Given data
Pressure P = 80 kPa
Temperature T = 10°C = 283 K
Velocity V = 200 m/s
Area of diffuser = 0.5 m2
Gas constant R =0.287 kPa-m3 /kg-K
Part a
Calculate the specific volume
= R x T/P
= 0.287 kPa-m3 /kg-K x 283 K / 80 kPa
= 1.015 m3/kg
Mass flow rate = velocity x Area / Specific volume
= 200 x 0.5 / 1.015
= 98.497 kg/s
Part b
At T1 = 283 K
Enthalpy, h1 = 283.14 kJ/kg
At steady state
Enthalpy in = enthalpy out
283.14 x 200 x 200 / 2 = h2
h2 = 303.14 kJ/kg
From the air properties
T2 = 303.14 K
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