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Title: Simultaneous Dehydration of Glucose and Xylose Present in a Process-Relevant Biorefinery Hydrolysate to Furfurals Using Heterogeneous Solid Acid Catalysts

Abstract

In this work, we report the simultaneous dehydration of glucose and xylose present in a process-relevant biorefinery hydrolysate to furfural and 5-hydroxymethylfurfural (HMF) using heterogeneous solid acid catalysts in a microwave reactor. Initially, several solid acid catalysts with varied Bronsted and Lewis acidity were screened to evaluate their activity and selectivity in dehydration of pure glucose to HMF. A noticeable improvement in HMF yield from dehydration of 8 wt% glucose was obtained by combining an acidic ion-exchange resin (Purolite CT-275DR) with an amorphous silica-alumina catalyst (Davicat-3115) resulting in HMF yields of 27-33% using a homogeneous solvent system of aqueous dioxane (dioxane/water, 2:1 v/v) at 195 °C in 5 min. Under the same reaction conditions, catalysts, and solvent system but with the addition of NaCl in catalytic amounts (33-100 mM), a more than 2-fold increase in HMF yields (66-70%) was achieved for the dehydration of 8 wt% glucose, whereas furfural yields approaching 95% were achieved for the dehydration of 6 wt% xylose, when conducted separately. Notably, using the same catalyst and solvent system while slightly modifying the reaction conditions to 197 °C and 5 min, simultaneous dehydration of 4 wt% xylose and 9 wt% glucose present in a process-relevant corn stovermore » hydrolysate resulted in furfural and HMF yields of 96 and 74%, respectively, resulting in a combined furfural yield of 80%. The results further showed that the pH of the reaction solution played an important role in maximizing product yields. A pH < 2 resulted in low HMF yields due to the increased formation of HMF degradation products, whereas a pH 2-3 gave high HMF yields by possibly stabilizing the reaction intermediates and product, suppressing the occurrence of side reactions.« less

Authors:
ORCiD logo [1]; ORCiD logo [2]; ORCiD logo [3]; ORCiD logo [1]
  1. Renewable Resources and Enabling Sciences Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States
  2. Catalytic Carbon Transformation & Scale-up Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States
  3. Biochemical Process Integration Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States
Publication Date:
Research Org.:
National Renewable Energy Laboratory (NREL), Golden, CO (United States)
Sponsoring Org.:
USDOE; USDOE Office of Energy Efficiency and Renewable Energy (EERE), Office of Sustainable Transportation. Bioenergy Technologies Office (BETO)
OSTI Identifier:
1996288
Alternate Identifier(s):
OSTI ID: 2005577
Report Number(s):
NREL/JA-2800-80807
Journal ID: ISSN 0887-0624
Grant/Contract Number:  
AC36-08GO28308
Resource Type:
Published Article
Journal Name:
Energy and Fuels
Additional Journal Information:
Journal Name: Energy and Fuels Journal Volume: 37 Journal Issue: 17; Journal ID: ISSN 0887-0624
Publisher:
American Chemical Society
Country of Publication:
United States
Language:
English
Subject:
09 BIOMASS FUELS; 37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY; Aldehydes; Carbohydrates; Catalysts; Dehydration; Oxides; catalyst; dehydration; furfural; glucose; heterogeneous; HMF; hydrolysate; xylose

Citation Formats

Mittal, Ashutosh, Ruddy, Daniel A., Chen, Xiaowen, and Johnson, David K. Simultaneous Dehydration of Glucose and Xylose Present in a Process-Relevant Biorefinery Hydrolysate to Furfurals Using Heterogeneous Solid Acid Catalysts. United States: N. p., 2023. Web. doi:10.1021/acs.energyfuels.3c01597.
Mittal, Ashutosh, Ruddy, Daniel A., Chen, Xiaowen, & Johnson, David K. Simultaneous Dehydration of Glucose and Xylose Present in a Process-Relevant Biorefinery Hydrolysate to Furfurals Using Heterogeneous Solid Acid Catalysts. United States. https://doi.org/10.1021/acs.energyfuels.3c01597
Mittal, Ashutosh, Ruddy, Daniel A., Chen, Xiaowen, and Johnson, David K. Tue . "Simultaneous Dehydration of Glucose and Xylose Present in a Process-Relevant Biorefinery Hydrolysate to Furfurals Using Heterogeneous Solid Acid Catalysts". United States. https://doi.org/10.1021/acs.energyfuels.3c01597.
@article{osti_1996288,
title = {Simultaneous Dehydration of Glucose and Xylose Present in a Process-Relevant Biorefinery Hydrolysate to Furfurals Using Heterogeneous Solid Acid Catalysts},
author = {Mittal, Ashutosh and Ruddy, Daniel A. and Chen, Xiaowen and Johnson, David K.},
abstractNote = {In this work, we report the simultaneous dehydration of glucose and xylose present in a process-relevant biorefinery hydrolysate to furfural and 5-hydroxymethylfurfural (HMF) using heterogeneous solid acid catalysts in a microwave reactor. Initially, several solid acid catalysts with varied Bronsted and Lewis acidity were screened to evaluate their activity and selectivity in dehydration of pure glucose to HMF. A noticeable improvement in HMF yield from dehydration of 8 wt% glucose was obtained by combining an acidic ion-exchange resin (Purolite CT-275DR) with an amorphous silica-alumina catalyst (Davicat-3115) resulting in HMF yields of 27-33% using a homogeneous solvent system of aqueous dioxane (dioxane/water, 2:1 v/v) at 195 °C in 5 min. Under the same reaction conditions, catalysts, and solvent system but with the addition of NaCl in catalytic amounts (33-100 mM), a more than 2-fold increase in HMF yields (66-70%) was achieved for the dehydration of 8 wt% glucose, whereas furfural yields approaching 95% were achieved for the dehydration of 6 wt% xylose, when conducted separately. Notably, using the same catalyst and solvent system while slightly modifying the reaction conditions to 197 °C and 5 min, simultaneous dehydration of 4 wt% xylose and 9 wt% glucose present in a process-relevant corn stover hydrolysate resulted in furfural and HMF yields of 96 and 74%, respectively, resulting in a combined furfural yield of 80%. The results further showed that the pH of the reaction solution played an important role in maximizing product yields. A pH < 2 resulted in low HMF yields due to the increased formation of HMF degradation products, whereas a pH 2-3 gave high HMF yields by possibly stabilizing the reaction intermediates and product, suppressing the occurrence of side reactions.},
doi = {10.1021/acs.energyfuels.3c01597},
journal = {Energy and Fuels},
number = 17,
volume = 37,
place = {United States},
year = {Tue Aug 22 00:00:00 EDT 2023},
month = {Tue Aug 22 00:00:00 EDT 2023}
}

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