Question 4 of 9: Isentropic Compression of an N₂/CO₂ Mixture
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-BS-10, Thermodynamics — December 2015. 3 hours, Closed-Book Exam
(approved calculator and one double-sided 8.5x11-inch aid sheet permitted; property tables and
charts supplied in an appendix). Part A: answer 2 of Questions 1-3 (20 marks each). Part B: answer
4 of Questions 4-9 (15 marks each), for a 100-mark paper. Only the first two Part-A and first four
Part-B questions as they appear in the answer book are marked. All nine questions (Part A complete,
Part B complete) are solved below for completeness.
Reference texts: Cengel & Boles, Thermodynamics: An Engineering
Approach, 8th ed.; Moran, Shapiro, Boettner & Bailey, Fundamentals of Engineering
Thermodynamics, 8th ed. All state properties (water/steam, air, N₂, CO₂, moist air)
were computed from high-accuracy equations of state
in place of printed property-table interpolation; every boxed numeric result.
Question 4: Isentropic Compression of an N₂/CO₂ Mixture (15 marks)
Given. Mixture: 80% N$_2$ + 20% CO$_2$ by mole. Inlet: $P_1=100$ kPa,
$T_1=1000$ K. Exit: $P_2=500$ kPa, isentropic. Constant specific heats evaluated at 300 K.
Species
Mole fraction
M (kg/kmol)
Mass fraction
$c_p$ @300K (kJ/kg·K)
N$_2$
0.80
28.013
0.7180
1.0414
CO$_2$
0.20
44.01
0.2820
0.8526
Find. $w_{in}$ [kJ/kg mixture].
Approach
Convert the given mole fractions to mass fractions using each species' molar mass, then form the
mixture's mass-weighted constant-property $c_p$, gas constant, and specific-heat ratio $k$. Since
the compression is isentropic and $k$ is treated as constant, use the ideal-gas isentropic relation
directly on temperature and pressure, then get the specific work from $w=c_p\Delta T$.
Mixture composition (mass basis). Per kmol of mixture: $m_{N_2}=0.80\times
28.013=22.410$ kg, $m_{CO_2}=0.20\times44.01=8.802$ kg, so $M_{mix}=31.212$ kg/kmol, giving mass
fractions $mf_{N_2}=0.7180$, $mf_{CO_2}=0.2820$.
Mixture properties at 300 K.
$$c_{p,mix}=mf_{N_2}c_{p,N_2}+mf_{CO_2}c_{p,CO_2}=0.7180\times1.0414+0.2820\times0.8526=\boxed{0.9881\ \text{kJ/kg}\cdot\text{K}}.$$
$$R_{mix}=\frac{R_u}{M_{mix}}=\frac{8.314}{31.212}=0.2664\ \text{kJ/kg}\cdot\text{K},\qquad
k_{mix}=\frac{c_{p,mix}}{c_{p,mix}-R_{mix}}=\boxed{1.3691}.$$
Work input per unit mass of mixture. For an isentropic, steady-flow compressor
with negligible KE/PE change, $w_{in}=\Delta h=c_{p,mix}(T_2-T_1)$:
$$w_{in}=0.9881\times(1543.2-1000)=\boxed{536.7\ \text{kJ/kg mixture}}.$$