BIOPROCESS DEVICE ASSEMBLY AND INOCULATION METHOD

Abstract

A bioprocess device assembly includes at least a first bioreactor and a second bioreactor, and a transfer system for transferring a certain volume of a medium contained in the first bioreactor into the second bioreactor. A biomass sensor is associated to the first bioreactor. A control unit is configured for receiving measurement data from the biomass sensor and controlling the transfer system. An inoculation method makes use of such a device assembly wherein the biomass sensor measures at least one parameter of biomass contained in the first bioreactor; the biomass sensor sends measurement data to the control unit; and the control unit evaluates the measurement data and, based on an evaluation of the measurement data decides whether the viable cell density is sufficient for inoculation, determines a necessary inoculation volume, and controls the transfer system to transfer the determined inoculation volume from the first bioreactor into the second bioreactor.

Claims

1. A bioprocess device assembly, comprising: at least a first bioreactor and a second bioreactor, a transfer system for transferring a certain volume of a medium contained in the first bioreactor into the second bioreactor, a biomass sensor associated to the first bioreactor for measuring at least one parameter relating to a quantity and/or a quality of biomass contained in the first bioreactor, and a control unit configured for receiving measurement data from the biomass sensor and controlling the transfer system, the control unit being parametrized such that, based on an evaluation of the measurement data received from the biomass sensor, the control unit: (a) decides whether a biomass status is sufficient for inoculation, (b) determines a necessary inoculation volume, and (c) controls the transfer system to transfer the determined inoculation volume from the first bioreactor into the second bioreactor.

2. The bioprocess device assembly according to claim 1, characterized in that the biomass sensor is capable of measuring capacitance.

3. The bioprocess device assembly according to claim 1, characterized in that the biomass sensor is capable of measuring at least one of the following: electrical impedance; oxygen transmission rate; oxygen uptake rate; scattered light; radiation intensity; concentration of a metabolite; metabolite consumption rate; product formation rate.

4. The bioprocess device assembly according to claim 1, characterized in that the biomass sensor and the control unit are configured for monitoring the at least one parameter and controlling the transfer system in real-time.

5. The bioprocess device assembly according to claim 1, characterized in that the transfer system includes at least one of the following controllable conveyor devices: a pump; a pneumatic drive; a gravimetric feeder.

6. An inoculation method performed within a bioprocess, the method making use of a device assembly according to claim 1 and comprising the following steps: the biomass sensor constantly or repeatedly measures at least one parameter relating to the quantity and/or quality of the biomass contained in the first bioreactor; the biomass sensor sends measurement data to the control unit; and the control unit evaluates the measurement data received from the biomass sensor and, based on an evaluation of the measurement data; (a) decides whether the biomass status is sufficient for inoculation, (b) determines a necessary inoculation volume, and (c) controls the transfer system to transfer the determined inoculation volume from the first bioreactor into the second bioreactor.

7. The method according to claim 6, characterized in that the steps of evaluating the measurement data received from the biomass sensor and controlling the transfer system to transfer the determined inoculation volume from the first bioreactor into the second bioreactor are performed in real-time.

8. The method according to claim 6, characterized in that the necessary inoculation volume is calculated based on the evaluated measurement data of the biomass sensor.

9. The method according to claim 6, characterized in that the transfer of the inoculation volume is performed based on one of the following driving principles: hydraulic pressure; pneumatic pressure; gravity.

10. The method according to claim 6, characterized in that the first bioreactor is operated in a perfusion mode.

11. The method according to claim 6, characterized in that initial conditions in the second bioreactor and/or process control and process parameters of the second bioreactor are adapted or adjusted depending on at least one of the following: an amount or concentration of a metabolite in the transferred inoculation volume; one or more physicochemical characteristics of the transferred inoculation volume.

12. The method according to claim 6, characterized in that the method is performed multiple times with a cascade of pre-culture bioreactors.

13. The method according to claim 6, wherein the one or more physicochemical characteristics of the transferred inoculation volume include at least one of pH, oxygen saturation, or temperature.

14. The method according to claim 6, wherein the biomass status is a viable cell density.

15. The bioprocess device assembly according to claim 1, wherein the biomass status is a viable cell density.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0023] Further features and advantages of the invention will become apparent from the following description and from the accompanying drawings to which reference is made. In the drawings:

[0024] FIG. 1 shows an example setup of a bioprocess device assembly according to the invention using a control system;

[0025] FIG. 2 shows an example correlation between viable cell density and capacitance; and

[0026] FIG. 3 shows generally a cascade of a plurality of controlled bioreactors in an assembly according to the invention.

DETAILED DESCRIPTION OF THE INVENTION

[0027] FIG. 1 schematically depicts a possible setup of a bioprocess device assembly 10 for performing an inoculation within a fed-batch bioprocess. The bioprocess device assembly 10 includes at least two bioreactors 12, 14. The first bioreactor 12 is used as a seed bioreactor (N−1 stage) and preferably operated in a perfusion mode, while a second bioreactor 14 is used as a fed-batch bioreactor (N stage). The bioreactors 12, 14 shown in FIG. 1 are both rocking motion (RM) bioreactors.

