22-Mec-A1 Applied Thermodynamics and Heat Transfer · May 2015
Question 4 of 8: Freon-12 Vapour-Compression Refrigeration
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 2015. 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, vapour and gas power cycles 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 / LMTD-correction heat-exchanger methods. Freon-12 property data are taken from the appendix supplied with the exam; steam, air and water data from standard tables.
Figure 3 — T–s schematic of the Freon-12 cycle: 1→2 compression (80 % efficient), 2→3 condensation and subcooling to 48 °C, 3→4 throttling at constant enthalpy, 4→1 evaporation at 15 °C absorbing the refrigeration effect.
Approach. Find the isentropic discharge enthalpy at the condenser pressure, apply the 80 % efficiency for the real work, take the throttle as isenthalpic to fix the evaporator inlet, then form the capacity and COP from the evaporator enthalpy rise.
Compressor work. The ideal (isentropic) lift is $h_{2s}-h_1=212.1-193.6=18.5\ \text{kJ/kg}$; with $\eta_c=0.80$ the real specific work is$$w_\text{in}=\frac{h_{2s}-h_1}{\eta_c}=\frac{18.5}{0.80}=\boxed{23.1\ \text{kJ/kg}}.$$
(c) Coefficient of performance. $$\text{COP}=\frac{q_L}{w_\text{in}}=\frac{110.9}{23.1}=\boxed{4.8}.$$
Check
The discharge state 2s is only mildly superheated (≈ 62 °C at 1.4 MPa), so $h_{2s}$ is estimated from the saturated-vapour enthalpy plus a small $c_p\,\Delta T_\text{sup}$ term using a reconstructed superheated Freon-12 table. A ±1 kJ/kg uncertainty in $h_{2s}$ moves the COP by about ±0.2 and the power by ±5 W; the capacity is unaffected. Subcooling to 48 °C (below the 56 °C saturation) raises the refrigeration effect over a saturated-liquid exit.