Steam expands steadily at a constant temperature. The flow rate is 13.6 kg/min with an inlet state of wet steam (water) at 80% quality to a final state of 700C and 2.5 MPa. The change of kinetic energy across the device is 3.5 kJ/kg, and the heat added is 21.81 kW. Determine (a) the enthalpy of conditions 1 &2, (b) the heat transfer in kJ/kg, (c) the work, and (d) the system power.
(a) Mass flow rate = 13.6 kg/min
Inlet state quality (x) = 0.8
Final state : temperature T2 = 70 °C
P2 = 2.5 MPa.
Change in kinetic energy = 3.5 KJ/Kg
Heat added (Q) = 21.81 KW
Steam is expanding at constant temperature
Therefore T1 = T2
or T1 = 70 °C
And x = 0.8
at temperature T = 70 °C
hf = 293.02 KJ/Kg
hg = 2626.01 KJ/Kg
So h1 = hf + x × (hg- hf)
= 293.02 + 0.8×(2626.01-293.02)
= 2159.41 KJ/Kg
P2 = 2.5 MPa
T2= 70 °C
At this set of temperature and pressure fluid is in liquid state.
h2 = 295.04 KJ/Kg
(b) Heat transfer in KJ/ Kg
Heat transfer = 21.81 KW
Mass flow rate = 13.6 Kg/ min
"= \\frac{13.6 }{ 60} \\; Kg\/s \\\\\n\n=0.227 Kg\/s"
So heat transfer in KJ/Kg "= \\frac{21.81}{0.227}"
=96.08 KJ/Kg
(c) Energy equation per unit mass
"h_1 + \\frac{v^2_1}{2g} + H_1 + \\frac{dQ}{dm} = h_2 + \\frac{v^2_2}{2g} + H_2 + \\frac{dW}{dm} \\\\\n\n\u0394K \\times E = 3.5 \\;kg\/kg \\\\\n\nH_1=H_2 \\\\\n\n\\frac{dQ}{dm} = 96.08 \\;kJ\/kg \\\\\n\n2159.41 + 96.08 = 295.04 + 3.5 + \\frac{dW}{dm} \\\\\n\n\\frac{dW}{dm} = 1956.95 \\;kJ\/kg"
(d) System power "= \\frac{dW}{dm} \\times \\frac{dm}{dt}"
"= 1956.95 \\times 0.227 \\\\\n\n= 444.23 \\;kW"
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