23-Chem-B2 Environmental Engineering · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Paper format. EGBC 04-Chem-B2 Environmental Engineering, December 2014, 3 hours, closed-book with a candidate-prepared double-sided 8½×11-inch aid sheet. Seven problems, each worth 20 marks; candidates attempt any five, and only the first five answers in the workbook are marked. All seven problems are solved below as a complete study resource.
Reference texts: G. Tchobanoglous, F. L. Burton & H. D. Stensel (Metcalf & Eddy), Wastewater Engineering: Treatment and Reuse (4th ed., McGraw-Hill) — BOD kinetics, dissolved air flotation, activated-sludge design, nutrient removal; M. L. Davis & D. A. Cornwell, Introduction to Environmental Engineering (5th ed., McGraw-Hill) — drinking-water treatment, air pollution control, ion exchange, reverse osmosis, soil remediation; C. D. Cooper & F. C. Alley, Air Pollution Control: A Design Approach — fabric filtration, thermal oxidation, adsorption, odour control; S. P. Turner, Workbook of Atmospheric Dispersion Estimates (2nd ed., CRC Press) — the Gaussian plume model and Pasquill–Gifford stability classes. Canadian context follows the Canadian Environmental Protection Act (CEPA 1999), the Canadian Council of Ministers of the Environment (CCME) Municipal Wastewater Effluent and Drinking Water Quality guidelines, and provincial air/water permitting practice (e.g. BC Environmental Management Act, Metro Vancouver air-quality bylaws), which govern effluent/emission limits and treatment-technology selection referenced throughout.
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.
| Quantity | Symbol | Value |
|---|---|---|
| Stack (effective) height | $H$ | $40\ \text{m}$ |
| SO₂ emission rate | $Q$ | $20\ \text{g/min}=0.3333\ \text{g/s}$ |
| Average wind speed | $u$ | $12\ \text{m/s}$ |
| Insolation | — | strong solar radiation |
| Stability class (Turner lookup) | — | $u>6\ \text{m/s}$, strong insolation ⇒ Class C |
| Class-C coefficients | $a,b,c,d,e,f$ | $110,\ 1.0,\ -0.005,\ 60,\ 1.2,\ 0.02$ |
| Target ground-level concentration | $C$ | $2\ \mu\text{g/m}^3$ |
Find. The downwind distance $x$ on the plume centerline ($y=0$) at ground level ($z=0$) at which the predicted concentration falls to about 2 µg/m³.
Approach. The Turner wind-speed/insolation lookup table selects the stability class before the dispersion coefficients can be evaluated: at 12 m/s (above the ≈6 m/s mechanical-turbulence threshold) with strong insolation, the table gives Class C, not the more-unstable A/B that "strong solar radiation" alone might otherwise suggest. Class-C coefficients feed the standard ground-level, on-axis Gaussian plume formula; because $\sigma_y,\sigma_z$ are themselves power-law functions of $x$, the concentration-vs-distance relation is evaluated numerically.
| Quantity | Result |
|---|---|
| Peak ground-level concentration | ≈1.95 µg/m³ at x≈0.56 km |
| Distance where C most nearly reaches 2 µg/m³ | x ≈ 0.56 km (point of closest approach; target not crossed) |
Because the computed peak (1.95 µg/m³) sits so close to the 2 µg/m³ target, the conclusion is sensitive to the stability-class assignment: the standard Turner wind-speed/insolation table gives Class C for >6 m/s wind with strong insolation (used here), but if a Class D (neutral) assumption were instead applied the peak would be ≈5.5 µg/m³ — clearly above target, with a genuine crossing distance. The exam's own phrase "moderated unstable" is, in Turner's naming, Class B (moderately unstable); using the Class B row instead gives a peak of ≈5.1 µg/m³ at x≈0.26 km that falls back through 2 µg/m³ at x≈0.58 km — essentially the same distance as the Class C answer, so the reported x ≈ 0.56–0.58 km is robust to that reading. The Class-C result is retained as the correct table lookup for a 12 m/s wind with strong solar radiation, but the closeness of the margin is itself an engineering finding worth noting.
Measure 1 — Flue-gas desulfurization (FGD). A wet limestone/lime scrubber downstream of the boiler removes SO₂ before it reaches the stack, directly cutting the emission rate $Q$ in the dispersion formula. Carbon footprint: the most effective source-reduction measure (routinely >90% SO₂ removal), but the scrubber's induced-draft fans, pumps and limestone-slurry preparation impose a parasitic auxiliary-power load on the plant, marginally raising its CO₂ intensity per unit net power delivered even though it does not touch the fuel-combustion CO₂ itself.
Measure 2 — Increase effective stack height. Raising $H$ increases the $\exp(-H^2/2\sigma_z^2)$ dilution term, lowering ground-level concentration at any given $x$. Carbon footprint: essentially carbon-neutral (a structural, one-time modification with no ongoing energy penalty) but it achieves no reduction in total SO₂ mass emitted — it only redistributes the same load over a larger area/greater distance, so it does nothing for the plant's actual carbon or SO₂ mass footprint, only the local ground-level peak.
Measure 3 — Fuel switching to lower-sulfur natural gas supply. Sourcing a pipeline gas blend with lower sulfur content reduces $Q$ at the source without any new equipment. Carbon footprint: genuinely reduces the SO₂ mass emitted with essentially no change in the plant's CO₂ intensity (natural gas combustion CO₂ is set by carbon content/heating value, largely independent of the trace sulfur content), making this the lowest-carbon-footprint of the three measures, though it is constrained by regional gas-supply sulfur specifications and may carry a fuel-price premium.
Preferred measure. Low-sulfur fuel switching is preferred on a carbon-footprint basis: it achieves genuine source-side SO₂ mass reduction (unlike stack-height increase) without FGD's parasitic auxiliary-power CO₂ penalty, making it the option with the smallest incremental carbon footprint for a comparable SO₂ benefit — though FGD remains the more robust choice where fuel-supply sulfur content cannot be controlled.