TY - JOUR
T1 - Adapted ultra scale-down approach for predicting the centrifugal separation behavior of high cell density cultures
AU - Tustian, Andrew D.
AU - Salte, Heidi
AU - Willoughby, Nicholas A.
AU - Hassan, Inass
AU - Rose, Michael H.
AU - Baganz, Frank
AU - Hoare, Michael
AU - Titchener-Hooker, Nigel J.
PY - 2007/11
Y1 - 2007/11
N2 - The work presented here describes an ultra scale-down (USD) methodology for predicting centrifugal clarification performance in the case of high cell density fermentation broths. Existing USD approaches generated for dilute systems led to a 5- to 10-fold overprediction of clarification performance when applied to such high cell density feeds. This is due to increased interparticle forces, leading to effects such as aggregation, flocculation, or even blanket sedimentation, occurring in the low shear environment of a laboratory centrifuge, which will not be apparent in the settling region of a continuous-flow industrial centrifuge. A USD methodology was created based upon the dilution of high solids feed material to ~2% wet wt/vol prior to the application of the clarification test. At this level of dilution cell-cell interactions are minimal. The dilution alters the level of hindered settling in the feed suspensions, and so mathematical corrections are applied to the resultant clarification curves to mimic the original feed accurately. The methodology was successfully verified: corrected USD curves accurately predicted pilot-scale clarification performance of high cell density broths of Saccharomyces cerevisiae and Escherichia coli cells. The USD method allows for the rapid prediction of large-scale clarification of high solids density material using millilitre quantities of feed. The advantages of this method to the biochemical engineer, such as the enabling of rapid process design and scale-up, are discussed. © 2007 American Chemical Society and American Institute of Chemical Engineers.
AB - The work presented here describes an ultra scale-down (USD) methodology for predicting centrifugal clarification performance in the case of high cell density fermentation broths. Existing USD approaches generated for dilute systems led to a 5- to 10-fold overprediction of clarification performance when applied to such high cell density feeds. This is due to increased interparticle forces, leading to effects such as aggregation, flocculation, or even blanket sedimentation, occurring in the low shear environment of a laboratory centrifuge, which will not be apparent in the settling region of a continuous-flow industrial centrifuge. A USD methodology was created based upon the dilution of high solids feed material to ~2% wet wt/vol prior to the application of the clarification test. At this level of dilution cell-cell interactions are minimal. The dilution alters the level of hindered settling in the feed suspensions, and so mathematical corrections are applied to the resultant clarification curves to mimic the original feed accurately. The methodology was successfully verified: corrected USD curves accurately predicted pilot-scale clarification performance of high cell density broths of Saccharomyces cerevisiae and Escherichia coli cells. The USD method allows for the rapid prediction of large-scale clarification of high solids density material using millilitre quantities of feed. The advantages of this method to the biochemical engineer, such as the enabling of rapid process design and scale-up, are discussed. © 2007 American Chemical Society and American Institute of Chemical Engineers.
UR - http://www.scopus.com/inward/record.url?scp=37149022911&partnerID=8YFLogxK
U2 - 10.1021/bp070175d
DO - 10.1021/bp070175d
M3 - Article
SN - 8756-7938
VL - 23
SP - 1404
EP - 1410
JO - Biotechnology Progress
JF - Biotechnology Progress
IS - 6
ER -