23-Chem-A5 Chemical Plant Design and Economics · December 2017
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — December 2017 — 16-Chem-A5 Chemical Plant Design and Economics. Three-hour, closed-book exam; one two-sided aid sheet and an approved calculator permitted. Six questions are offered; five (5) of equal value (20 marks each) constitute a complete paper and only the first five in the answer book are marked. All six questions are solved below for completeness. The paper is one economics calculation (Q2) plus a process-synthesis design (Q1) and four qualitative process-design / safety questions (Q3–Q6). Property data not printed on the paper (straight-line depreciation convention, WHMIS/GHS section list) are stated explicitly where used.
Reference texts: Turton, Bailie, Whiting, Shaeiwitz & Bhattacharyya, Analysis, Synthesis, and Design of Chemical Processes (4th ed., Prentice Hall) — process synthesis, profitability analysis and waste treatment; Peters, Timmerhaus & West, Plant Design and Economics for Chemical Engineers (5th ed., McGraw-Hill) — capital/operating cost and return-on-investment analysis; Towler & Sinnott, Chemical Engineering Design (2nd ed., Butterworth-Heinemann) — reactor-design procedure and waste management; Crowl & Louvar, Chemical Process Safety (4th ed., Prentice Hall) — inherently safer design and SDS content.
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.
Good practice follows the waste-management hierarchy — first reduce at source, then reuse/recycle, then treat, and only then dispose — so that the quantity and hazard of waste requiring final disposal are minimised.
Gaseous effluents are treated by absorption (wet scrubbing of acid gases or solvents into a liquid, as in the Q1 flowsheet), adsorption of trace organics onto activated carbon, condensation to recover volatile solvents, and thermal or catalytic incineration (thermal oxidisers and flares) to destroy combustible vapours. Particulate-laden gases are cleaned by cyclones, fabric (bag) filters, electrostatic precipitators or wet scrubbers; dilute biodegradable streams can be treated in biofilters.
Organic liquid wastes are best recovered by distillation where a solvent has value, or otherwise incinerated — high-calorific streams are often blended and burned as supplementary fuel with heat recovery. Phase separation (decanting) removes immiscible water or solids first, and any resulting aqueous phase is routed to aqueous treatment.
Solids are managed by recovery/recycling where practical, incineration to reduce volume and destroy organics, and, for the residue, secure landfill with prior stabilisation/encapsulation of hazardous solids; biodegradable organic solids may be composted.
Aqueous effluents are treated in the classic sequence: physical pre-treatment (equalisation, screening, sedimentation, flotation, filtration) to remove suspended solids and oils; chemical treatment (neutralisation of acids/alkalis, precipitation of heavy metals, chemical oxidation of refractory organics); biological treatment (activated sludge, trickling filters or anaerobic digestion) to remove dissolved biodegradable organics; and, for polishing or reuse, membrane processes (ultrafiltration, reverse osmosis) or activated-carbon adsorption, before discharge to sewer or watercourse within permit limits.