| Parameter | Products |
| Temperature, °C | 380 | 360 | 380 | Pressure, MPa | 5.5 | LHSV, h−1 | 1 | H2/feed, L/Lh | 965 | 504 | 970 | 525 | 985 | 544 | CTO content in feed, % vol. | 20 | 30 | Hydrocarbons C1–C5, % wt. | 1,42 | 0,93 | 0,57 | 1,19 | 1,19 | 0,45 | Propane, % wt. | 0,60 | 0,40 | 0,24 | 0,51 | 0,51 | 0,32 | CO content, % wt. | 0,84 | 0,55 | 0,34 | 0,71 | 0,70 | 1,27 | CO2 content, % wt. | 0,28 | 0,18 | 0,11 | 0,23 | 0,23 | 0,96 | Liquid product, % wt. | 96.00 | 97.21 | 98.05 | 97.36 | 96.64 | 95.85 | Reaction water, % wt. | 0.86 | 0.73 | 0.69 | 1.07 | 0.73 | 1.15 | Sulphur content, mg/kg | 239 | 120 | 176 | 291 | 84 | 97 | Acid value, mg KOH/g | 0.01 | 0.01 | 0.04 | 0.02 | 0.02 | 0.04 | Nitrogen content, mg/kg | 1 | 1.2 | 1.5 | 1.6 | 0.8 | 0.9 | Density at 15°C. kg/m3 | 801 | 813 | 814 | 814 | 826 | 830 | Monoaromatics, % wt. | 16.5 | 19.6 | 20 | 21.2 | 19.8 | 20.4 | Σ Di- and Tri-aromatics, % wt. | 1.66 | 3.32 | 2.68 | 2.39 | 3.23 | 3.99 | Cetane number | 56,5 | 55 | 53,5 | 54 | 57 | 56,8 |
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