22-Mec-B3 Energy Conversion and Power Generation · May 2018
Question 3 of 8: Nuclear Plant Output
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. 16-Mec-B3
Energy Conversion and Power Generation, National Examinations, May 2018.
Three hours, closed book. Two sections: Section A is calculative
(Questions 1–5) and Section B is descriptive (Questions 6–8).
Candidates answer four questions from Section A and two from Section B; six
questions of 10 marks each constitute a complete paper (60 marks). Reference
data for individual questions are bound in as attachments on pages 9–15,
reference formulae and constants on pages 16–19, and Granet &
Bluestein steam tables are supplied. All eight questions are solved
below, because the set is a study resource rather than a timed attempt.
Reference texts.
Granet, I. and Bluestein, M., Thermodynamics and Heat Power, 6th ed.
— the steam tables issued with this paper, and the vapour-cycle and
gas-cycle chapters.
Çengel, Y. A. and Boles, M. A., Thermodynamics: An Engineering
Approach, 9th ed. — Brayton and Rankine cycles, combined cycles,
isentropic component efficiencies.
El-Wakil, M. M., Powerplant Technology — heat recovery steam
generators and pinch behaviour, condensers and their off-design response,
boiler heat-absorption surfaces, load scheduling.
Lamarsh, J. R. and Baratta, A. J., Introduction to Nuclear
Engineering, 4th ed. — the pressurised water reactor, primary loop
heat removal, once-through steam generators.
Dixon, S. L. and Hall, C. A., Fluid Mechanics and Thermodynamics of
Turbomachinery, 7th ed. — hydraulic turbines, net head and the energy
accounting of a waterway.
Wherever the paper's own attachments carry a value that duplicates a computed
result — the Koeberg terminal temperature difference and back pressure on
page 10, the gas-turbine output quoted in the preamble to Question 2,
the published rating of the Oconee unit — that printed value is used as an
independent check and the agreement is quoted in the answer.
Given. One pressurised water reactor unit circulates 16 460 kg/s of primary coolant at 15 MPa, heating it from 290 °C to 318 °C in the core; the two once-through steam generators raise slightly superheated steam at 6 MPa, and the steam cycle and station auxiliaries have stated efficiencies.
Find. The reactor and steam generator heat output rates, the steam flow to the turbine, the gross and net electrical output, and the heat rejected to the cooling water, together with a labelled system sketch.
Question 3(a) — the complete unit with feedwater heating omitted, as the question directs. The primary loop (red) carries heat from the reactor at 318 °C to the steam generators and returns at 290 °C; the steam cycle (green) takes 6 MPa steam at 300 °C to the turbine and exhausts at 30 °C; the cooling water (blue) rises from 10 °C to 20 °C.
Approach. Take the reactor duty from the enthalpy rise of compressed liquid water across the core, add the pump work that also enters the coolant, apply the steam generator efficiency, divide the resulting duty by the water-to-steam enthalpy rise for the flow, and close an energy balance on the steam cycle for the rejected heat.
Part (b) — do not use the 4.19 constant for the primary coolant. At 15 MPa the water is a compressed liquid near 300 °C, where its specific heat is far above the room-temperature value. Reading the compressed-liquid table, $h(15\ \text{MPa},\,290\ ^\circ\text{C}) = 1284.7$ and $h(15\ \text{MPa},\,318\ ^\circ\text{C}) = 1441.8\ \text{kJ/kg}$, so $$\Delta h = 1441.8 - 1284.7 = 157.1\ \text{kJ/kg},$$ an effective $c_p = 157.1/28 = 5.61\ \text{kJ/kg K}$ — a third higher than 4.19. Using the page-17 constant here would understate the reactor power by a quarter.
Reactor heat output. The core delivers $$\dot{Q}_{\text{reactor}} = M \Delta h = 16\,460 \times 157.1 = \boxed{2\,586\,000\ \text{kW} = 2586\ \text{MW(th)}} .$$ The published rating of an Oconee unit is 2568 MW(th), so the calculation lands 0.7 % from the real machine — a free confirmation that the compressed-liquid reading, and not the 4.19 shortcut, is the intended route.
