- Viscous effects are neglected
- The only losses included are major losses
- All losses are included
With the given Q=0.80 lt/s
Pipe diameter = 2cm
a. Pressure at station 1 when there is no head loss
Energy equation between (1) and (9):
where:
z1 = 0
P9 = 0
z9 = 8.12 m
So pressure head is:
compare with z = 8.12m
b. Pressure at station 1 when there is only major head loss
From the same basic BEE equation, add head loss to station 9. After rearranging, you will get:
Using Moody diagram, f can be projected using Re=45062 and
f = 0.0215
L = total length of pipe from station 1 to station 9 = 4.6m+ 6(3m) = 22.60m
c. Pressure at station 1 including all head losses
With the same BEE equation, add major head loss (using Darcy Weisbach formula) and minor losses (in terms of velocity head), then you get:
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