A PC comprises a measurement unit, a consumption rate calculation unit, a culture medium replacement detection unit, and a next step transition determination unit. The measurement unit acquires the amount of consumed glucose from the result of continuously measuring the concentration of glucose contained in a culture medium (X) of a culture vessel. The consumption rate calculation unit calculates the consumption rate at which glucose is consumed by differentiating the amount of glucose consumed. The culture medium replacement detection unit detects that the culture medium (X) in the culture vessel has been replaced or added. When the culture medium (X) is replaced or added, the next step transition determination unit determines whether or not to proceed to the next step according to whether or not the consumption rate after the replacement or addition of the culture medium (X) calculated by the consumption rate calculation unit satisfies a specific condition.

The invention provided herein relates to methods for protein synthesis, characterisation and purification on a digital microfluidic device.

A method of controlling a bioreactor system includes providing a cell culture in a bioreactor, wherein conditions in the bioreactor enable the cell culture to produce a protein of interest (POI), measuring process parameters (PPs) of the culture within the bioreactor by RAMAN, wherein the process parameters are selected from the group consisting of nutrient concentration, viable cell concentration, and protein attributes, measuring a predetermined weight of the bioreactor with the cell culture, removing cell-free spent media from the cell culture using a first output conduit at a first specified rate, removing cells from the cell culture using a second output conduit at a second specified rate, and introducing one or both of fresh media or nutrients into the cell culture using an input conduit at a third specified rate.

A pre-programmed non-feedback continuous feeding method based on mass balance of the substrate in the bioreactor for use in culture growth and maintenance is provided. The disclosed method does not rely on instrument, probe or operator feedback. The method provides an efficient and effective alternative to bolus feeding.

The present invention relates to cell culture in bioreactors, such as flexible cellbag bioreactors. More closely the invention relates to a method and system for determining the cell density in a bioreactor culture and for controlling the perfusion rate of a suspension culture of cells in a bioreactor, comprising measuring the oxygen uptake of primary mononuclear cells in a non-static bioreactor.

Bioreactor systems and controlled operation of bioreactor systems are disclosed herein. The bioreactor systems can include at least one bioreactor chamber, at least one reservoir, a plurality of sensors, and a fluid circuit. The operational methods disclosed herein are directed towards growing cells or tissue while measuring various parameters, and a controlled operation of the various parameters during the operation of the bioreactor systems. The controlled operation of the parameters includes, for example, cell concentration; a rate of flow; a volume; a pH; a temperature; a level of oxygen; a level of carbon dioxide; a level of bicarbonate ion; nutrient compound; and any combination thereof.

A cell culture control system includes a controller configured to control parameters of a culture fluid which exists in a processor in accordance with a control value which is preliminarily set, a generator configured to generate time-series data by using a concentration value of the metabolic substances in the culture fluid, the concentration value of the metabolic substances being detected by a sensor, an extractor configured to extract a characteristic point of the time-series data generated by the generator, and a control value setter configured to change the control value in accordance with the characteristic point extracted by the extractor.

Generation of bubbles in an organic-substance production apparatus is suppressed. A gas treatment method including: an adsorption step of passing a source gas containing at least carbon dioxide and nitrogen through an adsorption unit housing an adsorbent for adsorbing carbon dioxide to reduce a carbon dioxide concentration in the source gas; a supply step of supplying the source gas whose carbon dioxide concentration has been reduced by the adsorption step to an organic-substance production apparatus that produces an organic substance; and a monitoring step of monitoring a carbon dioxide concentration and a nitrogen concentration in the source gas before passing through the adsorption unit, a carbon dioxide concentration and a nitrogen concentration in the source gas after having passed through the adsorption unit, or a carbon dioxide concentration and a nitrogen concentration in the source gas having been supplied to the organic-substance production apparatus; wherein the adsorption step has an ability regulation step of enhancing an ability of the adsorption unit to reduce a carbon dioxide concentration in the source gas, when a total concentration of the carbon dioxide concentration and the nitrogen concentration monitored in the monitoring step exceeds a threshold value.

High throughput cultivation systems are used in pharmaceutical research and development. In this connection, samples are taken and analyzed for important parameters using external analysis. The results of the analysis serve to assess the cultivation process and provide important information about the process. Especially with cultivations carried out in parallel, the manual effort of sample preparation is great and can lead to errors. In order to avoid the need for sampling and thus to minimize the errors, a method is described in the present patent application which makes desired target parameters accessible in the form of soft sensors by means of previously recorded process variables. Herein is described a method for determining process-relevant parameters in CHO processes (Chinese hamster ovary) in high-throughput cultivations, in particular glucose, lactate and the live cell density or the live cell volume.

The invention concerns a bioreactor for production of virus and virus-like particles (VLPs), methods for production of virus and VLPs, methods for regulating the concentration of molecules inhibitory to viral and VLP yield in a cell culture chamber of a bioreactor, such as the extracapillary space of a hollow fiber bioreactor.