Page 623 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

Appendix 585
A-14.
Commercial Wrought Steel Pipe Data
(Based on ANSI 836.10 wall thicknesses)
--------------
··- -- ----····· ·-··· .. ······-·----
Nominal Outside Thick- Inside Inside Diameter Functions i Transverse
Pipe Diam- ness Dia met.er t In Inches) I Internal Area
Size eter -- d I /) - - :-r:��
- �� /
Inches Inches I nchcs Inches Feet d' d' d' d�
0 14 14 0.250 13.5 1. 125 182. 25 2460.4 33215. 448400. 143 .14 0.994
16 ! 6 0. 250 15.5 1.291 240.25 3723.9 57720. 894660. 188.69 1.310
18 18 0.250 17.5 1.4583 306.25 5359.4 93789. 1641309. 240.53 1.670
20 20 0.250 19.5 1.625 380.25 7414.9 144590. 2819500. 298.65 2.074
24 24 0.250 23.5 1. 958 552. 25 12977. 304980. 7167030. 433.74 J.012
JO 30 0.312 29.376 2 .448 862. 95 25350. 744288. 21864218. 677.76 4.707
8 8.625 0.250 II 8.12510.677111 66.02 536.38 I 4359.J 35409. 51.85 0.3601
1
10 10.75 i 0.250 10.25 0.8542 105.06 1076.9 11038. , 113141. 82.52 0.5731
0
"' ., 12 12.75 i 0.250 12.25 1.021 150.06 1838.J I 22518. I 275855. 117.86 0.8185
'3 14 14 0.312 __ lJ.376 i 1.111_: 178.92 - 2J9J.2 I 32012. 428185. 140.52 0.9758
.. --- . ··--- -··
.,
"O 16 16 0.312 15.376 1.281 236.42 3635.2 55894. 859442. 185.69 11.290
..c 18 18 0.312 17.376 1.448 301.92 5246.J 91156. 1583978. 237.13 ! 1.647
u 12.021
rJ) 20 20 0.375 19. 250 1.604 370.56 7133.J 137317. 2643352. 291.04
24 24 0.375 23.25 1.937 540.56 12568. 292205. 6793832. 424. 56 2. 948
JO 30 0.500 29.00 2.417 841.0 24389. 707281. 205J1149. 660.52 :4.587
8 I 8.625 0.277 8.071 0.6726 65.14 525.75 424.3. 2 34248. 51. 16 0.3553
1
10 10.75 0.307 10.136 0.8447 102.74 1041.4 10555. 106987. 80.69 0.5603
0
M 12 12.75 O.JJO 12.09 I .0075 146.17 1767.2 21366. 258304. 114. 80 0.7972
0.375
14
14
.,
'3 -· .. - ··--· ----- .. 13.25 1.1042 175.56 2326.2 30821. 408394 . 137.88 I 0.9575
-o 16 16 0.375 15. 2511. 2708 2ji. 56 -· - 354b. 6 ... . .. 54084 .- ·- . --,- 824801 . . ·1· isz. 65-1- . 268 ....
..c 18 18 0.438 17.124 1.4270 293.23 5021.J 85984. 1472397. 230.JO 1.599
� 20 20 0.500 19.00 1.5833 361.00 6859.0 130321. ! 2476099. 1283.53 1.969
Ii
24 24 0.562 22. 876 I.90631523.J 1 11971. 273853. i 6264703. 411.00 2.854
JO 1 30 0.625 28.75 2 .3958 826.56 23764. 683201. ; 1%42160. 1649.18 4.508
0.405 0.0&8 I 0.26910.0224! 0.0724 1 0.0195 I 0.005242 1. 0.00141 I 0.057 0.00040
I
0.540 0.088 0.364 O.OJOJ 0.1325 0.0482 0.01756 0.00639 0.104 0.00072
0.675 I 0 .091 0. 493 0. 0411 0. 2430 0 .1198 0 .05905 I O. 02912 0 .191 0 .00133
- - - -- --· ----- -·- - --- . . -----
l/2 0.840 I 0.109 0.622 0.0518 0.3869' 0.2406 1 0.1497 0.09310 0.304!0.00211
% 1.050 0.113 0.824 0.0f>87 0.679 0.5595 0.4610 0.3799 0.533 I 0.00371
1 1.315 I O.IJJ 1.049 0.0874 1.100 1.154 1.210 1.270 0.864!0.00600
