TURBULENT HEAT AND MOMENTUM TRANSFER FOR GASES IN A CIRCULAR TUBE AT WALL- TO BULK TEMPERATURE RATIOS TO SEVEN Page: 66 of 97
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Extracted Text
The following text was automatically extracted from the image on this page using optical character recognition software:
0
RUN 107
TP, STAG
F
TC 1 -257.74
TC 2 -255.14
TC 3 -250.31
TC 4 -241.66
TC 5 -226.49
TC 6 -198.97
TC 7 -154.42
TC 8 -87.33
TC 9 -19.73
TC10 62.46
TC11 133.42V
FT/SEC
1C1.264
1C2.S17
1C5.P 1
111.437
120.73F
137.651
165.C23
2C7.166
252.63C
313.555
365.141TBSIAT ThAtN
F F-25E.48
-255.SC
-251.13
-242.61
-227.6C
-2CC.45
-156.57
-SC.73
-24. F
54.45
122.67-257.78
-255.18
-25C.35
-241.72
-226.57
-1S9.08
-154.60
-87.64
-20.22
61.63
132.26OPP,GAS
BTU/HRF f2
53359.7
60517.5
65599.9
67041.6
67870. 1
69042.9
68449.4
68793.6
68579. 7
68887.4
68195.0PARAMETERS BASED UN BILK TEMPERATURE
NU, B
TC 1
TC 2
TC 3
TC 4
TC 5
TC 6
TC 7
TC 8
TC 9
TC10
TC11683.07
493.33
382.87
318.87
284.71
233.66
187.50
159.1 C
147.26
146.31
140.91RE,h
215121.6
21643E.4
211643.5
2C3645.3
1S1tC2.6
173374.4
151277.C
12685F.7
111 17.3
9745F.3
P8752.1PRB
.F455
.E414
.E338
.F2CS
.* C72
.7p57
.7652
.7523
.7366
.72C6
.71CCTt/TB
1.668
2. 021
2.362
2. 545
2.538
2. 53o
2.401
2.138
1. 899
1.666
1.550TI /2
1.431
1.637
1.825
1.923
1.919
1.918
1.846
1.702
1.567
1.429
1.359FILP CCEFF
BTU/FHRFT2
399.04
291.73
231.50
200.36
190.70
173.97
161.97
165.09
177.48
204.68
219.55
PARAMETER 1
1045.10
865.16
751.59
663.63
595.30
493.63
385.23
303.46
260.72
238.39
219.61
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Perkins, H.C. & Worsoe-Schmidt, P. TURBULENT HEAT AND MOMENTUM TRANSFER FOR GASES IN A CIRCULAR TUBE AT WALL- TO BULK TEMPERATURE RATIOS TO SEVEN, report, September 1, 1964; United States. (https://digital.library.unt.edu/ark:/67531/metadc1034374/m1/66/: accessed April 28, 2024), University of North Texas Libraries, UNT Digital Library, https://digital.library.unt.edu; crediting UNT Libraries Government Documents Department.