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 ...
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6/ TABLE A-2 CORRECTION FACTORS FOR GLYCERINE VISCOSITY EQUATION Temperat1Jll:'@l liT f' (eC) (ex- 1 ) (eeJ5lt-1~(l)is$) 100 2 .. 68 x 10- 3 0 90 2 .. 75 x 10 -3 0 80 2 .. 83 x 10- 3 0 70 2.91 x 10- 3 0 •.5 60 3 .. 00 x :LO -3 3.0 ,50 3 .. 09 :x 10- 3 9 .. ,5 L~O 3 .. 19 x 10"'3 27 30 3.30 x 10- 3 '71 20 3.41 :x ].0 -3 222 10 3 .. 53 x. 10- 3 6:>67 ~e eerreetion f'aeter was p10tted versus liT ~d f'ouad to deseribe a straight liJ5le on semileg pa~er (Figure A-2). It eould thus be expressed i' := C 10 D/T (A-6 T1:le i'our eonstaJ.fl.ts were evaluated as A ::: -4.14.5 B ::: 1.88 x 10 3 C ::: -12 .. 23
- Page 122 and 123: 10 I r "'" , •• ,'., "",' """",
- Page 124 and 125: 112 correlations for the prediction
- Page 126 and 127: TABLE 5 - 4 Correlation Constants A
- Page 128 and 129: 1/6 Table 5-5 and 5-6. A measure of
- Page 130 and 131: TABLE S - 6 IMPELLER Correlation Co
- Page 132 and 133: 120 greater than 2.0. In this case
- Page 134 and 135: 12.2
- Page 136 and 137: TABLE 5 - 9 CORRELATION E t (a/n +1
- Page 138 and 139: TABLE 5 - 10 IMPELLER Correlation C
- Page 140 and 141: TABLE 5 - 11 CORRELATION G (1.30/61
- Page 142 and 143: 1.30 of the substantial improvement
- Page 144 and 145: 1.3 2. The probable error in the ca
- Page 146 and 147: 134 .,;' : :: :::: : ~ !~. , " . .'
- Page 148 and 149: T." ••••••• ,_ .....
- Page 150 and 151: 38 the cooling of nitration liquors
- Page 152 and 153: 140 The average deviation of the me
- Page 154 and 155: 42 tween 0.25 and 0.58. L~~l had re
- Page 156 and 157: 144 transfer coefficients to non-Ne
- Page 158 and 159: 16 of fit and it may t...herefore b
- Page 160 and 161: 148 'tvas insufficient data to eval
- Page 162 and 163: 50 A ::: Apr ... B ::: C p ::: CPr
- Page 164 and 165: 52. Q ::. Average heat transfer rat
- Page 166 and 167: Xc = Function of Reynolds nL:l.m.be
- Page 168 and 169: IS6 G REE:>{ ALPHABET 0 ::: Value o
- Page 170 and 171: 158 coefficient. Thus, for the wate
- Page 174 and 175: 162 I , . I . "I '1 I i I 1 I 1· '
- Page 176 and 177: 64 ncr --~iIluto e torque of the in
- Page 178 and 179: 166 rive different temperatures; ab
- Page 180 and 181: 168 TABLE A-4. SLOPE OF "LOG SHEAR
- Page 182 and 183: TABLE 11.-5 RHEOLOGICAL DATA FOR CA
- Page 184 and 185: TABLE A-5 (eollt. ) /12 o . 24;;& C
- Page 186 and 187: '11 The flow behavior index and flu
- Page 188 and 189: i .f.C ·F s o 6 1 6 I
- Page 190 and 191: · . . . " , · . :::11" ': "'" ~ .
- Page 192 and 193: 180 Tke thermal e€l1'!ciluetlvity
- Page 194 and 195: 182 Heat capacity data for 100% gly
- Page 196 and 197: IB4- wkiek ex~resses the aensity e
- Page 198 and 199: 186 Ts - Torque X :: Peree~t 0~ ful
- Page 200 and 201: Phase I Calcu13tiJ~ of Slope of !oG
- Page 202 and 203: 3 REAL). N. ti •• D 4 cN=N E'I'
- Page 204 and 205: ~~-- ~---- --~--~ ~~~--------------
- Page 206 and 207: Phase IV Correlation of Flow Behavi
- Page 208 and 209: 96 HEAT TRANSFER DATA FOR WA'fER US
- Page 210 and 211: DATA /98 Batch \'ieight '" 94 •.
- Page 212 and 213: zoo Run Center Dia!!1ec;er Ri'M Are
- Page 214 and 215: DATA 20l. WATER - TUHBINSS Batch We
- Page 216 and 217: 204- HEAT T'rtANSFEH DATA USED IN C
- Page 218 and 219: DATA ANCHor;: 206 Batch :'Ieight =
- Page 220 and 221: 2.08 Run Diameter RP!'1 Area Dynamo
6/<br />
TABLE A-2<br />
CORRECTION FACTORS FOR GLYCERINE VISCOSITY<br />
EQUATION<br />
Temperat1Jll:'@l liT f'<br />
(eC) (ex- 1 ) (eeJ5lt-1~(l)is$)<br />
100 2 .. 68 x 10- 3 0<br />
90 2 .. 75 x 10 -3<br />
0<br />
80 2 .. 83 x 10- 3 0<br />
70 2.91 x 10- 3 0 •.5<br />
60 3 .. 00 x :LO -3 3.0<br />
,50 3 .. 09 :x 10- 3 9 .. ,5<br />
L~O 3 .. 19 x 10"'3 27<br />
30 3.30 x 10- 3 '71<br />
20 3.41 :x ].0 -3 222<br />
10 3 .. 53 x. 10- 3 6:>67<br />
~e eerreetion f'aeter was p10tted versus liT ~d<br />
f'ouad to deseribe a straight liJ5le on semileg pa~er (Figure<br />
A-2). It eould thus be expressed<br />
i' := C 10 D/T<br />
(A-6<br />
T1:le i'our eonstaJ.fl.ts were evaluated as<br />
A ::: -4.14.5<br />
B ::: 1.88 x 10 3<br />
C ::: -12 .. 23
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