J2006 termodinamik 1 unit10

THE SECOND LAW OF THERMODYNAMICS J2006/10/1
THE SECOND LAW OF THERMODYNAMICS
OBJECTIVES
General Objective : To define and explain the Second Law of Thermodynamics and
perform calculations involving the expansion and compression of
perfect gases.
Specific Objectives : At the end of the unit you will be able to:
 sketch the processes on a temperature-entropy diagram
 calculate the change of entropy, work and heat transfer of
perfect gases in reversible processes at:
i. constant pressure process
ii. constant volume process
iii. constant temperature (or isothermal) process
iv. adiabatic (or isentropic) process
v. polytropic process
UNIT 10

10.0 The P-V and T-s diagram for a perfect gas
Property diagrams serve as great visual aids in the thermodynamic analysis of
processes. We have used P-V and T-s diagrams extensively in the previous unit
showing steam as a working fluid. In the second law analysis, it is very helpful to
plot the processes on diagrams which coordinate the entropy. The two diagrams
commonly used in the second law analysis are the pressure-volume and
temperature-entropy.
Fig. 10.0-1 shows a series of constant temperature lines on a P-V diagram. The
constant temperature lines, T3 > T2 > T1 are shown.
Figure 10.0-1 The constant temperature lines on a P-V diagram for a perfect gas
Since entropy is a property of a system, it may be used as a coordinate, with
temperature as the other ordinate, in order to represent various cycles graphically. It
is useful to plot lines of constant pressure and constant volume on a T-s diagram for
a perfect gas. Since changes of entropy are of more direct application than the
absolute value, the zero of entropy can be chosen at any arbitrary reference
temperature and pressure.
INPUTINPUT
T3 > T2 > T1
P
V
T1
T2
T3
Constant temperature lines

Fig. 10.0-2 shows a series of constant pressure lines on a T-s diagram and Fig.10.0-3
shows a series of constant volume lines on a T-s diagram. It can be seen that the
lines of constant pressure slope more steeply than the lines of constant volume.
Note:
 Fig. 10.0-2, shows the constant pressure lines, P3 > P2 > P1;
 Fig. 10.0-3, shows the constant volume lines, v1 > v2 > v3.
As pressure rises, temperature also rises but volume decreases; conversely as the
pressure and temperature fall, the volume increases.
T
s
P1
P2
P3
Figure 10.0-2
Constant pressure lines on a T-s diagram
T
s
v2
v1
v3
Figure 10.0-3
Constant volume lines on a T-s diagram

10.1 Reversible processes on the T-s diagram for a perfect gas
The various reversible processes dealt with in Units 4 and 5 will now be considered
in relation to the T-s diagram. In the following sections of this unit, five reversible
processes on the T-s diagram for perfect gases are analysed in detail. These
processes include the:
i. constant pressure process,
ii. constant volume process,
iii. constant temperature (or isothermal) process,
iv. adiabatic (or isentropic) process, and
v. polytropic process.
10.1.1 Reversible constant pressure process
It can be seen from Fig. 10.1.1 that in a constant pressure process, the
boundary must move against an external resistance as heat is supplied; for
instance a fluid in a cylinder behind a piston can be made to undergo a
constant pressure process.
During the reversible constant pressure process for a perfect gas, we have
The work done as
W = P(V2 – V1) kJ (10.1)
or, since PV = mRT , we have
W = mR(T2 - T1) kJ (10.2)
The heat flow is,
Q = mCp(T2 – T1) kJ (10.3)
The change of entropy is, then
T
s
P1
= P2
v2
v1
1
2
s1
s2
Q
Figure 10.1.1 Constant pressure process on a T-s diagram

