Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-Chem-B2, Environmental Engineering — May 2016. 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 5: Atmospheric Dispersion of SO2 (20 marks)
(i) Ground-level centerline concentration vs. downwind distance
Given.
Quantity
Value
Emission rate, Q
20 g/min = 0.333 g/s
Stack (effective release) height, H
120 m
Wind speed, u
5 m/s
Insolation
Moderate solar radiation
Target ground-level concentration
< 2 µg/m³
Find. The downwind distance x beyond which the predicted ground-level centerline
concentration stays below 2 µg/m³.
Approach. Classify the Pasquill–Gifford stability class from wind speed +
insolation, read a/b/c/d/e/f from the supplied table, build σy(x) and σz(x), then evaluate the
ground-level (z=0) centerline (y=0) Gaussian-plume concentration
$C(x,0,0,H)=\dfrac{Q}{\pi u\sigma_y\sigma_z}\exp\!\left[-\dfrac{1}{2}\left(\dfrac{H}{\sigma_z}\right)^2\right]$
over the downwind distance and locate where it crosses the 2 µg/m³ line.
Stability class. Wind 5 m/s with moderate insolation classifies as Pasquill
Class C (“moderately unstable”) — exactly the case the exam table calls
out (“moderated unstable dispersion parameters”). From the table: a=120, b=1.0, c=−0.006,
d=70, e=1.0, f=0.05.
Dispersion coefficients. With x in km and σ in m, the ln term sits in the
exponent: $\sigma_y=120\,x^{\,1.0+0.006\ln x}$ and $\sigma_z=70\,x^{\,1.0-0.05\ln x}$. At x=1 km
(ln 1 = 0): σy = 120 m, σz = 70 m; at x=1.21 km: σy ≈ 145 m, σz ≈ 84.4 m
— consistent with published Pasquill–Gifford Class-C curves (σy≈120–150 m,
σz≈65–80 m at 1 km), confirming the parameter mapping.
Ground-level centerline concentration. Evaluating
$C(x)=\dfrac{Q}{\pi u\sigma_y(x)\sigma_z(x)}\exp\!\left[-\dfrac12\left(\dfrac{H}{\sigma_z(x)}\right)^2\right]$
across x=0.1–10 km (numerically, since σy,σz are transcendental in x) traces the usual
elevated-source shape: C(x) rises from 0 near the stack, peaks, then falls slowly at large x. See Fig. 5.
Locate the peak. The maximum occurs at
$$x_{max}\approx 1.21\ \text{km}, \qquad C_{max}\approx\boxed{0.63\ \mu\text{g/m}^3}$$
Compare to the 2 µg/m³ threshold. Because even the theoretical maximum
ground-level concentration (0.63 µg/m³, at x≈1.21 km) is already below 2 µg/m³,
the predicted concentration is below the 2 µg/m³ threshold at every downwind distance
x>0 — there is no finite crossing distance because the plume never reaches the limit in the
first place. (This conclusion is insensitive to the exact stability class chosen: repeating the calculation
for Classes A through E gives Cmax between 0.62 and 1.33 µg/m³, all below 2
µg/m³.)
Fig. 5 — Predicted ground-level centerline SO2 concentration vs. downwind
distance (Class C), against the 2 µg/m³ threshold.
Quantity
Value
Stability class
C (moderately unstable)
Peak location, xmax
≈1.21 km
Peak ground-level concentration, Cmax
≈0.63 µg/m³
Distance at which C < 2 µg/m³
All x > 0 (limit never reached)
Check: the stack's physical height (120 m) is used directly as the effective release
height H, since no exit velocity/temperature is given for a plume-rise correction — a real plume-rise
addition (Briggs) would only push the peak farther out and the concentration lower still, reinforcing the
conclusion.
(ii) Engineering measures to reduce ground-level SO2
Three measures, ranked from purely dispersive to source-reducing:
Increase effective stack height (taller stack, or higher exit velocity/temperature for
more plume rise). Lowers ground-level concentration near the source (Cmax∝1/H²
approximately) but does not reduce the total SO2 mass emitted — it relocates the impact farther
downwind and increases the source's contribution to regional/long-range transport and acid deposition.
“Dilution” solutions like this are the weakest long-term choice.
Flue-gas desulfurization (wet limestone scrubbing). Removes SO2 mass from the stack gas
before release (90–98% capture), directly cutting total loading everywhere, not just at ground level
near the stack. Produces a gypsum/scrubber-sludge by-product needing disposal or beneficial reuse, and has
the highest capital and O&M cost of the three.
Fuel switching / pre-combustion desulfurization (lower-sulfur natural gas blend, or
sulfur removal upstream). Reduces SO2 at the source with lower capital cost than FGD, but is constrained by
fuel supply/cost and does not achieve as deep a reduction as scrubbing for a high-sulfur feed.
Recommendation: flue-gas desulfurization (or fuel switching where fuel supply allows) is
preferred over stack-height dilution, because it reduces the total mass of SO2 released rather than merely
relocating where it lands — consistent with the pollution-prevention hierarchy (reduce at source before
disperse/dilute) and avoiding the regional acid-deposition liability a taller stack creates.