Microbioreactor for continuous cell culture

• US 20060199260A1
• Filed: 09/26/2005
• Published: 09/07/2006
• Est. Priority Date: 05/01/2002
• Status: Abandoned Application

• Current Assignee: Massachusetts Institute of Technology
• Original Assignee: Massachusetts Institute of Technology
• Inventors: Zhang, Zhiyu, Choi, Hyun-Goo, Jensen, Klavs F., Sinskey, Anthony J., Boccazzi, Paolo
• Application Number:
  US11/236,453
• Publication Number:
  US 20060199260A1
• Time in Patent Office: Days
• US Class Current: 435/293.1
• CPC Class Codes: B01F 33/30 Micromixers
• CPC Class Codes: B01F 33/453 using supported or suspended stirring elements
• CPC Class Codes: B01L 2300/0822 Slides
• CPC Class Codes: B01L 2300/0887 Laminated structure
• CPC Class Codes: B01L 2300/10 Means to control humidity and/or other gases
• CPC Class Codes: B01L 3/502707 characterised by the manufacture of the container or its components by shaping or joining plastic parts B29C59/00, B29C65/00; by laminating B32B37/00; manufacture of microstructural devices in general B81C
• CPC Class Codes: B01L 3/502715 characterised by interfacing components, e.g. fluidic, electrical, optical or mechanical interfaces
• CPC Class Codes: B01L 3/502723 characterised by venting arrangements
• CPC Class Codes: B01L 7/00 Heating or cooling apparatus autoclaves B01J3/04; Heat insulating devices
• CPC Class Codes: B82Y 30/00 Nanotechnology for materials or surface science, e.g. nanocomposites
• CPC Class Codes: C12M 23/16 Microfluidic devices; Capillary tubes integrated microfluidic structures B01L3/5027; microreactors B01J19/0093
• CPC Class Codes: C12M 23/24 Gas permeable parts
• CPC Class Codes: C12M 23/34 Internal compartments or partitions
• CPC Class Codes: C12M 27/02 Stirrer or mobile mixing elements
• CPC Class Codes: C12M 29/04 Filters; Permeable or porous membranes or plates, e.g. dialysis
• CPC Class Codes: C12M 41/26 of pH
• CPC Class Codes: C12M 41/32 of substances in solution
• CPC Class Codes: G01N 33/48707 by electrical means G01N33/49, G01N33/493 take precedence

Abstract

The present invention microscale bioreactors (microfermentors) and microscale bioreactor arrays for use in culturing cells. The microfermentors include a vessel for culturing cells and means for providing oxygen to the interior of the vessel at a concentration sufficient to support cell growth, e.g., growth of bacterial cells. Depending on the embodiment, the microfermentor vessel may have various interior volumes of less than approximately 1 ml. The microfermentors may include an aeration membrane and optionally a variety of sensing devices. Methods of using the microfermentors, e.g., to select optimum cell strains or bioprocess parameters are provided. The microbioreactors having a variety of different designs, some of which incorporate active fluid mixing and/or have the capability to operate in batch, fed-batch, or continuous mode. In certain embodiments the microreactors operate as microchemostats. Methods for culturing cells under chemostat conditions in a microbioreactor are also provided.

Claims

1. A microbioreactor comprising comprising:

at least one culture vessel having an interior volume of less than 1 ml;

a mechanism for actively mixing the contents of the culture vessel;

an inflow port to allow fresh culture medium to be continuously supplied to the culture vessel; and

an outflow port to allow culture medium to be continuously removed from the culture vessel at the same rate as fresh medium is supplied, such that a constant fluid volume and constant growth conditions are maintained within the culture vessel for a prolonged period of time after cells cultured in the culture vessel reach a steady state.

138. The microbioreactor of claim 1, wherein the microbioreactor is capable of operating as a microchemostat.

139. The microbioreactor of claim 1, wherein the mechanism for actively mixing the contents of the culture vessel comprises a stirbar.

140. The microbioreactor of claim 1, wherein at least a portion of a wall of the culture vessel comprises a gas-permeable membrane.

141. The microbioreactor of claim 1, further comprising:

an internal sensor that detects or measures dissolved oxygen within the vessel; and

an internal sensor that detects or measures pH within the vessel.

142. The microbioreactor of claim 1, further comprising an inflow channel or tube in communication with the inflow port and an outflow channel or tube in communication with the outflow port.

143. The microbioreactor of claim 142, wherein the inflow channel flows through a portion of the microbioreactor that inhibits cell growth within and movement of living cells into or through at least a portion of the inflow channel.

144. The microbioreactor of claim 142, further comprising means for inhibiting cell growth within, and movement of living cells into or through, at least a portion of the inflow channel or tube.

