18-Env-A4 Water and Wastewater Engineering · May 2018
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — May 2018 — 04-Env-A4 / Water and Wastewater Engineering. 3 hours duration; closed book with one double-sided aid sheet; approved Casio/Sharp 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.) — population equivalent, oxygen sag/Streeter–Phelps, activated-sludge process control (RAS/WAS, HRT/SRT), secondary clarifier design; Davis & Cornwell, Introduction to Environmental Engineering (6th ed.) — turbidity, alkalinity chemistry, digester fundamentals; MWH’s Water Treatment: Principles and Design (3rd ed.) — coagulation-flocculation mechanisms, ozonation, disinfection by-products, pH.
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 hydrogen-ion activity, $pH=-\log_{10}[H^+]$, giving the familiar 0–14 scale on which 7 is neutral (pure water at 25 °C), values below 7 acidic and above 7 alkaline. Two process-critical equilibria in water treatment depend directly on it.
Disinfection. Aqueous free chlorine exists in equilibrium between hypochlorous acid and the hypochlorite ion, $HOCl \rightleftharpoons H^+ + OCl^-$, with a pKa near 7.5. The neutral, uncharged HOCl species — dominant below pH ≈7.5 — diffuses through microbial cell walls roughly 80–100 times faster than the charged OCl− ion and is correspondingly the far more effective biocide, so raising pH weakens chlorine disinfection unless dose and contact time (CT) are increased to compensate.
Coagulation-flocculation. Hydrolyzing metal coagulants only precipitate as the insoluble, positively-charged hydroxide flocs responsible for charge neutralization and sweep coagulation within a narrow optimum pH window — roughly 5.5–7.5 for alum, a somewhat wider 4–11 for ferric salts. Below or above that window the metal either stays in soluble form (no floc) or, at high pH, redissolves as an anionic aluminate/ferrate, so pH adjustment (lime, soda ash, or CO2/acid) immediately ahead of rapid mix is essential to reliable turbidity removal, exactly as described in Question 2.
Given.
| Quantity | Symbol | Value |
|---|---|---|
| Sample volume | $V_s$ | 20 mL |
| Titrant normality | $N$ | 0.02 N H2SO4 |
| Volume to phenolphthalein end point (pH 8.3) | $V_P$ | 4 mL |
| Volume to Bromocresol Green end point (pH 4.5, cumulative) | $V_T$ | 6 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 cumulative 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, $P$ | 200 mg/L as CaCO3 |
| Total alkalinity, $T$ | 300 mg/L as CaCO3 |
| Hydroxide alkalinity, $OH^-$ | 100 mg/L as CaCO3 |
| Carbonate alkalinity, $CO_3^{2-}$ | 200 mg/L as CaCO3 |
| Bicarbonate alkalinity, $HCO_3^-$ | 0 mg/L as CaCO3 |