Steam generator heat output. The four reactor coolant pumps do 16 MW of work on the coolant, and that work is degraded to heat inside the primary loop, so it must be carried to the steam generators along with the fission heat. Applying the 98 % steam generator efficiency to the sum, $$\dot{Q}_{sg} = \eta_{sg}(\dot{Q}_{\text{reactor}} + P_{\text{pump}}) = 0.98 \times (2\,586\,000 + 16\,000) = \boxed{2\,549\,500\ \text{kW} = 2550\ \text{MW}} .$$ The 2 % shortfall, about 52 MW, is casing and pipework loss to the containment atmosphere.
Part (c) — enthalpy rise across the steam generator. At 6 MPa the saturation temperature is 275.6 °C, so the 220 °C feedwater is indeed subcooled and the 300 °C outlet is superheated, exactly as the question states — a once-through generator, with no drum and no recirculation. From the compressed-liquid and superheat tables, $$h_{fw} = 944.6\ \text{kJ/kg},\qquad h_{\text{steam}} = 2885.5\ \text{kJ/kg},$$ $$\Delta h_{sg} = 2885.5 - 944.6 = 1940.9\ \text{kJ/kg} .$$
Steam mass flow. Dividing the steam generator duty by that rise, $$M_{\text{steam}} = \frac{\dot{Q}_{sg}}{\Delta h_{sg}} = \frac{2\,549\,500}{1940.9} = \boxed{1314\ \text{kg/s}} ,$$ that is 4730 t/h, split between the two steam generators.
Part (d) — turbine power. The steam cycle efficiency is defined on the heat supplied to it, so $$P_{\text{gross}} = \eta_{cy}\dot{Q}_{sg} = 0.36 \times 2\,549\,500 = \boxed{917\,800\ \text{kW} = 918\ \text{MW(e)}} .$$
Part (e) — net electrical output. Auxiliaries take 7 % of that gross figure: $$P_{\text{aux}} = 0.07 \times 917\,800 = 64\,200\ \text{kW},\qquad P_{\text{net}} = 0.93 \times 917\,800 = \boxed{853\,600\ \text{kW} = 854\ \text{MW(e)}} .$$ The overall station efficiency is then $853.6/2586 = 33.0$ %, which is the figure the real units achieve and is a second free check on the whole chain.
Part (f) — heat rejected to the cooling water. The steam cycle receives $\dot{Q}_{sg}$ and delivers $P_{\text{gross}}$ as electricity; everything else leaves through the condenser. The 16 MW of pump work is already inside that balance because it entered the primary coolant, whereas the remaining 48 MW of auxiliary load is dissipated to atmosphere and never reaches the condenser. Hence $$\dot{Q}_{\text{rej}} = \dot{Q}_{sg} - P_{\text{gross}} = 2\,549\,500 - 917\,800 = \boxed{1\,631\,700\ \text{kW} = 1632\ \text{MW}} .$$ As a check on scale, the cooling water carrying it away at a 10 K rise must flow at $1\,631\,700/(4.19 \times 10) = 38\,940\ \text{kg/s}$, that is 38.9 m3/s — the once-through circulating water demand of a large PWR, and the reason such stations sit on a lake or a large river.
Final results
Quantity
Symbol
Value
Reactor heat output
$\dot{Q}_{\text{reactor}}$
2586 MW(th)
Steam generator heat output
$\dot{Q}_{sg}$
2550 MW
Steam flow to the turbine
$M_{\text{steam}}$
1314 kg/s
Gross turbine output
$P_{\text{gross}}$
918 MW(e)
Station auxiliary demand
$P_{\text{aux}}$
64 MW
Net electrical output
$P_{\text{net}}$
854 MW(e)
Heat rejected to cooling water
$\dot{Q}_{\text{rej}}$
1632 MW
Cooling water flow required
$\dot{V}$
38.9 m3/s
Overall station efficiency
$\eta_{\text{overall}}$
33.0 %
Check: the reactor coolant pump work is charged to the cycle. The question isolates the pumps deliberately — it says the auxiliary heat is dissipated to atmosphere but not that of the reactor coolant pumps. Their 16 MW is therefore added to the fission heat before the steam generator efficiency is applied, which is what a pressurised water reactor actually does: the pumps sit inside the pressure boundary and every watt they absorb reappears as heat in the coolant. Omitting it changes the answers by about 0.6 %, which is inside the "approximate" tolerance the question claims for its data, but stating the treatment is worth a mark.