Niobium-modified hydrotalcite catalysts: Sustainable conversion of waste glycerol to valuable chemicals

[Display omitted] •Niobium-modified hydrotalcite prepared by ion exchange using peroxoniobate species.•Catalyst calcination produces a composite material (an MgAl mixed oxide and Nb2O5).•Catalytic tests performed in continuous-flow fixed bed reactor (PBR) on pilot-scale.•High glycerol conversion to...

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Veröffentlicht in:Applied catalysis. A, General General, 2020-09, Vol.606, p.117814, Article 117814
Hauptverfasser: Padula, Izabela D., Santos, Brenda M.A., Rodrigues, Ana P.H., Gastelois, Pedro Lana, Mendes, Isolda M.C., Portilho, Márcio F., Oliveira, Luiz C.A., Oliveira, Cinthia C.
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Sprache:eng
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Zusammenfassung:[Display omitted] •Niobium-modified hydrotalcite prepared by ion exchange using peroxoniobate species.•Catalyst calcination produces a composite material (an MgAl mixed oxide and Nb2O5).•Catalytic tests performed in continuous-flow fixed bed reactor (PBR) on pilot-scale.•High glycerol conversion to valuable products like formic acid and diglycerol.•Nb increases the acidity of the MgAl catalyst and the diglycerol formation. Nb-modified MgAlmixed oxide catalysts were prepared by ion exchange using an MgAl hydrotalcite and peroxoniobate complex as precursors. After calcination, the Nb-MgAl revealed to be a composite material (MgAl mixed oxide with segregated Nb2O5 nanoparticles), with an increased specific surface area (229 m2 g−1) compared to bare MgAl (88 m2 g−1). XRD confirmed that part of the Nb atoms was inserted in the MgAl lattice thus causing the oxide doping. Furthermore, the Nb precursor favored the incorporation of a high amount of Nb in the catalyst (18 wt.%). Reactions performed in a continuous flow fixed-bed reactor (PBR) on a pilot scale showed that the MgAl and Nb-MgAl are quite active and stable catalysts for the conversion of the waste glycerol (> 90 %), as generated in the biodiesel industry. The valuable chemicals obtained (i.e., diglycerol, formic acid, and dioxane) demonstrates the potential industrial use of the catalysts presented in this work.
ISSN:0926-860X
1873-3875
DOI:10.1016/j.apcata.2020.117814