Oleaginous yeast platform for producing biofuels via co-solvent hydrothermal liquefaction

Table 3 Analysis of water-soluble aqueous phase co-products (ACP)

HTL experimental conditions and reactor type	N and P, expressed in mg L⁻¹					NVR, %	TOC, mg L⁻¹
HTL experimental conditions and reactor type	NO₃ and NO₂	NH₃–N	KN	Total P	pH	NVR, %	TOC, mg L⁻¹
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

All HTL runs were performed for 30 min residence time
N nitrogen, KN Kjeldahl nitrogen, NVR non-volatile residue, TP total phosphorous, TOC total organic carbon

ISSN: 2731-3654