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22-Mec-B3 Energy Conversion and Power Generation · May 2013

Question 3 of 6: Belledune Heat Balance Diagram — cycle efficiency, HP turbine power and feed pump performance at 430 MW

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

Notes on this paper

Paper format. National Examinations, May 2013 — 07-Mec-B3 Energy Conversion and Power Generation. Three hours, closed book. Section A (calculative) carries Questions 1 to 4 and Section B (descriptive) carries Questions 5 and 6; a candidate answers three from Section A and one from Section B, so four questions constitute a complete paper of 60 marks and every question is worth 15 marks. Reference data for particular questions are supplied on pages 9 to 12 of the paper (Matla Power Station data sheet, the natural-draught cooling-tower evaporative-loss chart, the combined-cycle system diagram and the Belledune heat balance diagram), reference formulae and constants on pages 13 to 16, and steam tables from Granet and Bluestein are provided. All six questions are solved here.

Reference texts.

Question 3: Belledune Heat Balance Diagram — cycle efficiency, HP turbine power and feed pump performance at 430 MW (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. The Belledune heat balance diagram of page 12, at a rated generator output of 430 MW. The streams that bear on the six parts are listed below; G denotes a mass flow in kg/h, H a specific enthalpy in kJ/kg, P a pressure in MPa and T a temperature in °C, following the annotation convention of the diagram itself.

Streams read from the page-12 heat balance diagram
StreamFlow (kg/h)Conditions
Main steam / final feedwater1 287 30916.65 MPa, 538 °C, $h=3397.5$; feedwater 19.8 MPa, 280 °C, $h=1231.4$
HP extraction to the top heater127 7296.72 MPa, 404.1 °C, $h=3175.9$
HP gland and valve-stem leak-offs12 220 + 3 940 + 1 600 + 340 = 18 100leave at throttle enthalpy, doing no work
HP exhaust (cold reheat header)1 141 480$h=3002.7$
Steam reheated1 039 160hot reheat $h=3542.5$
Boiler feed pump turbine steam50 140in 0.542 MPa, $h=3068.9$; exhaust 0.0046 MPa, $h=2432.6$
Feed pump1 287 309$\Delta h=24.45$ kJ/kg; suction 0.554 MPa; discharge 19.8 MPa; $\rho=912$ kg/m3

Find. The steam cycle efficiency on boiler heat input, the HP turbine shaft power, the steam power supplied to the boiler feed pump turbine, the shaft and hydraulic powers of the feed pump, and hence the feed pump efficiency.

Q3 Belledune Generating Station - principal heat balance streams at 430 MWBOILERandREHEATERHPIP / LPG430 MWCONDBFPTDEAERATORFEED PUMPTOP HEATERAEDCBto gridLP exhaustFFcondensateHGBFPT shaft drives the boiler feed pumpStream data read from the heat balance diagramAMain steam and final feedwater flow 1 287 309 kg/h; 16.65 MPa, 538 C, h = 3397.5 kJ/kgBHP extraction to the top heater 127 729 kg/h; 6.72 MPa, 404.1 C, h = 3175.9 kJ/kgCHP gland and valve-stem leak-offs 12 220 + 3 940 + 1 600 + 340 = 18 100 kg/h at throttle enthalpyDHP exhaust to the cold reheat header 1 141 480 kg/h at h = 3002.7 kJ/kg, of which 1 039 160 kg/h is reheatedEHot reheat to the IP turbine 1 039 160 kg/h at h = 3542.5 kJ/kgFBFPT steam 50 140 kg/h; in 0.542 MPa, h = 3068.9 kJ/kg; exhaust h = 2432.6 kJ/kg; coupling 8 741 kWGBoiler feed pump discharge 19.8 MPa; enthalpy rise across the pump 24.45 kJ/kg; density 912 kg/m3HDeaerator (pump suction) 0.554 MPa, 155.7 C, h = 656.9 kJ/kg
The principal streams of the Belledune heat balance, with the stream data listed beneath the schematic. The boiler heat input is the sum of the main steam duty (A against G) and the reheat duty (E against D); the boiler feed pump turbine F is driven by extraction steam and its shaft carries the feed pump.

Approach. The boiler heat input is the sum of two duties, the main steam pass and the reheat pass, each computed from its own mass flow and enthalpy rise. The HP turbine power is then a steady-flow energy balance on a control volume enclosing the HP cylinder, with the leak-off flows removed before the expansion because they never do work. The feed pump is analysed twice, thermodynamically from its enthalpy rise and hydraulically from its pressure rise, and the ratio of the two is the pump efficiency.

