Kerosene & Jet Fuel
Straight-Run Kerosene as a fraction of distillation of crude oil and its derivatives like Jet Fuel (Fuel Oil #1), Road/Rail/Marine Gas Oil (Fuel Oil#2) and Diesel (FuelOil#3) are all included in the products offered by “Ever Brilliant Trading Co.” to its clients worldwide.
“Ever Brilliant General Trading LLC.” Serves its client by providing fuel oil which mainly consists of residues from crude-oil distillation. It is used primarily for steam boilers in power plants, aboard ships, and in industrial plants. Commercial fuel oils usually are blended with other petroleum fractions to produce the desired viscosity and flash point.
| TEST ITEM | Min | Max | METHOD | ||
|---|---|---|---|---|---|
| Density | 820 | 820 | Kg/M3 | ||
| Distillation | |||||
| Recovered at 185 °C | 50 | VOL% | |||
| Recovered at 210 °C | 90 | VOL% | |||
| Recovered at 235 °C | 95 | VOL% | |||
| F.B.P | 275 | °C | |||
| Carbon Residue | 2 | VOL% | |||
| loss | 1.5 | VOL% | |||
| Corrosion | 3hr @ 100°C | la | |||
| Pour Point | -3 | °C | |||
| Cloud Point | 2 | °C | |||
| Sulphur | 0.15 | VOL% | |||
| Color | 25 | ASTM D156 | |||
| Odor | Merchantable | ||||
| Flash Point | 38 | 43 | °C | ||
| Smoke Point | 25 | ||||
| Acidity | mg KOH/100CM2 | 0.7 | |||
| Mercaptan Sulphur | 0.001 | VOL% |
Jet Fuel
| 1 | Appearance | |||
|---|---|---|---|---|
| 1.1 | Visual Appearance | Clear & Bright, free from solid matter & undissolved water at ambient temperature | Clear & Bright | |
| 1.2 | Color | Report | ASTM D 156 or ASTM D 6054 | 25 |
| 1.3 | Particulate Contamination, at point of manufacture, mg/l | 1.0 Max. | IP 423/ASTM D 5425 | 0.8 |
| 1.4 | Particulate, at point of manufacture | |||
| 1.4.1 | > 4 µ µ (c) | Report | IP 564 or IP 565 | 2500 |
| 1.4.2 | > 6 µ µ (c) | Report | 950 | |
| 1.4.3 | >14 µ µ (c) | Report | 99 | |
| 1.4.4 | >21 µ µ (c) | Report | 22 | |
| 1.4.5 | >25 µ µ (c) | Report | 15 | |
| 1.4.6 | >30 µ µ (c) | Report | 10 | |
| 2 | Composition | |||
| 2.1 | Total Acidity, mg KOH/gm | 0.015 Max. | ASTM D 3242 | 0.009 |
| 2.2 | Aromatic Hydrocarbon Types | |||
| 2.2.1 or | Aromatics % v/v | 25 Max. | IP156/ASTMD1319 | 18.5 |
| 2.2.2 | Total Aromatics % v/v | 26.5 Max. | IP 436/ASTM D 6379 | 18.5 |
| 2.3 | Sulphur. Total % m/m | 0.3 Max. | ASTM D 4294 | 0.25 |
| Sulphur Mercaptan % m/m | 0.003 Max. | ASTM D 3227 | 0.002 | |
| 2.4 | ||||
| Or | Doctor Test | Doctor negative | IP 30 | |
| 2.5 | ||||
| 2.6 | Refining Component, at the Point of manufacture | |||
| 2.6.1 | 1. Hydro processed component. % v/v | Report | ||
| 2.6.2 | 2. Severely Hydro processed component. % v/v | Report | ||
| 3 | Volatility | |||
| 3.1 | Distillation - IBP °C. | • | ASTM D 86 | 15 |
| Fuel recovered 10% by volume at °C | 205 Max. | • | 171 | |
| Fuel recovered 50% by volume at °C | Report | - | 195 | |
| 1 | Appearance | |||
|---|---|---|---|---|
| 1.1 | Visual Appearance | Clear & Bright, free from solid matter & undissolved water at ambient temperature | Clear & Bright | |
| 1.2 | Color | Report | ASTM D 156 or ASTM D 6054 | 25 |
| 1.3 | Particulate Contamination, at point of manufacture, mg/l | 1.0 Max. | IP 423/ASTM D 5425 | 0.8 |
| 1.4 | Particulate, at point of manufacture | |||
| 1.4.1 | > 4 µ µ (c) | Report | IP 564 or IP 565 | 2500 |
| 1.4.2 | > 6 µ µ (c) | Report | 950 | |
| 1.4.3 | >14 µ µ (c) | Report | 99 | |
| 1.4.4 | >21 µ µ (c) | Report | 22 | |
| 1.4.5 | >25 µ µ (c) | Report | 15 | |
| 1.4.6 | >30 µ µ (c) | Report | 10 | |
| 2 | Composition | |||
| 2.1 | Total Acidity, mg KOH/gm | 0.015 Max. | ASTM D 3242 | 0.009 |
| 2.2 | Aromatic Hydrocarbon Types | |||
| 2.2.1 or | Aromatics % v/v | 25 Max. | IP156/ASTMD1319 | 18.5 |
| 2.2.2 | Total Aromatics % v/v | 26.5 Max. | IP 436/ASTM D 6379 | 18.5 |
| 2.3 | Sulphur. Total % m/m | 0.3 Max. | ASTM D 4294 | 0.25 |
| Sulphur Mercaptan % m/m | 0.003 Max. | ASTM D 3227 | 0.002 | |
| 2.4 | ||||
| Or | Doctor Test | Doctor negative | IP 30 | |
| 2.5 | ||||
| 2.6 | Refining Component, at the Point of manufacture | |||
| 2.6.1 | 1. Hydro processed component. % v/v Report | |||