AUTOMATED AND DYNAMICALLY ADJUSTABLE GAS MIXER FOR BIOREACTOR SYSTEM
20210230531 · 2021-07-29
Assignee
Inventors
- Giacomo CATTARUZZI (Fagagna (UD), IT)
- Fabio TOMASINO (Tarcento (UD), IT)
- Francesco ARMANI (Udine (UD), IT)
Cpc classification
C12M41/00
CHEMISTRY; METALLURGY
International classification
Abstract
A gas mixer system includes a first line carrying a first gas component, and a first flow rate controller adapted to receive data relating to a measure of a first parameter and adjust a first flow rate of the first gas component based on the measure of the first parameter. The gas mixer system also includes a second line carrying a second gas component, and a second flow rate controller adapted to receive data relating to a measure of a second parameter and adjust a second flow rate of the second gas component based on the measure of the second parameter. The gas mixer system further includes a vessel connected to the first and second flow rate controllers, wherein the first gas component and the second gas component are mixed in the vessel to produce a gas mixture, and at least one outlet port. For example, the gas mixer may be connected to and provide a gas mixture to a bioreactor.
Claims
1. A bioreactor system including: a bioreactor comprising: a bioreactor environment comprising a volume adapted to hold one or more gases; a cell culture disposed in the bioreactor environment; and a sensor adapted to generate a measure of a parameter of the bioreactor environment; and a gas mixer comprising: a first line carrying a first gas component; a first flow rate controller adapted to adjust a first flow rate of the first gas component based on the measure of the parameter; a second line carrying a second gas component; a second flow rate controller adapted to adjust a second flow rate of the second gas component; a vessel connected to the first and second flow rate controllers, wherein the first gas component and the second gas component are mixed in the vessel to produce a gas mixture; and at least one outlet port through which the gas mixture is provided to the bioreactor environment.
2. The bioreactor system of claim 1, wherein: the first gas component includes one of: ambient air, oxygen, carbon dioxide, and nitrogen; and the second gas component includes one of: ambient air, oxygen, carbon dioxide, and nitrogen.
3. The bioreactor system of claim 1, wherein the parameter includes one of: a pressure of the bioreactor environment, a proportion of oxygen in the bioreactor environment, a proportion of carbon dioxide in the bioreactor environment, a proportion of nitrogen in the bioreactor environment, a measure of a growth rate of the cell culture, a pH level of the cell culture, and a temperature in the bioreactor environment.
4. The bioreactor system of claim 3, wherein the sensor comprises one of: a pressure sensor, an oxygen sensor, a carbon dioxide sensor, a nitrogen sensor, a growth rate sensor, a pH sensor, and a temperature sensor.
5. The bioreactor system of claim 1, wherein: the first gas component is carbon dioxide; the parameter is a pH level of the cell culture; and the first flow rate controller is adapted to adjust a first flow rate of the carbon dioxide based on the pH level.
6. The bioreactor system of claim 1, wherein: the first gas component is oxygen; the parameter is a measure of a growth rate of the cell culture; and the first flow rate controller is adapted to adjust a first flow rate of the oxygen based on the measure of the growth rate.
7. The bioreactor system of claim 1, further comprising: a pressure regulator disposed between the vessel and the at least one outlet port.
8. A gas mixer system comprising: a first line carrying a first gas component; a first flow rate controller adapted to: receive data relating to a measure of a first parameter; and adjust a first flow rate of the first gas component based on the measure of the first parameter; a second line carrying a second gas component; a second flow rate controller adapted to: receive data relating to a measure of a second parameter; and adjust a second flow rate of the second gas component based on the measure of the second parameter; a vessel connected to the first and second flow rate controllers, wherein the first gas component and the second gas component are mixed in the vessel to produce a gas mixture; and at least one outlet port through which the gas mixture flows.
9. The gas mixer system of claim 8, wherein: the first gas component includes one of: air, oxygen, carbon dioxide, and nitrogen; and the second gas component includes one of: air, oxygen, carbon dioxide, and nitrogen.
