In: Chemistry
Propane vapor initially at 7.0 bar and 50C (State 1) is contained within a piston-cylinder device. The refrigerant is cooled at constant volume until its temperature reaches -10C (State 2) and is then compressed isothermally to a pressure of 6.0 bar (State 3). (a) Locate the state points on appropriately labeled p-v diagram. (b) Determine the specific volume (in m3 /kg), internal energy (in kJ/kg) and enthalpy (in kJ/kg) at each state point.
a) We will be plotting Pressure vs Volume states in P-V diagram.
That is plotted in attached excel file.
b) We will be calculating specific volume (in m3 /kg), internal energy (in kJ/kg) and enthalpy (in kJ/kg) at each state point. T will be converted to Kelvin.
T |
V (state) |
P |
50 |
1 |
7 |
-10 |
2 |
7 |
-10 |
3 |
6 |
Specific Volume
v = RT/ P
State 1
v = RT/P = ((8.314 * 10 ^-5) * 323.15) / 7
= 0.003838 m3 /kg
State 2
v = RT/P = ((8.314 * 10 ^-5) * 263.15) / 7
= 0.003125 m3 /kg
State 3
v = RT/P = ((8.314 * 10 ^-5) * 263.15) / 6
= 0.003646 m3 /kg
Internal energy
State 1
E = 3/2 RT
= 3/2 * 8.314 * 323.15
= 4030 * 10^-3 kJ/kg
State 2
E = 3/2 RT
= 3/2 * 8.314 * 263.15
= 3281.74 * 10^-3 kJ/kg
State 3
E = 3/2 RT
= 3/2 * 8.314 * 263.15
= 3281.74 * 10^-3 kJ/kg
Enthalpy
H = E + PV as V is constant take it as 1.
State 1
H = E + PV
= 4030 * 10^-3 + 7 * 1
= 11.03 kJ/kg
State 2
H = E + PV
= 3281.74 * 10^-3 + 7 * 1
= 10.28 kJ/kg
State 3
H = E + PV
= 3281.74 * 10^-3 + 7 * 1
= 10.28 kJ/kg