Five kilograms of steam initially at 1.40 MPa and 650 °C are reversibly and adiabatically expanded to Tsat= 40 °C. Determine the quality of the steam in its final state and the work required.
(Cp=33.59 J/mole-K CV=25.275 J/mole-K)
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Inlet state at 1.40 MPa and 650 °C = superheated steam
Outlet state 40 °C = saturated steam
Specific Entropy of Superheated Steam S = 7.998 kJ/kg-K
Specific Entropy of Saturated Steam Sg = 8.255 kJ/kg-K
Specific Entropy of Saturated Water Sf = 0.5724 kJ/kg-K
Entropy balance
In reversibly and adiabatically expansion
Entropy intlet = entropy outlet
S = xSg + (1-x)Sf
7.998 = x * 8.255 + (1-x)*0.5724
x = (7.998 - 0.5724) / (8.255 - 0.5724)
Quality of steam x = 0.97
Enthalpy of inlet steam H1 = 3807.85 kJ/kg
Enthalpy balance at outlet
H2 = xHg + (1-x)Hf = 0.97*2573.54 + 0.03*167.541
H2 = 2501.36 kJ/kg
Work required W = m (H2 - H1)
= 5 kg x (2501.36 - 3807.85) kJ/kg
= - 6532.45 kJ
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