3D CFD-class fire and explosion modelling — VCE, BLEVE, jet fire, flash fire, domino
FERA underpins facility siting, occupied-building protection, F&G mapping, fireproofing scope, emergency response, and quantitative escalation logic. The discipline has shifted decisively over the last decade from empirical TNT-equivalent and Multi-Energy methods to 3D CFD-class modelling (FLACS, KFX, Ansys Fluent) that captures real congestion, confinement, and ventilation — the difference being orders of magnitude in overpressure prediction for typical petrochemical layouts. The Buncefield 2005 event, where overpressures exceeded all prior modelling expectations, drove a regulator-led move toward CFD for high-consequence cases. Modern FERA work integrates leak frequency from OGP 434 / FRED, ignition probability per Cox-Lees with congestion uplift, BLEVE consequence per Roberts / CCPS, jet-fire radiation per Chamberlain / Cook-Cullis, and Bow-Tie escalation pathways for domino assessment. The hardest decisions remain the boundary conditions: which scenarios merit CFD vs phenomenological modelling, and how to communicate uncertainty to non-technical decision-makers.

A structured, facilitated process — from scope definition through close-out — producing defensible, actionable outputs.
Define FERA scenario set from leak frequency data (OGP 434 / HSE FRED); specify orifice sizes (3 / 10 / 25 mm equivalent for gas; 3 / 50 mm for liquid), fluid phases, and release orientations; calculate source terms including two-phase flash and cryogenic pool formation.
Model pool fires (Thomas / Mudan thermal flux model), jet fires (Chamberlain / Cook-Cullis with radiant fraction), and flash-fire LFL envelopes; calculate radiation iso-contours at 4 / 12.5 / 37.5 kW/m² for PFP scope, detector siting, and occupied-building impact.
Apply TNT, Multi-Energy, and Baker-Strehlow-Tang methods for screening; deploy FLACS or KFX 3D CFD for high-consequence VCE cases requiring congestion parameterisation (volume blockage ratio, obstacle density); produce overpressure and positive-impulse iso-contours.
Model BLEVE fireball (Roberts / Hasegawa correlation) for LPG / LNG / pressure-liquefied gas; calculate fragment trajectory and mechanical damage radius; apply Cozzani / IChemE domino thresholds (radiation 37.5 kW/m², overpressure 0.3 bar) for escalation identification.
Apply Cox-Lees ignition model with delayed-ignition conditional split (VCE vs pool / jet fire); integrate frequency × consequence to produce risk metrics; identify dominant risk contributors; generate F&G mapping cloud-size inputs and facility-siting overpressure dataset.
Issue PFP scope optimisation from actual thermal radiation field; provide blast-load specification (peak overpressure, impulse) per API RP 752 for occupied-building assessment; recommend firewater demand and deluge coverage; produce COMAH / EPA RMP-compliant consequence documentation.

Speak with our team to scope an engagement tailored to your facility, regulatory context, and lifecycle stage.