23-Chem-A5 Chemical Plant Design and Economics · May 2016
Question 5 of 6: Startup and Shutdown Safety
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — May 2016 — 04-Chem-A5 Chemical Plant Design and Economics. Three-hour, closed-book exam; one two-sided aid sheet and an approved 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. Questions 1–3 are numerical (distillation heat integration, after-tax net present worth, and a coagulant-dosage cost optimisation); questions 4–6 are qualitative essays on materials of construction, plant startup/shutdown safety, and equipment-selection factors.
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 (interest and profitability Ch. 7–10, materials of construction Ch. 12, plant safety and loss prevention Ch. 3, equipment selection throughout Ch. 14–22); R. Smith, Chemical Process Design and Integration (2nd ed., Wiley) and B. Linnhoff et al., A User Guide on Process Integration (IChemE) — pinch analysis and column heat integration behind Question 1; R.K. Sinnott & G. Towler, Chemical Engineering Design (Coulson & Richardson vol. 6) — materials selection and equipment sizing; supporting Canadian practice from CCOHS, provincial OH&S process-safety-management regulations and the CSA Z767 (PSM) framework.
Question 5: Startup and Shutdown Safety (20 marks)
Given / Find. A qualitative safety-review question drawn from process-safety-management practice: the pre-startup safety review (PSSR) checklist and the controlled-shutdown checklist. The answer is a checklist of the key questions, each tied to the hazard it guards against.
(a) Ten startup safety questions
Purging — Have all vessels and lines been purged of air (or of process gas) so that no flammable air/fuel mixture can form when hydrocarbons are admitted?
Leak/pressure test — Has the system been pressure-tested and confirmed leak-tight at operating pressure before introducing hazardous fluids?
Blinds and isolation — Have all blinds/spades used for maintenance been removed (and any required blinds installed), and are isolation valves lined up correctly?
Relief and venting — Are all relief valves, rupture discs and vent systems in service, correctly set and not isolated?
Instrumentation and interlocks — Are all instruments, alarms, trips and safety interlocks calibrated, functional and enabled (not bypassed)?
Utilities — Are all utilities (cooling water, steam, instrument air, inert gas, electrical power) available and stable before startup?
Drains and low points — Are drains and low-point valves closed, and has accumulated water/liquid been removed to avoid slugging or thermal shock?
Materials and inventory — Are the correct feedstocks and catalysts loaded, and is the initial inventory within safe limits (no overfill)?
Rate of change — Are heat-up/pressurisation rates controlled within metallurgical and thermal-stress limits, avoiding rapid transients?
Personnel and procedures — Are operators trained on the startup procedure, is the work-permit/lockout cleared, and are emergency-response provisions (fire water, PPE, evacuation) in place?
(b) Five shutdown safety questions
Depressurisation — Is the plant being depressurised and cooled in the correct controlled sequence to prevent thermal shock or vacuum collapse?
Inventory removal — Has hazardous inventory been drained, pumped out or routed to safe disposal/flare before equipment is opened?
Purging and inerting — Have vessels been purged/inerted to remove flammables (and to prevent an air ingress that could form an explosive mixture)?
Isolation and lockout — Are energy sources and process connections positively isolated (blinded, locked out/tagged out) before hand-over to maintenance?
Cooling and reactive hazards — Are exothermic/reactive materials safely quenched or removed, and is residual heat dissipated so no runaway or auto-ignition can occur while the plant is down?
Check: these questions map directly onto the elements of a Pre-Startup Safety Review (PSSR) and controlled-shutdown procedure required under process-safety-management practice. In Canada the framework is the CSA Z767 PSM standard together with provincial OH&S regulations; the specific checklist items above are the generic industry questions and would be expanded into a site-specific procedure.