Abstract

Micro- and nanosize lignin has recently gained interest due to its improved properties compared to standard lignin available today. As the second most abundant biopolymer after cellulose, lignin is readily available but used for rather low-value applications. Applications for lignin in micro- to nanoscale however, ranging from improvement of mechanical properties of polymer nanocomposites, have bactericidal and antioxidant properties and impregnations to hollow lignin drug carriers for hydrophobic and hydrophilic substances. This research represents a whole biorefinery process chain and compares different precipitation setups to produce submicron lignin particles from lignin containing an organosolv pretreatment extract from wheat straw. A batch precipitation in a stirred vessel was compared with continuous mixing of extract and antisolvent in a T-fitting and mixing in a T-fitting followed by a static mixer. The precipitation in the combination of T-fitting and static mixer with improved precipitation parameters yields the smallest particle size of around 100 nm. Furthermore, drying of particles did not influence the particle sizes negatively by showing decreased particle diameters after the separation process.

Highlights

  • Lignocellulosic biomass residues are estimated to exceed 2 × 1011 t/year worldwide and offers a vast source for lignin [1]

  • Three different types of lignins can be distinguished: softwood lignins are comprised almost solely of coniferyl alcohol, hardwood lignins of both coniferyl and sinapyl alcohol, and grass lignins of all three types [6]

  • Extract and antisolvent in a T-fitting followed by a static mixer

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Summary

Introduction

Lignocellulosic biomass residues are estimated to exceed 2 × 1011 t/year worldwide and offers a vast source for lignin [1]. The major part of the lignin is used as an energy source. Considering a lignocellulose biorefinery producing bioethanol, only around 40% of the produced lignin is needed to cover the thermal energy demand [2,3]. 60% of the generated lignin is available to maximize valorization in addition to the valorization of the carbohydrate fractions. This increased valorization is necessary to improve the utilization of the entire biomass and to enhance the economical value [4]. The high complexity and inhomogeneity of the lignin structure is, in many cases, even further increased by currently applied pretreatment technologies and adds additional challenges for lignin’s downstream processing and valorization [7,8]

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