16-Civ-B5 Water Supply and Wastewater Treatment · May 2013
Question 3 of 5: Effluent phosphorus limit from receiving-water assimilative capacity
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Examination, May 2013 — 98-Civ-B5 Water Supply and Wastewater Treatment. Three hours, closed book, one aid sheet written on both sides, approved calculator permitted. Question 1 is compulsory and the candidate attempts any three of the remaining four; every question carries 25 marks, so the examinable total is 4 × 25 = 100 marks. Page-1 Note 2 invites the candidate to submit a clear statement of any assumption made where a question is open to interpretation, and Note 6 makes clarity and organisation part of the mark. All five questions are solved here, because this set is a study resource rather than a timed sitting.
Reference texts. Metcalf & Eddy | AECOM, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (wastewater characterisation, primary sedimentation, attached-growth processes); J. C. Crittenden et al., MWHʹs Water Treatment: Principles and Design, 3rd ed. (coagulation, flocculation, settling theory); M. L. Davis & D. A. Cornwell, Introduction to Environmental Engineering, 5th ed. (water-quality parameters, unit operations); J. R. Mihelcic & J. B. Zimmerman, Environmental Engineering: Fundamentals, Sustainability, Design, 3rd ed. (mass balances on receiving waters); Health Canada, Guidelines for Canadian Drinking Water Quality (GCDWQ) and CCME, Canadian Environmental Quality Guidelines (CEQG) for the Canadian regulatory frame; Wastewater Systems Effluent Regulations, SOR/2012-139 (WSER) for national effluent limits.
Check — conventions used throughout this paper. Concentrations in mg/L are treated as g/m3 throughout, which is exact for dilute aqueous solutions and is what makes the load arithmetic in Questions 3 and 4 one-line conversions. Wastewater flows quoted as m3/d are converted to m3/s with 86 400 s/d and are taken as steady average-day values, since the paper gives no peaking factor. Where a Canadian regulatory number is quoted (WSER, GCDWQ, CEQG) it is named at the point of use; the exam itself sets no jurisdiction, and none of the numerical answers depends on the citation.
Given. The discharge and the receiving water are fully specified by five numbers, collected below.
Given data — Question 3
Quantity
Symbol
Value
Wastewater treatment plant flow
Qe
10 000 m3/d
River flow upstream of the outfall
Qr
5.79 m3/s
Current effluent TP limit
Ce
1.0 mg TP/L
Background TP upstream of the outfall
Cup
0.01 mg/L
TP the river can assimilate
Cassim
0.02 mg/L
Find. Whether the existing 1.0 mg/L effluent limit protects the river against the 0.02 mg/L assimilative ceiling, and if it does not, the numerical effluent limit that would, together with the size of the required tightening.
Figure 3.1. Mixing-zone control volume at the outfall. Total phosphorus is conservative over this reach, so the mass entering with the river and with the effluent must equal the mass leaving in the fully mixed downstream flow.
Approach. Treat the mixing zone as a steady-state, conservative, completely mixed control volume around the outfall: write a total-phosphorus mass balance on it, evaluate the downstream concentration produced by the current limit, compare that with the assimilative ceiling, and then invert the same balance to find the effluent concentration that lands exactly on the ceiling.
Put the two flows into the same units. The plant flow is quoted per day and the river flow per second, and nothing can be compared until they agree:
$$Q_e = \frac{10\,000\ \text{m}^3/\text{d}}{86\,400\ \text{s}/\text{d}} = 0.1157\ \text{m}^3/\text{s}$$
against a river flow of Qr = 5.79 m3/s. The dilution available is therefore Qr/Qe = 50.0, or almost exactly fifty parts of river to one part of effluent. That single number already tells us what to expect: a 1.0 mg/L effluent diluted fifty-fold contributes about 0.02 mg/L on its own, which is the entire assimilative ceiling before the background is even counted.
Write the mass balance across the mixing zone. Total phosphorus is conservative over the short reach of a mixing zone — it is neither created nor destroyed, only redistributed between dissolved and particulate forms — so at steady state the mass entering equals the mass leaving:
$$Q_r C_{up} + Q_e C_e = (Q_r + Q_e)\,C_{mix}$$
which rearranges to give the fully mixed downstream concentration:
$$C_{mix} = \frac{Q_r C_{up} + Q_e C_e}{Q_r + Q_e}$$
Evaluate the downstream concentration produced by the current limit. Substituting the given values with Ce = 1.0 mg/L:
$$C_{mix} = \frac{(5.79)(0.01) + (0.1157)(1.0)}{5.79 + 0.1157} = \frac{0.05790 + 0.11574}{5.9057}$$
$$\boxed{C_{mix} = 0.0294\ \text{mg TP/L}}$$
The river can assimilate 0.02 mg/L. A plant discharging at exactly its permitted limit therefore drives the receiving water to 0.0294 mg/L — about 1.47 times the concentration the study identifies as the threshold for deterioration of water quality and aquatic life.
