Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Examinations — 04-BS-10, Thermodynamics. Three hours. Closed-book exam with one
8.5×11 in. double-sided sheet of notes allowed and an approved Casio or Sharp calculator;
property tables and charts are supplied and interpolation is not necessary — the closest tabular
value may be used. Part A: two of three 20-mark questions; Part B: four of six 15-mark questions.
Every question is answered in full.
Reference texts. Cengel & Boles, Thermodynamics: An Engineering
Approach, 8th ed. (Vapor Power Cycles Ch. 10; Gas Power Cycles Ch. 9; Refrigeration Cycles
Ch. 11; Gas Mixtures Ch. 13; Psychrometrics Ch. 14; Exergy Ch. 8).
Check — paper format. The paper is headed "National Examination – May 2019 / 04-BS-10, Thermodynamics, 3 Hours Duration": four question pages followed by a 22-page appendix of property tables and a psychrometric chart. All nine questions are answered in full (Part A questions 1–3 at 20 marks each, Part B questions 4–9 at 15 marks each; the paper asks for two of Part A and four of Part B). Two wording notes from the printed page: Question 2's final sub-part is printed "(d) the second law efficiency" after an earlier "(d)", i.e. the paper repeats the letter, and Question 3(d) is printed "in kJ/K" for a quantity that is a rate of exergy destruction in kJ/s.
Walk the five states of the dual cycle in order — isentropic compression $1\to2$,
constant-volume heat addition $2\to3$, constant-pressure heat addition $3\to4$, isentropic expansion
$4\to5$ back to $V_1$, constant-volume heat rejection $5\to1$ — using cold-air-standard
relations throughout.
Isentropic compression, state 2.
$$T_2=T_1\,r^{\,k-1}=300\times9^{0.4}=722.47\ \text{K}.$$
Constant-pressure heat addition — part (a), $T_4$.
$q_{3\to4}=\tfrac13\times1400=466.67$ kJ/kg.
$$T_4=T_3+\frac{q_{3\to4}}{c_p}=2022.4+\frac{466.67}{1.005}=2022.4+464.35=\boxed{2486.7\ \text{K}}.$$
Cutoff ratio $r_c=T_4/T_3=1.2296$.
Isentropic expansion, state 5. Expansion volume ratio $V_5/V_4=r/r_c=7.318$:
$$T_5=T_4\left(\frac{r_c}{r}\right)^{k-1}=2486.7\times\left(\frac{1.2296}{9}\right)^{0.4}=1121.6\ \text{K}.$$
Heat rejected, net work, thermal efficiency — parts (b), (c).
$$q_{out}=c_v(T_5-T_1)=0.718\times(1121.6-300)=589.9\ \text{kJ/kg}.$$
$$w_{net}=q_{in}-q_{out}=1400-589.9=\boxed{810.1\ \text{kJ/kg}}.$$
$$\eta_{th}=\frac{w_{net}}{q_{in}}=\frac{810.1}{1400}=\boxed{0.5786\ (57.9\%)}.$$
Mean effective pressure — part (d).
$$v_1=\frac{RT_1}{P_1}=\frac{0.287\times300}{100}=0.8610\ \text{m}^3/\text{kg},\quad v_2=v_1/r=0.09567\ \text{m}^3/\text{kg}.$$
$$MEP=\frac{w_{net}}{v_1-v_2}=\frac{810.1}{0.8610-0.09567}=\boxed{1058.5\ \text{kPa}}.$$