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

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LIST OF FIGURES<br />

page<br />

2-1 FlGW Behavior <strong>of</strong> Pseudoplastic5<br />

3-1 Flow Patterns in Propeller Agitated Baffled Vessel<br />

4-1 Heat Transfer Vessel<br />

4-2 Location <strong>of</strong> Wall Thermocouples and Scale<br />

4-3 Piping Diagram<br />

4-4 Anchor Agitator<br />

4-5 Recorder Chart<br />

5-1 Effect <strong>of</strong> Impeller Height <strong>for</strong> Heating <strong>of</strong> Water;<br />

5.2 inch Propeller<br />

5-2 Effect <strong>of</strong> Impeller Height <strong>for</strong> Heating <strong>of</strong> Water;<br />

Anchor<br />

5-3 Effect <strong>of</strong> Impeller Height <strong>for</strong> Heating <strong>of</strong> Water;<br />

6 inch Disk and Vane Turbine<br />

5-4 Batch He~t Transfer Using Propellers<br />

5-5 Batch Heat Transfer Using Propellers<br />

6-1 Comparison <strong>of</strong> Newtonian Fluid Data with<br />

Literature Correlations: Anchor<br />

6-2 Comparison <strong>of</strong> Newtonian Fluid Data with<br />

Literature Correlations: Paddle<br />

6-3 Comparison <strong>of</strong> Newtonian Fluid Data with<br />

Literature Correlations: Propeller<br />

6-4 Comparison <strong>of</strong> Newtonian Fluid Data with<br />

Literature Correlations: Turbines<br />

A-I<br />

A-2<br />

Viscosity <strong>of</strong> 93.7% Glycerine Vs. 1/'1'<br />

Correction Factor, f, in Equation <strong>for</strong><br />

Viscosity <strong>of</strong> 93.1% Glycerine<br />

A-3 Constant Temperature Apparatus <strong>for</strong><br />

Viscometer<br />

A-4 Rheology <strong>of</strong> 0.15 Percent Carpopol<br />

A-S Rheology <strong>of</strong> 0.20 Percent Carbopol<br />

A-6 Rheology <strong>of</strong> 0.24 Percent Carbopol<br />

1<br />

58<br />

75<br />

71<br />

80<br />

8S<br />

92<br />

109<br />

109<br />

110<br />

122<br />

125<br />

134<br />

136<br />

137<br />

139<br />

160<br />

162<br />

161<br />

176<br />

171<br />

178

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