10. The gas mixer system of claim 8, wherein: the first parameter includes one of: a pressure of the bioreactor environment, a proportion of oxygen in the bioreactor environment, a proportion of carbon dioxide in the bioreactor environment, a proportion of nitrogen in the bioreactor environment, a measure of a growth rate of the cell culture, a pH level of the cell culture, and a temperature in the bioreactor environment; and the second parameter includes one of: a pressure of the bioreactor environment, a proportion of oxygen in the bioreactor environment, a proportion of carbon dioxide in the bioreactor environment, a proportion of nitrogen in the bioreactor environment, a measure of a growth rate of the cell culture, a pH level of the cell culture, and a temperature in the bioreactor environment.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0014]
[0015]
[0016]
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
DETAILED DESCRIPTION
[0023] In accordance with an embodiment, a bioreactor system is provided. The bioreactor system includes a bioreactor having a bioreactor environment comprising a volume adapted to hold one or more gases, a cell culture disposed in the bioreactor environment, and a sensor adapted to measure a parameter of the bioreactor environment. The bioreactor system also includes a gas mixer having a first line carrying a first gas component, a first flow rate controller adapted to adjust a first flow rate of the first gas component based on the parameter, a second line carrying a second gas component, a second flow rate controller adapted to adjust a second flow rate of the second gas component, a vessel connected to the first and second flow rate controllers, wherein the first gas component and the second gas component are mixed in the vessel to produce a gas mixture, and at least one outlet port through which the gas mixture is provided to the bioreactor environment.
[0024] In one embodiment, the first gas component includes one of: ambient air, oxygen, carbon dioxide, and nitrogen. The second gas component includes one of: ambient air, oxygen, carbon dioxide, and nitrogen.
[0025] In another embodiment, the parameter includes one of: a pressure of the bioreactor environment, a proportion of oxygen in the bioreactor environment, a proportion of carbon dioxide in the bioreactor environment, a proportion of nitrogen in the bioreactor environment, a measure of a growth rate of the cell culture, a pH level of the cell culture, and a temperature in the bioreactor environment.
[0026]
[0027]
[0028] In accordance with an embodiment, gas mixer 120 is supplied with a 100% CO.sub.2 line at 1.0 Bar (or higher) pressure. The pressurized CO.sub.2 is supplied via inlet port 220. Ambient air is collected from the environment via inlet port 202 and compressed by a diaphragm pump. The ambient air is then filtered and dehumidified (e.g., by air filter 204). Air pressure regulator 208 and CO.sub.2 pressure regulator 221 set pressure in the air line and pressure in the CO.sub.2 line at 0.9 Bar. The filtered/dehumidified air and carbon dioxide are then supplied to air gas flow adjuster 212 and to CO.sub.2 gas flow adjuster 225, respectively. Flow rate is set in order to obtain a 5% and a 95% over the total amount of 400 SCCM:20 SCCM CO.sub.2 and 380 SCCM of Air.
[0029] Air and CO.sub.2 are then mixed in tank 240, which may be, for example, a two-liter (2 L) pressure vessel. Discharge valve 262, which may be, for example, an overpressure actuated discharge valve, is connected to tank 240 and ensures that pressure of the gas mixture does not exceed 0.7 Bar. This serves as an overpressure safety control and as a means to keep the two flow regulators working in their linear control region.
[0030] Gas mix precision pressure regulator 251 is set to 0.5 Bar and connected to tank 240. Gas mix precision pressure regulator 251 provides a regulated 5% CO.sub.2 gas mixture to outlet ports 290.
[0031] In accordance with an embodiment, automated gas mixer 120 provides to bioreactor 150 a gas mixture containing a plurality of components. Information relating to one or more parameters of the bioreactor environment are provided to the gas mixer, and the gas mixer dynamically adjusts the amounts of one or more of the components in the gas mixture based on the information.
