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

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

archives.njit.edu
from archives.njit.edu More from this publisher
04.11.2014 Views

112 correlations for the prediction of batch side heat transfer coefficients. These data are summarized in Table 5-3. Two general types of correlations were evaluated, those based on the dDJlensional analysis developed in Chapter 3, and those which are semi-emperical alterations of the present correlation for Nel,rtonian fluids .. FO'ur different types of impellers '(-Jere used in this study: anchor, paddle, propeller, and turbine. Since tl1.e geometry and flovl patterns for each L.'1lpeller may be different, the constants of any correlations tested Her'e evaluated separately for each impeller type. Only one anchor agitator was used and therefore the effects of impeller diameter and ,,,,idth could not be evaluated for the anchor .. The propellers were geometrically similar and therefore only the diameter effect was measured. Results of Dimensional Analysis The dimensional analysis of Chapter 3 provided (~~~ra.) a. b )C(: d e AlMI~C~~ fl!p/t" (~) (g: :;) ~ (3-8.0 as an equation 1:Jhich characterizes the batch heat transfer system. The constants of this correlation\labeled correlation A) Here evaluated and are presented in Table 5-4. correIa tion ",ri th its constants Has then used to calculate a "predicted Nusselt number" for each of the data pOints. The percentage error The

3 Smll~L4.RY OF DATA POINTS USED IN CORRELATIONS . Number of Data Points _Flov.r Behavior Index ::: 1 .. 0 Impel:}..er Type 0 .. 69 0 .. 36 Total Anchor 16 8 8 7 39 Paddle Propeller Turbine l51~ 26 48 48 15 16 ~L6 7 15 29 6 277 54 83 TOTAL 87 76 -----------------------------------------~--~--~~--------

112<br />

correlations <strong>for</strong> the prediction <strong>of</strong> <strong>batch</strong> side <strong>heat</strong> <strong>transfer</strong><br />

<strong>coefficients</strong>. These data are summarized in Table 5-3. Two<br />

general types <strong>of</strong> correlations were evaluated, those based<br />

on the dDJlensional analysis developed in Chapter 3, and<br />

those which are semi-emperical alterations <strong>of</strong> the present<br />

correlation <strong>for</strong> Nel,rtonian <strong>fluids</strong> ..<br />

FO'ur different types <strong>of</strong> impellers '(-Jere used in this<br />

study: anchor, paddle, propeller, and turbine. Since tl1.e<br />

geometry and flovl patterns <strong>for</strong> each L.'1lpeller may be different,<br />

the constants <strong>of</strong> any correlations tested Her'e evaluated<br />

separately <strong>for</strong> each impeller type.<br />

Only one anchor<br />

agitator was used and there<strong>for</strong>e the effects <strong>of</strong> impeller<br />

diameter and ,,,,idth could not be evaluated <strong>for</strong> the anchor ..<br />

The propellers were geometrically similar and there<strong>for</strong>e<br />

only the diameter effect was measured.<br />

Results <strong>of</strong> Dimensional Analysis<br />

The dimensional analysis <strong>of</strong> Chapter 3 provided<br />

(~~~ra.) a. b )C(: d e<br />

AlMI~C~~ fl!p/t" (~) (g: :;) ~ (3-8.0<br />

as an equation 1:Jhich characterizes the <strong>batch</strong> <strong>heat</strong> <strong>transfer</strong><br />

system.<br />

The constants <strong>of</strong> this correlation\labeled correlation<br />

A) Here evaluated and are presented in Table 5-4.<br />

correIa tion ",ri th its constants Has then used to calculate<br />

a "predicted Nusselt number" <strong>for</strong> each <strong>of</strong> the data pOints.<br />

The percentage error<br />

The

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!