Generated ERQ

✓ passed B.1 Thermal energy transfers × A.3 Work, energy and power 12 marks HL 3 passes 132.29s $0.8339
## 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. --- ## 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.