145. The microbioreactor of claim 144, wherein the means comprises one or more items selected from the group consisting of:

(i) a heating element, (ii) a device that emits electromagnetic radiation sufficient to kill cells, and (iii) a filter having a pore size selected to prevent passage of cells through the filter.

146. The microbioreactor of claim 142, further comprising:

a collection chamber in communication with the outflow channel; and

a second channel or tube in communication with the outflow channel.

147. The microbioreactor of claim 142, wherein the collection chamber is located in a portion of the microbioreactor that maintains conditions that inhibit metabolic activity of cells within the collection chamber.

148. The microbioreactor of claim 146, further comprising means for inhibiting metabolic activity of cells within the collection chamber.

149. The microbioreactor of claim 148, wherein the means comprises one or more items selected from the group consisting of:

(i) a cooling element;

(ii) a second channel or tube in communication with the collection chamber and a supply of a cytostatic or cytotoxic agent, so that the chamber is supplied with a cytotoxic or cytostatic agent that inhibits metabolic activity of cells within the collection chamber.

150. A culture system comprising the microbioreactor of claim 1, further comprising:

means for collecting an optical signal from the interior of the culture vessel.

151. The microbioreactor of claim 1, wherein the interior of the culture vessel comprises a well located at least in part within a first body layer of material.

152. The microbioreactor of claim 151, wherein the well is located entirely within the first body layer of material.

153. The microbioreactor of claim 151, wherein the inflow port and outflow port are in communication with channels located at least in part within the first body layer.

154. The microbioreactor of claim 151, further comprising a second body layer having a void therein, wherein the first and second body layers are separated by a gas-permeable membrane and are positioned such that the void in the second body layer is separated from the well in the first body layer by the gas-permeable membrane, so that gas is exchanged between the interior of the culture vessel and the external environment.

155. The microbioreactor of claim 154, further comprising a layer of material covering the void, so that the void and the covering layer define an enclosed headspace located substantially opposite the interior of the culture vessel.

156. The microbioreactor of claim 151, wherein the first body layer is substantially made of a rigid material.

157. The microbioreactor of claim 151, further comprising:

a second body layer having a void therein; and

a third body layer having a void therein and located between the gas-permeable membrane and the second body layer, wherein both the second and third body layers are positioned such that the voids in the second and third body layers are located substantially opposite one another and separated from the well in the first body layer by the gas-permeable membrane, so that gas is exchanged between the interior of the culture vessel and the external environment.

158. The microbioreactor of claim 157, further comprising a layer of material covering the void in the second body layer, so that the void and the covering layer define an enclosed headspace located substantially opposite the interior of the culture vessel.

159. The microbioreactor of claim 157, wherein the first and second body layers are substantially made of a rigid substance.

160. The microbioreactor of claim 157, wherein the third body layer serves as a gasket for the gas-permeable membrane.

161. The microbioreactor of claim 157, further comprising a substrate layer that supports the first body layer.

162. The microbioreactor of claim 151, wherein the first body layer comprises a central section in which the well is located and one or more sections spaced apart from the central portion but physically connected thereto by one or more connecting elements.

163. The microbioreactor of claim 162, wherein at least one channel extends from the culture vessel through a connecting element and into an adjacent section.

164. The microbioreactor of claim 162, wherein at least one of the sections comprises a zone that inhibits cell movement, cell growth, or both, and through which a medium inflow channel passes.

165. The microbioreactor of claim 164, wherein the zone that inhibits cell movement, cell growth, or both is located within a section spaced apart from the section in which the well is located.

166. The microbioreactor of claim 164, wherein the zone is heated to a temperature sufficient to substantially inhibit bacterial chemotaxis.

167. The microbioreactor of claim 162, wherein a section that is spaced apart from the section in which the well is located comprises a zone that inhibits cell metabolism and that contains a sample collection chamber.

168. The microbioreactor of claim 167, wherein the zone is cooled to a temperature sufficiently low to a temperature low enough to substantially inhibit cell metabolism.

169. The microbioreactor of claim 1, wherein the microbioreactor optionally comprises one or more channels in communication with the culture vessel, and wherein at least a portion of an interior surface of the culture vessel, at least a portion of an interior surface of one or more of the channels, or both, is modified to resist adherence of cells, proteins, or both.

170. The microbioreactor of claim 169, wherein the modification comprises attachment of a polymer containing PEG to the surface.

171. The microbioreactor of claim 170, wherein the polymer is a polymer comprising a poly(acrylic acid) backbone with PEG-containing side chains grafted thereto.

