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18-Env-B5 Industrial & Hazardous Waste Management · December 2015

Question 16 of 18: Important Process Design Variables for Five Treatment/Disposal Unit Processes

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

Notes on this paper

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 16: Important Process Design Variables for Five Treatment/Disposal Unit Processes (10 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.

Unit processKey design variable(s)Why important
16.1 IncineratorCombustion temperature & residence timeMust be high enough, and held long enough, to fully destroy hazardous organics and minimize products of incomplete combustion.
Excess air ratioEnsures complete combustion (avoids fuel-rich, sooty/PIC-forming conditions) without wasting auxiliary fuel on excess heating of air.
Waste heating value / moisture contentGoverns whether the waste is self-sustaining or requires auxiliary fuel to maintain design temperature.
16.2 Membrane separatorPore size / molecular weight cut-offSets which contaminants are physically rejected versus pass through with the permeate.
Transmembrane pressure & fluxGoverns throughput per unit membrane area and drives the rate of fouling.
Feed pretreatment / cross-flow velocityControls fouling rate and cake-layer formation, which otherwise degrade flux and shorten cleaning intervals.
16.3 Conventional activated sludgeF/M ratio & MLSS/MLVSSBalances 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 oxygenSets available reaction time and ensures adequate oxygen supply for aerobic metabolism.
16.4 Anaerobic digesterOrganic (VS) loading rate & HRT/SRTControls 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 / alkalinityMethanogens tolerate only a narrow pH band (~6.8–7.2); alkalinity buffers against VFA-driven pH drop.
16.5 Aerobic digesterSolids retention timeSets the degree of volatile-solids destruction (stabilization) achieved.
Dissolved oxygen & mixing/oxygen-transfer capacityMust sustain aerobic conditions throughout the digester volume for continued endogenous respiration.
TemperatureGoverns the rate of biological VS destruction, as with any biological process.