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Prediction of batch heat transfer coefficients for pseudoplastic fluids ...

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22><br />

<strong>fluids</strong> studied (apparent viscosities behv-een 3000 and 11,000<br />

centipoise) there was little effect <strong>of</strong> baffles on power<br />

cons~mption, even at Dt/Da as low as 1.67. Dual impellers<br />

required tvdce the pOl-leI' <strong>of</strong>' a single impeller and this remained<br />

true <strong>for</strong> various spacings between the impellers.<br />

Quality <strong>of</strong> Mixing<br />

The quality <strong>of</strong> mixing is a very important criterllnto<br />

be considered Hhen designing an agitation system, since the<br />

quality or composition <strong>of</strong> a product is dependent upon the<br />

degree to Hhich reactant or temperature fluctuations are<br />

minimized throughout the vessel. This is especially true<br />

Hi th many processes involving nOn-Nev.Itonian f1uids:l such as<br />

the <strong>heat</strong>ing <strong>of</strong> food products or the polymerization <strong>of</strong> a<br />

monomer.<br />

l1etzner and Taylor (127) studied the f'lovJ patterns in<br />

an agitated vessel in an attempt to learn more about the<br />

mechanism <strong>of</strong>' mixing in such a system. They suspended 0.02<br />

"<br />

inch spheres <strong>of</strong> Plexiglas": in both Ne,itonian and <strong>pseudoplastic</strong>s<br />

<strong>fluids</strong> and photographed them as the fluid was<br />

being mixed by a disk and vane turbine. The loqal<br />

velocities<br />

were calculated by measuring the streak lengths and dividing<br />

by the exposure time.<br />

A plot <strong>of</strong> the local velocity versus<br />

radius was differentiated to obtain the local shear rates.<br />

';"Trademark <strong>of</strong> Rohm and Haas Co.

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