exposing a hydrocarbonaceous feed to a catalyst in a reactor under fluid catalytic cracking conditions comprising a temperature of 535° C. or less and 20 wt % to 65 wt % conversion of compounds with boiling points of more than 221° C. to compounds with boiling points of 221° C. or less, to form one or more liquid products and coke associated with the catalyst, the one or more liquid products comprising 25 wt % or more of a diesel boiling range fraction relative to a weight of the hydrocarbonaceous feed;

passing at least a portion of the catalyst and the associated coke into a regenerator;

passing a supplemental fuel into the regenerator, a vessel associated with the regenerator, or a combination thereof, a ratio of an adjusted weight of a low carbon intensity fraction of the supplemental fuel to a weight of the associated coke being 0.01 or more;

combusting, in the regenerator, the vessel associated with the regenerator, or the combination thereof, at least a portion of the associated coke and at least a portion of the supplemental fuel to form at least heated catalyst and CO₂; and

passing at least a portion of the heated catalyst into the reactor.