Antibody process

Patent metadata

Field	Value
Publication number	US-2016347833-A1
Application number	US-201515114655-A
Country	US
Kind code	A1
Filing date	Feb 6, 2015
Priority date	Feb 7, 2014
Publication date	Dec 1, 2016
Grant date	—

Abstract

The present invention provides a method for removing unwanted antibody aggregates, and/or antibody dimers, and/or antibody pre-monomers.

First claim

1 . A method for removing antibody pre-monomers from an aqueous recombinant antibody solution, wherein said method comprises a step of separating the pre-monomers and optionally antibody dimers from monomeric antibodies using hydrophobic interaction chromatography (HIC).

2 . A method according to claim 1 , comprising the steps of
i) obtaining an antibody preparation comprising a pre-monomer component, ii) loading said antibody preparation to a hydrophobic interaction chromatography (HIC) column, iii) allowing binding of the antibody and the pre-monomer to the column material, iv) sequentially eluting the antibody components of the preparation, and v) selecting eluate fractions that do not comprise (substantial amount of) the pre-monomer and thereby obtaining a composition of monomeric antibodies.

3 . The method according to claim 2 , wherein the monomeric antibodies are obtained in the fractions eluting prior to the fractions including a high content of pre-monomer.

4 . The method according to claim 2 , wherein the monomeric antibodies are obtained in the fractions eluting prior to the fractions including the majority of pre-monomers and antibody dimers.

5 . The method according to claim 2 , wherein the pre-monomer is removed by deselecting eluate fractions when the accumulation of pre-monomers and other aggregates reaches around 1%.

6 . The method according to claim 1 , wherein said antibody is an IL-21 antibody.

7 . The method according to claim 1 , wherein the HIC column material has a binding capacity of 50 g antibody/L or more and/or wherein the HIC column material comprises 4-8% cross-linked agarose comprising a covalently coupled phenyl group and/or wherein the HIC column material comprises 20-45 μMol phenyl groups/ml.

8 . The method according to claim 1 , wherein said method comprises the step of loading said antibody on the HIC column in the presence of an ammonium sulphate concentration of 0.8-1.5 mol/kg, and subsequently eluting said antibody from the HIC column with a decreasing ammonium sulphate gradient.

9 . The method according to claim 8 , wherein the monomeric antibody is obtained in the eluate fractions obtained when the ammonium sulphate concentration is decreasing from 0.8 mol/kg to 0.4 mol/kg.

10 . The method according to claim 1 , wherein said method results in reduction of virus particles.

11 . A method according to claim 1 , wherein said method comprises the following steps:
a. expressing an antibody in a host cell, wherein said host cell comprises a vector encoding said antibody, b. collecting cell media comprising said antibody from step (a), c. binding antibodies from the cell media obtained in step (b) on a protein A affinity column, and eluting said antibodies 10 mmol formic acid/kg at pH 3.5, d. loading the eluate obtained in step (c) on a cation exchange chromatography column (CIEX), and eluting said antibodies with a NaCl gradient, e. subjecting the eluate obtained in step (d) to virus filtration, f. pumping the filtered eluate obtained in step (e) on a flow through membrane, g. loading the filtered eluate obtained in step (f) on a hydrophobic interaction chromatography column in the presence of 0.8-1.5 mol/kg ammonium sulphate concentration, and h. eluting said antibodies with a decreasing ammonium sulphate gradient, i. concentrating said antibodies in the eluate obtained in step (g) by ultrafiltration and diafiltration, and j. adding surfactant to the concentrated eluate obtained in step (h).

12 . A method for preparing an antibody composition comprising at most 1% antibody aggregates (HMWP total), comprising removing antibody pre-monomers from an aqueous recombinant antibody solution by using hydrophobic interaction chromatography (HIC).

13 . The method according to claim 12 , wherein pre-monomers and optionally antibody dimers are separated from monomeric antibodies using hydrophobic interaction chromatography (HIC).

14 . (canceled)

15 . A pharmaceutical product obtained by a process according to claim 1 .

16 . The method according to claim 6 , wherein the IL-21 antibody comprises the three CDR sequences as set forth in SEQ ID NO: 2 and the three CDR sequences as set forth in SEQ ID NO: 3.

17 . The method according to claim 2 , wherein the HIC column material has a binding capacity of 50 g antibody/L or more and/or wherein the HIC column material comprises 4-8% cross-linked agarose comprising a covalently coupled phenyl group and/or wherein the HIC column material comprises 20-45 μMol phenyl groups/ml.

18 . The method according to claim 2 , wherein said method comprises the step of loading said antibody on the HIC column in the presence of an ammonium sulphate concentration of 0.8-1.5 mol/kg, and subsequently eluting said antibody from the HIC column with a decreasing ammonium sulphate gradient.

19 . The method according to claim 18 , wherein the monomeric antibody is obtained in the eluate fractions obtained when the ammonium sulphate concentration is decreasing from 0.8 mol/kg to 0.4 mol/kg.

20 . The method according to claim 2 , wherein said antibody is an IL-21 antibody.

21 . The method according to claim 20 , wherein the IL-21 antibody comprises the three CDR sequences as set forth in SEQ ID NO: 2 and the three CDR sequences as set forth in SEQ ID NO: 3.

Assignees

• Novo Nordisk As

Inventors

• Jensen Ole Elvang
• Chadfield Mark Simon

Classifications

• C07K2317/34

  Identification of a linear epitope shorter than 20 amino acid residues or of a conformational epitope defined by amino acid residues · CPC title

• C07K1/18

  Ion-exchange chromatography · CPC title

• C07K1/20

  Partition-, reverse-phase or hydrophobic interaction chromatography · CPC title

• C07K1/34

  by filtration, ultrafiltration or reverse osmosis · CPC title

• C07K1/22

  Affinity chromatography or related techniques based upon selective absorption processes · CPC title