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Chemical Engineering Topics

Industrial tank engulfed in flames during an ATEX-related explosion in a chemical plant

Hazardous Area Classification: ATEX Zones

Understand the fundamentals of ATEX zone classification for gases, vapours, and mists according to Directive 1999/92/EC. This article explains where …
P&ID diagram showing control valve leakage scenario with modulating valve and on-off valve in a distillation system.

Control Valve Leakage: Often Used Upstream

Even a small internal leakage through a control valve can change process behavior and compromise safety. This article explains why …
Chemical engineer inspecting industrial equipment inside a process plant facility

Chemical Engineering Core Disciplines – A Practical Overview

Chemical engineering core disciplines: a concise overview of the main engineering fields that structure chemical engineering, from thermodynamics and fluid …
Cryogenic VOC abatement system with CO₂ solidification and catch tank, featuring reactors, cryogenic skid, and DN piping lines.

VOC emission control: CO₂ Solidification Risks

CO₂ solidification in cryogenic abatement systems can reduce VOC emission control performance by causing blockages and loss of operability …
Process diagram with rupture disc protecting a reactor, discharging to a catch tank for flammable solution containment

Rupture Disc Activation: Near Miss or PS Event

When a rupture disc activates, it represents a process deviation that must be recorded within the Safety Management System. Depending …
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: P&ID Example

Cryogenic VOC abatement systems are highly effective but face operational limits when CO₂ or water freezes at low temperatures. This …
Chemical reactor vessel with flanged nozzles and a manway — industrial process equipment

Rupture Disc Positioning: Best Practices

A practical comparison between What-If Analysis and HAZOP for process safety studies, with real examples from chemical plants. Learn when …
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 …
Technical diagram of two reactors RX-01 and RX-02 connected to a process vent collector (vent line DN100-DN200)

Vent Header Design: Why Top Tie-Ins Are Safer

Vent header design is critical for safe reactor operation. This article explains why top tie-ins are preferred over bottom tie-ins, …