[0032]
[0033] Bioreactor environment 330 is an enclosed volume adapted to hold a cell culture in a controlled environment. The enclosed volume can be any structure known in the field for growing cell cultures such as a cell culture bag, a cell culture flask or a cell culture tray. In the illustrative environment, a cell culture is maintained in a cell culture medium 375 within bioreactor environment 330. Bioreactor environment 330 also holds a gas mixture 332. Cell culture medium 375 is exposed to gas mixture 332. An inlet 386 allows gases to enter bioreactor environment 330. An outlet 384 allows gases to leave bioreactor environment 330.
[0034] Bioreactor environment 330 may include one or more sensors adapted to measure selected parameters of the environment. In the illustrative embodiment, a pH sensor 361, an O.sub.2 sensor 363, a CO.sub.2 sensor 365, and a pressure sensor 367 are disposed in bioreactor environment 330. The pH sensor 361 measures a pH level of cell culture medium 375. O.sub.2 sensor 363 measures a level of oxygen within bioreactor environment 330. For example, O.sub.2 sensor 363 may determine a proportion of oxygen in the air within bioreactor environment 330 (e.g., in the form of a percentage). CO.sub.2 sensor 365 measures a level of carbon dioxide within bioreactor environment 330. For example, CO.sub.2 sensor 363 may determine a proportion of carbon dioxide in the air within bioreactor environment 330 (e.g., in the form of a percentage). Pressure sensor 367 measures pressure within bioreactor environment 330.
[0035] In other embodiments, bioreactor 150 may include other types of sensors. For example, bioreactor 150 may include a temperature sensor, a scale adapted to measure a mass of the cell culture, etc.
[0036] Bioreactor 150 also includes a growth rate monitor 340 adapted to measure the growth rate of a cell culture in cell culture medium 375. Growth rate monitor 340 may include one or more cameras adapted to obtain images of the cell culture, and one or more sensors such as a temperature sensor, a scale adapted to measure the mass of the cell culture, etc. Growth rate monitor 340 analyzes images of the cell culture and measurements obtained by one or more sensors and determines a growth rate of the cell culture in cell culture medium 375. Growth rate monitor 340 may include an algorithm for estimating number of cells within a captured image, an algorithm for estimating area covered by cells within the captured image area, and an algorithm for calculating the increase of cells number and cells coverage in a certain amount of time.
[0037] Bioreactor 150 also includes a gas mixer interface 350. Gas mixer interface 350 transmits signals to automated gas mixer 120 based on information obtained by one or more sensors within bioreactor 150. In the illustrative embodiment, gas mixer interface 350 transmits information to automated gas mixer 120 via antenna 353.
[0038] In one embodiment, gas mixer interface 350 may transmit signals to various components of gas mixer 120. For example, gas mixer interface 350 may transmit information relating to one or more parameters (such as oxygen levels, carbon dioxide levels, pH levels, pressure, growth rates, etc.) to air gas flow adjuster 212, CO.sub.2 gas flow adjuster 225, gas mix precision pressure regulator 251, and/or to other components of gas mixer 120.
[0039] In another embodiment, information relating to bioreactor 150 is provided to gas mixer 120 via electrical signals. For example, gas mixer interface 350 may transmit electrical signals to automated gas mixer 120 via one or more wires. The wires may link gas mixer interface to selected components of gas mixer 120. The wires may carry electrical signals containing information relating to measurements obtained by pH sensor 361, O.sub.2 sensor 363, CO.sub.2 sensor 365, pressure, the cell culture growth rate determined by growth rate monitor 340, and other parameters.
[0040] One or more components of automated gas mixer 120 receive information from bioreactor 150 and adjust the flow of selected gases, pressure levels of selected gases, and/or other operating conditions in response to the information. For example, certain components of gas mixer 120 receive information relating to oxygen levels, carbon dioxide levels, pH levels, pressure, growth levels, and/or other parameters, and adjust the flows of one or more gases based on these parameters.
