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18-Env-A4 Water and Wastewater Engineering · December 2015

Question 3 of 5: Lagoon Treatment and the BOD Test

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

Notes on this paper

National Exams — December 2015 — 04-Env-A4 / Water and Wastewater Engineering. 3 hours duration; closed book with one double-sided aid sheet; approved calculator permitted. Question 1 is compulsory; the paper instructs candidates to attempt any three of the remaining four (100 marks total); all five are solved below for completeness. (The source page prints an internal header inconsistency — "NATIONAL EXAMINATION, MAY 2015" beside a page footer reading "December 2015" — the period is taken as December 2015 per the footer; this does not affect any question content.)

Reference texts. Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery; Davis & Cornwell, Introduction to Environmental Engineering; MWH's Water Treatment: Principles and Design; Guidelines for Canadian Drinking Water Quality (Health Canada).

Question 3: Lagoon Treatment and the BOD Test (25 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.

a. Facultative Lagoon BOD/Nutrient Removal vs. Aerated Lagoon (10 marks)

A facultative lagoon stratifies naturally into three zones: an aerobic surface layer, where photosynthetic algae generate oxygen during daylight that supports aerobic bacteria oxidizing soluble BOD; an anaerobic bottom sludge layer, where settled solids decompose anaerobically, releasing CO₂, methane and soluble by-products; and a facultative middle zone where bacteria switch between aerobic and anaerobic metabolism depending on locally available oxygen. BOD removal is driven by a symbiotic algal-bacterial relationship: bacteria oxidize organic matter to CO₂ and mineral nutrients, algae consume that CO₂ and those nutrients through photosynthesis and release O₂, which the bacteria then use — a self-sustaining oxygen supply that needs no mechanical aeration, sustained over a long hydraulic retention time (commonly 20–180 days) that allows extensive biological stabilization. Nutrient removal is more limited: nitrogen is reduced mainly through algal biomass uptake and through ammonia volatilization at the elevated pH that algal CO₂ consumption drives, while phosphorus is removed only modestly, through algal uptake and some precipitation at high pH.

An aerated lagoon instead supplies oxygen mechanically (surface or diffused aeration) throughout the full water depth, eliminating dependence on sunlight/photosynthesis and permitting a much shorter retention time (typically 3–10 days) and greater depth (up to 4–6 m, versus 1–2.5 m for a facultative lagoon). Because mixing and oxygenation are mechanical, an aerated lagoon behaves as a complete-mix suspended-growth reactor — conceptually close to an extended-aeration activated-sludge process without solids recycle — whereas the facultative lagoon relies on quiescent gravity settling and a stratified, largely passive biology. The trade-off is that aerated lagoons need continuous electrical power and mechanical equipment (higher energy and O&M cost) but occupy a smaller footprint and deliver more consistent year-round effluent than a facultative lagoon, whose performance tracks seasonal light and temperature (ice cover and reduced algal photosynthesis noticeably degrade winter performance).

b. BOD Test — 4-Day, 5-Day and Ultimate BOD (15 marks)

01234567890100200300400Time, t (days)Oxygen demand exerted, BOD_t (mg/L)BOD_u = 459 mg/LBOD4 = 276.4BOD5 = 314.0
First-order BOD exertion curve, $\text{BOD}_t=\text{BOD}_u(1-10^{-k_1t})$ with the assumed $k_1=0.10\ \text{d}^{-1}$, showing the measured 4-day point and the derived 5-day point on the same curve.

Given.

Given data
QuantitySymbolValue
Sample volume$V_s$5 mL
Total (diluted) bottle volume$V_b$300 mL
Initial DO$DO_i$9.0 mg/L
DO after 4 days incubation at 20°C$DO_f$4.3 mg/L
Fraction of depletion attributed to seed—2%
Check: the paper says "over this 3 day period" immediately after stating the sample was incubated for 4 days — the "3 day" phrase is treated as a typo for the 4-day period actually run here. The seed correction is therefore applied to the full 4-day depletion. Separately, the exam supplies no deoxygenation rate constant $k_1$; a typical base-10 rate constant for raw domestic sewage at 20°C, $k_1=0.10\ \text{day}^{-1}$ (Metcalf & Eddy / Davis & Cornwell typical range 0.05–0.30 day⁻¹), is assumed and stated explicitly.

Find. The 4-day BOD ($\text{BOD}_4$), 5-day BOD ($\text{BOD}_5$) and ultimate BOD ($\text{BOD}_u$) of the undiluted sewage sample.

Approach. Compute the dilution fraction, correct the observed DO depletion for the seed's own contribution, scale by the dilution fraction to get $\text{BOD}_4$ of the undiluted sample, then use the assumed first-order BOD-exertion model to back out $\text{BOD}_u$ and forward-compute $\text{BOD}_5$.

  1. Dilution fraction. $$P=\frac{V_s}{V_b}=\frac{5}{300}=0.01667.$$
  2. Seed-corrected oxygen depletion in the bottle. Observed depletion $=DO_i-DO_f=9.0-4.3=4.7$ mg/L; with 2% of this attributed to the seed, the sewage's own depletion is $4.7\times(1-0.02)=4.606$ mg/L.
  3. 4-day BOD of the undiluted sample. Dividing by the dilution fraction scales the bottle reading up to the full-strength sample: $$\text{BOD}_4=\frac{4.606}{0.01667}=\boxed{276.4\ \text{mg/L}}.$$
  4. Ultimate BOD from the assumed rate constant. With $k_1=0.10\ \text{day}^{-1}$ (base-10) and $\text{BOD}_t=\text{BOD}_u(1-10^{-k_1t})$, at $t=4$: $1-10^{-0.40}=0.6019$, so $$\text{BOD}_u=\frac{276.4}{0.6019}=\boxed{459.2\ \text{mg/L}}.$$
  5. 5-day BOD. Applying the same curve at $t=5$: $1-10^{-0.50}=0.6838$, so $$\text{BOD}_5=459.2\times0.6838=\boxed{314.0\ \text{mg/L}}.$$
QuantityResult
Dilution fraction $P$0.01667
4-day BOD, $\text{BOD}_4$276.4 mg/L
5-day BOD, $\text{BOD}_5$314.0 mg/L
Ultimate BOD, $\text{BOD}_u$459.2 mg/L