Abstract

The extraction and characterization of defined and carboxyl-rich oligomeric lignin fragments with narrow molecular weight distribution is presented herein. With regard to the well-known pulp bleaching process, oxidative lignin depolymerization was investigated using hydrogen peroxide in an aqueous alkaline solution (i.e., at T = 318 K, t = 1 h) and subsequent selective fractionation with a 10/90 (v/v) acetone/water mixture. While the weight average molecular weight (MW) of lignin in comparison to the starting material was reduced by 82% after oxidation (T = 318 K, t = 1 h, clignin = 40 g L−1, cH2O2 = 80 g L−1, cNaOH = 2 mol L−1) and subsequent solvent fractionation (T = 298 K, t = 18 h, ccleavage product = 20 g L−1), the carboxyl group (–COOH) content increased from 1.29 mmol g−1 up to 2.66 mmol g−1. Finally, the successful scale-up of this whole process to 3 L scale led to gram amounts (14% yield) of oligomeric lignin fragments with a MW of 1607 g mol−1, a number average molecular weight (MN) of 646 g mol−1, a narrow polydispersity index of 3.0, and a high –COOH content of 2.96 mmol g−1. Application of these oligomeric lignin fragments in epoxy resins or as adsorbents is conceivable without further functionalization.

Highlights

  • After cellulose, lignin is the second most abundant biopolymer on earth and the only highly available renewable source for aromatic hydrocarbons [1]

  • The oxidative depolymerization of Kraft lignin with H2 O2 in an aqueous alkaline solution followed by solvent fractionation (10/90 (v/v) water/acetone) of the oligomeric fragments was successfully demonstrated

  • This process yielded carboxyl-rich oligomeric lignin fragments with lower molecular weights and narrower molecular weight distribution compared to the starting material

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Summary

Introduction

Lignin is the second most abundant biopolymer on earth and the only highly available renewable source for aromatic hydrocarbons [1]. 50 Mt lignin worldwide is generated from lignocellulosic biomass as a low-value byproduct in pulp and paper mills from the Kraft process [2,3,4]. This so-called Kraft lignin (KL) is mainly (98%) burned to generate heat and power for the pulping process and for the supply of renewable energy to the grid. Hu et al [2] stated that a future lignin biorefinery can only be realized if a stable and cheap feed supply can be realized, e.g., by upgrading a Kraft mill

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