[0028] The first bioreactor 12 is equipped with a biomass sensor 16 for measuring at least one parameter relating to the quantity and/or quality of the biomass contained in the first bioreactor 12. The biomass sensor 16 preferably is or includes a capacitance sensor. In addition, or alternatively, the biomass sensor 16 may be capable of measuring at least one of the following parameters or any derivative thereof: electrical impedance; oxygen transmission rate (OTR); oxygen uptake rate (OUR); scattered light; radiation intensity; concentration of a metabolite (e.g., glucose); metabolite (e.g., glucose) consumption rate; product formation rate.

[0029] A transfer system 18 makes it possible to transfer a medium contained in the first bioreactor 12 into the second bioreactor 14. In the example embodiment shown in FIG. 1 the transfer system 18 includes a hose line 20 connecting the two bioreactors 12, 14 and a controllable pump 22 integrated in the hose line 20. However, other automatically or semi-automatically controllable transfer concepts may be employed. In particular, the transfer system 18 may also include a pneumatic drive, a gravimetric feeder, or the like.

[0030] The biomass sensor 16 and the transfer system 18 are connected to a control unit 24 which is configured for receiving measurement data from the biomass sensor 16 and for controlling the transfer system 18. The control unit 24 can be a specific unit mainly dedicated for these purposes, or it can be a flexible digital control unit which is generally capable of performing a variety of process control operations. In any event, the control unit 24 may be part of, or connected to, a higher level control system for controlling several or all steps in a bioprocess.

[0031] The control unit 24 is capable of controlling the transfer system 18 such that a previously determined amount of medium contained in the first bioreactor 12, in particular an inoculation volume, is transferred from the first bioreactor 12 into the second bioreactor 14. For exactly measuring the weight or volume of the transferred amount of medium one or more weight and/or volume sensors associated to one or both of the bioreactors 12, 14 are connected to the control unit 24.

[0032] The control unit 24 itself is parametrized such that, based on an evaluation of the measurement data received from the biomass sensor 16 in the first bioreactor 12, the control unit 24 performs the following steps:

[0033] (a) deciding whether the viable cell density (VCD) is sufficient for inoculation,

[0034] (b) determining a necessary inoculation volume, and

[0035] (c) controlling the transfer system 18 to transfer the determined inoculation volume from the first bioreactor 12 into the second bioreactor 14.

[0036] The parametrization of the control unit 24 is based on a known correlation between VCD and the parameter(s) measured by the biomass sensor 16, especially capacitance. The correlation was determined earlier empirically or, especially if empirical data is not available, in parallel to the actual seed steps. The correlation can also be obtained by modelling. The correlation is stored in the control unit 24. An example of a substantially linear correlation between VCD and capacitance is shown in the diagram of FIG. 2.

[0037] The inoculation within the bioprocess is performed as follows. The biomass sensor 16 continuously or repeatedly provides measurement data to the control unit 24, and the control unit 24 continuously or repeatedly evaluates the measurement data in real-time (online monitoring). When the control unit 24 determines, based on the above-mentioned known correlation, that the VCD is sufficient or has reached a desired, pre-determined threshold value, inoculation is immediately and automatically initiated.

[0038] Before the actual medium transfer from the first bioreactor 12 into the second bioreactor 14, the control unit 24 determines a necessary amount of biomass for inoculation (inoculation volume) according to the present circumstances, especially based on the measured VCD. The medium transfer is then automatically activated by the control unit 24.

[0039] In the example embodiment shown in FIG. 1 the transfer of the inoculation volume is mainly performed by operating the pump 22 in the hose line 20 between the two bioreactors 12, 14. Operation of the pump 22 (at least starting and stopping the pump 22) is controlled by the control unit 24. Additionally, valves for opening and closing the bioreactor ports connected to the hose line 20 may also be controlled by the control unit 24. If another type of transfer system is used, e.g., based on a pneumatic drive, a gravimetric feeder, or the like, the control unit 24 controls these components accordingly.

[0040] As soon as the calculated amount of inoculation volume is transferred by the transfer system 18, the control unit 24 automatically terminates the medium transfer based on the measurement data received from the weight and/or volume sensor(s).

[0041] The amount or concentration of metabolites, e.g., glucose, contained in the inoculation volume and/or one or more physicochemical characteristics of the inoculation volume, such as pH, oxygen saturation (dissolved oxygen, DO), temperature etc., are determined by calculation or measurement. Based on the determined value(s), the initial conditions in the second bioreactor 14 are adapted or adjusted accordingly to the new amount of metabolites and/or physicochemical characteristics. The same can be done with the process control and process parameters (PID) of the second bioreactor 14, i.e., they can be adapted or adjusted according to the determined value(s).

[0042] An optional biomass sensor may be provided in the second bioreactor 14 for examining the effectively transferred biomass.

[0043] The above-described concept, or parts of it, can be scaled up as indicated by the dashed lines in FIG. 1. In particular, the transfer of medium between several pre-culture bioreactors (N−x stage to N−x+1 stage) can be automatically initiated and automatically performed as described above with the same control unit 24 or several control units. A corresponding cascade of controlled bioreactors is generally shown in FIG. 3.

LIST OF REFERENCE SIGNS

[0044] 10 bioprocess device assembly [0045] 12 first bioreactor [0046] 14 second bioreactor [0047] 16 biomass sensor [0048] 18 transfer system [0049] 20 hose line [0050] 22 pump [0051] 24 control unit