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Some of the topic in thermodynamics are: Property tables and ideal gases, First law for closed and open (steady and unsteady) systems, Entropy and maximum work calculations, Isentropic efficiencies, Cycle calculations (Rankine, refrigeration, air standard) with mass flow rate ratios. This quiz is about: Heat, Internal Energy and the First Law, Constant Pressure, Constant Volume, Expansion to a Volume, Internal Energy, First Law, Enthalpy
Typology: Exercises
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1 A mass of 0.1 kg of water fills a piston-cylinder apparatus with an initial volume of V 1 = 0.01 m^3. The water then undergoes a three step path where the initial and final states are the same:
a. an expansion to a volume of V 2 = 0.02 m^3 following the path equation P = a + b/V where a = 3 MPa and b = – 0.02 MPa·m 3 .
b. a constant volume decrease in pressure P 3 = P 1 , the initial pressure.
c. a constant pressure decrease in volume to V 4 = V 1 , the initial volume.
Find the heat transfer for (i) part a of the path and (ii) the entire path.
We can use the path equation to find the work for part a as pathPdV.
1
2 2 1 ln
2
1
dV aV V b V
b W PdV a
V
patha V
a
MPa m MJ kJ
m
m MPa m m MPa m V
Wa aV V b
ln 3 0. 02 0. 01 0. 02 ln
3
3
3 3 3 3
1
2 2 1
The heat transfer along this path can be found from the first law: Qa = Ua + Wa = (u 2 – u 1 ) + Wa. We can find the internal energy, u 1 at the initial state v 1 = V 1 /m = (0.01 m^3 )/(0.1 kg) = 0.1 m^3 /kg and P 1 = a + b/V 1 = (3 MPa) + (-0.02 MPa·m 3 ) / (0.01 m 3 ) = 1 MPa. From the saturation table at P 1 = 1 MPa we see that this specific volume is between vf and vg, so we must be in the mixed region. We can find the internal energy from the quality:
3
3 3
1
1 1 1
kg
m
kg
m kg
m
v P MPa
v v P MPa x fg
f
kg
kJ kg
kJ kg
u u P MPa xu P MPa kJ 1 f (^11 ) 1 fg ( 1 1 )^761.^37 (^0.^5115 )^1821.^8 ^1693.^2
Since the tables do not have internal energy, we have to compute it from the enthalpy. At the final state, P 2 = a + b/V 2 = 3 MPa + (–0.02 MPa·m 3 )/(0.2 m 3 ) = 2 MPa, and v 2 = V 2 /m = (0. m^3 )/(0.1 kg) = 0.2 m^3 /kg. At this pressure and specific volume we see that the temperature is very close to 600 o C. If we used interpolation we would find the final enthalpy as follows:
kg
kJ
kg
m
kg
m
kg
m
kg
m
kg
kJ
kg
kJ
kg
kJ h
3 3
(^2 )
We can now find the internal energy at the end of the first path, u 2.
kg
kJ
MPa m
kJ
kg
m MPa kg
kJ u h Pv
3
3
2 2 2 2
We can now find the heat transfer for step a from the first law.
kg
kJ
kg
kJ Q (^) a mu u Wa kg 16. 137
Qa = 176.2 kJ
For the entire path the initial and final states are the same so the internal energy change is zero.
(U depends only on the state; it the initial and final states are the same, the value of u at both
states is the same so DU = 0) This gives Q = W = Wa + Wb + Wc for the overall path. We have
found Wa = 16.137 kJ and we know that Wb = 0 for the constant volume step in part b of the path.
The third part of the path, at constant pressure P 3 = P 4 = P 1 = 1 MPa is found as follows: Wc =
Pconst (V 4 – V 3 ) = (1 MPa)(0.01 m 3
transfer for the overall path is then found to be Q = W = Wa + Wb + Wc = 16.137 kJ + 0 + (–10 kJ)
or Q = 6.137 kJ