Research Article
Filter Cake Oil-Wax as Raw Material for the Production of Biodiesel: Analysis of the Extraction Process and the Transesterification Reaction
Table 1
Fatty acid concentrations and acid values of the extracts obtained by Soxhlet, OSE, UAE, and SFE.
| | Fatty acid composition (mg/kg) | Acid value | Palmitic (C16:0) | Stearic (C18:0) | Oleic (C18:1) | Linoleic (C18:2) | Linolenic (C18:3) |
| Soxhlet | 11.5 | 24.5 | 2.38 | 5.28 | 6.40 | 6.55 | OSE (3 : 1) | 3.3 | 5.6 | n.d | 0.4 | 1.6 | 15.93 | OSE (5 : 1) | 9.4 | 15.7 | 7.5 | 17.6 | 15.7 | 12.18 | OSE (7 : 1) | 10.7 | 20.2 | n.d | n.d | 5.8 | 12.19 | OSE (9 : 1) | 12.1 | 27.3 | n.d | 0.8 | 3.9 | 13.57 | UAE () | 7.6 | 17.9 | n.d | 0.1 | 2.5 | 8.46 | UAE () | 3.40 | 8.96 | 0.4 | 0.5 | 1.9 | 4.43 | SFE CO2 | | | | | | | 200 bar/35°C | 75.09 | 38.79 | 143.07 | 160.66 | 21.65 | 19.35 | 200 bar/55°C | 63.66 | 44.55 | 144.16 | 131.66 | 6.8 | 26.02 | 400 bar/35°C | 106.30 | 77.10 | 226.59 | 205.29 | 10.85 | 22.21 | 400 bar/55°C | 83.69 | 79.19 | 175.37 | 162.46 | 13.7 | 24.45 | SFE CO2/methanol | | | | | | | 200 bar/35°C | 14.51 | 23.54 | 5.31 | 4.44 | 2.65 | 29.44 | 200 bar/55°C | 15.89 | 26.58 | 6.00 | 5.01 | 2.70 | 22.41 | 400 bar/35°C | 23.63 | 37.51 | 5.64 | 5.53 | 3.87 | 11.58 | 400 bar/55°C | 25.13 | 43.65 | 5.36 | 5.72 | 3.47 | 20.57 |
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