Tangential flow depth filtration systems and methods of filtration using same

Patent metadata

Field	Value
Publication number	US-10767152-B2
Application number	US-201916687864-A
Country	US
Kind code	B2
Filing date	Nov 19, 2019
Priority date	Mar 8, 2018
Publication date	Sep 8, 2020
Grant date	Sep 8, 2020

Abstract

The present disclosure relates to hollow fiber tangential flow filters, including hollow fiber tangential flow depth filters, for various applications, including bioprocessing and pharmaceutical applications, systems employing such filters, and methods of filtration using the same.

First claim

What is claimed is:

1. A bioprocessing system comprising:
a process vessel;
a tangential flow depth filtration (TFDF) unit comprising a thick-walled hollow fiber formed from at least one polymer and comprising a porous wall defining a lumen that is in fluid communication with the process vessel;
a permeate fluid outlet in fluid communication with an exterior surface of the porous wall; and
a pump in fluid communication with the lumen;
wherein a density of the hollow fiber is between 51% and 56% of the density of an equivalent solid volume of the polymer.

2. The bioprocessing system of claim 1 , wherein an average pore size of the thick-walled hollow fiber is about 0.2 μm to about 10 μm.

3. The bioprocessing system of claim 1 , wherein the density is about 53%.

4. The bioprocessing system of claim 1 , wherein the porous wall has a thickness ranging from 2 mm to 7 mm.

5. The bioprocessing system of claim 1 , wherein the pump is configured to provide a pulsed flow of fluid through the lumen.

6. The bioprocessing system of claim 1 , further comprising a polymer coating along an inside of the porous wall of the hollow fiber.

7. The bioprocessing system of claim 6 , wherein the coating is selected from the group consisting of polyolefin, polyethylene, polypropylene, and polyvinylidene fluoride (PVDF).

8. The bioprocessing system of claim 6 , wherein the coating on the porous wall reduces a pore size of the hollow fiber.

9. The bioprocessing system of claim 1 , wherein the hollow fiber comprises bi-component filaments having a core and a coating.

10. The bioprocessing system of claim 9 , wherein the core comprises polyolefin and the coating comprises polyester.

11. The bioproces sing system of claim 9 , wherein the core comprises polyethylene terephthalate and the coating comprises polypropylene.

12. The bioprocessing system of claim 11 , wherein the bi-component filaments are further coated with polyvinylidene fluoride (PVDF).

13. A tangential flow depth filtration (TFDF) unit comprising:
a hollow fiber formed from at least one polymer and comprising a porous wall having a density between 51% and 56% of the density of an equivalent solid volume of the polymer, the porous wall defining a lumen;
an inlet in fluid communication with the lumen; and
a permeate fluid outlet in fluid communication with a permeate chamber comprising an exterior surface of the hollow fiber.

14. The TFDF unit of claim 13 , further comprising a polymer coating along an inside of the porous wall of the hollow fiber.

15. The TFDF unit of claim 14 , wherein the coating is selected from the group consisting of polyolefin, polyethylene, and polypropylene polyvinylidene fluoride (PVDF).

16. The TFDF unit of claim 13 , wherein the hollow fiber comprises bi-component filaments having a core and a coating.

17. A method of filtering a fluid comprising cells, the method comprising:
flowing a fluid comprising the cells from a process vessel into a tangential flow depth filter (TFDF) unit comprising a thick-walled hollow fiber formed from at least one polymer and comprising a porous wall having a pore size and a density between 51% and 56% of the density of an equivalent solid volume of the polymer, the porous wall defining the lumen that is in fluid communication with the process vessel, the TFDF unit having a permeate fluid outlet in fluid communication with the porous wall,
wherein the fluid is separated into a retentate comprising the cells and a permeate, and wherein the retentate is returned to the process vessel.

18. The method of claim 17 , wherein the fluid is a culture medium and the cells of the culture medium have been cultured for a period of at least two days.

19. The method of claim 18 , further comprising the step of adding a fluid volume to the process vessel equivalent to a volume of permeate, thereby maintaining an overall volume of the fluid.

20. The method of claim 17 , wherein the permeate comprises a bioproduct produced by the cells.

21. The method of claim 17 , the TFDF unit further comprising a polymer coating disposed along an inside of the porous wall of the hollow fiber.

22. The method of claim 21 , wherein the coating is selected from the group consisting of polyolefin, polyethylene, and polypropylene polyvinylidene fluoride (PVDF).

23. The method of claim 17 , wherein the hollow fiber comprises bi-component filaments having a core and a coating.

24. The method of claim 17 , wherein the flow of fluid into the TFDF unit is a pulsed flow.

Assignees

• Repligen Corp

Inventors

• Bransby Michael
• Carroll Derek

Classifications

• B01D2325/0283

  Pore size · CPC title

• B01D71/261

  Polyethylene · CPC title

• B01D71/262

  Polypropylene · CPC title

• B01D67/00041

  by sintering · CPC title

• B01D71/48

  Polyesters · CPC title