Question 7 of 9: Two-Phase Water Expansion, Pv = Constant
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-BS-10, Thermodynamics — December 2018. 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, interpolation not required — the closest tabular value may be used). 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, R-134a, air, N₂, O₂, humid
air) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.
Question 7: Two-Phase Water Expansion, Pv = Constant (15 marks)
Given. $m=5$ kg, $P_1=500$ kPa, $x_1=0.98$. Expands to $P_2=150$ kPa with
$Pv=\text{const}$ (polytropic, $n=1$).
Find. (a) $W$ [kJ]; (b) $Q$ [kJ].
Fig. Q7 — The $Pv=\text{const}$ (hyperbolic) expansion path from a wet
state ($v_1=0.3673$ m³/kg) to a state at 150 kPa where $v_2=1.2244$ m³/kg exceeds
$v_g(150\ \text{kPa})=1.1593$ m³/kg, so state 2 is actually superheated, not wet.
Approach
Fix state 1 from the given quality, use the process relation to get $v_2$ directly (no iteration
needed since $n=1$ makes $v_2=P_1v_1/P_2$ explicit), check whether state 2 lands inside or outside the
dome at 150 kPa, and evaluate $u_2$ accordingly. The polytropic work integral for $n=1$ is the
logarithmic (isothermal-form) expression, and $Q$ follows from the closed-system first law.
State 1. At 500 kPa, $x_1=0.98$: $v_f=0.001093$, $v_g=0.3748$ m³/kg
$\Rightarrow v_1=v_f+x_1(v_g-v_f)=\boxed{0.3673\ \text{m}^3/\text{kg}}$; $u_f=639.54$,
$u_{fg}=1921.17$ kJ/kg $\Rightarrow u_1=u_f+x_1 u_{fg}=2522.3$ kJ/kg.
State 2 from $Pv=\text{const}$.
$$v_2=\frac{P_1v_1}{P_2}=\frac{500\times0.3673}{150}=\boxed{1.2244\ \text{m}^3/\text{kg}}.$$
At 150 kPa, $v_g=1.1593$ m³/kg $< v_2$, so state 2 is superheated (not wet): this specific
volume at 150 kPa corresponds to $T_2\approx 131.1\ ^\circ$C, $u_2=2550.7$ kJ/kg.
Work (part a). For $Pv=\text{const}$ ($n=1$), the boundary-work integral takes
the isothermal (logarithmic) form:
$$w=\int_1^2 P\,dv=P_1v_1\ln\frac{v_2}{v_1}=500\times0.3673\times\ln\frac{1.2244}{0.3673}
=183.65\times1.204=221.13\ \text{kJ/kg}$$
$$W=m\,w=5\times221.13=\boxed{1105.6\ \text{kJ}}.$$
Heat transfer (part b). Closed-system first law:
$$q=(u_2-u_1)+w=(2550.7-2522.3)+221.13=28.4+221.13=249.60\ \text{kJ/kg}$$
$$Q=m\,q=5\times249.60=\boxed{1248.0\ \text{kJ}}.$$