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The highest furfural yield (57.80 %) was obtained from the hydrolysates with the maximum xylose content.
The highest furfural yield (57.80 %) was obtained at 190 °C for 10 min from hydrolysates with the maximum xylose content.
To understand the relationship between the hydrolysate composition and the furfural yields, three specific samples with the maximum xylose content (160 °C, 90 min), the maximum xylobiose (X2) content (180 °C, 15 min), and the maximum total xylose content in monosaccharide and oligosaccharides (DP ≤ 6 °C160 °C, 60 min) were selected for the following experiments.
Hydrolysates with the maximum xylose content (99.94 mg g−1, 160 °C, 90 min), the maximum xylobiose content (20.89 mg g−1, 180 °C, 15 min), and the maximum total xylose content in monosaccharide and oligosaccharides (DP ≤ 6) (272.06 mg g−1, 160 °C, 60 min) were further converted to furfural using tin-loaded montmorillonite as the catalyst in a biphasic system.
During the second stage, hydrolysates with the maximum xylose content (160 °C, 90 min), the maximum xylobiose (X2) content (180 °C, 15 min), and the maximum total xylose content in monosaccharide and oligosaccharides (DP ≤ 6 °C160 °C, 60 min) were further conducted to produce furfural using Sn-MMT as the catalyst in the SBP/NaCl-DMSO system, respectively.
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The maximum activity was reached for different substrate compositions: at high xylose content for xylanase, and at low xylose content for the four cellulolytic activities for which the maximum was reached at different glucose/inducer ratio, depending also on the inducer choice.
The maximum xylose yield was 40.9% (on the base of hemicellulose) in the reaction at 150 °C for 4.0 h.
Kinetic parameters describing xylose consumption are ( V_{{hbox{max} {text{Xy}}}} ) maximum xylose uptake rate, ( K_{{m{text{Xy}}}} ) saturation constant for xylose uptake, ( K_{{G{text{Xy}}}} ) glucose repression constant for xylose uptake, ( K_{{E{text{Xy}}}} ) ethanol inhibition constant for xylose uptake, and ( K_{{A{text{Xy}}}} ) acetate inhibition constant for xylose uptake.
The significant changes in xylose content may significantly influence the rheological properties of the gum.
However, both purified gums A and B had the lower xylose content than the crude gum (Figure 2a).
This significant xylose content makes HSSL a suitable substrate for pentose-fermenting yeasts, such as Scheffersomyces stipitis [2,5].
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