We
here report experimental and kinetic modeling studies on the
conversion of sucrose to levulinic acid (LA) and 5-hydroxymethylfurfural
(HMF) in water using sulfuric acid as the catalyst. Both compounds
are versatile building blocks for the synthesis of various biobased
(bulk) chemicals. A total of 24 experiments were performed in a temperature
window of 80–180 °C, a sulfuric acid concentration between
0.005 and 0.5 M, and an initial sucrose concentration between 0.05
and 0.5 M. Glucose, fructose, and HMF were detected as the intermediate
products. The maximum LA yield was 61 mol %, obtained at 160 °C,
an initial sucrose concentration of 0.05 M, and an acid concentration
of 0.2 M. The maximum HMF yield (22 mol %) was found for an acid concentration
of 0.05 M, an initial sucrose concentration of 0.05 M, and a temperature
of 140 °C. The experimental data were modeled using a number
of possible reaction networks. The best model was obtained when using
a first order approach in substrates (except for the reversion of
glucose) and agreement between experiment and model was satisfactorily.
The implication of the model regarding batch optimization is also
discussed.