The lignocellulosic biomass has been
identified as a potential
renewable feedstock for production of levulinic acid (LA). In the
present study, the catalytic thermo liquefaction (CTL) process for
liquefaction of rice straw into LA was studied by integrating the
polyethyleneimine functionalized acidic ionic liquid (PolyE-IL) catalyst.
The screening of various PolyE-IL catalysts with variable counter
ions showed the remarkable formation of carbohydrates, LA, formic
acid, and acetic acid (AA). Among the tested PolyE-IL catalysts, PolyE-IL
with a [HSO4]− counter ion showed the
maximum conversion efficiency. The process intensification study to
evaluate the influence of reaction parameters such as catalyst concentration,
reaction temperature, time, and slurry concentrations was conducted
to achieve the maximum conversion and yield of organic acids. Moreover,
the influence of feedstock pretreatment was also studied. The pretreated
rice straw provided maximum yields of LA and FA. The intensified CTL
process for untreated rice straw resulted in 49.8% LA, 50.5% FA, and
100% AA, while CTL of pretreated rice straw resulted in 65.5% LA,
75.8% FA, and 26.7% AA of the theoretical maximum at 210 °C for
120 min. The separation of the catalyst and other liquefaction products
was achieved using adsorption followed by membrane separation processes.
The adsorption process leads to separation of the undesired polymeric
side products, while membrane separation provides efficient separation
of the catalyst and organic acids with >98% efficiency. The undesired
side products separated in the adsorption process were concentrated
as CTL-Oil and characterized for physiochemical properties. CTL-Oil
is C-, H-, and O-rich feedstock with a caloric value of 24–26
MJ/Kg and thus could be explored for multiple fuel and energy applications.
Thus, an efficient valorization of rice straw was achieved using a
recyclable, robust, and efficient catalyst.