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ARUP; ISBN: 978-0-9562121-5-3 - CMBBE 2012 - Cardiff University

ARUP; ISBN: 978-0-9562121-5-3 - CMBBE 2012 - Cardiff University

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value of p nearest to dqc=0 we continue the solution using dp/ dz g(<br />

z,<br />

p)<br />

until the end of<br />

the device is reached. This gives us an axial partial pressure profile in the cell region.<br />

5. RESULTS<br />

Results and graphs of oxygen outlet partial pressure versus time for the 13 fiber and 19<br />

fiber FIF bioreactors for selected flow rates are given in Figure 2. Studying OTR and the<br />

perfusion flow rate gives a better understanding of the behaviour of the FIF bioreactor.<br />

Therefore, two different modules (13FIF and 19FIF) of bioreactors (5 for each) were used<br />

in these studies. Figure 2 shows that 13 FIF and 19 FIF bioreactors do not have a similar<br />

behavior to the oxygen transfer through the silicone rubber hollow fiber into the other two<br />

Compartments. Figure 2 also shows that the 19FIF bioreactor has a higher OTR than that of<br />

the13FIF bioreactor for all the flow rates except for 40ml/h. The dependency of the OTR<br />

on the flow rate can also be seen.<br />

600<br />

500<br />

400<br />

OTR 300<br />

(nmol/min)<br />

200<br />

100<br />

0<br />

Flow rate and the module type<br />

Figure 2: Calculated OTR from the experimental work on the 13 FIF and 19 FIF bioreactors. The key legend<br />

denotes the module size, the compartment with water flow and the flow rate. E.g. 19B40 is an experiment<br />

with a 19 fiber set bioreactor, water flow in compartment B and a flow rate of 40 ml/h.<br />

Calculated data from experimental work of OTR with distilled water were used to validate<br />

the theoretical model. Physical and mechanical properties of the FIF bioreactors were used<br />

as Input parameters for the computer implementation. Oxygen transfer for 3 different water<br />

flow rates (40ml/h, 70ml/h &160ml/h) in FIF bioreactor were used to validate the model.<br />

Results showed 70% agreement with experimental results (table 1). The results show that<br />

the model over-predicted the actual OTR by 12% to 28% over the range of flow rates<br />

tested.<br />

Flow rate ml/h OTR nmol/min Experimental 19FIF OTR nmol/min Predicted 19FIF<br />

40 123 142<br />

70 234 234<br />

160 562 532<br />

Table 1: Experimental and predicted OTRs in compartment B in the FIF bioreactor (40, 70 & 160ml/h).<br />

19 A 40<br />

19 B 40<br />

19 A 70<br />

19 B 70<br />

19 A 90<br />

19 B 90<br />

19 A 160<br />

19 B 160<br />

13 A 40<br />

13 B 40<br />

13 A 70<br />

13 B 70<br />

13 A 90<br />

13 B 90<br />

13 A 160<br />

13 B 160

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