A process for hydrolysed reforming of lignocellulose biomass to produce bio-gasoline, characterized in that it comprises the following steps: hydrolysing the lignocellulose biomass to obtain a hydrolysed raw material solution, by; a. hydrolysing the lignocellulose biomass in a high-temperature liquid water medium at 180 to 200°C under 2.0 to 5.0 MPa for 40 to 90 minutes and then filtered, the filtrate being the high temperature liquid water hydrolysis solution; b. hydrolysing the residue after the filtration step in step a) in a maleic acid solution with a mass concentration of 0.06 to 0.08% at 160 to 220°C and under 2.0 to 5.0 MPa for 10 to 30 minutes and then filtered, the filtrate being the maleic acid hydrolysis solution; c. mixing the high temperature liquid water hydrolysis solution from step a) and the maleic acid hydrolysis solution from step b) to obtain the hydrolysed raw material solution; reacting the hydrolysed raw material solution in a low-temperature reforming reactor containing a Ni/Al 2 O 3 - SiO 2 catalyst at 160 to 210°C and under 4.0 to 6.5 MPa hydrogen; reacting the reactant from the low-temperature reforming reactor in a high-temperature reforming reactor containing a Ni/HZSM-5 catalyst at 210 to 270°C and under 2.0 to 5.6 MPa hydrogen; subjecting the reactant from the high-temperature reforming reactor to gas-liquid separation in a gas-liquid separator after being condensed, discharging and decompressing uncondensed bio-gasoline, which enters an absorption tank containing a C 6 alkane absorption liquid, and subjecting the liquid to aqueous phase separation through a phase separator, wherein bio-gasoline product is obtained at the upper layer of the phase separator. hydrolysing the lignocellulose biomass to obtain a hydrolysed raw material solution, by; a. hydrolysing the lignocellulose biomass in a high-temperature liquid water medium at 180 to 200°C under 2.0 to 5.0 MPa for 40 to 90 minutes and then filtered, the filtrate being the high temperature liquid water hydrolysis solution; b. hydrolysing the residue after the filtration step in step a) in a maleic acid solution with a mass concentration of 0.06 to 0.08% at 160 to 220°C and under 2.0 to 5.0 MPa for 10 to 30 minutes and then filtered, the filtrate being the maleic acid hydrolysis solution; c. mixing the high temperature liquid water hydrolysis solution from step a) and the maleic acid hydrolysis solution from step b) to obtain the hydrolysed raw material solution; a. hydrolysing the lignocellulose biomass in a high-temperature liquid water medium at 180 to 200°C under 2.0 to 5.0 MPa for 40 to 90 minutes and then filtered, the filtrate being the high temperature liquid water hydrolysis solution; b. hydrolysing the residue after the filtration step in step a) in a maleic acid solution with a mass concentration of 0.06 to 0.08% at 160 to 220°C and under 2.0 to 5.0 MPa for 10 to 30 minutes and then filtered, the filtrate being the maleic acid hydrolysis solution; c. mixing the high temperature liquid water hydrolysis solution from step a) and the maleic acid hydrolysis solution from step b) to obtain the hydrolysed raw material solution; reacting the hydrolysed raw material solution in a low-temperature reforming reactor containing a Ni/Al 2 O 3 - SiO 2 catalyst at 160 to 210°C and under 4.0 to 6.5 MPa hydrogen; reacting the reactant from the low-temperature reforming reactor in a high-temperature reforming reactor containing a Ni/HZSM-5 catalyst at 210 to 270°C and under 2.0 to 5.6 MPa hydrogen; subjecting the reactant from the high-temperature reforming reactor to gas-liquid separation in a gas-liquid separator after being condensed, discharging and decompressing uncondensed bio-gasoline, which enters an absorption tank containing a C 6 alkane absorption liquid, and subjecting the liquid to aqueous phase separation through a phase separator, wherein bio-gasoline product is obtained at the upper layer of the phase separator.