Characterization of an AA9 LPMO from Thielavia australiensis, TausLPMO9B, under industrially relevant lignocellulose saccharification conditions

纤维素 多糖 纤维素酶 化学 水解 基质(水族馆) 木聚糖 半纤维素 甲壳素 生物化学 生物 生态学 壳聚糖
作者
Federica Calderaro,Mesut Keser,Michiel Akeroyd,Loes E. Bevers,Vincent G. H. Eijsink,Anikó Várnai,M. A. Berg
出处
期刊:Biotechnology for Biofuels [Springer Nature]
卷期号:13 (1) 被引量:29
标识
DOI:10.1186/s13068-020-01836-3
摘要

Abstract Background The discovery of lytic polysaccharide monooxygenases (LPMO) has changed our perspective on enzymatic degradation of plant biomass. Through an oxidative mechanism, these enzymes are able to cleave and depolymerize various polysaccharides, acting not only on crystalline substrates such as chitin and cellulose, but also on other polysaccharides, such as xyloglucan, glucomannan and starch. Despite their widespread use, uncertainties related to substrate specificity and stereospecificity, the nature of the co-substrate, in-process stability, and the nature of the optimal reductant challenge their exploitation in biomass processing applications. Results In this work, we studied the properties of a novel fungal LPMO from the thermophilic fungus Thielavia australiensis, Taus LPMO9B. Heterologous expression of Taus LPMO9B in Aspergillus niger yielded a glycosylated protein with a methylated N-terminal histidine showing LPMO activity. High sequence identity of the AA9 domain to that of Mt LPMO9B (MYCTH_80312) from Myceliophthora thermophila (84%) indicated strictly C1-oxidizing activity on cellulose, which was confirmed experimentally by the analysis of products released from cellulose using HPAEC. The enzyme was stable and active at a pH ranging from 4 to 6, thus matching the conditions commonly used in industrial biomass processing, where a low pH (between 4 and 5) is used due to the pH-optima of commercial cellulases and a desire to limit microbial contamination. Conclusion While the oxidative cleavage of phosphoric acid swollen cellulose (PASC) by Taus LPMO9B was boosted by the addition of H 2 O 2 as a co-substrate, this effect was not observed during the saccharification of acid pretreated corn stover. This illustrates key differences between the lab-scale tests with artificial, lignin-free substrates and industrial settings with lignocellulosic biomass as substrate.
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