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Handbook of Size Exclusion Chromatography and Related ...

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Figure 6shows the results <strong>of</strong> acontinuous reactor experiment in which the<br />

concentration <strong>of</strong> initiator in the monomer feed was varied, as shown, while<br />

the monomer feed concentration <strong>and</strong> r were kept constant. As the initiator<br />

concentrationincreases,theamount<strong>of</strong>conversionincreasesaccordingtoEq.(13).<br />

Similarly, Eq. (14) predicts that Mw will decrease as initiator concentration<br />

increases, which is also seen in Fig. 6. The exponential approaches to the steady<br />

state are seen between the increments in initiator concentration.<br />

The inset to Fig. 6shows the extrapolation <strong>of</strong> Mw to f¼0. In the QSSA<br />

Mw(f ¼0) should be proportional to the inverse square root <strong>of</strong> the initial initiator<br />

concentration, aprediction born out in the inset. Combining the Mw <strong>and</strong> f data<br />

allows for the determination <strong>of</strong> k 2 p =kt from a single experiment, such as in<br />

Fig. 6. The value is 11.7L/M s.<br />

Figure 7shows the effect <strong>of</strong> fluctuating conditions on f <strong>and</strong> Mw. In the first<br />

part an uninterrupted steady state is obtained. Then, deliberate temperature<br />

Figure 6 Mw <strong>and</strong> f from ACOMP <strong>of</strong> a continuous reactor, where the feed reservoir ratio<br />

<strong>of</strong> initiator to monomer increased after the steady state for each condition was reached. The<br />

inset shows the expected inverse square root dependence on initiator <strong>of</strong> Mw ( f ¼ 0). (From<br />

Ref. 34.)<br />

© 2004 by Marcel Dekker, Inc.

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