Maybury J P, Hoare M, Dunnill P
The Advanced Centre for Biochemical Engineering, Department of Biochemical Engineering, University College London, Torrington Place, London WC1E 7JE, UK.
Biotechnol Bioeng. 2000 Feb 5;67(3):265-73. doi: 10.1002/(sici)1097-0290(20000205)67:3<265::aid-bit2>3.0.co;2-j.
A method for using a bench-top centrifuge is described in order to mimic the recovery performance of an industrial-scale centrifuge, in this case a continuous-flow disc stack separator. Recovery performance was determined for polyvinyl acetate particles and for biological process streams of yeast cell debris and protein precipitates. Recovery of polyvinyl acetate particles was found to be well predicted for these robust particles. The laboratory centrifugation scale-down technique again predicted the performance of the disc stack centrifuge for the recovery of yeast cell debris particles although there was some suggestion of over-prediction at high levels of debris recovery due to the nature of any cell debris aggregates present. The laboratory centrifuge scale-down technique also proved to be an important investigative probe into the extent of shear-induced breakup of shear-sensitive protein precipitate aggregates during recovery in continuous high speed centrifuges. Such breakup can lead to over 10-fold reduction in separator capacity.
描述了一种使用台式离心机的方法,以模拟工业规模离心机(在这种情况下是连续流碟片式离心机)的回收性能。测定了聚醋酸乙烯酯颗粒以及酵母细胞碎片和蛋白质沉淀物的生物工艺流的回收性能。发现对于这些坚固的颗粒,聚醋酸乙烯酯颗粒的回收情况得到了很好的预测。实验室离心缩小技术再次预测了碟片式离心机回收酵母细胞碎片颗粒的性能,尽管由于存在的任何细胞碎片聚集体的性质,在高碎片回收率水平下有过度预测的迹象。实验室离心机缩小技术还被证明是一种重要的研究手段,可用于探究在连续高速离心机回收过程中,剪切敏感的蛋白质沉淀聚集体因剪切而破碎的程度。这种破碎会导致分离器容量降低超过10倍。