New developments in online OUR monitoring and its application to animal cell cultures.

The increasing demand for biopharmaceuticals produced in mammalian cells has driven the industry to enhance the productivity of bioprocesses through intensification of culture process. Fed-batch and perfusion culturing strategies are considered the most attractive choices, but the application of these processes requires the availability of reliable online measuring systems for the estimation of cell density and metabolic activity. This manuscript reviews the methods (and the devices used) for monitoring of the oxygen consumption, also known as oxygen uptake rate (OUR), since it is a straightforward parameter to estimate viable cell density and the physiological state of cells. Furthermore, as oxygen plays an important role in the cell metabolism, OUR has also been very useful to estimate nutrient consumption, especially the carbon (glucose and glutamine) and nitrogen (glutamine) sources. Three different methods for the measurement of OUR have been developed up to date, being the dynamic method the golden standard, even though DO and pH perturbations generated in the culture during each measurement. For this, many efforts have been focused in developing non-invasive methods, such as global mass balance or stationary liquid mass balance. The low oxygen consumption rates by the cells and the high accuracy required for oxygen concentration measurement in the gas streams (inlet and outlet) have limited the applicability of the global mass balance methodology in mammalian cell cultures. In contrast, stationary liquid mass balance has successfully been implemented showing very similar OUR profiles compared with those obtained with the dynamic method. The huge amount of studies published in the last years evidence that OUR have become a reliable alternative for the monitoring and control of high cell density culturing strategies with very high productivities.

A new strategy for fed-batch process control of HEK293 cell cultures based on alkali buffer addition monitoring: comparison with O.U.R. dynamic method.

The increasing demand for biopharmaceuticals produced in mammalian cells has driven the industry to enhance productivity of bioprocesses through different strategies. This is why fed-batch and perfusion cultures are considered more attractive choices than batch processes. In this context, the availability of reliable online measuring systems for cell density and metabolic activity estimation will help the application of these processes. The present work focuses on the comparison of two different monitoring tools for indirect estimation of biomass concentration in a HEK293 cell cultures producing IFN-γ: on one side, the oxygen uptake rate (O.U.R.) determination, by means of application of the dynamic method measurement which is already a widely used tool and, on the other side, a new robust online monitoring tool based on the alkali buffer addition used to maintain the pH set point. Both strategies allow a proper monitoring of cell growth and metabolic activity, with precise identification of the balanced cell growth and the most important action in the process, as is the media feeding. The application of these monitoring systems in fed-batch processes allows extending the growth of HEK293 cells, which in turn results in higher final cell concentrations compared with Batch strategy (7 · 106 cells mL-1), achieving 14 · 106 cells mL-1 for the fed-batch based on O.U.R. and 19 · 106 cells mL-1 for the fed-batch based on the alkali addition. Product titter is also increased in respect of the batch strategy (3.70 mg L-1), resulting in 8.27 mg L-1 when fed-batch was based on O.U.R. and 11.49 mg L-1 when it was based on the alkali buffer strategy. Results prove that fed-batch strategy based on the alkali buffer addition is a robust online monitoring method that has shown its great potential to optimize the feeding strategy in HEK293 fed-batch cultures.

Effect of continuous feeding of CO2 and pH in cell concentration and product titers in hIFNγ producing HEK293 cells: Induced metabolic shift for concomitant consumption of glucose and lactate.

Although pH control at physiological levels is generally considered as the optimal culture condition, in some cases other strategies should be taken into account for their beneficial effects on process performance. pH and CO2 levels are chemical variables that have a major impact in cell growth and product titers in cell culture since their effect on key metabolic routes. HEK293 cells expressing recombinant hIFNγ showed different metabolic behavior when cultured in shake flask compared to pH-controlled bioreactors, in which a decrease in cell density and product titer were observed. This yield loss observed in bioreactor cultures could be reverted by adding 1% CO2 to air inlet flow in a non-controlled pH bioprocess. With this strategy, a significant outcome of 4-fold increase in terms of maximum cell density and 2-fold increase in volumetric concentration of recombinant protein (hIFNγ) when compared to the pH-controlled culture in bioreactor (standard culture conditions) has been obtained. Results evidenced the importance of pH and CO2 concentration in this case, in order to reproduce the behavior observed in optimization experiments performed in shake flasks. Thus, it was demonstrated that not always constant controlled variable setpoint (like pH or CO2 addition) becomes the best bioprocess performance strategy.

Electrical impedance spectroscopy measurements using a four-electrode configuration improve on-line monitoring of cell concentration in adherent animal cell cultures.

