Abstract
Selective hydrogenation of lignin-derived alkyl-phenol to alkyl-cyclohexanone is a key step in the synthesis of renewable caprolactone from lignin-derived monomers. Selective hydrogenation of p-cresol, a model compound for lignin-derived monomers, to 4-methyl-cyclohexanone was conducted using Pd/γ-Al2O3 in a continuous three-phase flow reactor, with side products of 4-methyl cyclohexanol. High conversion (85%) and selectivity (>93%) was demonstrated at ambient reaction pressure. Evaluation of the hydrogenation at different reaction parameters showed that the reaction selectivity was determined by the surface coverage of p-cresol and 4-methyl cyclohexanone. High selectivity to 4-methyl cyclohexanone was also attributed to the lower apparent activation barrier of p-cresol hydrogenation (67 ± 2 kJ/mol) compared to hydrogenation 4-methyl cyclohexanone (92 ± 11 kJ/mol), with a faster rate of initial hydrogenation of p-cresol relative to carbonyl hydrogenation of 4-methyl-cyclohexanone.
Supplementary materials
Title
Supplementary Materials for Catalytic Hydrogenation of Alkylphenols for Renewable Caprolactone
Description
S1. P-cresol Hydrogenation, S2. Temperature profile of up-flow packed bubble column reactor., S3. Inert diluent effect, S4. Transport limitations, S5. Hydrogen residence time, S6 Response Surface Model, S7. Alkyl Group Effect
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