Aqueous acetone organosolv
fractionation of the lignocellulosic
biomass using a batchwise operation is a robust technology option
to produce cellulose, sugars, and lignin. Such fractionation is typically
characterized by fast solubilization of most of the lignin and hemicellulose
sugars in the early stages of the process, gradually followed by slower
removal of the remaining, more recalcitrant part at later stages.
As a result, most of the solubilized sugars and lignin experience
a relatively long residence time in the hot liquor, leading to undesired
sugar degradation and lignin depolymerization-condensation reactions.
A lab-scale, semicontinuous countercurrent flow fractionation design
is presented here as a solution to this issue and studied as an intermediate
step toward an envisioned scaled-up design involving a series of percolation
reactors coupled for liquid exchange. Counter-current semicontinuous
processing (SCP) reduces the overall residence time of the solubilized
sugars and lignin. While even slightly improving on fractionation
performance, i.e., sugar and lignin solubilization, most importantly,
SCP resulted in less sugar degradation and more hemicellulose oligomers
compared to the simple batch process. SCP lignin proved to be of higher
quality with increased β-O-4 content and, consequently, a higher
abundance of lignin aliphatic hydroxyl groups, less formation of Hibbert
ketones, and reduced condensation. The more native nature of the lignin
is reflected in its improved reactivity in reductive partial depolymerization
to lower molar mass and dispersity lignin building blocks. Overall,
SCP thus provides a powerful and scalable strategy for improving the
efficiency and effectiveness of aqueous acetone organosolv fractionation.