We have developed lumped reaction schemes to optimize
the yields
of products from selective hydrogenations of HAH, a biomass-derived
platform chemical produced by two-step aldol condensations of 5-hydroxymethyl
furfural (H) with acetone (A). Reaction schemes consisting of 7, 9,
and 11 steps were examined to describe the rates of formation of the
observed products and reaction intermediates for hydrogenation of
HAH over Ru and Pd catalysts, and a 3-step scheme was studied over
Cu catalysts. Rate constants and activation energies were calculated
using these reaction schemes, and we then apply the schemes to explore
the effects of water addition on the hydrogenation pathways. The effects
of water addition to isopropanol (IPA) solvents on the hydrogenation
of HAH were markedly different over Pd, Ru, and Cu catalysts. Over
the Pd catalyst, the addition of water to IPA increased hydrogenation
rates and promoted the hydrogenation of furan rings. The addition
of water to IPA yielded significant carbon losses over the Ru catalyst,
and slowed hydrogenation steps over Cu, while significantly inhibiting
hydrogenation of the ketone group. This behavior opened routes toward
increased production rates of PHAHO (a partially hydrogenated,
P, form of HAH containing a CO bond), a product in which the
diene groups of the furan rings were not hydrogenated. The addition
of water also allowed increased feed concentrations of HAH that were
previously not possible in pure IPA solvents. The insights presented
in this work provide a more mechanistic description of the hydrogenation
of HAH, the behavior of specific intermediates, and the reactivity
of key functional groups.