From: Oleaginous yeast platform for producing biofuels via co-solvent hydrothermal liquefaction
HTL experimental conditions and reactor type | N and P, expressed in mg L−1 |  | NVR, % | TOC, mg L−1 | |||
---|---|---|---|---|---|---|---|
NO3 and NO2 | NH3–N | KN | Total P | pH | |||
Non-catalytic, 300 °C, 2-L Parr | 0.10 | 659 | 1220 | 1254 | 3.74 | 16.28 | 4281 |
Catalytic, 300 °C, 2-L Parr | 0.24 | 502 | 979 | 1335 | 3.92 | 10.34 | 4611 |
Non-catalytic, co-solvent 240 °C, 2-chamber | 0.20 | 521 | 927 | 1722 | 3.83 | 1.46 | 5091 |
Catalytic, co-solvent 240 °C, 2-chamber | 0.22 | 438 | 800 | 1794 | 4.11 | 1.26 | 5643 |