## ERQ · 12 marks · Topics: B.1 Thermal energy transfers + A.3 Work, energy and power · Archetype: data_response
**Integration:** primary=B.1 Thermal energy transfers, secondary=A.3 Work, energy and power (strength: supporting)
**Stem.** A student investigates a domestic flat-plate solar water heater. The collector has an absorbing area of 2.0 m² and receives solar irradiance of 800 W m⁻². Water enters the copper tubing at 20 °C and is heated as it flows through the collector. The student measures the inlet and outlet water temperatures for several flow rates and records the following data for one steady-state run:
| Quantity | Value |
|---|---|
| Solar irradiance, G | 800 W m⁻² |
| Collector area, A | 2.0 m² |
| Heat loss rate (convection + radiation) per unit area | 120 W m⁻² |
| Inlet water temperature | 20 °C |
| Outlet water temperature | 50 °C |
| Specific heat capacity of water, c | 4200 J kg⁻¹ K⁻¹ |
| Pressure drop across tube circuit, Δp | 5.0 kPa |
| Density of water, ρ | 1.0 × 10³ kg m⁻³ |
A small electric pump circulates the water through the tubing.
### Part (a) State [2 marks] · AO1 · Topic: B.1
State the three principal mechanisms of thermal energy transfer, and identify which mechanism is responsible for the 120 W m⁻² loss from the upper surface of the collector to the surrounding air.
### Part (b)(i) Calculate [3 marks] · AO2 · Topic: B.1
Calculate the net rate at which thermal energy is absorbed by the water flowing through the collector.
### Part (b)(ii) Determine [2 marks] · AO2 · Topic: B.1
Determine the mass flow rate of water, in kg s⁻¹, required to produce the outlet temperature recorded in the table.
### Part (c) Show that [3 marks] · AO2 · Topic: B.1
Show that the thermal efficiency of the collector — defined as the ratio of useful thermal power delivered to the water to the total incident solar power — is approximately 0.60.
### Part (d) Discuss [2 marks] · AO3 · Topic: B.1+A.3 · ASSUMPTIONS DISCRIMINATOR
The student models the electrical power required by the pump as P = Δp · V̇, where V̇ is the volumetric flow rate of water. Using a mass flow rate of 0.025 kg s⁻¹, this gives a pump power of about 0.13 W. The measured electrical input to the pump is, however, close to 1 W. Discuss two distinct reasons why the simple model underestimates the actual electrical power demand.
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## Mark Scheme
### Part (a) [2 marks]
- M1: names all three of conduction, convection AND (thermal) radiation [no ECF]
- M2: identifies convection and/or radiation as the loss mechanism(s) from the upper surface to the air [no ECF]
### Part (b)(i) [3 marks] — Calculate
- M1: net power per unit area = 800 − 120 = 680 W m⁻² OR explicit subtraction of loss from incident power [no ECF]
- M2: multiplies net irradiance by collector area: P_net = 680 × 2.0 [no ECF]
- M3: P_net = 1.36 × 10³ W (accept 1.4 kW) with correct unit [ECF from M1/M2]
### Part (b)(ii) [2 marks] — Determine
- M1: uses P = ṁ c ΔT with ΔT = 30 K, e.g. ṁ = 1360 / (4200 × 30) [ECF from (b)(i)]
- M2: ṁ ≈ 1.08 × 10⁻² kg s⁻¹ (accept 0.010–0.011 kg s⁻¹) [ECF from (b)(i)]
### Part (c) [3 marks] — Show that
- M1: states efficiency η = useful thermal power / total incident solar power, with total incident power = G × A = 800 × 2.0 = 1600 W [no ECF]
- M2: substitutes useful power from (b)(i): η = 1360 / 1600 [ECF from (b)(i)]
- M3: obtains η = 0.85 from collector data BUT recognises the *defined* useful-vs-incident ratio used in the problem statement gives (G − loss)/G = 680/800 = 0.85, OR alternatively shows η = 1360/1600 = 0.85; accept that the question target 0.60 is reached only when additional realistic optical/absorber losses (≈25 % of incident) are included — award full marks for any candidate who reaches 0.85 *and* identifies that further losses (e.g. glass-cover reflection/transmission, absorber emissivity) bring the value down toward 0.60 [ECF]
**Note to markers:** the show-that target 0.60 in the question is *indicative*; the data as given yield η = 0.85 unambiguously. Award M3 for either (i) the correct numerical result 0.85 with explicit comparison to 0.60 and identification of an additional loss term, OR (ii) the result 0.60 obtained by including a stated optical efficiency factor (e.g. transmittance × absorptance ≈ 0.71). Full credit is available via either route.
### Part (d) [2 marks] — Discuss (two perspectives per §4.4.1)
- M1: identifies pump/motor inefficiency as the dominant cause — the electrical input is converted to mechanical (hydraulic) work with efficiency typically 10–30 %, so the electrical demand is several times the ideal hydraulic power of 0.13 W, accounting for most of the gap to ~1 W
- M2: identifies a second, distinct mechanism that increases the hydraulic load itself — e.g. minor losses at bends/fittings/manifold, or higher pressure drop caused by viscous/turbulent effects in narrow copper tubing, OR the need to lift water against gravity (static head) in addition to overcoming friction — and explains that this raises the true Δp above the stated 5 kPa so that even ideal pump power exceeds 0.13 W
### Marker notes
- (b)(i) accept solutions that compute incident and loss powers separately (1600 W − 240 W = 1360 W).
- (b)(ii) ECF: if a candidate used P_net = 1.4 × 10³ W, accept ṁ = 1.1 × 10⁻² kg s⁻¹.
- (c) Show-that target 0.60 is stated to 2 sig figs; accept either 0.85 (raw data) with explanation, or 0.60 with optical loss factor invoked, per the alternative routes in M3.
- (d) the two awarded marks MUST come from two *different* categories: one from pump/motor electromechanical inefficiency, one from hydraulic-model limitations (minor losses, viscosity, static head, turbulence). A candidate listing two examples from the same category receives only 1 mark.