---
title: "Degree of treatment, industrial wastewater"
subject: "Sanitary Engineering"
chapter: 6
key: "semester_6/sanitary_engineering:degree-treatment-industrial-waste"
source: https://www.bctengineer.com/q/semester_6/sanitary_engineering/degree-treatment-industrial-waste
site: BCT Engineering
---

# Degree of treatment, industrial wastewater

Sanitary Engineering · Chapter 6: Wastewater Disposal

- Asked in: 2074 Bhadra, 8 marks
- Answer checked by Claude Opus 5.5 (high effort) on 2026-10-14
- Page: https://www.bctengineer.com/q/semester_6/sanitary_engineering/degree-treatment-industrial-waste
- Whole chapter: https://www.bctengineer.com/md/semester_6/sanitary_engineering/chapter-6

## Question

You are assigned by an industry as a Sanitary Engineer to recommend the degree of treatment required for their industrial waste water. The effluent from the treatment plant is to be discharged into a river with a minimum flow of 5000 lps, a dissolved oxygen content of 7.4 mg/l and BOD of zero. In order to thrive aquatic life, it is necessary to maintain a minimum DO content of 4 mg/l in the river. A sanitary survey reveals the characteristics of industrial waste water as follows: Discharge = 2*10⁶ l/day; BOD = 5000 mg/l; DO = 0. Recommend the degree of treatment required for the plant. Assume saturation DO of 9.2 mg/l in the river after mixing with wastewater. It is equal to DO content of river before mixing. Assume any other appropriate data if required.

## Short answer

Using Streeter-Phelps with base-10 constants (K=0.1, R=0.4), the permissible mixture ultimate BOD is 30.93 mg/l. After mixing with river (5 m³/s), the effluent BOD5 must be reduced from 5000 mg/l to 4589 mg/l, requiring 8.2% BOD removal.

## Answer

Convert flows to m³/s: $Q_s = 2\times 10^6/(86400\times 1000) = 0.0231$ m³/s and $Q_r = 5.0$ m³/s. The river is at about 20°C, so I assume the standard constants $K=0.1$/day and $R=0.4$/day (base 10), $f=4$. Saturation DO after mixing is 9.2 mg/l, and the minimum DO to be kept is 4 mg/l.
#### Step 1: Mixing and permissible deficit

$$
\begin{aligned}
DO_{mix} &= \frac{0.0231\times 0 + 5.0\times 7.4}{5.023} = 7.37\ \text{mg/l}\\
D_0 &= DO_{sat}-DO_{mix} = 9.2-7.37 = 1.83\ \text{mg/l}\\
D_{c(allowed)} &= DO_{sat}-DO_{min} = 9.2-4.0 = 5.20\ \text{mg/l}
\end{aligned}
$$

#### Step 2: Permissible BOD of the mixture

With $K=0.1$ and $R=0.4$ (base 10), $f=R/K=4.00$. The critical deficit is

$$
t_c=\frac{1}{K(f-1)}\log_{10}\left[f\left\{1-(f-1)\frac{D_0}{L_m}\right\}\right],\qquad D_c = \frac{L_m}{f}10^{-Kt_c}
$$

and $D_c$ must not exceed 5.20 mg/l. Solving these two equations for $L_m$ by trial (with $D_0=1.83$ fixed) gives $L_m=30.93$ mg/l, with $t_c=1.723$ days (check: $D_c=5.20$ mg/l).

#### Step 3: Permissible BOD of the effluent

$$
\begin{aligned}
L_{raw} &= \frac{BOD_5}{1-10^{-5K}} = \frac{5000}{0.6838} = 7312.38\ \text{mg/l}\\
L_r &= 0.00\ \text{mg/l (river)}\\
L_s &= \frac{L_m(Q_s+Q_r)-Q_rL_r}{Q_s} = \frac{30.93\times 5.023 - 5.0\times 0.00}{0.0231} = 6712.02\ \text{mg/l}
\end{aligned}
$$

So the treated effluent can have $BOD_5 \approx 4589.49$ mg/l.

$$
\text{Degree of treatment} = \frac{7312.38-6712.02}{7312.38}\times 100 = 8.2\%
$$
**Answer: the effluent BOD5 must be brought from 5000 mg/l down to about 4589.49 mg/l, i.e. about 8.2% treatment (BOD removal) is required.** The required degree is small only because the river dilution is very large (5 m³/s against 0.023 m³/s of waste); if the river flow were lower, much higher treatment would be needed.

## Check yourself

The answer's key points as multiple-choice questions, with the correct option and why.

1. What is the waste flow in m3/s for 2 x 10^6 l/day?
   A. 2.31 m3/s
   B. 0.0231 m3/s
   C. 23.1 m3/s
   D. 0.231 m3/s
   Answer: B. 2 x 10^6 l/day = 2000 m3/day = 0.0231 m3/s. (Key point: Flow conversion)

2. Why is only about 8.2% treatment needed despite BOD of 5000 mg/L?
   A. The BOD is low
   B. The river DO is zero
   C. The waste has high DO
   D. The river flow is very large compared with the waste flow
   Answer: D. Dilution by 5 m3/s against 0.023 m3/s makes the mixture BOD small; a lower river flow would need much more treatment. (Key point: Small treatment)

3. What is the maximum deficit allowed?
   A. 9.2 - 4 = 5.2 mg/L
   B. 4 mg/L
   C. 9.2 mg/L
   D. 1.83 mg/L
   Answer: A. The DO must stay at least 4 mg/L, so Dc max = saturation - 4. (Key point: Allowable deficit)

## Related in Sanitary Engineering

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- [Degree of treatment, domestic + industrial](https://www.bctengineer.com/question.md?key=semester_6%2Fsanitary_engineering%3Adegree-treatment-town-40000) — Sanitary Engineering, chapter 6
- [Is treatment necessary? Industry near river](https://www.bctengineer.com/question.md?key=semester_6%2Fsanitary_engineering%3Atreatment-industry-river-1p72) — Sanitary Engineering, chapter 6
- [Degree of treatment, city 1200 l/s](https://www.bctengineer.com/question.md?key=semester_6%2Fsanitary_engineering%3Adegree-treatment-city-1200ls) — Sanitary Engineering, chapter 6
- [River flow required for 1500 population](https://www.bctengineer.com/question.md?key=semester_6%2Fsanitary_engineering%3Ariver-flow-for-1500-population) — Sanitary Engineering, chapter 6
- [Is treatment necessary? Town wastewater 300 l/s](https://www.bctengineer.com/question.md?key=semester_6%2Fsanitary_engineering%3Atreatment-needed-town-300-ls) — Sanitary Engineering, chapter 6

## Related in other subjects

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- [Dissolved oxygen by titrimetric method](https://www.bctengineer.com/question.md?key=semester_5%2Fwater_supply_engineering%3Adissolved-oxygen-titrimetric) — Water Supply Engineering, chapter 4
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