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23-Chem-B2 Environmental Engineering · December 2019

Question 7 of 7: Sources and Dispersion of Atmospheric Pollutants

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

Notes on this paper

National Exam 16-Chem-B2, Environmental Engineering — December 2019. 3 hours, Closed-Book Exam with a candidate-prepared 8½×11" double-sided aid sheet. Any five (5) of the seven questions constitute a complete paper (100 marks); all seven are solved below for completeness.

Reference texts: Metcalf & Eddy (Tchobanoglous, Burton, Stensel), Wastewater Engineering: Treatment and Reuse, 4th ed.; Davis & Cornwell, Introduction to Environmental Engineering, 5th ed.; Turner, Workbook of Atmospheric Dispersion Estimates, 2nd ed.; Cooper & Alley, Air Pollution Control: A Design Approach, 4th ed.

Problem 7: Sources and Dispersion of Atmospheric Pollutants (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) Ground-level centerline NO₂ concentration at x = 1000 m

Given.

QuantityValue
Stack height, H50 m
Emission rate, Q100 g/s
Wind speed, u (at 10 m)4 m/s
Time / sky condition1 h before sunrise, thinly overcast, >4/8 cloud cover
Downwind distance, x1,000 m

Find. Ground-level centerline concentration C(x,0,0,H) at x=1,000 m, µg/m³.

Check — stability class and dispersion-coefficient source

Stability class. Per the exam's own wind-speed/insolation table, u=4 m/s falls in the "3–5 m/s" row; at night with >4/8 cloud cover that row gives Class D (the "<3/8 cloud" night column in the same row also gives D, so the choice is unambiguous regardless of exactly how "large cloud cover" is read).

Dispersion coefficients. Read from the exam's own Pasquill–Gifford σy/σz log-log charts (the standard Turner curves) on the Class D curve at x=1,000 m: σy≈68 m and σz≈33 m. Chart-reading tolerance is roughly ±2 m on σy and ±1 m on σz. As an analytic cross-check, the Briggs (1973) rural Class D fit to the same curves (x and σ in metres) is:

$$ \sigma_y = 0.08x(1+0.0001x)^{-1/2}, \qquad \sigma_z = 0.06x(1+0.0015x)^{-1/2} $$

Also assumed: the 10 m wind speed is used directly at stack height (no power-law height correction, the standard simplification for this exam series), and the emission rate is used as given (the 10 t/hr, 3% heavy-oil figures are flavour text — Q is already stated directly in g/s).

Approach. Evaluate the ground-level centerline Gaussian plume equation (y=0, z=0) with the Class D dispersion coefficients at x=1,000 m.

  1. Dispersion coefficients at x=1,000 m (exam charts, Class D).
    $$ \sigma_y \approx \boxed{68\ \text{m}}, \qquad \sigma_z \approx \boxed{33\ \text{m}} $$
  2. Ground-level centerline concentration.
    $$ C(x,0,0,H) = \frac{Q}{\pi\,u\,\sigma_y\,\sigma_z}\exp\!\left[-\frac{1}{2}\left(\frac{H}{\sigma_z}\right)^2\right] $$
    $$ C = \frac{100}{\pi\times4\times68\times33}\exp\!\left[-\frac{1}{2}\left(\frac{50}{33}\right)^2\right]\times10^6 $$
    $$ C = \boxed{1{,}125\ \mu\text{g/m}^3} $$

    Within the chart-reading tolerance the result lies between about 1,050 and 1,200 µg/m³.

  3. Cross-check with the Briggs rural Class D fit.
    $$ \sigma_y = 0.08(1000)(1.1)^{-1/2} = 76.28\ \text{m}, \qquad \sigma_z = 0.06(1000)(2.5)^{-1/2} = 37.95\ \text{m} $$
    $$ C = \frac{100}{\pi\times4\times76.28\times37.95}\exp\!\left[-\frac{1}{2}\left(\frac{50}{37.95}\right)^2\right]\times10^6 = 1{,}154\ \mu\text{g/m}^3 $$

    This agrees with the chart-based value to within 3%.

peak 1211 µg/m³ @ x=0.82 kmx=1.0 kmC=1154 µg/m³0.00.51.01.52.02.53.0downwind distance x (km)ground-level centerline C (µg/m³)
Fig. 1 — Ground-level centerline NO₂ concentration vs. downwind distance (Class D, u=4 m/s, H=50 m), drawn with the continuous Briggs fit to the Class D curves: the profile peaks at 1,211 µg/m³ near x=0.82 km; at the asked x=1.0 km the concentration has just started to fall from the peak (1,154 µg/m³ on this fit; 1,125 µg/m³ using the chart-read σ values).
QuantityValue
σy(1,000 m), Class D chart≈68 m
σz(1,000 m), Class D chart≈33 m
Ground-level centerline C at x=1,000 m≈1,125 µg/m³ (Briggs cross-check 1,154)
(context) Peak concentration (Briggs fit)1,211 µg/m³ at x≈820 m

Even at x=1 km, the predicted ground-level concentration (≈1,125 µg/m³) is very high relative to typical ambient NO₂ guidelines (on the order of a few hundred µg/m³ for a 1-hour average) — consistent with the large stated emission rate (100 g/s) and the stable Class D dispersion conditions, which disperse the plume relatively slowly compared to a daytime unstable atmosphere. This magnitude is exactly why part (ii) asks for engineering measures to reduce the ground-level impact.

(ii) Engineering measures to reduce ground-level NO₂ and carbon-footprint comparison

MeasureEffect on ground-level NO₂Carbon-footprint comparison
Increase effective stack heightRaises H, increasing σz at the point the plume reaches ground level and directly lowering C (C∝exp[−½(H/σz)²]) — does not reduce total mass emitted, only relocates and dilutes the ground-level impact farther downwind. Essentially carbon-neutral relative to baseline: no change in fuel burned or NO₂ mass emitted, so CO₂ footprint is unchanged; a taller stack has a small embodied-construction carbon cost but negligible operating-footprint impact.
Low-NOₓ combustion retrofit (staged combustion / flue-gas recirculation)Reduces the NO₂ emission rate Q at the source (lower peak flame temperature suppresses thermal-NOₓ formation), directly lowering C at every downwind distance in proportion to Q. Slightly increases the plant's own operating carbon footprint (marginal efficiency penalty from staged combustion can increase fuel burned per unit output by a small percentage), but this is a much smaller footprint cost than the emission-reduction benefit and is far lower-footprint than an add-on treatment system.
Selective catalytic reduction (SCR)Achieves the largest NOₓ removal (typically 80–95%) via post-combustion ammonia/urea injection over a catalyst, giving the biggest reduction in Q and hence C. Highest carbon-footprint cost of the three: manufacturing and transporting the ammonia/urea reagent has its own embodied carbon footprint, and the induced-draft fan pressure drop across the catalyst bed increases the plant's parasitic electrical load (and associated CO₂ if that electricity is not carbon-free).

The three measures form a clear trade-off: stack-height increase is carbon-neutral but does not cut total emissions (a dilution, not a reduction, strategy); combustion modification cuts emissions at the source for a small footprint penalty; and SCR achieves the deepest emission cut but carries the largest ancillary carbon cost, so the "best" choice from a whole-system carbon-footprint perspective depends on how much NOₓ reduction is actually required to meet the receptor-level standard.

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