Tuning the acid-base properties of layered double hydroxides for the selective obtention of cyclohexane and cyclohexanol in the hydrodeoxygenation of guaiacol

• Catalysts from Ni/Al & Ni/Cu/Al hydrotalcites (HT) were more selective to cyclohexane. • High reaction temperature is determinant to obtain cyclohexane with catalysts from HT. • Catalysts from more basic Ni/Mg/Al & Ni/Cu/Mg/Al HT were more selective to cyclohexanol. • Additional Brønsted acidity led to overproduction of cyclohexane caused by the solvent. • Additional Lewis acidity reduced Ni available favoring the obtention of cyclohexanol. Ni and NiCu catalysts were prepared from Ni/Al, Ni/Cu/Al, Ni/MgAl, and Ni/Cu/Mg/Al hydrotalcites (HT) and tested for the hydrodeoxygenation of guaiacol, a lignin model compound, under H 2 pressure at 300 °C to obtain the added-value products cyclohexane and cyclohexanol. The catalysts prepared from HT without magnesium were more selective to cyclohexane (48–65 %) than those prepared from HT with magnesium, which obtained higher selectivity to cyclohexanol (46–72 %). The presence of magnesium oxide species decreased the reducibility and the metallic area of the catalysts, decreased the Ni content in the NiCu alloy formed in the bimetallic catalyst, and, due to their higher basicity, inhibited the dehydration of cyclohexanol, a key step for obtaining cyclohexane. The obtention of cyclohexane with catalysts prepared from HT is remarkable and could be mainly explained by the reaction temperature used (300 °C) since when it was lowered to 240 °C, a significant decrease of cyclohexane accompanied by an increase of cyclohexanol was observed. When these catalysts were combined with H-βeta, the additional Brønsted acidity led to the overproduction of cyclohexane due to the parallel transformation of the solvent used, dodecane, under the reaction conditions. The detection of some amounts of benzene and toluene suggested a different reaction pathway compared with the catalysts without H-βeta. Finally, the addition of small amounts of Lewis acidity (ReOx) to the Ni/Al and NiCu/Al catalytic systems made difficult the reducibility to Ni of their catalytic precursors and promoted the binding of the oxygenated compounds, favoring the formation of cyclohexanol.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-04-05
DOI
https://doi.org/10.1016/j.cej.2025.162226
Citations
6
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
Field-Weighted Citation Impact
4.28

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article

Tuning the acid-base properties of layered double hydroxides for the selective obtention of cyclohexane and cyclohexanol in the hydrodeoxygenation of guaiacol

Jean‐Jacques Delaunay, Yolanda Cesteros, Judith Granados-Reyes, Angie C. Rueda et al.
6 citations
Chemical Engineering Journal
Catalysis and Hydrodesulfurization Studies
4.28
article

Tuning the acid-base properties of layered double hydroxides for the selective obtention of cyclohexane and cyclohexanol in the hydrodeoxygenation of guaiacol

Jean‐Jacques Delaunay, Yolanda Cesteros, Judith Granados-Reyes, Angie C. Rueda, Pau Mora Masià
article en
6 citations

Abstract

• Catalysts from Ni/Al & Ni/Cu/Al hydrotalcites (HT) were more selective to cyclohexane. • High reaction temperature is determinant to obtain cyclohexane with catalysts from HT. • Catalysts from more basic Ni/Mg/Al & Ni/Cu/Mg/Al HT were more selective to cyclohexanol. • Additional Brønsted acidity led to overproduction of cyclohexane caused by the solvent. • Additional Lewis acidity reduced Ni available favoring the obtention of cyclohexanol. Ni and NiCu catalysts were prepared from Ni/Al, Ni/Cu/Al, Ni/MgAl, and Ni/Cu/Mg/Al hydrotalcites (HT) and tested for the hydrodeoxygenation of guaiacol, a lignin model compound, under H 2 pressure at 300 °C to obtain the added-value products cyclohexane and cyclohexanol. The catalysts prepared from HT without magnesium were more selective to cyclohexane (48–65 %) than those prepared from HT with magnesium, which obtained higher selectivity to cyclohexanol (46–72 %). The presence of magnesium oxide species decreased the reducibility and the metallic area of the catalysts, decreased the Ni content in the NiCu alloy formed in the bimetallic catalyst, and, due to their higher basicity, inhibited the dehydration of cyclohexanol, a key step for obtaining cyclohexane. The obtention of cyclohexane with catalysts prepared from HT is remarkable and could be mainly explained by the reaction temperature used (300 °C) since when it was lowered to 240 °C, a significant decrease of cyclohexane accompanied by an increase of cyclohexanol was observed. When these catalysts were combined with H-βeta, the additional Brønsted acidity led to the overproduction of cyclohexane due to the parallel transformation of the solvent used, dodecane, under the reaction conditions. The detection of some amounts of benzene and toluene suggested a different reaction pathway compared with the catalysts without H-βeta. Finally, the addition of small amounts of Lewis acidity (ReOx) to the Ni/Al and NiCu/Al catalytic systems made difficult the reducibility to Ni of their catalytic precursors and promoted the binding of the oxygenated compounds, favoring the formation of cyclohexanol.

Chemical Engineering JournalVol. 512
Universitat Rovira i Virgili (ES)
Ministerio de Ciencia, Innovación y Universidades, European Commission, Ministerio de Ciencia e Innovación, Agència de Gestió d'Ajuts Universitaris i de Recerca, Agencia Estatal de Investigación
Openalex Percentile: Top 6%
Catalysis and Hydrodesulfurization Studies
4.28
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