Tandem purification of proteins
View Patent ↗The present disclosure provides methods for purifying products from a fluid. In some embodiments, provided purification methods use a combination of purification modes (e.g., protein A and ion exchange) operated in tandem, wherein at least one of the modes utilizes weak partitioning. In some embodiments, provided purification methods operate under robust conditions in which a degree of binding between a product and resin is maintained despite variations in operating parameters.
1. A method of recovering a purified protein product from a load fluid, the method comprising:
a) providing a first column comprising a first resin, wherein the first resin comprises protein A;
b) providing a second column comprising a second resin, wherein the second resin comprises an anion exchange resin, wherein the first column is arranged in tandem with the second column;
c) exposing the load fluid comprising a protein product to the first column under conditions in which the product binds to the first resin;
d) recovering fluid comprising the product from the first resin to produce a first eluate;
e) titrating the first eluate with a titrant continuously as it passes to the second resin, wherein the titrant comprises a pH buffer and at least 150 mM of a salt, and wherein the titrant is added at a target volumetric ratio to the first eluate such that there is a change in partition coefficient of less than 20% when the actual volumetric ratio of the first eluate to the titrant varies up to about 40% from the target volumetric ratio;
f) exposing the titrated eluate to the second column under conditions in which the product binds to the second resin; and
g) recovering fluid comprising the product from the second resin to produce a second eluate, thereby recovering the purified protein product from the load fluid.
2. The method of claim 1 , wherein the first eluate is titrated with the titrant in a volumetric ratio of between about 95:5 to 80:20.
3. The method of claim 1 , wherein a first pump delivers the load fluid to the first resin, a second pump delivers the titrant to the first eluate, and wherein the pumps are operated at a ratio of flow rates that varies by less than 30%.
4. The method of claim 1 , wherein the titrant and first eluate are passed through a mixer, prior to exposure to the second resin.
5. The method of claim 1 , wherein the method comprises detecting pH of the titrated eluate, prior to exposure to the second resin.
6. The method of claim 1 , wherein the titrated eluate is passed through a filter, prior to exposure to the second resin.
7. The method of claim 1 , wherein solids are removed from the load fluid by precipitation.
8. The method of claim 1 , wherein the load fluid comprises cell culture medium.
9. The method of claim 1 , wherein the protein comprises an antigen-binding portion of an antibody.
10. The method of claim 1 , wherein the first resin selectively binds immunoglobulins.
11. The method of claim 1 , wherein the titrant alters one or more conditions of the first eluate such that product in the titrated eluate binds to the second resin in a weak partitioning mode.
12. The method of claim 11 , wherein the conditions of the titrated eluate and the resin are such that the partition coefficient of the product for the resin is 0.1-20.
13. The method of claim 1 , wherein the titrant has a pH which is 0.5 pH units above a pH at which the anion exchange resin binds to product in the titrated eluate in a weak partitioning mode.
14. The method of claim 1 , wherein the titrant increases ionic strength of the eluate of the first resin such that the product maintains binding to the second resin over a range of titrant volume additions.
15. The method of claim 1 , wherein the method comprises treating the load fluid, the first eluate, or the second eluate with one or more virus reduction treatments.
16. The method of claim 1 , wherein the method comprises treating the load fluid, the first eluate, or the second eluate with one or more viscosity reducing treatments.
17. The method of claim 1 , wherein the second resin is an anion exchange resin, and wherein the product is recovered from the first resin in a fluid comprising a buffer which has a pKa that is near conditions under which the product elutes from the resin and a buffer having a pKa near conditions under which the product binds to the second resin in a weak partitioning mode.