Hydrothermal liquefaction of Elaeis guineensis trunks

Lessons learned from a case study in Guatemala

Journal Article (2023)
Author(s)

L. Cutz IJchajchal (TU Delft - Large Scale Energy Storage)

H.A. Maldonado de León (TU Delft - BT/Bioprocess Engineering)

Gamaliel Zambrano (Universidad del Valle de Guatemala)

Majd Al-Naji (Technical University of Berlin)

Wiebren De de Jong (TU Delft - Large Scale Energy Storage)

Research Group
Large Scale Energy Storage
Copyright
© 2023 L. Cutz, H.A. Maldonado de León, Gamaliel Zambrano, Majd Al-Naji, W. de Jong
DOI related publication
https://doi.org/10.1016/j.indcrop.2023.117552
More Info
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Publication Year
2023
Language
English
Copyright
© 2023 L. Cutz, H.A. Maldonado de León, Gamaliel Zambrano, Majd Al-Naji, W. de Jong
Research Group
Large Scale Energy Storage
Volume number
206
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Abstract

The oil palm industry has been under public scrutiny during the last decades due to environmental and social issues related to its practices. Oil palm (Elaeis guineensis Jacq.) trunks (OPTs) are of special interest as they are left idle in the field after the replanting process which is performed every 25 years. This common practice results in harvesting challenges, phytosanitary risks, and a loss of bioenergy potential. Due to their high moisture content and fibrous nature, OPTs present a problem for traditional conversion processes that require a dry and homogeneous material. This study evaluates the feasibility of converting OPTs into a bio-crude oil and biochar to increase the sustainability of the oil palm sector. To date, research efforts have primarily focused on hydrothermal liquefaction (HTL) of OPT without catalysts, resulting in a limited understanding of the potential of OPTs. Thus, the main novelty of this work is the evaluation of the effects of catalyst dosage (0–5 wt%) on the bio-oil yield, reaction temperature (260–300C), and residence time (15–60 min) using a half-fraction experimental design methodology. For this, OPTs extracted from two plantations in Guatemala were used. The maximum bio-oil yield (26.77 ± 3.60 wt%) was found at 260C for 15 min and 5 wt% catalyst with a high heating value (HHV) of 19.29 ± 1.33 MJ kg−1. Nonetheless, the bio-oils produced without a catalyst at 300C and 15 min have higher HHV (27.63 ± 1.35 MJ kg−1) and are similar to Diesel fuel based on their H/C and O/C ratio. These results indicate that there is a potential trade-off between the bio-crude oil mass yield and HHV when using the catalyst.