Purification of fkpa and uses thereof for producing recombinant polypeptides
US-2018327446-A1 · Nov 15, 2018 · US
US11518781B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11518781-B2 |
| Application number | US-201816957160-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2018 |
| Priority date | Dec 29, 2017 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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A process for providing a mono-PEGylated protein composition is provided. The process is particularly suitable for providing mono-PEGylated erythropoietin composition. The process comprises subjecting a mixture comprising non-PEGylated, mono-PEGylated and oligo-PEGylated to a hydrophobic interaction chromatography process.
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The invention claimed is: 1. A process for producing a mono-PEGylated protein composition comprising at least about 90% mono-PEGylated protein, comprising the steps of: a) providing a protein mixture comprising non-PEGylated protein, mono-PEGylated protein and oligo-PEGylated protein; b) subjecting the protein mixture to a two-stage hydrophobic interaction chromatography (HIC) step, comprising: applying the protein mixture to a first HIC material to provide a first HIC flow-through solution; and applying the first HIC flow-through solution to a second HIC material to provide a second HIC flow-through solution, wherein the second HIC material is different from the first HIC material; and wherein the two-stage HIC step is performed under two-stage HIC conditions, which two-stage HIC conditions are suitable for binding oligo-PEGylated protein to the first HIC material and binding mono-PEGylated protein to the second HIC material; and c) eluting the mono-PEGylated protein from the second HIC material to provide a second HIC eluate, wherein the second HIC eluate provides the mono-PEGylated protein composition. 2. The process according to claim 1 , wherein the protein is a hormone, a cytokine, an enzyme or an antibody. 3. The process according to claim 1 , wherein the protein is erythropoietin. 4. The process according to claim 1 , wherein the first HIC material and the second HIC material are directly connected in series. 5. The process according to claim 1 , wherein under the two-stage HIC conditions the first HIC material does not bind non-PEGylated protein or mono-PEGylated protein, and wherein the second HIC material does not bind non-PEGylated protein. 6. The process according to claim 1 , wherein in comparative HIC elution chromatograms the first HIC material and the second HIC material have well-resolved peaks for mono-PEGylated protein. 7. The process according to claim 1 , wherein a) the first HIC material has substantially the same selectivity as Phenyl Sepharose HP under the two-stage HIC conditions; and b) the second HIC material has substantially the same selectivity as Toyopearl Phenyl 650M under the two-stage HIC conditions. 8. The process according to claim 1 , wherein a) the first HIC material is Phenyl Sepharose HP; and/or b) the second HIC material is Toyopearl Phenyl 650M. 9. The process according to claim 1 , comprising the further step of: d) eluting the oligo-PEGylated protein from the first HIC material to provide a first HIC eluate. 10. The process according to claim 9 , wherein eluting the oligo-PEGylated protein from the first HIC material comprises a linear gradient elution. 11. The process according to claim 1 , wherein i. the two-stage HIC conditions are at a conductivity of about 54-55 mS/cm; and/or ii. eluting the mono-PEGylated protein from the second HIC material is at a conductivity of about 40-41 mS/cm; and/or iii. eluting the oligo-PEGylated protein from the first HIC material is carried out by linear gradient from about 54-55 mS/cm to about 1-5 mS.cm and wherein optionally the protein is EPO. 12. The process according to claim 1 , wherein the process is carried out using a mixture of buffer A and buffer B, wherein buffer A comprises 25 mM HEPES, pH 7.5, 500 mM Na 2 SO 4 , and wherein buffer B comprises 25 mM HEPES, pH 7.5, and wherein i. the two stage HIC conditions are at about 13.5% buffer B; and/or ii. eluting the mono-PEGylated protein from the second HIC material is at about 40% buffer B; and/or iii. eluting the oligo-PEGylated protein from the first HIC material is carried out by linear gradient from about 13.5% to about 80% buffer B and wherein optionally the protein is EPO. 13. The process according to claim 1 , wherein elution of the mono-PEGylated protein from the second HIC material comprises a step elution, optionally followed by a gradient elution. 14. The process according to claim 1 , wherein the mono-PEGylated protein composition comprises at least about 99% mono-PEGylated protein. 15. The process according to claim 1 , wherein the protein mixture comprises at least 10% oligo-PEGylated protein. 16. The process according to claim 1 , wherein mono-PEGylated protein comprises a PEG residue having a molecular weight of at least about 20 kDa. 17. The process according to claim 1 , wherein the mono-PEGylated protein composition is a pharmaceutical composition, the process further comprising formulating the second HIC eluate with a pharmaceutical excipient.
the organic macromolecular compound being a polyoxyalkylene oligomer, polymer or dendrimer, e.g. PEG, PPG, PEO or polyglycerol · CPC title
Erythropoietin [EPO] · CPC title
placed in series · CPC title
Ion-exchange chromatography · CPC title
Partition-, reverse-phase or hydrophobic interaction chromatography · CPC title
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