A method for depolymerizing
lignocellulosic biomass, comprising the following steps: (a) depolymerizing
lignocellulosic biomass under supercritical conditions in the presence of at least one
alcohol having 1 to 5 carbon atoms, preferably 1 to 2 carbon atoms, at a temperature of 200°C to 300°C, preferably 220°C to 295°C, at a pressure of 40 bar to 170 bar, preferably 50 bar to 150 bar, at a
lignocellulosic biomass /
alcohol ratio of 0.1 to 1, preferably 0.15 to 0.8 wt / wt (w / w), for a time of 5 to 150 minutes, preferably 10 to 130 minutes, to obtain: (i) a mixture comprising a
liquid phase and a
solid phase, the
liquid phase comprising depolymerized lignocellulosic
biomass and at least one
alcohol, the
solid phase comprising carbon residue (“
char”), depolymerized lignocellulosic
biomass, and optionally undepolymerized lignocellulosic
biomass; (ii) an optional
gas phase; (b) A
liquid phase comprising depolymerized lignocellulosic biomass and at least one alcohol is separated from the mixture (i) obtained in step (a) to obtain: (iii) a liquid phase comprising depolymerized lignocellulosic biomass and at least one alcohol; (iv) a
solid phase comprising carbon residue (“
char”), depolymerized lignocellulosic biomass, and optionally undepolymerized lignocellulosic biomass; (c) the liquid phase (iii) comprising depolymerized lignocellulosic biomass and at least one alcohol obtained in step (b) is purified to obtain: (v) depolymerized lignocellulosic biomass; and (vi) at least one alcohol. The depolymerized lignocellulosic biomass obtained by the above method can be advantageously used as, for example, an
antioxidant or UV protectant in biofuels, which can be used as is or blended with other fuels in automotive or
aviation diesel engines. Furthermore, the depolymerized lignocellulosic biomass obtained by the above method can be advantageously used as an
antioxidant in, for example, biological feedstocks (e.g., vegetable oils and animal or vegetable fats) to slow their rancidity during transport and storage.