Nitrogen (molecular weight 28) expands reversibly in a cylinder behind a
piston at a constant pressure of 1.05 bar. The temperature is initially at
27o
C. It then rises to 500o
C; the initial volume is 0.04 m3
. Assuming
nitrogen to be a perfect gas and take Cp = 1.045 kJ/kg K, calculate the:
a) mass of nitrogen
b) work done by nitrogen
c) heat flow to or from the cylinder walls during the expansion
d) change of entropy
Sketch the process on a T-s diagram and shade the area which represents
the heat flow.
S2 – S1 = mCp ln
T
T
2
1





 kJ/K
(10.4)
or, per kg of gas we have,
s2 – s1 = Cp ln
T
T
2
1





 kJ/kg K (10.5)
Example 10.1
Solution to Example 10.1
The given quantities can be expressed as;
T1 = 27 + 273 K = 300 K
P1 = P2 = 1.05 bar (constant pressure process)
V1 = 0.04 m3
T2 = 500 + 273 = 773 K
M = 28 kg/kmol
Cp = 1.045 kJ/kg.K
a) From equation 3.10, we have

kg0.0471
300x0.297
0.04x10x1.05
havewe,=sinceThen
KkJ/kg0.297
28
3144.8
2
1
11
===
===
RT
VP
m
mRTPV
M
R
R o

b) the work done by nitrogen can be calculated by two methods. Hence,
we have
Method I:
From equation 10.2, work done
W = mR(T2 - T1)
= 0.0471 x 0.297 (773 - 300)
= 6.617 kJ
Method II:
For a perfect gas at constant pressure,
2
2
1
1
T
V
T
V
=
kJ6.615
0.04)-(0.10310x1.05
)(
donework10.1,equationFrom
m0.103
300
773
0.04
2
12
3
1
2
12
=
=
−=
=





=





=
VVPW
T
T
VV
c) From equation 10.3, heat flow
Q = mCp(T2 - T1)
= 0.0471 x 1.045 (773 - 300)
= 23.28 kJ
d) From equation 10.4, change of entropy
s2 - s1 = mCp ln
T
T
2
1






=






=
0.0471 x 1.045 ln
773
300
kJ / K0 0466.
The T-s diagram below shows the constant pressure process. The shaded
area represents the heat flow.
T
s
P1
= P2
= 1.05 bar
v2
= 0.103 m3
v1
= 0.04 m3
1
2
s1
s2
Q
T1
= 300 K
T2
= 773 K

10.1.2 Reversible constant volume process
In a constant volume process, the working substance is contained in a rigid
vessel (or closed tank) from which heat is either added or removed. It can be
seen from Fig. 10.1.2 that in a constant volume process, the boundaries of the
system are immovable and no work can be done on or by the system. It will
be assumed that ‘constant volume’ implies zero work unless stated otherwise.
During the reversible constant volume process for a perfect gas, we have
The work done, W = 0 since V2 = V1.
The heat flow
Q = mCv(T2 – T1) kJ (10.6)
The change of entropy is therefore
S2 – S1 = mCv ln
T
T
2
1





 kJ/K
(10.7)
or, per kg of gas we have,
s2 – s1 = Cv ln
T
T
2
1





 kJ/ kg K (10.8)
T
s
v1
= v2
P1
1
2
s1
s2
Q
P2
Figure 10.1.2 Constant volume process on a T-s diagram

Air at 15o
C and 1.05 bar occupies a volume of 0.02 m3
. The air is heated at
constant volume until the pressure is at 4.2 bar, and then it is cooled at
constant pressure back to the original temperature. Assuming air to be a
perfect gas, calculate the:
a) mass of air
b) net heat flow
c) net entropy change
Sketch the processes on a T-s diagram.
Given:
R = 0.287 kJ/kg K, Cv = 0.718 kJ/kg K and Cp = 1.005 kJ/kg K.
Example 10.2
T1 = 15 + 273 K = 288 K
P1 = 1.05 bar
Process 1 - 2 (constant volume process): V1 = V2 = 0.02 m3
Process 2 - 3 (constant pressure process) : P2 = P3 = 1.05 bar
T3 = T1 = 288 K
a) From equation 3.6, for a perfect gas,
kg0.0254
288x0.287
0.02x10x1.05 2
1
11
===
RT
VP
m
b) For a perfect gas at constant volume,
2
2
1
1
T
P
T
P
= , hence
K1152
05.1
2.4
288
1
2
12 =





=





=
P
P
TT
From equation 10.6, at constant volume
Q12 = mCv(T2 – T1) = 0.0254 x 0.718 (1152 – 288) = 15.75 kJ
From equation 10.3, at constant pressure
Q23 = mCp(T3 – T2) = 0.0254 x 1.005 (288 – 1152) = -22.05 kJ

