RT Journal Article
T1 Solvent selection and optimisation of the liquid-liquid extraction of volatile fatty acids from the aqueous stream of the HTL-WO process for the production of aviation biofuels
A1 Martín Gutiérrez, Diego
A1 Barras, David
A1 Suárez Rodríguez, Pablo
A1 Biller, Patrick
A1 Schuck, Carolin Eva
A1 Águeda Maté, Vicente Ismael
A1 Larriba Martínez, Marcos
PB Elsevier
YR 2026
FD 2026-01-19
LK https://hdl.handle.net/20.500.14352/130870
UL https://hdl.handle.net/20.500.14352/130870
LA eng
NO Diego Martín-Gutiérrez, David Barras, Pablo Suárez-Rodríguez, Patrick Biller, Carolin Eva Schuck, Vicente Ismael Águeda, Marcos Larriba, Solvent selection and optimisation of the liquid-liquid extraction of volatile fatty acids from the aqueous stream of the HTL-WO process for the production of aviation biofuels, Separation and Purification Technology, Volume 390, 2026, 136923, ISSN 1383-5866, https://doi.org/10.1016/j.seppur.2026.136923.
NO Hydrothermal liquefaction (HTL) is a thermochemical process used to produce advanced biofuels. Besides bio-crude oil, HTL generates an aqueous stream containing organic compounds that can be decreased in concentration or transformed by wet oxidation (WO), producing water rich in volatile fatty acids (VFAs) and ammonium. This study explores liquid-liquid extraction to recover and valorise VFAs from the HTL-WO aqueous stream. Using molecular simulation with the COSMO-RS method, six terpenes and four conventional organic solvents were selected for experimental investigation. First, synthetic aqueous mixtures of VFAs were tested, followed by a real aqueous sample obtained from the HTL-WO of a straw and manure mixture. Optimisation of operating variables for acetic and propionic acid extraction was carried out. Using geraniol, citronellol, verbenone, and methyl isobutyl ketone (MIBK) as solvents, with a solvent-to-feed ratio (S/F) of 2, extraction temperature of 303.2 K, and water pH of 2, the recovery of VFAs was maximised in the real stream. Extraction yields exceeded 50% for acetic acid and 80% for propionic acid in both batch and continuous-parallel extraction using a packed column. Under the same conditions, cross-current multistage extraction was studied. Finally, counter-current extraction in a column was simulated with the Kremser method, showing that over 99% of VFAs in the aqueous stream could be extracted in five stages. These results demonstrate the effectiveness of terpenes as green solvents for VFA recovery in HTL-WO process water.
NO Comisión Europea
NO Comunidad Autónoma de Madrid
DS Docta Complutense
RD 19 mar 2026