18-Env-A1 Principles of Environmental Engineering · May 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — May 2014 — 04-Env-A1 / Principles of Environmental Engineering. 3 hours duration; closed book with an 8.5×11 in double-sided aid sheet; Casio or Sharp approved calculator only. Any five questions constitute a complete paper (first five answers marked); all seven are solved below for completeness. Each question is worth 20 marks.
Reference texts. Davis & Cornwell, Introduction to Environmental Engineering (6th ed.); Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery (5th ed.); MWH’s Water Treatment: Principles and Design (3rd ed.); Guidelines for Canadian Drinking Water Quality (Health Canada); Canadian Council of Ministers of the Environment (CCME) water-quality guidelines; Canadian Environmental Protection Act, 1999 (CEPA); Andrews, Canadian Professional Engineering and Geoscience (professional ethics).
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.
| Method | Advantage | Limitation | Best Application |
|---|---|---|---|
| Activated-carbon adsorption (fixed source) | Very high removal efficiency for VOCs (benzene, acetone) at low-to-moderate concentration; recoverable solvent if regenerated | Carbon bed saturates and must be regenerated/replaced; poor performance at high humidity or high VOC loading | Solvent-use industries (printing, degreasing) with dilute, intermittent VOC streams |
| Thermal/catalytic oxidation (fixed source) | Near-complete destruction of VOCs (>95–99%) rather than transfer to another medium; catalytic version runs at lower temperature/fuel cost | Fuel-cost and $\text{NO}_x$ trade-off at high temperature; catalyst poisoning by particulates or certain compounds | Continuous, moderate-to-high-concentration VOC streams (paint-curing ovens, chemical process vents) |
| Baghouse fabric filtration / catalytic converters (fixed-source PM, mobile-source $PM_{2.5}$/CO/HC) | Very high $PM_{2.5}$ collection efficiency (baghouse, >99%); catalytic converters simultaneously cut CO, HC and $\text{NO}_x$ from vehicle exhaust | Baghouse: pressure-drop and bag-replacement maintenance; converter: requires unleaded fuel and proper operating temperature, does not address fine PM from brake/tire wear | Baghouse for fixed-source particulate (cement, metals processing); catalytic converters mandated on all light-duty mobile sources |
The three methods span the two broad control strategies engineers choose between: capture-and-destroy (thermal/catalytic oxidation, converting the toxic to $\text{CO}_2$/$\text{H}_2\text{O}$) versus capture-and-collect (adsorption, filtration, which concentrates the pollutant for disposal or recovery) — the choice is driven mainly by concentration, flow rate and whether the recovered material has value.
With only five years of remaining landfill capacity against a 25-year planning horizon, the plan cannot rely on landfilling alone and must combine waste reduction with new capacity and processing infrastructure, sequenced so that diversion measures reduce the tonnage that must ultimately be landfilled or processed at a new facility.
Each strategy is explicitly tied to a regulatory hook — provincial diversion targets, landfill design/liner standards, air-emission limits for waste-to-energy, and methane-reduction regulations — so that the plan is not just technically sound but demonstrably compliant with the environmental quality standards the local regulator will use to evaluate the new capacity.