∴ Net heat flow = Q12 + Q23 = (15.75) + ( -22.05) = -6.3 kJ
c) From equation 10.7, at constant volume
S2 – S1 = mCv ln
T
T
2
1






From equation 10.4, at constant pressure
S3 – S2 = mCp 





2
3
ln
T
T
∴ Net entropy change, (S3 – S1) = (S2 – S1) + (S3 – S2)
= (0.0253) + (-0.0354)
= - 0.0101 kJ/K
i.e. decrease in entropy of air is 0.0101 kJ/K.
Note that since entropy is a property, the decrease of entropy in example
10.2, given by (S3 – S1) = (S2 – S1) + (S3 – S2), is independent of the
processes undergone between states 1 and 3. The change (S3-S1) can also
be found by imagining a reversible isothermal process taking place between
kJ/K0253.0
288
1152
ln0.718x0.0254
=






=
kJ/K0354.0
1152
288
ln1.005x0.0254
−=






=
T
s
P2
= P3
= 4.2 bar
v1
= v2
= 0.02 m3
v3
3
2
s3
s2
T1
= T3
= 288 K
T2
= 1152 K
1
P1
= 1.05 bar
s1

1 and 3. The isothermal process on the T-s diagram will be considered in
the next input.
10.1.3 Reversible constant temperature (or isothermal) process
A reversible isothermal process for a perfect gas is shown on a T-s diagram
in Fig. 10.1.3. The shaded area represents the heat supplied during the
process,
i.e. Q = T(s2 - s1) (10.9)
For a perfect gas undergoing an isothermal process, it is possible to evaluate
the entropy changes, i.e. (s2 – s1). From the non-flow equation, for a
reversible process, we have
dQ = du + P dv
Also for a perfect gas from Joule’s Law, du = Cv dT,
dQ = Cv dT + P dv
For an isothermal process, dT = 0, hence
dQ = P dv
Then, since Pv = RT, we have
v
v
RTQ
d
d =
T
s
P2
v2v1
1 2
s1
s2
Q
Figure 10.1.3 Constant temperature (or isothermal) process on a T-s diagram
P1
T1
= T2

Now from equation 9.5
∫∫∫ ===−
2
1
2
1
ddd2
1
12
v
v
v
v v
v
R
Tv
vRT
T
Q
ss
i.e. 





=





=−
2
1
1
2
12 lnln
p
p
R
v
v
Rss kJ/kg K (10.10)
or, for mass, m (kg), of a gas
S2 – S1 = m(s2 – s1)
i.e. 





=





=−
2
1
1
2
12 lnln
p
p
mR
v
v
mRSS kJ/K (10.11)
Therefore, the heat supplied is given by,
( ) 





=





=−=
2
1
1
2
12 lnln
p
p
RT
v
v
RTssTQ
or, for mass, m (kg), of a gas
( ) 





=





=−=
2
1
1
2
12 lnln
p
p
mRT
v
v
mRTSSTQ
In an isothermal process,
(U2 – U1) = mCv (T2 - T1)
= 0 ( i.e since T1 = T2)
From equation Q - W = (U2 – U1),
∴ W = Q (10.12)
0

0.85 m3
of carbon dioxide (molecular weight 44) contained in a cylinder
behind a piston is initially at 1.05 bar and 17 o
C. The gas is compressed
isothermally and reversibly until the pressure is at 4.8 bar. Assuming
carbon dioxide to act as a perfect gas, calculate the:
e) mass of carbon dioxide
f) change of entropy
g) heat flow
h) work done
Sketch the process on a P-V and T-s diagram and shade the area which
represents the heat flow.
Example 10.3
V1 = 0.85 m3
M = 44 kg/kmol
P1 = 1.05 bar
Isothermal process: T1 = T2 = 17 + 273 K = 290 K
P2 = 4.8 bar
kJ/kgK189.0
44
3144.8
===
M
R
R o
Then, since PV = mRT, we have
kg1.628
290x0.189
0.85x10x1.05 2
===
RT
PV
m
b) From equation 10.11, for m kg,
kJ/K0.4676
8.4
05.1
ln0.189x1.628ln
2
1
12 −=