t.660 0.140 i.aso 0.1150 1.904 2.628 J.625 s.oos 1.495:0.01040
P/ 4
----·- -·-· -· ---·--· ----·-···- ·- --- --- -------·-·--
Jl/2 1.900 0.145 1.610 0.13421 2.592 4.173 6 718 I . IO 87 2.0J6j0.01414
� 1 � 8::2! � 5051_1 _:·7 � 25- J.3551
0 2 2.J75 o. t54 2.067 0.1722 4.272 8.831 27J97 : o.02JJO
""' ., 2 1/2 2.875 0.203 2.469 0.2057 6.0% 15.051 4.788 0.03322
'3 J 3.5o_ o __ 0.21?_ -�-068 o._255�1. 9.413 __ 28.878 _ _ .. 7 .J9J _o...:��!-"!_O_
.,
"O Jl/2 4.000 I 0.226 J.548 0.2957 12.59 44.66J 158.51 562.2 Ii 9.886/0.06870
..c 4 4.500 0.2J7 4.026 0.3355 16.21 65.256 262.76 1058. 12.73010.08840
1
u 5 5. 563 0. 258 5. 047 0. 4206 25. 47 128. 56 648. 72 J275. 20. 006 0. 1390
rJ)
c, 6.625 I 0.280 6.065 o.5o54 36.78 22J.10 1352.8 8206. 28.891 0.2006
--- 8 -- - 8.625- 0.322 7.'981 0.6651' 63.70 - -- 508.36 .. -- 4057.7-- ---J2J80. J 50.027 0.3474
/
10 10.75 0.365 10.02 0.8J50 100.4 1006.0 10080. 101000. i 78.85510.5475
12 12.75 0.406 11.938 0.9965 142.5 1701.J 20306. 242470. 0 111.9] 0.777J
14 14.o o.438 13.124 t.09J7 172.24 2260.5 29666. J89J40. ; 135.28 lo.9394
--- • - -· - • - --------. -- •• , ------- --- • ···---· j_ -----------------
16 16.0 0.500 15.000 1.250 225.0 JJ75.0 50625. 759375. 1176.72 11.2272
18 18.0 0.562 16.876 1.406J 284.8 4806.J 81111. 1368820. 223.68 1.5533
20 20.0 0.59J 18.814 1.5&78 J54.0 6659.5 125J20. 2357244. ; 278.00 1 1.9305
24 24.0 0.687 22.626 1.8855 511.9 1158J. 262040. 5929784. 1402.07 12.7921
8 IL 625 0. 406 7. 813 0. 651 l 61.04 476. 93 J725. 9 29113. ! 47. 94 IO .JJ29
o 10 IO. 75 0. 500 9 .750 0. 8125 95 .06 926 .86 9036. 4 88110. ! 74 .66 0. 5185
! 12 12.75 0.562 11.626 0.9688135.16 1571.4 18268. 212J99. il06.16 0.7372
'3 _0 14.()_ 0.593 12.:�14_ !.:�678 16�:20 2104.0 26?.62_:._ J45480. i 128.% ,0.8956
] 16 16.0 0.656 14.688 1.1240 215.74 Jl68.8 46544. 68J618. 169.44 1.1766
{j 18 18.0 0.750 16.500 1.J750 272.25 4492.1 74120. 1222982. 21J.8J 1.4849
C/J 20 20.0 0.812 18.376 1.5JlJ 3J7.68 6205.2 114028. 2095.342. 265.21 1.8417
24 24.0 0.968 22.064 1.8J87 486.82 10741. 236994. 52290Jb. J82.35 2.6552
Va I 0.405 0.095 0.215 ,0.01791 0.04b21 0.009941 0.0021341 0.000459 J O.OJ6 0.00025
0 I 0.119 I 0.302 0.0252 I 0.00050
00 1/4 0.540 0.0912 0.0275 0.008317 0.00251J: 0.072
., 3/s 0.675 0.126 0.423 O.OJ5J 0.1789 0.0757 0.03200 O.OIJ54 i 0.141 0.00098
� ---v � ----0 � -840_1_0.147 0.546 0.0455--0.2981 -- 0.1628 ---0.08886 .. ---0.0485i O.iJ40�0016J-
j
1 lA 1.050 0.154 10.7420.0618 0.5506 0.4085 0.3032 0.2249 0.4JJ,0.00JOO
1,
� 1 1.315 I 0.179 o.957 o.0797 o.9158 o.8765 o.8387 o.8027 o.719 0.00499
Jlf. 1.660 0.191 1.278 0.1065 1.633 2.087 2.6667 J.409 l.28J 0.00891
Courtesy Crane Co., Technical Manual 410, Flow of Fluids. (continuea on next page)