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16-Civ-A3 Elementary Environmental Engineering · May 2018

Question 1 of 7: Air Pollution Control and Water Treatment

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format. National Exams, May 2018 — 16-Civ-A3 Elementary Environmental Engineering. Three hours; closed book with one candidate-prepared 8½ × 11 double-sided aid sheet; approved Casio or Sharp calculator only. Seven problems are printed, each worth 20 marks, and any five constitute a complete paper (maximum 100 marks). All seven are solved here, because the set is intended as a study resource rather than an exam script. Section marks are shown in brackets at the left margin of each question and are reproduced from the final-page Marking Scheme.

Reference texts.

Check: Problem 4(ii) quotes a rate constant as “20 dm6/mol2” with no time unit, and states the fundamental reaction 2A + B ⇌ C. It is solved as a forward-rate second-in-A/first-in-B rate law with $k=20\ \text{dm}^{6}\,\text{mol}^{-2}\,\text{s}^{-1}$ (the only reading that makes $-r_A=k\,C_A^{2}C_B$ dimensionally a rate); the time unit is taken as seconds per NOTE 1. Because no feed flow rate is supplied, the well-posed deliverable is the flow-independent space-time $\tau$ (with $V=\tau\,v_0$ for any stated feed basis), not an absolute volume.

Question 1: Air Pollution Control and Water Treatment (20 marks)

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.

Part (i) — Technical and non-technical controls for VOCs and PM10 (10 marks)

A technical control is an end-of-pipe or in-process engineering device that physically captures or destroys the pollutant; a non-technical control is a management, regulatory or source-substitution measure that reduces the emission without a treatment device. VOCs (gaseous organic vapours) and PM10 (respirable particulate, aerodynamic diameter ≤ 10 µm) require different technical devices, so a representative device is chosen for each pollutant.

Two air-pollution controls, with two advantages and two limitations each
ControlHow it worksTwo advantagesTwo limitations
Technical — regenerative thermal oxidiser (RTO) for VOCs and a fabric-filter baghouse / electrostatic precipitator for PM10 The oxidiser destroys VOCs at 760–820 °C (95–99% destruction); the baghouse or ESP removes PM10 by filtration or electrostatic capture (>99%). (1) Very high, reliable removal of the targeted pollutant; (2) treats the actual exhaust regardless of upstream process changes. (1) High capital and, for the oxidiser, fuel/energy cost (and CO2 from combustion); (2) a technology chosen for gases (oxidiser) does not remove particulate and vice-versa, so two devices are needed.
Non-technical — source reduction / material substitution and administrative controls (low-VOC or water-based solvents, enclosed handling, permit emission limits, preventive maintenance) Reformulating to water-based coatings and enclosing dusty transfer points lowers the VOC and PM generated at the source, before any device sees it. (1) Prevents the emission rather than treating it, so it avoids operating cost and secondary wastes; (2) often the cheapest and most durable reduction and improves worker exposure at the same time. (1) A substitute product may not meet the product-performance spec, and reductions are limited by what the process can tolerate; (2) relies on management commitment and enforcement — harder to guarantee and verify than a metered device.

Part (ii) — Drinking-water train for dissolved solids and odours; distribution safeguards (10 marks)

The source water carries both dissolved solids (which pass a conventional filter and so demand a membrane or softening step) and taste-and-odour compounds (dissolved organics such as geosmin/MIB, best removed by adsorption or oxidation). Three main processes therefore anchor the train: (1) conventional coagulation/flocculation/sedimentation to strip turbidity and colloids ahead of the sensitive downstream units; (2) granular activated carbon (GAC) adsorption (or ozone/advanced oxidation) to remove the odour compounds; and (3) reverse-osmosis / nanofiltration membrane softening to remove the dissolved solids. Disinfection and a clearwell finish the train before distribution.

Raw waterintake +screening Coagulation /Flocculation /Sedimentation GAC adsorption(taste & odour) RO / membrane(dissolved solids) Disinfection+ clearwell→ distribution removes odours removes dissolved solids
Schematic drinking-water train. The three main processes are the conventional clarification stage, GAC adsorption for odour, and RO/membrane softening for dissolved solids.

Two non-technical principles to protect potable quality through the distribution system. (1) Maintain a protective disinfectant residual and a multi-barrier management programme — a monitored free-chlorine or chloramine residual to the far ends of the network, backflow-prevention by-law, cross-connection control, and routine main flushing/valve exercising, all under an operator-certification and source-to-tap safety-plan framework. (2) Sustained monitoring, record-keeping and public reporting under the GCDWQ — regular bacteriological and residual sampling, prompt boil-water advisories, asset-renewal budgeting for aging mains, and transparent reporting to the public, so that deterioration is detected and corrected before consumers are exposed.

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