=





=−
p
p
mRSS
c) Heat rejected = shaded area on T-s diagram

= T (S2 – S1)
= 290 K(-0.4676 kJ/K)
= -135.6 kJ (-ve sign shows heat rejected from the system to
the surroundings)
d) For an isothermal process for a perfect gas, from equation 10.12
W = Q
= -135.6 kJ (-ve sign shows work is transferred into the system)
T
s
P1
= 1.05 bar
2 1
s2
s1
Q
P2
= 4.8 bar
T1
= T2
= 290 K

TEST YOUR UNDERSTANDING BEFORE YOU CONTINUE WITH THE
NEXT INPUT…!
10.1 0.1 m3
of air at 1 bar and temperature 15o
C is heated reversibly at constant
pressure to a temperature of 1100o
C and volume 0.48 m3
. During the process,
calculate the:
a) mass of air
b) change of entropy
c) heat supplied
d) work done
Show the process on a T-s diagram, indicating the area that represents the
heat flow.
Given, R = 0.287 kJ/kg K and Cp = 1.005 kJ/kg K.
10.2 0.05 kg of nitrogen (M = 28) contained in a cylinder behind a piston is
initially at 3.8 bar and 140 o
C. The gas expands isothermally and reversibly
to a pressure of 1.01 bar. Assuming nitrogen to act as a perfect gas,
determine the:
a) change of entropy
b) heat flow
c) work done
Show the process on a T-s diagram, indicating the area which represents the
heat flow.
Activity 10A

Feedback To Activity 10A
10.1 The given quantities can be expressed as;
P1 = P2 = 1 bar (constant pressure process)
T1 = 15 + 273 K = 288 K
V1 = 0.1 m3
T2 = (1100 + 273) = 1373K
V2 = 0.48 m3
R = 0.287 kJ/kg.K
Cp = 1.005 kJ/kg.K
a) From equation PV =mRT, we have
kg0.121
288x0.287
0.1x10x1 2
1
11
===
RT
VP
m
b) From equation 10.4, change of entropy
s2 - s1 = mCp ln
T
T
2
1






kJ/K1899.0
288
1373
ln1.005x0.121
=






=
c) From equation 10.3, heat flow
Q = mCp(T2 - T1)
= 0.121 x 1.005 (1373 - 288)
= 131.9 kJ

d) The work done by air can be calculated by using two methods which
give the same results.
Method I:
From equation 10.2, the work done
W = mR(T2 - T1)
= 0.121 x 0.287 (1373 - 288)
= 38 kJ
Method II:
kJ83
0.1)-(0.48101.x
)(
doneworkthe10.1,equationFrom
2
12
=
=
−= VVPW
The T-s diagram below shows the constant pressure process. The shaded
area represents the heat flow.
T
s
P1
= P2
= 1bar
v2
= 0.48 m3
v1
= 0.1 m3
1
2
s1
s2
Q
T1
= 288 K
T2
= 1373 K

m = 0.05 kg
M = 28 kg/kmol
P1 = 3.8 bar
Isothermal process: T1 = T2 = (140 + 273 K) = 413 K
P2 = 1.01 bar
kJ/kgK297.0
28
3144.8
===
M
R
R o
From equation 10.11, for m kg of gas,
kJ/K01968.0
01.1
8.3
ln0.297x05.0
ln
2
1
12
=






=






=−
p
p
mRSS
b) Heat flow = shaded area on T-s diagram
= T (S2 – S1)
= 413 (0.01968)
= 8.1278 kJ
c) For an isothermal process for a perfect gas, from equation 10.12
W = Q
= 8.1278 kJ
T
s
P1
= 3.8 bar
1 2
s1
s2
Q
P2
= 1.01 bar
T1
= T2
= 413 K
INPUTINPUT

