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1.
Biotechnol J ; 12(5)2017 May.
Article in English | MEDLINE | ID: mdl-28233468

ABSTRACT

Continuous disk-stack centrifugation is typically used for the removal of cells and cellular debris from mammalian cell culture broths at manufacturing-scale. The use of scale-down methods to characterise disk-stack centrifugation performance enables substantial reductions in material requirements and allows a much wider design space to be tested than is currently possible at pilot-scale. The process of scaling down centrifugation has historically been challenging due to the difficulties in mimicking the Energy Dissipation Rates (EDRs) in typical machines. This paper describes an alternative and easy-to-assemble automated capillary-based methodology to generate levels of EDRs consistent with those found in a continuous disk-stack centrifuge. Variations in EDR were achieved through changes in capillary internal diameter and the flow rate of operation through the capillary. The EDRs found to match the levels of shear in the feed zone of a pilot-scale centrifuge using the experimental method developed in this paper (2.4×105 W/Kg) are consistent with those obtained through previously published computational fluid dynamic (CFD) studies (2.0×105 W/Kg). Furthermore, this methodology can be incorporated into existing scale-down methods to model the process performance of continuous disk-stack centrifuges. This was demonstrated through the characterisation of culture hold time, culture temperature and EDRs on centrate quality.


Subject(s)
Automation, Laboratory/methods , Cell Culture Techniques/methods , Animals , Automation, Laboratory/instrumentation , Biomechanical Phenomena , Biotechnology , CHO Cells , Cell Culture Techniques/instrumentation , Centrifugation , Cricetinae , Cricetulus , Equipment Design
2.
Biotechnol Bioeng ; 113(9): 1934-41, 2016 09.
Article in English | MEDLINE | ID: mdl-26927621

ABSTRACT

In the production of biopharmaceuticals disk-stack centrifugation is widely used as a harvest step for the removal of cells and cellular debris. Depth filters followed by sterile filters are often then employed to remove residual solids remaining in the centrate. Process development of centrifugation is usually conducted at pilot-scale so as to mimic the commercial scale equipment but this method requires large quantities of cell culture and significant levels of effort for successful characterization. A scale-down approach based upon the use of a shear device and a bench-top centrifuge has been extended in this work towards a preparative methodology that successfully predicts the performance of the continuous centrifuge and polishing filters. The use of this methodology allows the effects of cell culture conditions and large-scale centrifugal process parameters on subsequent filtration performance to be assessed at an early stage of process development where material availability is limited. Biotechnol. Bioeng. 2016;113: 1934-1941. © 2016 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.


Subject(s)
Centrifugation/methods , Filtration/methods , Models, Theoretical , Shear Strength , Animals , CHO Cells , Cell Count , Cell Culture Techniques , Cell Survival/physiology , Cricetinae , Cricetulus
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