3D Consequence Modeling — Real Facility Photography

See what happens
when the tank
goes boom.

Three-dimensional BLEVE, Water Hammer, and CUI consequence visualization built from your actual facility photography. Not contour plots. Not CFD queues. Real physics, real geometry, delivered in days.

Reserve a Pilot Slot ↓
BLEVE SIMULATION
Scenario: BLEVE Vessel: 2,145 m³ propane Pressure: 1.7 MPa Duration: 36s

I was across the street when the tank went boom.

I was working at Imperial Oil Baseline when a high-pressure line failed in the AT Plastics pipe rack. I felt the blast from across the road. Nobody on that site had a tool that could show what a pipe rack rupture consequence looked like before it happened.

I spent 23 years inside petrochemical facilities as a journeyman industrial painter — sandblasting, spray coating, metalizing. I know what these plants look like from the inside because I coated the steel they're built from.

Tank Go Boom exists because consequence modeling shouldn't require a six-figure CFD license and a three-month queue. Your facility safety lead should be able to see the fireball radius, the blast wave, and the fragment trajectories from their actual plant geometry — in days, not months.

Three Scenario Types

Each delivered as a 3D visualization video + one-page computed values summary.

🔥

BLEVE

Boiling Liquid Expanding Vapour Explosion. Pressurized vessel catastrophic failure with fireball, blast wave, and fragment projection.

  • Fireball diameter & duration
  • Blast overpressure at key distances
  • Thermal radiation isopleths
  • Ballistic fragment trajectories
💧

Water Hammer

Pressure surge from sudden valve closure or pump trip. Pipe stress analysis with rupture consequence mapping.

  • Peak pressure wave propagation
  • Pipe stress vs. rated capacity
  • Rupture location probability
  • Release consequence envelope
🧱

CUI

Corrosion Under Insulation. Progressive degradation mapping showing wall thickness loss and failure probability over time.

  • CUI progression mapping
  • Wall thickness loss rate
  • Failure probability timeline
  • Inspection priority zones
20

Consequence Scenarios

Every scenario a process safety team encounters — modeled in three dimensions from your actual facility geometry.

🔥

Fire & Thermal Radiation

BLEVE LIVE DEMO
Jet Fire
Pool Fire
Flash Fire
Boilover
Flare Radiation
💥

Explosion & Overpressure

Vapor Cloud Explosion
Unconfined VCE
Pressure Vessel Burst
Dust Explosion
Confined Explosion
☣️

Toxic Release & Dispersion

H₂S Sour Gas Release
Ammonia Dispersion
Chlorine Release
LNG / Cryogenic Spill
🔧

Mechanical Failure & Degradation

Water Hammer IN DEV
Corrosion Under Insulation IN DEV
Pipeline Rupture
Tank Overflow / Dike Breach
⚠️

Cascading & Complex

Domino Effects

Need a scenario not listed here? Custom consequence models are available — additional time and pricing apply. Get in touch.

Pilot Program

Five engagements. First come, first served.

$4,750
per scenario · CAD · upfront
  • 3D consequence visualization from your facility photography
  • One-page summary sheet with all computed values
  • Fireball, blast wave, thermal, or fragment outputs
  • Delivered as video file + PDF summary
  • 2–5 business day turnaround from complete inputs
Request a Pilot Slot

All outputs require validation by a qualified professional before use in safety decisions.
Terms of Service

20%

Twenty percent of every engagement goes to Alberta.

$950 from every scenario funds verified industrial site reclamation — contamination cleanup at mining sites, heavy oil operations, and legacy industrial facilities across the province. The same facilities I spent my career inside.

Get in Touch

Sean Morin
23 YEARS IN PETROCHEMICAL FACILITIES · EDMONTON, AB