Catalytic transfer hydrogenation of sugarcane bagasse in ionic liquid and alcohol media for enhanced fructose and sorbitol production

Catalytic transfer hydrogenation (CTH) process and ionic liquids (ILs) are common methods for biomass transformation used to produce biochemicals from lignocellulosic biomass (LCB). This study employed an IL combined with a CTH process to valorize and transform sugarcane bagasse (SCB), aiming to co-produce fructose and sorbitol. This was achieved using a Paar reactor under various operating conditions optimized by a response surface methodology (RSM) using the Box-Behnken design (BBD). The two ILs, [1-Allyl-3-mim][Cl] and [1-Allyl-3-mim][HSO4], were tested for their catalytic potential in a CTH process using pure glucose and fructose in an alcohol medium. The [HSO4]-based catalyst showed higher activity than the Cl-based catalyst, stemming from its dual functionality namely efficient solvent and catalyst that can initiate the hydrolysis step. Specifically, 33.27% fructose and 61.08% sorbitol were obtained with 97.6% glucose conversion in 1,4-butanediol, while the Cl-based catalyst in 1,4-butanediol produced 28.6% fructose and 32.23% sorbitol at 99.56% glucose conversion. The [HSO4]-based ionic liquid (IL) was chosen for further optimization using SCB as the feedstock, and the results demonstrated how parameters (time, temperature, stock, and catalyst loading) affected yields of fructose and sorbitol, reaching 44.12% and 46.17%, respectively, under optimal conditions with [1-Allyl-3-mim][HSO4] + 1,4-butanediol system. The impact of these operating parameters, and the alcohol medium used were clear, as shown by the differences in yields when using SCB versus pure glucose, which can be attributed to the recalcitrant nature of SCB (comprising lignin, hemicellulose, and cellulose) which often influences the yields especially when the biomass is not pretreated. Overall, the production of both sorbitol and fructose from glucose strongly supports the potential of using SCB which contains convertible glucose units as a green feedstock for biochemical production.

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Journal
Discover Environment
Published
2026-02-17
DOI
https://doi.org/10.1007/s44274-026-00589-4
Primary Topic
Catalysis for Biomass Conversion
Type
article
Field-Weighted Citation Impact
0.00

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article

Catalytic transfer hydrogenation of sugarcane bagasse in ionic liquid and alcohol media for enhanced fructose and sorbitol production

Nirmala Deenadayalu, Vuyolwethu Tokoyi
Discover Environment
Catalysis for Biomass Conversion
article

Catalytic transfer hydrogenation of sugarcane bagasse in ionic liquid and alcohol media for enhanced fructose and sorbitol production

Nirmala Deenadayalu, Vuyolwethu Tokoyi
article en

Abstract

Catalytic transfer hydrogenation (CTH) process and ionic liquids (ILs) are common methods for biomass transformation used to produce biochemicals from lignocellulosic biomass (LCB). This study employed an IL combined with a CTH process to valorize and transform sugarcane bagasse (SCB), aiming to co-produce fructose and sorbitol. This was achieved using a Paar reactor under various operating conditions optimized by a response surface methodology (RSM) using the Box-Behnken design (BBD). The two ILs, [1-Allyl-3-mim][Cl] and [1-Allyl-3-mim][HSO4], were tested for their catalytic potential in a CTH process using pure glucose and fructose in an alcohol medium. The [HSO4]-based catalyst showed higher activity than the Cl-based catalyst, stemming from its dual functionality namely efficient solvent and catalyst that can initiate the hydrolysis step. Specifically, 33.27% fructose and 61.08% sorbitol were obtained with 97.6% glucose conversion in 1,4-butanediol, while the Cl-based catalyst in 1,4-butanediol produced 28.6% fructose and 32.23% sorbitol at 99.56% glucose conversion. The [HSO4]-based ionic liquid (IL) was chosen for further optimization using SCB as the feedstock, and the results demonstrated how parameters (time, temperature, stock, and catalyst loading) affected yields of fructose and sorbitol, reaching 44.12% and 46.17%, respectively, under optimal conditions with [1-Allyl-3-mim][HSO4] + 1,4-butanediol system. The impact of these operating parameters, and the alcohol medium used were clear, as shown by the differences in yields when using SCB versus pure glucose, which can be attributed to the recalcitrant nature of SCB (comprising lignin, hemicellulose, and cellulose) which often influences the yields especially when the biomass is not pretreated. Overall, the production of both sorbitol and fructose from glucose strongly supports the potential of using SCB which contains convertible glucose units as a green feedstock for biochemical production.

Discover EnvironmentVol. 4(1)
Durban University of Technology (ZA)
Durban University of Technology, National Research Foundation
Clean water and sanitation
Openalex Percentile: Top 54%
Catalysis for Biomass Conversion
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