This paper describes the improvement in the use of electrical impedance spectroscopy (EIS) for animal cell concentration monitoring of adherent cultures by using a four-electrode configuration instead of the commonly used two-electrode configuration. This four-electrode configuration prevents cell concentration measurements from external masking effects such as the electrode covering ratio, the degree of cellular adherence to the electrodes and the impedance of the measuring electrodes. Cell concentration was monitored using both four-electrode and two-electrode configurations in vero cell and human mesenchymal stem cell cultures in order to analyze the attained improvement in two cell lines with opposite growth characteristics. The experiments performed with vero cell cultures evidenced that the four-electrode configuration enables cell concentration measurements along all culture phases, even once the culture reached cell confluence (over 2×10(5) cells/cm(2)), confirming that this configuration is less effected by all the external influences. The experiments performed with human mesenchymal stem cells demonstrated good sensitivity of the measurement at very low cell concentrations, as well as a very good robustness all over the 12-days experiment. Finally, off-line cell measurements during cell cultures proved good accuracy of impedance measurements carried out with a four-electrode configuration along all cell growth phases, enabling determination of relevant cell growth parameters.

Optimization of HEK-293S cell cultures for the production of adenoviral vectors in bioreactors using on-line OUR measurements.

The culture of HEK-293S cells in a stirred tank bioreactor for adenoviral vectors production for gene therapy is studied. Process monitoring using oxygen uptake rate (OUR) was performed. The OUR was determined on-line by the dynamic method, providing good information of the process evolution. OUR enabled cell activity monitoring, facilitating as well the determination of the feeding rate in perfusion cultures and when to infect the culture. Batch cultures were used to validate the monitoring methodology. A cell density of 10×10(5)cell/mL was infected, producing 1.3×10(9) infectious viral particles/mL (IVP/mL). To increase cell density values maintaining cell specific productivity, perfusion cultures, based on tangential flow filtration, were studied. In this case, OUR measurements were used to optimize the dynamic culture medium feeding strategy, addressed to avoid any potential nutrient limitation. Furthermore, the infection protocol was defined in order to optimize the use of the viral inoculum, minimizing the uncontrolled release of particles through the filter unit mesh. All these developments enabled an infection at 78×10(5)cell/mL with the consequent production of 44×10(9)IVP/mL, representing a cell specific productivity 4.3 times higher than for the batch culture.

Application of on-line OUR measurements to detect actions points to improve baculovirus-insect cell cultures in bioreactors.

The continuous monitoring of a process based on the culture of Sf9 insect cells and infection by a baculovirus as a vector to obtain recombinant VP2 protein is studied. On-line OUR determination is based on the direct oxygen measurement in the cell culture vessel and the application of the dynamic method. This approximation allows a proper description of cell growth, with precise identification of the balanced cell growth end and the most important action times in the process, as virus infection time and final cell harvesting. A detailed study of the OUR profiles allows on-line monitoring of the effects of infection and expression protein process, a tool enabling the automatisation of the protein production process in a baculovirus-insect cell system. These parameters have been defined as time of action (TOAs), and include the most relevant actions to take in these type of processes: time of infection (TOI), time of feeding (TOF) and time of harvesting (TOH).

Multiple automated minibioreactor system for multifunctional screening in biotechnology.

The current techniques applied in biotechnology allow to obtain many types of molecules that must be tested on cell cultures (high throughput screening HTS). Although such tests are usually carried out automatically on mini or microwell plates, the procedures in the preindustrial stage are performed almost manually on higher volume recipients known as bioreactors. The growth conditions in both stages are completely different. The screening system presented in this work is based on the multiwell test plates philosophy, a disposable multiple minibioreactor that allows reproduction of industrial bioreactor culture conditions: aeration, stirring, temperature, O2, pH and visible range optical absorbance measurements. It is possible to reproduce the growth conditions for both suspended and adherent animal cell types using 1 to 10 ml vol. bioreactors. In the case of bacteria or yeast, it is not possible to achieve a high biomass concentration, due to the reduced head volume air supply.

On-line monitoring of yeast cell growth by impedance spectroscopy.

The application of impedance spectroscopy to estimate on-line cell concentration was studied. The estimation was based on the relative variation between electrical impedance measured at low (10 kHz) and high frequencies (10 MHz). Studies were carried out to characterise the influence of changes in physical and chemical parameters on the impedance measurement. Two different possibilities to perform on-line measurements were tested: a simple set-up, based on an in situ probe, gave good results but was not suitable for high agitation and aeration rates. An ex situ flow-through on-line measuring cell was used to overcome these problems, showing a better performance. The use of this set-up for the growth monitorisation of a Saccharomyces cerevisiae culture showed an efficient performance, having the correlation between estimated and measured S. cerevisiae a Pearson coefficient of 0.999.