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

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the batch than the other ticJO thermocouples.
At high iropeller
speeds, the wall temperature became relatively constant
over the whole surface.
It was felt that these data sh~wed
that the local heat
trruLsfer coefficients vary from point to point in the vessel.
In those portions of the vessel v!hich V·Jere best agitated
the heat was conducted from the wall at a faster rate than
in the poorly agitated regions.
Considering a unit area of the wall for any portion of
the vessel the ratio of the driving force to the resistance
is a constant for each of the resistances in series. Thus,.
negle cting the heat capacity of the l