The effect of CO2 and increased initial pressure on hydrothermal liquefaction for the production of high value fatty acids

• Study on the effect of CO 2 , N 2 and pressure on HtL. • CO 2 creates a reactive medium that drives carboxylation reactions in HTL. • CO 2 enhanced VFA production, yielding 2 g/ L acetic acid. • Hydrochar HHV peaked at 35 MJ/ kg at 350 °C. • Pressure significantly affected VFA/FAME yields at ≤ 350 °C. Hydrothermal liquefaction (HTL) of waste biomasses has been widely studied, yet the influence of the reaction atmosphere on carboxylation chemistry is often overlooked. In this study, HTL of anise ( Pimpinella anisum L.) waste was performed at 310, 350 and 390 °C solely with air (no added pressure), under N 2 with and without increased initial pressure, solely with CO 2 , and with combined N 2 /CO 2 and increased pressure. The aim was to assess how total pressure and gas/ atmosphere composition affect product distribution and high‑value compound formation. Dissolved CO 2 was found to acidify the aqueous phase and participate in carboxylation reactions that convert hydrolysis intermediates into volatile fatty acids (VFAs), as measured via a GC-BID in the form of fatty‑acid methyl esters (FAMEs). Chemical oxygen demand (COD) in the aqueous phase increased from 10,000 to 30000 mg/ L and was consistently higher under CO 2 . Hydrochar higher heating value peaked at approximately 35 MJ/ kg at 350 °C and declined at 390 °C. CO 2 ‑rich runs exhibited an order‑of‑magnitude increase in VFA production, with acetic‑acid concentrations up to 2 g/ L. FAMEs formation increased with temperature; at 390 °C the combined N 2 / CO 2 system produced methyl hexanoate concentrations of approx. 13 g/ L and methyl octanoate 11.9 g/ L, more than threefold higher than in single‑gas or non‑pressurized runs. One‑way ANOVA revealed that pressure significantly influenced VFA and FAME yields at 310–350 °C but this effect diminished at 390 °C. These results highlight the importance of optimizing both gas atmosphere and pressure in HTL processes and demonstrate that reactive CO 2 atmospheres can drive carboxylation pathways leading to higher yields of valuable fatty acids.

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Journal
Fuel
Published
2026-01-08
DOI
https://doi.org/10.1016/j.fuel.2026.138317
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
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article

The effect of CO2 and increased initial pressure on hydrothermal liquefaction for the production of high value fatty acids

Dimitris Liakos, Stergios Vakalis, Maria Iosifidou
Fuel
Thermochemical Biomass Conversion Processes
article

The effect of CO2 and increased initial pressure on hydrothermal liquefaction for the production of high value fatty acids

Dimitris Liakos, Stergios Vakalis, Maria Iosifidou
article en

Abstract

• Study on the effect of CO 2 , N 2 and pressure on HtL. • CO 2 creates a reactive medium that drives carboxylation reactions in HTL. • CO 2 enhanced VFA production, yielding 2 g/ L acetic acid. • Hydrochar HHV peaked at 35 MJ/ kg at 350 °C. • Pressure significantly affected VFA/FAME yields at ≤ 350 °C. Hydrothermal liquefaction (HTL) of waste biomasses has been widely studied, yet the influence of the reaction atmosphere on carboxylation chemistry is often overlooked. In this study, HTL of anise ( Pimpinella anisum L.) waste was performed at 310, 350 and 390 °C solely with air (no added pressure), under N 2 with and without increased initial pressure, solely with CO 2 , and with combined N 2 /CO 2 and increased pressure. The aim was to assess how total pressure and gas/ atmosphere composition affect product distribution and high‑value compound formation. Dissolved CO 2 was found to acidify the aqueous phase and participate in carboxylation reactions that convert hydrolysis intermediates into volatile fatty acids (VFAs), as measured via a GC-BID in the form of fatty‑acid methyl esters (FAMEs). Chemical oxygen demand (COD) in the aqueous phase increased from 10,000 to 30000 mg/ L and was consistently higher under CO 2 . Hydrochar higher heating value peaked at approximately 35 MJ/ kg at 350 °C and declined at 390 °C. CO 2 ‑rich runs exhibited an order‑of‑magnitude increase in VFA production, with acetic‑acid concentrations up to 2 g/ L. FAMEs formation increased with temperature; at 390 °C the combined N 2 / CO 2 system produced methyl hexanoate concentrations of approx. 13 g/ L and methyl octanoate 11.9 g/ L, more than threefold higher than in single‑gas or non‑pressurized runs. One‑way ANOVA revealed that pressure significantly influenced VFA and FAME yields at 310–350 °C but this effect diminished at 390 °C. These results highlight the importance of optimizing both gas atmosphere and pressure in HTL processes and demonstrate that reactive CO 2 atmospheres can drive carboxylation pathways leading to higher yields of valuable fatty acids.

FuelVol. 413
National Technical University of Athens (GR), University of the Aegean (GR)
Clean water and sanitation
Openalex Percentile: Top 96%
Thermochemical Biomass Conversion Processes
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