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22-Mec-A1 Applied Thermodynamics and Heat Transfer · May 2014

Question 3 of 8: Compression-Ignition (Dual) Cycle

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper: National Examinations — 07-Mec-A1 Applied Thermodynamics and Heat Transfer, May 2014. Open-book, 3-hour paper. Part A (Thermodynamics, Q1–Q4) and Part B (Heat Transfer, Q5–Q8); a complete paper is any five questions — three from one part and two from the other, all of equal value. Full worked solutions to all eight questions are given below.

Reference texts: Çengel & Boles, Thermodynamics: An Engineering Approach (9th ed., McGraw-Hill) — closed- and open-system energy balances, steam tables, gas power cycles, reciprocating compressors and vapour-compression refrigeration; Çengel & Ghajar, Heat and Mass Transfer (6th ed.) and Incropera, DeWitt, Bergman & Lavine, Fundamentals of Heat and Mass Transfer (8th ed., Wiley) — composite-wall conduction, internal-flow and cross-flow convection correlations, natural convection with radiation, and the ε–NTU heat-exchanger method. Freon-12 property data are taken from the appendix supplied with the exam; steam and air data from standard tables.

Question 3: Compression-Ignition (Dual) Cycle (equal value)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given. Dual (mixed) air-standard cycle: state 1 at $P_1=100\ \text{kPa}$, $T_1=50\ ^\circ\text{C}=323.15\ \text{K}$; compression ratio $r=V_1/V_2=13$; maximum pressure $P_3=P_4=4500\ \text{kPa}$; heat split $Q_v:Q_p=2:1$; $\gamma=1.4$, $c_v=0.718\ \text{kJ/kg}\cdot\text{K}$.

Find. The temperatures $T_1$–$T_5$ and the thermal efficiency.

volume VP23451const V (2→3)const P (3→4)expansion 4→5const V rejection 5→1
Figure 2 — p–V diagram of the dual (mixed) cycle: 1→2 isentropic compression, 2→3 constant-volume heat addition to the maximum pressure, 3→4 constant-pressure heat addition, 4→5 isentropic expansion, 5→1 constant-volume heat rejection.

Approach. Fix state 2 from the isentropic compression, state 3 from the constant-volume rise to the maximum pressure, split the heat 2:1 to locate state 4, expand isentropically to state 5, then form the efficiency from the heat added and rejected.

  1. Isentropic compression 1→2. $$T_2=T_1r^{\gamma-1}=323.15(13)^{0.4}=\boxed{901\ \text{K}},\qquad P_2=P_1r^{\gamma}=100(13)^{1.4}=3627\ \text{kPa}.$$
  2. Constant-volume heat addition 2→3. At fixed volume the temperature scales with pressure to the maximum 4500 kPa:$$T_3=T_2\frac{P_3}{P_2}=901\frac{4500}{3627}=\boxed{1119\ \text{K}}.$$
  3. Constant-pressure heat addition 3→4 from the 2:1 heat split. $Q_v=c_v(T_3-T_2)$ is twice $Q_p=c_p(T_4-T_3)$, so $c_v(T_3-T_2)=2c_p(T_4-T_3)$, i.e. $(T_3-T_2)=2\gamma(T_4-T_3)$:$$T_4=T_3+\frac{T_3-T_2}{2\gamma}=1119+\frac{217}{2.8}=\boxed{1196\ \text{K}}.$$ The cut-off ratio is $\rho_c=V_4/V_3=T_4/T_3=1.069$.
  4. Isentropic expansion 4→5. Since $V_5=V_1$ and $V_3=V_2$, the expansion ratio is $V_5/V_4=r/\rho_c=13/1.069=12.16$:$$T_5=T_4\!\left(\frac{V_4}{V_5}\right)^{\gamma-1}=1196(12.16)^{-0.4}=\boxed{440\ \text{K}}.$$
  5. Thermal efficiency. Heat added $Q_\text{in}=c_v(T_3-T_2)+c_p(T_4-T_3)=c_v(217+108.5)=325.5\,c_v$; heat rejected $Q_\text{out}=c_v(T_5-T_1)=117.2\,c_v$. Hence$$\eta=1-\frac{Q_\text{out}}{Q_\text{in}}=1-\frac{117.2}{325.5}=\boxed{0.640\ (64.0\%)}.$$
PointTemperaturePressure
1323 K (50 °C)100 kPa
2901 K3627 kPa
31119 K4500 kPa
41196 K4500 kPa
5440 K136 kPa
Thermal efficiency64.0 %