10.1.4 Reversible adiabatic (or isentropic) process
In the special case of a reversible process where no heat energy is transferred
to or from the gas, the process will be a reversible adiabatic process. These
special processes are also called isentropic process. During a reversible
isentropic process, the entropy remains constant and the process will always
appear as a vertical line on a T-s diagram.
For a perfect gas, an isentropic process on a T-s diagram is shown in Fig.
10.1.4. In Unit 4 it was shown that for a reversible adiabatic process for a
perfect gas, the process follows the law pvγ
= constant.
Since a reversible adiabatic process occurs at constant entropy, and is known
as an isentropic process, the index γ is known as the isentropic index of the
gas.
For an isentropic process,
Change of entropy, s2 - s1 = 0
T
s
P2
v2
v1
1
2
s1
= s2
Figure 10.1.4 Reversible adiabatic (or isentropic) process on a T-s diagram
P1
T1
T2

In an air turbine unit, the air expands adiabatically and reversibly from 10
bar, 450 o
C and 1 m3
to a pressure of 2 bar. Air is assumed to act as a
perfect gas. Given that Cv = 0.718 kJ/kg K, R = 0.287 kJ/kg K and γ = 1.4,
calculate the:
a) mass of air
b) final temperature
c) work energy transferred
Sketch the process on a T-s diagram.
Heat flow, Q = 0
From the non-flow equation,
dQ - dW = dU
dW = -dU
= -mCv dT
= -mCv(T2 - T1)
∴ W = mCv(T1 -T2) (10.13)
or, since 1−
=
γ
R
Cv , we have
1
)( 21
−
−
=
γ
TTmR
W (10.14)
or, since PV = mRT, we also have
1
2211
−
−
=
γ
VPVP
W (10.15)
Note that the equations 10.13, 10.14 and 10.15 can be used to find the work
done depending on the properties of gases given. Each equation used gives
the same result for a work done.
Similarly, equation 10.16 can also be used to determine the temperature,
pressure and volume of the perfect gases.
T
T
P
P
V
V
2
1
2
1
1
1
2
1
=





 =






−
−
γ
γ
γ
(10.16)
Example 10.4

P1= 10 bar
V1 = 1 m3
T1 = (450 + 273) = 723K
P2 = 2 bar
Cv = 0.718 kJ/kg K
R = 0.287 kJ/kg K
γ = 1.4
Isentropic process, s2 = s1
a) From equation PV = mRT, for a perfect gas
kg82.4
723x0.287
1x10x10 2
1
11
===
RT
VP
m
b) The final temperature can be found using equation 10.16
K5.456
10
2
x723
x
4.1
14.1
1
1
2
12
=






=






=
−
−
γ
γ
P
P
TT
c) The work energy transferred can be found using equation 10.13
W = mCv(T1 -T2)
= 4.82 x 0.718 (723 – 456.5)

= 922 kJ
Similarly, the equation 10.14 gives us the same result for the value of
work energy transferred as shown below,
1
)( 21
−
−
=
γ
TTmR
W
kJ922
14.1
)5.456723(287.0x82.4
=
−
−
=
10.1.5 Reversible polytropic process
T
s
P2
= 2 bar
v2
v1
= 1 m3
1
2
s1
= s2
P1
= 10 bar
T1
= 723 K
T2
= 456.5 K

For a perfect gas, a polytropic process on a T-s diagram is shown in Fig.
10.1.5. In Unit 5 it was shown that for a reversible polytropic process for a
perfect gas, the process follows the law pvn
= constant.
For a reversible polytropic process,
Work done by a perfect gas is,
1
2211
−
−
=
n
VPVP
W (10.17)
or, since PV = mRT, we have
( )
W
mR T T
n
=
−
−
1 2
1
(10.18)
Change of internal energy is,
U2 -U1 = mCv(T2 -T1) (10.19)
The heat flow is,
Q = W + U2 -U1 (10.20)
It was shown in Unit 5 that the polytropic process is a general case for perfect
gases. To find the entropy change for a perfect gas in the general case,
consider the non-flow energy equation for a reversible process as,
T
s
P2
v2
v1
1
2
s1
Figure 10.1.5 Reversible polytropic process on a T-s diagram
P1
T1
T2
A B
s2
sA
sB

dQ = dU + P dv
Also for unit mass of a perfect gas from Joule’s Law dU = CvdT , and from
equation Pv = RT ,
∴
v
vRT
TCQ v
d
dd +=
Then from equation 9.5,
v
vR
T
TC
T
Q
s v ddd
d +==
Hence, between any two states 1 and 2,






