Abstract
Research on monosaccharide dehydration primarily focuses on combining catalysts and organic solvents to maximize product yields. This study evaluates reaction performance and solvent recyclability experimentally and through process simulation, emphasizing their role in biorefinery design. Glucose and xylose, at intermediate aqueous sugar concentration, were dehydrated over aluminum chloride using 1,4-dioxane or acetone as co-solvents. Both organic systems exhibited comparable results, with 100% sugar conversion. The 5-hydroxymethylfurfural yield reached 60.9 +- 0.2 for 1,4-dioxane and 59.5 +- 0.6% for acetone systems, while the furfural yield reached 78.1 +- 0.8% and 78.9 +- 1.5%, respectively. Process simulations indicate that using acetone instead of 1,4-dioxane can significantly reduce heat duty during the solvent recovery stage by 72%, solvent loss by 60%, and catalyst loss by 48%. A multi-stage continuous distillation system was built to recover solvents from model solutions. The results highlight the advantages of using acetone instead of 1,4-dioxane, offering insights for improving energy efficiency in biorefinery processes.
Original language | American English |
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Number of pages | 10 |
Journal | Journal of Environmental Chemical Engineering |
Volume | 13 |
Issue number | 2 |
DOIs | |
State | Published - 2025 |
NREL Publication Number
- NREL/JA-2800-94164
Keywords
- azeotrope
- bioeconomy
- biorefinery
- heat duty
- process design
- solvent recovery