Use this URL to cite or link to this record in EThOS: https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.790559
Title: Scale-down characterisation of post-centrifuge flocculation processes and the study of its impact upon downstream processing during mammalian cell antibody production
Author: Espuny Garcia del Real, G.
ISNI:       0000 0004 8498 5213
Awarding Body: UCL (University College London)
Current Institution: University College London (University of London)
Date of Award: 2016
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Abstract:
The high demand for biopharmaceuticals has been met thanks to improved upstream productivity. Downstream, which has not advanced at the same pace, calls for new clarification strategies to cope with the increased process-related impurities associated with upstream improvements. This thesis has focused on the implementation of polyelectrolyte flocculation between centrifugation and depth filtration during the primary recovery of a monoclonal antibody Chinese hamster ovary (CHO) cell process. A high-throughput, automated ultra scale-down (USD) flocculation methodology was developed with industrial relevance in mind for process development activities. The impact flocculation had on depth filtration and protein A chromatography performance was subsequently investigated and supported by analytical assays and techniques to assess impurity removal. Cell densities at time of harvest > 20x10^6 cells/mL were critical for flocculation to occur on centrifuged CHO cell cultures. Flocculant addition time limited the flocculation scale-up success between two vessels with different geometrical ratios and working volumes (1.5 L and 800 µL). The influence of mixing time scales (macromixing, mesomixing and micromixing) on this variable defined the USD flocculation scale-up basis, which was: predominance of micromixing in the vessels (flocculant addition time scale-up) and constant power input per unit volume (impeller speed scale-up). The implementation of constant pressure, single-layer USD filtration methods with flocculated feeds was precluded due to the low filter capacity values obtained (< 35 L/m^2). In contrast, constant flux filtration with multi-layer depth filters at laboratory scale reached manufacturing-scale filter capacity values (> 490 L/m^2). Flocculation achieved larger depth filtration capacities and lower process-related impurities before protein A chromatography when compared to the current manufacturing processing option. Post-protein A chromatography, the clear eluate obtained with flocculation contrasted with the turbid eluate of the current processing option. Mass spectrometry data confirmed the turbid eluate was mainly constituted of negatively charged CHO cell protein precipitates.
Supervisor: Not available Sponsor: Not available
Qualification Name: Thesis (Ph.D.) Qualification Level: Doctoral
EThOS ID: uk.bl.ethos.790559  DOI: Not available
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