Abstract

BackgroundLignocellulosic biomass has the potential to be a major source of renewable sugar for biofuel production. Before enzymatic hydrolysis, biomass must first undergo a pretreatment step in order to be more susceptible to saccharification and generate high yields of fermentable sugars. Lignin, a complex, interlinked, phenolic polymer, associates with secondary cell wall polysaccharides, rendering them less accessible to enzymatic hydrolysis. Herein, we describe the analysis of engineered Arabidopsis lines where lignin biosynthesis was repressed in fiber tissues but retained in the vessels, and polysaccharide deposition was enhanced in fiber cells with little to no apparent negative impact on growth phenotype.ResultsEngineered Arabidopsis plants were treated with the ionic liquid (IL) 1-ethyl-3-methylimidazolium acetate 1-ethyl-3-methylimidazolium acetate ([C2C1im][OAc]) at 10 % wt biomass loading at either 70 °C for 5 h or 140 °C for 3 h. After pretreatment at 140 °C and subsequent saccharification, the relative peak sugar recovery of ~26.7 g sugar per 100 g biomass was not statistically different for the wild type than the peak recovery of ~25.8 g sugar per 100 g biomass for the engineered plants (84 versus 86 % glucose from the starting biomass). Reducing the pretreatment temperature to 70 °C for 5 h resulted in a significant reduction in the peak sugar recovery obtained from the wild type to 16.2 g sugar per 100 g biomass, whereas the engineered lines with reduced lignin content exhibit a higher peak sugar recovery of 27.3 g sugar per 100 g biomass and 79 % glucose recoveries.ConclusionsThe engineered Arabidopsis lines generate high sugar yields after pretreatment at 70 °C for 5 h and subsequent saccharification, while the wild type exhibits a reduced sugar yield relative to those obtained after pretreatment at 140 °C. Our results demonstrate that employing cell wall engineering efforts to decrease the recalcitrance of lignocellulosic biomass has the potential to drastically reduce the energy required for effective pretreatment.Electronic supplementary materialThe online version of this article (doi:10.1186/s13068-015-0275-2) contains supplementary material, which is available to authorized users.

Highlights

  • Lignocellulosic biomass has the potential to be a major source of renewable sugar for biofuel production

  • While significant progress has been made in improving the economic viability and commercial scalability of renewable biofuels, there remain significant challenges that must be addressed before these processes reach their full potential [1,2,3]

  • We report the impact of these engineered lines relative to wild type (WT) in terms of pretreatment efficacy, sugar yields, and mass balances for ionic liquid (IL) pretreatment at 70 and 140 °C

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Summary

Introduction

Lignocellulosic biomass has the potential to be a major source of renewable sugar for biofuel production. While significant progress has been made in improving the economic viability and commercial scalability of renewable biofuels, there remain significant challenges that must be addressed before these processes reach their full potential [1,2,3] These challenges include the relatively low energy density of the biomass feedstocks, the recalcitrance of the plant cell walls to enzymatic hydrolysis [1,2,3], and the current high cost of pretreatment required to reduce this recalcitrance [4]. Increasing the accumulation of polysaccharides in biomass and improving biomass digestibility would have significant beneficial impacts on the cost of lignocellulosic biofuel production, both by increasing fermentable sugar yield per acre and reducing the severity of pretreatment [2, 17]

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