Comment on the current limit. The finding condemns it. The existing 1.0 mg TP/L limit is not protective of the receiving environment: a plant in full compliance with its permit would still push the river 47 % past its assimilative capacity, and the exceedance is not marginal or dependent on a modelling refinement. Note also what has been assumed in the plantʹs favour — complete and instantaneous mixing, no upstream sources other than the stated background, and a river flow of 5.79 m3/s that is treated as always available. Relaxing any of those assumptions makes the picture worse, not better. The limit must be tightened.
Invert the balance for the protective effluent limit. Setting Cmix equal to the assimilative ceiling of 0.02 mg/L and solving the same equation for Ce:
$$C_{e,\text{new}} = \frac{C_{assim}(Q_r + Q_e) - Q_r C_{up}}{Q_e} = \frac{(0.02)(5.9057) - (5.79)(0.01)}{0.1157}$$
$$C_{e,\text{new}} = \frac{0.11811 - 0.05790}{0.1157} \quad\Longrightarrow\quad \boxed{C_{e,\text{new}} = 0.520\ \text{mg TP/L}}$$
Substituting 0.520 mg/L back into the balance returns Cmix = 0.0200 mg/L exactly, which confirms the inversion.
State the required change in the two forms a regulator uses. As a concentration, the limit must fall from 1.0 to 0.520 mg TP/L — a tightening of 0.480 mg/L, or 48 % of the present limit. As a mass load, which is how a discharge permit is more usefully written because it cannot be met by dilution:
$$L = C_e \times Q_e \;\Rightarrow\; L_{\text{now}} = 10.0\ \text{kg TP/d}, \qquad L_{\text{new}} = 5.20\ \text{kg TP/d}$$
so the permitted phosphorus load must be cut by 4.80 kg/d, slightly more than half.
Cross-check against the riverʹs headroom. An independent route to the same answer confirms it. The river downstream carries (Qr + Qe) = 5.906 m3/s, or 510 256 m3/d, and may rise from 0.01 to 0.02 mg/L — a headroom of 0.01 g/m3, which is 5.10 kg TP/d. Adding back the phosphorus the effluent flow would carry even at background concentration, 0.01 g/m3 × 10 000 m3/d = 0.10 kg/d, gives 5.20 kg/d — identical to the limit load computed in Step 6.
Final results — Question 3
Quantity
Value
Effluent flow in consistent units
0.1157 m3/s (dilution 50:1)
Downstream TP at the current 1.0 mg/L limit
0.0294 mg/L
Assimilative ceiling
0.020 mg/L — exceeded by 47 %
Verdict on the current limit
Not protective; must be tightened
Protective effluent TP limit
0.520 mg TP/L
Required tightening
0.480 mg/L, i.e. 48 % of the present limit
Permitted TP load, present → required
10.0 → 5.20 kg TP/d (a cut of 4.80 kg/d)
Check — engineering assumptions behind the 0.520 mg/L figure. Three assumptions are implicit in the calculation and would be stated in an answer paper under page-1 Note 2. First, complete and instantaneous mixing at the outfall: a real plume needs a mixing length, and concentrations within it exceed the fully mixed value, so a regulator would normally define a mixing-zone boundary and could impose a stricter limit than 0.520 mg/L. Second, a river flow of 5.79 m3/s that is treated as always available; assimilative-capacity limits in Canadian practice are set at a low-flow design condition such as the 7Q10 (the seven-day average low flow with a ten-year return period), and because the required effluent concentration is very nearly proportional to river flow, a design low flow of half the stated value would roughly halve the allowable limit again. Third, that total phosphorus behaves conservatively over the mixing zone, which is appropriate for a short reach but conservative for a long one. All three point the same way, so 0.520 mg TP/L should be read as the least stringent defensible limit, not as a target. For context, 0.5 mg/L is a routine chemical-phosphorus-removal target for a conventional plant, whereas going below about 0.1 mg/L requires tertiary filtration.