SECOND LAW OF THERMODYNAMICS AND ENTROPY 287dharm
/M-therm/th5-4.pm5Solution. Given : VA = 0.25 m^3 ; pAi = 1.4 bar ; TAi = 290 K ; VB = 0.25 m^3 ; pBi = 4.2 bar ;
TBi = 440 K ; cv = 0.715 kJ/kg K.
(i)Final equilibrium temperature, Tf :Mass of air, mA =
pV
RTAi A
Ai= ××
××(. ).
(. )14 10 025
0 287 1000 2905
= 0.4205 kgmB = pV
RTBi B
Bi= ××
××(. ).
(. )42 10 025
0 287 1000 4405
= 0.8315 kgLet Tf be the final equilibrium temperature (K). Since the diaphragm is conducting,
Heat gained by air in chamber A = Heat lost by air in chamber B
mA cv (Tf – 290) = mB cv(440 – Tf)
or, 0.4205 × (Tf – 290) = 0.8315(440 – Tf)
or, 0.4205 Tf – 121.94 = 365.86 – 0.8315 Tf
∴ Tf = 389.6 K. (Ans.)
(ii)Final pressure on each side of the diaphragm : pAf ; pBf
pAf = 1 4 389 6
290..× = 1.88 bar. (Ans.)pBf = 4 2 389 6
440..× = 3.72 bar. (Ans.)(iii)Entropy change of the system :Entropy change for chamber A = mA cv logeT
Tf
AiF
HGI
KJ= 0.4205 × 0.715 × loge 389 6
290F.
HGI
KJ = 0.0888 kJ/KEntropy change for chamber B = mB cv logeT
Tf
BiF
HGI
KJ= 0.8315 × 0.715 × loge 389 6
440F.
HGI
KJ
= – 0.0723 kJ/K∴ Net change of entropy = 0.0888 + (– 0.0723) = 0.0165 kJ/K. (Ans.)
Example 5.42. A certain gas has a specific heat at constant volume of 1.25 kJ/kg K. When
it is expanded reversibly and adiabatically from a specific volume of 0.0624 m^3 /kg and a tempera-
ture of 530 K to a specific volume of 0.186 m^3 /kg its temperature falls by 165 K. When it is
expanded into an evacuated space from the same initial condition to the same final specific
volume its temperature falls only by 25 K.
Find the change in entropy in each of the adiabatic processes.
Solution. Refer Fig. 5.44.
Specific heat of gas at constant volume, cv = 1.25 kJ/kg K
Initial specific volume, v 1 = 0.0624 m^3 /kg
Initial temperature, T 1 = 530 K
Final specific volume, v 2 = 0.186 m^3 /kg