Aliağa, Mersin and Samsun ports host tank farms storing gasoline, diesel and jet fuel. A single tank can reach 50,000-100,000 m3; the 2005 Buncefield blast caused damage across an area about 1 km in diameter. NFPA 30 covers flammable and combustible liquids and dike dimensions, while API 650 covers tank design.
NFPA 30 Classification
- Class IA: Flash <23 °C, BP <38 °C
- Class IB: Flash <23 °C, BP >=38 °C (gasoline)
- Class IC: Flash 23-38 °C
- Class II: Flash 38-60 °C (diesel)
- Class IIIA: Flash 60-93 °C (fuel oil)
Tank Setback Distances
- Class I tank: 1.5x tank dia to neighbor
- Dike: 110 percent tank volume
- Dike wall: 1.8 m min height
- Tank-dike: Dia/2 min 3 m
- Property line: 1x dia min
Foam and Cooling Rates (NFPA 11-2024, hydrocarbons)
- Floating-roof rim seal foam: 12.2 L/min/m2 (top-of-seal with foam dam, Section 5.3)
- Full surface: 4.1 L/min/m2 with fixed foam discharge outlets (Table 5.2.5.2.2); 6.5 L/min/m2 with monitors and handlines (Table 5.2.4.2.2)
- Dike foam: 4.1 L/min/m2 with low-level fixed outlets, 6.5 L/min/m2 with foam monitors (Table 5.7.3.2)
- Cooling water: 2.0 L/min/m2 burning tank
- Neighbour cooling: 4.1 L/min/m2 within 30 m
Lightning and Overfill
- API 2003: Lightning grounding
- Bypass ring: Upper rim bonded
- Overfill protection: 95 percent alarm, 98 percent stop
- Tank gauging: Radar + servo
- Cathodic protection: Bottom CP
Major Incidents
- Buncefield UK 2005: Overfill - 43 injured
- Caribbean 2009: Lightning
- İzmir (Aliağa) refinery: about 12 Mt/y capacity
- Alsancak port 2013: Tank fire
- CSB investigation: Large incident analysis

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