Page 137 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

Fluid Flow 123

Table 2-16 Table 2-17
ase Multipliers For Quantity* Temperature-Base Multipliers For

14.4 460 + new temperature base, O F.
Multiplier = Multiplier =
New pressure base, Lbs./sq. in. abs. 460 + 60
~~ ~~ ~ ~~
New Pressure Basey Lbs:./sq.in. abs. Multiplier New Temperature Base, " F. Multiplier
-
12.00 1.2000 45 0.9712
13.01D 1.1077 50 0.9808
14.00 1.0286 55 0.9904
14.40 1 .oooo 60 1 .0000
14.65 0.9829 65 1.0096
14.7 0.9796 70 1.0192
$4.9 0.9664 75 1.0288
15.4 0.9351 80 1.0385
16.4: 0.8780 85 1.0481
90 1.0577
*By permission, Johnson, T. W. and Berwaid, W. B., Flow oflvatural Gas 95 1.0673
Through High Pressure Transmission Lanes, l\/lonopuph No. 6, US. Dept. of 100 1.0769
Interior, Bureau of Mines, Washington, DC.
*By permission, Johnson, T. W. and Berwald, W. B., Flow of Natural Gas
Through High Pressure Transmission Lines, Monograph No. 6, US. Dept. of
Interior, Bureau of Mines, Washington, D.C.
Table 2-18
Specific Gravity Multipliers For Quantity*
-
0.600
Multiplier = I"
actual Specific Gravity
0.04 1

Specific Gravity 0.01 0.02 -- -~--- --__- ----
0.08
0.09
0.03
0.05 1 0.06
1.0954
1.0541
1.0445
0.5 1 1.0000 1 1.0847 1.0742 1.0640 0.9005 1 0.8944 1 1.0351 1.0171 1.0084
0.6 0.9918 0.9837 0 9759 0.9682 0.9608 0.9535 0.9393 0.9325
0.7 0.9258 0.9193 0.9129 0.9066 0.8885 0.8771 0.8715
0.7255 1
1
0.8660 1
0.8 1 1 0.8607 0.8554 0.8502 0.8452 I 0.8402 I 0.8353 0.8257 0.8211
0.9 0.8165 0.8120 0.8076 0.8032 0.7989 0.7947 0.7906 0.7825 0.7785
1 .o 0.7746 0.77018 0.7670 0.7632 0.7596 0.7559 0.7524 0.7454 0.7419
1.1 0.7385 0.7352 0.7319 0.7287 0.7223 I 0.7192 0.7131 0.7101
I I
*By permission, Johnson, T. W. and Berwald, W. B., Flow ofNaturul Gas Through High Pressure Transmission Lines, Monogruph No. 6, US. Dept. of Inte-
rior, Bureau of Mines, Washington, De.
Table 2-19
Flowing-Temperature Multipliers For Quantity*
460 + 60 %
Multiplier =
460 + actual flowing temperature
Temp. "F.
9
-- - I -___ I I I I 1 ! ILJ-L-l-----
.. 1.0632 1.062 1 1.0609 1.0598 1.0586 1.0575 1.0564 1.0552 1.0541 1.0530
101 1.0518 1.05017 1.0496 1.0485 1.0474 1.0463 1.0452 1.0441 1.0430 1.0419
20 1.0408 1.0398 1.0387 1.0376 1.0365 1.0355 1.0344 1.0333 1.0323 1.0312
30 1.0302 1.02981 1.0281 1.0270 1.0260 1.0249 1.0239 1.0229 1.0219 1.0208
40 1.0198 1.0188 1.0178 1.0167 1.0157 1.0147 1.0137 1.0127 1.0117 1 GI07
50 1.0098 1.0088 1.0078 1.0068 1.0058 1.0048 1.0039 1.0029 1.0019 1.0010
60 4.0000 0.9990 0.9981 0.9971 0.9962 0.9952 0.9943 0.9933 0.9924 0.9915
~
-
70 0.990rp 0.98916 0.9887 0.9877 0.9868 0.9859 0.9850 0.9841 _ _ 0.9831 0.9822
~-
0.9795
0.9777
80 1 0.9813 0.9715 1 0.9706 1 0.9697 1 0.9688 1 0.9680 1 0.9671 1 0.9662 1 0.9653 1 U.Y'I3Y
- ^_^^
0.9786
5.9804
0.9759
0.9750
0.9768
0.9741
90 0.9723 0.9645
"By permission, Johnson, T. %V. and Berwakd, W, B., Flow of?Jaturul Gas Through High Pressure Transmission Lines, kfonopaph No. 6, US. Dept. of Interi-
or, Bureau of Mines, Washington, DG.