Page 626 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

588 Applied Process Design for Chemical and Petrochemical Plants

A-15.
Stainless Steel Pipe Data
(Based on ANSI 836.19 wall thicknesses)

Nominal Outside Thick- Inside Inside Diameter Functions Transverse
Pipe Diam- ncss Dl arriet er I In Inches I Internal Arca
Size et er
d' .Sq.\"\. I SqAFt
Inches Inches Schedule 5 S

2
--li- ----�-:�:f- iiif-· �:�!�- -fi�:� ,- --�-::�: 0.358 0.254 o. 1804 0.3% 0.00275
0.779
0.716
I I . 315 0. 065 I . 185 0. OCJ88 I . 404 1.664 1.972 0.659 0. 664 0. 00.Jfi I
0.007b6
l.103
2.337
Jl/4 I. 660 0. 065 I. 530 0. 1275 2. 341 3.582 5.480 8.384 I. 8.JCJ 0. 01277
Jl/2 1.900 0.065 I. 770 0.1475 3.133 5.545 9.815 17.37 2.461 0.0170CJ
2 2.375 0.065 2.245 0.1871 5.040 II .JI 25.40 57.03 3.958 0.02749
2 1/2 2.875 0.083 2.709 0. 2258 7.339 19.88 53.86 145.9 5.764 0.0400.!
3 3.500 0.083 3.334 0. 2778 11. 12 37.06 12.J.6 411.9 8.733 O.Ob065
3% 4.000 0.083 3.834 0.3195 14.70 56.36 216.1 828.1 11. 545 0.08017
4 4.500 0.083 4 .. 1.34 o. 3612 18.78 81.41 352.8 1529. 14.750 0.1024
5 5.563 0.109 5.345 0.4454 28.57 152.7 816.2 4363. 22.43CJ 0.1558
6 6.625 0.109 b.407 0.5339 41.05 263.0 isss. 107%. 32.241 0.22J<J
8 8.625 0.109 I 8.407 0.7006 70.68 594.2 4995. 41996. 55.512 0.3855
10 10.750 0.1.34 10.482 0.8375 109.9 1 1152. 12072. 126538. 86.315 0.59<J.J
12 j 12.750 0.156 I 12.4.38 1.0.365 154.7 1924. 23933. 297682. 121.50 0.84.38
I
Schedule 10 S
----------
--·-··-···
1' 0 �� 08881 -- o .oo;;;- � o- . � 7-4 � :;o·o; � -
1/s 0.04() 0.307 0.0256 O.OCJ42 0.0289 1 --
114 0.405 0.065 0. 41 0 0. 034 2 0. 1681 0.0689 0.02826 0.0115() 0. IJ2 0.000()2
0.540
3/g 0.675 0.065 0.545 0.0454 0.2970 0.161() 0.08822 0.04808 0. 2J3 0.00162
l/2 0.840 0.083 0.674 0.0562 0.4543 0 .. 1062 0. 2064 0.1.391 0.357 0.00248
% 1.050 0.083 0.884 0.0737 0.7815 0.6CJ08 0.6107 0.5398 0.fil4 0.00426
I I. 315 0.109 1.097 0.0914 I. 203 I. 320 1. 448 I 1.589 0.945 , 0.00fi56
Jl/4 1.660 0.109 I 1.442 0. 1202 2.079 2.CJ98 4.324 6. 2.35 I . 633 0. 0 I I 34
Jl/2 I. 900 0. 109 1.682 0.1402 2.829 4.759 8.004 13.46 2. 222 0.01543
2 2.375 0.109 2.157 0.1798 4.65.l 10.04 21. 65 46.69 3.654 0.02538
2 1/2 2.875 0. 120 2. 6.35 0. 2196 6. 943 18.30 48.21 127.0 5.453 0.03787
3 3.500 0.120 3. 260 0. 2717 IO. 63 34.65 112.9 368.2 8.347 0.057%
31/2 4.000 0.120 3.760 0.3133 14.14 53.16 ICJ9.9 751.5 II.II 0.07712
4 4.500 0.120 4. 260 0.3550 18.15 77.31 329.3 1403. 14.26 0.09899
5 5.563 0.134 5.295 0.4413 28.04 148.5 786.1 4162. 22.02 0.152<J
6 6.625 0.134 6.357 0.5298 40.41 256.9 1633. 10382. 31.74 0. 2204
8 8.625 0.148 8.329 0.6CJ4l 69.37 577.8 4813. 40083. 54.48 0.3784
10 10.750 0.165 10.420 0.8683 108.6 113 I. 11789. 122840. 85.2() 0.5923
12,, 12.750 0.180 12..190 I 1.0325 153.5 1902. 23566. I 291982. 1120.6 0.8.372
Schedule 40 S

\lg
to Values ure the same, �i:c for size, ns those shown on the facing r.1gc
for StanJarJ \V;ill J)ipc: (hcu vicxt weight <>n K, 10, ;ind 12-inch sicc·,1.
12
Schedule 80 S
Ys
to Vuluc-, ;in .. : t hc xunc. size for size, <l'i t ho-«- sbown
on t hc f.icing p;igc fur 1:xrra .Strong P,pc.
12
Courtesy Crane Co., Technical Manual 410, Flow of Fluids.