Deep deoxygenation of biocrudes utilizing fluidized catalytic cracking co-processing with hydrocarbon feedstocks

A fluid catalytic cracking system, comprising:

• a riser comprising at least one inlet;
• a first catalyst and a second catalyst disposed within the riser;
• wherein the riser is operable to receive and facilitate catalytic conversion of a biological feed comprising a biomass-derived liquid and a hydrocarbon feed comprising between 60 volume % and 100 volume % hydrocarbons having a boiling point above 343° C., by the first catalyst and the second catalyst to convert at least a portion of the biological feed and at least a portion of the hydrocarbon feed to hydrocarbon products, wherein the hydrocarbon products comprise oxygen in an amount ranging from about 0.005 wt. % to about 6 wt. %;
• wherein the first catalyst and the second catalyst are compositionally different;
• wherein the first catalyst comprises about 10 wt. % to about 60 wt. % kaolin, about 20 wt. % to about 65 wt. % aluminum oxide, about 2 wt. % to about 30 wt. % silicon dioxide, and about 5 wt. % to about 60 wt. % of a first zeolite, said first zeolite having a pore diameter from about 0.2 nanometers to about 0.8 nanometers and 10 to 12 membered rings;
• and
• wherein the second catalyst comprises about 10 wt. % to about 40 wt. % aluminum oxide, about 0 wt. % to about 60 wt. % magnesium oxide, about 0.1 wt. % to about 30 wt. % aluminum orthophosphate, about 0.1 wt. % to about 10 wt. % vanadyl sulfate, and a second zeolite, said second zeolite having a pore diameter of about 0.2 nanometers to about 0.7 nanometers and 10 or less membered rings;
• a reactor;
• a regenerator;
• and
• a fractionator.