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

Question 4 of 8: Freon-12 Refrigeration Cycle (Coefficient of Performance)

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 4: Freon-12 Refrigeration Cycle (Coefficient of Performance) (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. A real (irreversible, with line pressure drops) vapour-compression cycle. The compressor runs 1→2 and rejects $q_\text{out}=4\ \text{kJ/kg}$; the condenser exit / throttle inlet is state 5; throttling holds enthalpy so $h_7=h_6=h_5$; the evaporator absorbs heat 7→8. Enthalpies from the supplied Freon-12 tables:

StateCondition$h\ (\text{kJ/kg})$
1 — compressor inlet125 kPa, −10 °C (superheated)185.2
2 — compressor exit1.20 MPa, 100 °C (superheated)245.5
5 — throttle inlet≈ sat. liquid, 40 °C74.5
7 — evaporator inlet140 kPa, $h_7=h_5$74.5
8 — evaporator exit100 kPa, −20 °C (superheated)179.9

Find. The cycle coefficient of performance, $\text{COP}=q_L/w_\text{in}$.

entropy sTsaturation dome12 (100 °C)5 (cond., 40 °C)7,8evaporation (q_L in)condensation (q_H out)
Figure 3 — T–s schematic of the Freon-12 cycle: 1→2 compression (with 4 kJ/kg heat loss), 2→5 condensation/de-superheating to saturated liquid at 40 °C, 5→7 throttling (constant enthalpy), 7→8 evaporation absorbing the refrigeration effect. Irreversibilities and line pressure drops make the actual path non-ideal.
Check
State 5 (1.15 MPa, 40 °C) is a subcooled liquid; its enthalpy is taken as $h_f$ at 40 °C = 74.5 kJ/kg (compressed-liquid enthalpy ≈ saturated-liquid value at the same temperature). The evaporator exit (state 8) at 100 kPa, −20 °C is superheated vapour ($h=179.9$ kJ/kg). The stated point-by-point pressure drops confirm this is a real, not idealised, cycle.

Approach. Write the first law over the compressor (heat loss increases the work input), take the refrigeration effect as the evaporator enthalpy rise with $h_7=h_5$ from the throttle, then form the COP.

  1. Compressor work with heat loss. Energy balance $h_1+w_\text{in}=h_2+q_\text{out}$ gives$$w_\text{in}=(h_2-h_1)+q_\text{out}=(245.5-185.2)+4.0=\boxed{64.4\ \text{kJ/kg}}.$$
  2. Refrigeration effect (evaporator). Throttling keeps $h_7=h_6=h_5=74.5$ kJ/kg, so$$q_L=h_8-h_7=179.9-74.5=\boxed{105.3\ \text{kJ/kg}}.$$
  3. Coefficient of performance. $$\text{COP}=\frac{q_L}{w_\text{in}}=\frac{105.3}{64.4}=\boxed{1.64}.$$
QuantityResult
Compressor work input64.4 kJ/kg
Refrigeration effect $q_L$105.3 kJ/kg
Coefficient of performance≈ 1.64