EventsThe 1st International Online Conference on Recycling
Published
This submission belongs to the session S1. Advances in Recycling Technologies of the event The 1st International Online Conference on Recycling
Published date
02 Sep, 2026
Academic Editor
author-avatarHuijuan Dong
Citation
Paulo Bonjour, Alexandre Jorge, Jorge Pereira, Extraction and Recovery of High-Value Chemical Compounds from Aqueous Phase Pyrolysis Bio-Oil, in Proceedings of The 1st International Online Conference on Recycling, 7 September–8 September 2026, MDPI: Basel, Switzerland
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Extraction and Recovery of High-Value Chemical Compounds from Aqueous Phase Pyrolysis Bio-Oil

Paulo Bonjour 1
Alexandre Jorge 1
image
1. CERES, Department of Chemical Engineering, University of Coimbra, 3030-790 Coimbra, Portugal
Abstract

Pyrolysis bio-oil is a complex mixture rich in oxygenated compounds with significant commercial potential. Among its fractions, the bio-oil aqueous phase (BOAP) contains valuable phenolics, furanics, alcohols, and carboxylic acids that can be recovered and valorized. This study investigates liquid–liquid extraction (LLE) as a strategy for recovering value-added chemicals from Eucalyptus globulus BOAP using both conventional and bio-based solvents. Solvent screening was performed with toluene, heptane, hexane, ethyl acetate (EA), cyclopentyl methyl ether (CPME), 2-methyltetrahydrofuran (2-MTHF), turpentine, and octanoic acid. A systematic thermodynamic modeling framework was applied to select the most suitable model for process simulation. A representative BOAP mixture was implemented in Aspen Plus and validated against experimental equilibrium data at 293.15 K and 101.3 kPa. Subsequently, techno-economic assessment (TEA) was conducted to evaluate process performance. The results showed that aromatic and moderately polar solvents, particularly toluene, CPME, and 2-MTHF, achieved extraction efficiencies exceeding 80% for phenolic and furanic compounds, whereas non-polar aliphatic solvents such as hexane and heptane exhibited lower extraction capacities. Carboxylic acid extraction increased with solvent carbon chain length, while methanol remained predominantly in the aqueous phase. Root mean square error (RMSE) analysis identified NRTL-HOC as the most reliable thermodynamic model, with deviations ranging from 0.07 to 0.19, outperforming COSMO-RS and COSMO-SAC approaches. TEA results revealed a strong influence of solvent selection on process economics. EA provided the lowest minimum selling price (MSP) of approximately 2,525 USD/ton, followed by 2-MTHF, while CPME and hexane were less economically attractive due to higher operating costs. Overall, bio-based ethers demonstrated competitive extraction performance, highlighting their potential as sustainable alternatives for BOAP valorization.

Keywords
Eucalyptus globulus
Techno-economic assessment
liquid-liquid extraction
Simulation
Thermodynamics
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