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22-Mec-B3 Energy Conversion and Power Generation · May 2018

Question 6 of 8: Coal Fired Boiler

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.

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.

Question 6: Coal Fired Boiler (10 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.

FURNACE(water-wall tubes,radiant absorption)pulverisedcoal + primaryair burnersDRUMBoiler (steam) drumdowncomerSEC.S/HRE-HEATERPRIMARYSUPERHEATERECONOMISER(feedwater)rear (convection) passflue gas to air heater,precipitator and stackfeedwater into drumsaturated steam to primary S/Hto secondary (finishing) superheatermain steamcold reheat from HP turbinehot reheatRadiant zone: furnace water walls · convective zone: superheaters, reheater, economiserGas temperature falls continuously from the furnace exit to the economiser outlet
Question 6(a) — the page-13 attachment with its heat absorption components identified. Gas leaves the furnace, crosses the two pendant banks hung in the furnace roof, turns down at the nose into the rear convection pass and passes in turn over the primary superheater and the economiser before leaving for the air heater and stack. Water lines are solid, steam lines dashed, as in the legend on the attachment.

(a) Identification of the components. The tall left-hand shaft, lined on all four walls with closely spaced tubes and containing the flame, is the furnace. The horizontal cylinder at the top left, joined to the bottom of the furnace by the external downcomer and to the top of the water walls by the risers, is the boiler drum. In the rear pass, where the gas is coolest, the lowest horizontal serpentine bank carries the incoming feedwater and is the economiser; immediately above it, the first bank fed with saturated steam from the drum is the primary superheater. The two pendant banks hung in the furnace roof take the hottest gas: the one at the furnace exit, which finishes the main steam, is the secondary (finishing) superheater, and the one immediately downstream of it, fed from the cold reheat line returning from the high-pressure turbine, is the reheater. On the returned attachment these six labels are written directly against the corresponding features.

(b) Combustion system, fuel preparation and conveying. The arrangement is a pulverised-fuel suspension-fired boiler with wall-mounted burners on opposite furnace walls, which is what the burner ports drawn on both sides of the furnace indicate. Raw coal is delivered from the bunkers through gravimetric feeders to the mills, where it is ground until roughly seventy per cent passes a 75 µm sieve. Hot primary air, drawn through the air heater and tempered to control mill outlet temperature, is blown through the mill to dry the coal and then carries the pulverised fuel in suspension along the fuel pipes to the burners. At the burner the fuel-laden primary air is discharged into a swirling stream of secondary air supplied from the windbox by the forced draught fan; the swirl anchors the flame and completes the combustion in the furnace volume. Because the particles are so fine, they burn in suspension in one or two seconds, which is what allows a furnace of this size to release the several hundred megawatts of heat a large unit needs. Ash leaves in two streams: the heavier fraction falls into the hopper at the furnace bottom, while the fly ash is carried with the gas to the precipitator or bag filter downstream of the air heater.

(c) Radiation and convection surfaces. The furnace water walls, and the leading rows of the pendant secondary superheater that see the flame directly, absorb heat overwhelmingly by radiation from the luminous flame and the hot gas; radiation dominates wherever the gas temperature is high, because the exchange goes as the fourth power of absolute temperature. Everything in and beyond the furnace nose — the rest of the pendant banks, the reheater, the primary superheater and the economiser in the rear pass — absorbs mainly by convection from gas that is now cool enough and clean enough of luminous particles that radiation is secondary. The banks nearest the furnace exit are genuinely mixed, and that mixed character is exploited deliberately, as the next part explains.

(d) Purpose and placement of each surface. The economiser recovers the last useful heat from the flue gas into the feedwater. It sits at the cold end of the rear pass because the feedwater is the coldest fluid in the unit, so it is the only surface that can still extract heat from gas at 300 °C or below; putting it anywhere hotter would waste high-grade heat on low-grade duty and risk steaming in the tubes. Its practical limit is the acid dew point of the gas, which is why the gas is not cooled further until it reaches the air heater.

The superheaters raise the steam above saturation, which increases the enthalpy drop available in the turbine and, more importantly, keeps the expansion dry enough to protect the last-stage blading. They are split into a primary and a secondary section for control: the primary sits in the convective rear pass, where its absorption rises with gas flow and hence with load, while the secondary hangs in the radiant furnace exit, where its absorption falls relatively as load rises. Combining the two opposite characteristics, with an attemperator between them, is what holds the final steam temperature nearly constant over the load range. The secondary section must be last on the steam side and first on the gas side because it produces the hottest steam and therefore needs the largest driving temperature difference.

The reheater returns the steam exhausted from the high-pressure turbine to close to main-steam temperature before it enters the intermediate-pressure turbine. This adds several points of cycle efficiency and, again, keeps the low-pressure exhaust dry. It is placed just downstream of the secondary superheater, in gas hot enough to reach the required steam temperature but not so hot as to overheat tubes that carry steam at only a quarter of the main-steam pressure and therefore have thin walls and poor cooling at low flows. Its position also explains why the reheater must never be fired with the turbine off load: with no steam flow through it, the tubes have nothing to carry the absorbed heat away.

Check: which pendant bank is the reheater. The attachment distinguishes steam lines from water lines but does not name the two pendant banks. The identification above places the secondary superheater first in the gas path and the reheater immediately behind it, which is the usual arrangement and is consistent with the dashed line entering the second bank from the right-hand side of the drawing, that is, from the turbine hall. A candidate who reverses the two and gives the same reasoning — hottest gas to the surface that must reach the highest steam temperature — should be given the mark.