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(Reference retrieved automatically from Web of Science through information on FAPESP grant and its corresponding number as mentioned in the publication by the authors.)

Use of amorphous Nb2O5 and Nb2O5/Al2O3 as acid catalysts for the dehydration of xylose to furfural

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Author(s):
de Lima, Leticia Franzo [1] ; Lima, Julia Leticia Montanari [1] ; Jorqueira, Diogo Silva Sanches [1] ; Landers, Richard [2] ; Moya, Silvia Fernanda [1] ; Suppino, Raphael Soeiro [1]
Total Authors: 6
Affiliation:
[1] Univ Estadual Campinas, Sch Chem Engn, Dept Proc Engn, 500 Albert Einstein Ave, BR-13083852 Campinas, SP - Brazil
[2] Univ Estadual Campinas, Gleb Wataghin Inst Phys, Dept Appl Phys, 777 Sergio Buarque de Holanda St, BR-13083859 Campinas, SP - Brazil
Total Affiliations: 2
Document type: Journal article
Source: Reaction Kinetics Mechanisms and Catalysis; v. 132, n. 1 JAN 2021.
Web of Science Citations: 0
Abstract

This work compared the catalytic performance of the amorphous Nb2O5 (NB) and 12 wt% Nb2O5/Al2O3 (NB-AL) catalysts for the xylose dehydration to furfural carried out for 6 h at 140 and 160 degrees C using water or a 1:0.8 (v/v) water/isopropanol mixture as solvents. The solids were characterized by XRD, N-2 adsorption, TGA, XPS, TPD-NH3 and FTIR-Pyridine. Results indicated a specific surface area of 144 and 108 m(2)/g and an average pore diameter of 44 and 76 angstrom to NB and NB-AL respectively. The solids presented similar density of acid sites (6.0 for NB and 5.7 mu molNH(3)/m(2) for NB-AL), but different strength distribution of the acid sites. Moreover, the fraction of Bronsted acid sites on NB was 27%, whereas on NB-AL it was only 2%. Concerning the catalytic tests, the highest conversion of xylose for NB and NB-AL (99.0 and 91.1%, respectively) was achieved for the reactions at 160 degrees C in water/isopropanol mixture, whilst the highest selectivities to furfural were obtained in reactions with water at 160 degrees C (60.1% to NB and 35.1% to NB-AL). Finally, using water as solvent, the selectivity to furfural increased with both catalysts at the highest temperature, though the carbon balance decreased. (AU)

FAPESP's process: 15/20630-4 - Biorefinery development integrated to a bioethanol sugar cane plant with zero CO2 emission: routes to convert renewable resources to bio-products and bio-electricity
Grantee:Rubens Maciel Filho
Support Opportunities: Research Projects - Thematic Grants
FAPESP's process: 18/20532-0 - Use of niobium-based catalysts for dehydration of xylose to furfural in liquid phase: effects of reaction conditions on catalyst performance
Grantee:Julia Letícia Montanari Lima
Support Opportunities: Scholarships in Brazil - Scientific Initiation