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

02.
CHAPTER !2.
RESUI,TS
Many heat transfer runs 1,\fere made '\vith water in the
vessel in order to gain familiarity l..ri th the equipment and
to obtain enough information to formulate the program to
be fol101,-led with the non-Nelvtonian fluids e
To be more
specific, 319 data points ,,,ere obtained using the many
i...mpellers ,listed in Chapter ~_..
163 of these points 1,..Jere
not used for evaluating the constants of the correlations
because the impellers "Jere not at the standard posi tions
listed in Table 5-1. These data, summarized in Table 5-2,
provided much qualitative and quantitative information
about the "Hall temperature, the effect of i...mpeller position,
and the impeller geometry ..
156 of the "\..Jater data points 1-Jere measured at the impeller
heights listed in Table 5-1.
These data, in addition
to 297 data points obtained with glycerine and Carbopol
solutions, "t-Jere used in evaluating constants for the correlations
discussed later in this chapter.