The
faster depleting natural reserves of fossil fuel and growing
global climate change crisis have shifted the focus of researchers
toward the extraction of bio-fuel and value-added chemicals from biomass.
In this quest, supercritical (SC) water as a medium has been experimentally
explored to derive bio-oil from biomass and deoxygenate the oxygenated
compounds of it. Levulinic acid (LA) and pentanoic acid or valeric
acid (VA) are two standard value-added products obtained from the
biomass treatment. Thus, in this study, the authors report the kinetics
of the conversion of levulinic acid to valeric acid at four different
supercritical conditions using an implicit solvation model available
within the framework of density functional theory (DFT) and compare
them with their gas and aqueous phase counterparts. Prior to obtaining
the new results, the present approach is first benchmarked with the
existing experimental and theoretical literature under the supercritical
water conditions. The conversion of levulinic acid is studied in two
competing pathways. For each of the reaction pathways, the enthalpy
and Gibbs free energy changes have been discussed. It is found that
the production of valeric acid is equally likely to proceed by the
protonation of the fourth carbon of the acid or by the protonation
of the oxo-group at the fourth carbon atom. The solvent effects are
found to be favorable, especially under two supercritical conditions,
SC1 (ρ = 0.089 g/cc, T = 773 K, P = 250 bar) and SC2 (ρ = 0.109 g/cc, T = 723
K, P = 250 bar) compared to SC3 (ρ = 0.190
g/cc, T = 700 K, P = 304 bar) and
SC4 (ρ = 0.360 g/cc, T = 723 K, P = 463 bar) conditions.