Counter-pressure filtration of proteins
View Patent ↗A method is disclosed for filtering a protein in a liquid mixture in a manner that does not substantially damage or otherwise limit the recovery of the protein in the filtration filtrate. The method generally includes passing a liquid mixture containing a protein (e.g., an aqueous vWF mixture) through a filter while applying a counter pressure to the liquid mixture filtrate to accurately reduce and control the pressure differential across the filter. The disclosed method has the advantage that relatively high filtration flow rates can be achieved at relatively low pressure differentials, in contrast to high pressure differentials, which actually reduce the filtration flow rate of protein liquid mixtures. Further, the method can recover substantially all of the protein that is initially present in the liquid mixture.
1. A method of filtering a liquid protein mixture, the method comprising:
providing a liquid mixture at a first pressure (P 1 ), the liquid mixture comprising a carrier liquid, a protein at a first concentration (C 1 ) relative to the carrier liquid, and a dispersed contaminant;
passing the liquid mixture through a filter to form a filtrate at a second pressure (P 2 ), the filtrate comprising the carrier liquid and the protein at a second concentration (C 2 ) relative to the carrier liquid, wherein P 1 is greater than ambient pressure and less than about 1 bar gauge, P 2 is greater than ambient pressure and less than P 1 , and the filter is sized to remove at least a portion of the dispersed contaminant from the liquid mixture; and,
applying a counter pressure to the filtrate to ensure that a pressure differential between the first and second pressures (P 1 −P 2 ) is not more than about 300 mbar, wherein at least about 85% of the protein present in the liquid mixture is recovered in the filtrate.
2. The method of claim 1 , wherein the pressure differential is not more than about 90 mbar.
3. The method of claim 1 , wherein at least about 95% of the protein present in the liquid mixture is recovered in the filtrate.
4. The method of claim 3 , wherein at least about 99% of the protein present in the liquid mixture is recovered in the filtrate.
5. The method of claim 1 , wherein the first pressure (P 1 ) is at least about 200 mbar gauge.
6. The method of claim 1 , wherein the carrier liquid comprises water.
7. The method of claim 1 , wherein the dispersed contaminant comprises a microorganism.
8. The method of claim 1 , wherein the filtrate is substantially free of the dispersed contaminant.
9. The method of claim 1 , wherein the filter comprises a porous membrane, the porous membrane comprising pores sized from about 0.1 μm to about 0.5 μm.
10. The method of claim 9 , wherein the pores are sized at about 0.2 μm or about 0.22 μm.
11. A method of filtering a liquid protein mixture, the method comprising:
providing a liquid mixture at a first pressure (P 1 ), the liquid mixture comprising a carrier liquid, a protein at a first concentration (C 1 ) relative to the carrier liquid, and a dispersed contaminant;
passing the liquid mixture through a filter to form a filtrate at a second pressure (P 2 ), the filtrate comprising the carrier liquid and the protein at a second concentration (C 2 ) relative to the carrier liquid, wherein P 1 is greater than ambient pressure and less than about 1 bar gauge, P 2 is greater than ambient pressure and less than P 1 and the filter is sized to remove at least a portion of the dispersed contaminant from the liquid mixture; and,
applying a counter pressure to the filtrate sufficient to yield an average filtrate flow rate of at least about 300 g/min·m 2 of filter surface area, wherein at least about 85% of the protein present in the liquid mixture is recovered in the filtrate.
12. The method of claim 11 , wherein at least about 95% of the protein present in the liquid mixture is recovered in the filtrate.
13. The method of claim 12 , wherein at least about 99% of the protein present in the liquid mixture is recovered in the filtrate.
14. The method of claim 11 , wherein the carrier liquid comprises water.
15. The method of claim 11 , wherein the dispersed contaminant comprises a microorganism.
16. The method of claim 11 , wherein the filtrate is substantially free of the dispersed contaminant.
17. The method of claim 11 , wherein the filter comprises a porous membrane, the porous membrane comprising pores sized from about 0.1 μm to about 0.5 μm.
18. The method of claim 17 , wherein the pores are sized at about 0.2 μm or about 0.22 μm.
19. A method of filtering a liquid protein mixture, the method comprising:
providing a liquid mixture at a first pressure (P 1 ), the liquid mixture comprising a carrier liquid, a protein at a first concentration (C 1 ) relative to the carrier liquid, and a dispersed contaminant;
passing the liquid mixture through a filter to form a filtrate at a second pressure (P 2 ), the filtrate comprising the carrier liquid and the protein at a second concentration (C 2 ) relative to the carrier liquid, wherein P 1 is greater than ambient pressure and less than about 1 bar gauge, P 2 is greater than ambient pressure and less than P 1 , and the filter is sized to remove at least a portion of the dispersed contaminant from the liquid mixture; and,
applying a counter pressure to the filtrate to ensure that a pressure differential between the first and second pressures (P 1 −P 2 ) is not more than about 300 mbar and to yield an average filtrate flow rate of at least about 300 g/min·m 2 of filter surface area, wherein at least about 85% of the protein present in the liquid mixture is recovered in the filtrate.
20. The method of claim 19 , wherein the protein comprises a blood coagulation factor.
21. The method of claim 20 , wherein the blood coagulation factor is von Willebrand factor (vWF).
22. The method of claim 20 , wherein the blood coagulation factor is Factor VIII.
23. The method of claim 20 , wherein at least 90% of the activity of the blood coagulation factor present in the liquid mixture is recovered in the filtrate.