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Process safety is not a separate role within a plant. It is a responsibility shared by every chemical engineer.

— Ing. Ivet Miranda

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Emergency pressure relief configurations for non-fouling reactor systems (rupture disc, RD-PSV combination, and PSV to emergency catch tank)

Pressure Safety Valve vs Rupture Disc: Key Differences

A practical engineering comparison with a real reactor example, covering PSV, rupture disc, and RD+PSV configurations used in chemical plants …
HAZOP worksheet example showing deviations, causes, consequences.

What Is HAZOP Analysis? Example and Template

A practical HAZOP analysis example showing how deviations, causes, consequences, safeguards, and risk are evaluated using a real worksheet …
P&ID example showing safety interlocks on a hot-water tank with rupture disc, control valves and emergency catch tank in a chemical plant

Safety Interlocks: From P&ID to Control Logic

Cryogenic VOC abatement systems are highly effective but face operational limits when CO₂ or water freezes at low temperatures. This …


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