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Millistak+HC AppGd_textC.qxd - Millipore

Millistak+HC AppGd_textC.qxd - Millipore

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How Are Millistak+ HC<br />

Filters Used?<br />

The typical downstream recovery<br />

process for mammalian cell derived<br />

biologics consists of multiple clarification<br />

steps to prepare the liquid-borne<br />

product for either sterile filtration or<br />

direct chromatographic purification.<br />

In the first stage or primary separation<br />

step, the bulk of the cell mass is<br />

removed from the broth—depending<br />

on the volume and type of fermentation<br />

process, different clarification<br />

methods are used, as shown in<br />

Figure 3.<br />

Batch Processing<br />

In large-scale (> 1,000 liter) batch<br />

and fed-batch fermentations, the bulk<br />

of the cell mass is ordinarily separated<br />

by centrifugation or tangential flow<br />

microfiltration. For small batch fermentations<br />

(< 1,000 liter), cartridge depth<br />

filters (NFF) are often used in the pore<br />

size range of 3–5 µm.<br />

Perfused Bioreactor<br />

In contrast to batch processes, perfused<br />

bioreactors are harvested continuously<br />

over extended operating periods<br />

lasting several weeks or months.<br />

For primary clarification, the flowcontrolled<br />

product stream from the<br />

perfusion bioreactor will typically pass<br />

through either a membrane separator<br />

(hollow fiber TFF) or a gravity settler,<br />

with the cell mass recycled to the<br />

fermenter. The crude product is pooled<br />

and then batch-processed for secondary<br />

clarification and final sterile filtration.<br />

A Single Step for Clarification<br />

and Prefiltration<br />

The effluent of these various primary<br />

clarification steps is generally unsuitable<br />

for either sterile filtration or<br />

chromatographic processing. The level<br />

of suspended matter in all cases<br />

(which varies by method) will cause<br />

rapid downstream fouling, with significant<br />

cost impact. The turbidity ranges<br />

noted in the process schematic in<br />

Figure 3 are indicative of the particle<br />

loads present. Even in the case of<br />

TFF microfiltration—typically executed<br />

with a 0.45 – 0.65 µm membrane—<br />

particle loading in the permeate does<br />

not allow for direct sterile filtration at<br />

any reasonable capacity or cost.<br />

Further clarification is required, for<br />

which disposable NFF filters are<br />

normally used (depth or surface types).<br />

The challenge confronting the process<br />

engineer is to arrive at an integrated<br />

clarification and sterile filtration train that<br />

will minimize overall production costs.<br />

In many cases, secondary clarification<br />

of tissue culture fluid involves several<br />

(two or three) serial filtration steps. The<br />

need for multiple separations arises from<br />

the broad range of particle sizes and<br />

Millistak+ HC Filters Application Guide 3

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