+





=+=− ∫∫ 1
2
1
2
12 lnln
dd 2
1
2
1 v
v
R
T
T
C
v
v
R
T
T
Css v
v
v
T
T
v (10.21)
This can be illustrated on a T-s diagram as shown in Fig. 10.1.5. Since in the
process in Fig. 10.1.5, T2 < T1, then it is more convenient to write the
equation as






−





=−
2
1
1
2
12 lnln
T
T
C
v
v
Rss v (10.22)
There are two ways to find the change of entropy (s2 – s1). They are:
a) According to volume
It can be seen that in calculating the entropy change in a polytropic
process from state 1 to state 2 we have in effect replaced the process
by two simpler processes; i.e. from 1 to A and then from A to 2. It is
clear from Fig. 10.1.5 that
s2 - s1 = (sA - s1) - (sA - s2)
The first part of the expression for s2 -s1 in equation 10.22 is the
change of entropy in an isothermal process from v1 to v2.
From equation 10.10
(sA - s1)=





R
v
v
ln 2
1
(see Fig. 10.1.5)
In addition, the second part of the expression for s2 -s1 in equation
10.22 is the change of entropy in a constant volume process from T1
to T2,
i.e. referring to Fig. 10.1.5,

(sA - s2) =





C
T
Tv ln 1
2
∴ s2 - s1 =





−





R
v
v
C
T
Tvln ln2
1
1
2
kJ/kg K
(10.23)
or, for mass m, kg of gas we have
S2 - S1 





−





=
2
1
1
2
lnln
T
T
mC
v
v
mR v kJ/K (10.24)
b) According to pressure
According to pressure, it can be seen that in calculating the entropy
change in a polytropic process from state 1 to state 2 we have in
effect replaced the process by two simpler processes; i.e. from 1 to B
and then from B to 2 as in Fig. 10.1.5. Hence, we have
s2 - s1 = (sB - s1) - (sB - s2)
At constant temperature (i.e. T1) between P1 and P2, using equation
10.10,
(sB - s1) =





R
p
p
ln
1
2
and at constant pressure (i.e. P2) between T1 and T2 we have
(sB - s2) =





C
T
Tp ln
1
2
Hence,
s2 - s1 =





−





R
p
p
C
T
Tpln ln1
2
1
2
kJ/kg K
(10.25)
or, for mass m, kg of gas we have

S2 - S1 





−





=
2
1
2
1
lnln
T
T
mC
p
p
mR p kJ/K (10.26)
Similarly, the equation 10.27 can also be used to determine the
temperature, pressure and volume of the perfect gases in polytropic
process.
1
2
1
1
1
2
1
2
−
−






=





=
n
n
n
V
V
P
P
T
T
(10.27)
Note that, there are obviously a large number of possible equations for the
change of entropy in a polytropic process, and it is stressed that no attempt
should be made to memorize all such expressions. Each problem can be
dealt with by sketching the T-s diagram and replacing the process by two other
simpler reversible processes, as in Fig. 10.1.5.

0.03 kg of oxygen (M = 32) expands from 5 bar, 300 o
C to the pressure of 2
bar. The index of expansion is 1.12. Oxygen is assumed to act as a perfect
gas. Given that Cv = 0.649 kJ/kg K, calculate the:
i) change of entropy
j) work energy transferred
Sketch the process on a T-s diagram.
Example 10.5
m = 0.03 kg
M = 32 kg/kmol
P1= 5 bar
T1 = (300 + 273) = 573K
P2 = 2 bar
Cv = 0.649 kJ/kg K = 649 J/kg K
PV1.12
= C
KJ/kg260
32
8314
===
M
R
R o
Then from equation R = Cp - Cv , we have
Cp = R + Cv
= 260 + 649
= 909 J/kg K
From equation 10.27, we have
T
T
p
p
n
n
2
1
2
1
1
=






