It is a steady flow process, so,
(DH + Dv2)/2 + gDz = Q + Ws
Here,
Ws = 0 as it does not have shaft work,
Dz = 0 as there is a straight horizontal flow,
Q = 0 as no heat is being transferred
So,
(DH + Dv2)/2 + g(0) = (0) + (0)
DH + Dv2/2 = 0
Now continuity equations are:
A1v1= A2v2
Therefore,
A1/A2 = v2/v1 = (d1)^2/(d2)^2 = (2.54)^2 / (3.81)^2 = 6.4516/14.5161
=0.444444444439
v2 = 9.144 x 0.44444= 4.06399 m/s
Now,
DH = [(v2)^2 - (v1)^2)] / 2
DH = [(4.06399)^2 - (9.144)^2) / 2
DH = -33.54836 j/kg
Enthalpy change = 33.54836 per kg mass
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