[0041]
[0042]
[0043]
[0044] Gas mixer 120 provides a gas mixture that includes one or more gases to maintain a desired environment within bioreactor 150. For example, in one embodiment, gas mixer 120 may provide a gas mixture that includes two different gases. In another embodiment, gas mixer 120 may provide more than two gases (e.g., CO.sub.2, N.sub.2, O.sub.2) in variable proportions, for example, to optimize cell growth.
[0045] Gas mixer 120 provides to bioreactor 150 a gas mixture that is appropriate for a cell culture maintained within bioreactor 150. For example, gas mixer 120 may provide a “standard” gas mixture containing 95% Air/5% CO.sub.2, which is commonly used for many cell cultures, regardless of substrate-dependent growth or suspension growth. This is due to most cell culture media (CCM) being based on a carbonate buffer. In another embodiment, a 90% Air/10% CO.sub.2 mixture may also be used in other carbonate-based buffered CCMs.
[0046] In accordance with an embodiment, various parameters and conditions associated with the environment within bioreactor 150 are monitored. The gas mixer is controlled based on one or more of these parameters and conditions.
[0047] Advantageously, the gas mixer 120 functions in a manner that is very simple, very precise, and robust compared to other commercial solutions that we tested.
[0048] It has been observed that because the environment within a bioreactor is dynamic, it can be challenging to maintain desired proportions of different gases within a bioreactor environment. Advantageously, the inventive bioreactor system monitors selected parameters within the bioreactor environment and dynamically adjusts the proportions of components in the gas mixture provided to the bioreactor environment based on the measured parameters, in order to maintain one or more desired conditions within the bioreactor environment.
[0049] In accordance with an embodiment, active controls are implemented in order allow the gas mixer to be adaptive with respect to the environment inside the bioreactor where cells are growing. Gas mixer 120 may adjust the proportion of a selected component of a gas mixture based on measurements of one or more parameters of the bioreactor environment.
[0050] For example, in one embodiment, components of the gas mixture provided to bioreactor 150 are dynamically adjusted based on a measure of the pH level within the cell culture medium maintained in bioreactor 150.
[0051] At step 510, a gas mixture that includes carbon dioxide and at least one other gas is provided to a bioreactor environment. Gas mixer 120 provides a gas mixture to bioreactor 150. The gas mixture is provided to bioreactor environment 330 via inlet 386.
[0052] While the gas mixture is provided to bioreactor 150, the pH level of the cell culture medium within the bioreactor environment is monitored. For example, pH level within the cell culture medium may be measured by pH sensor 361. In one embodiment, pH sensor includes a contactless pH estimation subsystem.
[0053] At step 520, a measurement of a pH level of a cell culture medium within the bioreactor is obtained. In the illustrative embodiment of
[0054] Referring to
[0055] At step 530, the proportion of carbon dioxide in the gas mixture is adjusted based on the pH level. For example, when a decrease of pH is detected, the gas mixer may be controlled in order to alter (e.g., increase) the CO.sub.2 percentage in the bioreactor. More specifically, if the pH level is below a predetermined level, the proportion of CO.sub.2 within the gas mixture provided to the bioreactor is increased to a selected level. In the illustrative embodiment, CO.sub.2 gas flow adjuster 225 may increase the proportion of carbon dioxide added to the gas mixture in response to the pH level measurement data.
[0056] At step 540, the gas mixture with the adjusted proportion of carbon dioxide is provided to the bioreactor environment. Gas mixer 120 provides the adjusted gas mixture to bioreactor 150. Referring to
[0057] In another embodiment, a level of carbon dioxide in the bioreactor environment (e.g., a percentage of CO.sub.2 in the air within the bioreactor) is monitored. For example, this parameter may be measured by the CO.sub.2 sensor 365.
[0058] In another embodiment, a level of oxygen in the bioreactor environment (e.g., a percentage of O.sub.2 in the air within the bioreactor) is monitored. For example, this parameter may be measured by the O.sub.2 sensor 363.
