60 
BULLETIN 376, V. S. DEPARTMENT OF AGRICULTURE. 
Service were designed with, the entry loss taken as half the velocity 
head, even though there were more or less rounding and taper in the 
intake structures. In Table 5, column 3, is shown the amount of 
entry loss when taken as half the velocity head (column 2); and the 
sum of the entry and velocity losses is shown in column 4. 
Table 5. — Mean velocity in pipe, V, in feet per second; and head of elevation lost creating 
this velocity and overcoming entrance conditions, h v -\-h e , in feet. 
1 
2 
3 
4 
1 
2 
3 
4 
V 
hv 
he 
hv-rhe 
V 
hv 
h e 
hv+he 
Ft.persec. 
Feet. 
Feet. 
Feet. 
Ft.versec. 
Feet. 
Feet. 
Feet. 
1.0 
0.016 
0.008 
0.024 
5.0 
0.389 
0.195 
0.584 
.2 
.022 
.011 
.033 
.2 
.420 
.210 
.630 
.4 
.030 
.015 
.045 
.4 
.453 
.227 
.680 
.6 
.040 
.020 
.060 
.6 
.488 
.244 
.732 
.8 
.050 
.025 
.075 
.8 
.523 
.262 
.785 
2.0 
.062 
.031 
.093 
6.0 
.560 
.280 
.840 
.2 
.075 
.037 
.112 
.2 
.598 
.299 
.897 
.4 
.090 
.045 
.135 
.4 
.637 
.319 
.956 
.6 
.105 
.053 
.158 
.6 
.677 
.339 
1.016 
.8 
.122 
.061 
.183 
.8 
.719 
.359 
1.078 
3.0 
.140 
.070 
.210 
7.0 
.762 
.381 
1.143 
.2 
.159 
.080 
.239 
.2 
.806 
.403 
1.209 
.4 
.180 
.090 
.270 
.4 
.851 
.426 
1.277 
.6 
.202 
.101 
.303 
.6 
.89S 
.449 
1.347 
.8 
.224 
.112 
.336 
.8 
.946 
.473 
1.419 
4.0 
.249 
.125 
.374 
8.0 
.995 
.498 
1.493 
.2 
.274 
.137 
.411 
.2 
1.045 
.523 
1.568 
.4 
.301 
.151 
.452 
.4 
1.097 
.549 
1.646 
.6 
.329 
.165 
.494 
.6 
1.150 
.575 
1.725 
.8 
.358 
.179 
.537 
.8 
1.204 
.602 
1.806 
Where the usual types of inlet and outlet structures are employed, 
with but little construction and consequent expense incurred for con- 
servation of entry and velocity heads it is recommended that the 
figures in Table 5 be used. In that case any influence on the total 
loss of head, derived from the rate of flow toward the intake as in 
condition 2, where water enters the pipe from an open channel, will 
introduce a small factor of safety for conservative cons time tion. 
The same may be said of any slight recovered velocity head where 
the pipe discharges into an open channel. 
In figure 1, Plate XII, probably the most common form of con- 
struction for both inlet and outlet of a wood-stave siphon is shown. 
In some cases taper staves are used in both inlet and outlet, so that 
the velocity is gradually increased in entering the pipe, thus reduc- 
ing the entry loss. This construction classes the pipe under 
condition 3. The velocity is gradually decreased at the outlet, 
preserving the velocity head. The usual practice in this type of con- 
struction is to place the center of the pipe opening for the inlet cham- 
ber at or below the bottom of the leading canal. The pipe at the 
outlet is usually placed so that the top of the opening is slightly 
below the high-water line at full capacity. 
