Viscous losses are neglected so only minor losses needed to be considered
Now there are three region for these losses
1. at entrance of Pipe 1
2. Sudden contraction from pipe 1 to pipe 2
3. at the exit from pipe 2
velocity in pipe 1 = Flow rate / Cross-section 1 = Q/(/4*0.1^2)= 127.324 Q m/s
Velocity in pipe 2 = Flow rate / Cross-section 2 = Q/(/4*0.05^2)=509.29 Q m/s
K entrance (loss coefficient =0.5)
loss at entrance = Kentrance * V1^2/2g = 0.5*127.3242Q2/19.62= 413.13 Q2
loss at contraction =K V2^2/2g
K= 0.4 at A2/A1 = 0.25
0.4*509.29 2/19.62 = 5287.99 Q^2
loss at exit = V22/2g = 13219..99 Q^2
so 20 = (413.13+ 5287.99+13219.99 )Q^2
Q=0.0325 m3/s or 3.25 litres/s Ans
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