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Automotive Gas Oil (AGO)
| Property | Unit | Typical Value |
| Density at 15°C | kg/m³ | 0.920 – 0.999 |
| Kinematic Viscosity at 50°C | mm²/s | 28 – 300 |
| Flash Point (Open Cup) | °C | > 60 |
| Pour Point | °C | -10 to 30 |
| Sulphur Content | % by weight | 2.5 – 3.5 |
| Ash Content | % by weight | 0.01 – 0.03 |
| Carbon Residue (Conradson) | % by weight | < 14 |
| Water Content | % by weight | < 0.5 |
| Heating Value | MJ/kg | 35 – 45 |
| Total Sediment | % by weight | < 0.1 |
Diesel Gasoil (D2)
| Density at 15°C (kg/m³) | 820 – 845 |
| Kinematic Viscosity at 40°C (cSt) | 2.0 – 4.5 |
| Flash Point (°C) | 52 – 96 |
| Pour Point (°C) | -15 to -40 |
| Cetane Number | 45 – 55 |
| Sulfur Content (% mass) | 0.001 – 0.05 (Ultra-Low Sulfur Diesel, ULSD) |
| Cloud Point (°C) | -5 to -15 (Winter Grade) |
| Lubricity (HFRR, μm) | 460 maximum |
| Distillation Temperature Range (°C) | 200 – 350 |
EN590 10PPM
| Property | Specification | Test Method |
| Density at 15°C | 820-845 kg/m³ | EN ISO 12185 |
| Kinematic Viscosity at 40°C | 2.0-4.5 mm²/s | EN ISO 3104 |
| Flash Point (PMCC) | >55°C | EN ISO 2719 |
| Cloud Point | -11°C (max) | EN 23015 |
| Pour Point | -15°C (max) | EN ISO 3016 |
| Cetane Number | >51 | EN ISO 5165 |
| Sulfur Content | ≤10 ppm | EN ISO 20846 |
| Distillation 95% recovered at 350°C | ≤85% | EN ISO 3405 |
| Copper Strip Corrosion (3 hours at 50°C) | Class 1 (max) | EN ISO 2160 |
| Total Contamination | ≤24 mg/kg | EN 12662 |
| Water Content | ≤200 mg/kg | EN ISO 12937 |
| Ash Content | ≤0.01% (m/m) | EN ISO 6245 |
| Carbon Residue on 10% Residue | ≤0.30% (m/m) | EN ISO 10370 |
| Sulfated Ash | ≤0.02% (m/m) | EN ISO 3987 |
| Lubricity at 60°C | HFRR ≤460 µm | EN ISO 12156-1 |
| Oxidation Stability | ≥6 hours | EN ISO 12205 |
| Acid Number | ≤0.50 mg KOH/g | EN 14104 |
ESPO Crude Oil
| API Gravity | 31.2° – 36.6° (typically around 32°) |
| Sulfur Content | 0.08% – 0.2% (typically around 0.1%) |
| Density (at 15°C) | 838 – 857 kg/m³ |
| Pour Point | Below -33°C (-27°F) |
| Viscosity (at 50°C) | 6.3 – 7.4 cSt |
| Acid Number | 0.05 mg KOH/g |
| Total Nitrogen Content | < 0.12 wt% |
| Salt Content | < 5 PTB (Pounds per Thousand Barrels) |
| Reservoir Sulfur Content | Typically low sulfur |
Jet A1
| Chemical Formula | C10H20 to C15H28 |
| Density at 15°C (59°F) | 0.775 – 0.840 kg/l |
| Flash Point | -43°C (-45°F) minimum |
| Freeze Point | -47°C (-53°F) maximum |
| Autoignition Temperature | 210°C (410°F) minimum |
| Kinematic Viscosity at -20°C | 8.0 – 10.0 mm²/s |
| Thermal Stability | Pass |
| Smoke Point | 25 mm minimum |
| Sulfur Content | 0.30% maximum |
| Aromatics Content | 25% maximum |
| Acidity (pH) | 5.0 maximum |
| Copper Strip Corrosion (3 hrs at 100°C) | 1a maximum |
| Particulate Contamination | None visible at 5 ppm |
