22-Agric-B11 Principles of Waste Management · December 2017
Question 5 of 5: Dissolved Oxygen Sag Below a Meat-Processing Discharge
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — 04-Agric-B11, Principles of Waste Management — December 2017. 3-hour duration, open-book exam. Answer Question 1 plus any three of Questions 2 to 5; all five questions are answered below as a complete study resource.
Reference texts: Tchobanoglous, Burton & Stensel, Metcalf & Eddy Wastewater Engineering: Treatment and Resource Recovery; MWPS-18, Livestock Waste Facilities Handbook (MidWest Plan Service); Rynk et al., On-Farm Composting Handbook (NRAES-54); Sommer & Christensen (eds.), Animal Manure Recycling: Treatment and Management; Haug, The Practical Handbook of Compost Engineering; White, Fluid Mechanics.
Question 5: Dissolved Oxygen Sag Below a Meat-Processing Discharge (25 marks)
Q = 10 m³/h, BOD5 = 50 mg/L, DO = 2 mg/L, T = 15 °C
Upstream river
Q = 50 m³/h, BOD5 = 3 mg/L, DO = 7 mg/L, T = 10 °C
Deoxygenation rate, k1 (base-10, 20 °C)
0.15 d-1 (θ1 = 1.135)
Reaeration rate, k2 (base-10, 20 °C)
0.28 d-1 (θ2 = 1.056)
Saturated DO after mixing
9.2 mg/L
Regulatory DO limit
6.0 mg/L
Find. Whether the minimum downstream dissolved oxygen falls below the 6.0 mg/L regulatory limit.
Streeter-Phelps DO sag curve downstream of the mixing point; the critical (minimum) point stays just above the 6.0 mg/L regulatory limit.
Approach. Mix the effluent and river flows to get the blended BOD5, DO and temperature at the discharge point, correct the rate constants to that stream temperature, convert BOD5 to ultimate BOD using the standard 20 °C lab-test rate constant, then apply the Streeter-Phelps critical-deficit solution to find the minimum downstream DO and compare it to the 6.0 mg/L limit.
Temperature-corrected rate constants. Correcting $k_1,k_2$ from 20 °C to the mixed stream temperature via $k_T = k_{20}\,\theta^{T-20}$: $$k_{1,T}=0.15(1.135)^{10.8-20}=\boxed{0.047\ \text{d}^{-1}},\qquad k_{2,T}=0.28(1.056)^{10.8-20}=\boxed{0.170\ \text{d}^{-1}}$$
Ultimate BOD (L0). The BOD5-to-ultimate-BOD conversion uses $k_1$ at the standard 20 °C BOD-bottle test condition (not the temperature-corrected river rate, which governs decay IN the river, not the lab test itself): $$L_0 = \frac{BOD_{mix}}{1-10^{-k_{1,20}(5)}} = \frac{10.8}{1-10^{-0.75}} = \boxed{13.2\ \text{mg/L}}$$
Initial deficit and critical point. $D_0 = DO_{sat}-DO_{mix}=9.2-6.17=3.03\ \text{mg/L}$. Since $k_1,k_2$ are explicitly base-10 constants here, the deficit curve is $D(t)=A(10^{-k_{1,T}t}-10^{-k_{2,T}t})+D_0\,10^{-k_{2,T}t}$ with $A=k_{1,T}L_0/(k_{2,T}-k_{1,T})$, and setting $dD/dt=0$ (using $\log_{10}$, consistent with the base-10 exponent — NOT the natural-log form used for base-e rate constants) gives the time to the critical (minimum-DO) point: $$t_c=\frac{1}{k_{2,T}-k_{1,T}}\log_{10}\!\left[\frac{(A-D_0)\,k_{2,T}}{A\,k_{1,T}}\right] = \boxed{1.28\ \text{d}}$$ and the critical deficit is $$D_c = \frac{k_{1,T}}{k_{2,T}}L_0\,10^{-k_{1,T}t_c} = \boxed{3.17\ \text{mg/L}}$$
Minimum downstream DO and compliance check. $$DO_{min} = DO_{sat}-D_c = 9.2-3.17 = \boxed{6.03\ \text{mg/L}}$$ 6.03 mg/L stays above the 6.0 mg/L regulatory limit, but only just — the margin is a mere 0.03 mg/L, occurring about 1.3 days (equivalently, at a river velocity of, say, 0.3 m/s, roughly 33 km) downstream of the discharge. The dissolved oxygen does NOT fall below the regulatory limit, but the result is essentially right at the boundary: within the precision of the given rate constants and temperature-correction factors, this discharge should be treated as marginal rather than comfortably compliant, and any small increase in effluent BOD or drop in reaeration capacity would push it into violation.
Quantity
Result
Mixed BOD5 / DO / T
10.8 mg/L / 6.17 mg/L / 10.8 °C
Ultimate BOD, L0
13.2 mg/L
Time to critical deficit, tc
1.28 days
Critical deficit, Dc
3.17 mg/L
Minimum downstream DO
6.03 mg/L — stays above the 6.0 mg/L limit, but only marginally