⛛ Tank Spec & Inventory
CYLINDRICALGEOMETRY & DIMENSIONS
Auto-synced with calculated geometric volume
LEVELS & DIP GAUGE READINGS
CRACK / ORIFICE SPECIFICATION
⚡ Inverse Hole Size Estimator
If hole size is unknown, estimate diameter from observed level drop rate:
⚡ Real-Time Shell Depletion & Thermal Profile
HEAD: 11.70 m
Remaining to Shell Hole Depletion
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Vol: 0 m³
Total Tank Empty Time (to LLL)
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Current Rate: 0 m³/h
EXECUTIVE CRISIS LOG & TIME STAMPS
[00:00:01] INCIDENT COMMENCED. Depletion modeling initialized.
[00:00:02] Hydrostatic head: 11.7m above orifice elevation.
[00:00:03] Foam / Water deluge parameters loaded. NFPA 11 compliant rate check.
🛡️ Fire Suppression & Extinguishment
ACTIVE INTERVENTIONFIRE FIGHTING / DELUGE INTERVENTION
NFPA 11 std: 4.1 - 8.1 L/min/m²
Water spray for boilover / BLEVE prevention
PREDICTIVE FIRE EXTINCTION & BURNOUT TIMES
🔥 Without Intervention
Time to Burn-Out:
-- hrs
Boilover Risk Window:
-- hrs
Hole Depletion:
-- min
Spill Pool Diameter:
-- m
🧯 With Intervention
Est. Extinction Time:
-- min
Foam Stock Duration:
-- min
Cooling Water Margin:
Adequate
BLEVE Suppression:
Mitigated
PRODUCT COMBUSTION PROFILE
Density (ρ):
850 kg/m³
Liquid Regression Rate (v_b):
4.0 mm/min
Boilover Potential:
High (Heat Wave Formation)
Thermal Radiation Range (15 kW/m²):
~65 m