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

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:Run Diameter h Np .,u<br />

N N Re<br />

N pr K/K<br />

x Height<br />

Po w<br />

2.1-7<br />

84 7.0 x 3.0 650 1980 4.23 89,176 2.76 0;89<br />

85 7.0 x 3.0 836 2595 4.54 126,969 3.17 0.91<br />

86 7.0 x 3.0 1072 :Slj·~3 4.94 171,139 3.95 0.94<br />

87 7.0 x 3.0 1294 3983 5.23 301,058 2.98 0.93<br />

75 8.0 x 1.0 424 1349 0.68 91, Enl 3.83 0.87<br />

76 8.0 x 1.0 410 1321 0.61 81,872 4.31 0.88<br />

77 8.0 x 1.0 627 1975 0.88 187,564 3.57 0.90<br />

78 8.0 x 1.0 875 2'729 1.02 347,186 3.30 0.92<br />

79 8.0 x 1.0 lu74 yi.50 1.04 395,001 4.16 0.94<br />

71 8.0 x 2.0 49~ 1539 1.80 77,031 4.16 0.94<br />

72 8.0 x 2.0 659 2114 2.52 116,131 4.12 0.91<br />

73 8.0 x 2.0 1260 3710 2.78 363,951 2.19 0.91<br />

74 8.0 x 2.0 1325 4286 2.96 270, ~1l~8 l~ .41 0.95<br />

eo 8.0 x 4.0 689 2051 3.62 106, 1()l.~ 2.3"5 0.87<br />

81 8.0 x 4.0 886 2748 '+' 57 127,621 3.16 0.91<br />

82 8.0 x 4.0 1086 3437 5.25 179,982 3.69 0.93<br />

83 8.0 x 4.0 1263 3938 5.48 267,892 3.29 0.93

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