The
catalytic condensation of ethanol to n-butanol
and higher alcohols, known collectively as Guerbet reactions, has
attracted attention in recent years as ethanol becomes increasingly
available as a biorenewable feedstock. Results are presented here
for the continuous, condensed-phase conversion of ethanol to higher
alcohols using Ni/La2O3/γ-Al2O3 catalysts and for catalysts containing a second metal
(Cu, Co, Pd, Pt, Fe, Mo) in addition to nickel. Detailed characterization
of the catalyst surface and bulk properties has been carried out and
is correlated to catalyst activity and selectivity. The best results
obtained for nickel catalysts are a selectivity to higher alcohols
of 75–80% and a turnover frequency of 200 mol ethanol/mol Ni
site/h at 230 °C. The addition of cobalt nearly doubles the ethanol
conversion rate relative to Ni alone, with only a slight reduction
in higher alcohol selectivity. Results of catalyst characterization,
a simple kinetic model, and experiments with reaction intermediates
support the initial dehydrogenation of ethanol as the rate-limiting
step of the condensed-phase reaction.