Flow of fluid = 10 kg/min
Properties of fluid at the inlet :
Pressure p1=1.5bar=1.5×105N/m2
Density ρ1=26kg/m3
Velosity C1=110m/s
Internal energy u1=910kJ/kg
Properties of the fluid at the exit :
Pressure p2=5.5bar=5.5×105N/m2
Density ρ2=5.5kg/m3
Velocity C2=190m/s
Internal energy u2=710kJ/kg
Heat rejected by the fluid, Q=55kJ/s
Rise is elevation of fluid = 55 m
(i) The change in enthalpy,
Δh=Δu+Δ(pv)(i)Δ(pv)=1p2v2−p1v1=ρ2p2−ρ1p1=1×105−0.0577×105=105×0.9423Nm=94.23kJΔu=u2−u1=710−910=−200kJ/kg
Substituting the value in eqn. (i), we get
Δh=−200+94.23=−105.77kJ/kg
(ii) The steady flow equation for unit mass flow can be written as
Q=ΔKE+ΔPE+Δh+W
where Q is the heat transfer per kg of fluid
Q=55kJ/s=6010kg/s55kJ/s=55×6=330kJ/kgΔKE=2C22−C12=21902−1102Nm=12000J=12kJΔPE=(Z2−Z1)g=(55−0)×9.81Nm=539.5J=0.54kJ
Substituting the value in steady flow equation,
−330=12+0.54−105.77+WW=−236.77kJ/kg
Work done per second =−236.77×6010=−39.46kJ/s=−39.46kW
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