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04-BS-10 · May 2013

Question 5 of 9: R-134a Heat Pump — Power Input and Comparison with Resistance Heating

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

Notes on this paper

National Exam 04-BS-10, Thermodynamics — May 2013. 3 hours, Closed-Book Exam (approved calculator and one double-sided 8.5x11-inch aid sheet permitted). Part A: answer 2 of Questions 1-3 (20 marks each). Part B: answer 4 of Questions 4-9 (15 marks each), for a 100-mark paper. Only the first two Part-A and first four Part-B questions as they appear in the answer book are marked. All nine questions (Part A complete, Part B complete) are solved below for completeness.

Reference texts: Cengel & Boles, Thermodynamics: An Engineering Approach, 8th ed. All state properties (R-134a, water/steam, air, N₂, CO₂) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.

Question 5: R-134a Heat Pump — Power Input and Comparison with Resistance Heating (15 marks)

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. R-134a heat pump; house heat loss (condenser duty) $\dot Q_H=60{,}000$ kJ/h $=16.667$ kW. Compressor inlet: $P_1=280$ kPa, $T_1=0\ ^\circ\text{C}$ (superheated). Compressor exit: $P_2=1$ MPa, $T_2=60\ ^\circ\text{C}$ (superheated). Condenser exit: $T_3=30\ ^\circ\text{C}$ at 1 MPa — note $T_{sat}(1\ \text{MPa})=39.39\ ^\circ\text{C}$, so the condenser exit is a subcooled liquid, about 9.4°C below saturation, not a saturated-liquid state.

Find. (a) compressor power input; (b) rate of heat absorption from the ground water (evaporator duty); (c) additional electric power needed if a simple resistance heater replaced the heat pump.

Approach

The condenser duty $\dot Q_H$ (given, equal to the house heat loss) fixes the mass flow rate once $h_2$ and $h_3$ are known from the compressor-exit and condenser-exit states; compressor power and evaporator duty then follow directly, and the resistance-heater comparison is a simple energy-balance difference since a resistance heater converts 100% of its electrical input to heat.

  1. Fix the four states. $h_1=h(280\ \text{kPa},0\ ^\circ\text{C})=398.98$ kJ/kg; $h_2=h(1\ \text{MPa},60\ ^\circ\text{C})=441.53$ kJ/kg; $h_3=h(1\ \text{MPa},30\ ^\circ\text{C},\text{subcooled})=241.72$ kJ/kg; throttling to the evaporator is isenthalpic, $h_4=h_3=241.72$ kJ/kg.
  2. Mass flow rate from the condenser energy balance. $$\dot m=\frac{\dot Q_H}{h_2-h_3}=\frac{16.667}{441.53-241.72}=\boxed{0.0834\ \text{kg/s}}.$$
  3. Compressor power input (part a). $$\dot W_{in}=\dot m(h_2-h_1)=0.0834\times(441.53-398.98)=\boxed{3.549\ \text{kW}}.$$
  4. Heat absorbed from the ground water (part b), evaporator. $$\dot Q_L=\dot m(h_1-h_4)=0.0834\times(398.98-241.72)=\boxed{13.117\ \text{kW}}.$$ Check: $\dot Q_L+\dot W_{in}=13.117+3.549=16.667$ kW, matching $\dot Q_H$ to within rounding.
  5. Resistance heater comparison (part c). A resistance heater must supply the full $\dot Q_H$ electrically (COP $=1$), so the increase in electric power over the heat pump is $$\Delta \dot W=\dot Q_H-\dot W_{in}=16.667-3.549=\boxed{13.117\ \text{kW}}.$$
QuantityResult
(a) $\dot W_{in}$3.549 kW
(b) $\dot Q_L$13.117 kW
(c) $\Delta \dot W$ (resistance heater)13.117 kW