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18-Env-A5 Air Quality and Pollution Control Engineering · May 2013

Question 7 of 7: Control of SOx and NOx, Flue Gas Desulfurisation and Photochemical Smog

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

Notes on this paper

National Exams — May 2013 — 04-Env-A5 / Air Quality and Pollution Control Engineering. 3 hours duration; closed book with a candidate-prepared 8.5×11 in double-sided aid sheet; Casio or Sharp approved calculator only. Any five (5) questions constitute a complete paper (the first five answers as they appear are marked); all seven are solved below for completeness. Each question is worth 20 marks with section marks shown in brackets.

Reference texts. Cooper & Alley, Air Pollution Control: A Design Approach (4th ed.); Wark, Warner & Davis, Air Pollution: Its Origin and Control (3rd ed.); Davis & Cornwell, Introduction to Environmental Engineering (6th ed.); Canadian Environmental Protection Act, 1999 (CEPA) and the Canadian Ambient Air Quality Standards (CAAQS) administered by Environment and Climate Change Canada.

Question 7: Control of SOx and NOx, Flue Gas Desulfurisation and Photochemical Smog (20 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.

(i) Two NOx Control Strategies: Comparison Matrix

Combustion modification vs. post-combustion SCR for NOx control
StrategyMechanismTypical NOx reductionAdvantagesCosts / drawbacks
Combustion modification (staged/low-NOx burners, flue-gas recirculation)Lowers peak flame temperature and local O2 availability, suppressing thermal-NOx formation at its source (Question 1(ii))≈ 30–50%No consumable reagent; low incremental operating cost; can often retrofit existing burnersCannot reach the very low NOx limits some jurisdictions require; some loss of combustion efficiency/flame stability if over-applied
Selective catalytic reduction (SCR)Injects NH3/urea ahead of a catalyst bed to reduce NOx to N2 and H2O after it has already formed≈ 80–90%+Reaches the deepest NOx reduction of any single technology; effective regardless of how NOx formedHigh capital cost (catalyst, reactor, reagent injection/storage); ongoing reagent and catalyst-replacement cost; risk of ammonia slip if over-dosed

The two strategies are complementary rather than substitutes: combustion modification is the low-cost first step that reduces the load the (much more expensive) SCR system must then polish to meet a strict emission limit, which is why most modern coal-fired stations use both together.

(ii) Two Engineering Principles Controlling FGD Effectiveness

Principle 1 — liquid-to-gas ratio and gas–liquid contact time. In a wet limestone/lime scrubber, SO2 must diffuse from the bulk gas into the alkaline slurry droplets/film and react before the gas exits the absorber; effectiveness rises with a higher liquid-to-gas (L/G) flow ratio and longer residence time in the spray/packed zone, because both increase the cumulative mass-transfer area and contact time available for absorption, up to the point where gas-side pressure drop or flooding becomes limiting.

Principle 2 — slurry alkalinity (stoichiometric ratio) and pH control. SO2 absorption and its conversion to a stable sulfite/sulfate product depend on maintaining sufficient dissolved alkalinity (limestone/lime fed at a stoichiometric ratio typically 1.02–1.10 relative to the SO2 load) and a controlled slurry pH (typically 5.5–6.0 for limestone systems); too little alkalinity or too low a pH starves the absorption reaction and lets SO2 slip through, while too high a pH risks scaling/plugging from calcium sulfite/sulfate precipitation on the internals.

(iii) Two Necessary Conditions for Photochemical Smog Formation

Condition 1 — an adequate supply of NOx and reactive VOC (hydrocarbon) precursors. Photochemical smog is the product of a radical chain reaction between NOx (chiefly from combustion, especially vehicle exhaust) and reactive volatile organic compounds (from vehicle exhaust, solvent evaporation, and biogenic sources); without both precursor classes present together in sufficient concentration the ozone-forming cycle has no chain to propagate — NOx alone or VOC alone cannot sustain net ozone production.

Condition 2 — strong solar UV radiation (and typically a temperature inversion trapping the precursors). The chain is initiated by photolysis of NO2 ($\text{NO}_2 + h\nu \rightarrow \text{NO} + \text{O}$), which requires sunlight of sufficient intensity and UV content — this is why smog episodes peak on clear, sunny, warm afternoons rather than at night or under heavy overcast. A low-level temperature inversion (common with light wind and strong daytime heating trapped under a stable layer aloft) is typically also present, because it confines the precursors near ground level long enough for the sunlight-driven chain reaction to build ozone and other oxidants to smog-episode concentrations rather than letting them disperse and dilute before reacting.

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