Loading…
Direct conversion of glucose to 5-hydroxymethylfurfural using a mixture of niobic acid and niobium phosphate as a solid acid catalyst
[Display omitted] •HMF was produced by solid acid-catalyzed glucose in an aqueous medium.•Nb2O5·nH2O, NbOPO4·nH2O and a mixture of both was used as a solid acid catalyst.•CCD was used for process optimization for maximizing the glucose conversion to HMF.•Highest HMF selectivity was 56%, obtained for...
Saved in:
Published in: | Fuel (Guildford) 2017-12, Vol.210, p.67-74 |
---|---|
Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Summary: | [Display omitted]
•HMF was produced by solid acid-catalyzed glucose in an aqueous medium.•Nb2O5·nH2O, NbOPO4·nH2O and a mixture of both was used as a solid acid catalyst.•CCD was used for process optimization for maximizing the glucose conversion to HMF.•Highest HMF selectivity was 56%, obtained for a mixture of NbO and NbP.•The mixture of NbO and NbP is an effective catalyst for glucose dehydration to HMF.
The aim of this work was to optimize the acid-catalyzed conversion of glucose into 5-hydroxymethylfurfural (HMF) in an aqueous medium using niobic acid (NbO), niobium phosphate (NbP) and a mixture of both solid acid catalysts. A simplex-centroid mixture design was applied to optimize the mixture ratio between NbO and NbP. A central composite design was applied to process optimization. The studied variables were temperature (T), time (t) and substrate to catalyst weight ratio (RS/C). The mixture design revealed excellent glucose conversion (55%) and HMF selectivity (56%) when the weight ratio between NbO and NbP was equal to 1:1. The experimental results demonstrate that a mixture of both solid acids provides a better combination of Brønsted and Lewis acidity for effective glucose dehydration into HMF than each individual catalyst. |
---|---|
ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2017.08.035 |