18-Env-B5 Industrial & Hazardous Waste Management · December 2015
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Reference texts: Nemerow & Dasgupta, Industrial and Hazardous Waste Treatment, 2nd ed.; Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed.; Davis & Cornwell, Introduction to Environmental Engineering, 6th ed.; LaGrega, Buckingham & Evans, Hazardous Waste Management, 2nd ed.; CCME, Guidelines for the Management of Biomedical Waste in Canada (1992); Canadian Environmental Protection Act (CEPA), 1999; Basel Convention on the Control of Transboundary Movements of Hazardous Wastes (1989); provincial hazardous waste regulations (e.g. BC's Environmental Management Act and Hazardous Waste Regulation).
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.
| Unit process | Key design variable(s) | Why important |
|---|---|---|
| 16.1 Incinerator | Combustion temperature & residence time | Must be high enough, and held long enough, to fully destroy hazardous organics and minimize products of incomplete combustion. |
| Excess air ratio | Ensures complete combustion (avoids fuel-rich, sooty/PIC-forming conditions) without wasting auxiliary fuel on excess heating of air. | |
| Waste heating value / moisture content | Governs whether the waste is self-sustaining or requires auxiliary fuel to maintain design temperature. | |
| 16.2 Membrane separator | Pore size / molecular weight cut-off | Sets which contaminants are physically rejected versus pass through with the permeate. |
| Transmembrane pressure & flux | Governs throughput per unit membrane area and drives the rate of fouling. | |
| Feed pretreatment / cross-flow velocity | Controls fouling rate and cake-layer formation, which otherwise degrade flux and shorten cleaning intervals. | |
| 16.3 Conventional activated sludge | F/M ratio & MLSS/MLVSS | Balances organic loading against available biomass; governs removal efficiency and sludge settleability (bulking risk). |
| Solids retention time (SRT) | Controls whether nitrifiers are retained (SRT must exceed their minimum growth rate) and sets net sludge production. | |
| Hydraulic retention time & dissolved oxygen | Sets available reaction time and ensures adequate oxygen supply for aerobic metabolism. | |
| 16.4 Anaerobic digester | Organic (VS) loading rate & HRT/SRT | Controls reactor sizing and prevents overloading, which can sour the digester (VFA accumulation). |
| Temperature (mesophilic ~35°C or thermophilic ~55°C) | Governs methanogen kinetics; must be held stable since methanogens are highly temperature-sensitive. | |
| pH / alkalinity | Methanogens tolerate only a narrow pH band (~6.8–7.2); alkalinity buffers against VFA-driven pH drop. | |
| 16.5 Aerobic digester | Solids retention time | Sets the degree of volatile-solids destruction (stabilization) achieved. |
| Dissolved oxygen & mixing/oxygen-transfer capacity | Must sustain aerobic conditions throughout the digester volume for continued endogenous respiration. | |
| Temperature | Governs the rate of biological VS destruction, as with any biological process. |