18-Env-A4 Water and Wastewater Engineering · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — December 2014 — 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.
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 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 defined as the negative base-10 logarithm of the hydrogen-ion activity, $\text{pH}=-\log_{10}[\text{H}^+]$, giving a dimensionless 0–14 scale (7 neutral at 25°C) that describes how acidic or basic water is at the instant of measurement. Its significance to disinfection is direct and large: chlorine's active disinfecting species, hypochlorous acid (HOCl), is in a pH-dependent equilibrium with the far weaker hypochlorite ion, $\text{HOCl}\rightleftharpoons\text{H}^++\text{OCl}^-$ (pKℎ ≈ 7.5); HOCl is roughly 80–100 times more effective a disinfectant than OCl⁻, so as pH rises from 6.5 toward 8.5 the fraction present as HOCl falls sharply and required CT (or chlorine dose) for the same log-inactivation rises correspondingly — plants therefore typically chlorinate in the pH 6.5–7.5 range for efficiency. pH is equally critical to coagulation-flocculation: metal coagulants (alum, ferric chloride/sulfate) only hydrolyze to insoluble, positively-charged metal-hydroxide flocs within a defined optimum pH band (roughly 5.5–7.5 for aluminum, 5–8.5 for ferric); outside that band the coagulant remains soluble or redissolves, colloidal charge neutralization fails, and turbidity/NOM removal collapses. Because both processes have narrow, different, and downstream-linked pH optima, treatment plants routinely dose lime, soda ash, CO₂ or acid to bring the water into the coagulation window first and re-adjust before final chlorination.
The phenolphthalein end point (pH 8.3) marks the point where all hydroxide has been neutralized and carbonate has been converted only halfway, to bicarbonate ($\text{CO}_3^{2-}+\text{H}^+\rightarrow\text{HCO}_3^-$); the acid volume to this point defines the phenolphthalein alkalinity, P. Continuing the same titration to the Bromocresol Green end point (pH 4.5) neutralizes all remaining bicarbonate (both the original bicarbonate and that just formed from carbonate); the total acid volume to this point defines the total alkalinity, T. Comparing P against T/2 (the standard Sawyer & McCarty classification) then reveals which of hydroxide, carbonate and bicarbonate alkalinity are actually present — this is the "other type of alkalinity" the question is asking for beyond the two directly-titrated numbers.
Given.
| Quantity | Symbol | Value |
|---|---|---|
| Sample volume | $V_s$ | 50 mL |
| Acid normality | $N$ | 0.02 eq/L (0.02N H₂SO₄) |
| Acid volume to phenolphthalein end point (pH 8.3) | $V_P$ | 5 mL |
| Acid volume to Bromocresol Green end point (pH 4.5), cumulative from start | $V_T$ | 8 mL |
Find. The type and value of alkalinity indicated by each end point, and any additional alkalinity component(s) that can be derived from the two titration volumes.
Approach. Convert each titration volume to an alkalinity in mg/L as CaCO₃ using the standard normality relation, then apply the Sawyer & McCarty P-vs-T/2 classification to split the total alkalinity into its hydroxide, carbonate and bicarbonate components.
| Quantity | Value |
|---|---|
| Phenolphthalein alkalinity, P (indicates OH⁻ + ½ CO₃²⁻) | 100 mg/L as CaCO₃ |
| Total alkalinity, T (indicates OH⁻ + CO₃²⁻ + HCO₃⁻) | 160 mg/L as CaCO₃ |
| Hydroxide alkalinity, OH⁻ (derived from P and T) | 40 mg/L as CaCO₃ |
| Carbonate alkalinity, CO₃²⁻ (derived from P and T) | 120 mg/L as CaCO₃ |
| Bicarbonate alkalinity, HCO₃⁻ | 0 mg/L as CaCO₃ |