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

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158<br />

coefficient. Thus, <strong>for</strong> the water and glycerine it was<br />

only necessary to evaluate the viscosity coefficient and<br />

express it in the correct units.<br />

The viscosity <strong>of</strong> l-Iater \·ras determined from Bingham t s<br />

equation <strong>for</strong> the fluidity, ( ¢ ), <strong>of</strong> water as a fUl~ction<br />

<strong>of</strong> temperature (17).<br />

¢ = 0.021~-B2 [(T-8.L~35) + j8078.~. + (T-8.435)2] - 1.20 (A-l<br />

\.Jhere ¢ is expressed in centipoise -1 and<br />

T is the temperature in degrees Centigrade.<br />

The relationship betl-Jeen fluidity and viscosi ty is<br />

jl = l/¢<br />

(A-2<br />

The fluid consistency index in the proper units is obtained<br />

by multiplying the viscosity in centipoise by<br />

6.72 x 10-4<br />

K = 6.72 x 10-4p<br />

(A-3<br />

The viscosity <strong>of</strong> 93.7 percent clycerine was graphically<br />

interpolated from data <strong>of</strong> Segur and Oberstar (177) and is<br />

given in Table A-l.

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