pressure of at least 0.58 MPa when packed at 300+/−10 mm bed height in a 35 mm separation column; and the Protein A domains comprise an Fc-binding polypeptide defined by, or having at least 80% identity to SEQ ID NO: 53 and X 1 QX 2 AFYEILX 3 LPNLTEEQRX 4 X 5 FIX 6 X 7 LKDX 8 PSX 9 SX 10 X 11 X 12 LAEAKX 13 X 14 N X 15 AQ (SEQ ID NO: 53), wherein individually of each other: X 1 =A or Q or is deleted; X 2 =E, K, Y, T, F, L, W, I, M, V, A, H, or R; X 3 =H or K; X 4 =A or N; X 5 =A, G, S, Y, Q, T, N, F, L, W, I, M, V, D, E, H, R, or K; X 6 =Q or E; X 7 =S or K; X 8 =E or D; X 9 =W or V or is deleted; X 10 =K, R, or A, or is deleted; X 11 =A, E, or N, or is deleted; X 12 =I or L; X 13 =K or R; X 14 =L or Y; and X 15 =D, F, Y, W, K, or R. 2. The separation matrix of claim 1 , wherein the cross-linked polymer particles have a dry solids weight of from 55 mg/ml to 80 mg/ml. 3. The separation matrix of claim 1 , wherein the cross-linked polymer particles have a dry solids weight of from 60 mg/ml to 78 mg/ml. 4. The separation matrix of claim 1 , wherein the cross-linked polymer particles have a dry solids weight of from 65 mg/ml to 78 mg/ml. 5. The separation matrix of claim 1 , wherein the cross-linked polymer particles have a volume-weighted median diameter (d50,v) of from 56 μm to 66 μm. 6. The separation matrix of claim 1 , wherein the cross-linked polymer particles comprise cross-liked polysaccharide particles. 7. The separation matrix of claim 1 , wherein the cross-linked polymer particles comprise cross-linked agarose particles. 8. The separation matrix of claim 1 , wherein the cross-linked polymer particles have a pore size corresponding to an inverse gel filtration chromatography Kd value of 0.69-0.85 for dextran of Mx 100 kDa. 9. The separation matrix of claim 1 , wherein the multimers comprise tetramers, pentamers, hexamers, or heptamers of alkali-stabilized Protein A domains. 10. The separation matrix of claim 1 , wherein the multimers comprise hexamers of alkali-stabilized Protein A domains. 11. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 45 mg/ml at 2.4 minutes residence time. 12. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 50 mg/ml at 2.4 minutes residence time. 13. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 55 mg/ml at 2.4 minutes residence time. 14. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 60 mg/ml at 6 minutes residence time. 15. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 65 mg/ml at 6 minutes residence time. 16. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 70 mg/ml at 6 minutes residence time. 17. The separation matrix of claim 1 , having a 10% breakthrough dynamic binding capacity for IgG of at least 75 mg/ml at 6 minutes residence time. 18. The separation matrix of claim 11 , wherein the 10% breakthrough dynamic binding capacity for IgG at 2.4 minutes residence time is reduced by less than 20% after incubation for 31 hours in 1.0 M aqueous NaOH at 22+/−2° C. 19. The separation matrix of claim 1 , having a dissociation constant for IgG2 of below 0.2 mg/ml in 20 mM phosphate buffer, 180 mM NaCl, pH 7.5. 20. The separation matrix of claim 1 , having a dissociation constant for IgG2 of below 0.1 mg/ml in 20 mM phosphate buffer, 180 mM NaCl, pH 7.5. 21. The separation matrix of claim 1 , wherein individually of each other: X 1 =A or is deleted; X 2 =E; X 3 =H; X 4 =N; X 6 =Q; X 7 =S; X 8 =D; X 9 =V or is deleted; X 10 =K or is deleted; X 11 =A or is deleted; X 12 =I; X 13 =K; and X 14 =L. 22. The separation matrix of claim 1 , wherein the amino acid sequence has at least 90% identity to SEQ ID NO: 53. 23. The separation matrix of claim 1 , wherein the amino acid sequence has at least 95% identity to SEQ ID NO: 53. 24. The separation matrix of claim 1 , wherein the amino acid sequence has at least a 98% identity to SEQ ID NO: 53. 25. The separation matrix of claim 1 , wherein the amino acid sequence is identical to SEQ ID NO: 53. 26. The separation matrix of claim 1 , wherein the polypeptides are linked by linkers comprising up to 25 amino acids. 27. The separation matrix of claim 1 , wherein at least two polypeptides are linked by likers comprising or consisting essentially of a sequence having at least 90% identity with an amino acid sequence selected from the group consisting of APKVDAKFDKE (SEQ ID NO: 96), APKVDNKFNKE (SEQ ID NO: 97), APKADNKFNKE (SEQ ID NO: 98), APKVFDKE (SEQ ID NO: 99), APAKFDKE (SEQ ID NO: 100), AKFDKE (SEQ ID NO: 101), APKVDA (SEQ ID NO: 102), VDAKFDKE (SEQ ID NO: 103), APKKFDKE (SEQ ID NO: 104), APK, APKYEDGVDAKFDKE (SEQ ID NO: 105), and YEDG (SEQ ID NO: 106). 28. The separation matrix of claim 1 , comprising from 15 mg/ml to 21 mg/ml Fc-binding ligands covalently coupled to the porous support. 29. The separation matrix of claim 1 , comprising from 17 mg/ml to 21 mg/ml Fc-biding ligands covalently coupled to the porous support. 30. The separation matrix of claim 1 , comprising from 18 mg/ml to 20 mg/ml Fc-binding ligands covalently coupled to the porous support. 31. A method of isolating an immunoglobulin, comprising the steps of: a) contacting an immunoglobulin with a separation matrix according to claim 1 ; b) washing the separation matrix with a washing liquid; c) eluting the immunoglobulin from the separation matrix with an elution liquid; and d) cleaning the separation matrix with a cleaning liquid. 32. The method of claim 31 , wherein the cleaning liquid comprises from 0.1 to 1.0 M NaOH or KOH. 33. The method of claim 32 , wherein steps a)-d) are repeated at least 10 times. 34. The method of claim 32 , wherein in step c) the elution liquid has a pH of from 2.5 to 4.5. 35. The method of claim 32 , wherein in step b) the washing liquid has a pH of from 6 to 8. 36. The method of claim 32 , wherein in step b) residence time of the liquid on the separation matrix is from 2 minutes to 20 minutes. 37. The method of claim 32 , wherein the cleaning liquid comprises at least 0.5 M NaOH. 38. The method of claim 33 , wherein in step d) contact time between the separation matrix and the cleaning liquid is less than 10 minutes.
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