TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The catalyst comprises at least one group VIB metal, and/or at least one group VIII metal (preferably cobalt-molybdenum (CoMo), nickel-molybdenum (NiMo) or nickel-tungsten (NiW) type catalyst).    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: The converting is by fast pyrolysis reaction. The cracking reaction is a catalytic cracking reaction utilizing a powdered catalyst at a reaction temperature of 500-600 degrees C, and a reaction pressure of 1400-2000 KPa. The cracking reaction is a catalytic cracking reaction utilized to convert less than or equal to 12C hydrocarbons into a hydrocarbon product selected from at least one gasoline or fuel oil. The method involves processing the oil in a hydroprocessing reaction, where the hydroprocessing reaction additionally produces a hydrocarbon product selected from at least one gasoline, lower olefins, or naphtha (preferably naphtha intermediate). The step of processing the oil in a hydroprocessing reaction is omitted. The cracking reaction is a steam cracking reaction utilizing steam at a reaction temperature of 850-1200 degrees C to convert the naphtha into a hydrocarbon product selected from at least one fuel oil, gasoline, methane, ethane, liquid petroleum gas (LPG), or lower olefins (preferably ethylene, propylene, or butylenes). The method additionally involves catalytically polymerizing the lower olefins, where the polymerizing produces a product selected from at least one plastic, polyethylene, polypropylene, synthetic rubber or adhesives; oxidizing the lower olefins, where the oxidizing produces an organic chemical product selected from at least one ethylene oxide or acrolein. The hydroprocessing reaction is a catalytic hydroprocessing reaction utilizing a catalyst comprising an active metal or a combination of active metals. The hydroprocessing reaction is performed in a hydroprocessing plant and produces 1-4C hydrocarbons, and where the 1-4C hydrocarbons are used as a fuel source for burners in the hydroprocessing plant. The hydroprocessing reaction is performed in a single stage hydroprocessing plant or two-stage hydroprocessing plant; or in a multi-bed hydroprocessing plant or a series flow hydroprocessing plant. The hydroprocessing plant is integrated with a methanol plant, hydrogen produced from methanol plant is fed to the hydroprocessing plant for use in the catalytic hydroprocessing reaction, and 1-4C hydrocarbons produced from the hydroprocessing reaction are used as a feedstock for the methanol plant. Preferred Components: The feedstock is comprised of at least 50 (preferably at least 75, especially at least 90)% of the bio-oil. The hydrocarbon product is at least 50 (preferably at least 75, especially at least 90)% renewable product. EXAMPLE - No suitable example given.