| Water Content | 0.05% maximum |
JP54
| Appearance | Clear and Bright Liquid |
| Color | Max 3.0 Saybolt Color |
| Density at 15°C (kg/m³) | 776 – 840 |
| Flash Point (°C) | Min 38 |
| Freeze Point (°C) | Max -40 |
| Kinematic Viscosity at 20°C (cSt) | 8.0 – 11.0 |
| Thermal Stability (JFTOT) at 260°C | Max 25% loss in volume |
| Sulfur Content (wt%) | Max 0.30 |
| Aromatics Content (vol%) | Max 25 |
| Smoke Point (mm) | Min 19 |
| Water Content (vol%) | Max 0.05 |
| Microbial Contamination | Not detectable |
| Acidity (mg KOH/g) | Max 0.015 |
| Corrosion (copper strip) at 100°C | Not worse than No. 1 |
| Total Acidity (mg KOH/g) | Max 0.10 |
| Net Heat of Combustion (MJ/kg) | Min 42.8 |
| Particle Count (4μm and larger) | Max 12,000 per ml |
| Lubricity (HFRR, μm) | Max 520 |
| Copper Strip Corrosion (3 hrs at 100°C) | Max 1a |
Light Cycle Oil (LCO)
| Property | Value |
| Chemical Formula | LiCoO2 |
| Molecular Weight | 97.87 |
| Density | 5.0 – 5.1 |
| Color | Dark gray or black |
| Crystal Structure | Hexagonal |
| Melting Point | 1,128°C (2,062°F) |
| Boiling Point | N/A |
| Thermal Conductivity | 5 – 6 W/m·K |
| Specific Heat Capacity | ~620 J/kg·K |
| Electrical Conductivity | 10^-5 to 10^-6 S/cm |
| Solubility | Insoluble in water |
| Particle Size | Typically in the micron range |
Liquified Natural Gas (LNG)
| Chemical Composition | Primarily Methane (CH4) |
| Boiling Point | Approximately -162°C |
| Density | Approximately 0.41 g/cm³ |
| Energy Content | ~22 MJ/L (lower heating value) |
| Color | Clear, colorless |
| Odor | Odorless |
| Flammability | Highly flammable |
| Autoignition Temperature | Approximately 580°C |
| Vapor Pressure | < 1 kPa at -162°C |
| Flash Point | Below -160°C |
| Liquefaction Temperature | < -162°C |
| Expansion Ratio | 1:600 (1 volume of LNG expands to 600 volumes of natural gas) |
Liquified Petroleum Gas(LPG)
| Chemical Formula | C3H8 |
| Molecular Weight | 44.1 g/mol |
| Boiling Point | -42.1°C (-43.8°F) |
| Melting Point | -188.1°C (-306.6°F) |
| Density (at 25°C/77°F) | 0.51 g/cm³ |
| Energy Content | 46.4 MJ/kg |
| Energy Content (per liter) | 25.5 MJ/liter |
| Color | Colorless |
| Odor | Odorized with Mercaptan |
| Flammable Range | 2.1% to 9.5% (Volume) |
| Autoignition Temperature | 410°C (770°F) |
| Vapor Pressure (at 25°C) | 8 – 10 bar (116 – 145 psi) |
Mazut 100
| Property | Unit | Typical Value |
| Density at 15°C | kg/m³ | 0.920 – 0.999 |
| Kinematic Viscosity at 50°C | mm²/s | 28 – 300 |
| Flash Point (Open Cup) | °C | > 60 |
| Pour Point | °C | -10 to 30 |
| Sulphur Content | % by weight | 2.5 – 3.5 |
| Ash Content | % by weight | 0.01 – 0.03 |
| Carbon Residue (Conradson) | % by weight | < 14 |
| Water Content | % by weight | < 0.5 |
| Heating Value | MJ/kg | 35 – 45 |
| Total Sediment | % by weight | < 0.1 |