17-Phys-B6 Applied Thermodynamics and Heat Transfer · May 2013
Question 1 of 8: Helium Cycle — p–v Diagram and Thermal Efficiency
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. 98-Phys-B6 Applied Thermodynamics and Heat Transfer,
National Examination May 2013 — an open-book examination (any textbook, reference or
non-communicating calculator permitted). Part A (Thermodynamics, Q1–4) and Part B (Heat
Transfer, Q5–8) together form the paper; a complete exam is five answers, drawn either
three-from-A/two-from-B or two-from-A/three-from-B. Every question is nonetheless answered in
full below so the paper remains a complete study resource. All eight questions carry equal
value in the grading.
Reference texts. Y. A. Çengel & M. A. Boles, Thermodynamics: An
Engineering Approach, 8th ed. (ideal-gas cycles, vapour power cycles with reheat, gas
compressors, vapour-compression refrigeration); F. P. Incropera & D. P. DeWitt,
Fundamentals of Heat and Mass Transfer, 7th ed. (critical radius of insulation,
internal/external forced convection correlations, natural convection from horizontal cylinders,
radiation exchange, LMTD/effectiveness–NTU heat-exchanger analysis).
Question 1: Helium Cycle — p–v Diagram and Thermal Efficiency (Part A, 20 marks)
Given. Helium (ideal gas, $M=4.003$ g/mol) executes a closed
three-process cycle: 1→2 constant $p=300$ kPa, $T_1=20^{\circ}\text{C}$,
$T_2=145^{\circ}\text{C}$; 2→3 constant volume, cooling to $T_3=20^{\circ}\text{C}$; 3→1
isothermal compression back to 300 kPa.
Find. $w$ and $q$ for each of the three processes (kJ/kg) and the cycle's
thermal efficiency $\eta$.
Figure — p–v diagram of the Helium cycle. 1→2 constant-pressure
expansion, 2→3 constant-volume cooling, 3→1 isothermal compression (dashed, a $pv=\text{const}$
hyperbola) closing the loop back onto state 1.
Approach. Treat helium as an ideal gas with $R=R_u/M=2.077$ kJ/kg·K,
$c_v=\tfrac{3}{2}R=3.116$, $c_p=\tfrac{5}{2}R=5.193$ kJ/kg·K (monatomic, $k=5/3$); find
$v_1,v_2$ from the ideal-gas law at the constant-pressure leg, then evaluate $w$ and $q$ process-by-process
before closing the cycle.
Specific volumes and state 3's pressure.
$$v_1=\frac{RT_1}{p_1}=\frac{2.077\times293.15}{300}=2.030\ \text{m}^3/\text{kg},\qquad
v_2=\frac{RT_2}{p_1}=\frac{2.077\times418.15}{300}=2.895\ \text{m}^3/\text{kg}.$$
Process 2→3 is constant volume ($v_3=v_2$), so at $T_3=293.15$ K,
$$p_3=\frac{RT_3}{v_3}=\frac{2.077\times293.15}{2.895}=\boxed{210.3\ \text{kPa}}.$$
Process 1→2 — constant-pressure expansion.
$$w_{12}=p(v_2-v_1)=R(T_2-T_1)=2.077\times125=259.6\ \text{kJ/kg},$$
$$q_{12}=c_p(T_2-T_1)=5.193\times125=\boxed{649.1\ \text{kJ/kg}}\quad(\text{heat IN}).$$
($\Delta u_{12}=c_v(T_2-T_1)=389.5$ kJ/kg, and $q_{12}=\Delta u_{12}+w_{12}$ checks:
$389.5+259.6=649.1$.)
Process 2→3 — constant-volume cooling. No boundary work is done
($w_{23}=0$), so all the internal-energy change leaves as heat:
$$q_{23}=\Delta u_{23}=c_v(T_3-T_2)=3.116\times(-125)=\boxed{-389.5\ \text{kJ/kg}}\quad(\text{heat OUT}).$$
Process 3→1 — isothermal compression. $\Delta u=0$ for an ideal gas
at constant $T$, so $q_{31}=w_{31}$:
$$w_{31}=RT_1\ln\!\frac{v_1}{v_3}=2.077\times293.15\times\ln\!\frac{2.030}{2.895}
=\boxed{-216.3\ \text{kJ/kg}}\quad(\text{work IN, heat OUT}).$$
Cycle net work and thermal efficiency. Summing the three legs (and
confirming $\sum q=\sum w$, since $\oint du=0$):
$$w_{net}=259.6+0-216.3=\boxed{43.4\ \text{kJ/kg}}=q_{12}+q_{23}+q_{31}=649.1-389.5-216.3=43.4\
\checkmark$$
Only $q_{12}$ is heat added to the gas, so
$$\eta=\frac{w_{net}}{q_{in}}=\frac{43.4}{649.1}=\boxed{6.68\%}.$$