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American Society of Heating and Ventilating Engineers Guide, 1937
tinued turning in the threaded joint may in time result in a leak, par. ticularly when the pressure is high. The amount of elongation which a swivel joint can take up js controlled by the length of the swing piece employed and by the lateral displacement which is permissible in the long pipe runs.
Probably the most economical method of providing for expansion of piping in a long run is to take advantage of the directional changes which must necessarily occur in the piping and proportion the offsets so that sufficient flexibility is secured. Ninety-degree bends with long, straight tangents in either a horizontal or a vertical plane are an excellent means for securing adequate flexibility with larger sizes of pipe, When flexi bility cannot be obtained in this manner, it is necessary to make use of some type of expansion bend. The exact calculation of the size; of ex pansion bends required to take up a given amount of thermal expansion
Offset U bend
LFig. 1. Measurement of on Various Pipe Bends
is relatively complicated1. The following approximate method, however, has been found to give reasonably good results and is deemed to be sufficiently accurate for most heating work.
Fig. 1 shows several types of expansion bends commonly used for taking up thermal expansion. The amount of pipe, L, required in each of these bends may be computed from the following formula:
L = 6.16 ^~DA
(2)
where
L = length of pipe, feet. D = outside diameter of the pipe used, inches. A = the amount of expansion to be taken up, inches.
This formula, based on the use of mild-steel pipe with wall thicknesses not heavier than extra-strong, assumes a maximum safe value of fiber stress of 16,000 lb per square inch. When square type bends are used, the width of the bend should not exceed about two times the height: It is further assumed that the corners are made with screwed or flanged elbows or with arcs of circles having radii five to six times the pipe diameter.
All risers must be anchored and safeguarded so that the difference in
lPiping Handbook, by Walker and Crocker, and A Manual for the Design of Piping for Flexibility by the Use of Graphs, by E. A. Wert, S. Smith, and E. T. Cope, published by The Detroit Edison Company.
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Chapter 34--Pipe, Fittings, Welding
length when hot from the length when cold shall not disarrange the normal and orderly provisions for drainage of the branches.
It is especially necessary with light-weight radiators so to anchor the oiping and so to give it freedom for expansion that no strain therefrom shall be allowed to distort the radiators. When expansion strains from the pipes are permitted to reach these light metal heaters they usually
~,:e cnunds of distress which are exceedingly troublesome.
100Table 6. Thermal Expansion of Pipe in Inches per
Fra
(For superheated steam and other fluids refer to temperature column)
SiTOSltM STBiM
Elongation in Inches per 100 ft from --20 F UP
Saturates Steam
Elongation in Inches per 100 ft from --20 F UP
-- IMeasure Tem-
Vacuum
India
ofHg.
Pounds . erature per Degrees
Square Fahren Inch heit
CastIron Pipe
Sted Kpe
brought Copper Iron Pipe Pipe
Pressure Pounds
Square Inch Gage
Tem-
eratore Degrees
Fahren heit
CastIron
Pipe
Steel
Pipe
brought
Iron Pipe
Copper Pipe
Gage
-------
-20
0
20
40
29.39 ------- 60
28.89 27.99 26.48
--
---- ... ----- -
80 100 120
140 160
180
200
2.5 220
10 3 240
20.7 260
34.5 280
52.3 300
74.9 320
103.3 340
138.3 360
180.9 380
232.4 400
293.7 420
366.1 440
451.3 460
550.3 480
0 0 0 0 664.3 0.127 0.145 0.152 0.204 795.3 0.255 0.293 0.306 0.442 1 945.3 0.390 0.430 0.465 0.655 1115.3 0.518 0.593 0.620 0.88811308.3 0.649 0.725 0.780 1.100 U525.3 0.787 0.898 0.939 1-338[1768.3 0.926 1.055 1.110 1.57012041.3 1.051 1.209 1.265 1.794 12346.3 1.200 1.368 1.427 2.00812705 1.345 1.528 1.597 2.255 13080 1.495 1.691 1.778 2:5001 1.634 1.852 1:936 2.7201 1.780 2.020 2.110 2.9601 1.931 2.183 2.279 3.1891 2.085 2.350 2.465 3.4221 2.233 2.519 2.630 3-6651 2.395 2.690 2.800 3.9001 2.543 2.862 2.988 4.1451 2.700 3.029 3.175 4.3801
2.859 3.211 3.350 4.6281 3.008 3.375 3.521 4.870 3.182 3.566 3.720 5.1181 3.345 3.74C 3.900 5.358 3.511 3.929 4.096 5.612 1 3.683 4.100 4.280 5.8551
500 520
3.847 4.296 4.477 4.020 4.487 4.677
6.110 6.352
540 56U
4.190 4.670 4.866 4.365 4.860 5.057
6.614 6.850
580 4.541 5.051 5.268 7.123
600 4.725 5.247 5.455 7.388
620 640
4.896 5.437 5.660 5.082 5.627 5.850
7.636 7.893
660 680
5.260 5.831 6.067 5.442 6.020 6.260
8.153 8.400
700 720
5.629 6.229 6.481 5.808 6.425 6.673
8.676 8.912
740 760
6.006 6.635 6.899 6.200 6.833 7.100
9.203 9.460
780 800
6.389 7.046 7.314 6.587 7.250 7.508
9.736 9.992
820 6.779 7.464 7.757 10.272
840 6.970 7.662 7.952 10.512
860 7.176 7.888 8.195 10.814
880 7.375 8.098 8.400 11.175
900 7.579 8.313 8.639 11.360
920 7.795 8.545 8.867 11.625
940 7.989 8.755 9.089 11.911
960 8.200 8.975 9.300 12.180
980 8.406 9.196 9.547 12.473
1000 8.617 9.421 9.776 12.747
From Piping Handbook, by Walker and Crocker. This table gives the expansion from -- 20 F to the
temperature in question. To obtain the amount of expansion between any two temperatures take the difference between the figures in the table for those temperatures. For example,- if a steel pipe is installed at a temperature of 60 F and is to operate at 300 F, the expansion would be 2.519 0.593 = 1.926 in.
PIPE THREADS
All threaded pipe for heating and ventilating installations uses the American Standard taper pipe thread which is made with a taper of 1-in 16 measured on the diameter of the pipe so as to secure a tight joint. Threads of fittings are tapped to the same taper. The number of threads per inch varies with the different pipe sizes. All threaded pipe should be made up with a thread paste suitable for the service under which the pipe is to be used.
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