18-Env-A4 Water and Wastewater Engineering · May 2017
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — May 2017 — 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 questions — all five are solved below for completeness.
Reference texts. Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery (5th ed.) — oxygen sag/Streeter-Phelps, MLSS/MLVSS, population equivalent, primary clarifier design; Davis & Cornwell, Introduction to Environmental Engineering (6th ed.) — turbidity, alkalinity chemistry; MWH’s Water Treatment: Principles and Design (3rd ed.) — coagulation-flocculation, softening, disinfection by-products, pH; Guidelines for Canadian Drinking Water Quality (Health Canada).
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.
pH is the negative base-10 logarithm of the hydrogen-ion activity, $pH = -\log_{10}[H^+]$, giving a 0–14 scale on which 7 is neutral (pure water at 25 °C), values below 7 acidic and above 7 alkaline. In water treatment pH governs two process-critical equilibria addressed directly by this exam.
Disinfection. Free chlorine in water exists as an equilibrium between hypochlorous acid (HOCl) and the hypochlorite ion (OCl−), $HOCl \rightleftharpoons H^+ + OCl^-$, with a pKa near 7.5. HOCl, the dominant species below pH ≈7.5, is roughly 80–100 times more effective a biocide than OCl− because its neutral charge lets it penetrate microbial cell walls far more readily. Raising pH shifts the equilibrium toward the far weaker OCl−, so a plant must either hold pH low during chlorine contact or dose substantially more chlorine (and provide longer contact time, i.e. a larger CT) to achieve the same log-inactivation at higher pH.
Coagulation-flocculation. Hydrolyzing metal coagulants (alum, ferric chloride) only form the insoluble, positively-charged hydroxide precipitates responsible for charge neutralization and sweep-floc capture within a narrow optimum pH band — roughly 5.5–7.5 for alum, a wider 4–11 for ferric salts. Outside that window the metal hydroxide either fails to precipitate (stays soluble, no floc forms) or, at high pH, redissolves as an anionic aluminate/ferrate, so pH control (often with lime, soda ash, or CO2) directly ahead of rapid mix is essential to reliable turbidity removal.
Given.
| Quantity | Symbol | Value |
|---|---|---|
| Sample volume | $V_s$ | 50 mL |
| Titrant normality | $N$ | 0.02 N H2SO4 |
| Volume to phenolphthalein end point (pH 8.3) | $V_P$ | 5 mL |
| Volume to Bromocresol Green end point (pH 4.5, cumulative) | $V_T$ | 8 mL |
Find. The alkalinity indicated by each end point, its numerical value, and any further alkalinity species (hydroxide/carbonate/bicarbonate) recoverable from the two readings.
Approach. Convert each titrant volume to an alkalinity as mg/L CaCO3, then apply the standard phenolphthalein/total alkalinity relationships (Sawyer & McCarty) to split the total into its hydroxide, carbonate and bicarbonate components.
| Quantity | Value |
|---|---|
| Phenolphthalein alkalinity, $P$ | 100 mg/L as CaCO3 |
| Total alkalinity, $T$ | 160 mg/L as CaCO3 |
| Hydroxide alkalinity, $OH^-$ | 40 mg/L as CaCO3 |
| Carbonate alkalinity, $CO_3^{2-}$ | 120 mg/L as CaCO3 |
| Bicarbonate alkalinity, $HCO_3^-$ | 0 mg/L as CaCO3 |