Systems and methods for exchange of buffer solutions
Systems and methods for exchanging buffer solutions are disclosed. In accordance with some embodiments, the methods and systems for buffer exchange may be automated and/or the methods and systems may include mixing during filtering operations.
1. An automated method for exchange of buffer solutions from admixtures comprising a first buffer solution and a biological component, the method comprising:
providing a plurality of individual reservoirs containing an admixture comprising a biological component and a first buffer solution, wherein each reservoir of the plurality of individual reservoirs contains a semi-permeable membrane;
pressurizing each reservoir to force the first buffer solution through the semi-permeable membranes to produce a filtrate and a buffer-depleted residue;
removing the filtrate from each reservoir;
detecting, for each reservoir, an amount of the removed filtrate that was produced by forcing the first buffer solution through the semi-permeable membranes; and
adding a second buffer solution to each reservoir, an amount of the second buffer solution added to each reservoir being determined by the detected amount of the filtrate that was removed from each reservoir.
2. The method as set forth in claim 1 , further comprising mixing the admixtures to reduce fouling of the semi-permeable membranes.
3. The method as set forth in claim 2 , wherein mixing is performed simultaneously with pressurizing each reservoir to reduce fouling of the semi-permeable membranes while forcing the first buffer solution through the semi-permeable membranes to produce the buffer-depleted residue.
4. The method as set forth in claim 2 , wherein mixing comprises vortexing the admixtures.
5. The method as set forth in claim 4 , wherein vortexing is controlled to maintain a constant flow rate through the semi-permeable membranes.
6. The method as set forth in claim 4 , wherein vortexing is controlled to maintain a minimum flow rate through the semi-permeable membranes.
7. The method as set forth in claim 4 , further comprising controlling the temperature of the admixtures by circulation of a heating or a cooling fluid during vortexing of the admixtures.
8. The method as set forth in claim 1 , comprising adding the second buffer solution in two or more cycles until a target exchange of the first buffer solution is achieved.
9. The method as set forth in claim 1 , wherein the amount of the filtrate removed from each reservoir is detected by sensing a level of the admixture in each reservoir.
10. The method as set forth in claim 1 , wherein the amount of the filtrate that was removed from each reservoir is detected by acoustic sensing, capacitance, light reflectance, displaced air volume, or weight measurement of the removed filtrate.
11. The method as set forth in claim 1 , wherein the detected amount of the filtrate removed from each reservoir is a detected volume.
12. The method as set forth in claim 1 , wherein the biological component is selected from the group consisting of proteins, peptides, antigens, antibodies, enzymes, microorganisms, DNA and RNA.
13. The method as set forth in claim 1 , wherein the biological component is a protein and has a molecular weight of greater than about 20 kDa.
14. The method as set forth in claim 1 , wherein the semi-permeable membranes are characterized by a molecular weight cut off of about 100 kDa or less.
15. The method as set forth in claim 1 , wherein the semi-permeable membranes are characterized by a molecular weight cut off of about 10 kDa or less.
16. The method as set forth in claim 1 , wherein the first or second buffer solution comprises an excipient.
17. The method as set forth in claim 1 , wherein the plurality of individual reservoirs are mounted on a single substrate.
18. The method as set forth in claim 1 , wherein the volumetric ratio of the filtrate removed from each reservoir relative to the second buffer solution added to each reservoir is about 1:1.
19. The method as set forth in claim 1 , wherein the volumetric ratio of the filtrate removed from each reservoir relative to the second buffer solution added to each reservoir is less than 1:1 to dilute the biological component or greater than 1:1 to concentrate the biological component.