A method for producing gasoline blending components while maximizing aromatic production using naphtha, the method comprising the steps of: introducing stabilized hydrocracked naphtha to a light hydrocracked naphtha splitter of a gasoline blending components production system; forming a light hydrocracked naphtha and a light hydrocracked naphtha splitter bottoms in the light hydrocracked naphtha splitter from the received stabilized hydrocracked naphtha; passing the light hydrocracked naphtha splitter bottoms into a medium hydrocracked naphtha splitter that couples to the light hydrocracked naphtha splitter; forming a medium hydrocracked naphtha and a heavy hydrocracked naphtha in the medium hydrocracked naphtha splitter from the received light hydrocracked naphtha splitter bottoms, where the medium hydrocracked naphtha is useful for gasoline blending without additional treatment; introducing a straight run naphtha, the lighted hydrocracked naphtha, and the heavy hydrocracked naphtha to a naphtha hydrotreater (NHT, 140) that couples to both the light hydrocracked naphtha splitter and the medium hydrocracked naphtha splitter; producing a sweetened light hydrotreated naphtha and a sweetened heavy hydrotreated naphtha in the NHT from the received straight run naphtha, the light hydrocracked naphtha and the heavy hydrocracked naphtha; introducing the sweetened light hydrotreated naphtha and a light raffinate to an isomerization unit that couples to both the NHT and an aromatics complex; producing an isomerate in the isomerization unit from the received sweetened light hydrotreated naphtha and the light raffinate, where the isomerate is useful for blending without additional treatment; introducing the sweetened heavy hydrotreated naphtha to a continuous catalytic reformer (CCR, 160) that couples to the NHT; producing a reformate in the CCR from the received sweetened heavy hydrotreated naphtha; and introducing the reformate to an aromatics complex that couples to the CCR; and producing a refined benzene product, a refined para-xylene product, a C7s cut, a C9+ cut and the light raffinate from the received reformate, where the C7s cut and the C9+ cut are useful for gasoline blending without additional treatment. introducing stabilized hydrocracked naphtha to a light hydrocracked naphtha splitter of a gasoline blending components production system; forming a light hydrocracked naphtha and a light hydrocracked naphtha splitter bottoms in the light hydrocracked naphtha splitter from the received stabilized hydrocracked naphtha; passing the light hydrocracked naphtha splitter bottoms into a medium hydrocracked naphtha splitter that couples to the light hydrocracked naphtha splitter; forming a medium hydrocracked naphtha and a heavy hydrocracked naphtha in the medium hydrocracked naphtha splitter from the received light hydrocracked naphtha splitter bottoms, where the medium hydrocracked naphtha is useful for gasoline blending without additional treatment; introducing a straight run naphtha, the lighted hydrocracked naphtha, and the heavy hydrocracked naphtha to a naphtha hydrotreater (NHT, 140) that couples to both the light hydrocracked naphtha splitter and the medium hydrocracked naphtha splitter; producing a sweetened light hydrotreated naphtha and a sweetened heavy hydrotreated naphtha in the NHT from the received straight run naphtha, the light hydrocracked naphtha and the heavy hydrocracked naphtha; introducing the sweetened light hydrotreated naphtha and a light raffinate to an isomerization unit that couples to both the NHT and an aromatics complex; producing an isomerate in the isomerization unit from the received sweetened light hydrotreated naphtha and the light raffinate, where the isomerate is useful for blending without additional treatment; introducing the sweetened heavy hydrotreated naphtha to a continuous catalytic reformer (CCR, 160) that couples to the NHT; producing a reformate in the CCR from the received sweetened heavy hydrotreated naphtha; and introducing the reformate to an aromatics complex that couples to the CCR; and producing a refined benzene product, a refined para-xylene product, a C7s cut, a C9+ cut and the light raffinate from the received reformate, where the C7s cut and the C9+ cut are useful for gasoline blending without additional treatment.