TY - JOUR
T1 - Two-stage alkaline hydrothermal liquefaction of wood to biocrude in a continuous bench-scale system
AU - Sintamarean, Iulia-Maria
AU - Grigoras, Ionela
AU - Jensen, Claus Uhrenholt
AU - Toor, Saqib Sohail
AU - Pedersen, Thomas Helmer
AU - Rosendahl, Lasse Aistrup
PY - 2017/11
Y1 - 2017/11
N2 - Feedstock pumpability is one of the main obstacles for continuous processing of biomass through hydrothermal liquefaction (HTL), due to their tendency to form heterogeneous slurries. In this work, a novel strategy is proposed to ensure lignocellulosic feed pumpability in HTL processing, even while applying elevated biomass loadings. In the first stage, a pumpable feed is prepared by an alkaline treatment of coarse wood chips at 180 °C, 120-min reaction time, and 0.35 NaOH-to-wood ratio. In a subsequent stage, the treated feedstock is converted into a biocrude in a continuously operated 20 kg/h scale unit. In total, 100 kg of wood paste with 25% dry matter is processed at 400 °C and 30 MPa, demonstrating the usefulness of this two-stage liquefaction strategy. An additional advantage liquefaction of such pretreated wood shows increased biocrude yields with approximately 10% compared to the case where non-pretreated wood is liquefied.
AB - Feedstock pumpability is one of the main obstacles for continuous processing of biomass through hydrothermal liquefaction (HTL), due to their tendency to form heterogeneous slurries. In this work, a novel strategy is proposed to ensure lignocellulosic feed pumpability in HTL processing, even while applying elevated biomass loadings. In the first stage, a pumpable feed is prepared by an alkaline treatment of coarse wood chips at 180 °C, 120-min reaction time, and 0.35 NaOH-to-wood ratio. In a subsequent stage, the treated feedstock is converted into a biocrude in a continuously operated 20 kg/h scale unit. In total, 100 kg of wood paste with 25% dry matter is processed at 400 °C and 30 MPa, demonstrating the usefulness of this two-stage liquefaction strategy. An additional advantage liquefaction of such pretreated wood shows increased biocrude yields with approximately 10% compared to the case where non-pretreated wood is liquefied.
KW - Lignocellulosic
KW - Feedstock pumpability
KW - Alkaline pretreatment
KW - Biocrude
U2 - 10.1007/s13399-017-0247-9
DO - 10.1007/s13399-017-0247-9
M3 - Journal article
SN - 2190-6815
VL - 7
SP - 425
EP - 435
JO - Biomass Conversion and Biorefinery
JF - Biomass Conversion and Biorefinery
IS - 4
ER -