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Millistak+HC AppGd_textC.qxd - Millipore

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typical operating conditions). The<br />

addition of the membrane layer further<br />

enhances the retention capability of<br />

the A1HC prefilter, to increase sterile<br />

filter protection dramatically.<br />

In order to achieve this level of<br />

sterile filter capacity, the prefilter must<br />

be highly retentive to small particles<br />

and colloidal materials. The correlation<br />

of sterile filter capacity with the turbidity<br />

of prefilter effluent is shown in<br />

Figure 5. The data show that, to reach<br />

sterile filter capacities in the range of<br />

500 L/m 2 , the prefilter must reduce<br />

fluid turbidity to well below 10 NTU.<br />

0.22 µm Durapore Capacity<br />

(L/m2 @ 20 psid)<br />

700<br />

600<br />

500<br />

400<br />

300<br />

200<br />

100<br />

0<br />

0<br />

Clarified Mammalian Cell Culture<br />

Figure 5. Sterile Filter Capacity as a Function of Feed Turbidity<br />

Depending on the primary clarification<br />

process employed (as shown<br />

in the process schematic in Figure 3<br />

above), secondary clarification will<br />

further reduce turbidity levels by a<br />

factor of 5:1—100:1. Note that<br />

monitoring effluent turbidity can be<br />

a useful guide in determining prefilter<br />

performance, but it should not be used<br />

for actual sterile filter sizing, due to<br />

the complexities of membrane fouling.<br />

Post-Centrifuge<br />

Centrifugation is by far the most<br />

widely practiced method of bulk<br />

cell mass removal for fermentation<br />

10 20 30 40 50<br />

Turbidity (NTU)<br />

1.54 PCV,<br />

60% Viability<br />

Millistak+ HC Filters Application Guide 7

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