IN-SITU CELL RETENTION PERFUSION BIOREACTORS
The bioreactor may include a single-use, rigid-sided bioreactor vessel containing a fluid to be mixed and a vertical mixing wheel. A perfusion dip tube with a screen filter incorporated on the end is secured to the vessel from the top lid and partially submerged in the fluid, preferably into close proximity with an outer circumference of the vertical mixing wheel. The screen filter of appropriate mesh size allows spent cell culture medium to be withdrawn from the bioreactor vessel while retaining cell aggregates or microcarriers on which cells are attached and growing in the vessel. Alternating flow of fluid out from and into the dip tube enables removal of spent medium and unclogging of the dip tube filter.
1 . A perfusion bioreactor, comprising:
a. a vessel having an upper lid and sized to contain a volume of fluid or medium;
b. a vertically-oriented mixing wheel positioned within the vessel and having a horizontally-oriented axle supported within the vessel about which the mixing wheel rotates, the mixing wheel having outer vanes at an outer extent thereof configured to mix the fluid in the vessel;
c. a dip tube extending downward through the upper lid, the dip tube terminating at a lower end in an input/output port covered with a filter, the input/output port and filter being located within 1-3 inches of the outer vanes of the mixing wheel; and
d. a pump system connected to an upper end of the dip tube for alternately causing perfusion outflow through the dip tube from the vessel or inflow through the dip tube into the vessel.
2 . The bioreactor of claim 1 , wherein the pump system is a bi-directional pump connected in line with the dip tube.
3 . The bioreactor of claim 2 , wherein the bi-directional pump is a peristaltic pump.
4 . The bioreactor of claim 1 , wherein the pump system includes two separate pumps each connected to separate lines leading to a branch point at an upper end of the dip tube, and a valve at the branch point connected to enable conversion of flow between the two lines and the dip tube.
5 . The bioreactor of claim 1 , wherein the filter is made of a porous material that is gamma-sterilizable.
6 . The bioreactor of claim 5 , wherein the filter is made of a material selected from the group consisting of sintered polyethylene mesh, polyvinylidene fluoride (PVDF) mesh, and stainless steel mesh.
7 . The bioreactor of claim 1 , wherein the filter is a cylindrical shape with an axis parallel to the horizontally-oriented axle of the mixing wheel.
8 . The bioreactor of claim 7 , wherein the dip tube includes an elongated vertical section that extends down from the upper lid that transitions at a gently curved 90° elbow section to a horizontally-oriented section terminating in the input/output port and filter.
9 . The bioreactor of claim 1 , wherein the input/output port and filter are located above the horizontally-oriented axle of the mixing wheel.
10 . The bioreactor of claim 9 , wherein the input/output port and filter are located at about a 45° angle extending from the horizontally-oriented axle above a horizontal plane through the horizontally-oriented axle.
11 . A perfusion bioreactor, comprising:
a. a single-use vessel having a top edge and sized to contain a volume of fluid or medium, a vertically-oriented mixing wheel positioned within the vessel and having a horizontally-oriented axle supported within the vessel about which the mixing wheel rotates, the mixing wheel having outer vanes at an outer extent thereof configured to mix the fluid in the vessel;
b. a bioreactor system having a frame that receives the single-use vessel, and an upper lid that fits onto the top edge of the vessel and has access ports for a plurality of supply conduits and measurement instruments housed mounted to and controlled by the bioreactor system;
c. a dip tube extending downward through the upper lid, the dip tube terminating at a lower end in an input/output port covered with a filter located adjacent to and parallel to the horizontally-oriented axle of the mixing wheel; and
d. a pump system connected to an upper end of the dip tube for alternately causing perfusion outflow through the dip tube from the vessel or inflow through the dip tube into the vessel.
12 . The bioreactor of claim 11 , wherein the pump system is a bi-directional pump connected in line with the dip tube.
13 . The bioreactor of claim 12 , wherein the bi-directional pump is a peristaltic pump.
14 . The bioreactor of claim 11 , wherein the pump system includes two separate pumps each connected to separate lines leading to a branch point at an upper end of the dip tube, and a valve at the branch point connected to enable conversion of flow between the two lines and the dip tube.
15 . The bioreactor of claim 11 , wherein the mixing wheel has at least one magnetic or ferromagnetic driven element mounted thereon, the bioreactor system further including a drive system positioned outside of the vessel in close proximity therewith having at least one drive element configured to exert either an attractive or repulsive magnetic force to the driven element and rotate the mixing wheel.
16 . The bioreactor of claim 11 , wherein the filter is made of a porous material that is gamma-sterilizable.
17 . The bioreactor of claim 16 , wherein the filter is made of a material selected from the group consisting of sintered polyethylene mesh, polyvinylidene fluoride (PVDF) mesh, and stainless steel mesh.
18 . The bioreactor of claim 11 , wherein the filter is a cylindrical shape with an axis parallel to the horizontally-oriented axle of the mixing wheel.
19 . The bioreactor of claim 18 , wherein the dip tube includes an elongated vertical section that extends down from the upper lid that transitions at a gently curved 90° elbow section to a horizontally-oriented section terminating in the input/output port and filter.
20 . The bioreactor of claim 11 , wherein the input/output port and filter are located above the horizontally-oriented axle of the mixing wheel.
21 . The bioreactor of claim 20 , wherein the input/output port and filter are located at about a 45° angle extending from the horizontally-oriented axle above a horizontal plane through the horizontally-oriented axle.