15 research outputs found
In planta expression of A. cellulolyticus Cel5A endocellulase reduces cell wall recalcitrance in tobacco and maize
The glycoside hydrolase family 5 endocellulase, E1 (Cel5A), from Acidothermus cellulolyticus was transformed into both Nicotiana tabacum and Zea mays with expression targeted to the cell wall under a constitutive promoter. Here we explore the possibility that in planta expression of endocellulases will allow these enzymes to access their substrates during cell wall construction, rendering cellulose more amenable to pretreatment and enzyme digestion. Tobacco and maize plants were healthy and developed normally compared with the wild type (WT). After thermochemical pretreatment and enzyme digestion, transformed plants were clearly more digestible than WT, requiring lower pretreatment severity to achieve comparable conversion levels. Furthermore, the decreased recalcitrance was not due to post-pretreatment residual E1 activity and could not be reproduced by the addition of exogenous E1 to the biomass prior to pretreatment, indicating that the expression of E1 during cell wall construction altered the inherent recalcitrance of the cell wall
Elucidating the role of ferrous ion cocatalyst in enhancing dilute acid pretreatment of lignocellulosic biomass
<p>Abstract</p> <p>Background</p> <p>Recently developed iron cocatalyst enhancement of dilute acid pretreatment of biomass is a promising approach for enhancing sugar release from recalcitrant lignocellulosic biomass. However, very little is known about the underlying mechanisms of this enhancement. In the current study, our aim was to identify several essential factors that contribute to ferrous ion-enhanced efficiency during dilute acid pretreatment of biomass and to initiate the investigation of the mechanisms that result in this enhancement.</p> <p>Results</p> <p>During dilute acid and ferrous ion cocatalyst pretreatments, we observed concomitant increases in solubilized sugars in the hydrolysate and reducing sugars in the (insoluble) biomass residues. We also observed enhancements in sugar release during subsequent enzymatic saccharification of iron cocatalyst-pretreated biomass. Fourier transform Raman spectroscopy showed that major peaks representing the C-O-C and C-H bonds in cellulose are significantly attenuated by iron cocatalyst pretreatment. Imaging using Prussian blue staining indicated that Fe<sup>2+ </sup>ions associate with both cellulose/xylan and lignin in untreated as well as dilute acid/Fe<sup>2+ </sup>ion-pretreated corn stover samples. Analyses by scanning electron microscopy and transmission electron microscopy revealed structural details of biomass after dilute acid/Fe<sup>2+ </sup>ion pretreatment, in which delamination and fibrillation of the cell wall were observed.</p> <p>Conclusions</p> <p>By using this multimodal approach, we have revealed that (1) acid-ferrous ion-assisted pretreatment increases solubilization and enzymatic digestion of both cellulose and xylan to monomers and (2) this pretreatment likely targets multiple chemistries in plant cell wall polymer networks, including those represented by the C-O-C and C-H bonds in cellulose.</p
Production of Furfural from Process-Relevant Biomass-Derived Pentoses in a Biphasic Reaction System
Furfural
is an important fuel precursor which can be converted
to hydrocarbon fuels and fuel intermediates. In this work, the production
of furfural by dehydration of process-relevant pentose rich corn stover
hydrolyzate using a biphasic batch reaction system has been investigated.
Methyl isobutyl ketone (MIBK) and toluene have been used to extract
furfural and enhance overall furfural yield by limiting its degradation
to humins. The effects of reaction time, temperature, and acid concentration
(H<sub>2</sub>SO<sub>4</sub>) on pentose conversion and furfural yield
were investigated. For the dehydration of 8 wt % pentose-rich corn
stover hydrolyzate under optimum reaction conditions, 0.05 M H<sub>2</sub>SO<sub>4</sub>, 170 °C for 20 min with MIBK as the solvent,
complete conversion of xylose (98–100%) and a furfural yield
of 80% were obtained. Under these same conditions, except with toluene
as the solvent, the furfural yield was 77%. Additionally, dehydration
of process-relevant pentose rich corn stover hydrolyzate using solid
acid ion-exchange resins under optimum reaction conditions has shown
that Purolite CT275 is as effective as H<sub>2</sub>SO<sub>4</sub> for obtaining furfural yields approaching 80% using a biphasic batch
reaction system. This work has demonstrated that a biphasic reaction
system can be used to process biomass-derived pentose rich sugar hydrolyzates
to furfural in yields approaching 80%