Shear protectants in harvest microfiltration
The addition of buffer to a harvest stream during diafiltration can cause increased turbidity and have other undesirable effects including limiting product recovery. Methods and compositions related to the use of a non-ionic surfactant are provided for improving diafiltration.
1. A method for harvesting a product from a cell culture by diafiltration, the method comprising
(a) providing a retentate for diafiltration, wherein the retentate is a retentate from harvest microfiltration of a cell culture;
(b) adding a non-ionic surfactant to the retentate; and
(c) performing diafiltration of the retentate, thereby harvesting a product from a cell culture.
2. The method of claim 1 , wherein the non-ionic surfactant is Pluronic® F68.
3. The method of claim 1 , wherein the non-ionic surfactant is polyvinyl alcohol (PVA).
4. The method of claim 1 , wherein the non-ionic surfactant is in a buffer.
5. The method of claim 1 or claim 2 , wherein the non-ionic surfactant is in a buffer and the concentration of the non-ionic surfactant in the buffer is between 0.2 g/L and 4 g/L, 0.2 g/L and 3 g/L, 0.5 g/L and 2.5 g/L, 0.5g/L and 2 g/L, and 0.5 g/L and 1.5 g/L.
6. The method of claim 1 or claim 2 , wherein the concentration of the non-ionic surfactant in the buffer is about 1 g/L or 2.5 g/L.
7. The method of claim 1 or claim 2 , wherein the retentate comprises cells and culture medium.
8. The method of claim 1 or claim 2 , wherein the turbidity of the filtrate resulting from the diafiltration is reduced compared to the diafiltration performed in the absence of non-ionic surfactant.
9. The method of claim 1 or claim 2 , wherein the qualitative or quantitative recovery of a product from the retentate is increased in the presence of the non-ionic surfactant compared to recovery of the product in the absence of the non-ionic surfactant.
10. The method of claim 1 or claim 2 , wherein the retentate comprises a pharmaceutical product.
11. The method of claim 1 or claim 2 , wherein the retentate comprises a recombinant protein.
12. The method of claim 1 or claim 2 , wherein the retentate comprises a buffer isotonic to a cell in the retentate.
13. The method of claim 1 or claim 2 , wherein the retentate comprises phosphate buffered saline (PBS).
14. The method of claim 1 or claim 2 , wherein the diafiltration step occurs at a temperature of about 20° C. to 25° C. 2° C. to 37° C., or 2° C. to 25° C.
15. The method of claim 1 , wherein the diafiltration is discontinuous diafiltration.
16. The method of claim 1 , wherein the diafiltration is constant volume diafiltration.
17. The method of claim 1 , wherein the concentration of the non-ionic surfactant does not substantially change during diafiltration.
18. The method of claim 1 , wherein the non-ionic surfactant is in a cell culture medium.
19. The method of claim 17 , wherein the concentration of non-ionic surfactant is maintained at about 1 g/L.