IP Library Granted Patent US 11,339,377
Granted Patent B2
US 11,339,377 · App. 16/762,119 · Granted May 24, 2022

SO3 chromatography for use in a method for virus purification

Inventors: Markus Wolschek (Vienna, AT); Manfred Reiter (Vienna, AT); Ales Strancar (Ajdovscina, SI); Mojca Tajnik Sbaizero (Bagnaria Arsa, IT)
Assignee: BLUESKY IMMUNOTHERAPIES GMBH
C12N7/00C12N2760/16152C12N2760/16252
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 11,339,377
App. No.
16/762,119
Granted
May 24, 2022
Kind
B2
Abstract

The present invention refers to a process for purifying virus particles from cell culture, comprising the steps of subjecting the cell culture to centrifugation to get a supernatant fraction of virus particles, incubating said fraction with a nuclease, diluting the fraction with low conductivity buffer, subjecting said diluted fraction to a SO3 chromatography step, performing a washing step with low conductivity buffer, and eluting virus particles.

Claims (25)

1. A process for purifying virus particles from cell culture, comprising the steps in the following order:

a) subjecting the cell culture to centrifugation to obtain a supernatant fraction of virus particles,

b) incubating the supernatant fraction with a nuclease,

c) diluting the supernatant fraction with a low conductivity dilution buffer to obtain a diluted fraction,

d) subjecting the diluted fraction to a SO3 chromatography step,

e) performing a washing step with low conductivity wash buffer, wherein the wash buffer has a conductivity of 12 mS/cm or less, and

f) eluting virus particles.

2. The process of claim 1 , wherein the virus is an influenza virus.

3. The process of claim 1 , wherein the virus particles are diluted after elution.

4. The process according to claim 1 , wherein an ultra and/or sterile filtration is performed after elution.

5. The process according to claim 1 , wherein the SO3 chromatography step is a column chromatography step.

6. The process according to claim 1 , wherein the dilution buffer has a conductivity of 5 mS/cm or less.

7. The process according to claim 1 , wherein the wash buffer further contains EDTA.

8. The process according to claim 1 , wherein the dilution buffer or the wash buffer comprises a component selected from the group consisting of Hepes, Tris, Tris base, potassium phosphate, sodium phosphate, Mops, Bis-Tris propane Bicine, Mes and Bis-Tris.

9. The process according to claim 1 , wherein the dilution buffer or the wash buffer further contains sucrose, sorbitol and/or mannitol.

10. The process according to claim 1 , wherein virus is eluted with a stepwise elution or linear gradient elution.

11. The process according to claim 2 , wherein the influenza virus is selected from the group consisting of influenza A, influenza B and influenza C virus.

12. The process according to claim 11 , wherein the influenza virus is selected from the group consisting of a wild type influenza virus and an influenza virus containing modifications, wherein the modifications comprise substitution mutations, insertions and/or deletions.

13. The process according to claim 1 , wherein centrifugation is performed at a speed of is least 2,000 g, at least 3,000 g, at least 4,000 g, or at least 4,100 g.

14. The process according to claim 1 , wherein cell culture is performed with Vero cells.

15. The process according to claim 1 , wherein at least 50%, at least 60%, at least 70%, at least 80%, at least 85%, at least 90%, at least 95%, or at least 99% of cell protein is removed.

16. The process according to claim 1 , wherein at least 50%, at least 60%, at least 70%, at least 80%, at least 85%, at least 90%, at least 95%, or at least 99% of cell DNA is removed.

17. The process according to claim 5 , wherein the column chromatography step is performed with a methacrylate monolith column.

18. The process according to claim 6 , wherein the dilution buffer has a conductivity of 1 mS/cm or less.

19. The process according to claim 10 , wherein the linear gradient elution is a sodium chloride gradient elution.

Assignments (4)
CHANGE OF NAME Recorded Dec 30, 2022
From: BIA SEPARATIONS D.O.O.
To: SARTORIUS BIA SEPARATIONS D.O.O.
Reel/Frame 062254/0148 →
CHANGE OF NAME Recorded Jul 8, 2020
From: BLUE SKY VACCINES GMBH
To: BLUESKY IMMUNOTHERAPIES GMBH
Reel/Frame 053155/0739 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 29, 2020
From: STRANCAR, ALES; SBAIZERO, MOJCA TAJNIK
To: BIA SEPARATIONS D.O.O
Reel/Frame 052793/0940 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 29, 2020
From: WOLSCHEK, MARKUS; REITER, MANFRED
To: BLUE SKY VACCINES GMBH
Reel/Frame 052796/0994 →
Priority Claims (1)
EP 17200517 · Nov 8, 2017 · regional
Continuity (1)
Related Publication 20200332264A1 · Oct 22, 2020