[0059] In accordance with an embodiment, the growth rate of the cell culture is monitored. This may be calculated, for example, using an integrated imaging system and confluency estimation SW, and, given the desired timing in which a certain confluency percentage is to be reached (es. x % in y days), may influence gas mixture composition. Imaging system may correspond to a lens or a group of lenses providing appropriate magnification to visualize cells, a light source to provide appropriate illumination of the area to be photographed, and a sensor to acquire photographs. Photographs are elaborated by a SW which provides an estimation of number of cells contained within the area of the acquired image, or an estimation of cell confluency (that is, percentage of area covered by cells over the total area of the acquired image). Growth rate is provided by calculating the increase of cells number or cells confluency in a certain amount of time.
[0060] In one embodiment, components of the gas mixture provided to bioreactor 150 are dynamically adjusted based on a measure of the growth rate of a cell culture within the cell culture medium maintained in bioreactor 150.
[0061] For example, if cell growth is determined to be below a predetermined level, oxygen level may be altered (e.g., decreased) to promote cell growth. It is well known that low oxygen concentrations (3-5%) enhance growth of mesenchymal stem cells (and other primary cells). Therefore, in one embodiment, in order to achieve a low oxygen concentration, CO.sub.2, O.sub.2 and N.sub.2 (and no air) may be mixed together. In another embodiment, a mixture of air and carbon dioxide may be adjusted by decreasing the proportion of air in the mixture in order to achieve low oxygen levels.
[0062]
[0063] At step 610, a gas mixture that includes oxygen and at least one other gas is provided to a bioreactor environment. Gas mixer 120 provides a gas mixture to bioreactor 150. The gas mixture is provided to bioreactor environment 330 via inlet 386.
[0064] While the gas mixture is provided to bioreactor 150, the growth rate of the cell culture in cell culture medium 375 within bioreactor environment 330 is monitored by growth rate monitor 340.
[0065] At step 620, a measure of the growth rate of the cell culture within the bioreactor is obtained. In the illustrative embodiment of
[0066] In the illustrative embodiment, suppose, for example, that the measured growth rate of the cell culture is (or falls) below a predetermined, desired level.
[0067] At step 630, the proportion of oxygen in the gas mixture is adjusted based on the growth rate level. For example, if the growth rate is determined to be below a predetermined level, the proportion of air within the gas mixture provided to the bioreactor may be decreased to a selected level (e.g., from an atmospheric level of 21% to as low as 5%). The decrease in the proportion of ambient air will in turn decrease the proportion of oxygen within the gas mixture if the other gas flow parameters remain unchanged. As known to those skilled in the art, cells cultured in low oxygen environment (i.e., subjected to hypoxia) will typically grow faster, live longer, and show lower stress. In the illustrative embodiment, air gas flow adjuster 212 may decrease the proportion of ambient air added to the gas mixture in response to the growth rate data.
[0068] At step 640, the gas mixture with the adjusted proportion of oxygen is provided to the bioreactor environment. Gas mixer 120 provides the adjusted gas mixture (with decreased oxygen levels) to bioreactor 150. Referring to
[0069] In accordance with an embodiment, the settings on gas mixer 120 related to various parameters, including percentages of selected gases (e.g., CO.sub.2, O.sub.2, N.sub.2), pressure, and flow rates, are continuously recorded and used to provide a profile (plot) of the gas mixture administered to the bioreactor over time.
[0070]
[0071] The foregoing Detailed Description is to be understood as being in every respect illustrative and exemplary, but not restrictive, and the scope of the invention disclosed herein is not to be determined from the Detailed Description, but rather from the claims as interpreted according to the full breadth permitted by the patent laws. It is to be understood that the embodiments shown and described herein are only illustrative of the principles of the present invention and that various modifications may be implemented by those skilled in the art without departing from the scope and spirit of the invention. Those skilled in the art could implement various other feature combinations without departing from the scope and spirit of the invention.