US2016100570A1PendingUtilityA1

Ultra-high density cell banking methods

Assignee: GENZYME CORPPriority: Sep 18, 2014Filed: Sep 17, 2015Published: Apr 14, 2016
Est. expirySep 18, 2034(~8.2 yrs left)· nominal 20-yr term from priority
C12M 23/14C12M 27/16C12M 29/10C12N 5/0603A01N 1/142A01N 1/162A01N 1/125A01N 1/10A01N 1/0221C12M 3/06C12M 23/26
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Claims

Abstract

Provided are methods for the creation of ultra-high density cryopreserved cell banks. In certain embodiments, these methods employ altered perfusion culture techniques that allow for production of ultra-high density cell cultures that can be cryopreserved at unexpectedly high cell densities without the need for any cell concentration steps, while retaining excellent cell viability and quality.

Claims

exact text as granted — not AI-modified
1 . A method for producing an ultra-high density frozen cell bank directly from a population of cultured cells, the method comprising:
 a) culturing cells in a perfusion bioreactor to obtain an ultra-high density cell population with a concentration of at least about 1.0×10̂8 cells/mL, wherein the perfusion bioreactor is coupled to a cell retention system; and   b) adding cryoprotectant to the ultra-high density cell population to produce an ultra-high density frozen cell bank, wherein the ultra-high density frozen cell bank has a concentration of at least about 1.0×10̂8 cells/mL, and   
       wherein no additional concentrating step is performed between culturing the cells and adding cryoprotectant to the ultra-high density cell population. 
     
     
         2 . The method of  claim 1 , wherein the cell retention system comprises an alternating tangential flow filtration system comprising a filter. 
     
     
         3 . The method of  claim 2 , wherein the filter has a surface area of at least about 0.08 m 2 . 
     
     
         4 . The method of  claim 3 , wherein the filter has a surface area of about 0.3 m 2  to about 0.5 m 2 , about 0.5 m 2  to about 1.0 m 2 , about 0.7 m 2  to about 0.8 m 2 , about 1.0 m 2  to about 2.0 m 2 , about 2.0 m 2  to about 3.0 m 2 , about 3.0 m 2  to about 4.0 m 2 , or about 4.0 m 2  to about 5.5 m 2 . 
     
     
         5 . The method of  claim 2 , wherein the filter has a pore size selected from the group consisting of 0.7 μm, 1.2 μm, and 7 μm. 
     
     
         6 . The method of  claim 1 , wherein the ultra-high density cell population has a cell density selected from the group consisting of about 1.0×10̂8 cells/mL, about 1.1×10̂8 cells/mL, about 1.2×10̂8 cells/mL, about 1.3×10̂8 cells/mL, about 1.4×10̂8 cells/mL, about 1.5×10̂8 cells/mL, about 1.6×10̂8 cells/mL, about 1.7×10̂8 cells/mL, about 1.8×10̂8 cells/mL, about 1.9×10̂8 cells/mL, and about 2.0×10̂8 cells/mL. 
     
     
         7 . The method of  claim 1 , wherein adding cryoprotectant comprises adding dimethyl sulphoxide (DMSO) to the ultra-high density cell population at a final concentration of about 5% to about 10%, vol/vol. 
     
     
         8 . The method of  claim 1 , wherein the production of a high density cell bank comprises freezing at least a portion of the ultra-high density cell population in a container appropriate for storage under cryopreservation conditions. 
     
     
         9 . The method of  claim 8 , wherein the container is a vial. 
     
     
         10 . The method of  claim 9 , wherein the ultra-high density frozen cell bank comprises about 4.5×10̂8 cells/vial. 
     
     
         11 . The method of  claim 8 , wherein the container is a cryobag. 
     
     
         12 . The method of  claim 11 , wherein the ultra-high density frozen cell bank comprises about 100×10̂8 cells/cryobag. 
     
     
         13 . The method of  claim 1 , wherein the ultra-high density frozen cell bank has a cell density of at least about 1.1 10̂8 cells/mL. 
     
     
         14 . The method of  claim 1 , wherein the perfusion rate in the perfusion bioreactor is between about 0.02 nL/cell/day to about 0.5 nL/cell/day. 
     
     
         15 . The method of  claim 1 , wherein the perfusion rate in the perfusion bioreactor is between 0 and 15 reactor volumes per day. 
     
     
         16 . The method of  claim 1 , wherein the perfusion bioreactor cell culture has a pH of between about 6.8 to about 7.2. 
     
     
         17 . The method of  claim 1 , wherein the perfusion bioreactor cell culture has a dissolved oxygen concentration (DO) of at least about 30%. 
     
     
         18 . The method of  claim 1 , wherein the bioreactor is a flexible bag bioreactor. 
     
     
         19 . The method of  claim 1 , wherein the ultra-high density frozen cell bank has a post-thaw cell viability of at least about 60%, at least about 70%, at least about 80%, at least about 90%, or at least about 95%. 
     
     
         20 . The method of  claim 1 , wherein the cells are mammalian cells. 
     
     
         21 . The method of  claim 20 , wherein the mammalian cells are selected from the group consisting of: CHO, CHO-DBX11, CHO-DG44, CHO-S, CHO-K1, Vero, BHK, HeLa, COS, MDCK, HEK-293, NIH-3T3, W138, BT483, Hs578T, HTB2, BT20, T47D, NS0, CRL7030, HsS78Bst cells, PER.C6, SP2/0-Ag14, and hybridoma cells. 
     
     
         22 . The method of  claim 1 , wherein the cells are transfected cells. 
     
     
         23 . The method of  claim 1 , wherein the cells express a therapeutic protein. 
     
     
         24 . The method of  claim 1 , wherein:
 a) the perfusion bioreactor comprises a flexible bag bioreactor;   b) the filter has a filter surface area of at least 0.08 m 2  and a molecular mass cut off (MWCO) size of at least 50 kDa;   c) the cryoprotectant added to the ultra-high density cell population is DMSO; and   d) the ultra-high density frozen cell bank comprises about 5% to about 10%, vol/vol DMSO.   
     
     
         25 . The method of  claim 1 , wherein the pH and DO of the culture are controlled by automated methods. 
     
     
         26 . The method of  claim 1 , wherein the pH and DO of the culture are controlled by non-automated methods. 
     
     
         27 . The method of  claim 26 , wherein the pH and DO are controlled through any one or more of the following: adjustment of the mixture of gases that are introduced to the culture, adjustment of the rock rate of the bioreactor, or adjustment of the rock angle of the bioreactor. 
     
     
         28 . The method of  claim 27 , wherein the bioreactor is rocked at 25 rpm with a rock angle of 12°. 
     
     
         29 . The method of  claim 27 , wherein the bioreactor is rocked at 22 rpm with a rock angle of 10°. 
     
     
         30 . The method of  claim 1 , wherein the ultra-high density cell population is cooled to and maintained at a temperature of about 4° C. prior to and during the addition of the cryoprotectant and dispensing. 
     
     
         31 . The method of  claim 1 , wherein the ultra-high density cell population is maintained at a temperature of about 20° C. to about 26° C. prior and during the addition of the cryoprotectant and dispensing. 
     
     
         32 . The method of  claim 1 , wherein the ultra-high density cell population is maintained at an uncontrolled cold temperature by using an ice water bath prior to and during the addition of the cryoprotectant and dispensing. 
     
     
         33 . The method of  claim 1 , wherein the bioreactor comprises a built-in filter.

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