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23-Chem-A5 Chemical Plant Design and Economics · December 2018

Question 3 of 6: Top Five Items in a Pilot-Plant Investigation

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

Notes on this paper

National Exams — December 2018 — 16-Chem-A5 Chemical Plant Design and Economics. Three-hour, closed-book exam; one two-sided aid sheet and an approved Sharp/Casio calculator permitted. Six equally weighted (20-mark) questions are posed and the candidate answers any five; only the first five are marked. All six are answered below for completeness. Question 1 is a process-synthesis flowsheet (catalytic propane dehydrogenation), Question 2 is a numerical discounted-cash-flow (DCFROR) minimum-selling-price calculation, and Questions 3–6 are qualitative design/economics essays (pilot-plant investigation, technical design factors, economic design factors, and a solvent-emission abatement scheme).

Reference texts: M.S. Peters, K.D. Timmerhaus & R.E. West, Plant Design and Economics for Chemical Engineers (5th ed., McGraw-Hill) — the exam's named primary text (pilot plants Ch. 3, general design considerations and plant-location factors Ch. 2–3, interest/depreciation/profitability Ch. 7–10); R.K. Sinnott & G. Towler, Chemical Engineering Design (Coulson & Richardson vol. 6) — economic analysis, cash-flow/DCFROR and flowsheeting; R. Smith, Chemical Process Design and Integration (2nd ed., Wiley) — reaction–separation–recycle structure; supporting Canadian practice from CCOHS, provincial OH&S regulation and Environment and Climate Change Canada air-emission guidance.

Question 3: Top Five Items in a Pilot-Plant Investigation (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.

Given / Find. A qualitative design-methodology question: identify and describe the five most important items a pilot-plant programme must resolve before a full-scale plant can be designed with confidence. The pilot plant exists to supply data that neither the laboratory (too small, idealised) nor pure calculation can give reliably.

A pilot plant bridges the gap between bench chemistry and a commercial plant: it is large enough to expose the real-fluid, real-material and real-control behaviour that governs scale-up, yet small enough to fail cheaply. The five items below are the ones that most often decide whether the full-scale design succeeds.

  1. Reaction kinetics, catalyst life and deactivation. The pilot plant runs long enough to measure how conversion and selectivity change over weeks or months of continuous operation — catalyst ageing, coking, poisoning by feed impurities and the regeneration cycle. Laboratory runs are too short to reveal deactivation, yet it directly sets reactor size, catalyst inventory and the reactor replacement/regeneration schedule.
  2. Heat- and mass-transfer scale-up. Mixing, heat-transfer coefficients, temperature and concentration gradients, and residence-time distribution all change with vessel size. The pilot unit provides the transport data needed to size heat exchangers and agitators and to confirm that hot spots, mass-transfer limitations or poor mixing found at scale will not degrade yield or safety in the commercial reactor.
  3. Materials of construction and corrosion/erosion. Extended operation on the real (not idealised) process fluid, including trace corrosive impurities, reveals corrosion, erosion and fouling rates that short laboratory exposure cannot. Coupons and instrumented sections identify the correct alloys and linings and establish realistic maintenance and equipment-life expectations.
  4. Recycle and impurity build-up. A closed, continuously recycled system lets trace by-products, inerts and unconverted species accumulate to steady state — behaviour invisible in single-pass bench work. The pilot plant quantifies these build-ups and fixes the necessary purge rates, so the commercial recycle loops can be designed to hold impurities below the level that harms the reaction or the product.
  5. Separation performance and product quality. The pilot plant verifies that the separation train (distillation, absorption, filtration, drying) actually delivers on-specification product from the real process streams, including the effect of trace components on relative volatility, foaming, emulsions and phase behaviour. It confirms recovery, purity and the final product properties that the market and any regulatory limits demand.
Check: the emphasis on catalyst life, recycle impurity build-up and real-fluid corrosion reflects that these are precisely the items that "eliminate the compromise acceptance of data" — the phenomena a designer would otherwise have to guess at from short laboratory tests and conservative factors. Operability, control tuning and waste/effluent characterisation are close runners-up and would round out a longer list.