| Parameter | Products |
| Temperature, °C | 380 | 360 | Pressure, MPa | 5.5 | 5,5 | LHSV, h−1 | 1 | 1 | H2/feed, L/Lh | 1034 | 511 | 1054 | 503 | CTO content in feed, % vol. | 20 | Hydrocarbons C1–C5, % wt. | 1,27 | 1,14 | 0,68 | 0,44 | Propane, % wt. | 0,49 | 0,44 | 0,53 | 0,27 | CO content, % wt. | 0,28 | 0,99 | 0,22 | 0,60 | CO2 content, % wt. | 2,57 | 2,93 | 1,66 | 0,67 | Liquid product, % wt. | 95,12 | 94,52 | 95,72 | 96,64 | Reaction water, % wt. | 2,31 | 2,55 | 2,62 | 1,38 | Sulphur content, mg/kg | 58.8 | 100.5 | 218.4 | 473.4 | Acid value, mg KOH/g | 0.14 | 0.17 | 0.05 | 0.07 | Nitrogen content, mg/kg | 0.58 | 0.8 | 1 | 1.2 | Density at 15°C. kg/m3 | 831 | 837 | 830 | 829 | Monoaromatics, % wt. | 21.2 | 24.5 | 16.8 | 16.8 | Σ Di- and Tri-aromatics, % wt. | 2.3 | 2.9 | 1.4 | 1.5 | Cetane number | 56.6 | 56.3 | 59 | 59 |
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