Question 7 of 9: Non-Ideal Air-Standard Diesel Cycle
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Examinations — December 2019, 04-BS-10, Thermodynamics. 3-hour
closed-book exam (one 8.5×11 in. double-sided note sheet allowed); property tables/charts
supplied, no interpolation required. 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).
Questions 1, 3, 4, 6, 9 are fully legible and solved as printed. Question 2's specific
numbers (pressure ratio, reheat pressure, temperatures, efficiencies) were reconstructed from
surviving fragments that match a well-known textbook archetype (see Q2's callout). Questions 5, 7
and 8 have genuinely blank gaps in the source with no fully-confirming fingerprint; clearly-labelled
representative values are substituted so every question can still be solved in full (see each
question's own check callout).
Check — reconstructed missing values. The compression ratio
(15), $p_1=100$ kPa, $T_1=300$ K, and the expansion efficiency (90%) are all legible/confirmed. Representative round-number values of $T_{max}=2200$ K and $\eta_c=95\%$ are adopted (paired with the
given $\eta_e=90\%$) so the question can still be solved and checked in full; the method below applies
unchanged to any other $T_{max}$/$\eta_c$ pair.
Fig. Q7 — $p$–$v$ diagram: 1→2 actual
(inefficient) adiabatic compression, 2→3 constant-$P$ heat addition to $T_{max}$, 3→4 actual
(inefficient) adiabatic expansion back to $v_1$, 4→1 constant-volume heat rejection.
Approach
Get the isentropic compression temperature from the compression ratio, then apply the compression
efficiency to find the ACTUAL state 2 (same volume, more work, higher $T$). Heat addition at constant
pressure to $T_{max}$ fixes the cutoff ratio. The isentropic expansion temperature follows from the
volume ratio $v_4/v_3=CR/r_c$; applying the expansion efficiency gives the actual state 4. Net work
MUST be taken as $q_{in}-q_{out}$ (full-cycle energy balance) rather than the difference of the two
adiabatic-stroke works alone, since that difference omits the boundary work done during the
constant-pressure heat-addition stroke.
Actual compression (1→2).
$$T_{2s}=T_1\,CR^{k-1}=300\times15^{0.4}=886.3\ \text{K},\qquad
w_{c,a}=\frac{c_v(T_{2s}-T_1)}{\eta_c}=\frac{0.718(886.3-300)}{0.95}=443.08\ \text{kJ/kg}$$
$$T_2=T_1+\frac{w_{c,a}}{c_v}=300+\frac{443.08}{0.718}=\boxed{917.1\ \text{K}}.$$
Heat addition and cutoff ratio (2→3).
$$r_c=\frac{T_3}{T_2}=\frac{2200}{917.1}=\boxed{2.399},\qquad
q_{in}=c_p(T_3-T_2)=1.005(2200-917.1)=\boxed{1289.31\ \text{kJ/kg}}.$$
Actual expansion (3→4). $v_4/v_3=CR/r_c=15/2.399=6.253$:
$$T_{4s}=\frac{T_3}{(v_4/v_3)^{k-1}}=\frac{2200}{6.253^{0.4}}=1056.7\ \text{K},\qquad
w_{e,a}=\eta_e\,c_v(T_3-T_{4s})=0.90\times0.718(2200-1056.7)=738.75\ \text{kJ/kg}$$
$$T_4=T_3-\frac{w_{e,a}}{c_v}=2200-\frac{738.75}{0.718}=\boxed{1171.1\ \text{K}}.$$
Net work (part a) and thermal efficiency (part b). Full-cycle energy balance
($\Delta U=0$ over one complete cycle) requires $w_{net}=q_{in}-q_{out}$:
$$w_{net}=1289.31-625.45=\boxed{663.85\ \text{kJ/kg}}$$
$$\eta_{th}=\frac{w_{net}}{q_{in}}=\frac{663.85}{1289.31}=\boxed{0.5149\ (51.5\%)}.$$