146 ENGINEERING THERMODYNAMICS
dharm
/M-therm/Th4-3.pm5
= (15 × 10^5 ) × 0.15 × loge (4)
= 311916 J = 311.9 kJ
Considering constant volume process 2–3,
we get
V 2 = V 3 = 4 × 0.15 = 0.6 m^3
p
T
p
T
2
2
3
3
=
or, p 3 = p 2 × T
T
3
2
375 290
550
=×. = 1.98 bar
W2–3 = 0
... since volume remains constant
Consider polytropic process 3–1 :
p 3 V 3 n = p 1 V 1 n or
p
p
V
V
n
1
3
3
1
=
F
HG
I
KJ
Taking log on both sides, we get
loge (p 1 /p 3 ) = n loge (V 3 /V 1 )
or, n = log ( / )
log ( / )
log ( /. )
log (
e
e
e
e
pp
VV
13
31
15 1 98
4)
= = 1.46
W3–1 = pV pV
n
33 11
55
1
19810 061510 015
146 1
−
−
= ××−××
−
...
(. )
= – 230869 J or – 230.87 kJ
∴Net work done= W1–2 + W2–3 + W3–1
= 311.9 + 0 + (– 230.87) = 81.03 kJ. (Ans.)
For a cyclic process, zzδδQW=
∴ Heat transferred during the cycle = 81.03 kJ. (Ans.)
Example 4.33. A system consisting of 1 kg of an ideal gas at 5 bar pressure and 0.02 m^3
volume executes a cyclic process comprising the following three distinct operations : (i) Reversible
expansion to 0.08 m^3 volume, 1.5 bar pressure, presuming pressure to be a linear function of
volume (p = a + bV), (ii) Reversible cooling at constant pressure and (iii) Reversible hyperbolic
compression according to law pV = constant. This brings the gas back to initial conditions.
(i)Sketch the cycle on p-V diagram.
(ii)Calculate the work done in each process starting whether it is done on or by the system
and evaluate the net cyclic work and heat transfer.
Solution. Given : m = 1 kg ; p 1 = 5 bar ; V 1 = 0.02 m^3 ; V 2 = 0.08 m^3 ; p 2 = 1.5 bar.
(i)p-V diagram : p-V diagram of the cycle is shown in Fig. 4.26.
(ii)Work done and heat transfer :
l Process 1-2 (Linear law) :
p = a + bV ...(Given)
The values of constants a and b can be determined from the values of pressure and volume
at the state points 1 and 2.
15 1
p 2
V=C
p (bar)
0.15 V(m )^3
pV=C
pV = Cn
p 3 3 (290 K)
V=V 23
2
Fig. 4.25