−
T T
P
P
n
n
2 1
2
1
1 1 12 1
1 12
573
2
5
519 4=





 =





 =
− −.
.
. K
∴ From equation 10.26, the change of entropy (S2 - S1 ) is,

S2 - S1 = (SB - S1) - (SB - S2)
J/K4.47
)68.2()15.7(
519.4
573
lnx909x0.03
2
5
lnx260x0.03
lnln
2
1
2
1
=
−=






−





=






−





=
T
T
mC
p
p
mR p
b) From equation 10.18, we have
( )
W
mR T T
n
=
−
−
1 2
1
J3.417
1
519.5)(573260x0.03
=
−
−
=
n
T
s
P2
= 2 bar
1
2
s1
P1
= 5 bar
T1
= 573 K
T2
= 519.4 K
B
s2
sB
Activity 10B

TEST YOUR UNDERSTANDING BEFORE YOU PROCEED TO THE SELF-
ASSESSMENT…!
10.3 0.225 kg of air at 8.3 bar and 538 o
C expands adiabatically and reversibly to a
temperature of 149 o
C. Determine the
a) final pressure
b) final volume
c) work energy transferred during the process
Show the process on a T-s diagram.
For air, take Cp = 1.005 kJ/kg K and R = 0.287 kJ/kg K.
10.4 1 kg of air at 1.01 bar and 27 o
C, is compressed according to the law
PV1.3
= constant, until the pressure is 5 bar. Given that Cp = 1.005 kJ/kg K
and R = 0.287 kJ/kg K, calculate the final temperature and change of entropy
and then sketch the process on a T-s diagram.

Feedback To Activity 10B
m = 0.225 kg
P1 = 8.3 bar
T1 = 538 + 273 K = 811 K
T2 = 149 + 273 K = 422 K
Cp = 1.005 kJ/kg K
R = 0.287 kJ/kg K
Adiabatic / isentropic process : s2 = s1
Cv = Cp – R = 1.005 – 0.287 = 0.718 kJ/kg K
Then, from equation 3.17, we have
4.1
718.0
005.1
===
v
p
C
C
γ
For a reversible adiabatic process for a perfect gas, PVγ
= constant.
From equation 10.16
bar0.844
811
422
)3.8(
14.1
4.1
2
1
1
2
1
2
=






=






=
−
−
P
T
T
P
P γ
γ
b) From the characteristic gas equation PV = mRT, hence, we have at
state 2

3
2
2
2
2 m0.323
10x0.844
422x0.287x0.225
===
P
mRT
V
c) The work energy transferred can be found from equation 10.13
W = mCv(T1 -T2)
= 0.225 x 0.718 (811 – 422)
= 62.8 kJ
Similarly, the equation 10.14 gives us the same result for the value of
work energy transferred as shown below,
1
)( 21
−
−
=
γ
TTmR
W
kJ8.62
14.1
)422811(287.0x.2250
=
−
−
=
m = 1 kg
P1= 1.01 bar
T1 = (27 + 273) = 300 K
T
s
P2
= 0.844 bar
v2
v1
1
2
s1
= s2
P1
= 8.3 bar
T1
= 811 K
T2
= 422 K

P2 = 5 bar
Cp = 1.005 kJ/kg K
R = 0.287 kJ/kg K
PV1.3
= C
From the quantities given, we can temporarily sketch the process as shown in
the diagram below.
From equation 10.27, we have
T
T
p
p
n
n
2
1
2
1
1
=






−
K434
01.1
5
)300(
3.1
13.1
1
1
2
12
=






=






=
−
−
n
n
P
P
TT
∴ From equation 10.25, the change of entropy (S1 – S2) is,
S1 – S2 = (SB – S2) - (SB – S1)
T
s
P2
= 5 bar
2
1
s2
P1
= 1.01 bar
T1
= 300 K
T2
= ?
B
s1
sB

kJ/K088.0-
)459.0()371.0(
1.01
5
lnx0.287x0.1
300
434
lnx1.005x0.1
lnln
1
2
1
2
=
−=






