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iii) wet steam of 95% steam quality and 65.0 bar is expanded to wet steam of 80% steam quality at 1.0 bar using a turbine in

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Answer #1

To solve the above question, thermodynamic tables must be looked at.

The equation to be used is: w = h_i - h_e + \frac{V_i^2 - V_e^2}{2} + g(Z_i - Z_e) .

However, there is no change in kinetic or potential energy in this case. Therefore, the work can be calculated simply by looking at the change in enthalpy of the 2 states.

State 1

x1 = 0.95

P = 65 bar = 6500000 Pa

From the tables, hi = 2701.23 kJ/kg

State 2

x2 = 0.8

P = 1 bar

From the tables, he = 2223.58 kJ/kg

a) The shaft work is 477.648 kJ/kg

b) Since the process is adiabatic, the removal of heat is zero. This makes the efficiency of the expander infinity.

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