Multidimensional synergistic model for sustainable and directed conversion of hemicellulose to xylose via mandelic acid pretreatment

While current research largely emphasizes high-value utilization through hemicellulose separation, the potential of its sugar components remains underexplored. This study systematically investigates the structural evolution and kinetic behavior of sugar products during mandelic acid (MA) pretreatment. At low MA concentrations (2 %), the process primarily induces mild hydrolysis of the hemicellulose main chain, yielding high-value xylooligosaccharides (31.45 g/kg). As MA concentration increases, xylooligosaccharides are further hydrolyzed into xylose, alongside the formation of degradation products such as furfural. Post-pretreatment, the main structure of residual hemicellulose is β-D-xylose. Notably, key side-chain groups, including 4-O-methyl-α-D-glucuronic acid and O-acetyl groups, are preserved under mild acidic conditions but progressively cleaved with increasing pretreatment severity. This structural evolution lays the foundations for targeted depolymerization into xylose. Kinetic analysis reveals a biphasic hydrolysis pattern: a fast phase (k f = 6.09 ×10 5 min −1 , E a = 62.39 kJ/mol) associated with the amorphous region, and a slower phase (k s = 1.10 ×10 13 min −1 , E a = 123.54 kJ/mol) corresponding to crystalline resistance. The overall hydrolysis rate of hemicellulose exceeds the degradation rate of xylose (k 2 = 7.06 ×10⁶ min −1 , E a = 76.66 kJ/mol), enabling selective xylose production. Optimal conditions, 150 °C and 5 % MA, maximize xylose yield while minimizing degradation. The activation energy landscape positions xylose degradation between the fast and slow hydrolysis phases of hemicellulose. Based on these findings, a multi-parameter synergistic model integrating temperature, acidity, and time was developed to guide the efficient and selective conversion of hemicellulose to xylose. This approach enhances the valorization of hemicellulose and supports ecological sustainability and the advancement of a green sugar-based bioeconomy. • The selective preparation of xylooligosaccharides and xylose was achieved. • The β-D-xylose structure of the hemicellulose main chain was effectively retained. • The biphasic kinetic of xylose dissolution in mandelic acid pretreatment was discovered. • A "temperature-acidity-time" synergistic regulation model was established.

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Publication Details

Journal
Industrial Crops and Products
Published
2025-08-25
DOI
https://doi.org/10.1016/j.indcrop.2025.121786
Primary Topic
Biofuel production and bioconversion
Type
article
Field-Weighted Citation Impact
0.00

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article

Multidimensional synergistic model for sustainable and directed conversion of hemicellulose to xylose via mandelic acid pretreatment

Shuangquan Yao, Yi Xie, Baojie Liu, Caoxing Huang et al.
Industrial Crops and Products
Biofuel production and bioconversion
article

Multidimensional synergistic model for sustainable and directed conversion of hemicellulose to xylose via mandelic acid pretreatment

Shuangquan Yao, Yi Xie, Baojie Liu, Caoxing Huang, Hongyu Chen, Liang Chen, Shanshan Wang, Guirong Bao, Chengrong Qin
article en

Abstract

While current research largely emphasizes high-value utilization through hemicellulose separation, the potential of its sugar components remains underexplored. This study systematically investigates the structural evolution and kinetic behavior of sugar products during mandelic acid (MA) pretreatment. At low MA concentrations (2 %), the process primarily induces mild hydrolysis of the hemicellulose main chain, yielding high-value xylooligosaccharides (31.45 g/kg). As MA concentration increases, xylooligosaccharides are further hydrolyzed into xylose, alongside the formation of degradation products such as furfural. Post-pretreatment, the main structure of residual hemicellulose is β-D-xylose. Notably, key side-chain groups, including 4-O-methyl-α-D-glucuronic acid and O-acetyl groups, are preserved under mild acidic conditions but progressively cleaved with increasing pretreatment severity. This structural evolution lays the foundations for targeted depolymerization into xylose. Kinetic analysis reveals a biphasic hydrolysis pattern: a fast phase (k f = 6.09 ×10 5 min −1 , E a = 62.39 kJ/mol) associated with the amorphous region, and a slower phase (k s = 1.10 ×10 13 min −1 , E a = 123.54 kJ/mol) corresponding to crystalline resistance. The overall hydrolysis rate of hemicellulose exceeds the degradation rate of xylose (k 2 = 7.06 ×10⁶ min −1 , E a = 76.66 kJ/mol), enabling selective xylose production. Optimal conditions, 150 °C and 5 % MA, maximize xylose yield while minimizing degradation. The activation energy landscape positions xylose degradation between the fast and slow hydrolysis phases of hemicellulose. Based on these findings, a multi-parameter synergistic model integrating temperature, acidity, and time was developed to guide the efficient and selective conversion of hemicellulose to xylose. This approach enhances the valorization of hemicellulose and supports ecological sustainability and the advancement of a green sugar-based bioeconomy. • The selective preparation of xylooligosaccharides and xylose was achieved. • The β-D-xylose structure of the hemicellulose main chain was effectively retained. • The biphasic kinetic of xylose dissolution in mandelic acid pretreatment was discovered. • A "temperature-acidity-time" synergistic regulation model was established.

Industrial Crops and ProductsVol. 235
Guangxi University (CN), Nanjing Forestry University (CN)
Natural Science Foundation of Guangxi Province
Responsible consumption and production
Openalex Percentile: Top 79%
Biofuel production and bioconversion
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