| Parameter | Products |
| Temperature, °C | 380 | 360 | Pressure, MPa | 5.5 | 5,5 | LHSV, h−1 | 1 | 1 | H2/feed, L/Lh | 1030 | 541 | 1034 | 531 | CTO content in feed, % vol. | 20 | Hydrocarbons C1–C5, % wt. | 0,98 | 0,48 | 0,55 | 0,37 | Propane, % wt. | 0,38 | 0,33 | 0,69 | 0,46 | CO content, % wt. | 0,65 | 0,32 | 0,68 | 0,48 | CO2 content, % wt. | 0,38 | 1,25 | 2,07 | 1,40 | Liquid product, % wt. | 96.74 | 97.73 | 96.00 | 95.67 | Reaction water, % wt. | 0.86 | 1.02 | 1.93 | 2.93 | Sulphur content, mg/kg | 128.8 | 308.3 | 114.2 | 38.2 | Acid value, mg KOH/g | 0.15 | 0.03 | 0.11 | 0.04 | Nitrogen content, mg/kg | 2.4 | 2.8 | 1.5 | 1.8 | Density at 15°C. kg/m3 | 839 | 835 | 832 | 833 | Monoaromatics, % wt. | 25 | 23.2 | 20.7 | 21.4 | Σ Di- and Tri-aromatics, % wt. | 2.9 | 2.6 | 2 | 2 | Cetane number | 55 | 56.4 | 55.8 | 56.7 |
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