430 ENGINEERING THERMODYNAMICSdharm
\M-therm\Th9-2.pm5Now cvCO 2 =RCO 2
γ− 1
=
8 314
44 1 286 1.
(. − ) [forCO.]Qγ^2 =1 286
= 0.661 kJ/kg K
and cpCO 2 = 1.286 × 0.661 = 0.85 kJ/kg K
For the mixture :cp =mc m c
mmNCp Op
NCO2 NC 2 2 O 2
22+
+=
4 1 039 6 0 85
46×+×
+..
() = 0.925 kJ/kg K. (Ans.)cv =mc m c
mmNCvvO
NCO2 NC 2 2 O 2
22+
+=4 0 742 6 0 661
46×+×
+..
() = 0.693 kJ/kg K. (Ans.)
When the mixture is heated at constant volume :
Change in internal energy,
U 2 – U 1 = mcv(T 2 – T 1 ) = 10 × 0.693(50 – 20) = 207.9 kJ. (Ans.)
Change in entropy,
H 2 – H 1 = mcp(T 2 – T 1 ) = 10 × 0.925(50 – 20) = 277.5 kJ. (Ans.)
Change in entropy,S 2 – S 1 = mcv loge T
T2
1+ mR loge V
V2
1
= mcv loge
T
T2
1()QVV 12 == 10 × 0.693 × loge
273 50
273 20+
+F
HGI
KJ
= 0.675 kJ/kg K. (Ans.)
When the mixture is heated at constant pressure :
If the mixture is heated at constant pressure ∆U and ∆H will remain the same.
The change in entropy will beS 2 – S 1 = mcp logeT
T2
1- mR loge
p
p2
1
= mcp loge
T
T2
1()Qpp 12 == 10 × 0.925 loge
323
293F
HGI
KJ = 0.902 kJ/kg K. (Ans.)
Example 9.11. A vessel of 1.8 m^3 capacity contains oxygen at 8 bar and 50°C. The vessel is
connected to another vessel of 3.6 m^3 capacity containing carbon monoxide at 1 bar and 20°C. A
connecting valve is opened and the gases mix adiabatically. Calculate :
(i)The final temperature and pressure of the mixture ;
(ii)The change of entropy of the system.
Take : For oxygen Cv = 21.07 kJ/mole K.
For carbon monoxide Cv = 20.86 kJ/mole K.