TY - JOUR
T1 - Cellulosic glycols
T2 - an integrated process concept for lignocellulose pretreatment and hydrogenolysis
AU - te Molder, Thimo D.J.
AU - Kersten, Sascha R.A.
AU - Lange, Jean Paul
AU - Ruiz, M. Pilar
N1 - Funding Information:
The authors thank Shell Global Solutions International BV for funding this research, and Benno Knaken, Johan Agterhorst, Ronald Borst, and Erna Fränzel‐Luiten for the technical support.
Publisher Copyright:
© 2021 The Authors. Biofuels, Bioproducts and Biorefining published by Society of Industrial Chemistry and John Wiley & Sons Ltd.
PY - 2021/11/1
Y1 - 2021/11/1
N2 - Lignocellulose is the most abundant source of saccharides and it is therefore a promising feedstock for glycols, such as ethylene-glycol, via catalytic hydrogenolysis of the polysaccharides that it contains. However, this catalytic hydrogenolysis step is hampered by the presence of lignin and other biomass contaminants, such as ash, which need to be removed in a pretreatment step. We propose an organosolv-like pre-treatment that can delignify and de-ash lignocellulose to a level that allows it to be upgraded to glycol with comparable yields to pure cellulose under demanding hydrogenolysis conditions. This work identifies the main design constraints of the integrated process and provides an initial experimental validation of it. Pretreatment of biomass in water/ethanol/acetic acid solutions at 180–200 °C can reduce the lignin content of the solid residue to ≤6 wt%. The addition of an organic acid, such as acetic acid, appears important to improve the removal of the recalcitrant Ca2+, which is a known inhibitor of the tungstate catalyst typically used in this process. The pretreatment medium is designed to use the by-product(s) of the process as organic solvent, to reduce the need for fresh solvent input. However, the process still needs a high solvent recovery (between 93.5 and 99.9 wt%). This can be achieved by selecting volatile component as organic solvent, as it allows recovery by evaporation from the dissolved lignin and ashes.
AB - Lignocellulose is the most abundant source of saccharides and it is therefore a promising feedstock for glycols, such as ethylene-glycol, via catalytic hydrogenolysis of the polysaccharides that it contains. However, this catalytic hydrogenolysis step is hampered by the presence of lignin and other biomass contaminants, such as ash, which need to be removed in a pretreatment step. We propose an organosolv-like pre-treatment that can delignify and de-ash lignocellulose to a level that allows it to be upgraded to glycol with comparable yields to pure cellulose under demanding hydrogenolysis conditions. This work identifies the main design constraints of the integrated process and provides an initial experimental validation of it. Pretreatment of biomass in water/ethanol/acetic acid solutions at 180–200 °C can reduce the lignin content of the solid residue to ≤6 wt%. The addition of an organic acid, such as acetic acid, appears important to improve the removal of the recalcitrant Ca2+, which is a known inhibitor of the tungstate catalyst typically used in this process. The pretreatment medium is designed to use the by-product(s) of the process as organic solvent, to reduce the need for fresh solvent input. However, the process still needs a high solvent recovery (between 93.5 and 99.9 wt%). This can be achieved by selecting volatile component as organic solvent, as it allows recovery by evaporation from the dissolved lignin and ashes.
KW - Ethylene glycol
KW - Hydrogenolysis
KW - Lignocellulosic biomass
KW - Organosolv
KW - Pretreatment
KW - Solvent recovery
KW - UT-Hybrid-D
UR - http://www.scopus.com/inward/record.url?scp=85110102334&partnerID=8YFLogxK
U2 - 10.1002/bbb.2269
DO - 10.1002/bbb.2269
M3 - Article
AN - SCOPUS:85110102334
SN - 1932-104X
VL - 15
SP - 1725
EP - 1736
JO - Biofuels, Bioproducts and Biorefining
JF - Biofuels, Bioproducts and Biorefining
IS - 6
ER -