Continuous production of recombinant proteins
A technology of recombinant protein and bioreactor, applied in the direction of immunoglobulin, specific-purpose bioreactor/fermenter, biochemical instrument, etc., can solve problems such as limited experience
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Embodiment 1
[0063] Embodiment 1: Continuous production of recombinant protein
[0064] A 100-L booster perfusion bioreactor coupled with dual ATF was used to produce recombinant monoclonal antibodies (mAbs) over a 70-day time course. Cell-free mAb-containing medium (harvest) was continuously pumped to a 100-L harvest buffer vessel for further processing.
[0065] Capture using a 2X 1-L (8x 20cm) prepacked and irradiated Protein A affinity column operated in bind and elute MCC mode on a pilot-scale steam-in-place PCC slide Medium containing antibodies. The capture step was performed such that one of the two columns was always loaded from the harvest buffer vessel and the average inlet volumetric flow rate to the capture step matched the average outlet volumetric flow rate from the perfusion bioreactor. The loading on the Protein A column was controlled by ΔUV to approximately 3% breakthrough. Prior to virus inactivation, separate trap column eluates were collected in a 5-L mixing vessel...
Embodiment 2
[0071] Embodiment 2: Continuous production of recombinant protein
[0072] A 100-L booster perfusion bioreactor coupled with dual ATF was used to produce recombinant monoclonal antibodies (mAbs) over a 27 day time course. Cell-free mAb-containing medium (harvest) was continuously pumped to a 100-L harvest buffer vessel for further processing.
[0073] Using a 2X 1-L (8x20cm) prepacked and irradiated Protein A affinity column operated in bind and elute MCC mode on a pilot-scale steam-in-place PCC slide to capture the protein A affinity column containing Antibody medium. The capture step was performed such that one of the two columns was always loaded from the harvest buffer vessel and the average inlet volumetric flow rate to the capture step matched the average outlet volumetric flow rate from the perfusion bioreactor. The loading on the Protein A column was controlled by ΔUV to approximately 3% breakthrough. Prior to virus inactivation, separate trap column eluates were co...
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