In: Mechanical Engineering
Thermodynamics
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Given data :
Ammonia at P1 = 10 bar ; T1 = 18 degree celcius And P2 = 5.0 bar
Ammonia enters the expansion valve as compressed liquid.
From saturated liquid tables for Ammonia, we get for T(sat) = 18 degree celcius , we get P(sat) = 8.035 bar
Since we have 10 bar at inlet, we have 10 bar < P(sat). So state of ammonia at intet is compressed liquid.
From the tables we get, h(f) = h(1) = 265.5 kJ/ kg (In the absence of compressed liquid data, we can consider the ammonia as saturated liquid at the given temperature)
Now at exit we have P2 = 5.0 bar and h2 = h1 = 265.5 kJ/kg
From the same saturated tables, we get h(f2) = 199.18 kJ/kg ; h(g2) = 1446.19 kJ.kg
Since h(f2) < h2 < h(g2) , we have saturated liquid-vapor mixture at the exit.
265.5 = 199.18 + x2 (1446.19 - 199.18)
x2 = 0.053
x2 = 5.3%
And T2 = 4.13 degree celcius (from the saturated tables for ammonia)
Students can refer to the saturated tables for ammonia externally.
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