  1. Part (a) — boiler heat input. The boiler adds heat in two passes. The main pass takes the final feedwater to main steam conditions and carries the whole feedwater flow, and the reheat pass takes cold reheat steam to hot reheat conditions and carries only the reheated flow: $$\dot{Q}_{b}=\frac{G_{ms}}{3600}(h_{ms}-h_{fw})+\frac{G_{rh}}{3600}(h_{hrh}-h_{crh})$$ The main pass gives $(1\,287\,309/3600)\times(3397.5-1231.4)=774\,567\ \text{kW}$ and the reheat pass $(1\,039\,160/3600)\times(3542.5-3002.7)=155\,816\ \text{kW}$.
  2. Part (a) continued — cycle efficiency. The total is $$\dot{Q}_{b}=774\,567+155\,816=930\,383\ \text{kW}$$ so with 430 MW at the generator terminals $$\eta_{cycle}=\frac{430\,000}{930\,383}=\boxed{0.4622}$$ that is 46.2 %, equivalent to a station heat rate of $3600/0.4622=7789\ \text{kJ}\cdot(\text{kW}\cdot\text{h})^{-1}$ on boiler heat. The reheat pass supplies 16.7 % of the boiler duty, and note that this efficiency is measured on heat into the steam, so it excludes the boiler loss and is properly compared with the 48 % assumed in Question 1, not with an overall plant figure.
  3. Part (b) — HP turbine shaft power, control volume. Take a control volume around the HP cylinder. Steam enters at the throttle, three streams leave: the gland and valve-stem leak-offs, which are tapped upstream of the blading and so leave at throttle enthalpy having done no work; the extraction to the top heater at state $h_{ext}$; and the exhaust to the cold reheat header at $h_{crh}$. Removing the leak-offs first, the flow that actually expands is $1\,287\,309-18\,100=1\,269\,209\ \text{kg}\cdot\text{h}^{-1}$, and the diagram closes exactly on $1\,269\,209=1\,141\,480+127\,729$, which confirms the leak-off total.
  4. Part (b) continued — energy balance. The shaft power is the enthalpy the expanding steam gives up: $$\dot{W}_{HP}=\frac{1}{3600}\left[(G_{ms}-G_{leak})(h_{ms}-h_{ext})+G_{exh}(h_{ext}-h_{crh})\right]$$ The first group is the whole working flow dropping 3397.5 to 3175.9, that is 221.6 kJ/kg, and the second is the surviving exhaust flow dropping a further $3175.9-3002.7=173.2\ \text{kJ}\cdot\text{kg}^{-1}$. Substituting, $$\dot{W}_{HP}=\frac{1\,269\,209\times221.6+1\,141\,480\times173.2}{3600}=\boxed{133\,045\ \text{kW}}$$ The HP cylinder therefore accounts for 30.9 % of the 430 MW at the terminals, the IP and LP cylinders supplying the rest.
  5. Part (c) — steam power into the feed pump turbine. The boiler feed pump turbine is a small back-pressure machine taking 50 140 kg/h of steam at 0.542 MPa and exhausting to the main condenser: $$\dot{W}_{steam}=\frac{G_{bfpt}}{3600}(h_{in}-h_{out})=\frac{50\,140}{3600}\times(3068.9-2432.6)=\boxed{8862\ \text{kW}}$$ an available enthalpy drop of 636.3 kJ/kg. This is the steam power presented to the turbine, not yet the power delivered to the pump.
  6. Part (d) — shaft power into the pump. Measured on the water side, the shaft power is whatever raises the enthalpy of the whole feedwater flow by the stated 24.45 kJ/kg across the pump: $$\dot{W}_{shaft}=\frac{G_{fw}}{3600}\,\Delta h_{pump}=\frac{1\,287\,309}{3600}\times24.45=\boxed{8743\ \text{kW}}$$ The diagram itself prints 8741 kW at the feed pump turbine coupling, so the two agree to 0.02 %. Comparing with part (c), the feed pump turbine converts its 8862 kW of steam power into 8743 kW at the coupling, an internal and mechanical efficiency of 98.7 %; on a real machine that number would be nearer 80 %, and the near unity here indicates that the diagram treats the small turbine as a nearly ideal expander whose exhaust enthalpy has already been credited with its losses.
  7. Part (e) — hydraulic power. Hydraulically the pump does work against the pressure rise from the deaerator to the discharge, and because water is nearly incompressible that work is $v\,\Delta p=\Delta p/\rho$ per kilogram: $$\dot{W}_{hyd}=\frac{G_{fw}}{3600}\cdot\frac{(p_{d}-p_{o})}{\rho}=\frac{1\,287\,309}{3600}\times\frac{(19.8-0.554)\times10^{3}}{912}$$ The specific work is $19\,246/912=21.10\ \text{kJ}\cdot\text{kg}^{-1}$ against a volume flow of $0.3921\ \text{m}^{3}\cdot\text{s}^{-1}$, giving $$\dot{W}_{hyd}=\boxed{7546\ \text{kW}}$$
  8. Part (f) — feed pump efficiency. The pump efficiency is the useful hydraulic output over the shaft input: $$\eta_{pump}=\frac{\dot{W}_{hyd}}{\dot{W}_{shaft}}=\frac{7546}{8743}=\boxed{0.863}$$ The missing 13.7 % appears as the difference between the actual enthalpy rise of 24.45 kJ/kg and the ideal 21.10 kJ/kg, that is as a 3.35 kJ/kg temperature rise of the feedwater, which is exactly what an 86 % efficient boiler feed pump of this size would be expected to return.
Final Results — Question 3
PartQuantityResult
(a)Boiler heat input (main 774 567 + reheat 155 816)$930\,383\ \text{kW}$
(a)Steam cycle efficiency on boiler heat input$0.4622$ (46.2 %)
(b)HP turbine shaft power$133\,045\ \text{kW}$
(c)Steam power into the boiler feed pump turbine$8862\ \text{kW}$
(d)Shaft power into the boiler feed pump$8743\ \text{kW}$
(e)Hydraulic power output of the feed pump$7546\ \text{kW}$
(f)Feedwater pump efficiency$0.863$ (86.3 %)
Three independent checks confirm the readings: the HP turbine mass balance closes exactly ($1\,287\,309-18\,100=1\,141\,480+127\,729$), the cold-reheat header closes exactly ($1\,141\,480=1\,039\,160+101\,910+410$), and the diagram saturation temperatures agree with the steam tables at the pressures printed beside them (0.554 MPa against 155.7 °C, 6.31 MPa against 278.9 °C). The computed feed pump shaft power of 8743 kW also reproduces the 8741 kW printed at the coupling. No datum here is reconstructed. One incidental reading is genuinely illegible: the mark allocation printed against part (e) on page 5. It is taken as 3 marks, because the other five parts are legible at 3, 4, 2, 2 and 1 and the question carries a stated total of 15.