4.6 Article

Hydrogenation of Furfural to Cyclopentanone in Tert-Butanol-Water Medium: A Study of the Reaction Intermediates Reactivity Using Cu/ZnO/Al2O3 as Catalyst

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CATALYSTS
卷 13, 期 11, 页码 -

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MDPI
DOI: 10.3390/catal13111394

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cyclopentanone; furfural; hydrogenation; Cu/ZnO/Al2O3; reaction intermediates

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The catalytic transformation of furfural to cyclopentanone was studied using different solvents. The presence of tert-butanol inhibits key steps in the overall conversion and requires higher H-2 pressure and temperature. The obtained productivities per gram of catalyst and mols of Cu basis are substantially higher than other copper-based catalysts.
The catalytic transformation of furfural to cyclopentanone has been investigated using two different liquid phases as solvent: water and 30 wt.% tert-butanol in water. When using neat water at 160 degrees C, 40 bar of H-2, and after 2 h of reaction time, furfural polymerizes, and the yield of cyclopentanone is just 42% with a low carbon balance, indicating that furfural is transformed to non-detected by-products, likely heavy resins. When using 30 wt.% tert-butanol in water, the yield of cyclopentanone is ca. 20%, and the major product is furfuryl alcohol with a 47% yield. We have studied the catalytic transformation of the most relevant reaction intermediates in the overall conversion of furfural to cyclopentanone. In the presence of tert-butanol, two steps are inhibited in the overall pathway: (i) the Piancatelli rearrangement of furfuryl alcohol and (ii) the transformation of cyclopentenone. This inhibition is attributed to the neutralization of protons from water dissociation by surface sites on the catalyst, preventing their participation in the overall reaction. To counteract these inhibitions when tert-butanol is present, higher H-2 pressure (60 bar) and temperatures (200 degrees C) are required. We have been able to obtain productivities per gram of catalyst and mols of Cu basis of 411 g(prod)h(-1)g(cat)(-1) and 14 g(prod)s(-1)mol(Cu)(-1), respectively, which is substantially above that found for other copper-based catalysts.

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