172. The microbioreactor of claim 171, wherein the polymer is a PAA-g-(PEG-r-PPG) comb polymer.

173. A culture system comprising the microbioreactor of claim 1, further comprising a pumping system.

174. A culture system comprising the microbioreactor of claim 1, further comprising:

a medium reservoir in communication with the culture vessel and elevated above it so as to create pressure that drives medium into and out of the culture vessel.

187. A method of selecting a strain that produces a desired product or degrades an unwanted compound comprising steps of:

culturing a plurality of different strains, each in a microbioreactor of claim 1;

measuring the amount of the desired or unwanted product in each of the microbioreactors; and

selecting a strain that produces an optimum amount of a desired product or degrades a maximum amount of the unwanted compound.

188. A method of selecting a bioprocess parameter comprising steps of:

culturing cells of an organism type in a plurality of individual microbioreactors of claim 1 under constant growth conditions, wherein the microbioreactors are operated under conditions in which the value of the bioprocess parameter varies between the individual microbioreactors and wherein the organism produces a product or degrades a compound;

monitoring biomass, product formation, or compound degradation in each of the microbioreactors; and

identifying the value of the bioprocess parameter that results in optimum biomass, optimum product formation, or optimum compound degradation.

189. The method of claim 188, in which the bioprocess parameter is actively controlled.

190. A method of performing a fermentation comprising:

culturing cells in a production scale fermentor, wherein one or more bioprocess parameters for the production scale fermentor is selected according to the method of claim 188.

2-137. -137. (canceled)

175. A method of performing cell culture comprising:

introducing at least one cell into a microbioreactor that comprises a culture vessel having an interior volume of less than 1 ml;

continuously flowing fresh culture medium into the vessel while continuously removing culture medium containing cells from the culture vessel at the same rate as that with which fresh medium enters the vessel so that a constant medium volume is maintained in the culture vessel;

actively mixing the contents of the culture vessel;

maintaining the cells for sufficient time to achieve a first steady state.

176. The method of claim 175, further comprising:

maintaining the at least one cell under constant culture conditions for an additional period of time.

177. The method of claim 175, wherein the cells produce a product used in the pharmaceutical, food, and/or chemical industries.

178. The method of claim 177, wherein the product is selected from the group consisting of:

primary and secondary metabolites, enzymes, recombinant proteins, and vaccine antigens.

179. The method of claim 175, further comprising altering the dissolved oxygen concentration in the medium in the culture vessel, altering the mass transfer coefficient (k_La) of oxygen into the medium in the culture vessel, altering the composition of the medium entering the culture vessel, altering the pH of the contents of the culture vessel, or any combination of the foregoing.

180. The method of claim 175, further comprising measuring cell density, dissolved oxygen, pH, or any combination of the foregoing while culturing the at least one cell.

181. The method of claim 175, further comprising introducing medium into the culture vessel through an inflow channel or tube and inhibiting cell growth within, and movement of living cells into or through, at least a portion of the inflow channel or tube.

182. The method of claim 175, further comprising collecting cells in a collection chamber in communication with the culture vessel and inhibiting metabolic activity of cells within the collection chamber.

183. The method of claim 175, further comprising:

collecting one or more samples of the medium that is removed from the vessel in the continuous removal step; and

performing an analytical procedure on the sample or samples.

184. The method of claim 183, further comprising selecting a cell strain or bioprocess parameter based on the result of the analytical procedure.

185. The method of claim 175, further comprising:

altering the medium inflow and outflow rates, oxygenation rate, pH, composition, or any combination of the foregoing, so as to alter the growth conditions in the culture vessel; and

maintaining the culture for a time sufficient to reach a second steady state.

186. The method of claim 175, further comprising steps of:

collecting one or more samples of the medium that is removed from the vessel in the continuous removal step while the culture is in the first steady state;

collecting one or more samples of the medium that is removed from the vessel in the continuous removal step while the culture is in the second steady state; and

performing an analytical procedure on the sample or samples removed in the first and second steady states.

191. A method of modifying a polymeric surface other than a PDMS surface so as to confer resistance to adherence of cells, proteins, or both, comprising steps of:

assembling an amine-terminated self assembled monolayer on the surface; and

contacting the surface with a PEG-containing polymer under conditions in which the PEG-containing polymer contains sufficient negative charges to cause adsorption to the self-assembled monolayer.

192. The method of claim 191, wherein the polymeric surface is PMMA or poly(carbonate).

193. The method of claim 191, wherein the PEG-containing polymer comprises a PAA or PMAA backbone.

194. The method of claim 191, further comprising the step of:

generating free OH groups on the polymeric surface prior to assembling the amine-terminated self-assembled monolayer.

195. An apparatus comprising at least one polymeric surface modified according to the method of claim 191.