Promoting enzymatic hydrolysis of lignocellulosic biomass by inexpensive soy protein

dc.contributor.authorLuo, Xiaolinen
dc.contributor.authorLiu, Jingen
dc.contributor.authorZheng, Peitaoen
dc.contributor.authorLi, Mengen
dc.contributor.authorZhou, Yangen
dc.contributor.authorHuang, Liulianen
dc.contributor.authorChen, Lihuien
dc.contributor.authorShuai, Lien
dc.contributor.departmentSustainable Biomaterialsen
dc.date.accessioned2019-03-18T12:30:05Zen
dc.date.available2019-03-18T12:30:05Zen
dc.date.issued2019-03-13en
dc.date.updated2019-03-17T04:20:01Zen
dc.description.abstractBackground Liquid hot water (LHW) pretreatment has been considered as one of the most industrially viable and environment-friendly methods for facilitating the transformation of lignocelluloses into biofuels through biological conversion. However, lignin fragments in pretreatment hydrolysates are preferential to condense with each other and then deposit back onto cellulose surface under severe conditions. Particularly, lignin tends to relocate or redistribute under high-temperature LHW pretreatment conditions. The lignin residues on the cellulose surface would result in significant nonproductive binding of cellulolytic enzymes, and therefore negatively affect the enzymatic conversion (EC) of glucan in pretreated substrates. Although additives such as bovine serum albumin (BSA) and Tween series have been used to reduce nonproductive binding of enzymes through blocking the lignin, the high cost or non-biocompatibility of these additives limits their potential in industrial applications. Results Here, we firstly report that a soluble soy protein (SP) extracted from inexpensive defatted soy powder (DSP) showed excellent performance in promoting the EC of glucan in LHW-pretreated lignocellulosic substrates. The addition of the SP (80 mg/g glucan) could readily reduce the cellulase (Celluclast 1.5 L®) loading by 8 times from 96.7 to 12.1 mg protein/g glucan and achieve a glucan EC of 80% at a hydrolysis time of 72 h. With the same cellulase (Celluclast 1.5 L®) loading (24.2 mg protein/g glucan), the ECs of glucan in LHW-pretreated bamboo, eucalyptus, and Masson pine substrates increased from 57%, 54% and 45% (without SP) to 87%, 94% and 86% (with 80 mg SP/g glucan), respectively. Similar effects were also observed when Cellic CTec2, a newer-generation cellulase preparation, was used. Mechanistic studies indicated that the adsorption of soluble SP onto the surface of lignin residues could reduce the nonproductive binding of cellulolytic enzymes to lignin. The cost of the SP required for effective promotion would be equivalent to the cost of 2.9 mg cellulase (Celluclast 1.5 L®) protein (or 1.2 FPU/g glucan), if a proposed semi-simultaneous saccharification and fermentation (semi-SSF) model was used. Conclusions Near-complete saccharification of glucan in LHW-pretreated lignocellulosic substrates could be achieved with the addition of the inexpensive and biocompatible SP additive extracted from DSP. This simple but remarkably effective technique could readily contribute to improving the economics of the cellulosic biorefinery industry.en
dc.description.versionPublished versionen
dc.format.mimetypeapplication/pdfen
dc.identifier.citationBiotechnology for Biofuels. 2019 Mar 13;12(1):51en
dc.identifier.doihttps://doi.org/10.1186/s13068-019-1387-xen
dc.identifier.urihttp://hdl.handle.net/10919/88475en
dc.language.isoenen
dc.rightsCreative Commons Attribution 4.0 Internationalen
dc.rights.holderThe Author(s)en
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/en
dc.titlePromoting enzymatic hydrolysis of lignocellulosic biomass by inexpensive soy proteinen
dc.title.serialBIOTECHNOLOGY FOR BIOFUELSen
dc.typeArticle - Refereeden
dc.type.dcmitypeTexten

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