23-Chem-B2 Environmental Engineering · May 2015
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Paper format. EGBC 04-Chem-B2 Environmental Engineering, May 2015, 3 hours, closed-book with a candidate-prepared double-sided 8½×11-inch aid sheet. Seven problems, each worth 20 marks; candidates attempt any five, and only the first five answers in the workbook are marked. All seven problems are solved below as a complete study resource.
Reference texts: G. Tchobanoglous, F. L. Burton & H. D. Stensel (Metcalf & Eddy), Wastewater Engineering: Treatment and Reuse (4th ed., McGraw-Hill) — BOD kinetics, dissolved air flotation, activated-sludge design, nutrient removal; M. L. Davis & D. A. Cornwell, Introduction to Environmental Engineering (5th ed., McGraw-Hill) — drinking-water treatment, air pollution control, ion exchange, reverse osmosis, soil remediation; C. D. Cooper & F. C. Alley, Air Pollution Control: A Design Approach — fabric filtration, thermal oxidation, adsorption, odour control; S. P. Turner, Workbook of Atmospheric Dispersion Estimates (2nd ed., CRC Press) — the Gaussian plume model and Pasquill–Gifford stability classes. Canadian context follows the Canadian Environmental Protection Act (CEPA 1999), the Canadian Council of Ministers of the Environment (CCME) Municipal Wastewater Effluent and Drinking Water Quality guidelines, and provincial air/water permitting practice (e.g. BC Environmental Management Act, Metro Vancouver air-quality bylaws).
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.
A comparative matrix, as recommended by the question, is the clearest way to present the three control-technology families side by side.
| Technology | Main technology principle | Advantages (2) | Limitations (2) | Example application |
|---|---|---|---|---|
| (i) Oxidation-based — toxic gases | The toxic gas stream (e.g. H₂S, CO) is thermally or catalytically oxidized to a less hazardous species (H₂S→SO₂, CO→CO₂), with sufficient temperature/residence time/turbulence ("three T's") to complete the reaction. | Achieves near-complete destruction (not just phase transfer) of the toxic species regardless of its identity; catalytic oxidation can operate at a much lower temperature than thermal, cutting fuel cost. | Produces its own combustion by-products (SO₂ from H₂S oxidation may itself require downstream scrubbing); catalyst beds are vulnerable to poisoning (particulates, certain sulfur/metal species) that progressively degrades conversion efficiency. | Catalytic oxidation of H₂S-laden vent gas from a sour-gas processing or pulp-mill recovery operation. |
| (ii) Condensation-based — odorous vapours | The odorous vapour-laden gas is cooled (directly or via a refrigerated/chilled-water surface condenser) below the dew point of the target compound, condensing it out of the gas phase into a liquid that is collected and separately treated or recovered. | Can recover the condensed compound for reuse/disposal rather than destroying it, valuable for solvent-recovery applications; effective as a pretreatment stage ahead of a smaller downstream polishing unit (adsorption or scrubbing), reducing that unit's loading. | Only effective for compounds with a sufficiently high boiling point/low vapour pressure at an economically achievable condensing temperature — highly volatile odorants pass through largely uncondensed; refrigeration energy cost rises sharply as the required condensing temperature drops. | Refrigerated condensation recovery of solvent vapour ahead of a carbon-adsorption polishing stage at a chemical/coatings plant vent. |
| (iii) Adsorption-based — aerosols | The aerosol-laden gas passes through a packed/granular sorbent bed (e.g. activated carbon or a fibrous adsorptive media); the bed acts simultaneously as a depth filter capturing aerosol droplets/particles by impaction and interception on the packing surfaces, while any co-adsorbable vapour phase associated with the aerosol is captured by physisorption on the sorbent's internal pore surface. | Simultaneously addresses an aerosol's particulate and any accompanying semi-volatile vapour fraction in a single unit, unlike a pure-particulate device (e.g. a baghouse) which passes vapour straight through; effective even at the relatively low mass loadings typical of a fine mist/aerosol stream. | Aerosol droplets can progressively wet/blind the sorbent bed, raising pressure drop and shortening the effective service life compared with a dry-gas adsorption duty; regeneration/replacement is more frequent and costly than for a dedicated mist eliminator when the stream is aerosol-dominated rather than truly vapour-phase. | Activated-carbon adsorber polishing an oil-mist/solvent-aerosol vent from a metalworking or degreasing operation, downstream of a coarse mist eliminator. |