−





=






−





=
p
p
mR
T
T
mC p
From the calculation, we have S1 – S2 = - 0.088 kJ/K. This means that S2 is
greater than S1 and the process should appear as in the T-s diagram below.
CONGRATULATIONS, IF YOUR ANSWERS ARE CORRECT YOU CAN
PROCEED TO THE SELF-ASSESSMENT….
T
s
P2
= 5 bar
2
1
s2
P1
= 1.01 bar
T1
= 300 K
T2
= 434 K
B
s1
sB

You are approaching success. Try all the questions in this self-assessment
section and check your answers with those given in the Feedback to Self-
Assessment on the next page. If you face any problem, discuss it with your lecturer.
Good luck.
1. A quantity of air at 2 bar, 25o
C and 0.1 m3
undergoes a reversible constant
pressure process until the temperature and volume increase to 2155 o
C and
0.8 m3
. If Cp = 1.005 kJ/kg K and R = 0.287 kJ/kg K, determine the:
i. mass of air
ii. change of entropy
iii. heat flow
iv. work done
Sketch the process on a T-s diagram and shade the area which represents the
heat flow.
2. A rigid cylinder containing 0.006 m3
of nitrogen (M = 28) at 1.04 bar and 15o
C is
heated reversibly until the temperature is 90o
C. Calculate the:
i. change of entropy
ii. heat supplied
Sketch the process on a T-s diagram. For nitrogen, take γ = 1.4 and assume it
as a perfect gas.
3. 0.03 kg of nitrogen (M = 28) contained in a cylinder behind a piston is
initially at 1.05 bar and 15 o
C. The gas expands isothermally and reversibly
to a pressure of 4.2 bar. Assuming nitrogen to act as a perfect gas, determine
the:
i. change of entropy
ii. heat flow
iii. work done
heat flow.
SELF-ASSESSMENT

4. 0.05 kg of air at 30 bar and 300o
C is allowed to expand reversibly in a
cylinder behind a piston in such a way that the temperature remains constant
to a pressure of 0.75 bar. Based on the law pv1.05
= constant, the air is then
compressed until the pressure is 10 bar. Assuming air to be a perfect gas,
determine the:
i. net entropy change
ii. net heat flow
iii. net work energy transfer
Sketch the processes on a T-s diagram, indicating the area, which represents
the heat flow.
5. a) 0.5 kg of air is compressed in a piston-cylinder device from 100
kN/m2
and 17o
C to 800 kN/m2
in a reversible, isentropic process.
Assuming air to be a perfect gas, determine the final temperature and
the work energy transfer during the process.
Given: R = 0.287 kJ/kg K and γ = 1.4.
b) 1 kg of air at 30o
C is heated at a constant volume process. If the heat
supplied during a process is 250 kJ, calculate the final temperature
and the change of entropy. Assume air to be a perfect gas and take
Cv = 0.718 kJ/kg K.
6. 0.05 m3
of oxygen (M = 32) at 8 bar and 400o
C expands according to the law
pv1.2
= constant, until the pressure is 3 bar. Assuming oxygen to act as a
perfect gas, determine the:
i. mass of oxygen
ii. final temperature
iii. change of entropy
iv. work done
heat flow.

Have you tried the questions????? If “YES”, check your answers now.
1. i. m = 0.2338 kg
ii. S2 – S1 = 0.4929 kJ/K
iii. Q = 500.48 kJ
iv. W = 140 kJ
2. i. S2 – S1 = 0.00125 kJ/K
ii. Q = 0.407 kJ
3. i. S2 – S1 = -0.0152 kJ/K
ii. Q = - 4.3776 kJ
iii. W = - 4.3776 kJ
4. i. Σ ∆S = (S2 – S1) + (S3 – S2)
= 0.0529 + 0.0434
= 0.0963 kJ/K
ii. Σ Q = Q12 + Q23
= (30.31) + (-18.89)
= 11.42 kJ
iii. Σ W = W12 + W23
= (30.32) + (-21.59)
= 8.73 kJ
5. a) T2 = 525.3 K, W = - 84.4 kJ
b) T2 = 651 K, (S2 – S1) = 0.5491 kJ/K
6. i. m = 0.23 kg
ii. T2 = 571.5 K
iii. S2 – S1 = 0.0245 kJ/K
iv. W = 30.35 kJ
Feedback to Self-Assessment

J2006 termodinamik 1 unit10

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